Extended Impregnation Kraft Cooking of Softwood: Effects on Reject, Yield, Pulping Uniformity, and Physical Properties
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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. -
A Review on the Modeling, Control and Diagnostics of Continuous Pulp Digesters
processes Review A Review on the Modeling, Control and Diagnostics of Continuous Pulp Digesters Moksadur Rahman * , Anders Avelin and Konstantinos Kyprianidis School of Business, Society and Engineering, Mälardalen University, Box 883, 72123 Västerås, Sweden; [email protected] (A.V.); [email protected] (K.K.) * Correspondence: [email protected]; Tel.: +46-(0)21-10-1594 Received: 12 August 2020; Accepted: 23 September 2020; Published: 1 October 2020 Abstract: Being at the heart of modern pulp mills, continuous pulp digesters have attracted much attention from the research community. In this article, a comprehensive review in the area of modeling, control and diagnostics of continuous pulp digesters is conducted. The evolution of research focus within these areas is followed and discussed. Particular effort has been devoted to identifying the state-of-the-art and the research gap in a summarized way. Finally, the current and future research directions in the areas have been analyzed and discussed. To date, digester modeling following the Purdue approach, Kappa number control using model predictive controllers and health index-based diagnostic approaches by utilizing different statistical methods have dominated the field. While the rising research interest within the field is evident, we anticipate further developments in advanced sensors and integration of these sensors for improving model prediction and controller performance; and the exploration of different AI-based approaches will be at the core of future research. Keywords: Kraft pulping; pulp digester; modeling; control; diagnostics 1. Introduction With the widespread expansion of the Internet, electronic media and paperless communication, the demand for the graphic paper (i.e., newsprint and higher-value printing and writing paper) has been declining since 2000 [1]. -
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. -
Deinking of Screen-Printed Electrodes Printed on Invasive Plant-Based Paper
sustainability Article Article DeinkingDeinking of of Screen-Printed Screen-Printed Electrodes Printed on InvasiveInvasive Plant-Based Plant-Based Paper UrškaUrška Kav Kavˇciˇc*čič *, Igor, Igor Karlovits Karlovits and and Janja Janja Zule Zule PulpPulp and and Paper Paper Institute, Institute, Bogiši Bogiši´ceva8,ćeva 8, 1000 Ljubljana, Slov Slovenia;enia; igor.karlovits@icp-lj. [email protected] (I.K.); janja.zule@icp- [email protected] (J.Z.) (J.Z.) * Correspondence: [email protected] Received: 21 January 2020; Accepted: 6 February 2020; Published: date Received: 21 January 2020; Accepted: 9 February 2020; Published: 12 February 2020 Abstract: The deinking of paper-based printed electronics is a growing concern regarding the Abstract: The deinking of paper-based printed electronics is a growing concern regarding the increase increase of printed electronics products. The benefits of using paper-based substrates instead of of printed electronics products. The benefits of using paper-based substrates instead of polymer polymer or ceramic for the single-use printed electrodes can contribute to sustainability goals. The or ceramic for the single-use printed electrodes can contribute to sustainability goals. The use of use of invasive plant species for making paper substrates for printed electronics is a unique invasive plant species for making paper substrates for printed electronics is a unique opportunity opportunity to have several environmental benefits. In this study, the recycling issue of these to have several environmental benefits. In this study, the recycling issue of these products through products through the use of the deinking technique was evaluated. Screen-printed electrodes the use of the deinking technique was evaluated. -
Importance of Unbleached Pulp Lignin Content
ENVIRONMENTAL FOOTPRINT COMPARISON TOOL A tool for understanding environmental decisions related to the pulp and paper industry EFFECTS OF DECREASED RELEASE OF CHLORINATED COMPOUNDS ON ENERGY USE Importance of Unbleached Pulp Lignin Content Kappa number is a measure of the amount of lignin remaining in pulp. The higher the kappa number value, the higher the use of bleaching chemicals required to brighten the pulp. The kappa numbers of pulps leaving the digester are typically about 30 for softwoods and 20 for hardwoods in bleached kraft mills that employ conventional cooking methods. Several modifications to conventional cooking, known collectively as extended cooking (EC), have enabled kappa numbers to be further reduced in the digester in ways that minimize yield and strength losses. Kappa numbers associated with EC are about 20 for softwoods and about 14 for hardwoods. Oxygen delignification (OD) is another technology that is used extensively to lower the residual lignin content prior to the bleach plant. The technology is more selective than most extended cooking processes. Lignin reductions of approximately 50% are achievable with OD, resulting in softwood kappa number in the 14-18 range. Some mills use both extended cooking and oxygen delignification to achieve very low kappa number pulps prior to bleaching, producing pulps with kappa number values in the range of 10-12, perhaps even lower. Deterioration of pulp strength properties is the limiting obstacle for kappa number reduction prior to the bleach plant. More recent strategies have been focused away from obtaining the most delignification possible in the digester and toward optimizing the fiberline as a whole based on economic, quality, and environmental factors. -
