McCabe-Thiele method/Related Articles: Difference between revisions
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{{r|Distillation Design}} | {{r|Distillation Design}} | ||
{{r|Fenske equation}} | {{r|Fenske equation}} | ||
{{r|Reflux (distillation)}} | |||
{{r|Relative volatility}} | {{r|Relative volatility}} | ||
{{r|Theoretical plate}} | {{r|Theoretical plate}} | ||
Revision as of 01:14, 17 November 2008
- See also changes related to McCabe-Thiele method, or pages that link to McCabe-Thiele method or to this page or whose text contains "McCabe-Thiele method".
Parent topic
- 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]
Subtopics
- 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]Chemical engineering}}
- 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binary feed stream by a fractionation column operated at total reflux (i.e., meaning that no overhead product is being withdrawn from the column).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]
- Reflux (distillation) [r]: A distillation technique involving the condensation of the distilled product vapors and the return of a portion of the condensate to the distillation system from which it originated. [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]
- Theoretical plate [r]: A hypothetical zone or stage in a chemical engineering separation process in which two phases, such as the liquid and vapor phases of a substance, establish an equilibrium with each other. [e]