Abstract
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 H2 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.
| Original language | English |
|---|---|
| Title of host publication | 26 European Symposium on Computer Aided Process Engineering, 2016 |
| Publisher | Elsevier BV |
| Pages | 985-990 |
| Number of pages | 6 |
| Volume | 38 |
| ISBN (Print) | 9780444634283 |
| DOIs | |
| Publication status | Published - 2016 |
Publication series
| Name | Computer Aided Chemical Engineering |
|---|---|
| Volume | 38 |
| ISSN (Print) | 1570-7946 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 13 Climate Action
Keywords
- CO hydrogenation
- energy efficiency
- H stripping
- process simulation
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