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. -
Construction Health and Safety Manual: Pulp and Paper Mills
PULP AND PAPER MILLS 33 PULP AND PAPER MILLS The two common forms of chemical pulping are 1) the dominant “alkaline” or “kraft” process, and Processes 2) the “acid pulping” or “sulphite” process. Acid pulping has generally declined but is still in use. The A number of processes, grouped by type as mechanical, digester liquor is a solution of sulphurous acid, H SO , chemical, and semi-chemical (or hybrid), are used in 2 3 mixed with lime (CaO) or other base (magnesium, the preparation of wood pulp. In 1990 (according to sodium, or ammonium) to form bisulphites. Lockwood’s Directory) the distribution of pulp mills in Ontario and Quebec was as follows: Mechanical processes produce the highest yield from the wood, but have high energy demands. Mechanical pulping Process Type generally incorporates thermal or chemical pre-softening Chemical Processes Semi-chemical Mechanical Total of the wood chips, resulting in lower energy requirements. Kraft Sulphite Some chemical processes include mechanical features. Ontario 94 2 15 30 The division is not distinct and is generally based on Quebec 10 8241 61 efficiency of production from dry wood. Figure 22.1: Number of pulp mills by type in Ontario and Quebec Figure 22.2 provides a flow diagram for a semi-chemical pulp mill. In chemical pulping, the wood chips are cooked, using heat and a chemical solution that depends on the type of Of the chemical processes , alkaline pulping – the kraft process being used. The lignin binder, a natural glue that or sulphite process – is the most common and is shown in holds the wood cells (fibres) together, is dissolved. -
Sorption and Desorption of Black Liquor Xylan Onto Cellulose Fibers – a New Separation Technique
CELLULOSE CHEMISTRY AND TECHNOLOGY SORPTION AND DESORPTION OF BLACK LIQUOR XYLAN ONTO CELLULOSE FIBERS – A NEW SEPARATION TECHNIQUE SVERKER DANIELSSON Innventia AB, Stockholm, Sweden ✉Corresponding author: [email protected] The potential of xylan as a polymer in different new materials is large and not yet utilized. The availability in kraft pulp mills is large as the polymeric xylan dissolved in process liquors corresponds to up to 160 kg/adt and is today burnt to recover energy. A pre-requisite for using black liquor xylan in high-value products is to purify it from inorganic material and lignin in a technically effective and economical feasible way. This study combines two known properties of xylan: its affinity to cellulose and its solubility in alkali. The aim is to design an efficient separation process to produce black liquor xylan of high purity. A very pure xylan was reached with as low lignin contents as 1%. The hydroxide ion concentration was varied in the sorption step and it was found that an increase in hydroxide ion concentration resulted in a decreased amount of isolated xylan, decreased degree of substitution of uronic acids, but no effect on the lignin content and ash content was seen. Keywords : hardwood xylan, kraft pulping, separation, purification, precipitation, 4-O-methylglucuronic acid, hexenuronic acid, black liquor INTRODUCTION In the kraft pulping process, large amounts of tion from black liquor. The separation technique xylan are dissolved in the cooking liquor and end used in this study combines two well-known up as heat in the recovery boiler. The liquor is an phenomena of dissolved xylan in alkali: the attractive source for xylan production as the tendency of attaching to cellulose fibres 4-7 and the availability is high and the heat value for xylan possibility of dissolving xylan in alkali. -
Effect of Different Locations on the Morphological, Chemical, Pulping and Papermaking Properties of Trema Orientalis (Nalita)
Bioresource Technology 101 (2010) 1892–1898 Contents lists available at ScienceDirect Bioresource Technology journal homepage: www.elsevier.com/locate/biortech Effect of different locations on the morphological, chemical, pulping and papermaking properties of Trema orientalis (Nalita) M. Sarwar Jahan a,b,*, Nasima Chowdhury a, Yonghao Ni b a Pulp and Paper Research Division, BCSIR Laboratories, Dr. Qudrat-E-Khuda Road, Dhaka 1205, Bangladesh b Pulp and Paper Research Centre, University of New Brunswick, Fredericton, Canada article info abstract Article history: The chemical compositions and fiber morphology of stem and branch samples from Trema orientalis at Received 24 August 2009 three different sites planted in Bangladesh were determined and their pulping, bleaching and the result- Received in revised form 1 October 2009 ing pulp properties were investigated. A large difference between the stem and branch samples was Accepted 13 October 2009 observed. The stem samples have consistently higher a-cellulose and lower lignin content, and longer Available online 14 November 2009 fibers than the branch samples in all sites. T. orientalis from the Dhaka and Rajbari region had higher a-cellulose content and longer fiber length, resulting in higher pulp yield and better papermaking prop- Keyword: erties. The T. orientalis pulp from Rajbari region also showed the best bleachability. Trema orientalis, Variation of wood Ó 2009 Elsevier Ltd. All rights reserved. properties Stem and branch Pulping and bleaching 1. Introduction sely to those of Malaysian-grown mangium and other fast-grow- ing plantation species, including the traditionally-used pulpwood The increased demand for wood and fiber and declining avail- of the Philippines. -
