Organosolv Pulping. a Review and Distillation Study Related to Peroxyacid Pulping

Total Page:16

File Type:pdf, Size:1020Kb

Organosolv Pulping. a Review and Distillation Study Related to Peroxyacid Pulping ORGANOSOLV PULPING ESA A review and distillation study related to peroxyacid MUURINEN pulping Department of Process Engineering OULU 2000 ESA MUURINEN ORGANOSOLV PULPING A review and distillation study related to peroxyacid pulping Academic Dissertation to be presented with the assent of the Faculty of Technology, University of Oulu, for public discussion in Savonsali (Auditorium L 4), Linnanmaa, on June 30th, 2000, at 12 noon. OULUN YLIOPISTO, OULU 2000 Copyright © 2000 Oulu University Library, 2000 Manuscript received 16 May 2000 Accepted 18 May 2000 Communicated by Professor Juhani Aittamaa Doctor Jorma Sundquist ISBN 951-42-5661-1 ALSO AVAILABLE IN PRINTED FORMAT ISBN 951-42-5660-3 ISSN 0355-3213 (URL: http://herkules.oulu.fi/issn03553213/) OULU UNIVERSITY LIBRARY OULU 2000 To Paula and Dijon Muurinen, Esa, Organosolv pulping, a review and distillation study related to peroxyacid pulping Department of Process Engineering, University of Oulu, FIN-90014 University of Oulu, Finland 2000 Oulu, Finland (Manuscript received 16 May 2000) Abstract More than 900 papers related to organosolv pulping have been reviewed in this thesis. From the information included in those papers it can be concluded that organosolv pulping processes are still in a developing stage and are not yet ready to seriously threat the position of the kraft process as the main pulp manufacturing process in the world. Distillation seems to be the main alternative as the process for recovering the solvent in organosolv pulping. A good reason for this is that using simple distillation no potentially harmful components are introduced to the process. The effect of the feed composition on the operation of a separation sequence in an organosolv process using aqueous formic and acetic acids and corresponding peroxyacids was studied. When simple distillation was used as the separation method the effect was found to be significant. The unideal nature of the formic acid-acetic acid-water mixture, the separation of which was studied, makes the ternary composition space divide into four distillation regions. Which region the feed is located in, obviously determines the economy of the distillation sequence. Shortcut calculation methods cannot be recommended for use in designing a distillation sequence for the ternary mixture studied, but they give useful information for the comparison of such sequences. They were used to choose a limited number of alternatives for studies with rigorous calculation methods. Minimum work of separation can also be used to make a satisfying estimate for the relative easeness of separation of the formic acid-acetic acid-water mixture. Thermal integration using pinch technology was also tested and found to be very useful for decreasing the thermal energy consumptions of distillation processes. Thermodynamic efficiencies for separating the formic acid-acetic acid-water mixture by simple distillation were estimated. They were found to be lower than the average value for distillation presented in literature. Keywords: solvent recovery, pinch analysis, formic acid, acetic acid Acknowledgements This research work was carried out in the Mass and Heat Transfer Process Laboratory of the Department of Process Engineering, University of Oulu, Finland, in 1994-1999. I would like to thank my supervisor, Professor Jorma Sohlo, for his encouragement and valuable comments during this research. I want to acknowledge Professor Juhani Aittamaa and Dr. Jorma Sundquist for their review of the thesis and for their useful recommendations. The financial support from Oulun yliopiston tukisäätiö, Jenny ja Antti Wihurin rahasto and Tekniikan edistämissäätiö is gratefully acknowledged. Oulu, May 2000 Esa Muurinen Contents Abstract Acknowledgements Contents 1. Introduction............................................................................................... 13 2. Pulping with organic chemicals.....................................................................16 2.1. Alcohols............................................................................................16 2.1.1. Methanol.................................................................................. 16 2.1.1.1. Catalyzed methanol pulping........................................... 17 2.1.1.2. Methanol in sulphite pulping......................................... 20 2.1.1.3. The ASAM process...................................................... 21 2.1.1.4. Methanol in soda pulping.............................................. 29 2.1.1.5. The Organocell process..................................................31 2.1.1.6. Other alkaline methanol processes................................... 36 2.1.1.7. Methanol lignins..........................................................37 2.1.1.8. Summary....................................................................39 2.1.2. Ethanol.................................................................................... 39 2.1.2.1. Catalyzed and autocatalyzed ethanol pulping..................... 40 2.1.2.2. The Alcell process........................................................49 2.1.2.3. Alkaline ethanol pulping............................................... 57 2.1.2.4. Ethanol in sulphite pulping............................................62 2.1.2.5. Simulation of ethanol pulping........................................63 2.1.2.6. The kinetics and mechanism of delignification................... 64 2.1.2.7. Ethanol lignins............................................................65 2.1.2.8. Summary....................................................................66 2.1.3. Other alcohols........................................................................... 