Abstract
With conventional methanol reactor designs for CO2-based methanol synthesis, there is the risk of rapid catalyst deactivation with commercial Cu/ZnO/Al2O3 catalysts at high water partial pressures, related to the use of CO2 as carbon feed. As catalyst reactivity and exothermicity are influenced by the switch to a CO2-rich feed, also heat integration options are affected. A new reactor/process design, the Infinity Reactor, is proposed to both improve catalyst lifetime and reduce catalyst usage. The Infinity Reactor is a shell and tube type of reactor, with catalyst on both sides, utilising the difference in temperature between the inlet and outlet of the reactor to operate as a quasi-gas-cooled reactor. The gas loops over both sides of the reactor, with intermediate cooling and condensation. This modelling study shows around 35% savings in catalyst volume in comparison with adiabatic operation.
Original language | English |
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Title of host publication | 33rd European Symposium on Computer Aided Process Engineering |
Publisher | Elsevier |
Pages | 2309-2316 |
Number of pages | 8 |
DOIs | |
Publication status | Published - 18 Jul 2023 |
Event | 33rd European Symposium on Computer Aided Process Engineering, ESCAPE 2023 - Athens, Greece Duration: 18 Jun 2023 → 21 Jun 2023 Conference number: 33 |
Publication series
Name | Computer Aided Chemical Engineering |
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Volume | 52 |
ISSN (Print) | 1570-7946 |
Conference
Conference | 33rd European Symposium on Computer Aided Process Engineering, ESCAPE 2023 |
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Abbreviated title | ESCAPE 2023 |
Country/Territory | Greece |
City | Athens |
Period | 18/06/23 → 21/06/23 |
Keywords
- CO
- infinity
- intensification
- methanol
- reactor
- NLA