FIELD: heat power industry. SUBSTANCE: method includes deaeration of water in vacuum deaerator, withdrawal of deaerated water and formed flash steam. Initial water is preliminarily deaerated in additional vacuum deaerator under conditions of cold vacuum deaeration without supply of heating agent to deaerator. Formed flash steam from additional deaerator is withdrawn with help of additional gas withdrawing apparatus in form of water-jet ejector to which initial water is supplied as working medium which after ejector is poured into gas- separating tank, and then, directed to additional vacuum deaerator. EFFECT: higher quality of deaeration and economic efficiency of plant. 2 cl, 1 dwg
Title | Year | Author | Number |
---|---|---|---|
VACUUM DEAERATION PLANT | 2000 |
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VACUUM DEAERATOR UNIT | 2000 |
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RU2189946C2 |
Authors
Dates
2002-08-20—Published
2000-11-10—Filed