Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate

碩士 === 國立臺灣大學 === 化學工程學研究所 === 104 === In this work batch crystallization experiments of potassium aluminum sulfate was performed with manipulating various operation valuables. Experimental results are used to determine the kinetic parameters of nucleation rate and growth rate. The second part of th...

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Main Authors: Bo-Wen Chen, 陳柏彣
Other Authors: Jeffrey D.Ward
Format: Others
Language:en_US
Published: 2016
Online Access:http://ndltd.ncl.edu.tw/handle/61084409005821545843
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spelling ndltd-TW-104NTU050630832017-06-10T04:46:47Z http://ndltd.ncl.edu.tw/handle/61084409005821545843 Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate 硫酸鉀鋁批次結晶槽和長晶動力式模擬與最適化操作 Bo-Wen Chen 陳柏彣 碩士 國立臺灣大學 化學工程學研究所 104 In this work batch crystallization experiments of potassium aluminum sulfate was performed with manipulating various operation valuables. Experimental results are used to determine the kinetic parameters of nucleation rate and growth rate. The second part of this work is computer program simulation to optimize temperature trajectories operating batch cooling experiment with specific objective function. The purpose of the desupersaturation experiment is to determine the kinetic parameters of growth rate equation. Data are collected under different conditions, degree of supersaturation and temperature and fit to the model form G=(T,S)=〖 k〗_g e^((-E_a)/RT)×S^g. There are two experimental variables in this simulation: temperature (T), supersaturation (S). We can determine the pre-experimental factor (〖 k〗_g), activation factor (E_a) and g opponent for potassium aluminum sulfate by regression. In batch cooling crystallization, the results show that we achieve different crystal size distribution by manipulating the cooling rate and the initial degree of supersaturation. The study also include the crystal size distribution(CSD) and volume size distribution(VSD) result of the crystal products measured by Laser Diffraction Particle Size Analyzer(Coulter LS230). In this study we investigate the growth rate, and nucleation based on the CSD results. Furthermore, we analyze the CSD and VSD with the growth rate dispersion model. The dispersion model show that the effect of growth rate dispersion on the crystal size distribution may be significant. In this study, the result show the CSD and VSD comparison between constant growth rate model and Gamma distribution type of growth rate dispersion model. The method of optimizations are the method of iteration. This work use Matlab program to construct the optimization problem which is to find the minimum μ_(3.n)/μ_3 (minimize the nucleation mass) which is the objective function in this work. Jeffrey D.Ward 吳哲夫 2016 學位論文 ; thesis 77 en_US
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language en_US
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sources NDLTD
description 碩士 === 國立臺灣大學 === 化學工程學研究所 === 104 === In this work batch crystallization experiments of potassium aluminum sulfate was performed with manipulating various operation valuables. Experimental results are used to determine the kinetic parameters of nucleation rate and growth rate. The second part of this work is computer program simulation to optimize temperature trajectories operating batch cooling experiment with specific objective function. The purpose of the desupersaturation experiment is to determine the kinetic parameters of growth rate equation. Data are collected under different conditions, degree of supersaturation and temperature and fit to the model form G=(T,S)=〖 k〗_g e^((-E_a)/RT)×S^g. There are two experimental variables in this simulation: temperature (T), supersaturation (S). We can determine the pre-experimental factor (〖 k〗_g), activation factor (E_a) and g opponent for potassium aluminum sulfate by regression. In batch cooling crystallization, the results show that we achieve different crystal size distribution by manipulating the cooling rate and the initial degree of supersaturation. The study also include the crystal size distribution(CSD) and volume size distribution(VSD) result of the crystal products measured by Laser Diffraction Particle Size Analyzer(Coulter LS230). In this study we investigate the growth rate, and nucleation based on the CSD results. Furthermore, we analyze the CSD and VSD with the growth rate dispersion model. The dispersion model show that the effect of growth rate dispersion on the crystal size distribution may be significant. In this study, the result show the CSD and VSD comparison between constant growth rate model and Gamma distribution type of growth rate dispersion model. The method of optimizations are the method of iteration. This work use Matlab program to construct the optimization problem which is to find the minimum μ_(3.n)/μ_3 (minimize the nucleation mass) which is the objective function in this work.
author2 Jeffrey D.Ward
author_facet Jeffrey D.Ward
Bo-Wen Chen
陳柏彣
author Bo-Wen Chen
陳柏彣
spellingShingle Bo-Wen Chen
陳柏彣
Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
author_sort Bo-Wen Chen
title Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
title_short Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
title_full Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
title_fullStr Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
title_full_unstemmed Kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
title_sort kinetics modeling and optimized operation in batch seeded crystallization of potassium aluminum sulfate
publishDate 2016
url http://ndltd.ncl.edu.tw/handle/61084409005821545843
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