Pulp & Paper Industry Solutions

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Pulp & Paper Industry Solutions Accurate and Reliable Liquid Analysis Papermaking Process Overview Papermaking is a highly sophisti - Although not present at all mills, yields or improve the properties of cated process involving several there are five major steps to the the pulp. processing steps to turn wood papermaking process: mechanical preparation of the wood into wood Pulp stock leaving the digester is a logs into paper products. In addi - chips, wood digestion (pulping) brownish liquid that is usually tion to the actual papermaking to form pulp, pulp whitening bleached to make more acceptable process, there are also (bleaching), pulp stock preparation, white paper. This process uses large supporting areas such as waste and finally paper formation. quantities of expensive bleaching water treatment, recovery boiler chemicals (usually ClO 2) and operation, steam production, The first of these steps uses strictly represents raw material and waste mechanical processes to form small disposal challenges. pH measure- and cooling towers that benefit chips from the logs supplied to the ment in this area optimizes the from on-line analytical mill. Byproducts such as bark and efficiency of the bleaching process, measurements. even some of the chips themselves lowering bleach consumption, are used as fuel to produce electricity discharge and associated costs. You need a partner that can and steam for mill use. Although deliver the best in knowledge some water may be used for lubrica - Prior to running in the paper and systems, and do it quickly, tion purposes, this is primarily a dry machine, different batches of pulp process and proceeds with a mini- may be blended to produce paper of thoroughly and cost-effectively. mum of process instrumentation. various required properties. Starches Emerson Process Management’s and retention aids are added to Rosemount Analytical brand of The pulping process has many varia - improve the wetting properties of 2 products provide measurements tions. Most common is chemical the paper. The pH measurement of pH, ORP, conductivity and dis - pulping using either caustic (Kraft standardizes this process, helping to solved oxygen that are specially sulfate process) or acidic (sulfite produce the same quality paper day process) chemicals. in and day out. designed for long life and reliable results in the demanding The chemicals are used and regener - The paper machine is usually consid - environment of the pulp mill. ated in a recovery process that ered the last place to get conditions These measurements provide reduces chemical costs and right for the final product. A reliable substantial control benefits that minimizes waste disposal costs. pH signal at this location can prevent can reduce costs with a typical Process conductivity measurements large runs of off spec product. These payback time of less than one optimize both the pulp yield and the locations can represent difficult recovery of chemicals in this stage. applications for sensors, but recent year. Read on and discover how Other pulping techniques such as advances in sensor technology have the liquid analysis professionals groundwood o r sem ichemical use vastly improved the performance from Emerson can help you pH measurements to optimize and reliability of online sensors. improve your bottom line. Wood logs are broken into chips about the size of a quarter. Logging Debarking Chipping Chip Bin Digester Mechanical Wood Processing EMERSON. CONSIDER IT SOLVED .™ Kraft Pulping Process Overview Digester Logs White Liquor Black Liquor Chipper Bleach Towers Chlorine Dioxide Tank Machine Chest White Water Chest Refiner Paper Products 3 Head Waste Treatment Plant Box Paper Machine On-line electrochemical measurements such pulp slurry from wood chips, involves as pH, electrical conductivity and dissolved strong chemicals that are typically CONTENTS oxygen provide real improvements in regenerated and reused. Dosage of these process control, quality, efficiency and prof - chemicals and control of the recovery Kraft Pulping 4 itability in Pulp and Paper operations. Mill process is monitored using electrical Bleaching and the Wet-End 5 effluent, especially from bleaching conductivity measurement. The pulp slurry operations, is increasingly the target of envi - is treated using bleach, sizing agents and Chemical Recovery 7 ronmental regulations such as the Cluster other furnish before being run in the paper Boiler and Rule and must be monitored closely. machine. These pulp additives can be very Steam Plant Operations 8 ineffective if the pH of the pulp slurry is not There are many different processes that can controlled. Common measurement Waste Treatment 9 be used to make paper and each process locations are bleach towers, machine