Flash evaporation (or partial evaporation) is the partial vapor that occurs when a saturated liquid stream undergoes a reduction in pressure by passing through a throttling valve or other throttling device. This process is one of the simplest unit operations. If the throttling valve or device is located at the entry into a pressure vessel so that the flash evaporation occurs within the vessel, then the vessel is often referred to as a flash drum.
If the saturated liquid is a single-component liquid (for example, propane or liquid ammonia), a part of the liquid immediately "flashes" into vapor. Both the vapor and the residual liquid are cooled to the saturation temperature of the liquid at the reduced pressure. This is often referred to as "auto-refrigeration" and is the basis of most conventional vapor compression refrigeration systems.
If the saturated liquid is a multi-component liquid (for example, a mixture of propane, isobutane and normal butane), the flashed vapor is richer in the more volatile components than is the remaining liquid.
Uncontrolled flash evaporation can result in a boiling liquid expanding vapor explosion (BLEVE).
The flash evaporation of a single-component liquid is an isenthalpic process and is often referred to as an adiabatic flash. The following equation, derived from a simple heat balance around the throttling valve or device, is used to predict how much of a single-component liquid is vaporized.
{| border="0" cellpadding="2"
|-
|align=right|where:
|
|-
!align=right|
|align=left|= weight ratio of vaporized liquid / total mass
|-
!align=right|
|align=left|= upstream liquid enthalpy at upstream temperature and pressure, J/kg
|-
!align=right|
|align=left|= flashed vapor enthalpy at downstream pressure and corresponding saturation temperature, J/kg
|-
!align=right|
|align=left|= residual liquid enthalpy at downstream pressure and corresponding saturation temperature, J/kg
|}
If the enthalpy data required for the above equation is unavailable, then the following equation may be used.
Cette page est générée automatiquement et peut contenir des informations qui ne sont pas correctes, complètes, à jour ou pertinentes par rapport à votre recherche. Il en va de même pour toutes les autres pages de ce site. Veillez à vérifier les informations auprès des sources officielles de l'EPFL.
This course covers the fundamental and practical analysis of two-phase flow and heat transfer in various contexts including power generation, water purification, and cooling. Students will learn about
The course will cover fundamentals concepts of separation processes involving chemical equilibrium and mass transfer. Students will design separation processes widely used in the industry, for the sep
Explore les systèmes de réfrigération au gaz, y compris les cycles de Brayton et les pompes à chaleur, en discutant des principes, des performances et des approches d'optimisation.
La distillation du pétrole comprend deux procédés distincts : la distillation atmosphérique et la distillation sous vide. La distillation atmosphérique est un procédé de distillation qui consiste à séparer les unes des autres les fractions d'hydrocarbures contenues dans le pétrole brut. C'est la première étape du raffinage du pétrole, et les toutes premières raffineries de pétrole se résumaient à peu près à une colonne de distillation. Son fonctionnement est fondé sur la différence des températures d'ébullition de chacun des produits purs contenus dans le pétrole.
Le réfrigérateur à compression de vapeur est fondé sur la condensation de vapeur d'un fluide réfrigérant à la suite d'une compression, et son évaporation à la suite d'une détente. C'est le procédé le plus répandu pour la production du froid. Ce principe est identique à celui employé pour les pompes à chaleur. Ce procédé est à distinguer du turboréfrigérateur, dans lequel un gaz est comprimé, refroidi à température ambiante, puis détendu dans une turbine. Cet autre procédé ne fait pas intervenir de changement de phase.
Natural-gas processing is a range of industrial processes designed to purify raw natural gas by removing contaminants such as solids, water, carbon dioxide (CO2), hydrogen sulfide (H2S), mercury and higher molecular mass hydrocarbons (condensate) to produce pipeline quality dry natural gas for pipeline distribution and final use. Some of the substances which contaminate natural gas have economic value and are further processed or sold. Hydrocarbons that are liquid at ambient conditions: temperature and pressure (i.
Sublimation influences the water storage in snow covers and glaciers, which is important for water use and projections of the sea level rise. Yet, it is challenging to quantify sublimation for large areas or in conditions of snow transport. In-situ measure ...
Automated field sampling of streamwater or precipitation for subsequent analysis of stable water isotopes (H-2 and O-18) is often conducted with off-the-shelf automated samplers. However, when water samples are stored in the field for days and weeks in ope ...
COPERNICUS GESELLSCHAFT MBH2020
Cellulose nanocrystal (CNC) suspensions can self-assemble into chiral nematic films upon the slow evaporation of water. These films are brittle, as indicated by their fracturing instead of plastically deforming once they are fully elastically deformed. Thi ...