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  • Published: 18 December 2023

Country-specific net-zero strategies of the pulp and paper industry

  • Min Dai 1 ,
  • Mingxing Sun 2 ,
  • Bin Chen 1 ,
  • Lei Shi 3 ,
  • Mingzhou Jin   ORCID: orcid.org/0000-0002-2387-8129 4 ,
  • Yi Man   ORCID: orcid.org/0000-0002-3745-9128 5 ,
  • Ziyang Liang 1 ,
  • Cecilia Maria Villas Bôas de Almeida 6 ,
  • Jiashuo Li   ORCID: orcid.org/0000-0002-2915-4770 7 ,
  • Pengfei Zhang 7 ,
  • Anthony S. F. Chiu 8 ,
  • Ming Xu   ORCID: orcid.org/0000-0002-7106-8390 9 ,
  • Huajun Yu 1 ,
  • Jing Meng   ORCID: orcid.org/0000-0001-8708-0485 10 &
  • Yutao Wang   ORCID: orcid.org/0000-0001-8297-8579 1 , 11 , 12 , 13  

Nature volume  626 ,  pages 327–334 ( 2024 ) Cite this article

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  • Climate-change mitigation
  • Environmental impact
  • Environmental social sciences
  • Sustainability

The pulp and paper industry is an important contributor to global greenhouse gas emissions 1 , 2 . Country-specific strategies are essential for the industry to achieve net-zero emissions by 2050, given its vast heterogeneities across countries 3 , 4 . Here we develop a comprehensive bottom-up assessment of net greenhouse gas emissions of the domestic paper-related sectors for 30 major countries from 1961 to 2019—about 3.2% of global anthropogenic greenhouse gas emissions from the same period 5 —and explore mitigation strategies through 2,160 scenarios covering key factors. Our results show substantial differences across countries in terms of historical emissions evolution trends and structure. All countries can achieve net-zero emissions for their pulp and paper industry by 2050, with a single measure for most developed countries and several measures for most developing countries. Except for energy-efficiency improvement and energy-system decarbonization, tropical developing countries with abundant forest resources should give priority to sustainable forest management, whereas other developing countries should pay more attention to enhancing methane capture rate and reducing recycling. These insights are crucial for developing net-zero strategies tailored to each country and achieving net-zero emissions by 2050 for the pulp and paper industry.

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Data availability.

The detailed data of this study are available at https://zenodo.org/record/8369154 . The main data that support the findings of this study are as follows: (1) production and trade data on wood, pulp and paper products in 1961–2019 can be obtained from the FAOSTAT database ( https://www.fao.org/faostat/en/#data/FO ); (2) data on the energy mix of the pulp and paper industry is from IEA Data and Statistics ( https://www.iea.org/data-and-statistics/data-sets/?filter=all ); (3) the municipal WDM can be obtained from the OECD Stat database ( https://stats.oecd.org/viewhtml.aspx?datasetcode=MUNW&lang=en ); (4) the estimated population in 2050 is available from World Population Prospects 2019 conducted by the Department of Economics and Social Affairs, United Nations ( https://population.un.org/wpp/Download/Standard/Population/ ); and (5) the energy intensity of multiprocesses is from the literature and the main sources are listed in the  Supplementary information .

Code availability

The data-processing code that generates the results in this study can be found at https://zenodo.org/record/8369012 .

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Acknowledgements

This research was supported by the National Key R&D Program of China (grant no. 2020YFE0201400) and the National Natural Science Foundation of China (grant nos. 52022023, 52100210 and 72061147003).

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Authors and affiliations.

Fudan Tyndall Center and Shanghai Key Laboratory of Atmospheric Particle Pollution and Prevention (LAP3), Department of Environmental Science and Engineering, Fudan University, Shanghai, China

Min Dai, Bin Chen, Ziyang Liang, Huajun Yu & Yutao Wang

Key Laboratory of Ecosystem Network Observation and Modeling, Institute of Geographic Sciences and Natural Resources Research, Chinese Academy of Sciences, Beijing, China

Mingxing Sun

Watershed Carbon Neutrality Institute, Nanchang University, Nanchang, China

Industrial and Systems Engineering Department, Institute for a Secure and Sustainable Environment, The University of Tennessee at Knoxville, Knoxville, TN, USA

Mingzhou Jin

State Key Laboratory of Pulp and Paper Engineering, South China University of Technology, Guangzhou, China

Universidade Paulista, UNIP, São Paulo, Brazil

Cecilia Maria Villas Bôas de Almeida

Institute of Blue and Green Development, Shandong University, Weihai, China

Jiashuo Li & Pengfei Zhang

Gokongwei College of Engineering, De La Salle University, Manila, Philippines

Anthony S. F. Chiu

School of Environment, Tsinghua University, Beijing, China

The Bartlett School of Sustainable Construction, University College London, London, UK

IRDR International Center of Excellence on Risk Interconnectivity and Governance on Weather/Climate Extremes Impact and Public Health, Fudan University, Shanghai, China

Shanghai Institute for Energy and Carbon Neutrality Strategy, Fudan University, Shanghai, China

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Contributions

Y.W. and M.D. designed the study. M.D. collected and compiled data, performed the analyses and prepared graphs, with support from Z.L. and P.Z. on data collection, from M.S. and B.C. on analytical approaches and from M.S., B.C., L.S., M.J., Y.M., C.M.V.B.d.A., J.L., A.S.F.C., M.X., H.Y., J.M. and Y.W. on discussions. M.D. led the writing of the first draft, with input from M.S., B.C. and Y.W., and subsequent drafts were revised and approved by all co-authors to finalize the manuscript.

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Correspondence to Yutao Wang .

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Extended data figures and tables

Extended data fig. 1 system definition and ghg emissions inventory..

a , System boundary for inventory building and GHG emissions estimation. The processes in four stages from ‘cradle’ to ‘grave’ are described here. The critical factors for net-zero emissions along paper-related sectors are annotated by light-blue tags ( ① – ⑥ ). b , Schematic diagram of the carbon flows within the boundary of this study.

Extended Data Fig. 2 Diagram of global energy consumption of pulping, papermaking and printing accumulated in 1961–2019.

The full names of the abbreviations are as follows: CWP, chemical wood pulp; MP, mechanical pulp; NWP, non-wood pulp; RP, recycled pulp; PP, packaging paper; PW, printing and writing paper; PR, printing; NP, newsprint; HS, household and sanitary paper; OP, other paper. The top part denotes biomass-based energy, such as by-products (black liquid) or wood scraps.

Extended Data Fig. 3 Global GHG emissions of all processes accumulated in 1961–2019.

During S2 and S3, biomass energy use effectively helps this industry avoid considerable fossil-fuel emissions (represented by the dashed-bordered light-grey rectangle). In S4, the potential avoided emissions brought by energy recovery of waste paper and captured methane are not counted in the total net GHG emissions. The full names of the carbon sources and stocks in the bottom four panels are as follows: (1) forest carbon emissions during unsustainable pulpwood harvest and carbon dioxide emissions caused by chemical production and fibre collection activities; (2) carbon dioxide emissions caused by chemical wood pulping, mechanical pulping, recycled pulping and non-wood pulping; (3) carbon dioxide emissions caused by packaging paper production, printing and writing paper production, printing, newsprint production, household and sanitary paper production, and other paper production; (4) methane from landfill, methane from pulping wastewater treatment, methane from papermaking wastewater treatment, carbon stocks from landfill, carbon stocks from non-energy recovery, carbon stocks from in-use products, avoided emissions from energy recovery, avoided emissions from captured methane, carbon dioxide emissions during energy recovery, carbon dioxide emissions caused by landfill, carbon dioxide emissions caused by incineration disposal method, carbon dioxide emissions caused by the combustion of captured methane and carbon dioxide emissions caused by the escaped landfill methane oxidized near the surface.

Extended Data Fig. 4 Detailed information about forest carbon emissions in the first ten countries in Fig. 3 .

a , Breakdown of results of forest carbon emissions. b , Sensitivity analysis on the impact of sustainable certification rate on forest carbon emissions.

Extended Data Fig. 5 Net GHG emissions under three recycling measures in 30 countries when no other measures are taken.

a , Net GHG emissions for each country in 2050 under three scenarios: absolute recycling rate, the same recycling rate as 2019 and zero recycling rate. The colours of the ellipsoids in the top-left corner of the small charts indicate the different effects of recycling on net emissions. b , Map categorizing countries based on the effect of recycling rate scenarios on net GHG emissions. The colour of the ellipsoid in each small chart in a matches the colour scheme of the map in b ).

Extended Data Fig. 6 Net GHG emissions of 30 countries in 2019 and 2050 under the BAU scenario and 16 single-measure scenarios.

The order of countries is the same as that in Fig. 4a .

Extended Data Fig. 7 Statistics of factor scenario settings of net-zero scenarios.

The order of countries is the same as that in Fig. 5 . This figure, to some extent, embodies the measures of preference and the level of difficulty in achieving net-zero emissions for each country.

Extended Data Fig. 8 Distribution of net-zero scenarios by the number of best or medium measures.

a , Distribution of net-zero scenarios without best measures by the number of medium measures. b , Distribution of net-zero scenarios containing best measures by the number of best measures. The order of countries is consistent with Fig. 5 .

Extended Data Fig. 9 Carbon intensity of energy consumption in S2 and S3 across 30 countries from 1961 to 2019.

The dashed line represents the carbon intensity of total energy consumption, which includes biomass energy, whereas the solid line considers emissions from biomass energy as carbon neutral, focusing solely on emissions from fossil fuels.

Extended Data Fig. 10 Analytical framework of forest carbon emissions estimation.

The estimation method is constructed by means of a three-step process. Step 2 involves several important references: Persson et al. 64 , Henders et al. 65 , IPCC (2006) 88 and Pearson et al. 60 , 63 .

Supplementary information

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Pulp, paper, and packaging in the next decade: Transformational change

From what you read in the press and hear on the street, you might be excused for believing the paper and forest-products industry is disappearing fast in the wake of digitization. The year 2015 saw worldwide demand for graphic paper decline for the first time ever, and the fall in demand for these products in North America and Europe over the past five years has been more pronounced than even the most pessimistic forecasts.

But the paper and forest-products industry as a whole is growing, albeit at a slower pace than before, as other products are filling the gap left by the shrinking graphic-paper 1 The graphic-paper segment includes newsprint, printing, and writing papers. market (Exhibit 1). Packaging is growing all over the world, along with tissue papers, and pulp for hygiene products. Although a relatively small market as yet, pulp for textile applications is growing. And a broad search for new applications and uses for wood and its components is taking place in numerous labs and development centers. The paper and forest-products industry is not disappearing—far from it. But it is changing, morphing, and developing. We would argue that the industry is going through the most substantial transformation it has seen in many decades.

In this article, we outline the changes we see happening across the industry and identify the challenges CEOs and their leadership teams will need to manage over the next decade.

Changing industry structure

The structure of the industry landscape is changing. The changes are not dramatic individually, but the accumulation of changes over the long term has now reached a point where they are making a difference.

Consolidation has been a major factor in many segments of the industry. The big have become bigger in their chosen areas of focus. At the aggregate level, the world’s largest paper and forest-products companies have not grown much, if at all, and several of them have reduced in size. What they have done is focus their efforts on fewer segments. As a result, concentration levels in specific segments have generally, if not universally, increased (Exhibit 2). In some segments such as North American containerboard and coated fine paper, ownership concentration as defined by traditional approaches to drawing segment boundaries may be reaching levels where it would be difficult for companies to find further acquisition opportunities that could be approved by competition authorities.

A grouping of companies has emerged that is not identical to, but partly overlaps with, the group of largest companies, and is drawn from various geographies and market segments. Companies in this group have positioned themselves for further growth through high margins and low debt (Exhibit 3). Our analysis suggests the financial resources available to some members of this group for strategic capital expenditure could be five to ten times greater than other top players in the industry. This potentially represents a powerful force for change in the industry, and over the next few years it will be interesting to see how these companies choose to spend their resources. Some of these companies with large war chests and sizable annual cash flows deployable for strategic capex might even face a challenge to find opportunities on a scale that matches these resources.

Where there are leaders, there are also laggards. We believe the pronounced differences in performance among companies across the industry continues to pique the interest of investors and private-equity players in an industry that is already undergoing substantial restructuring and M&A.

Changing market segments

Whether companies are well positioned for further growth or still needing to earn the right to grow, they can expect demand to grow for paper and board products over the next decade. The graphic-paper market will continue to face declining demand worldwide, and our research has yet to find credible arguments for a specific floor for future demand. But this decline should be balanced by the increase in demand for packaging—industrial as well as consumer—and tissue products. All in all, demand for fiber-based products is set to increase globally, with some segments growing faster than others (Exhibit 4).

That picture is not without its uncertainties. One hazy spot in the demand skies might be concerns over how fast demand will grow in China. Expectations of growth from only a few years ago have proved a bit too optimistic, not only in graphic papers but also in tissue papers and packaging. And recently, as a result of turmoil in the market for recycled fiber, Chinese users of corrugated packaging have reduced their consumption, through weight reductions and use of reusable plastic boxes. Given China’s weight in the global paper and board market, even relatively modest changes can have significant impact.

How these demand trends will translate into industry profitability will of course be heavily influenced by the industry’s supply actions. Supply movements are notoriously difficult to forecast more than a few years out, but we believe the following observations are relevant to this discussion.

  • Graphic papers, particularly newsprint and coated papers but also uncoated papers, will continue to face a severe decline in demand and significant pressure to restructure production capacity. We are likely to see continuing machine conversions into packaging and specialty papers, as well as more innovative structural moves that include innovations in distribution and the supply chain. Such structural changes are already having an impact and the profitability of graphic-paper companies has reemerged from several years in the doldrums. The turbulence in graphic papers has meanwhile spilled over to packaging and tissue segments, with capacity increases in segments that don’t really need it.
  • Consumer packaging and tissue will be driven largely by demographic shifts and consumer trends such as the demand for convenience and sustainability. It will grow roughly on par with GDP. We expect innovation to be a critical success factor, particularly in light of recent concerns over plastic packaging waste, which could harbor both opportunities and challenges for fiber-based consumer packaging. But we are uncertain how far packaging players can drive innovation by themselves. Clearly, they can take the lead on materials development, but they may need to follow the lead of—and cooperate with—retailers and consumer-goods companies in areas such as formats, use, and technology. At the same time, the inflow of capacity from the graphic-paper segment will need to be managed.
  • Transport and industrial packaging will also see opportunities for innovation and a certain amount of value-creating disruption in the intersection between sustainability requirements, e-commerce, and technology integration. We estimate that e-commerce will drive roughly half of the demand growth in transport packaging over the next several years. As packaging adapts to this particular channel, it will have to find new solutions to a variety of issues, such as how to handle last-mile deliveries, the sustainability choice between fiber-based and lightweight plastic packaging, and the potential merging of transport (secondary) and consumer (primary) packaging, to name but a few.
  • Fiber has gone through some turbulent times in the past two years, largely to the delight of pulp producers and to the chagrin of users. Hardwood and softwood prices alike have seen steady increases since 2017, due to some slow start-up of capacity (hardwood pulp), limited capacity additions, and a certain measure of industry psychology. In the past two years, prices globally went through what we would term a “fly-up regime,” whereby prices are significantly and unusually higher than the cost of the marginal producer. Such situations, seen from time to time in many other basic-materials industries, are rarely long lived. Indeed, since the beginning of 2019, prices have come down—in China drastically so.

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But even with a readjustment of the market, the midterm prospects are likely to be in favor of the producers, with little new capacity until 2021–22 and some softwood capacity that is likely to be converted to other products, such as pulp for textile applications. For softwood particularly, challenges in expanding the forest supply are constraining new supply. Also, the fact that much of the industry’s softwood-production assets are aging and need complete renewal or substantial upgrades could further contribute to scarcity, especially since the scale of the investments required is a potential roadblock to them being made.

The lingering question is whether such supply-side challenges can trigger an accelerated development of applications that are less dependent on wood-fiber pulp.

Challenges for the next decade

In such an environment, what are the key challenges senior executives will need to address? What are the key battles they will have to fight? The paper and forest-products industry is often labelled a “traditional” industry. Yet given the confluence of technological changes, demographic changes, and resource concerns that we anticipate over the next decade, we believe the industry will have to embrace change that is, in character, as well as pace, vastly different from what we have seen before—and anything but traditional. This will pose significant challenges for CEOs regarding how they manage their companies.

