The Environmentally Benign Pulping Process of Non-Wood Fibers
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Making! the E-Magazine for the Fibrous Forest Products Sector
PAPERmaking! The e-magazine for the Fibrous Forest Products Sector Produced by: The Paper Industry Technical Association Volume 5 / Number 1 / 2019 PAPERmaking! FROM THE PUBLISHERS OF PAPER TECHNOLOGY Volume 5, Number 1, 2019 CONTENTS: FEATURE ARTICLES: 1. Wastewater: Modelling control of an anaerobic reactor 2. Biobleaching: Enzyme bleaching of wood pulp 3. Novel Coatings: Using solutions of cellulose for coating purposes 4. Warehouse Design: Optimising design by using Augmented Reality technology 5. Analysis: Flow cytometry for analysis of polyelectrolyte complexes 6. Wood Panel: Explosion severity caused by wood dust 7. Agriwaste: Soda-AQ pulping of agriwaste in Sudan 8. New Ideas: 5 tips to help nurture new ideas 9. Driving: Driving in wet weather - problems caused by Spring showers 10. Women and Leadership: Importance of mentoring and sponsoring to leaders 11. Networking: 8 networking skills required by professionals 12. Time Management: 101 tips to boost everyday productivity 13. Report Writing: An introduction to report writing skills SUPPLIERS NEWS SECTION: Products & Services: Section 1 – PITA Corporate Members: ABB / ARCHROMA / JARSHIRE / VALMET Section 2 – Other Suppliers Materials Handling / Safety / Testing & Analysis / Miscellaneous DATA COMPILATION: Installations: Overview of equipment orders and installations since November 2018 Research Articles: Recent peer-reviewed articles from the technical paper press Technical Abstracts: Recent peer-reviewed articles from the general scientific press Events: Information on forthcoming national and international events and courses The Paper Industry Technical Association (PITA) is an independent organisation which operates for the general benefit of its members – both individual and corporate – dedicated to promoting and improving the technical and scientific knowledge of those working in the UK pulp and paper industry. -
The Effect of Organosolv Pretreatment Variables on Enzymatic Hydrolysis of Sugarcane Bagasse
Chemical Engineering Journal 168 (2011) 1157–1162 Contents lists available at ScienceDirect Chemical Engineering Journal journal homepage: www.elsevier.com/locate/cej The effect of organosolv pretreatment variables on enzymatic hydrolysis of sugarcane bagasse L. Mesa a, E. González a, C. Cara b, M. González a, E. Castro b, S.I. Mussatto c,∗ a Center of Analysis Process, Faculty of Chemistry and Pharmacy, Central University of Las Villas, Villa Clara, Cuba b Department of Chemical Environmental and Materials Engineering, Faculty of Experimental Sciences, University of Jaén, Jaén, Spain c Institute for Biotechnology and Bioengineering, Centre of Biological Engineering, University of Minho, Campus de Gualtar, 4710-057 Braga, Portugal article info abstract Article history: Sugarcane bagasse pretreated with dilute-acid was submitted to an organosolv ethanol process with Received 10 November 2010 NaOH under different operational conditions (pretreatment time, temperature, and ethanol concentra- Received in revised form 27 January 2011 tion) aiming to maximize the glucose yield in the subsequent enzymatic hydrolysis stage. The different Accepted 3 February 2011 pretreatment conditions resulted in variations in the chemical composition of the solid residue as well as in the glucose recovered by enzymatic hydrolysis. All the studied variables presented significant (p < 0.05) Keywords: influence on the process. The optimum organosolv pretreatment conditions consisted in using 30% (v/v) Sugarcane bagasse ethanol at 195 ◦C, during 60 min. Enzymatic hydrolysis of the residue then obtained produced 18.1 g/l Organosolv Ethanol glucose, correspondent to a yield of 29.1 g glucose/100 g sugarcane bagasse. The scale-up of this process, Enzymatic hydrolysis by performing the acid pretreatment in a 10-l semi-pilot reactor fed with direct steam, was success- Glucose fully performed, being obtained a glucose yield similar to that found when the acid pretreatment was performed in autoclave. -
Master's Thesis
