Enhanced Process for Methanol Production by CO2 Hydrogenation

被引:4
|
作者
Kiss, Anton. A. [1 ,2 ]
Pragt, J. J. [1 ]
Vos, H. J. [1 ]
Bargeman, G. [1 ]
de Groot, M. T. [3 ]
机构
[1] AkzoNobel Res, Dev & Innovat, Strateg Res Grp Proc Technol, Zutphenseweg 10, NL-7418 AJ Deventer, Netherlands
[2] Univ Twente, Sustainable Proc Technol, POB 217, NL-7500 AE Enschede, Netherlands
[3] AkzoNobel Ind Chem, POB 247, NL-3800 AE Amersfoort, Netherlands
关键词
CO2; hydrogenation; H-2; stripping; energy efficiency; process simulation;
D O I
10.1016/B978-0-444-63428-3.50169-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the quest for a green chemical industry, much effort is devoted to the development of technologies for methanol synthesis by hydrogenation of CO2 - available from many sources. Low-cost sources of H-2 are less frequently found, but an additional source at industrial scale is the wet hydrogen by-product of chlorine production. This study presents an enhanced process for methanol synthesis by CO2 hydrogenation using wet hydrogen by-product from salt electrolysis. This process uses a stripping unit where the wet hydrogen flows counter-currently to the condensed methanol-water mixture from the flash separator after reactor. This operation removes CO2 from the methanol-water mixture thus allowing a complete recycle of CO2 while also removing the water from wet hydrogen thus avoiding its negative impact on chemical equilibrium conversion. Consumption figures are 550 kWh electricity and 0.48-1.16 ton steam per ton methanol.
引用
收藏
页码:985 / 990
页数:6
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