Instrumentation 10 involves several steps. Chemical pulping, chest, headbox, and white water chest. the most common process of producing a Kraft Pulping Kraft pulping produces strong Measuring the alkali concentration Conductivity can be correlated to pulp but typically needs further entering into the digester allows the A and B tests since the active processing such as bleaching to fine control of the liquor flow rate NaOH has much higher conductivity to match the wood loading, than the product. As the cook provide acceptable brightness improving throughput and continues, conductivity steadily for average users. Cost effective - minimizing variability. decreases. Conductivity is best ness comes from reuse of the measured in the upper recirculation pulping chemicals in the Inside the digester, at temperatures zone for rapid response to process recovery process (see page 7). near 180°C and pressures around changes, but the high solids concen - Pulping is conducted in a 250 psig, the following reaction tration at this location tends to plug most conductivity sensors. digester and the process can be occurs: operated in either batch or Na 2S + NaOH + wood chips —> continuous mode. There are Na 2SO 4 + Na 2CO 3 + pulp many kinds of pulping processes, but generally the most cost As this reaction proceeds, the effective one is the chemical Kappa number decreases until the process called Kraft pulping. “cook” is completed in about 2 to 4 hours. Kappa Number is difficult to The Model 242 measure, so many mills monitor the Toroidal digester by measuring the Conductivity In the Kraft process, wood chips are concentration of chemicals in the Sensor is built for cooked in a strong alkali solution high solids and 4 cooking liquor using three chemical called white liquor. The white liquor aggressive chemical applications titrations called “ABC tests”. Results is basically a solution of sodium of the ABC tests are used to Process measurements in heavy slur - hydroxide and sodium sulfide with establish NaOH, Na S, and Na CO ries such as cooking liquor require an effective concentration of about 2 2 3 levels in the liquor. As the cook pro - robust flow-through sensors like the 100 grams per liter. Measuring gresses, NaOH is consumed and Model 242 Toroidal Conductivity white liquor alkali concentration Na CO is produced. When the Sensor. This sensor consists of a allows optimization of cooking time 2 3 NaOH level has dropped to the replaceable ceramic liner and and product pulp properties. Direct appropriate level, the cook is externally mounted toroid measure - measurement of the alkali complete and the product (called ment coils. The toroidal conductivity concentration is possible using auto - brownstock) is released from the method is resistant to the effects of matic titrators. However, due to the digester and further processed. This coating, and the Model 242’s exter - difficulty of extractive sampling technique still requires that nal mounting protects the toroids many mills opt to use electrical con - samples be extracted and from the high temperature and ductivity to provide real-time processed by a lab every 2-4 hours. pressures in the digester. The Model control feedback. 242 is recommended for lines up to The retractable Although the application inside the 4" in diameter. Model 228 Toroidal The clarified white liquor feed to the Conductivity Sensor digester is significantly different digester is the optimum location to White Liquor Conductivity allows safe, conven - from the application in base white install the retractable Model 228 500 ient cleaning. liquor, electrical conductivity Toroidal Conductivity Sensor. This 450 y measurement is valuable here also. t i v 400 sensor has a unique lead screw i t c design that allows for safe u 350 d n retraction at up to 295 psig o 300 C for cleaning purposes. 250 50 70 90 110 Effective Alkali Bleaching and the Wet-End Bleaching is the process of A typical bleach sequence consists of The bleaching chemicals are aggres - purifying and whitening pulp by a pair of bleaching stages each sive and incompatible with many chemical treatment. Several followed by an extraction stage. sensor materials. The 70°C temper- Chlorine dioxide bleaching allows ature accelerates the rate of stages are typically used to efficient bleaching at lower pH (3.5 chemical attack. generate pulp with the desired to 4) without degrading the brightness. To meet environmen - cellulose component of the pulp. Emerson’s TUpH ™ sensor technology tal regulations, nearly all pulp The extraction stages are conducted minimizes the effects of coating mills use elemental chlorine free at elevated pH (10-11) to maximize by using a patented composite junc - bleaching (i.e. chlorine dioxide). color removal. pH measurement is tion with
Recommended publications
  • Basics of Kraft Pulping