67 2.1.3.1. Propanol and isopropanol...............................................67 2.1.3.2. Butanol...................................................................... 68 2.1.3.3. Glycols...................................................................... 70 2.1.3.4. Summary....................................................................73 2.2. Organic acids...................................................................................... 73 2.2.1. Formic acid............................................................................... 73 2.2.1.1. Pulping and bleaching with formic acid............................ 74 2.2.1.2. The Milox process........................................................75 2.2.1.3. Milox bleaching...........................................................79 2.2.1.4. Solvent recovery in Milox pulping..................................80 2.2.1.5. The chemistry of Milox pulping..................................... 84 2.2.1.6. Summary....................................................................85 2.2.2. Acetic acid................................................................................ 85 2.2.2.1. Acetic acid pulping and bleaching....................................85 2.2.2.2. Peroxyacetic acid..........................................................92 2.2.2.3. Acetosolv pulping........................................................96 2.2.2.4. Acetocell pulping.........................................................99 2.2.2.5. Formacell pulping........................................................99 2.2.2.6. Summary................................................................. 100 2.2.3. Other organic acids................................................................... 100 2.2.4. Salts of organic acids................................................................ 101 2.2.5. Summary................................................................................102 2.3. Phenol and cresols............................................................................. 102 2.3.1. Phenol....................................................................................102 2.3.2. Cresols...................................................................................106 2.3.3. Summary................................................................................108 2.4. Ethyl acetate.....................................................................................109 2.5. Amines and amine oxides....................................................................110 2.5.1. Ethylenediamine.......................................................................110 2.5.2. Hexamethylene diamine............................................................. 111 2.5.3. Methylamine........................................................................... 112 2.5.4. Ethanolamine.......................................................................... 112 2.5.5. Amine oxides...........................................................................113 2.6.6. Summary................................................................................113 2.6. Ketones........................................................................................... 114 2.7. Dioxane...........................................................................................117 2.8. Other organic compounds....................................................................120 2.9. Summary.........................................................................................122 3. Solvent recovery in peroxyacid pulping.........................................................124 3.1. The search for feasible separation methods..............................................125 3.1.1. Wells and Rose.......................................................................
Recommended publications
  • 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.
    [Show full text]
  • 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.
    [Show full text]
  • Entrained-Flow Gasification of Black Liquor and Pyrolysis Oil
    LICENTIATE T H E SIS Department of Engineering Sciences and Mathematics Division of Energy Science Yawer Jafri Entrained-Flow Gasification of Black Liquor and Pyrolysis Gasification of Black Liquor and Pyrolysis Jafri Entrained-Flow Yawer ISSN 1402-1757 Entrained-Flow Gasification of ISBN 978-91-7583-761-1 (print) ISBN 978-91-7583-762-8 (pdf) Black Liquor and Pyrolysis Oil Luleå University of Technology 2016 Pilot-Scale and Equilibrium Modelling Studies of Catalytic Co-gasification Yawer Jafri Energy Engineering Licentiate Thesis Entrained-Flow Gasification of Black Liquor and Pyrolysis Oil Pilot-scale and Equilibrium Modelling Studies of Catalytic Co-gasification Yawer Jafri Energy Engineering Division of Energy Science Department of Environmental Sciences and Mathematics Luleå University of Technology a Printed by Luleå University of Technology, Graphic Production 2016 ISSN 1402-1757 ISBN 978-91-7583-761-1 (print) ISBN 978-91-7583-762-8 (pdf) Luleå 2016 www.ltu.se b Abstract The last couple of decades have seen entrained-flow gasification of black liquor (BL) undergo an incremental process of technical development as an alternative to combustion in a recovery boiler. The ability of the technology to combine chemical recovery with the production of clean syngas renders it a promising candidate for the transformation of chemical pulp mills into integrated forest biorefineries. However, techno-economic assessments have shown that blending BL with the more easily transportable pyrolysis oil (PO) can not only increase the energy efficiency of the conversion process for methanol production, but also remove a significant roadblock to commercial deployment by partially decoupling production capacity from BL availability.
