Distillation Design/Related Articles: Difference between revisions
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==Parent topic== | |||
{{r|Chemical engineering}} | |||
==Other related topics== | |||
{{r|Perry's Chemical Engineers' Handbook}} | |||
{{r|Unit Operations of Chemical Engineering}} | |||
{{r|McCabe-Thiele method}} | |||
{{r|Fenske equation}} | |||
{{r|Relative volatility}} | |||
Revision as of 18:31, 15 May 2008
- See also changes related to Distillation Design, or pages that link to Distillation Design or to this page or whose text contains "Distillation Design".
Parent topic
- Chemical engineering [r]: a branch of engineering that uses chemistry, biology, physics, and math to solve problems involving fuel, drugs, food, and many other products [e]
- Perry's Chemical Engineers' Handbook [r]: The eighth edition of a chemical engineering reference book that has been a classic for more than seventy years. [e]
- Unit Operations of Chemical Engineering [r]: First published in 1956, this is the seventh edition of one of the oldest chemical enginering textbooks still in widespread use. [e]
- McCabe-Thiele method [r]: A graphical method considered to be the simplest, most instructive method for the analysis of binary distillation. [e]
- Fenske equation [r]: An equation for calculating the minimum number of theoretical plates needed to separate a binary feed stream by a fractionation column operated at total reflux (i.e., meaning that no overhead product is being withdrawn from the column). [e]
- Relative volatility [r]: A measure that compares the vapor pressures of components in a liquid mixture that is widely used in designing distillation and similar separation processes. [e]