We argue that there are three broad themes that paper and forest-products CEOs will have to address through 2020 and beyond:

  • Managing short-to-medium-term “grade turbulence”

Finding the next level of cost optimization

  • Finding value-creating growth roles for forest products in a fundamentally changing business landscape

Managing short-to-medium-term ‘grade turbulence’

The past couple of years have seen increased instability in forest-products segments. The negative impact of digital communications on graphic paper has led many companies to steer away from the segment and into higher-growth areas, either through conversion of machines or through redirection of investment funds. This is leading to a higher level of uncertainty and overcapacity in, for example, packaging grades. The instability has also been exacerbated by the capacity additions that primarily Asian producers have made despite the slowing demand growth in that region.

A case in point is virgin-fiber cartonboard. Several producers in Europe have converted machines away from graphic paper and into this segment, creating further oversupply in Europe and leading producers to redouble their efforts to sell to export markets. This is happening just as increasing capacity in Asia, and particularly in China, looks set to displace imports that have traditionally come into the region, mainly from Europe and North America. Some of the new Asian capacity could even find its way into export markets.

This development is likely to persist for several years until markets again find more of an equilibrium, and it poses challenging questions for companies. What, if any, safe havens exist for my products? How do I protect home-market volumes? How do I protect my export volumes? What is the appropriate pricing strategy to use in the different regions?

For CEOs looking to move into a new market segment, it will be equally important to make the right assessment of which segments to enter as they shift their footing. Where will I be the most competitive? How will my entry change market dynamics, and will this matter to me?

On the raw-materials (fiber) side, we have already described the past couple of years’ turbulence in virgin pulp. If that might seem to trend toward stabilization, the situation in recycled fibers is still very uncertain. As China, and gradually other Asian countries, have increasingly restricted the import of recovered fiber (as well as plastics and other recovered materials), the dynamics have shifted. While prices of old corrugated containers (OCC) and other papers for recycling have plummeted in North America and Europe, prices of domestic Chinese OCC have increased drastically, challenging both the price and availability of recycled-based corrugated board. In response, companies have set up capacity to produce recycled-fiber pulp to export to China, while the country is jacking up its import of containerboard for corrugated packaging, as well as virgin fiber for strengthening purposes.

This of course affects how companies, in any country, think about their fiber-supply strategies as well as their product focus.

Even though we see new ways of creating value in the forest-products industry, low cost is, and will remain, a critical factor for high financial performance. One of the characteristics shared by companies with high margins and high returns is that they have access to low-cost raw materials, primarily fiber. This will continue to be a high-priority area, albeit with some twists compared with today.

Beyond the price increases of the past couple of years, fresh fiber is facing other, more long-term, cost issues. It is unclear whether plantation land in the southern hemisphere (primarily for short-fiber wood) will continue to be available at current low prices. And as companies go to more remote areas to acquire inexpensive land, such as in Brazil, their infrastructure and logistics costs increase. Will higher productivity and yield allow the global industry to add ever more low-cost capacity, or are we going to see a gradual increase in raw-material costs? For long-fiber products, the difficulties to expand long-fiber pulp capacity will make such assets very valuable over the next several years. But at what point will development of the material properties of short-fiber pulps make them rival more expensive long-fiber pulps in a number of major applications?

Operating costs for paper and board production are another area where companies need to get a tighter grip. Despite the fact that this area receives continual focus from management, our experience suggests there is still significant potential for cost reduction by using conventional approaches to work smarter and reduce waste in the production chain. This is particularly the case in areas that are less the focus of management attention, such as converting.

Many companies need to go beyond the conventional approaches to a next level of cost optimization—and many are ready to take this step. Most if not all paper and forest-products companies have completed large fixed-cost reduction programs. But there are often broader systemic issues that companies still need to address to be able to build sustainable operating models. In addition, in some segments many companies fail to reduce fixed costs as quickly as capacity disappears. By radically rethinking the operating model, companies can significantly shift their fixed-cost structure. By doing so, they can set a very different starting point in terms of flexibility and agility for when market volumes go through their normal cyclical swings.

The paper and forest-products industry has much to gain from embracing digital manufacturing : according to our estimates, this could reduce the total cost base of a producer by as much as 15 percent. New applications such as forestry monitoring using drones or remote mill automation present tremendous opportunities for increased efficiency and cost reductions. This is also the case in areas where big data can be applied, for instance, to solve variability and throughput-related issues in each step of the integrated production flows (Exhibit 5). The industry is well placed to join the digital revolution, as paper and pulp producers typically start from a strong position when it comes to collected or collectable data.

At the customer-facing end, the opportunity for innovation is huge and has the potential to transform existing industries and create new ones, especially in packaging segments. Digital developments will also help disrupt previous B2B2C value chains, paving the way for direct B2C relationships between paper-product makers and end consumers, for example, in tissue products.

The digital world is unfamiliar territory to most paper industry CEOs. To avoid too much doodling with small uncoordinated efforts, it is necessary to undertake a thought-through program, preferably guided by digitally experienced people either on the top-management team or board.

Finding value-creating growth roles for forest products

For any paper-company CEO who looks out ten years, the really different challenges will not be around cost containment. Global trends are moving the industry into a new landscape, where the challenges and opportunities for finding value-creating growth roles for forest products are changing radically. For example, the industry’s historic linear value chains are giving way to more collaborative structures with players in and outside the industry. We believe examples will include new producer and distributor collaborations; pulp players collaborating more innovatively with non-integrated players; paper and packaging companies collaborating more intensively with retailers, consumer-goods companies, and technological experts; and new products such as bio-refinery products requiring novel go-to-market partnerships. Here are some interesting examples of how these and other trends could play out.

Staying relevant (and increasing relevancy) in a fast-changing packaging world. The packaging market is multifaceted and continuously morphing. Digital developments influence it both by stimulating demand for packaging used in e-commerce and by enabling the integration into packaging of sensors and other technology. E-commerce has highlighted new packaging topics such as improved product safety, the “un-boxing” experience, counterfeiting measures, optimization for last-mile delivery , and a growing interest—at least from the large e-commerce-based retailers—in the possibility of merging primary and secondary packaging. At the same time, the packaging industry has to deal with increasing pressures around cost, resource conservancy, and sustainability. That last topic has gained huge momentum in the past couple of years as concerns over plastic waste have added to the concern over CO 2 emissions from fossil-based packaging materials. Consumer-goods companies, retailers, packagers, and policy makers alike are now exploring a wide range of possible solutions for what tomorrow’s packaging will look like.

The opportunity for forest-products companies to develop a differentiated and distinct customer value proposition in this landscape has never been greater. Packaging-materials CEOs will have to address a number of choices and trade-offs as they seek the appropriate strategic posture. Should you be a pure upstream player or a packaging-solutions provider? Should you focus on fiber-based packaging only or providing multi-substrate solutions? Should you be at the forefront of technology integration and application development in packaging or focus on materials development?

To stay relevant, many companies in packaging are trying to move closer to the brand owner or end user. Only a few companies are positioned to successfully make this move, however, and even they should be cautious. We are already seeing brand owners and leading customers challenging the benefits of packaging companies coming with consumer-facing ideas such as complete packaging concepts. Some of these players would prefer packaging companies to focus instead on core competencies such as materials development or interfaces with other substrates such as plastics.

How the paper and forest-products industry thrives in the digital age

How the paper and forest-products industry thrives in the digital age

Finding the right path in next-generation bio-products. Wood is a biomaterial with exciting properties, from the log on down to fibers, micro- and nanofibers, and sugar molecules. A healthy niche industry making bio-products has existed for many years alongside large-volume pulp, paper, and board products. We are in the midst of an explosion of research activity to develop new bio-products, ranging from applications for nanofibers to composite materials and lignin-based carbon fiber. New processes  are being designed to extract hemicellulose as feedstock for sugars and chemical production while still keeping the cellulose parts of the wood chip for pulp products.

We believe wood-based products will find new ways to enlarge their footprint in a more sustainable global economy. But the challenges are legion, particularly for finding cost-effective production methods that can withstand competition not only from oil-based materials but also from other biomaterials. Finding the right balance between developing the “new” and safeguarding the “old” will be a crucial undertaking for executives running companies with access to fresh fiber.

Finding growth in adjacent areas. Over the past decade or two we have seen the larger forest-products companies performing a focus adjustment. Most companies have moved from being fairly broad conglomerates present in various forest-products segments to focusing on a few core businesses. To find value-creating growth in the next two decades, we expect companies to start broadening their corporate portfolio again, but broadening it around the core businesses they have been working on, so as to create differentiated customer value propositions. Finding value-creating adjacencies to the core business will be a challenging exercise in creativity and business acumen for executive teams.

Finding new value-creating growth for forest products will also put the spotlight on a number of functional executive topics. We believe the following will be most important.

  • Innovation: The forest-products industry has not been known for a fast-paced innovation agenda. By and large it hasn’t been necessary, as markets and demand characteristics have changed relatively slowly. In the future, however, innovation in products, processes, organizational setup, and business models will be imperative. For many companies, getting efficient innovation practices and organization up to speed will be an important challenge.

Talent management: The different skills required over the next ten to 15 years, dictated by developments such as new business models in an online world, increased need for innovation and commercialization of products, and digitalization’s impact on everything from manufacturing processes to the content of work will put particular onus on the talent pool  of forest-products companies. Installing an executive team that is able to understand new demands across customer businesses, digital, bio-products that cater to completely different value chains, and cross-industry collaboration will be a major task for CEOs and boards.

One particular war-for-talent battle that can become a key differentiator is the content of work. Our research on the future of work  highlights that already today, around 60 percent of all tasks, that is, not entire jobs or roles but their components, can be automated. And looking to the coming ten to 15 years, more than 30 percent of physical and manual skills risk becoming obsolete while technological skills will continue to grow very quickly. This will provide a critical and likely success-defining reskilling challenge for companies in the industry.

  • Commercial excellence: Paper and forest-products companies will need to transform their commercial interface to stay relevant, particularly in packaging and downstream paper. They will need to put in place a more professionalized and skilled organization that focuses on value creation instead of focusing primarily on sales volumes.

We believe the paper and forest-products industry is moving into an interesting decade, one that will see nothing less than a transformation of large parts of the industry. There will be many barriers to overcome and metaphorical cliffs to fall off. But the companies that are able to navigate through successfully can look forward to an industry that has a new sense of purpose and an increasingly vital role to play.

This article was updated in August 2019; it was originally published in May 2017.

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Peter Berg  is a director of knowledge in McKinsey’s Stockholm office, where Oskar Lingqvist  is a senior partner. Together they lead McKinsey’s global Paper & Forest Products Practice.

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Pulp and paper mill wastes: utilizations and prospects for high value-added biomaterials

  • Adane Haile 1 ,
  • Gemeda Gebino Gelebo 1 ,
  • Tamrat Tesfaye 1 ,
  • Wassie Mengie 1 ,
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A wide variety of biomass is available all around the world. Most of the biomass exists as a by-product from manufacturing industries. Pulp and paper mills contribute to a higher amount of these biomasses mostly discarded in the landfills creating an environmental burden. Biomasses from other sources have been used to produce different kinds and grades of biomaterials such as those used in industrial and medical applications. The present review aims to investigate the availability of biomass from pulp and paper mills and show sustainable routes for the production of high value-added biomaterials. The study reveals that using conventional and integrated biorefinery technology the ample variety and quantity of waste generated from pulp and paper mills can be converted into wealth. As per the findings of the current review, it is shown that high-performance carbon fiber and bioplastic can be manufactured from black liquor of pulping waste; the cellulosic waste from sawdust and sludge can be utilized for the synthesis of CNC and regenerated fibers such as viscose rayon and acetate; the mineral-based pulping wastes and fly ash can be used for manufacturing of different kinds of biocomposites. The different biomaterials obtained from the pulp and paper mill biomass can be used for versatile applications including conventional, high performance, and smart materials. Through customization and optimization of the conversion techniques and product manufacturing schemes, a variety of engineering materials can be obtained from pulp and paper mill wastes realizing the current global waste to wealth developmental approach.

Introduction

The demand and use of pulp and paper have marked the levels of civilization and development of many societies (Armstrong et al. 1998 ; Lwako et al. 2013 ). The pulp and paper mills mainly utilize wood sources for the production of pulp and paper. Though appropriate quantitative analysis of waste produced from pulp and paper mills has not been done yet; in general only a few percent of the wood sources are utilized for the actual pulp and paper production (Bajpai 2015b ). The rest is discarded as solid and liquid waste. Considering the developing countries' scenario both quantitative and qualitative analysis of biomass generated from the mills has not been done yet. Except for a few percent of wastepaper utilized in paper recycling the rest of the waste is left in the landfill or incinerated with no commercial significance; besides no satisfactory waste recycling scheme is implemented. Furthermore, in developing countries, the trend towards the conversion of the wastes into valuable materials is not practiced appreciably (Bajpai 2015d ).

Environmental sustainability is a priority issue as far as sustainable development of nations is progressive. It is also a global concern recently to get rid of the factors that counteract environmental sustainability such as climate change, natural sources depletion, ecosystem prevention, and environmental degradation (McKinnon 2010 ; Bajpai 2018b ; Carroll and Turpin 2002 ). The wastes from pulp mills one way or the other have a contributory effect on these factors and a feasible remedy needs to be designed for the overall protection of the environment for its sustainability. The pulp industry wastewater is generated from several sources like washing of raw wood materials before pulping, washing of cooked pulp and bleaching pulp, and finally, chemical recovery system (Song et al. 2019 ). Solid waste is produced primarily from the rejection of screening, primary and secondary sludge from wastewater management, and lime sludge from the chemical recovery system (Đurđević et al. 2020 ). Currently, a large amount of solid and liquid wastes are generated by the pulp and paper mills and environmental aspects are becoming a major concern that needs intervention.

The waste generated from pulp and paper mills adversely affects the environment from different perspectives. The emissions from pulp and paper industries have a significant effect on the environment. The generated waste from the pulp and paper industry causes severe harm to aquatic life, disturbs the food chain, and also causes various health implications (Gupta et al. 2019 ). The effect of pollutants on the environment has been assessed many times, but their mitigation still has a significant challenge (Gupta et al. 2019 ). Besides, many of the developing countries do not produce pulp. These paper mills use imported pulp and waste paper as raw materials.

It is vital from an environmental and socio-economic social point of view to utilize appropriate technology to convert the wastes from pulp and paper mills to highly valuable products that will have an impact on everyday life. This requires a thorough analysis of generated biomass quantitatively and qualitatively and the current review is limited to envisaging the availability of biomass from the said mills, the current utilization scheme, and the potentiality for biomaterial production and diversified application. Besides protection of the environment from undesired waste impacts, utilization of the wastes will greatly support the product diversity scheme and economic growth potency (Landrigan and Fuller 2015 ).

Overview of pulp and paper industry

Status of pulp and paper industry at a global perspective.

As one of the most important industries worldwide pulp and paper mills supply varied products for around 5 billion people for versatile applications (Bajpai, 2015c ). The paper is manufactured from pulp and a huge amount of trees is consumed for the pulp production with different shares by different countries in the world (Brännvall 2009 , Cabreha 2017 ). The overall trend in the consumption of paper and paperboard by different countries and the forecasted consumption is shown in Fig.  1 .

figure 1

Yearly trend and future forecast on world paper production

The pulp and paper industry is one of the largest industries in the world. The consumption of paper is dominated by North American, Northern European, and East Asian countries (Fig.  2 ) (Diesen et al. 1998 ; Gopal et al. 2019 ; Hammett et al. 2001 ). Other dominant countries with significant pulp and paper industries are Australia and South America. A massive and key contribution is expected from China and India in the upcoming few years.

figure 2

Global consumption of paper by major countries

Considering the significant variation in consumption of paper products per person from the country to country the global consumption of paper and paper board is estimated on average around 55 kg/person per year. The utilization of paper and board is increasing year to year though digitalization is expected to influence production and consumption in different ways. The dominant countries like North America, Europe, and Asia and low producers and consumers like African countries are still utilizing huge amounts of paper.

The key components in the paper are cellulose sheets. There are also other constituents derived from the woody and related raw materials. The raw materials for manufacturing pulp and paper are ample and mainly consist of cellulose. Besides wood which is a chief source of cellulose, recycled paper and other cellulose bearing agricultural residues can be used as a raw material. The scenario in developing countries showed around 60% cellulose is obtained from jute, sisal, bamboo, bagasse, and similar non-wood resources.

