Thermally self-sufficient process for single-step coproduction of methanol and dimethyl ether by CO&lt;sub&gt;2&lt;/sub&gt; hydrogenation

Vaquerizo, L.; Kiss, A.A.

doi:10.1016/j.jclepro.2024.140949

Thermally self-sufficient process for single-step coproduction of methanol and dimethyl ether by CO₂ hydrogenation

Title

Thermally self-sufficient process for single-step coproduction of methanol and dimethyl ether by CO₂ hydrogenation

Author

Vaquerizo, L. (TU Delft ChemE/Product and Process Engineering; University of Valladolid)
Kiss, A.A. (TU Delft ChemE/Product and Process Engineering)

Date

2024

Abstract

Methanol and DME are highly efficient fuels and relevant building blocks that can be synthesized by CO₂ hydrogenation. While several alternatives for methanol production by CO₂ hydrogenation have already been developed at a commercial scale, DME production is still based on methanol dehydration. In this sense, the development of bifunctional methanol synthesis/dehydration catalysts is a clear opportunity for the simultaneous coproduction of methanol and DME in a single-step process. Although a few alternatives for DME-methanol coproduction have been proposed, either they need external fuels or refrigerants, or part of the CO₂ used as raw material is purged, resulting in a loss of methanol and DME yields. This work presents a novel thermally self-sufficient process that hydrogenates CO₂ into methanol and DME in a single reactor at 100 % yield (only water as a byproduct at 0.94 kg_water/kg_product), that only consumes air, cooling water (0.006 m³ _water/kg_products) and electricity (net CO₂ emissions of −1.20 or 0.64 kg_CO2eq/kg_products when the plant is operated with green or grey electricity, respectively). The innovative design, based on the combination of a top-divided wall column, an integrated heat network, and limited pressure drop in the reaction-separation loop, results in a thermally self-sufficient process that uses only 0.76 kWh per kg products.