2008:081 MASTER'S THESIS Pulping Wastes and Abandoned Mine Remediation Application of green liquor dregs and other pulping by-products to the solidification/stabilisation of copper mine tailings Lucile Villain Luleå University of Technology D Master thesis Chemistry Department of Civil and Environmental Engineering Division of Architecture and Infrastructure 2008:081 - ISSN: 1402-1552 - ISRN: LTU-DUPP--08/081--SE Luleå University of Technology MASTER THESIS Pulping Wastes and Abandoned Mine Remediation Application of green liquor dregs and other pulping by-products to the solidification/stabilisation of copper mine tailings Lucile Villain June 2008 Department of Civil, Mining and Environmental Engineering Division of Architecture and Infrastructure ACKNOWLEDGEMENTS This master thesis was realised in Luleå University of Technology and in Ramböll Sverige AB consultancy in Luleå (Northern Sweden). I would like to express my gratitude to my supervisor Christian Maurice who made the project possible and who guided me throughout this work while granting me autonomy as well. I am also grateful to Ramböll team who nicely welcomed me in spite of my poor Swedish, and helped in practical issues. I would like to thank Nils Hoffner for his useful information, Tomas Forsberg for his valuable help in the laboratory, Ulla-Britt Uvemo for her kind and constant assistance, and Lea Rastas Amofah for her friendly company and wise advice. I am also thankful towards my family who encouraged me and sent me motivation from France; many thanks to my friends in Luleå who gave me support and joy during these days. 1 ABSTRACT Green liquor dregs are one type of chemical by-products produced by the pulp and paper industry which are usually landfilled, and cause concern to the pulp mills due to the cost of landfilling. -
Separation and Utilization of Solid Residue Streams from Kraft Pulp Mills
Separation and Utilization of Solid Residue Streams from Kraft Pulp Mills Master’s thesis in Innovative and Sustainable Chemical Engineering CECILIA STEEN Department of Chemistry and Chemical Engineering CHALMERS UNIVERSITY OF TECHNOLOGY Gothenburg, Sweden 2016 Master’s thesis 2016 Separation and Utilization of Solid Residue Streams from Kraft Pulp Mills CECILIA STEEN Department of Chemistry and Chemical Engineering Division of Forest Products and Chemical Engineering Chalmers University of Technology Gothenburg, Sweden 2016 Separation and Utilization of Solid Residue Streams from Kraft Pulp Mills CECILIA STEEN © CECILIA STEEN, 2016. Supervisors: Tuve Mattsson, Department of Chemistry and Chemical Engineering Maria Björk, Stora Enso Biomaterials Rickard Wadsborn, Stora Enso Pulp Competence Centre Examiner: Hans Theliander, Department of Chemistry and Chemical Engineering Master’s Thesis 2016 Department of Chemistry and Chemical Engineering Division of Forest Products and Chemical Engineering Chalmers University of Technology SE-412 96 Gothenburg Telephone +46 31 772 1000 Cover: A schematic of the chemical recovery process of a Kraft pulp mill. Typeset in LATEX Printed by Department of Chemistry and Chemical Engineering Gothenburg, Sweden 2016 iv Separation and Utilization of Solid Residues Streams from Kraft Pulp Mills CECILIA STEEN Department of Chemistry and Chemical Engineering Chalmers University of Technology Abstract Separation of solid residues serve as an important kidney of non-process elements in a kraft pulp mill. The separation and later utilization of these residues as a possible source of nutrients in the forest is of interest in this thesis. One such solid residue is green liquor dregs, which are removed from the green liquor by means of filtration. -
Basics of Kraft Pulping
Lignin Wood is composed of many chemical components, primarily extractives, carbohydrates, and lignin, which are distributed nonuniformly as the result of anatomical structure. Lignin is derived from the Latin term lignum, which means wood.1 Anselme Payen (1838) was the first to recognize the composite nature of wood and referred to a carbon- rich substance as the “encrusting material” which embedded cellulose in the wood. Schulze (1865) later defined this encrusting material as lignin. Lignin has been described as a random, three-dimensional network polymer comprised of variously linked phenylpropane units.2 Lignin is the second most abundant biological material on the planet, exceeded only by cellulose and hemicellulose, and comprises 15-25% of the dry weight of woody plants. This macromolecule plays a vital role in providing mechanical support to bind plant fibers together. Lignin also decreases the permeation of water through the cell walls of the xylem, thereby playing an intricate role in the transport of water and nutrients. Finally, lignin plays an important function in a plant’s natural defense against degradation by impeding penetration of destructive enzymes through the cell wall. Although lignin is necessary to trees, it is undesirable in most chemical papermaking fibers and is removed by pulping and bleaching processes. 