Dynamic Modeling of a Sub‐zero, Fed‐Batch, Packed Distillation Column to Produce Tetrafluoroethylene-Reference-Cited by-同舟云学术

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Dynamic Modeling of a Sub‐zero, Fed‐Batch, Packed Distillation Column to Produce Tetrafluoroethylene

Published:2021-03-17 Issue:6 Volume:44 Page:980-987
ISSN:0930-7516
Container-title:Chemical Engineering & Technology
language:en
Short-container-title:Chem Eng & Technol

Author:

Espach Johannes I.¹,Sonnendecker Paul W.¹,Crouse Philippus L.¹

Affiliation:

1. University of Pretoria Faculty of Engineering, Built Environment & IT epartment of Chemical Engineering Lynnwood Road, Hatfield 0002 Pretoria South Africa

Funder

Department of Science and Technology, Republic of South Africa

Department of Trade and Industry- South Africa

Publisher

Wiley

Subject

Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Link

https://onlinelibrary.wiley.com/doi/pdf/10.1002/ceat.202000078

Reference27 articles.

1. Pyrolysis of Polytetrafluoroethylene

2. Technological parameters of pyrolysis of waste polytetrafluoroethylene

3. Depolymerization of clean unfilled PTFE waste in a continuous process

4. F. J.Conradie Batch Separation of Tetrafluoroethylene Hexafluoropropylene and Octafluorocyclobutane M. Eng. Thesis University of Pretoria2011.

Cited by 1 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. The Simulation and Optimization of the Tetrafluoroethylene Rectification Process;Separations;2024-01-25

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