Water Reuse in Paper Mills Measurements and Control Problems in Biological Treatment Tomas Alexandersson Licentiate Thesis Department of Industrial Electrical Engineering and Automation Department of Industrial Electrical Engineering and Automation Lund University Box 118 SE-221 00 Lund Sweden http://www.iea.lth.se ISBN 91-88934-28-4 CODEN:LUTEDX/(TEIE-1036)/1-138/(2003) 2003 Tomas Alexandersson Printed in Sweden by Media-Tryck, Lund University Lund 2003 ii Abstract Paper manufacturing is a complex and multidisciplinary science due to the diversity of paper products, used raw materials and different production processes. Besides fibres different chemicals, water and energy are needed to produce paper. The use of fresh water has decreased significantly during the last decades and there are several reasons for this, such as: limited availability of fresh water, increased cost for effluent treatment and marketing benefits. This decreased consumption has been made possible by the reuse of process water instead of fresh water. However, at a certain degree of closure different problems occur. Many of them are in some way related to the growth of microorganisms in the system. One method to solve the problems is to implement an internal kidney consisting of at least a biological treatment step. Since nutrients, such as nitrogen and phosphorous, normally are limited in the whitewater these have to be added in order to have an efficient biological treatment process. One major challenge is to operate the biological system with low concentrations of nutrients in the effluent otherwise the conditions in the whitewater system will be negatively affected. Consequently, there is a need for automatic control of the nutrient addition. It is possible to control the flow of whitewater to the treatment process but not the actual concentrations of organic compounds in the whitewater, which therefore can be regarded as a process disturbance. An investigation was made at two different paper mills with different degrees of closure to determine the variation of chemical oxygen demand (COD) in the whitewater. The results showed that the whitewater concentration in an open mill could vary a lot whereas the conditions were more stable in a closed mill. For the control there is a need for information about the process state and output from the system. In this case, for controlling a biological treatment of whitewater, different on-line instruments are needed. First of all, a market survey, limited to instruments for measurements of organic matter, iii ammonium and orthophosphate, was conducted. The experiences gathered about use of on-line instruments at several of the Swedish municipal treatments plants were explored in a telephone survey. One interesting observation was that most on-line instruments were only used for monitoring. The number of instruments used for direct control was low but this number was increasing as new and better instruments are becoming available. As a conclusion of these two surveys, three different brands of instruments were deemed suitable for measurements in whitewater. Computer simulation is an important tool for evaluation of different controllers but requires a mathematical model of the system. Laboratory experiments were initiated to determine important parameters for such a model. Both mesophilic and thermophilic treatment of recycled fibre whitewater with a fluidised anaerobic reactor and an aerobic suspended biofilm process resulted in high removal of COD of around 90%. The nutrient requirement for the anaerobic mesophilic reactor was determined to 19 mg N/g COD and 2.5 mg P/g COD . For thermophilic reduced reduced degradation the requirement was determined to 24.5 mg N/g COD and reduced 4.4 mg P/g COD for the anaerobic process and the corresponding reduced values for the aerobic process were 37.1 mg N/g COD and 5.5 mg P/g reduced COD . A decrease of the added amount of nitrogen to 77% of what was reduced originally consumed did not have any immediate effect on the COD reduction. Pilot tests with the purpose to study both the stability of a biological treatment process and evaluate two different on-line instruments were conducted at a packaging board mill. The results demonstrated that the removal efficiency was not markedly affected from variations of the load to the combined anaerobic/aerobic treatment process and that both instruments failed to provide stable results. Experiences from other instruments have been gathered during the assembly of a complete system consisting of a pilot plant of a biological treatment process, on-line instruments and data-acquisition equipment. It has been demonstrated that it is possible to use on-line instruments for measurements in whitewater to acquire information about the biological treatment process. This information could be used in several different ways for the control of the addition of nutrients. Different control structures are suggested ranging from feed forward of the organic load with corrective feedback of concentrations in the anaerobic effluent to more complex model- based control structures with automatic update of model parameters. iv Acknowledgements I would like to first express my gratitude towards Dr. Thomas Welander who gave me the opportunity to continue my education. He performed an inhuman effort when he, in a very short time, wrote the major part of the project application for the ClosedCycle project, which I have been working on. The ClosedCycle project is financially supported by the European Commission, which is gratefully acknowledged. I am also very grateful for the support and encouragement throughout my project from my supervisor Prof. Gustaf Olsson and co-supervisor Assoc. Prof. Ulf Jeppsson. On numerous occasions I was very frustrated and felt rather lost. The feeling I had was the same feeling you would have if you were asked to put together a bicycle and your starting materials were some seeds for a rubber tree and pieces of iron ore. Although both of my supervisors are usually very busy people, they always had time to discuss the rubber tree and the iron ore and so with their help I managed to create the bicycle in the end. As a graduate student I had the privilege of attending various courses and met a lot of nice fellow Ph.D. students, such as the people from the department of Water and Environmental Engineering. Special thanks go to Michael Ljunggren, who provided me with pictures and practical information about some of the processes used in wastewater treatment. Michael also shared my interest for training and so during breaks there was always some stimulating discussion about strength training, pulse intervals, nutrition or something else in this area. Michael and I still do not understand why the others always started to shake their heads and looked so strangely at us when we started in on these discussions and distractions. My own department is filled with nice people. You have all made me feel welcomed although, as a chemical engineer, I was a long way from home (KC). Thanks for the stimulating atmosphere all of you created together. I v would especially like to mention Carina Lindström who provided delicious morning coffee or tea and Getachew Darge who assisted me with his technical knowledge. It is easy to take your services for granted and not appear to give them enough show of appreciation during hectic times. Thank you. A lot of people both at Anox AB and Cenox helped me in various ways. Dr. Anders Ternström and Dr. Alan Werker proof read parts of my manuscript, Åsa Malmqvist always had time for creative discussions, and Stig Stork made those very tedious runs for new batches of whitewater. I was encouraged by everyone's anticipation of when I was going to come back to Anox AB. Hopefully, I interpreted the concern in the right way and was missed; it could be that you just wanted to figure out how many happy days you had left. I am very grateful to Prof. Erik Dahlquist who took the time to read my thesis and travelled to Lund to discuss the work with me during my licentiate seminar. Finally, my thoughts turn to my room-mate at IEA, Sabine Marksell, who has become very dear to me and a part of my life. Thanks Sabine for always encouraging me and boosting my self-confidence. Lund, July 09, 2003 Tomas Alexandersson vi Contents CHAPTER 1 INTRODUCTION .......................................................1 1.1 PROBLEM DEFINITION....................................................................1 The project................................................................................................2 Other projects............................................................................................2 Challenges.................................................................................................3 1.2 OVERVIEW......................................................................................3 1.3 MAIN RESULTS................................................................................4 CHAPTER 2 PROCESSES INVOLVED..............................................7 2.1 PAPER..............................................................................................8 History of