    [Show full text]
  • Supply Chain
    COMPANY OVERVIEW 2015 MAKING PRODUCTS PEOPLE DEPEND ON EVERY DAY PERFORMANCE PEOPLE PLANET International Paper is a global leader in packaging, paper, and pulp. We use renewable resources responsibly to make recyclable products that people depend on every day. We are unified around shared commitments to strengthen our people and communities, provide solutions for our customers, and ensure the sustainability of our company and our planet. Our fiber sourcing policies promote healthy and productive forests for generations to come In 2015, 93% of our facilities operated without a serious injury $15.5 million donated to address critical community needs and improve MAKING our planet PRODUCTS PEOPLE DEPEND ON CONTENTS EVERY DAY 2 2015 Highlights 3 CEO Comments 4 Businesses 6 Performance 12 People $22.4 billion 20 Planet net sales in 2015 28 Awards & Recognitions 29 Vision 2020 Goals International Paper Company Overview 2015 2 65% 13% 22% REVENUE Industrial Consumer Paper 2015 GLOBAL HIGHLIGHTS Packaging Packaging and Pulp We use renewable resources responsibly to make recyclable products people depend on every day. BY BUSINESS $2.6 billion net sales Manufacturing operations in 24 countries EMEA*/ Russia North Asia ** America $1.3 billion net sales Global 55,000 India $17.2 billion Headquarters: employees globally net sales Memphis, Tenn. $0.2 billion Latin net sales America 44,000 $1.1 billion volunteer hours net sales *Europe, Middle East, Africa worked by employees **Includes the net sales of the International Paper Sun joint venture through
    [Show full text]
  • ( 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 ) .
    [Show full text]
  • Fpl 2009 Zhu002.Pdf
    Chemical Engineering Science 64 (2009) 474 --485 Contents lists available at ScienceDirect Chemical Engineering Science journal homepage: www.elsevier.com/locate/ces Specific surface to evaluate the efficiencies of milling and pretreatment of wood for ଁ enzymatic saccharification J.Y. Zhu a,c,∗, G.S. Wang b, X.J. Pan c, R. Gleisner a aUS Forest Service, Forest Products Laboratory, Madison, WI, USA bTianjin Key Laboratory of Pulp and Paper, Tianjin University of Science and Technology, Tianjin, China cDepartment of Biological Systems Engineering, University of Wisconsin, Madison, WI, USA ARTICLE INFO ABSTRACT Article history: Sieving methods have been almost exclusively used for feedstock size-reduction characterization in the Received 9 April 2008 biomass refining literature. This study demonstrates a methodology to properly characterize specific sur- Received in revised form 19 September 2008 face of biomass substrates through two dimensional measurement of each fiber of the substrate using a Accepted 21 September 2008 wet imaging technique. The methodology provides more information than sieving methods about biomass Available online 15 October 2008 substrate. The measured dimensions of individual fibers were used to estimate the substrate external sur- Keywords: face based on a cylinder model. The substrate specific surface and mechanical milling energy consumption Specific surface were then correlated to enzymatic hydrolysis glucose yield. Results indicated that the developed method- Bioprocessing ology is effective in differentiating various size-reduction and chemical pretreatment processes in terms Enzymatic saccharification/hydrolysis of cellulose to glucose conversion efficiency and size-reduction energy consumption. Thermomechanical Feedstock processing disk milling (DM-I), exposing cellulose, is more effective than a high pressure thermomechanical disk Size reduction milling (DM-II), exposing lignin, in subsequent enzymatic hydrolysis.
    [Show full text]
  • 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.
