IDEAS approach to process network synthesis: minimum utility cost for complex distillation networks-Reference-Cited by-同舟云学术

IDEAS approach to process network synthesis: minimum utility cost for complex distillation networks

Published:2002-08 Issue:15 Volume:57 Page:3095-3106
ISSN:0009-2509
Container-title:Chemical Engineering Science
language:en
Short-container-title:Chemical Engineering Science

Author:

Drake James E.,Manousiouthakis Vasilios

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference20 articles.

1. A simple synthesis method based on utility bounding for heat-integrated distillation sequences;Andrecovich;AIChE Journal,1985

2. Mass/heat exchange network representation of distillation networks;Bagajewicz;AIChE Journal,1992

3. Chemical Engineering News, (2000). Production: Gain best losses, vol. 78 (50).

4. Statistical abstract of the United States;Department of Commerce,1997

5. Department of Energy, (1993). New energy-efficient cocurrent distillation technology is a major step forward for industry. DOE Report DOE/CH10093, DE92016415, Washington, DC.

Cited by 31 articles. 订阅此论文施引文献订阅此论文施引文献，注册后可以免费订阅5篇论文的施引文献，订阅后可以查看论文全部施引文献

1. A Process Synthesis and Intensification Framework;Encyclopedia;2024-07-03

2. Integration of reactor network synthesis: A literature review and opportunities for future research;Asia-Pacific Journal of Chemical Engineering;2023-04-21

3. Synthesis of azeotropic distillation processes without using a decanter;Computer Aided Chemical Engineering;2022

4. Synthesis of extractive distillation structures for the purification of ethanol;Computer Aided Chemical Engineering;2022

5. Advancements in Optimization and Control Techniques for Intensifying Processes;Processes;2021-11-28