    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.
  • American Ft Forest & Paper 2QE5

    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

    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.
  • Paper Recycling Technology Detailed Part 1A

    Paper Recycling Technology Detailed Part 1A

    Paper Recycling Technology and Science Dr. Richard A. Venditti Paper Science and Engineering Forest Biomaterials Department North Carolina State University Lecture: Paper recycling and technology course introduction and objectives Dr. Richard Venditti Faculty member in the Paper Science and Engineering Program in the Forest Biomaterials Department at North Carolina State University PhD in Chemical Engineering, BS in Pulp and Paper Science and Chemical Engineering Research areas: � Paper recycling � Utilization of forest/agricultural materials for new applications � Life cycle analysis Named a TAPPI Fellow in 2012 Relevant research projects: – The detection of adhesive contaminants – The changes in fibers upon recycling – Automatic sorting of recovered papers – Flotation deinking surfactants – Agglomeration deinking – Screening phenomena and pressure sensitive adhesives – Deposition of adhesive contaminants – Neural networks to control deinking operations – Sludge conversion to bio-ethanol and to bio- materials Course Outline The US Paper Recycling Industry Recovered Paper Grades and Contaminants Effect of Recycling on Fibers/Paper Unit Operations � Pulping, Cleaning, Screening, Washing, Flotation, Dispersion, Bleaching, ….. Image Analysis, Deinking Chemicals System Design Advanced/Additional Topics Course Activities Viewing of the Videos of Lectures � Base lectures by Venditti � Guest lectures from industry leaders Homework assignments Final Exam Critical Issues in Recycling: Going deeper into the recovered paper stream
  • Alkaline Pulping: Deadload Reduction Studies in Chemical Recovery System

    Alkaline Pulping: Deadload Reduction Studies in Chemical Recovery System

    ALKALINE PULPING: DEADLOAD REDUCTION STUDIES IN CHEMICAL RECOVERY SYSTEM A Thesis Presented To The Academic Faculty By Yusup Chandra In Partial Fulfillments Of the Requirements for the Degree Master of Science in Paper Science Engineering School of Chemical & Biomolecular Engineering Georgia Institute of Technology November 8th, 2004 ALKALINE PULPING: DEADLOAD REDUCTION STUDIES IN CHEMICAL RECOVERY SYSTEM Approved by: Dr. Howard (Jeff) Empie, Advisor Dr. Yulin Deng Dr. Sujit Banerjee Date Approved: November 8th, 2004 ACKNOWLEDGMENT I would like to dedicate this thesis first and foremost to my parents, Azis and Rienni, who have given me all the love and support the years. I would like to thank IPST for this great opportunity to attend this Georgia Tech and to meet all of the wonderful people here. Dr. Empie thanks for introducing me to this new thesis topic and doing a great job. I know it has been difficult through this period of time, but we got through it. Dr. Banerjee and Dr. Deng thank you for taking the time out of your busy schedules. I appreciate all the assistance and advice I have received from everyone on the committee. Lastly, I would like to thank the people that made my stay here in Atlanta an exciting and memorable experience. Special thanks to Luis, Sheila, Daniel, Jacobo, Josh, and Trevor who made getting through the toughest times so much easier. iii TABLE OF CONTENTS Acknowledgment iii Table of Contents iv List of Tables vi List of Figures vii Summary viii Chapter 1 Introduction 1 1.1. Terms and Definitions 2 1.2.
  • Construction Health and Safety Manual: Pulp and Paper Mills

    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.
  • Fibre to Board

    Fibre to Board

    Fibre to board Fibre to board Today’s processes of separating fibre and making paper- compost and road-building material. Using the entire tree board take place in facilities characterised by capital is an important part of our ambition to carry out sustain- intensity, high production volumes and the application of able production. the latest techniques of materials handling, continuous production and process control. From timber to fibre – the pulping process In many cases, including the mills of Iggesund Paper- The timber logs which are delivered to the pulp mill are first board, the production of pulp and the manufacture of debarked, since bark does not contain fibre suitable for paperboard are carried out on the same site in a continu- pulp manufacture. Bark is removed by friction, as logs are ous integrated process, giving benefits in quality, efficiency tumbled together in a rotating drum. The bark is then used and economy. as a fuel within the mill or composted to create garden soil. Managed forests provide the primary source of cellulose The next process depends on the type of separation or fibre from wood varieties such as spruce, pine and birch. defibration process used. The fibre is separated by mechanical or chemical pulp- ing and the whiteness and purity may subsequently be Pulp manufacture improved by bleaching. Basically the choice is between long fibres (spruce and Processing on the paperboard machine starts with the pine) and short fibres (birch). The boardmaker optimises formation of a layer of entangled fibres on a moving wire sheet forming, appearance and performance properties or plastic mesh from which water is removed by drainage.
  • Flow Sheet Pulp and Paper Green Liquor / White Liquor Circuit