Wood is considered the primary raw material and the major source of pulp in paper production (Eugenio et al. 2019 ). The gross characteristic composition of wood indicates its major constituents are cellulose, lignin, and hemicellulose. It also contains a trace amount of extractives of different types.

Numerical observation revealed that wood contains around 40–50% of cellulose (Table 1 ) (Sjöström and Westermark 1999 ). Considering ultimate properties such as strength and printability of paper it is possible to use hardwood and softwoods separately or combined in the manufacturing process. (Liu et al. 2018 ; Asmare 2017 ).

An onsite availability study has been conducted on paper mills in Ethiopia. According to the study report, 25 paper enterprises are assessed and of which 12 companies are effective in producing different kinds of paper products with measurable production losses (Table 2 ).

The main aim of the preliminary study was to determine the availability of waste and possible ingredients for biomaterial synthesis. The production loss indicated the potential availability of wastes and allied potential ingredients from the mills. The availability study in the specified country ensured a potential for conversion of pulp and paper mill biomass into biomaterials. Limitation to produce pulp indigenously can also be solved for the satisfaction of the demand for paper and paper products.

Overview on pulp and paper manufacturing process

The availability of raw materials for pulp and paper manufacturing is versatile and mainly cellulosic fibers from wood and selected plants are utilized. Besides wood used most widely in many countries of the world plant resources such as sugar cane residues, residues on cottonseed, and remnants from flax and rags are also used (Osman Khider et al. 2012 ; Asmare 2017 ; Enayati et al. 2009 ; Jahan et al. 2004 ; Tutus et al. 2010 ). Besides, in case of scarcity of virgin raw material resources recycled paper after proper after-treatment, through appropriate blending and recycling process, is used in some paper manufacturing trends.

The different pulping operations and the integrated paper manufacturing process are shown in Fig.  3 . Two steps are involved in the manufacturing of paper. First cellulose sheets are converted into pulp which is the intermediate material for paper production. The second step involves the conversion of pulp into the paper with the necessary after-treatment depending on the targeted end-use. The overall manufacturing process is accompanied by multiple stages which mainly involve raw material preparation and handling, controlled pulping, and discrete or continuous paper manufacturing. The pulping involves the actual making of the pulp followed by pulp washing and screening. After proper chemical recovery and bleaching, the stock is prepared. Finally, the papermaking is carried out which itself has different stages. Pulp mills and paper mills may exist separately or as integrated operations (Bajpai 2018b ; de Alda 2008 ; Ragauskas 2002 ).

figure 3

Process flow in pulp and paper manufacturing mills

Operational mechanism of pulping

Pulp manufacturing starts with raw material preparation, which includes debarking, chipping, chip screening, chip handling, and storage (Bajpai 2011 , Brännvall 2009 ). The pulp needs to be free of dirt and superficial materials such as bark, and debarking is done for making the pulp physically clean. The next operation in raw material preparation is chipping to ensure better handling of the logs which is done through cutting to get the required size of logs for the subsequent pulping process. Pulping requirements need to be considered in optimizing chip handling and determining the suitable chip storage conditions (Bajpai 2015a ).

The pulping operation involves the separation of the wood chips to get the fibrous materials. In the process, lignin is removed from the lignocellulosic wood and the individual cellulose fibers are isolated. Though there are different pulping methods chemical and mechanical methods are the most widely used in paper mills. Either of the three techniques namely kraft, soda, or sulfite are used in the chemical pulping approach. In all the cases the cellulose is extracted via cooking of the chips in the aqueous solutions of the reagents at elevated pressure and temperature (Bajpai, 2011 , 2015a ). Physical energy is used in the mechanical pulping approach which mainly involves the removal of cellulose through grinding or shredding.

The most widely used pulping process is kraft pulping and uses alkaline cooking liquor of sodium hydroxide (NaOH) and sodium sulfide (Na 2 S) to digest wood. In the process, a digester is used for mixing the chips with the kraft cooking solution. The kraft pulping process uses an alkaline cooking liquor of sodium hydroxide and sodium sulfide to digest the wood. The process involves the digestion of wood chips at high temperature in the range of 145–170 °C and pressure in “white liquor,” which is a water solution of sodium sulfide (Na 2 S) and sodium hydroxide (NaOH), for a few hours (Huber et al. 2014 ). During this treatment, the hydroxide and hydrosulfide anions react with the lignin, causing the polymer to fragment into smaller water/alkali-soluble fragments and isolating the cellulose fibers.

After the wood chips have been cooked, the contents of the digester are discharged under pressure into a blow tank. As the mass of softened, cooked chips impacts the tangential entry of the blow tank, the chips disintegrate into fibers or “pulp.” The pulp and spent cooking liquor (black liquor) are subsequently separated in a series of brown stock washers (Alén 2019 ). After the required cooking is carried out the cooking liquor is discharged under pressure into a blow tank. The mechanistic tangential flow of the cooked chips in the blow tank isolates the chips into pulp (Yang and Liu 2005 ; Al-Dajani and Tschirner 2008 ).

After pulp production, after-treatment of pulp is carried out through washing to ensure removal of contaminants which include uncooked chips, and recycling of residual liquor is carried out via pulp washing operations. The pulp washers separate the pulp from the spent cooking liquor during chemical pulping (Dimmel and Gellerstedt 2009 , Chakar and Ragauskas 2004 ). After washing, screening is done to remove remaining off-size particles such as fragments from barky matters, bigger size chips, and chips that remained uncooked, and the material is delivered to the pulp bleaching process.

A very important process in the pulp mill is bleaching used for the removal of coloring and allied impurities in the raw pulp. Bleached pulp grades are used to produce white papers. Nearly half of the Kraft production is in bleached grades. The bleaching of pulp is carried out to increase the whiteness and brightness of the pulp (Bajpai 2013 ; Hammett et al. 2001 ). This is important for making the paper suitable for selected products such as those produced in tissue and printing enterprises. Enhancement of physical and optical qualities of the pulp is achieved by removing impurities such as entangles of fibers, barky fragments, or decolorizing the lignin making it a potential benefit in the chemical pulping process (Al-Dajani and Tschirner 2008 , Chakar and Ragauskas 2004 ).

Kraft bleaching has been refined into a stepwise progression of chemical reaction, evolving from a single-stage hypochlorite treatment to a multi-stage process, involving chlorine), chlorine dioxide, hydrogen peroxide, and ozone. The optimized and controlled condition must be used in the bleaching process. If bleaching conditions are too severe there will be fiber damage, leading to a lower strength of the paper (Brännvall 2009 ; Angevine, 1998 ). After bleaching stock preparation is conducted to convert raw stock into finished stock to be used in the paper machine. Raw stock can be available in different forms. In batch processes, the delivery can be in loose pulp or bale and the integrated pulp to paper conversion suspensions can be used as well (Dimmel and Gellerstedt 2009 , 2009 ).

In the chemical pulping process, it is necessary to recover the used cooking chemicals, and a proper chemical recovery system is needed (Gellerstedt 2009 ; Walker 2004 ). At the pulping mills, the weak black liquor also called spent cooking liquor, from the different rinsing stages is transferred to the chemical recovery which as well is situated alongside the mills (Santos et al. 2011 ; Al-Dajani and Tschirner 2008 ). The chemical recovery process is conducted at different stages to ensure proper reconstitution of the cooking liquor. Initially, the weak black liquor is concentrated followed by combustion of organic matters and reduction of inorganic matters. Finally, the cooking liquor is reconstituted in the required concentration. All the stages need critical control on the parametric allowances. The quality of paper produced from the pulp is affected by the quality of water and different companies have incorporated water treatment schemes along with the pulping process. To prevent deposits on pulp, water treatment chemicals such as anti-scale agents and pitch control agents are incorporated during the route of manufacturing.

As part of pulping process dregs, lime mud, and grits are generated in the chemical recovery process. Green liquor contains sodium sulfide and sodium carbonate; and insoluble unburned carbon and inorganic impurities called dregs, which are removed in a series of clarification tanks. The green liquor is a residue of dissolution of the molten inorganic salts (smelt) from the black liquor concentration process (Angevine 1998 , Brännvall 2009 ). The lime mud is generated in the causticization process of chemical recovery in the decantation of the green liquor using calcium oxide (lime) (Ai et al. 2007 ). The grits are originated from the white liquor slurry in the slacker by gravity and classified as unreacted lime (Kinnarinen et al. 2016 ). Grits are insoluble compounds, most of which come from purchased lime, which collect in the slacker and need to be removed and disposed of.

Final pulping operations are involved in the boiler unit which causes the generation of large content of ashes. In particular, fly ash is produced as by-products of the biomass combustion process which is generated during the high-temperature combustion of hog fuel in power boiler units (Cherian and Siddiqua 2019 ). As the flue gas approaches the low-temperature zones, the fused substances solidify to form fly ash. The fly ash consists of fine particulates and precipitated volatiles, typically with a high specific surface area, whereas bottom ashes tend to be coarser in texture (Cherian and Siddiqua 2019 ; Scheepers and du Toit 2016 ).

Most of the pulping operations so far especially those involving chemicals are not ecofriendly. Nowadays new pulping methods are used for manufacturing different grade pulps that utilize enzymes (Lin et al. 2018 ). These enzymatic pulping techniques are being used for the preparation of dissolving pulp for the production of fibrous materials. In the enzymatically assisted pulping process xylanase, cellulase, and hemicellulase enzymes are utilized for segregation of the pulp from the rest of lignocellulosic mass and after-treatment (Lin et al. 2018 ; Rashmi and Bhardwaj Nishi 2010 ; Yang et al. 2019b ). It is reported that the purity of enzymatically produced pulp is better than conventional kraft pulping processes.

Papermaking process

The process adopted for the making of paper is identical for all pulp types (Bajpai 2018b ; Woiciechowski et al. 2020 ). The pulp from the chest compartment is screened which when required is refined to the required level. The pulp slurry is formed by mixing the refined pulp in water in a wet end operation. This slurry at the headbox is put through a paper machine and pressed by the press compartment. In the press section, the sheet forming process is commenced through the draining of the water. The next operation is passing of the formed sheet in a dryer which involved hierarchically arranged compartments of the dry end for coating and drying. The final dried and finished product is transferred to calendaring operation for reducing the thickness of paper as required and sheet surface smoothing before winding on to the take-up reels.

Availability of by-products from pulp and paper mill

A global review of manufacturing sectors divulged that 17% of the total global waste comes from paper industries (Fig.  5 ) (Karak et al. 2012 ; Sakai et al. 1996 ). Pulp and paper mills contribute to air, water, and land pollution and discarded paper and paperboard make up roughly 26% of solid municipal waste in landfill sites (Pati et al. 2008 ; Ritchlin 2012 ). Waste data based on relative waste analysis from a specific global company revealed the large contribution of pulp and paper mill waste to the total solid waste indicative of a need to set up a platform for strategic intervention for the realization of a green environment (Mladenov and Pelovski 2010 ; Ince et al. 2011 ). The study reveals that from a total solid waste generation of 238,771 thousand tonnes, around 186 thousand tonnes is generated from pulp and paper industries.

Different types of solid wastes and sludge are generated in the pulp and paper mills at different sites of the process (Fig.  4 ). Potential wastes are generated from wood preparation and the actual pulp manufacturing and paper-making stages. Furthermore, an ample amount of different types of wastes are generated from chemical recovery, effluent treatment, and paper manufacturing methods that utilize recycled paper routes (Camberato et al. 2006 ; Akbari et al. 2018 ).

figure 4

Sites of waste generation in pulp and paper manufacturing

Among different factors that affect the identity and amount of generated waste from pulp and paper, mills is the type of manufacturing process amplified with the wastewater treatment technologies adopted. The pulp and paper mill waste mainly includes rejects at different stages such as woody and barky residues and sand particles, black liquor, and wastewater sludges. Inorganic sludges are isolated from the chemical recovery station and are composed mainly of calcite lime mud, the slacker grits, and green liquor dregs (Bird and Talberth 2008 ; Environmental 2007 ; Leponiemi 2008 ).

The sources of wastewater treatment residues as part of potential sludge are conveyed from two sources. The major part is the primary sludge from the entire manufacturing route and those generated from the secondary clarifier are categorized as biological sludge (Simão et al. 2019 ). Also, the sludge from the water treatment is regarded as chemical flocculation sludge. Deinking sludge from recycled paper production which contains mainly tiny fibers or fragmented fines and additives is another source of waste (Simão et al. 2018 ). The major source of waste from different stages of pulp and paper manufacturing is summarized in Table 3 .

The regions and different recycling processes and allied recycling rates determine the quantity of biomass generated from paper production. The variation within regions is also very wide. Due to internally established treatment and utilization routes for generated waste along with the manufacturing process by different pulp and paper mills, there is limited quantitative data on the total amount of waste generated from the mills. Estimated data on the quantity of solid waste from sample pulp and paper mill is reported. The potential woody wastes and rejects are from the preparation of pulpwood and contribute to solid waste generation (Table 4 ).

The predominant biomass available in large quantities in pulp mills is the black liquor. It is reported that kraft mill producing bleached paper engenders around 1.7–1.8 tonnes of black liquor per one tonne of pulp on a bone dry basis (Leponiemi 2008 ). This highly viscous liquor is a result of the conversion of almost half of the raw chips used in the hopper of the pulping operation. A report of IEA revealed about 170 million tonnes of black liquor per year is released from pulp and paper mills worldwide.

Another portion of the waste involves sludge of different types namely primary, secondary, and deinking sludge. From a total sludge of 40–50 kg per tonne of the virgin paper production, the primary sludge accounts for 70% and the rest 30% is the secondary sludge. On a glance approximation, the sludge generated from the manufacturing of different paper products varies from 20 to 40% on a dry mass. The grade of paper and the specific type of process adopted for the manufacturing of the paper product determines the amount of sludge generated. (Quina and Pinheiro 2020 ). In comparison, the amount of waste sludge generated from industries that utilize the recycled paper approach produces a large amount of sludge than the conventional approach through virgin raw materials. From each one tonne of reclaimed paper, a total of 300 kg sludge is generated.

Depending on production capacity and the type of pulping a large amount of fly ash is released annually from pulp and paper mills (Environmental 2007 ; Mikkanen 2000 ). A recent report in Finland indicated a release of 240,000 tonnes of ash every year. As an illustration of the availability of waste biomass from pulp and paper mills, it is reported that the collective fly ash and wood ash produced from Canadian mills is 1 million tonnes per year.

Most of the pulp and paper mill wastes have an impact on the environment and create health problems. The major sources of pollutants at different stages of pulping and paper manufacturing are summarized (Table 5 ) (Gavrilescu et al. 2012 ). The environmental impact generated by the manufacture of pulp and paper results mainly from wood pulping and pulp bleaching. In pulping processes, sulfur compounds and nitrogen oxides are emitted into the air, and during pulp bleaching, chlorinated and organic compounds and nutrients are discharged to the wastewaters (Gavrilescu et al. 2012 ; Singh and Chandra 2019 ).

The pulp paper industries release very complex organic and inorganic pollutants mainly from pulping and bleaching stages. Particularly, sulfur compounds and nitrogen oxides are emitted into the air, and chlorinated and organic compounds and nutrients are discharged to the wastewaters (Gavrilescu et al. 2012 ; Bank 1999 ). The pollutants are gaseous, inorganic, and organic type. The major pollutants include hydrogen sulfides, sodium sulfide, sulfur, chlorine dioxide, ferrous, copper, hexadecanoic acids, octacosane, phenol, and β-sitosterol. It has been reported that the different pollutants cause environmental and health impacts in terms of respiratory disorder and irritation to the skin, neurotoxicity, and direct toxicity of effluent to the reproductive system in aquatic flora and fauna are reported. Several of these pollutants are reported to contain endocrine-disrupting chemicals. Furthermore, the environmental pollution caused by the pollutants poses a threat to aquatic life as well as to plants and human beings (Bank 1999 ; Gavrilescu et al. 2012 ; Singh and Chandra 2019 ) .

Current utilization of pulp and paper mill waste

Characteristic components of major by-products.

The wastes from pulp and paper mills are both of organic and inorganic types. Most of the biomass generated from pulp and paper mills is organic residues. Black liquor consists of organic polymers (lignin, polysaccharides, and resinous compounds of a low molar mass) and inorganic compounds mainly soluble salt ions (Fig.  5 a) (Viel et al. 2020 ).

figure 5

Black liquor: a Gross structure of black liquor; b Black liquor separation

Black liquor is separated from the pulp in washing (Fig.  5 b). The biorefinery approach can be used for the conversion of lignin and hemicellulose in black liquor into biomaterials (Vakkilainen and Välimäki 2009 ; Vakkilainen 2016 ).

