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- W2379202461 abstract "A novel CO2cryogenic capture and liquefaction system is introduced and studied theoretically in this paper.The performance and advantages of the combined system are discussed theoretically in this research.This new system combines the CO2cryogenic capture and liquefaction system with the N2/O2 separation together.The aim is to reduce the energy consumption of CO2separation.Theoretical analysis and software-simulation of the combined system are carried out together.The results show that the energy consumption of the proposed new system is lower than the traditional amine solution capture system.When one ton CO2is separated and liquefied,the total primary energy consumption of this combined system is 3.29GJ,while the traditional amine solution capture system is 4.11GJ.In addition,the byproducts N2 and O2can be obtained as well.The study of this paper presents a new thought for the CO2cryogenic capture and liquefaction system." @default.
- W2379202461 created "2016-06-24" @default.
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- W2379202461 date "2012-01-01" @default.
- W2379202461 modified "2023-09-27" @default.
- W2379202461 title "Analysis of new system combining CO_2 cryogenic capture and liquefaction with N_2/O_2 separation" @default.
- W2379202461 hasPublicationYear "2012" @default.
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