    Flow Sheet Pulp and Paper Green Liquor / White Liquor Circuit

    WesTech’s Continuous Rotary Drum Filters provide a wide range of liquid-solids separation for many types of industrial processing flow sheets. They offer the operating flexibility to handle dewatering, washing, and filtration applications. Working with the customer, WesTech provides laboratory test data to assess process optimization, design, and sizing of the equipment supplied. WesTech Drum Filters are available up to 13.5 feet in diameter and 36 feet in length and are built for ease of operation as well as to meet demanding customer specifications. Pulp and Paper Dregs The most common process for making paper is called The dregs from the green liquor clarifier are sent to the Kraft or Kraft Mill process. In this process, wood a rotary vacuum filter called the “dregs filter.” Here chips are “cooked” at 150 - 165o C, under pressure the dregs are washed to remove residual chemicals in a liquid solution containing caustic (NaOH) and and are dewatered prior to disposal. The liquids are sodium sulphide (Na2S) to pulp the wood. recycled to the green liquor stabilization tank. White Liquor Slaker The solution of caustic and sodium sulfide is The clarified green liquor is fed to a “slaker” where referred to as “white liquor”. These chemicals, along NaOH is formed. The grit and unreacted lime settle with heat and pressure, release the lignin from the to the bottom where they are removed by means of fibers in the wood. The resulting “pulp” is washed, a screw conveyor. screened, and sent on to bleaching and becomes the feed stock for the paper-making process.
  • Resin Profile in a Bleached Kraft Pulp Process

    Resin Profile in a Bleached Kraft Pulp Process

    Resin Profile in a Bleached Kraft Pulp Process Jennie Berglund May 2012 Degree Project in Polymeric Materials, First Level Department of Fibre and Polymer Technology Royal Institute of Technology Stockholm, Sweden Abstract The aim with this project was to investigate how the amount and composition of resins varied during the process producing bleached birch pulp at the mill SCA Packaging Munksund. A literature study about how the resin removal can be improved has also been included. Problems with resins in the process are common at pulp and paper mills, especially when birch is used as a raw material. The resin can cause deposits on the equipment leading to process stops, but also lowered mechanical properties and spots on the paper products. The addition of tall oil to the digester is one way of improving the removal of resins, seasoning of wood, and a good debarking are other ones. Also the different washing and bleaching steps can affect the amount of resin remaining in the pulp. In this study pulp samples from eight different positions in the process were analyzed. To extract the samples a Soxtec device was used. Results showed that the most effective resin removal happened during the washing in their first washing step after the digester, a DD-washer. Here 77 % of the resin was removed, of totally 88 % during the whole process. Another step which was effective was the final washing step, the PO-press. About 36 % of the remaining resins in the pulp which entered the PO-press were washed out here. The extracts were analyzed with GC-FID and GC-MS to identify and quantify the substances, and determine how the composition varied over the manufacturing process.
  • GPI West Monroe Digester Optimization Project Valmet Inc

