乙烯衍生物製程之設計與整合：環氧乙烷與苯乙烯單體之案例研究

Ethylene-Derived Process Design and Integration:Case Studies of Ethylene Oxide and Styrene Monomer

胡偉駿(Wei-Chun Hu)

指導教授 ： 陳錫仁

淡江大學/工學院/化學工程與材料工程學系碩士班/碩士(2007年)

https://doi.org/10.6846/TKU.2007.01131

摘要

本篇摘要未授權

關鍵字

換熱器網路 ； 本質安全設計 ； 爆炸界線 ； 乙二醇 ； 環氧乙烷 ； 苯乙烯

並列摘要

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並列關鍵字

heat exchanger network ； inherent safe designs ； explosion limits ； ethylene oxide ； styrene

參考文獻

Ahmad, S., B. Linnhoff and R. Smith, “Cost Optimum Heat Exchanger Networks: II. Targets and Design for Detailed Capital Cost Models,”Comp. and Chem. Engng., 14, 751 (1990).

Britton, L.G., Using Material Data in Static Hazard Assessment, Plant/Operations Progress, 11, 2, 56 (1992).

Douglas, J.M. ,Conceptual Design of Chemical Processes, p.518 (New York: McGraw-Hill, 1988)

Floudas, C.A., A.R. Ciric and I.E. Grossmann, “Automatic Synthesis of Optimum Heat Exchanger Network Configurations,” AIChE J. 32, 276 (1986).

Gundersen, T. and I.E. Grossmann, “Improved Optimization Strategies for Automated Heat Exchanger Network Synthesis Through Physical Insights,”Comp. and Chem. Engng., 14, 925 (1990).