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dc.creatorPouilliart, R.en_US
dc.creatorVan Hecke, F. C.en_US
dc.date.accessioned2011-04-11T15:35:27Z
dc.date.available2011-04-11T15:35:27Z
dc.date.issued1981en_US
dc.identifier.otherESL-IE-81-04-20en_US
dc.identifier.urihttp://hdl.handle.net/1969.1/94407
dc.description.abstractAn exergy analysis of carbonate solution C02 removal systems which use solution flashing shows that there is no energy saving by using a mechanical thermocompressor instead of a steam-jet ejector. In a 1000 ShT/D ammonia plant an energy saving of approx. 27 GJ/h (GHV) of natural gas is possible by using exhaust steam from a back pressure turbine instead of L.T. shift gas as the heat supply source for a Carsol C02 removal system.en_US
dc.publisherEnergy Systems Laboratory (http://esl.tamu.edu)en_US
dc.publisherTexas A&M University (http://www.tamu.edu)en_US
dc.subjectAmmonia Planten_US
dc.subjectCO2 Removal Systemen_US
dc.subjectSteam Jet Ejectoren_US
dc.subjectMechanical Thermocompressoren_US
dc.titleEnergy Savings for CO2 Removal in Ammonia Plantsen_US
dc.contributor.sponsorCarbcchimen_US
dc.contributor.sponsorSaint-Ghislainen_US


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