    GPI West Monroe Digester Optimization Project Valmet Inc

    Kari Lampela, Solution Manager, Valmet Danny Zuver, APC Engineer, Valmet Dennis Carwile, Sr. Manager-Manufacturing Services/Pulp Leader, Graphic Packaging GPI West Monroe digester optimization project Valmet Inc. and Graphic Packaging Intl. (GPI) collaborated on continuous digester optimization projects that included three digesters in West Monroe, Louisiana. Graphic Packaging is one of the world’s largest manufacturers of folding cartons, unbleached paperboard, coated recycled board, microwave packaging and machinery. The West Monroe facility manufactures combined folding carton for use in beverage and other product packaging. Kraft pulp digester operation plays a critical role in the whole pulp mill economy. Furthermore, high and steady pulp quality results in additional bottom line profits for the paper mill. The key to pulp production and quality optimization is to ensure selective delignification, which can be accomplished by precise and strategic management and control of optimum cooking conditions. Accurate and reliable pulp quality measurements are essential elements of an advanced control package. Continuous cooking alkali profile management has become an increasingly important factor to maintain quality targets. Information about the cooking liquor composition within the process can be utilized to determine the alkali profile in the digester and to optimize the addition of cooking chemicals into the process. Cooking liquor measurements give indirect information about the extent of the cooking degree. Typical variation of the white liquor strength is generally 5 %, or greater after production breaks. If this variation is not measured and controlled, it will have a significant effect on cooking conditions and pulp quality. Kappa and residual alkali measurements provide an accurate estimate of pulp yield and with enhanced control of delignification and alkali profile, the mill can increase pulp yield while maintaining steady blow Kappa level.
  • Crude Tall Oil Low ILUC Risk Assessment Comparing Global Supply and Demand

    Crude Tall Oil Low ILUC Risk Assessment Comparing Global Supply and Demand

    Crude tall oil low ILUC risk assessment Comparing global supply and demand Crude tall oil low ILUC risk assessment Comparing global supply and demand By: Daan Peters, Viktorija Stojcheva Date: 24 April 2017 Project number: SISNL17494 © Ecofys 2017 by order of: UPM ECOFYS Netherlands B.V. | Kanaalweg 15G | 3526 KL Utrecht| T +31 (0)30 662-3300 | F +31 (0)30 662-3301 | E [email protected] | I www.ecofys.com Chamber of Commerce 30161191 Executive Summary UPM produces renewable diesel and naphtha from crude tall oil (CTO) in its biorefinery in Lappeenranta, Finland from early 2015 onwards. Because the company wanted clarity on the status and sustainability of its feedstock, UPM asked Ecofys in 2013 to assess whether CTO can be regarded as a residue and whether the feedstock would be low ILUC risk, meaning its use for biofuels would not lead to displace- ment effects of existing other uses. The current report is an updated version of the 2013 report. An important change since the previous report is that biofuel production at UPM has started, so any effects of CTO usage for biofuels has on the CTO market would be visible. Ecofys studies the following questions in this report: 1. Can CTO be defined as a residue based on biofuel legislation 2. Does the feedstock create an additional demand for land (is it a low ILUC risk feed stock?) 3. Does the use of the feedstock for biofuel production cause significant distortive effects on markets? The second and third question are closely interlinked. CTO in itself is a non-land using feedstock.
  • Conductivity Measurements for Kraft Pulping Application Note

    Conductivity Measurements for Kraft Pulping Application Note

    Conductivity Measurements for Kraft Pulping Application Note Industry: Pulp & Paper Products: Inductive Conductivity Process Liquid Analyzer Introduction Measuring conductivity in the recirculation zone of The kraft process, also known as kraft pulping or a continuous digester provides feedback to the the sulfate process, is a technology for conversion control system to reduce the variability in the of wood into wood pulp that consists of almost Kappa number of the product pulp. This enables pure cellulose fibers. Today, the kraft process is more efficient chemical use and higher quality used in approximately 80% of paper production. pulp In the process, wood chips are digested at elevated Process pressure and temperature by harsh chemicals known as “white liquor." White liquor is a water The kraft process is cyclical and self-sustaining. solution of sodium sulfide and sodium hydroxide. Wood chips are fed into a digester where they The lignin that binds the cellulose fibers together react with the cooking liquors, a combination of in the wood is chemically dissolved by the white white liquor and black liquor. Black liquor is a liquor. byproduct of the process within the digester. It is the spent cooking liquor that is a combination of The industry uses the Kappa number to estimate the removed lignin, water, and chemicals used in the amount of bleaching chemical, a potassium the extraction process. The inorganic portion of permanganate solution, that is required to extract the black liquor, white liquor, is the regenerated the lignin and obtain a pulp with the desired mixture of sodium hydroxide and sodium sulfide degree of brightness.