Black liquor being the major waste other potential wastes include sawdust, sludges of different types, waste paper, and fly ash. The major inorganic type wastes from pulping and after-treatment stage include the dregs, lime mud, and grits. The different wastes are obtained as extracted from different pulp and paper industries are summarized (Fig.  6 ).

figure 6

Major wastes generated from pulp and paper mills: a sawdust; b sludge; c waste paper; d inorganic wastes (dregs, lime mud, grits); e Fly ash

The sawdust (Fig.  6 a) as woody material is composed of cellulose, lignin, and hemicelluloses (Bajpai 2018a ). The cellulose composition of sawdust is by far higher than the lignin content. Accordingly, the interest in biomaterial synthesis relies on the cellulose component of the sawdust. The current preferably adapted extraction of cellulose from sawdust involves the preparation of sawdust (drying, cutting, and conditioning); dissolution of wood in appropriate ionic liquid, and precipitation of cellulose through the removal of lignin.

Another potential source of cellulose is wastewater treatment plants and recycled paper converters. The virgin or waste recycling sludge (Fig.  6 b) constitutes cellulosic materials. The mill sludge accounts for the main waste from pulp and recycled paper production. Pulp and paper mill sludge is an organic residual generated from wastewater treatments (Faubert et al. 2016 ). Per unit of paper production 23.4% sludge is generated. The major components of the paper mill sludge are inorganic residues and organic cellulosic fines and fragments (Albuquerque et al. 2015 ; Abdullah et al. 2015 ). The organic constitutes in primary sludge mainly consist of cellulosic fibers.

A noticeable quantity of cellulose can also be obtained from waste paper (Fig.  6 c) which is a release of every paper utilizer with a huge amount from office and related service providers. Directly or as part of recycling residue, the waste paper is considered as a major source of cellulose, and using appropriate cleaning and recycling procedures the cellulose can be made use of as a raw material for biomaterial synthesis (Kim and Kim 2019 ).

Inorganic wastes (Fig.  6 d) namely liquor dregs, calcite mud, and slacker grits are also considered as the major portion of solid waste in the mills (Quina and Pinheiro 2020 ). These mineral wastes are generated during the chemical recovery process at the pulping mill. The green liquor dregs are obtained The inorganic biomasses contain different types of minerals (Bird and Talberth 2008 ; Leponiemi 2008 ). The mineral Gipsite and Calcite are present in the dregs and the mud, whereas the minerals such as brucite, larnite, pirssonite, portlandite, and calcite are ingredients of the biomass grits. The mineral content of these wastes can be made administered and used for making biomaterials.

The successive development in the pulp and paper mill has headed to the release of a large quantity of fly ash (Fig.  6 e) as a result of combustion processes of waste biomass. The elemental composition survey on fly ash from pulp and paper mills revealed that the ash consists of different minerals predominantly iron oxide, silica, and alumina. The fly ash also consists of other metal oxides such as oxides of sodium, calcium, magnesium, potassium sulfur, and titanium (Na 2 O, CaO, MgO, K 2 O, SO 3, and TiO 2 ) in variable quantities. Through polymerization, the metal oxides can be converted to biopolymers for diversified end-use. The widely and adopted and conventionally established way of valorization of fly ash is geo-polymerization. In the polymerization process demand-driven three-dimensional aluminosilicate and similar materials so-called geopolymers are synthesized (Cherian and Siddiqua 2019 ; Sjöström and Westermark 1999 ).

Disposal technique

Waste management in pulp and paper mill.

The pulp and paper mill generates a large volume of wastes with an estimate of around 100 tonnes per 550 tonnes of pulp production. Though the toxicity of pulp and paper wastes is minimal appropriate disposal technique is required for appropriate management of the land, environment, and allied issues (Monte et al. 2009 ). As per the environmental policies recommend based on directives of the waste framework the landfill must be reduced by avoiding disposal of waste from industries. In certain cases, an obligation is placed for selected wastes to terminate as a waste resource. The wastes from pulp and paper mills have a tremendous negative and adverse impact on the environment. Inherently high consumption of water is the major cause, and the problems are wider in terms of generation of effluent and other wastes of solid and liquid type. These solid and liquid wastes along with air emissions require effective disposal and treatment approach (Bajpai 2015d ).

Three different approaches can be used in pulp and paper mill waste management. The first choice is to minimize waste in ensuring product efficiency, higher yield of materials, and lower waste management (Mladenov and Pelovski 2010 ). The second choice is to find a suitable way for reuse to maintain cost improvement and lower environmental approach. This could be done by material or energy valorization of the generated wastes. The final option is landfilling which shall only be done when a choice is not an option.

In minimizing waste generation, it is necessary to cope up with established concrete environmental legislations. In line with this concerns related to cost of disposal, treatment technologies, and opt for new utilization schemes need to be taken into consideration. Different techniques are adopted for the reuse of the mill wastes which include burning or incineration, biofuel production, gasification, pyrolysis, and anaerobic digestion (Bajpai 2015d ; Mladenov and Pelovski 2010 ). As far as the application is concerned; for solid wastes incineration techniques is widely used, whereas anaerobic digestion is widely practiced for wastewater. Landfilling is still the most widely adopted disposal technique.

Current trends in the disposal of pulp and paper mill wastes

In the current world pulp and paper mill practice, both landfill and incineration techniques are applied for the disposal of waste. The opt for incineration and other reuse options differ from country to country and are based on technology availability and economic growth hierarchy (Ince et al. 2011 ; Bahar et al. 2011 ). Most of the solid wastes generated from pulp and paper mills are disposed of as landfills. Landfilling with its critical limitations regarding increasing volumes and the possibility of hazardous substances is still the most widely used disposal technique by pulp and paper mills. The hazardous matters in the watercourse impose environmental dangers as well. As far as the context in most of the developing countries is concerned most of the waste is still landfilled and some are incinerated.

The black liquor is incinerated or gassed as a source of fuel energy and where the technology is not available it as well is discarded as a landfill. Rejects are dewatered and burnt for energy recovery (Bahar et al. 2011 ; Naqvi et al. 2010a ). Other wastes like sawdust and woody matters are also discarded in the landfill. The destination of liquor dregs, grits, lime mud, and mill ash is the landfill after dewatering and drying.

The wastewater sludge is disposed of through a burning approach. The conventional sludge treatment process includes the thickening of the sludge waste which is dehydrated by mechanical means. The prepared sludge is incinerated at optimal conditions. In the pretreatment process blending of sludges is done with the addition of polymer and dewatering is carried out to obtain a dry solid content of 25–40%. Incineration which is the widely practiced internal route for biofuel production in pulp and paper mills is carried out. The deinking sludge from recycled paper production can be incinerated or reused in other mills (Faubert et al. 2016 ).

Current uses of pulp and paper mill waste

The pulp and paper mill waste have different chemical constituents and physicochemical characteristics. Based on their chemical and physical properties the wastes are widely used in conventional and industrial applications. As most of these wastes are mainly based on woody features comprising lignocellulosic behavior they are used as fuel or energy sources for pulp and paper mill or other industries (Simão et al. 2018 ; Sarkar et al. 2017 ). Many are used for construction and building as potential and economic substitutes. The major schemes and sectorial applications followed in the current utilization of wastes from pulp and paper mill are summarized (Table 6 ).

The incinerated black liquor in recovery boilers is used in pulp and paper mills as an optional energy source as it provides steam. It is also possible to reclaim pulping chemicals for reuse. The current and alternative technology for reuse is the gasification of black liquor. This process has the potency to replicate the amount of production energy used in the pulp and paper mill (Naqvi et al. 2010b ). The sawdust as well can be used as a secondary raw material for pulp production and recycled for paper manufacturing (Srinivasakannan and Bakar 2004 ). It can also be used as filler for the manufacturing of bricks and cement material in the field of construction.

The sludge from pulp and paper mills can be recycled via different routes. Mainly the sludge can be used in construction and energy and as a chief source of energy. The suitability of sludge for utilization in power generation is the inherent compounds present in the sludge that are organic with a high degree of combustibility.

Commonly cement plants use fly ash as their raw material together with other ingredients. Fly ash is also used as fertilizer in modern agricultural practice. The suitability especially in cement application is due to the inherent high strength to weight ratio of fly ash as compared with other cement materials. This is also supplemented by carbon footprint and minimal energy consumption which makes fly ash a replacement for cement in cost-effective construction and eco-efficient geotechnical applications (Cherian and Siddiqua 2019 ). It can also be used as an immobilizer of pollutants. Their physical properties such as mechanical resistance and durability make the fly ashes used in concrete systems utilized in hostile environments.

The inorganic wastes from pulp and paper mills have been engineered for different applications (Fig.  7 ). Green liquor dregs have shown promising effects for correcting soil acidity and fertilizer. Dregs have also been used in wastewater treatment. The inorganic grits are mainly composed of calcium carbonate and can be used for the replacement of calcareous raw materials such as in building and construction (Quina and Pinheiro 2020 ).

figure 7

Current utilization of pulp and paper mill inorganic wastes ( GLD green liquor dregs, SG slacker grits, LM lime mud, BFA boiler fly ash)

Agriculturalists already investigated the lime mud can be used in soil healing such as for fertilizing and remedial agents. Compositionally lime mud is similar to the commercially available calcium carbonate and can be used as a potential substitute and replacement in building materials. The crude carbonate component of lime mud provides high alkalinity which makes the use of lime mud in precipitation and immobilization of heavy metals in watery streams, removal of phosphorus, and stabilization of sewage sludge.

Utilization of pulp and paper waste: future prospects

Most of the pulp and paper mill wastes in developing countries adopt recycling for lower grade paper; recycling being the only used pulp and paper mill waste utilization method. The scope and technology for utilization of the different wastes for other industrial applications are practically not available and not attempted (Raut et al. 2012 ; de Alda 2008 ). The biomass from pulp and paper mill is composed of different ingredients. The major wastes of biomaterial concern from these mills are black liquor, woody residues including sawdust, sludges of different types, and fly ash.

An abundant quantity of the mill wastes is disposed to landfill, and some are incinerated. Instead using an appropriate biorefinery approach, it is possible to extract different ingredients from the biomass for versatile utilization as a biomaterial in different fields of applications. Through the biorefinery approach environmental pollution is reduced or eliminated, product substitution is enhanced. Furthermore, the allied spinoff company for biomaterials and the industrial-scale prospect will boost the economic growth. The potential ingredients of current concern from the biomass are identified (Table 7 ). Based on the characteristics of ingredients in each biomass potential beneficiation routes are proposed for high value-added materials (Simão et al. 2018 ; Rajput et al. 2012 ).

The general challenges with regards to the forecasted application of pulp and paper industry wastes as high value-added materials can be broadly classified into three patterns. One major challenge is the lower yield from each biomass in terms of the continuous supply of certain waste types. The lower yield of biomaterial ingredients from selected biomass can be enhanced by the integration of pulp and paper industries especially in developing countries like Ethiopia. Another challenge which is still prominent in developing countries is the availability of suitable and integrated waste to energy and related biorefinery system (Ismail and Nizami, 2016 ; Diep et al. 2012 ). This directly affects the mass production of high valued-added materials from pulp and paper industry biomass. The other potential challenge is the adequacy of labor in terms of skill as the production of the high value-added biomaterials requires stringent control allied with health and environmental safety concerns and regulations. There are also specific challenges in terms of each high-value-added biomaterial addressed in the review. These challenges need critical investigation and can be amended with versatile possibilities as far as continuous marketability of the biomaterials and their high value-added application is targeted.

Beneficiation of black liquor for high value-added materials

High-performance carbon fiber from black liquor lignin.

There is an estimated 70 million tonnes of lignin from pulping processes worldwide (Dessbesell et al. 2020 ; Bajwa et al. 2019 ). Structurally lignin is a heterogeneous aromatic polymer and consists of mainly three precursors: p-coumaryl alcohol, coniferyl alcohol, and sinapyl alcohol (Fig.  8 ) (Chen 2012 ). It is a natural macromolecular with multiple aromatic ring compounds consisting of hydrophobic non-polar substructures of phenyl propane and polar groups like carboxyl.

figure 8

Major precursors of lignin ( a ) typical structural model of lignin ( b )

Several approaches have been used to purify the spent black liquor for the production of pure lignin (Hubbe et al. 2019 ; Xinde 1996 ). Acidification via precipitation is the most prominent. The extraction involved precipitation of the black liquor in acid solution, coagulation, and removal of lignin (Norberg 2012 ; Olsson et al. 2017 ; Bengtsson et al. 2018 ).

The biomaterial options for lignin are versatile. The modern interest in carbon fibers is very crucial, and lignin is one of the important biomasses for the production of carbon fibers. Carbon fiber is known for its extremely high strength-to-weight ratio which makes it an ideal engineering material for a load-bearing element in lightweight high-performance composites. The versatile application of carbon fiber in the modern industry especially in composites is related to its low density and excellent mechanical properties.

High-performance carbon fibers are currently produced primarily from polyacrylonitrile (PAN). Carbon-rich precursor fiber with a carbon content of more than 90% is required for the manufacturing of carbon fibers. Once the precursor is availed the transformation is carried out in a two-stage thermal process. The delicate and rigorous web spinning process used for polyacrylonitrile-based precursors is one of the bottlenecks in the cost-effective manufacturing of carbon fiber. Half the cost of manufacturing carbon fiber is spent in making the PAN precursor (Bengtsson et al. 2019 ). Another potential limitation of using PAN precursors is the raw materials are fossil-based which entails a high cost. The high price of carbon from the perspective of raw materials and production cost is the driving force of finding cheaper and renewable alternatives.

A potential and interesting substitute precursor for carbon fiber production is lignin. It can be utilized for the production of a high volume of carbon fibers for a multitude of applications. This is possible, because especially the lignin from kraft pulp consists of high carbon content of around 60–65% and the lignin is available in huge quantity. This also makes lignin a promising alternative precursor based on high yield after processing into carbon fiber (Olsson et al. 2017 ; Hubbe et al. 2019 ). The lignin can be used as a potential precursor for carbon fiber production by incorporating appropriate spinning and carbonization processes. The most common way of manufacturing carbon fibers from lignin involves melt spinning to produce precursor fibers, thermo-stabilization (200–350 °C), and carbonization (over 1000 °C under nitrogen atmosphere) to produce carbon fibers (Fig.  9 ). Wet spinning can also be used when rheological problems are encountered in melt spinning. It is reported that greater than 35% of manufacturing cost is reduced using renewable lignin as a precursor in carbon fiber production (Bengtsson et al. 2018 ; Gbenebor and Adeosun 2019 ). The challenges in regards to lignin to carbon fiber conversion are the availability of fiber spinning technologies (Souto et al. 2018 ) in some countries which limit the product diversification scheme.

figure 9

Spinning of lignin into carbon fiber (Gbenebor and Adeosun 2019 )

Bioplastics from black liquor hemicellulose

The hemicellulose from black liquor consists of xylan among other ingredients (Yang et al. 2019a ; Liu et al. 2012 ). The polysaccharide-based xylans are made up of β-1,4-linked xylose residues. They consist of α-arabinofuranose and α-glucuronic acids pendant branches that contribute to cross-linking of cellulose microfibrils and lignin through ferulic acid residues.

Xylan can be extracted from several locations in the pulp mill. During kraft pulping, xylan is partly dissolved in the cooking liquor but part of it will be redeposited onto the fibers in the later parts of the cook. The dissolved xylan can be isolated from black liquor for its utilization in the production of different biomaterials. Among the different methods used for xylan extraction, those utilizing alkali are most commonly and widely used.

Xylan is constituted by the black liquor along with fractions lignin fractions. The extraction of xylan from black liquor requires two-step precipitation. First, black liquor acidification is conducted and this is followed by precipitation by ethanol which ultimately provides the fractions of xylan (Stoklosa 2014 ). The xylan hemicellulose separation is done using potassium hydroxide (KOH) for hardwood and sodium hydroxide for softwood in aqueous media. The mechanism of separation of the hemicellulose is achieved through hydrolysis which involves the breakage of ester linkages between xylan and other alkaline black liquor components.