1.1.1 Biosynthesis Plant lignins can be broadly divided into three classes: softwood (gymnosperm), hardwood (angiosperm) and grass or annual plant (graminaceous) lignin.3 Three different phenylpropane units, or monolignols, are responsible for lignin biosynthesis.4 Guaiacyl lignin is composed principally of coniferyl alcohol units, while guaiacyl-syringyl lignin contains monomeric units from coniferyl and sinapyl alcohol. -
Black Liquor Gasification
Black Liquor Gasification Summary and Conclusions from the IEA Bioenergy ExCo54 Workshop This publication provides Wood and Wastes the record of a workshop organised by IEA Bioenergy. CO2 Pool Black liquor gasification is an interesting option for production of synthesis gas that can subsequently be converted to a variety of motor fuels. The technology can be integrated into modern, Carbon ecocyclic, kraft pulp mill Dioxide Pulp and Paper biorefineries. USA and Sweden lead developments in this field. It is of interest primarily among countries with strong pulp and paper industries and national policies which promote substitution of petrol and diesel by biofuels. IEA Bioenergy IEA BIOENERGY: ExCo:2007:03 INTRODUCTION a large pulp and paper industry. It is thus of great interest to convert the primary energy in the black liquor to an This publication provides a summary and the conclusions energy carrier of high value. from a workshop organised by IEA Bioenergy. It was held in conjunction with the 54th meeting of the Executive Worldwide, the pulp and paper industry currently processes Committee in Ottawa on 6 October 2004. The purpose of the about 170 million tonnes of black liquor (measured as dry workshop was to present the developments of black liquor solids) per year, with a total energy content of about 2EJ, gasification for the production of energy and/or biofuels making black liquor a very significant biomass source (see for transport and discuss the remaining barriers, either Figure 1). In comparison with other potential biomass technical or strategic, that need to be overcome in order sources for chemicals production, black liquor has the to accelerate the successful demonstration of black liquor great advantage that it is already partially processed and gasification technologies and subsequently their penetration exists in a pumpable, liquid form. -
( 12 ) United States Patent
US009902815B2 (12 ) United States Patent ( 10 ) Patent No. : US 9 ,902 , 815 B2 Tamminen et al. ( 45 ) Date of Patent: Feb . 27 , 2018 ( 54 ) FUNCTIONALIZED LIGNIN AND METHOD ( 58 ) Field of Classification Search OF PRODUCING THE SAME ??? . .. C07G 1 / 00 See application file for complete search history . @(71 ) Applicant : Teknologian tutkimuskeskus VTT , VTT (FI ) ( 56 ) References Cited U . S . PATENT DOCUMENTS @(72 ) Inventors : Tarja Tamminen , Espoo (FI ) ; Jarmo Ropponen , Espoo (FI ) ; Eva - Lena Hult , 2 ,429 , 102 A 10 / 1947 Lewis et al. Espoo ( FI) ; Kristiina Poppius- Levlin , 3 , 149 , 085 A 9 / 1964 Ball et al . Espoo (FI ) 4 ,017 ,430 A * 4 / 1977 Briggs .. .. .. 530 / 502 5 ,773 , 590 A * 6 / 1998 Hart 530 / 500 6 ,172 ,204 B1 * 1 /2001 Sarkanen et al. 530 /500 @(73 ) Assignee : Teknologian tutkimuskeskus VTT Oy, 2010 /0105798 A1 * 4 /2010 Hasegawa . .. .. 522 / 99 Espoo (FI ) 2010 /0152428 A1* 6 / 2010 Gifford et al . .. .. .. 530 / 504 2010 / 0204368 A1 * 8 / 2010 Benko et al. .. .. .. .. .. .. .. 524 / 73 ( * ) Notice : Subject to any disclaimer, the term of this 2010 / 0331531 A1 * 12 / 2010 Mykytka .. .. 530 / 501 patent is extended or adjusted under 35 2011/ 0263836 A1 * 10 / 2011 Vuorenpalo et al. .. .. 530 / 500 U . S . C . 154 ( b ) by 33 days. 2012 /0012035 A1 * 1 / 2012 Blank et al. .. .. 106 / 802 ( 21) Appl. No. : 14 /348 , 904 OTHER PUBLICATIONS (22 ) PCT Filed : Oct. 8 , 2012 Holmbom ( Journal of the American Oil Chemists Society , 1977 , p . 289 - 293 ) . * Stenberg et al . (Surface Coatings International Part B : Coatings ( 86 ) PCT No. : PCT/ FI2012 /050965 Transactions , vol. 88 , B2 , 83 - 156 , 2005 ) . -
What Happens to Cellulosic Fibers During Papermaking and Recycling? a Review
