Relative volatility/Related Articles: Difference between revisions
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==Other related topics== | ==Other related topics== | ||
{{r|Continuous distillation}} | |||
{{r|Distillation Design}} | |||
{{r|Fenske equation}} | |||
{{r|McCabe-Thiele method}} | {{r|McCabe-Thiele method}} | ||
Revision as of 21:04, 22 July 2008
- See also changes related to Relative volatility, or pages that link to Relative volatility or to this page or whose text contains "Relative volatility".
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]
- Continuous distillation [r]: An ongoing separation process in which a liquid mixture of two or more miscible components is continuously fed into the process and physically separated into two or more products by preferentially boiling the more volatile (i.e., lower boiling point) components out of the mixture. [e]
- Distillation Design [r]: A chemical engineering book that completely covers the design of industrial distillation columns. [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binary feed stream by a fractionation column operated at total reflux (i.e., meaning that no overhead product is being withdrawn from the column).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]
- McCabe-Thiele method [r]: A graphical method considered to be the simplest, most instructive method for the analysis of binary distillation. [e]