Xylan can be biorefined into lactic acid (Fig.  10 ). First, xylan is converted to low molecular weight sugars by hydrolysis using enzymes or chemically using acid hydrolysis. Then the resulting low molecular weight sugars can be converted to lactic acid by fermentation or alkali oxidation. Biomass-derived lactic acid is an important renewable chemical building block for synthesizing bioplastics (Fernández-Rodríguez et al. 2019 ; Chen 2012 ). Polylactic acid (polylactide) used as a precursor for plastics can be obtained by polymerization of a lactic acid refinery of xylan.

figure 10

Xylan to PLA route

Polylactic acid (polylactide) [PLA] is biodegradable as well as recyclable polyester made from renewable feedstock. PLA is synthesized by the condensation polymerization of lactic acid or ring-opening polymerization of the corresponding lactide. As one of the highly biodegradable and crystalline polymers the lactic acid polymer (PLA) has a high melting point and outstanding mechanical characteristics (Gordobil et al. 2015 ; Singhvi et al. 2019 ). It can be used for bioplastic manufacturing used for different engineering applications. Biomaterials of versatile need can be obtained from PLA using advanced manufacturing techniques such as electrospinning, especially for medical products. The major challenges in conversion and utilization of xylan are of two ways. One is the difficulty in obtaining fully purified xylan with the grade required for polymer production and the other is the lower melting pint of the PLA produced which limits its application for high-performance materials. Different researches are ongoing especially in maximizing extraction effectiveness of xylan and usage of modified polymerization and spinning technologies for manufacturing higher grade PLA products.

Beneficiation of cellulose for high value-added materials

Production of cellulose nanocrystals [cnc] from cellulosic residues.

Nanocellulose is a unique and promising natural compound derived from ordinary biomass. It is currently the most environmentally friendly compound that is techno-feasible and cost-effective, and also reduces effluent production (Clemons 2016 ). Nanocellulose has retained significant attention due to its tremendous functionality, i.e., greater surface chemistry, extraordinary biotic possessions, low toxicity, low cost, lower density, and significant mechanical properties. Cellulose Nanocrystals have many important physical properties Nanocrystalline cellulose has high heat stability which makes it suitable as a potential engineering material for aggressive temperature environments and its morphology with regards to small size and shape can be managed for different applications in solutions (Feng et al. 2015 ; Aguayo et al. 2018 ). The cellulose from the different waste sources in pulp and paper mills can be converted into cellulose nanocrystals (CNC) for wider application as a biomaterial in diversified fields of application (Fig.  11 ).

figure 11

Multitude application of CNC biomaterial

CNC is needle-shaped and highly crystalline material produced from cellulose pulp (Clemons 2016 ). The outlooked application of CNC is very wide and mostly its use in medical and industrial fields is tremendous. CNC can be used for the fabrication of medical products such as artificial skin, breast implants, versatile hygiene products, tissue-engineered materials, wound dressings, and drug delivery biomaterials. Industrially CNC can be used for the automotive interior, cosmetics industry, acoustics/photonics, build-tech, and different packaging materials.

Cellulose fiber is a key and characteristic component in pulp and paper mill sludge and is also constituted by sawdust and other woody residues (Aguayo et al. 2018 ). Cellulose is an important biopolymer that consists of semicrystalline regions which are responsible for the outstanding mechanical properties of the polymer. Cellulose as macromolecule is composed of many cellobiose repeat units which themselves are made up of glucose monomeric units (β-glucose) via β-1,4-glycosidic linkages. The individual extended cellulose chains are parallel to each other and the inherent stability and crystallization of cellulose polymers are due to the presence of extensive intramolecular and intermolecular hydrogen bonds.

In pulp and paper mills different conventional processes are used to recover cellulose from wastewater. The process of separation of cellulose from dried sludge is done using ionic liquid-based segregation techniques which involve cellulose precipitation from the sludge (Gibril et al. 2018 ). Direct extraction and utilization of cellulose from sawdust and woody matters are also possible.

The production of CNC from cellulose is an emerging possibility for the diversified utilization of trees for biomaterials (Fig.  12 ). A biorefinery approach can be used to convert cellulose from pulp and paper mill waste into nanocrystalline cellulose (Souza et al. 2017 ). The production of nanocellulose is attained by a two-step process (Clemons 2016 ). In the first step, the pretreatment process of native cellulose biomass is done which yields treated cellulose fibers. While in the second step, pretreated cellulose fibers are converted into nanocellulose using various routes, e.g., high-pressure homogenization, micro fluidization, micro grinding, high-intensity ultra-sonication, electrospinning, and steam explosion.

figure 12

Extracting CNC from trees

Method of synthesis of CNC generally adopts breakdown of cellulose chains to the desired nanoconfiguration via different techniques. The chemical and biological techniques utilize different chemicals and enzymes, while the physical technique involves the mechanical breakdown of the cellulose chains. The chemical process mainly involves hydrolysis using acids and alkalis or a series of reagents by the partial breaking of glucosidic bonds for obtaining the CNC. The four steps in the synthesis of CNC via mechanical method are high-pressure homogenization, fluidization to micro-level, grinding to fine particles, and finally smashing under freezing conditions. Conventionally combined methods are utilized for optimized processes and characteristics of the cellulose nanocrystal (Song et al. 2019 ). The biological and combined methods of the CNC synthesis method employed for hydrolysis minimize concerns with regards to environmental pollution. The production technique of CNC is well-practiced; ensuring high-grade purity of the cellulose with well-advanced extraction technology could eliminate the associated challenges in terms of high value-added products especially those used for medical items.

Synthesis of textile fibers from dissolving pulp

Dissolving pulp has versatile applications. Dissolving pulp can be used as a source of pulp for the paper mill (Kihlman 2012 ). This is particularly important as economic support for developing countries that are entirely based on imported pulp. Besides many chemicals used in washing and value additions in wet and chemical processing industries such as detergents, softeners, and binders can be produced using dissolving pulp as a precursor. These chemicals are cellulose ether-based and can be extracted from the dissolving pulp.

Dissolving pulp besides its utilization as raw material for the paper mill and surfactant synthesis it can be used for the manufacturing of textile fibers (Ma et al. 2011 ). The dissolving pulp can be prepared from cellulosic wastes using the same pulping route described in the current review and can be utilized for the making of viscose rayon and cellulose acetate fibers (Woodings 2001 ). Once the required grade of dissolving pulp is availed viscose rayon can be manufactured using wet spinning technology and cellulose acetate is manufactured using dry spinning technology. The manufactured viscose rayon and acetate fibers have diversified applications (Fig.  13 ).

figure 13

Dissolving pulp beneficiation: regenerated fibers

The use of dissolving pulp as a precursor for the manufacture of commodity textile fibers has an economic impact on developing countries that entirely depend on using a single fiber such as cotton for the production of textile materials. In the region of concern, where the supporting data for availability study is conducted it has been described that the paper mill entirely depends on the imported pulp and it is not possible to produce and market the important textile fibers. It is vital to consider the economic advantage of producing potential fibers from indigenous pulp and paper wastes. Modern manufacturing techniques such as dry jet wet spinning and electrospinning techniques can be utilized for the manufacturing of different grades of fibers, especially for high-performance applications. The major challenge in the utilization of pulping waste as a precursor for textile fibers is the limited availability of fiber manufacturing units in areas, where resources are abundant; and associated yield-related problems for producing textile fibers as per the global demand.

Biocomposites from pulp and paper mill waste

The global concerns for a safe environment and risk minimized livelihood of society are high. With this regard issues that need immediate intervention are the highest priorities of global nations. As far as feasible interventions are concerned focus needs to be given on increasing cost of petroleum and the allied depletion and frameworks in line with new environmental regulations. To this end engineering materials which have a vital impact in replacing existing petroleum-based materials and which are capable of addressing the environmental legislations are required. This was the rationale behind seeking eco-friendly green substitutes especially biocomposites for modern engineering applications (Soucy et al. 2014 ; Manesh 2012 ).

Renewable lignocellulosic materials are suitable for the reinforcement of polymers and provide biocomposites for the relevant industry. Such kinds of production trends provide relief with regards to problems encountered in using petroleum-based composites. These frequently available resources provide a remedial solution with regards to the production of attractive, sustainable, cost-effective, and eco-friendly materials so-called biocomposites with a safe environment as a result of preferred disposal and reuse options (Schorr et al. 2014 ).

The fly ash and other mineral-based wastes from pulp and paper mill are underutilized and fully discarded especially in developing countries (Novais et al. 2018 ). The fly ash is entirely composed of metal oxide minerals. Though it is not a concern of the present review the grits, dregs, and lime muds have also plenty of mineral content for specific biomaterial applications. The biomaterial which can be obtained by a suitable biorefinery technique from fly ash can be used for versatile engineering applications as a biocomposite. The prospective application of fly ash as a biomaterial is by converting the minerals into their polymer counterpart via geo-polymerization which normally are referred to as geopolymers (Mohammadkazemi 2018 ; Yoon-moon and Naik 2005 ).

Depending on the end-use the geopolymers can be incorporated in manufacturing composite materials mainly as the reinforcing component of the biocomposite. A polymer of fly ash that can be used for biocomposite is synthesized using predefined steps. The major step involves treatment with highly alkaline liquors such as using aqueous caustic soda in combination with silicate compounds such as sodium silicate in a process called alkali activation (Saeli et al. 2019 ; Rajamma et al. 2012 ). The highly alkaline environment will lead to the breaking of silica and alumina bonds in the fly ash which provides conditions for the dissolution of free silicon and aluminum ions. The reaction between the free silicon and aluminum ions with active alkali ions leads to the formation of an intermediate precursor which up on precipitation reorganize into the polymeric three-dimensional aluminosilicate structures.

Besides fly ash, sawdust from the pulp and paper mill waste is another potential source for the manufacturing of biocomposite (Zhang et al. 2020 ). Sawdust which mainly constitutes cellulose can be used in blending for synergistic enhancement of the reinforcement of the composite structures. The inherent biodegradability made it a preferred raw material in biocomposite applications (Zhang et al. 2020 ; Jiang et al. 2009 ).

Through advanced composite engineering and characterization, different biocomposites can be manufactured from sawdust and fly ash and modeled for a multitude of applications. The diverse applications of biocomposite from fly ash and saw dust-based biomaterials are summarized (Fig.  14 ). Both sawdust and fly ash-based biomaterial provide high heat resistant biocomposite suitable for high-performance applications. The biocomposite from sawdust cellulose can be used in the manufacturing of automotive interior, different boards, furniture, packaging, and so on, whereas fly ash based biocomposite can be used in the production of civil engineering materials mainly in construction technology (Zhang et al. 2020 ; Akampumuza et al. 2017 ; El‐Meligy et al. 2004 ). In both fly ash and sawdust systematic collection of sample raw material for biorefinery needs attention as they mostly are lightweight and interfere with a feasible collection. Improper management of sample collection could result in disturbance of the working environment and personal safety through inhalation needing high priority of conditioning at work stations.

figure 14

Possible applications of biocomposites from pulp and paper mill waste

Conclusions

Pulp and paper mills release a large amount of waste globally. Most of these wastes are directly disposed to landfills with minimal incineration and nil recycling. Though there are trials for the reuse of these wastes in some of the developed world the trend is almost none in developing countries. The present review has shown that the pulp and paper mill biomass; besides their conventional use, can be converted into biomaterials that have high value for versatile applications. It is revealed that the biomass generated from the mills provides ingredients for the synthesis of biomaterials such as lignin, hemicellulose, cellulose, and various minerals. The paramount importance of biomass ingredients is that they can be converted into high value-added biomaterials using an appropriate biorefinery system. With this regard, a possibility is observed that potentially important engineering materials such as carbon fiber, bioplastic, and fibers, CNC, and biocomposites can be manufactured from waste biomass for diversified engineering applications. The synthesized biomaterials through appropriate and feasible technologies will be useful for the manufacturing of versatile bio-based products that are used in widespread conventional, high-performance, and smart applications. Future study will entail extensive research and development work to develop appropriate technologies for their full utilization and commercialization as a source of some of the proposed applications mentioned in this review. In so doing dual the impact of the newly investigated materials is realized both from the economic point of view through product diversification and environment aspects in protection and hazard minimization.

Availability of data and materials

All data and materials are availed in the manuscript and no additional input is required.

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The authors would like to acknowledge the Higher Education and TVET program Ethiopia-Phase 3, PE479-Higher Education, KFW project No. 51235, and BMZ No. 201166305 for the financial support of this research.

The prerequisite funding support is from the Higher Education and TVET program Ethiopia, KFW Project, and Ethiopian Institute of Textile and Fashion Technology, Bahir Dar University. No other funding.

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Haile, A., Gelebo, G.G., Tesfaye, T. et al. Pulp and paper mill wastes: utilizations and prospects for high value-added biomaterials. Bioresour. Bioprocess. 8 , 35 (2021). https://doi.org/10.1186/s40643-021-00385-3

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Received : 28 January 2021

Accepted : 19 April 2021

Published : 29 April 2021

DOI : https://doi.org/10.1186/s40643-021-00385-3

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Non-wood fibers as raw material for pulp and paper industry

Pulp and paper industry in the world have been growing fast. As a result, there has been a massive request for pulp and paper raw materials. The raw materials used in papermaking can be classified into three groups: wood, non-wood, and recycled wastepaper. The Non-wood raw material is an important fiber resource in the regions where forest resources are limited. The current usage of non-wood plant fibers, as rice straws, corn stalks, cotton stalks, and bagasse would play a chief role in increasing papermaking raw materials. Using of non-wood plant fibers in the paper industry associated with some problems, including collection, transportation, storage and handling, washing, bleaching, papermaking, chemical recovery, supply of raw material and the properties of finished paper. Recently, a high-tech innovation in all the fields of papermaking has made non-wood more reasonable with wood as a raw material for papermaking. Although till now, use of non-wood fibers for pulp and paper manufacture was focused in countries with limited wood supply, it is now showing a growing effort even in countries with acceptable wood source due to environmental concerns. Consequently, the future of non-wood plant fibers as pulping and papermaking raw material looks bright.

Funding statement: The authors would like to express their gratitude to the National Research Centre, Egypt, for the financial support of the current work.

Conflict of interest: The authors declare no conflicts of interest regarding the submission.

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A deep learning-based approach for performance assessment and prediction: A case study of pulp and paper industries

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  • Sunil Kumar Jauhar 1 ,
  • Praveen Vijaya Raj Pushpa Raj 2 ,
  • Sachin Kamble   ORCID: orcid.org/0000-0003-4922-8172 3 ,
  • Saurabh Pratap 4 ,
  • Shivam Gupta 5 &
  • Amine Belhadi 6  

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The pulp and paper industry is critical to global industrial and economic development. Recently, India's pulp and paper industries have been facing severe competitive challenges. The challenges have impaired the environmental performance and resulted in the closure of several operations. Assessment and prediction of the performance of the Indian pulp and paper industry using various parameters is a critical task for researchers. This study proposes a framework for performance assessment and prediction based on Data Envelopment Analysis (DEA), Artificial Neural Networks, and Deep Learning (DL) to assist industry administration and decision-making. We presented a case study based on eight industries to demonstrate the methodology's applicability. This study analyses and predicts industry performance based on sample data observations over 30 years. The result suggests the DEA-DL-based efficiency prediction has an overall MSE of 0.08 compared with the actual efficiency. Furthermore, the efficiency rankings are compared between the three techniques. The results suggest that the integrated DEA-DL method is primarily accurate in most scenarios with the actual values. The findings of this study provide a comprehensive analysis of environmental performance for policymakers.