Single Fiber Lignin Distributions Based on the Density Gradient Column Method
Single Fiber Lignin Distributions Based on the Density Gradient Column Method Brian Boyer Patent Attorney 3676 Highland Avenue Redwood City, CA 94062 [email protected] Alan Rudie USDA Forest Service, Forest Products Laboratory One Gifford Pinchot Drive Madison, WI 53726 [email protected] ABSTRACT The density gradient column method was used to determine the effects of uniform and non-uniform pulping processes on variation in individual fiber lignin concentrations of the resulting pulps. A density gradient column uses solvents of different densities and a mixing process to produce a column of liquid with a smooth transition from higher density at the bottom to lower density at the top. Properly prepared pulp fibers float in the column, stabilizing at the level where the mixed solvent density equals the density of the fiber. Because lignin is the lowest density component of pulp fibers and has the largest influence on fiber density, the column effectively separates fibers by lignin concentration and allows them to be counted and the distribution of lignin concentrations determined. Ten experimental kraft pulps and three commercial pulps were evaluated. The laboratory pulps were produced from a single loblolly pine tree using 2.5-mm and 10-mm chips. All cooks used a 24% effective alkali (EA) charge on wood, 6-to-1 liquor-to-wood ratio, and 30% sulfidity. The cooking schedule was constant at 60 min rise to temperature and 240 min at temperature. The maximum cooking temperature was varied from 150°C to 170°C to provide a kappa number variation from about 60 to approximately 20. -
Energy Generation and Use in the Kraft Pulp Industry
ENERGY GENERAnON AND USE IN THE KRAFT PULP INDUSTRY Alex Orr, H.A.Simoos Ltd INTRODUCTION The pulp and paper industry is one of the largest users of energy among the process industries, but most of its requirements, both steam and electrical power, can be produced from by-product and waste material produced within the process. This paper will discuss energy utilisation and generation in kraft pulp mills, and briefly describe the basic kraft pulping process. THE KRAFT PROCESS The kraft process is the most widely used chemical pulping process for a number of reasons: it produces the strongest pulp; it can handle a wide range of furnish: softwood, hardwood, bagasse and bamboo; the cooking chemicals can be recovered economically; it is energy efficient Figure 1 shows a simplified schematic of a kraft mill. The wood furnish supplied to the mill can be in the form of logs (roundwood) or by-product chips from sawmills.. The source of the wood supply has a significant affect on the energy production.. Ifroundwood is chipped the waste wood produced per ton ofchips will be around 200 kg, but when sawmill by-product chips are used the waste wood produced in the sawmill will be in the range of 450 kg/ton chips, as most of the log goes to produce lumbero This waste wood may be available to the pulp mill at a low cost, or even negative cost, allowing the production of low cost steam and electrical power" The chips are mixed with white liquor (NaOH and N~S) and cooked, using steam, in a large pressure vessel called a digester, either in a continuous or batch process. -
Optimization of Ecf Bleaching and Refining of Kraft Pulping from Olive Tree Pruning
PEER-REVIEWED ARTICLE bioresources.com OPTIMIZATION OF ECF BLEACHING AND REFINING OF KRAFT PULPING FROM OLIVE TREE PRUNING Ana Requejo,a,* Alejandro Rodríguez,a Jorge L. Colodette,b José L. Gomide,b and Luis Jiménez a The aim of the present work was to find an optimum kraft pulping process for olive tree pruning (OTP) in order to produce a bleachable grade pulp of Kappa number about 17. The kraft pulp produced under optimized conditions showed a viscosity of 31.5 mPa.s and good physical, mechanical, and optical properties, which are acceptable for paper grade production. The strength and optical properties were measured on pulps unrefined and refined in a PFI mill with up to 2000 revolutions before and after bleaching. The OTP pulp was bleached to 90% ISO brightness (kappa < 1); however the process demanded a long sequence of stages, OD(EP)D(EP)D, and a higher than usual total chemical dosage (24.78 kg/odt pulp). Overall, OTP is suggested as an interesting raw material for cellulosic pulp production because its properties are comparable to those of other agricultural residues currently used in the paper industry. Keywords: Kraft pulping; Olea europaea; Agricultural wastes; Refining, ECF bleaching Contact information: a: Chemical Engineering Department, Campus de Rabanales, Building Marie Curie (C-3), University of Córdoba, 14071, Córdoba, Spain; b: Laboratory of pulp and paper, Department of Forest Engineering, Federal University of Viçosa, Campus UFV, 36570, MG, Brazil. * Corresponding author: [email protected] INTRODUCTION Pulp production in Europe amounts to 36.9 million tons per year, which represents 21.6% of the world’s production; the production of paper and cardboard accounts for 25.3% of the total with 88.7 million tons.