PEER-REVIEWED REVIEW ARTICLE ncsu.edu/bioresources WHAT HAPPENS TO CELLULOSIC FIBERS DURING PAPERMAKING AND RECYCLING? A REVIEW Martin A. Hubbe,* Richard A. Venditti, and Orlando J. Rojas Both reversible and irreversible changes take place as cellulosic fibers are manufactured into paper products one or more times. This review considers both physical and chemical changes. It is proposed that by understanding these changes one can make better use of cellulosic fibers at various stages of their life cycles, achieving a broad range of paper performance characteristics. Some of the changes that occur as a result of recycling are inherent to the fibers themselves. Other changes may result from the presence of various contaminants associated with the fibers as a result of manufacturing processes and uses. The former category includes an expected loss of swelling ability and decreased wet-flexibility, especially after kraft fibers are dried. The latter category includes effects of inks, de-inking agents, stickies, and additives used during previous cycles of papermaking. Keywords: Paper recycling, Drying, Deinking, Hornification, Inter-fiber bonding, Refining, Fines, Fiber length, Conformability Contact information: Department of Forest Biomaterials Science and Engineering, Box 8005, North Carolina State University, Raleigh, NC 27695-8005, USA; *Corresponding author: [email protected] INTRODUCTION Cellulosic fibers can change significantly when formed into a wet web of paper and subsequently subjected to such processes as pressing, drying, printing, storage, repulping, and deinking. Some of the changes can be subtle. Often it is possible to substitute recovered fibers in place of virgin fibers used for the production of paper or paperboard. On the other hand, characteristic differences between recycled fibers and virgin fibers (fresh from pulping wood, not recycled) can be expected; many of these can be attributed to drying. -
Fungal Pretreatment for Organosolv Pulping and Dissolving Pulp Production
13 Fungal Pretreatment for Organosolv Pulping and Dissolving Pulp Production ANDRÉ FERRAZ, LYUDMIL CHRISTOV, AND MASOOD AKHTAR INTRODUCTION Biopulping is the fungal pretreatment of wood chips, designed as a solid-state fer- mentation process, for production of mechanical or chemical pulps (cf. Chapters 10 and 12). The concept of biopulping is based on the ability of some white-rot fungi to colonize and degrade selectively the lignin in wood, thereby leaving the cellulose relatively intact. This chapter presents an evaluation of biopulping and biobleaching with white-rot fungi as pretreatment steps in organosolv pulping and in dissolving pulp production. Fungal-organosolv pulping is focused mainly on chemical and topo- chemical bases for the combination of biopulping and organosolv processes. Experi- mental data are presented to illustrate the potential of this fungal-chemical method to produce wood pulps. Biopulping and biobleaching with selected white-rot fungi are also evaluated as potential methods for production of dissolving pulp. A report in part has been submitted for publication in Enzyme and Microbial Technology. This chapter is based mainly on the work from a collaborative project between the Department of Microbiology and Biochemistry, The University of Orange Free State, of Bloemfontein South Africa and the USDA Forest Products Laboratory in Madison, Wisconsin. Fungal-organosolv pulping methods are based mainly on the work developed at the Department of Biotechnology in Lorena, Brazil, and the Renewable Resource Laboratory in Concepcion, Chile. ORGANOSOLV PULPING Background The need to find new technologies for pulp and paper production that cause less environmental impact has contributed to an increase in the number of studies on Environmentally Friendly Technologies for the Pulp and Paper Industry, edited by Raymond A. -
American Ft Forest & Paper 2QE5