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Jauhar, S.K., Raj, P.V.R.P., Kamble, S. et al. A deep learning-based approach for performance assessment and prediction: A case study of pulp and paper industries. Ann Oper Res 332 , 405–431 (2024). https://doi.org/10.1007/s10479-022-04528-3

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Yingju Miao , Siyu Xiang , Yingfen Wei , Xiaohui Long , Jie Qiu , Yingchun Miao; Physical Properties of Pulp and Paper: A Comparison of Forming Procedures. Forest Products Journal 1 March 2023; 73 (2): 175–185. doi: https://doi.org/10.13073/FPJ-D-23-00007

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In this work, we used the conventional wet papermaking process and the solution casting procedure to make paper sheets and optimized the relative content of eucalyptus and Simao pine pulps using the mechanical properties of the paper sheet as the evaluation index. The chemical composition, water retention value, zeta potential, carboxyl content, and drainage behavior of the pulp created using the optimal mass ratio for each method were measured, and the resulting paper sheets were characterized via Fourier-transform infrared spectroscopy, X-ray diffraction, scanning electron microscopy, and nitrogen adsorption/desorption isotherms. We found that for a ratio of eucalyptus to Simao pine pulps of 94:6 using the wet papermaking process, the mechanical properties of sheets took their optimal values, and the tear, tensile, and burst indexes and the folding endurance were equal to 4.43 mN·m 2 ·g −1 , 27.47 N·m·g −1 , 1.13 kPa·m 2 ·g −1 , and 11.38 times, respectively, whereas the ratio leading to the best possible mechanical performance in the solution casting process was 88:12, and the corresponding paper sheets had tear, tensile, and burst indexes and the folding endurance of 11.73 mN·m 2 ·g −1 , 23.03 N·m·g −1 , 0.68 kPa·m 2 ·g −1 , and 25.50 times, respectively. The cellulose, hemicellulose, and lignin contents of the pulp treated by the solution casting method were lower by 1.88, 3.11, and 2.67 percent, respectively, compared to that obtained via the wet papermaking process. However, the water retention value, zeta potential, and carboxyl content of the pulp obtained via solution casting were higher by 50.31, 123.41, and 50.15, percent, respectively, compared to that obtained via the wet papermaking process. The drainage time obtained via the solution casting method was one-fifth of that obtained via the wet forming process. The paper sheet prepared via the solution casting method was found to exhibit weaker hydrogen bonding, a decreased level of crystallinity (26.64% lower), and an increased compactness and N 2 gas adsorption capacity (19.55% and 66.7% higher, respectively) compared to the sheet obtained via the wet papermaking process. This work shows that the physical properties of the paper prepared via the two processes considered here, using their respective optimal weight ratios of the different types of pulp, have their own advantages.

In order to improve the mechanical properties of paper sheets, the pulp fibers that are to be manufactured into paper are pretreated using physical and/or chemical methods. Beating (or refining) is one of the most common physical means of fiber pretreatment. Via beating or refining, the fiber can be split to improve the swelling capacity of the pulp fibers and enhance the fiber–fiber bonding properties, which improves the mechanical properties of the paper ( Garcia et al. 2002 , Seo et al. 2002 , Nazhad 2004 ). Biological methods also effectively alter the properties of pulp fibers, including drainage characteristics, softness, fiber strength, and the degree of hornification, through enhancing the fiber–fiber bonding properties ( Bhardwaj et al. 1996 , Pastor et al. 2001 , Wolfaardt 2003, Zhang et al. 2008 , Bajpai 2010 ). Chemical treatment methods, especially those utilizing NaOH aqueous solutions, are another more effective and rapid way to change the fiber bonding properties and fiber strength through rapidly inducing significant lateral swelling of the fiber (Jie Cai et al. 2015). Freeland and Hrutfiord (1994) treated different recycled fibers with a NaOH solution; the short span compression index of the old corrugated containers, the linerboard, and the medium that were created from fibers subject to this treatment were found to increase by 10.6, 20.4, and 11.3 percent, respectively. Gurnagul (1995) also used a NaOH aqueous solution to treat a thermomechanical pulp as well as bleached and unbleached unbeaten low-yield kraft pulps; the increase in the swelling of the thermomechanical pulp fibers was found to be mirrored by the increase in the handsheet strength, but no correlation was found between the level of fiber swelling and handsheet strength in the case of the kraft pulps. Zanuttini et al. (2009) employed alkaline treatments on unbleached recycled softwood kraft pulp; it was found in this work that the alkaline treatment reduced the freeness of the pulp but improved the papermaking properties: the tensile strength and short column compressive strength were found to be enhanced by more than 50 and 5 percent, respectively, by this treatment.

Jie Cai (2005) reported that a NaOH/urea aqueous solution precooled to −13°C could quickly dissolve cotton linter pulps (α-cellulose content > 95%) with a polymerization degree of less than 700. It has also been reported that dissolved cellulose can be regenerated via hydrogen bond reconstruction in many systems, including water, inorganic salt solution, and organic solution systems ( Zhang et al. 2005 ). In previous work ( Miao et al. 2018 ), unbleached eucalyptus hardwood kraft pulp was treated in a NaOH/urea aqueous solution that was precooled to −13°C and reconstructed via hydrogen bonding in a 5 wt% H 2 SO 4 /5 wt% Na 2 SO 4 solution; it was found not only that an amount of cellulose film filled among the fiber network but also that each fiber could plump completely; thereby, the water retention capacity of the pulp and the mechanical properties of the resultant paper were significantly improved. However, in the process whereby the pulp was disintegrated into individual fibers, a large quantity of fine cellulose film was generated, and these films were removed in the white water used in the conventional papermaking process, resulting in a large amount of fiber losses and an increased cost of wastewater treatment. It can thus be concluded that fibers treated with a NaOH/urea aqueous solution precooled to −13°C are not suitable for use in the conventional papermaking procedure, but the solution casting method should be selected to form sheets via the self-assembly of fibers in the cellulose solution alongside solvent evaporation, which induces a phase separation for hydrogen bond reconstruction and sheet curing and avoids the fiber losses and whitewater treatment problems. In another study, the optimal process (fixing the ratio of NaOH to urea, solution precooled temperature, and regeneration system) involving a NaOH/urea aqueous solution was investigated; this process did not produce cellulose films but instead significantly swelled the fibers ( Miao et al. 2019 ). The pulp fibers used in both the above works ( Miao et al. 2018 , 2019 ) were unbleached eucalyptus kraft pulp fiber. Pulp fibers come from different plants, and their morphological properties and chemical composition can vary significantly; the mechanical properties of the resulting paper produced from these pulp fibers can also vary significantly ( Wangaard and Williams 1970 , Wangaard and Woodson 1972 , Kiaei and Samariha 2011 ). How the length and strength of fibers obtained from different plants influence the properties of pulp handsheets has been discussed by many authors. Numerous inconsistencies in experimental findings have also been reported.

Morais et al. (2019) reported that the eucalyptus pulp with high coarseness and deformations, low fines content, and low pentosan content is more suitable for making high-softness tissue paper. Wangaard and Woodson (1973) reported that for a given sheet density, both fiber strength and fiber length have a positive correlation with both the breaking length and the burst properties of the sheet, and that, as the sheet density increases, increasing fiber length leads to an increase in these properties until the maximum tear factor values are obtained at sheet densities at or beyond 0.50 g/cm 3 . However, Mittal et al. (1978) reported that properties such as tensile and burst strengths are largely independent of the fiber length and that the folding endurance of the sheet is only slightly affected by the length of the fiber; this work found that fiber length has a significant impact on paper tear strength. Eucalyptus kraft pulp is characterized as a rigid and short broadleaf hardwood ( Morais et al. 2019 ), and Simao pine fiber is a softwood fiber; softwood fibers are typically longer and more flexible than hardwood fibers (Jicheng Pei and Li 2012). In the present work, the effect of the dosage of eucalyptus and Simao pine pulps treated with different processes on the properties of the pulp and resultant paper sheet is investigated. The chemical composition, water retention value, zeta potential, carboxyl content, and drainage behavior of the pulps were measured, and the resulting paper sheets were characterized via Fourier-transform infrared spectroscopy (FT-IR), X-ray diffraction (XRD), scanning electron microscopy (SEM), and nitrogen adsorption/desorption isotherms.

Unbleached eucalyptus kraft dry pulp (UEKP) sheets (commercially available) and unbleached Simao pine kraft dry pulp (USKP) sheets (commercially available) were provided by Yunnan Yunjing Forestry and Pulp Mill Co., Ltd (Jinggu, China). The water retention values (WRVs) of UEKP and USKP were determined according to the Chinese standard GB 29286-2012 and were found to be 92.16 ± 1.08 percent and 97.58 ± 1.42 percent, respectively. Sodium hydroxide, urea, and ammonium sulfate were purchased from Shanghai Aladdin Biochemical Technology Co. Ltd (Shanghai, China). All chemical reagents used were analytical grade and used as received. Deionized water was used to prepare all the solutions throughout the experiment; for other processes requiring water, tap water was used.

Pulp treating and handsheet forming.—

First, UEKP and USKP sheets were torn into approximately 0.3 by 1-cm 2 pieces and mixed to achieve uniform distributions composed of different mass ratios. In accordance with our previous works ( Miao et al. 2018 , 2019 ), the above mixed pulp fibers were treated with different NaOH/urea aqueous solutions; the resultant pulps were then processed using different procedures to form sheets. Each sheet had a basis weight of 60 g/m 2 , and six sheets were prepared for each weight ratio considered here. The pulp treatments and sheet forming procedures used here are as follows.

Wet papermaking process ( Miao et al. 2019 ).—

Approximately 10 g of the above-mentioned mixed fiber was soaked in 100 g of 1.0-wt% NaOH/8.0-wt% urea aqueous solution and stored for 24 hours at 0°C in a refrigerator; the mixture was then mechanically stirred at 2,500 rpm for 5 minutes at room temperature; 200 mL of 7.0-wt% (NH 4 ) 2 SO 4 was then added while the mixture was stirred for a further 30 minutes. The resulting pulp slurry was then drained, washed, and filtered with tap water through a Buchner funnel sealed using a 200-mesh filter cloth at a vacuum level of 0.08 MPa until the pH of the pulp was neutral. A proportion of the as-prepared pulp was then used to test the physical properties of the pulp, and the remaining pulp was used to make handsheets according to Chinese standard GB/T24324-2009 on a standard apparatus (G 8E; Gockel & Co. GmbH, Munich, Germany). The wet handsheets were placed for 5 minutes on the drying plate of the standard apparatus at 95°C.

Solution casting method ( Miao et al. 2018 ).—

At room temperature, maintaining a solid–liquid weight ratio of 1:50, the mixed fibers described above were immersed in a 7.0-wt% NaOH/12.0-wt% urea aqueous solution that was precooled to −13°C and mechanically stirred at 2,500 rpm for 5 minutes. The resulting mixed pulp slurry was then divided into two parts. Part of the slurry was added to 200 mL of 7-wt% (NH 4 ) 2 SO 4 aqueous solution (with a ratio of dry fibers to solution of 2 g:200 mL) and was continuously stirred at 2,500 rpm for 5 minutes; this mixture was then drained and washed until the pH of the pulp was neutral. The pulp properties were measured from this sample. The remaining part of the mixed pulp slurry was poured into a square acrylic mold with a side length of 200 mm; it was then shaken, defoamed, and placed into a preheated electro-thermostatic blast oven for 4 hours at 60°C to solidify the sample and form a sheet. The formed sheets were soaked in 200 mL of the 7-wt% (NH 4 ) 2 SO 4 aqueous solution for 5 minutes and then washed with tap water until the pH of the sheets was neutral; they were then placed for 5 minutes on the heated plate of the standard apparatus at 95°C for drying.

Determination of the mechanical properties of the handsheets.—

The mechanical properties of the handsheets (tear, burst, and tensile indexes and folding endurance) were measured according to standards GB/T 455-2002, GB/T 454-2020, GB/T 12914-2018, and GB/T 457-2018, respectively. The tests were repeated six times for each sample; the standard deviation was calculated and is shown as the error bars in the plots from Figures 1 to 3 .

Mechanical properties of the paper sheets prepared via the wet papermaking process.

Mechanical properties of the paper sheets prepared via the wet papermaking process.

Mechanical properties of paper sheets prepared via the solution casting process.

Mechanical properties of paper sheets prepared via the solution casting process.

Comparison of the mechanical properties of the paper sheets prepared via the wet paper papermaking and solution casting processes.

Comparison of the mechanical properties of the paper sheets prepared via the wet paper papermaking and solution casting processes.

Evaluation of the properties of the pulp.—

The cellulose, hemicellulose, and lignin content of the as-prepared pulps were determined according to laboratory analytical procedures reported by the National Renewable Energy Laboratory ( Sluiter et al. 2010 ).

formula

The drainage behavior of the above as-prepared pulps was determined using a dynamic drainage jar (Mütek DFR-05; BTG, Säffle, Sweden); 1,000 mL of pulp suspension with 0.2 percent of content of dry fiber was poured into the dynamic drainage jar and stirred for 30 seconds at 750 rpm at 25°C; water filtration was then started, and the time required for 800 g of filtrate to be collected was determined.

The zeta potential values of the as-prepared pulps with a 0.2 percent content of dry fiber were measured in the sample cell of the Mütek SZP-10 System Zeta Potential (BTG) at a temperature of 25°C.

The carboxylate content of the as-prepared pulps was determined via the conduct metric titration method ( Chen et al. 2013 ).

All measurements were conducted on three samples (in addition to the drainage behavior); the standard deviations of the measurements were calculated and are shown in the tables.

Characterization of the handsheets.—

The functional group structure of the handsheets was recorded using an FT-IR spectrometer (Bruker Equinox 55; Bruker Spectroscopy Corp., Ettlingen, Germany). The sheet sample was clamped and placed in the spectrometer. The IR spectra were recorded in the range from 4,000 to 400 cm −1 with a resolution of 4 cm −1 over 32 scans. The obtained data were corrected to account for the presence of H 2 O and CO 2 in the atmosphere using the software supplied with the spectrometer.

The crystalline structure of the handsheets was determined using an X-ray diffractometer (X'Pert 3; Panalytical Co. Ltd, Almelo, Netherlands) in the range of 2θ = 5° to 80° using a scanning speed of 13.77 s/step, a step size of 0.01313°, and an operating voltage and current of 40 kV and 40 mA, respectively. The sample tablets for the XRD measurements were prepared by taping the sheet to the mold.

The cross section and surface morphology of the handsheets was observed using cold field emission SEM(SU8010; Hitachi High-Technologies Corp., Tokyo, Japan) operating at 1 kV.

Specific surface area and pore volume measurements of the handsheets were conducted at 77 K using a surface area and pore size analyzer (TriStar II 3flex; Micromeritics Instruments Corp., Norcross, GA, USA). Prior to all measurements, all the samples were degassed for 12 hours at 110°C under vacuum conditions.

Paper strength

Figures 1 and 2 show the effect of the mass ratio of the eucalyptus and Simao pine pulps on the mechanical properties of the paper sheets prepared via the wet paper forming and solution film casting processes. As can be seen from the figures, for a given ratio of eucalyptus and Simao pine, the mechanical properties of paper sheets observed differ due to the different processes used in their construction.

As shown in Figure 1 , with increasing amounts of Simao pine pulp fiber in the mixture, the mechanical properties of the paper are generally improved. Since Simao pine fibers are longer and more ductile, whereas eucalyptus fibers are shorter and harder, when the amount of Simao pine fiber exceeds 6 wt%, increasing quantities of Simao pine fiber leads to the mechanical properties of the paper sheets first decreasing before increasing, with the exception of the tensile strength, which was seen to increase slightly and then decrease. From the perspective of the paper strength, the optimal mass ratio of eucalyptus pulp to Simao pine pulp for use in this procedure is concluded to be between 94:6 and 85:15.

Figure 2 shows the effect of the amount of Simao pine pulp added to the eucalyptus pulp on the mechanical properties of paper sheets prepared via the solution film casting method. The mechanical properties of the paper prepared via this method are significantly different from those prepared via the wet papermaking process, which shows that the paper forming process has a notable influence on the mechanical properties of the resulting paper. As can be seen from the figure, with the increase in the content of Simao pine, the paper strength initially increases before decreasing. For a Simao pine fiber content of 12 wt%, the tensile and tear strength reached their maximum values of 23.03 N·m·g −1 and 11.73 mN·m 2 ·g −1 ; the maximum burst strength and folding endurance were 0.68 kPa·m 2 ·g −1 and 25.50 times for a Simao pine content of 15 and 18 wt%, respectively. The mass ratio of eucalyptus pulp and Simao pine pulp is in the range 88:12 to 85:15 mirrored to the paper strength relatively high, so from the perspective of paper strength, the most suitable mass ratio of eucalyptus pulp and Simao pine pulp for use in this procedure is between 88:12 and 85:15.

In order to better understand the influence of the two procedures on the paper strength, we selected tensile strength as the primary evaluation index and the other mechanical properties as auxiliary evaluation indexes to establish the most suitable process parameters. When the mass ratios of eucalyptus and Simao pine pulps is 94:6 for the wet paper papermaking and 88:12 for the solution casting methods, the tensile index of the resulting paper sheets is relatively high and the tear, burst, and folding endurance still increasing. Therefore, we selected the pulp and its resulting paper sheets treated with these two ratios for further analysis and characterization. The following sections, unless otherwise mentioned, refer to the paper or pulp obtained using these two ratios.