paper.........................................................................................8 Paper products...........................................................................................8 Paper production.......................................................................................9 2.2 PULPING..........................................................................................9 Raw material............................................................................................9 Mechanical pulping.................................................................................11 Chemical pulping....................................................................................11 Bleaching................................................................................................12 2.3 PAPER MAKING..............................................................................13 The paper machine..................................................................................13 The whitewater system.............................................................................14 Composition of the whitewater.................................................................15 Mass balances in the whitewater system....................................................17 vii 2.4 VARIATIONS IN THE WHITEWATER..............................................17 Mill no. 1...............................................................................................18 Mill no. 2...............................................................................................19 Sampling and storage..............................................................................19 Production disturbances...........................................................................20 Analyses..................................................................................................20 Results.....................................................................................................20 2.5 WASTEWATER TREATMENT (WWT)...........................................23 Introduction............................................................................................23 Internal versus external WWT.................................................................24 Wastewater composition..........................................................................24 2.6 MECHANICAL/PHYSICAL/CHEMICAL METHODS..........................25 Settling...................................................................................................25 Flotation.................................................................................................27 Sand filtration........................................................................................29 Membrane filtration................................................................................29 Chemical treatment.................................................................................29 Ozonation...............................................................................................30 2.7 BIOLOGICAL DEGRADATION........................................................31 Different energy and carbon strategies......................................................31 Microorganisms.......................................................................................32 Environmental demands..........................................................................33 Nutrient requirements.............................................................................34 2.8 AEROBIC BIOLOGICAL WWT.......................................................35 Activated sludge......................................................................................36 Biofilm...................................................................................................37 2.9 ANAEROBIC TREATMENT.............................................................38 viii CHAPTER 3 ON-LINE ANALYSERS...............................................41 3.1 INTRODUCTION...........................................................................41 3.2 MEASUREMENT PRINCIPLES.........................................................43 Organic compounds.................................................................................43 Ammonia................................................................................................44 Phosphate................................................................................................45 3.3 MARKET SURVEY...........................................................................46 Information sources.................................................................................47 Discussion...............................................................................................52 3.4 EXPERIENCES................................................................................53 Introduction............................................................................................53 Telephone survey.....................................................................................54 WWT plants...........................................................................................55 On-line instruments................................................................................55 Service and calibration............................................................................57 Discussion...............................................................................................57 3.5 CONCLUSIONS..............................................................................58 CHAPTER 4 CLOSURE OF PAPER MILLS......................................61 4.1 WATER USAGE...............................................................................61 4.2 BENEFITS.......................................................................................62 4.3 PROBLEMS.....................................................................................63 Microbial growth....................................................................................64 Corrosion................................................................................................64 Explosions...............................................................................................65 Interfering substances...............................................................................65 4.4 QUALITY RELATIONSHIPS.............................................................66 4.5 SOLUTIONS AND EXPERIENCES....................................................67 ix Biocides...................................................................................................67 Advanced water recycling.........................................................................68 Evaporation............................................................................................68 Fixing agents...........................................................................................69 Enzymes..................................................................................................69 Membrane filtration................................................................................69 Sand filtration........................................................................................70 Cost for water re-use................................................................................70 4.6 CONCLUSIONS..............................................................................72 CHAPTER 5 THE INTERNAL KIDNEY..........................................75 5.1 THE INTERNAL KIDNEY................................................................75 5.2 MOTIVATION FOR SELECTION OF PROCESS................................77 5.3 THE PROCESS................................................................................79 Biological process.....................................................................................79 Separation process....................................................................................81 Additional treatment process....................................................................81 5.4 IMPORTANT DESIGN AND OPERATIONAL PARAMETERS..............82 5.5 EXPERIMENTAL EXPERIENCES......................................................84 Biological process in lab scale...................................................................85 Pilot test and on-line instruments.............................................................89 Other experiences.....................................................................................91 5.6 INDUSTRIAL EXPERIENCES............................................................94 Zülpich Papier........................................................................................94 Westfield mill..........................................................................................94 Gissler & Pass paper mill.........................................................................95 Hennepin Paper Co.................................................................................95 AssiDoman Lecoursonnois........................................................................95 x