    [Show full text]
  • TECHNICAL REPORT – PATENT ANALYSIS Enhancing Productivity in the Indian Paper and Pulp Sector
    TECHNICAL REPORT – PATENT ANALYSIS Enhancing Productivity in the Indian Paper and Pulp Sector 2018 TABLE OF contEnts ACKNOWLEDGEMENTS 10 EXECUTIVE SUMMARY 11 1 INTRODUCTION 13 2 OVERVIEW OF THE PULP AND PAPER SECTOR 15 2.1. Status of the Indian Paper Industry 15 2.2. Overview of the Pulp and Papermaking Process 20 2.3. Patenting in the Paper and Pulp Industry: A Historical Perspective 22 2.4. Environmental Impact of the Pulp and Paper Industry 25 3 METHODOLOGY 27 3.1. Search Strategy 27 4 ANALYSIS OF PATENT DOCUMENTS USING GPI 31 4.1. Papermaking; Production of Cellulose (IPC or CPC class D21) 31 4.2. Analysis of Patenting Activity in Different Technology Areas using GPI 38 5 ANALYSIS OF THE INDIAN PATENT SCENARIO WITHIN THE CONTEXT OF THIS REPORT 81 5.1. Analysis of Patents Filed in India 81 6 CONCLUDING REMARKS 91 REFERENCES 93 ANNEXURE 94 Annexure 1. Technologies related to paper manufacturing 94 Annexure 2. Sustainable/green technologies related to pulp and paper sector 119 Annexure 3. Emerging Technology Areas 127 List OF FIGURES Figure 2.1: Geographical Spread of Figure 4.11: (d) Applicant vs. Date of Indian Paper Mills .................................16 Priority Graph: Paper-Making Machines Figure 2.2: Share of Different Segments and Methods ........................................42 in Total Paper Production .......................19 Figure 4.11: (e) Applicant vs. Date of Figure 2.3: Variety Wise Production of Priority Graph: Calendars and Accessories ..43 Paper from Different Raw Materials ........19 Figure 4.11: (f) Applicant vs. Date of Figure 2.4: Different Varieties of Paper Priority Graph: Pulp or Paper Comprising Made from Various Raw Materials ..........19 Synthetic Cellulose or Non-Cellulose Fibres ..43 Figure 2.5: Diagram of a Process Block Figure 4.11: (g) Applicant vs.
    [Show full text]
  • 4. Printing and Converting Performance
    4. Printing and converting performance Paperboard converting 147 Clean edges and surfaces 155 Handling paperboard 158 Offset lithography 160 UV-offset 161 Waterless offset 162 Hybrid offset 162 Flexography 163 Screen printing 164 Digital printing 165 Gravure printing 166 Hot foil stamping 169 Embossing 171 Die-cutting & creasing 174 Lasercutting 178 Scoring 182 Creasabilty & foldability 186 Gluing 194 Binding in practice - the last link 199 Heat sealing 206 Packaging operation 203 Deep drawing 212 146 Reference Manual | IGGESUND PAPERBOARD Paperboard converting Paperboard converting Paperboard has the ability to achieve or exceed the same The increasing demands in the brand promotion process excellent image reproduction as for the best fine papers. for graphic design and the use of non-print surface enhance- Paperboard offers equal possibilities to achieve new, ment are creating innovative shapes and multi-sensory ex- challenging shapes as competing packaging materials. periences for the consumer or user who hand les the product. However, increasing demands on performance of the An understanding of the interaction between paper- material in various converting processes have become board properties and converting effi ciency is essential for evident when speeds in both printing processes and post- designers and converters, since the ultimate design of the press converting have increased. Additionally, the accept- product together with the choice of paperboard will impact ance level for impurities or slight deviations in quality in the on crucial conversion factors like printability, fl atness, and fi nal product has dropped noticeably as a result of both creasing/folding properties. Considering all the variables, end-user demands and the use of modern quality control it is probably true to say that consistency in the behaviour equipment in the various converting machines.