Figure 3 provides a comparison of the mechanical properties of paper sheets prepared with two previously mentioned optimal parameters. It can be seen that the paper prepared via the wet papermaking process has superior tensile and burst strengths, but the tear strength and folding endurance are superior for the paper fabricated via the solution casting method. This finding can be attributed to the fact that more flexible and longer fibers lead to a higher folding endurance and tear strength in paper sheets ( Mittal et al. 1978 ).

In order to better understand the difference in mechanical properties of the paper fabricated via the two processes investigated here, we evaluated the microphysical properties of the paper sheets for ratios of eucalyptus to Simao pine pulps of 94:6 in the wet papermaking method and 88:12 in the solution casting method.

Pulp properties

Table 1 shows the cellulose, hemicellulose, and lignin compositions of the pulps with the selected mass ratios obtained via the previously described processes. The cellulose, hemicellulose, and lignin contents of the pulp fiber obtained via the solution casting method are slightly lower than in the pulp obtained via the wet papermaking process (the pulp obtained via the solution cast method showed cellulose, hemicellulose, and lignin contents that were lower by 1.88, 3.11, and 2.67 percent, respectively, compared to the values obtained via the wet papermaking process). This may be due to the fact that the pulp washing procedure used in the wet papermaking process requires direct contact between the single fiber and deionized water while the mixture is subject to stirring, whereas the solution casting method relies on a concentration difference to induce molecular diffusion from the inside to the outside of the paper sheet. In order to fully remove the sodium hydroxide and urea from within the sheet, considerably more washing would be required than the amount used in the wet papermaking process considered here, which would result in a further decrease in the cellulose, hemicellulose, and lignin contents.

Composition of the pulp samples treated according to the wet papermaking process and the solution casting method.

Composition of the pulp samples treated according to the wet papermaking process and the solution casting method.

Table 2 shows the WRVs, zeta potentials, and carboxyl group contents of the pulps with optimized mass ratios treated using the aforementioned processes. The WRV of a given pulp is known to have a positive correlation with the mechanical properties of the resulting paper sheet; that is, the mechanical properties of the paper sheets obtained from pulps with high WRV values are better. The WRVs of the solution casting pulp were found to be 56.02 percent higher than that of the wet papermaking process pulp, indicating that the solution casting process leads to considerably higher water retention of the pulp. The WRV of the pulp treated by the solution casting process is higher than those of the pulps treated using the wet papermaking process, and the corresponding mechanical properties of the paper were also found to be superior (as shown in Fig. 3 ). The zeta potential test is a measure of the electric charge at the surface of the fibers, which is an indirect assessment of the physical stability of the paper in water. The negative charge of the pulp obtained via the solution casting process is more than twice that of the pulp obtained via the wet papermaking process, indicating that the solution casting process dissociates more functional group fibers carrying ionizable negative charges to the fiber surface and improves the stability of the fiber in water. The negative charge on the fiber surface comes primarily from the carboxyl group, and the carboxyl group in the plant fiber exists mainly in hemicellulose. It can be seen from Table 2 that the carboxyl group content of the pulp obtained via the solution casting process is 50.15 percent higher than that of the pulp obtained in the wet papermaking process. It is thus hypothesized that the solution casting process detaches a larger quantity of hemicellulose from the plant cell wall, thereby increasing the carboxyl group content of the fiber surface. This hypothesis is supported by the results of the zeta potential tests performed on the fibers. These results indicate that the increase in carboxyl content enhances the swelling and/or bonding capacity of the cellulosic fibers and improves the bonding of the pulp fibers in paper; thus, the increased carboxyl content increases the strength of the resultant paper, which is consistent with previous reports in the literature ( Zhang et al. 2007 , Chen et al. 2010 ).

Water retention values (WRVs), zeta potentials, and carboxyl contents of the pulp samples with the optimal mass ratios of eucalyptus and Simao pine pulps obtained via the wet papermaking and solution casting procedures.

Water retention values (WRVs), zeta potentials, and carboxyl contents of the pulp samples with the optimal mass ratios of eucalyptus and Simao pine pulps obtained via the wet papermaking and solution casting procedures.

Figure 4 shows the drainage performance of the pulps with the optimal mass ratio of eucalyptus and Simao pulps obtained via the aforementioned processes. Under the same filtration conditions, 800 mL of suspension with a solid content of 0.2 percent (dry fiber) was found to require 335 seconds for the wet papermaking process pulp but only 66 seconds for the solution casting film process pulp; furthermore, the maximum drainage rate was obtained after 24 seconds in the case of the solution casting film and 44 seconds in the case of the wet papermaking process. This indicates that the solution casting process leads to improved drainage performance of the pulp, which can be attributed to the increased negative charge on the surface of the fibers obtained via this method.

Drainage behavior of the pulps with the optimal mass ratios of eucalyptus and Simao pine pulps.

Drainage behavior of the pulps with the optimal mass ratios of eucalyptus and Simao pine pulps.

Sheet characterization

Ft-ir spectroscopy.—.

Figure 5 shows the infrared absorption spectra of the sheets prepared using the selected mass ratios of the constituent pulps. The absorption bands of the paper sheets prepared using the processes considered here show a large degree of similarity, but there are some notable changes regarding some functional groups. Specifically, it is can be observed that the peaks that were present at 3,341 cm −1 in the case of the sheet made via the wet paper papermaking process, corresponding to the stretching of the –OH group, shifted to a higher wave number (approximately 3,447 cm −1 ) for the sheet made via the solution casting method; this shift indicates that the hydrogen bonds were weaker in the latter method ( GC Pimentel 1960 , Marechal and Chanzy 2000 ), which can be explained by the fact that the cellulose with a degree of polymerization less than 700 in the fiber was dissolved in NaOH/urea aqueous solution (Jie Cai 2005); this dissolved cellulose then coagulated in the (NH 4 ) 2 SO 4 aqueous solution, leading to a lower degree of hydrogen bond reconstruction. This is consistent with reports in the literature that state that the degree of polymerization of cellulose decreases after dissolution and regeneration. Furthermore, peaks observed at 1,720 cm −1 in the sheet obtained via the wet paper papermaking process, which corresponds to the C=O stretching vibration, were seen to be translated to a lower wave number (approximately 1,637 cm −1 ) in the case of the sheet obtained via the solution casting method; this change can be attributed to the carbonyl oxygen in the carboxyl group and to hydroxyl hydrogen in the hydroxyl group within the fiber forming intramolecular hydrogen bonds; the peak is also noted to be stronger in the latter case, which is due to more hemicellulose detaching from the plant cell wall. These results are consistent with the carboxyl contents determined above. Moreover, the peak observed at 1,113 cm −1 in the spectrum corresponding to the sheet obtained via the wet papermaking process, which corresponds to the C–O–C antisymmetric stretching vibration, disappeared as a result of the solution casting process; this indicates that the crystal phase of the cellulose changed from I to II due to the rotary isomerism of the oxymethyl groups ( Zhbankov et al. 2002 , Li et al. 2015 ), indicating that the solution casting process induces a more complete transformation of the cellulose.

Fourier-transform infrared spectroscopy spectra from the paper sheets prepared from the pulps with the optimal mass ratios.

Fourier-transform infrared spectroscopy spectra from the paper sheets prepared from the pulps with the optimal mass ratios.

In addition, we used the PeakFit software to perform Gauss peak fitting for the infrared hydrogen bond region of 3,000 to 3,800 cm −1 ( Oh et al. 2005 , Popescu et al. 2009 ); the fitting curves are shown in Figure 5 , and the fitting results are detailed in Table 3 .

Hydrogen bond energy (E H ), hydrogen bond distance (D), and the Gaussian fitting results for the paper sheets.

Hydrogen bond energy (EH), hydrogen bond distance (D), and the Gaussian fitting results for the paper sheets.

Gaussian fitting curves of the hydrogen bond zones of the Fourier-transform infrared spectroscopy spectra obtained from paper sheets prepared using the pulps containing the optimal ratios of eucalyptus and Simao pine pulps.

formula

Here, △ v = v 0 − v (cm −1 ), v 0 is the monomeric –OH stretching frequency (3,600 cm −1 ), v represents the stretching frequency observed in the infrared spectrum of the sample (cm −1 ), and D is the hydrogen bonding distance (Å).

The calculated energy of the hydrogen bonds and hydrogen bonding distance are given in Table 3 . As can be seen from Table 3 , the hydrogen bonding distances are similar for both the pulps obtained here. Moreover, the intermolecular hydrogen bond distances (∼2.74 Å) of the two samples were less than the intramolecular hydrogen bonds (2.78 to 2.85 Å), and the corresponding intramolecular hydrogen bond energies (∼23.00 to 0.05 kJ·mol −1 ) are smaller than the intermolecular hydrogen bond energy (∼35.70 kJ·mol −1 ) ( Struszczyk 1986 ), indicating that the stability of the cellulose chains depends primarily on intermolecular hydrogen bonds. It can also be seen that the energy of the hydrogen bonds corresponding to peaks 1 to 3 (see Table 3 ) undergoes a small decrease in the case of the solution casting method with respect to the wet forming procedure, but a small increase in bond energy is observed for peak 4. This result is hypothesized to be related to the pulp processing in the solution casting method leading to more cellulose with a polymerization degree of less than 700 being dissolved in the NaOH/urea solution, which leads to a smaller number of hydrogen bonds being created.

XRD analysis.—

The XRD patterns obtained from the paper sheets are dominated by the pattern that corresponds to cellulose, and the diffraction peaks at 2θ ≈ 15.88° and 22.59° in the (110) and (200) planes are characteristic of the cellulose I crystal in the raw materials ( Popescu et al. 2009 , Miao et al. 2018 ). Figure 7 shows the XRD spectra of the paper sheets obtained via both methods. The cellulose crystal structure of the paper sheet prepared via the wet forming process shows a large degree of similarity to that of the raw fiber; however, the patterns characteristic of cellulose crystals of the paper sheet obtained via the solution casting method are significantly shifted from being characteristic of cellulose I to cellulose II ( French and Cintron 2013 , French 2014 , Jin et al. 2016 ), and the corresponding peak can also be seen to have decreased and broadened with respect to that observed in the spectrum of the raw materials. We used the Jade 6.5 software to quantitatively calculate the X-ray crystallinity indexes for both samples, and we also used the empirical equation derived by Nelson and O'Connor (1964) to calculate the infrared crystallization index based on the infrared data.

X-ray diffraction spectra of paper sheets prepared via the two methods considered here.

X-ray diffraction spectra of paper sheets prepared via the two methods considered here.

formula

The results of the calculations of the crystallinity and infrared crystallinity are shown in Table 4 . The crystallization indexes of the sheets obtained via both procedures were found to decrease due to the presence of the dissolved cellulose with a lower degree of hydrogen bond reconstruction; the decline in the infrared crystallization index was not significant, whereas there was a large decrease in the X-ray crystallization index (26%); these results are consistent with previous studies ( Matsuda 1994 ).

Infrared and X-ray crystallinity indexes of paper sheets.

Infrared and X-ray crystallinity indexes of paper sheets.

SEM analysis.—

Figure 8 shows the SEM images of the surface and cross section of the paper sheets. All the paper sheets formed using the two methods considered here are formed via fiber self-assembly in a disorderly manner (see Figs. 8 a and 8 b), and there is no significant difference in terms of the manner in which the fibers are deposited. However, in terms of the single fiber shape ( Figs. 8 a and 8 b) and the extent of filling and weaving observed within the paper sheets ( Figs. 8 c and 8 d), the sheets show significant differences. For the paper sheet prepared via the wet forming method, each fiber in the network making up the paper sheet is flat and loosely woven, whereas the paper sheets prepared via the solution casting procedure exhibit fibers that are plump and form a compacted weave pattern. This illustrates that the compactness of the paper sheet obtained using the solution casting method is higher than that of the sheet obtained via the wet forming process. The compactness of the paper sheets was calculated to be 0.399 g/cm 3 for the sheet obtained via the wet forming method and 0.477 g/cm 3 for the sheet obtained via the solution casting method. In general, better mechanical properties, such as higher tear and burst indexes, of paper sheets are associated with higher compactness. It is likely the higher compactness of the paper sheet prepared via the solution casting method explains its superior mechanical properties.

Surface (a and b) and cross sections (c and d) of the paper sheets prepared from the two pulps (a and c correspond to sheets obtained via the wet papermaking process, and b and d correspond to sheets obtained via the solution casting method).

Surface (a and b) and cross sections (c and d) of the paper sheets prepared from the two pulps (a and c correspond to sheets obtained via the wet papermaking process, and b and d correspond to sheets obtained via the solution casting method).

Nitrogen adsorption isotherms and pore structure.—

Nitrogen adsorption/desorption isotherms at −77 K obtained from both samples are shown in Figure 9 . The isotherms of both samples were similar: The nitrogen adsorption capacities of the two samples are very small (a maximum of 2.5 cm 3 /g for the sample obtained via the solution casting method and 1.5 cm 3 /g for the sample obtained via the wet forming method), which indicates that there is not a strong interaction between either material and adsorbed gas and that adsorptive molecules gather around the most attractive sites on the surface. The two samples are largely nonporous, with the exception of a small number of micropores with a characteristic size of 2.5 nm. Due to a slight increase in the number of micropores, the nitrogen gas adsorption capacity of the paper sheets prepared by the solution casting method was 66.67 percent higher than that of the sheets prepared via the wet papermaking process; this is consistent with the analysis of the SEM results.

Nitrogen adsorption/desorption isotherms (left) and the corresponding pore size distributions curves (right) from the paper sheets prepared from the pulps considered in this work.

Nitrogen adsorption/desorption isotherms (left) and the corresponding pore size distributions curves (right) from the paper sheets prepared from the pulps considered in this work.

In this work, paper sheets were prepared via a wet forming process and a solution casting method, and the mechanical properties of the sheets were used as the evaluation index for the optimization of the contents of eucalyptus and Simao pine pulps in the two processes considered. The optimal ratio of eucalyptus pulp to Simao pine pulp was found to be 94:6 when considering the wet forming process; at this ratio, the tear, tensile, and burst indexes and the folding endurance were found to be 4.43 mN·m 2 ·g −1 , 27.47 N·m·g −1 , 1.13 kPa·m 2 ·g −1 , and 11.38 times, respectively. In the solution casting process, the optimal ratio of eucalyptus to Simao pine pulps was found to be 88:12, and at this ratio, the paper exhibited tear, tensile, and burst indexes and folding endurance of 11.73 mN·m 2 ·g −1 , 23.03 N·m·g −1 , 0.68 kPa·m 2 ·g −1 , and 25.50 times, respectively.

We measured the properties of the pulps and the physical characteristics of the resulting paper generated via these two processes with their respective optimal mass ratios. The cellulose, hemicellulose, and lignin contents of the pulp treated via the solution casting method were lower by 1.88, 3.11, and 2.67 percent, respectively, compared to the values obtained from the pulp treated by the wet papermaking process, but the water retention value, zeta potential, and carboxyl content were larger by 50.31, 123.41, and 50.15 percent, respectively, using the former process; the drainage time of the material obtained via the solution casting method was one-fifth that of the material obtained via the wet forming process. The paper sheet prepared via the solution casting method exhibited weaker hydrogen bonding and decreased crystallinity but a higher compactness and nitrogen gas adsorption capacity (19.55% and 66.7% higher, respectively) than that obtained via the wet papermaking process. This was hypothesized to be due to the single fibers being more plump and the cellulose with a polymerization degree of less than 700 having been dissolved and regenerated in solution cast process.

This work shows that the physical properties of the paper prepared via the two processes considered here, using their respective optimal weight ratios of the different types of pulp, have their own advantages. To obtain a paper with a higher tensile and burst strength, the wet forming method should be used; with the aim of creating sheets with other mechanical properties being higher, the solution casting process should be selected. However, it is noted that the solution casting process limits the possibility of large-scale continuous production.

The authors would like to acknowledge financial support from the Science and Technology Supported Foundation of the Guizhou Province (grant no. [2018]2334), the Top Science and Technology Talents Project of the Guizhou Education Department (grant no. qianjiaoji[2022]090), the Foundation of Liupanshui Normal University (grant no. LPSSYCYFZ202101), the High Level Talent Project of Liupanshui Normal University (grant no. LPSSYKYJJ202302), the Guizhou Provincial Key Laboratory of Coal Clean Utilization (grant no. qiankehepingtairencai [2020]2001), the Guizhou Provincial Creative Team Project of Coal Clean Processing and Utilization (grant no. qianheKYzi [2020]027), the Applied Basic Research Project of Qujing Normal University (grant no. 2077360172), the Scientific and Technological Innovation Team for Green Catalysis and Energy Materialien Yunnan Institutions of Higher Learning, and the Surface Project of Yunnan Province Science and Technology Department (grant no. 20210 A070001-050). The authors declare that they have no commercial or associative conflicts of interest.

