Low Temperature Applications for CO2 Capture in Hydrogen Production

被引：4

作者：

Kim, Donghoi ^{[1
]}

Berstad, David ^{[2
]}

Anantharaman, Rahul ^{[2
]}

Straus, Julian ^{[2
]}

Peters, Thijs A. ^{[3
]}

Gundersen, Truls ^{[1
]}

机构：

[1] Norwegian Univ Sci & Technol NTNU, Dept Energy & Proc Engn, N-7491 Trondheim, Norway

[2] SINTEF Energy Res, N-7465 Trondheim, Norway

[3] SINTEF Ind, N-0314 Oslo, Norway

来源：

30TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING, PTS A-C | 2020年 / 48卷

关键词：

Low temperature separation; CO2; capture; hydrogen production; liquefaction; CCS;

D O I：

10.1016/B978-0-12-823377-1.50075-6

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

The recent development of the protonic membrane reformer (PMR) technology allows an energy efficient hydrogen production from natural gas. To liquefy and separate CO2 from the retentate gas of the PMR, various low temperature processes are modelled and compared. The optimization results indicate that the single mixed refrigerant based process gives the smallest power consumption and fewest number of units. The cascade and the self-liquefaction processes can be considered as alternatives when the retentate gas is rich and lean in CO2 respectively.

引用

页码：445 / 450

页数：6

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