A 1 , i American Ft Forest & Paper 2QE5; Association , - May 6, 2015 Via Hand Delivery and by Email to iones.iim(a^epa.gov Administrator Gina McCarthy (1101A) Office of the Administrator Environmental Protection Agency 1200 Pennsylvania Avenue, N.W. Washington, DC 20460 Re: Reguest for Full Exemption of Four Pulping Chemicals from the TSCA Chemical Data Reporting Rule Reguirements Dear Administrator McCarthy: The American Forest & Paper Association (AF&PA) hereby petitions EPA to amend the Chemical Data Reporting rule (CDR), 40 C.F.R. Part 711, to exempt from all CDR requirements four pulping chemicals involved in the manufacture of paper and other pulp-based products. The four pulping chemicals are complex mixtures used in the kraft pulping process: • Sulfite Liquors and Cooking Liquors, white (CAS No. 68131-33-9) (white liquor) • Sulfite Liquors and Cooking Liquors, spent (CAS No. 66071-92-9) (black liquor) • Sulfite Liquors and Cooking Liquors, spent, oxidized (CAS No. 68514-09-0) (black liquor, oxidized) • Sulfite Liquors and Cooking Liquors, green (CAS No. 68131-30-6) (green liquor) Each of these substances is manufactured and recycled onsite in a continuous closed loop. EPA has an enormous amount of information about these pulping chemicals and little current interest in them, as their potential risks are well understood and adequately managed. 1101 K Street, N.W., Suite 700 • Was hington, D.C.20005 • (202) 463•2700 •afandpa.org May 6, 2015 Page 2 This petition first identifies the four pulping chemicals in greater detail and explains why the kraft chemical regeneration process has led to inflated production volumes for these pulping chemicals in CDR data. -
A Dynamic Na/S Balance of a Kraft Pulp Mill
A dynamic Na/S balance of a kraft pulp mill Modeling and simulation of a kraft pulp mill using WinGEMS En dynamisk Na/S balans av ett sulfatbruk Modellering och simulering av ett sulfatbruk i WinGEMS Per Andersson Faculty of Health, Science and Technology Department of Engineering and Chemical Science, Chemical Engineering, Karlstad University Master theisis, 30 credits Supervisors: Niklas Kvarnström (KAU), Maria Björk (Stora Enso), Rickard Wadsborn (Stora Enso) Examinat or: Lars Järnström (KAU) 2014 -01-08 Version : 2.0 Abstract The main scope of this thesis was to create a simulation model of a kraft pulp mill and produce a dynamic Na/S balance. The model was made in WinGEMS 5.3 and the method consisted of implementing a static Na/S balance from the mill and created a model that described this chemical balance. Input data from the mill was collected and implemented in the model. A number of different cases were simulated to predict the effects of different process changes over time, dynamic balances. The result from the static balance showed that the model can describes the mill case. The result from the dynamic simulation showed that the model can be used to predict the effect of process changes over shorter periods of time. Executive Summary In the kraft mill the chemical balance is of interest to minimize the production cost. Normally there is an excess of sulfur and low levels of sodium, compared to what the process requires. In the future, the pulp mill will most likely produce other products than just pulp. These new production processes will also most likely affect the sodium and sulfur balance and there is a need to be able to predict this change. -
M^Ittt of $I)Tlos!Opfip in CHEMISTRY
PHYSICO-CHEMICAL STUDIES ON HEAVY METALS IN INDUSTRIAL WASTES AND RIVER WATER DISSERTATION FOR M^ittt of $I)tlos!opfip IN CHEMISTRY BY RUBINA CHAUDHARY DEPARTMENT OF CHEMISTRY ALIGARH MUSLIM UNIVERSITY ALIGARH (INDIA) 1989 DS1531 /^: F-HJ-VES I CO'—CHEIM I C(=%L- OT'LJFJ T. ESS ON HEZi^SW METi^^LS I hJ I hJDLJSTR:: I s^^il W#=IISTIE:S (=mMO RIVER: WftTEFi A DISSERTATION SUBMITTED IN PARTIAL FULFILMENT OF THE REQUIREMINTS FOR THE DEGREE OF MASTER OF PHILOSOPHY IN CHEMISTRY RUBINA CHAUDHARY Department of Chemistry Aligarh Muslim University ALIGARH 1989 rnone : unice : t)U4Z Z. H. College of Engineering & Technology DEPARTMENT OF APPLIED CHEMISTRY Aligarh Muslim University ALIGARH—202002 (INDIA) Ref. No. Dated CERTIFICATE This is to certify that the work des cribed in this dissertation is the original work of Miss Rubina Chaudhary, carried out under my supervision and guidance. She has fulfilled all the requirements for the award of M.Phil, degree under the Academic Ordinaces of the Aligarh Muslim University, Aligerh. The work included in this disser tation has not been submitted elsewhere. 6.11.1989 PROF. MOHAMI^AD AsJl-'-y' ^ Supervisor ACKNOWLEDGEME Hr I am extremely grateful to my Supervisor Professor Mohansnad Ajmal for his guidance/ advice and personal interest during the course of this work, without whose sympathetic and inspiring attitude, timely assistance and affectionate encouragement this work would not have emerged in its present form. My thanks are also due to Prof. K.T.Nasim, Chairman, Department of Applied Chemistry, Z.H. College of Engineering & Technology, Allgarh Muslim university, Aligarh, for providing necessary facilities.