Modeling Project - Pulping and Bleaching - Fall 2007 | PSE 476, Study Guides, Projects, Research of Materials science

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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PSE 476
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:
1. Aldrich, Cooper, Greenwood, Hargrove.
2. Hua, Kim, Lin, McMahon
3. Noste, Ross, Salvatier
4. Schairbaum, Thein-Chen, Zuk
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PSE 476

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:

  1. Aldrich, Cooper, Greenwood, Hargrove.
  2. Hua, Kim, Lin, McMahon
  3. Noste, Ross, Salvatier
  4. Schairbaum, Thein-Chen, Zuk

Digester control problem

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.

  1. H-Factor control. You can use the pulping model to generate a set of data for H-factor and kappa. Plot H-factor vs. kappa. Obtain different values of the H-factor by varying the input pulping time and pulping temperature. Vary both to see if they give the same H-factor vs. Kappa curve. Use the default pulping conditions as a basis. Establishing some heuristics, rules of thumb, is good idea for any engineer in charge of a process. In this case we want to know the influence coefficient of the H-factor on the kappa. That is kappa/H-factor. This parameter will depend on the target kappa and may depend on the other pulping conditions (EA, Sulfidity) as well. Give the influence coefficient of H-factor on kappa and state any caveats associated with this parameter. If the control limit on kappa is  2, what should the control on the H-factor be?
  2. Alkali and Sulfidity control. We want to know the response of kappa to the EA charge and the sulfidty. Run a series of simulations to generate the response in kappa to changes in EA and Sulfidity. The results should be in a plot of EA (or Sulfidity) vs. Kappa. Use the default pulping conditions (18% EA, 25% sulf., 5 L/W, 60min heat- up, 133min. total time, 170oC pulping temp) as your basis. Establish the influence coefficients for EA and Sulfidity on the kappa (i.e. kappa/EA and kappa/ Sulfidity). What are the limits on EA and Sulfidity to keep the kappa range within 
    A mill may want to change its sulfidity for various reasons. For example there is considerable evidence that if you raise sulfidity substantially the pulp quality will improve. Of course, this will make the mill smell worse and could create a TRS (total reduced sulfur) problem. You need to establish with the pulping model whether the influence coefficient of the EA on the kappa is a function of sulfidity and if it is, at what sulfidities, both higher and lower, do you need to determine a new one to operate the digester.

Digester Comparison

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.