    [Show full text]
  • Government Paper Specification Standards
    Government March 2011 No. 12 Government March 2011 No. 12 Printed on recycled paper For sale by the Superintendent of Documents, U.S. Government Printing Office Internet: bookstore.gpo.gov Phone: toll free (866) 512-1800; DC area (202) 512-1800 F1ax: (202) 512-2104 Mail: Stop IDCC, Washington, DC 20402-000 ISBN 978-0-16-088382-8 U.S. GOVERNMENT PRINTING OFFICE WILLIAM J. BOARMAN Keeping America Informed I www.gpo.gov Public Printer of the United States March 16, 2011 The Honorable Joseph R. Biden The President of the Senate The Honorable John A. Boehner The Speaker of the House of Representatives Sirs: I have the honor to transmit herewith the Annual Report of the U.S. Government Printing Office (GPO) for the fiscal year ending September 30, 2010. The report contains the results of an audit of GPO’s financial statements conducted by an independent accounting firm. Respectfully submitted, WILLIAM J. BOARMAN Public Printer 732 North Capitol Street, NW, Washington, DC 20401-0001 I [email protected] TABLE OF CONTENTS Advisory Council on Paper Specifications ………………………………………… v Introduction …………………………………………………………………………. vii Recycled Fiber Content and Permanent Paper Standards ………...……….…………. ix Part 1. Specifications ………………...……………………………………………... 1 Runnability Requirements for Paper Used in a Federal Printing Plant ………………. 3 Printing Papers ………………………………………………………………………. 5 JCP A10: Newsprint JCP A25: Heat-Set Web Offset Machine-Finish Book JCP A50: Machine-Finish Book End JCP A55: Heat-Set Web Offset Book JCP A60: Offset Book JCP A61: No. 1 Offset
    [Show full text]
  • Conservation of Coated and Specialty Papers
    RELACT HISTORY, TECHNOLOGY, AND TREATMENT OF SPECIALTY PAPERS FOUND IN ARCHIVES, LIBRARIES AND MUSEUMS: TRACING AND PIGMENT-COATED PAPERS By Dianne van der Reyden (Revised from the following publications: Pigment-coated papers I & II: history and technology / van der Reyden, Dianne; Mosier, Erika; Baker, Mary , In: Triennial meeting (10th), Washington, DC, 22-27 August 1993: preprints / Paris: ICOM , 1993, and Effects of aging and solvent treatments on some properties of contemporary tracing papers / van der Reyden, Dianne; Hofmann, Christa; Baker, Mary, In: Journal of the American Institute for Conservation, 1993) ABSTRACT Museums, libraries, and archives contain large collections of pigment-coated and tracing papers. These papers are produced by specially formulated compositions and manufacturing procedures that make them particularly vulnerable to damage as well as reactive to solvents used in conservation treatments. In order to evaluate the effects of solvents on such papers, several research projects were designed to consider the variables of paper composition, properties, and aging, as well as type of solvent and technique of solvent application. This paper summarizes findings for materials characterization, degradative effects of aging, and some effects of solvents used for stain reduction, and humidification and flattening, of pigment-coated and modern tracing papers. Pigment-coated papers have been used, virtually since the beginning of papermaking history, for their special properties of gloss and brightness. These properties, however, may render coated papers more susceptible to certain types of damage (surface marring, embedded grime, and stains) and more reactive to certain conservation treatments. Several research projects have been undertaken to characterize paper coating compositions (by SEM/EDS and FTIR) and appearance properties (by SEM imaging of surface structure and quantitative measurements of color and gloss) in order to evaluate changes that might occur following application of solvents used in conservation treatments.
    [Show full text]
  • Services.Pdf
    852 Derwent Way Delta, British Columbia, Canada V3M 5R1 T: 604.526.4221 TF: 800.463.5700 F: 604.526.1898 E: [email protected] W: econotech.com the measure of quality Our History Our Mission Since its inception in 1972, Econotech Services has been recognized as a leading laboratory in pulp and paper Although industrial and testing technology has evolved since our company was formed, our mission has testing services. Within our facility, located just outside of Vancouver, we can perform a full range of analytical tests remained consistent. For over 40 years, our mission has been to provide our clients with independent and timely testing results that meet stringent quality standards. from specialized chemical analysis of pulp (wood and non-woods), pulping liquors and other process chemicals (smelt, ash, condensates, lime), to physical and optical testing of pulp or paper, species analysis, contamination Values identification (scale and plastics), as well as pulping and bleaching studies. Integrity. In all our business activities, integrity is at the core. We are honest and ethical in our interactions with employees, clients and vendors. Our Reputation Reliability. We value long-term relationships that are built through trust. We consistently deliver on Accurate, rapid and reliable results performed by professionals with extensive experience in industry specific our commitments and our clients know they can rely on us. methodologies and matrices has been key to our growth and longevity. We have a reputation for producing high quality results for our clients. We have earned this reputation by: Customer Service Excellence. We take pride in the quality of work we produce and the service we provide.
    [Show full text]