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Material Type: Project; Class: PULPING/BLEACHING; Subject: Paper Science and Engineering; University: University of Washington - Seattle; Term: Spring 2007;
Typology: Study Guides, Projects, Research
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Modeling project Rough Draft Due: 2 March 2007 Final Report Due: 9 March 2007 For this project you will work in teams of three or four. Each of you will use the model to carry out one of the studies listed below then pull your results together for the final report. I am looking for a thorough analysis of each of the problems given below. These are open-ended problems that have more than one correct answer. Your grade will depend on how thorough you analyzed a situation, the quality of your conclusions, and the professionalism of your final reports. The reports should be similar to that you would write if working in a mill. You should include the following in the report; state the objective of the project – a condensed reiteration of the problem statement, how you went about the analysis, a presentation and discussion of the results, final conclusions and recommendations. The reports need to be neat and well written. (I have become convinced that style is at least as important as content in the business world). I won’t put a page target for the report but I generally like things short. It is important that you Groups:
Kappa number from a batch digester is controlled mainly by setting H-factor, EA charge and Sulfidity. It is important to understand how fluctuations in each can effect the final kappa number. We will use the WinGEMS model to better understand the control requirements of a digester.
Use the pulping simulator to compare the performance of three commercial digesters. In this problem compare the pulp quality, as measured by pulp viscosity, and the pulp uniformity of a Kamyr, Batch, and M&D digester. In addition, determine which digester would have the greatest throughput (shortest pulping time). Is there are general correlation between production rate and pulp quality? The following table gives the general operating differences of these digesters: Property Batch Kamyr M&D Pulping time, min 145 Adjust to kappa Adjust to kappa Heat-up time, min 50 10 10 Max Temp 170 162 180 Liq/wood 4.5 3.1 3. Assume the chip size distribution of problem 2 (original), the EA charge and sulfidity can be assumed to be 18% and 25% respectively.