Author notes

The authors are, respectively, Professor, Guizhou Provincial Key Lab. of Coal Clean Utilization, School of Chemistry and Materials Engineering, Liupanshui Normal Univ., Liupanshui, Guizhou 553004, People's Republic of China ( [email protected] [corresponding author]); Undergraduate student, Guizhou Provincial Key Lab. of Coal Clean Utilization, School of Chemistry and Materials Engineering, Liupanshui Normal Univ., Liupanshui, Guizhou 553004, People's Republic of China; Undergraduate student, Guizhou Provincial Key Lab. of Coal Clean Utilization, School of Chemistry and Materials Engineering, Liupanshui Normal Univ., Liupanshui, Guizhou 553004, People's Republic of China; Undergraduate student, Guizhou Provincial Key Lab. of Coal Clean Utilization, School of Chemistry and Materials Engineering, Liupanshui Normal Univ., Liupanshui, Guizhou 553004, People's Republic of China; Undergraduate student, Guizhou Provincial Key Lab. of Coal Clean Utilization, School of Chemistry and Materials Engineering, Liupanshui Normal Univ., Liupanshui, Guizhou 553004, People's Republic of China; and Professor, College of Chemistry and Environ. Sci., Qujing Normal Univ., Qujing, Yunnan 655000, People's Republic of China ( [email protected] [corresponding author]). This paper was received for publication in January 2023. Article no. 23-00007.

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A re-view of Research Organizations from around the world supporting Pulp and Paper Industry's being and trend setting

Pulp and Paper industry has a few selected hot-spots across the globe. Irrespective of actual positions USA, Canada, Finland, Sweden, Japan, Australia and a few other Latin American countries. Paper making and pulp sourcing has to be backed by a renowned, up to the mark and unparalleled research centre, at least one if not more. Pulp and Paper Technology shall dig into such supporting entities in the most 'Pulp and Paper' happening regions in the world.

More than 75% of world's spending on paper and products is accumulated at a relatively small proportion of the world. This proportion includes earlier mentioned countries USA, Canada, Finland, Sweden, Japan and Australia. This huge in flow from many corners of the world makes evident that Paper industry in Finland, Sweden, Canada and so on are strongly supported with resources as well as distinguished research centres which provides time to time upgrades and establish trends by themselves instead of following a trend. Canada among its other peers has invested lot of knowledge into Pulp and Paper research that has pulled many firms to top of industry table. The Pulp and Paper Research Institute, Canada or most often called PaPRICan is the noted research centre on the planet for support of Pulp and Paper industries around the globe. Canada which provided resource base for paper world giants like the Domtar Inc, Canfor, IFP and once upon a time wealthy Abitibi Bowater Inc. has several State and Private universities and research centres working exclusively for the same reason. Apart from an exclusive research facility

PaPRICan also extends its diligence through extensive reach via universities across Canada. The McGill Research Centre at the McGill University, Canada, University of British Columbia and Dr. Jack McKenzie Limerick Pulp and Paper Research and Education centre, University of New Brunswick are also established with facilities to work Pulp and Paper related research in collaboration with each other.

Adjacent to Canada, the biggie, United States of America also sports several research entities across Universities and private firms of America. Some of those include Pulp and Paper Research Institute for Green Science at the Carnegie Mellon University, Pulp and Paper Research & Education Alliance at the University of Minnesota and Centre for the Biology and Natural Systems.

Coming to Europe, it is a land of paper world leaders SCA, UPM-Kymmene, Stora Enso, Norske Skog, Metsaliitto and a few more. But, most of these giants are out of a small portion of Europe; hence this part of the world is more densely populated with biggest and oldest paper mills of the world. These juggernauts are surrounded by some of the world renowned Pulp and Paper research institutes that spread across Sweden, Norway, Finland and the Netherlands. Svenska Papper and the Nordic Pulp & Paper Research Journal from Sweden, Pulp and Paper group at Norwegian University of Science & Technology and Paper & Fiber Research Institute from Norway, University of Technology, Delft at Netherlands and KesKus Laboratorio of Finland all are behind the lights of European Pulp and Paper reign. For Asia, Australia hosts the Australian Pulp and Paper Institute as well as Japan has a Pulp and Paper research Institute working for the same. All these Research institutes and organizations work to bring out a best solution for the task they take up.

Pulp and Paper Technology shall dig more into specific research interests of all these think tanks from around the globe who create trends rather than follow.

As an excerpt, here is a finding from archives of Pulp and Paper research dated back to early 2000s, Dr. Krotov from the Ukrainian Pulp and Paper Research Institute of Kiev deviced new design for a machine that can produce pulp from whole stalk hemp and other materials. Hemp is actually a cheapest, by all means, and source for best quality paper cellulose. So it can be used for best and optimum paper making. This has been crucial since its discovery but not paid a good deal of interest in recent times. There are several such issues buried and many are coming into existence. Pulp and Paper Technology shall give importance to everything that is good for Pulp and Paper industry.

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March 4, 2024 From lab to leadership: Q&A with Jessica Carette, Project Manager of R&D at Cascades

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February 26, 2024 Join the 2024 Women in Forestry virtual summit on March 8!

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January 4, 2024 Safest Mills in Canada 2022: A look at how Canadian mills are faring

April 23, 2024 kimberly-clark reports financial results for first quarter of 2024, april 23, 2024 sonoco shares its 2023 corporate sustainability report, april 23, 2024 canfor pulp, canfor jointly release 2023 sustainability report, april 22, 2024 domtar employees celebrate earth day in communities where the company operates, april 22, 2024 west fraser completes sale of two of its western canada pulp mills, april 18, 2024 paper excellence invests in the future of its communities through scholarships, april 16, 2024 fesbc funding supports sustainable forest management in b.c., april 16, 2024 international paper signs agreement to acquire ds smith, april 15, 2024 andritz, microsoft collaborate to drive innovation in the manufacturing industry, april 12, 2024 fsc canada appoints sean dolter as director of policy and standards, april 11, 2024 resolute shares steps taken to strengthen its collaborations with indigenous communities, april 10, 2024 b.c. introduces measures to streamline wildfire-damaged wood recovery, advertisement.

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Valmet launches its next generation distributed control system – Valmet DNAe

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Emerson introduces its Rosemount 9195 Wedge Flow Meter

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Toscotec introduces a new generation design of its TT Brain DCS

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Voith launches its digital solution OnView.Energy for the paper industry

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Kruger Products starts up $575M tissue plant, announces additional capacity

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CCCA launches video campaign to educate Canadians about the corrugated industry

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FPAC announces winners of its 2020 Awards of Excellence

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AF&PA debuts pulp and paper–focused video series on forestry practices

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Valmet honours four industry professionals on International Women’s Day

The power of persistence: q&a with victoria popnikolov, plant manager at cascades, from lab to leadership: q&a with jessica carette, project manager of r&d at cascades.

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Top 10 Under 40: Meet Tania Prevost from Kruger Prouducts

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Top 10 Under 40: Meet Taneal Brucks from Meadow Lake Pulp, Paper Excellence

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Revolutionizing brewing: Endress+Hauser unveils QWX43 fermentation monitor for real-time insights

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Clippard’s Cordis line: Precision proportional pressure and flow-control devices

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Unlock the power of thermal processing: Marion’s comprehensive handbook delivers expert guidance

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Festo fuels industrial transformation with cutting-edge automation products

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Westlock’s valve-monitoring solutions: The perfect match for oil and gas challenges

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Motion Terminal Festo Inc

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IMAGES

  1. Nordic Pulp & Paper Research Journal

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  2. (PDF) Blending of nonwood fiber pulp for making paper

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  3. Free Handbook Of Pulp And Paper Technology

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  4. The Pulp & Paper Industry: Myths vs. Facts

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  5. Research Paper vs. Review Paper: Differences Between Research Papers

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  6. Century Pulp and Paper start-up

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VIDEO

  1. Product journey: from waste paper to moulded pulp packaging

  2. Hilti Solutions for Pulp & Paper projects

  3. 😱 Paper & pulp

  4. Pulp Nonfiction: Low-Cost Touch Tracking for Paper

  5. Lec 17: Pulp and Paper Industry

  6. Endo Articles Review: Outcomes of Pulpotomies Clinical Study With Dr Fida and Meshkin Part 1 of 3

COMMENTS

  1. Decarbonizing the pulp and paper industry: A critical and systematic review of sociotechnical developments and policy options

    Research estimates that each tonne of paper manufactured produces 0.6 tonnes of fossil CO 2 [131] and consumes between 5 and 17 GJ of process heat [15]. ... Reference Document for the Production of Pulp, Paper and Board indicates that waste heat recovery from bleaching can reach steam savings of 30 MJ/t [59].

  2. (PDF) Pulp and paper production: A review

    Pulp and paper production are e xtremely complex an d incorporate a wide variety of process fields, including woo d. preparation, pulping, chemical recovery, bleaching and paper production, to ...

  3. Country-specific net-zero strategies of the pulp and paper industry

    The pulp and paper industry is an important contributor to global greenhouse gas emissions 1, 2. Country-specific strategies are essential for the industry to achieve net-zero emissions by 2050 ...

  4. Trends and strategies in the effluent treatment of pulp and paper

    The pulp and paper industry typically required a vast amount of water during various operational stages such as washing, pulping, bleaching, and paper-making. According to available data, the pulp and paper industry consumes 250-300 m 3 of water to produce 1 ton of paper (Chaudhry and Paliwal, 2018). As a result, substantial liquid waste is ...

  5. A Comprehensive Review on Pulp and Paper Industries Wastewater

    The pulp and paper industry generates vast amounts of wastewater, and its character heavily depends on various factors (raw material, the undertaken process, the final product, etc.). The wastewater from this sector, which originates from several sources in each mill and are mostly combined, is polluting and hazardous. This paper presents a state-of-the-art review of the physical, chemical ...

  6. Environmental Regulation in the Pulp and Paper Industry: Impacts and

    Purpose of Review In this article, we review existing research addressing how environmental regulations have influenced the pulp and paper industry. These regulations appear in different forms and designs and address air and water pollution as well as climate change. The paper devotes particular attention to how various regulations have affected sustainable technological change and the ...

  7. Processes and problems of pulp and paper industry: an overview

    The pulp and paper industry is a highly energy-intensive and water-consuming industry. This industry is known for the utilization of a wide range of raw materials, containing cellulose fibers (generally wood, recycled paper, and agricultural residues), for the production of various grades of paper. There are several processes involved in the conversion of raw materials to the paper product ...

  8. Pulp, paper, and packaging in the next decade ...

    A healthy niche industry making bio-products has existed for many years alongside large-volume pulp, paper, and board products. We are in the midst of an explosion of research activity to develop new bio-products, ranging from applications for nanofibers to composite materials and lignin-based carbon fiber.

  9. Overestimated carbon emission of the pulp and paper industry in China

    Pulp and paper industry is the fourth largest energy-intensive industry in the world that heavily impacts the environment [1].Under the background of COVID-19 epidemic, the demand for disposable paper products is increasing in recent year with a strong need of least environmental influences [2].As displayed in Fig. 1, Asia-Pacific region (mainly East Asia), Europe (mainly Western Europe) and ...

  10. A review of the traditional pulping methods and the recent ...

    The demand for paper and pulp-derived products to fulfill consumer needs is increasing considerably globally. This work provides a critical overview of the various traditional pulping methods and describes the recent improvements in pulping processes. A comparison of different pulping techniques has shown that the mechanical pulping process produces high pulp yields per unit volume of wood of ...

  11. (PDF) Pulp and paper industry: An overview on pulping technologies

    The pulp and paper sector currently plays important part in the world's economy. In this paper, we present a review of pulping technologies to convert logs or wood chips and non-woody materials ...

  12. Pulp and paper industry: An overview on pulping ...

    Abstract. The pulp and paper sector currently plays important part in the world's economy. In this paper, we present a review of pulping technologies to convert logs or wood chips and non-woody materials into pulp for use in papermaking which consist of mechanical, chemical and semi-mechanical. It also talks about the history of papermaking and ...

  13. Introduction to pulp and paper industry: Global scenario

    Berg P and Lingqvist. Pulp, Paper and packaging in the next decade: transformational change. McKinsey & Company for paper, forest products and packaging. 2019. Search in Google Scholar. 74. Toppinen A, Patari S, Tuppura A, Jantunen A. The European pulp and paper industry in transition to a bio economy: a Delphi study. Futures J. 2017;88:1-14.

  14. 21003 PDFs

    Explore the latest full-text research PDFs, articles, conference papers, preprints and more on PULP AND PAPER. Find methods information, sources, references or conduct a literature review on PULP ...

  15. Pulp and paper mill wastes: utilizations and prospects for high value

    The pulp and paper mill generates a large volume of wastes with an estimate of around 100 tonnes per 550 tonnes of pulp production. Though the toxicity of pulp and paper wastes is minimal appropriate disposal technique is required for appropriate management of the land, environment, and allied issues (Monte et al. 2009). As per the ...

  16. Non-wood fibers as raw material for pulp and paper industry

    Pulp and paper industry in the world have been growing fast. As a result, there has been a massive request for pulp and paper raw materials. The raw materials used in papermaking can be classified into three groups: wood, non-wood, and recycled wastepaper. The Non-wood raw material is an important fiber resource in the regions where forest resources are limited. The current usage of non-wood ...

  17. Multi-tier supply chain sustainability in the pulp and paper industry

    The pulp and paper industry has significant sustainability implications and necessarily requires a careful consideration of direct and lower-tier suppliers for effective sustainable supply chain management. ... and marketing. Her research has been published in MIS Quarterly, Decision Sciences Journal, Transportation research Part B, Journal of ...

  18. Future perspective of pulp and paper industry

    21.1. Introduction. In recent years, the manufacturing and demand for paper and paper products are rising dramatically around the globe. This leads to high energy consumption and emission of CO 2 in the paper and pulp industry for increased production. A large amount of waste generation as a result of industrial activities for producing paper is a significant problem.

  19. Full article: Exploring the Possibilities of Producing Pulp and Paper

    The increasing consumption of paper and the demand can be fulfilled by identifying potential sources for producing paper and pulp. The utilization of wood and fibers in pulp and paper making industry is mainly dependent upon three main factors namely the chemical composition of the fibers, the fiber extraction process and the anatomical ...

  20. A deep learning-based approach for performance assessment and

    The pulp and paper industry is critical to global industrial and economic development. Recently, India's pulp and paper industries have been facing severe competitive challenges. The challenges have impaired the environmental performance and resulted in the closure of several operations. Assessment and prediction of the performance of the Indian pulp and paper industry using various parameters ...

  21. Physical Properties of Pulp and Paper: A Comparison of Forming

    The compactness of the paper sheets was calculated to be 0.399 g/cm 3 for the sheet obtained via the wet forming method and 0.477 g/cm 3 for the sheet obtained via the solution casting method. In general, better mechanical properties, such as higher tear and burst indexes, of paper sheets are associated with higher compactness.

  22. Moulded Pulp Manufacturing: Overview and Prospects for the Process

    However, it remains a greatly under-researched area, and there is an arising need to consolidate the best practices from research and industry in order to increase its implementation. The goal of this paper is to give an overview of the main aspects involved in the manufacture of moulded pulp products.

  23. Full article: Use of modelling and simulation in the pulp and paper

    In pulp and paper the modelling and simulation of the pulp production processes was the first major application. Since then several other applications have been realised though papermaking has never been on the lead concerning the use of computer-based modelling and simulation. The complex nature of the materials is one of the most demanding ...

  24. Research Organizations Supporting Pulp and Paper Industry

    The Pulp and Paper Research Institute, Canada or most often called PaPRICan is the noted research centre on the planet for support of Pulp and Paper industries around the globe. Canada which provided resource base for paper world giants like the Domtar Inc, Canfor, IFP and once upon a time wealthy Abitibi Bowater Inc. has several State and ...

  25. Pulp and Paper Canada

    April 3, 2024Kemira closes manufacturing lines due to the ongoing political strikes in Finland. Pulp & Paper Canada reports on the pulp and paper industry in Canada through articles about mills, people, innovations in research, technology, management and financing, as well as forecasts of future trends.