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Dynamic modeling of paper machine sy...
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Barber, V. A.
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Dynamic modeling of paper machine systems using Matlab with Simulink.
紀錄類型:
書目-電子資源 : Monograph/item
正題名/作者:
Dynamic modeling of paper machine systems using Matlab with Simulink./
作者:
Barber, V. A.
面頁冊數:
103 p.
附註:
Source: Masters Abstracts International, Volume: 42-03, page: 0860.
Contained By:
Masters Abstracts International42-03.
標題:
Agriculture, Wood Technology. -
電子資源:
http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=1417177
ISBN:
0496219618
Dynamic modeling of paper machine systems using Matlab with Simulink.
Barber, V. A.
Dynamic modeling of paper machine systems using Matlab with Simulink.
- 103 p.
Source: Masters Abstracts International, Volume: 42-03, page: 0860.
Thesis (M.S.)--State University of New York College of Environmental Science and Forestry, 2003.
The development of models that accurately predict the performance of a paper machine are valuable to operators trying to optimize paper production and to those concerned with better understanding the process. In this study, a dynamic and modular paper machine simulator package was developed using Matlab with Simulink, and evaluated against data collected from a paper run.
ISBN: 0496219618Subjects--Topical Terms:
1031154
Agriculture, Wood Technology.
Dynamic modeling of paper machine systems using Matlab with Simulink.
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The development of models that accurately predict the performance of a paper machine are valuable to operators trying to optimize paper production and to those concerned with better understanding the process. In this study, a dynamic and modular paper machine simulator package was developed using Matlab with Simulink, and evaluated against data collected from a paper run.
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The results of the study show that the simulation reasonably modeled the chosen system. The simulated production rate of solids at the reel shows a <1% deviation from the measured value at steady-state. The average error of the simulated value of Li concentration in the headbox, mix chest, and white water trough, were calculated as 2.6%, 5.1% and 9.3%, respectively, after the step addition of LiCl solution; 3.7%, 4.4%, and 38.6%, respectively, after-the pulse addition of LiCl solution; and 2.2%, 4.6%, and 1.6%, respectively, after the step reduction of LiCl solution.
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http://pqdd.sinica.edu.tw/twdaoapp/servlet/advanced?query=1417177
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