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In thermodynamics and chemical engineering, the vapor–liquid equilibrium (VLE) describes the distribution of chemical species between the vapor phase and a liquid phase.
Technology, Overview & Thermodynamic description of vapor–liquid equilibrium
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liquid vapor components equilibrium pressure temperature component mixture mole mixtures vle point boiling two data pressures binary law temperatures distillation
| Subject | Predicate | Object | Confidence | Src |
|---|---|---|---|---|
| Raoult's law | instance of | The VLE concentration data can be determined experimentally or approximated with the help of theories | 0.80 | text |
| Dalton's law | instance of | The VLE concentration data can be determined experimentally or approximated with the help of theories | 0.80 | text |
| and Henry's law.Such vapor | instance of | The VLE concentration data can be determined experimentally or approximated with the help of theories | 0.80 | text |
| the DePriester charts.For binary mixtures | instance of | tables or graph | 0.80 | text |
| the ratio of the K values for the two components is called the relative volatility denoted by α α | instance of | tables or graph | 0.80 | text |
| 1 atm | instance of | At a given Ptot | 0.80 | text |
| a given liquid composition | instance of | At a given Ptot | 0.80 | text |
| T can be solved for to give the liquid mixture's boiling point or bubble point | instance of | At a given Ptot | 0.80 | text |
| although the solution for T may not be mathematically analytical | instance of | At a given Ptot | 0.80 | text |
| Vapor–liquid equilibrium | related to K values and relative volatility values | The | 0.60 | section |
| Vapor–liquid equilibrium | related to K values and relative volatility values | Henry's | 0.60 | section |
| Vapor–liquid equilibrium | related to K values and relative volatility values | There | 0.60 | section |
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