Process and system for producing dimethyl ether

Patent metadata

Field	Value
Publication number	US-10759728-B2
Application number	US-201716069145-A
Country	US
Kind code	B2
Filing date	Jan 12, 2017
Priority date	Jan 12, 2016
Publication date	Sep 1, 2020
Grant date	Sep 1, 2020

Abstract

The invention relates to an improved process and system for the synthesis of dimethyl ether (DME) from a feedstock comprising H2 and COx, wherein x=1-2. The process according to the invention comprises (a) subjecting the gaseous mixture comprising synthesis gas originating from step (c) to DME synthesis by contacting it with a catalyst capable of converting synthesis gas to DME to obtain a gaseous mixture comprising DME; (b) subjecting a gaseous mixture comprising the gaseous mixture originating from step (a) to a separation-enhanced reverse water gas shift reaction; and (c) subjecting the gaseous mixture originating from step (b) to DME/synthesis gas separation to obtain DME and a gaseous mixture comprising synthesis gas, which is recycled to step (a). Herein, the feedstock is introduced in step (a) or step (b) and the molar ratio of H2 to COx in the gaseous mixture which is subjected to step (b) is at least (x+0.8). Also a system for performing the reaction according to the invention is disclosed.

First claim

The invention claimed is:

1. A process for the synthesis of dimethyl ether (DME) from a feedstock comprising H 2 and CO x , wherein x=1 or 2, comprising sequentially:
(a) subjecting the gaseous mixture comprising synthesis gas from step (c) to DME synthesis by contacting the gaseous mixture with a catalyst capable of converting synthesis gas to DME to obtain a gaseous mixture comprising DME;
(b) subjecting a gaseous mixture comprising the gaseous mixture from step (a) to a separation-enhanced reverse water gas shift reaction; and
(c) subjecting the gaseous mixture from step (b) to DME/synthesis gas separation to obtain DME and a gaseous mixture comprising synthesis gas, which is recycled to step (a),
wherein the feedstock is introduced in step (a) or step (b) and wherein the molar ratio of H 2 to CO x in the gaseous mixture which is subjected to step (b) is at least (x+0.8).

2. The process according to claim 1 , wherein the feedstock comprises CO x , wherein x is 1.5-2 and the feedstock is introduced in step (b).

3. The process according to claim 2 , wherein the feedstock comprises CO x , wherein x is 1.9-2 and the feedstock is introduced in step (b).

4. The process according to claim 1 , wherein the feedstock comprises CO x , wherein x is 1-1.5 and the feedstock is introduced in step (a).

5. The process according to claim 4 , wherein the feedstock comprises CO x , wherein x is 1-1.2 and the feedstock is introduced in step (a).

6. The process according to claim 1 , wherein the molar ratio of H 2 to CO x in the feedstock is in the range of (x+1) to (x+10).

7. The process according to claim 1 , wherein step (a) and/or step (b) is performed in a separation-enhanced DME synthesis (SEDMES) reaction zone.

8. The process according to claim 7 , wherein the SEDMES reaction zone is sorption-enhanced and comprises a catalyst system which contains a direct DME catalyst system and a water-selective adsorbent.

9. The process according to claim 8 , wherein the water-selective adsorbent is a zeolite.

10. The process according to claim 9 , wherein the zeolite has an average pore diameter of at most 4 Å.

11. The process according to claim 8 , wherein step (a) is performed in a SEDMES reaction zone comprising a catalyst system which contains a direct DME catalyst system and a water-selective adsorbent.

12. The process according to claim 1 , wherein step (a) is performed in a direct DME synthesis reaction zone, comprising a catalyst system which contains a direct DME catalyst system and no water-selective adsorbent.

13. The process according to claim 1 , wherein the gaseous mixture originating from step (b) is separated in step (c) in DME and a gaseous mixture comprising synthesis gas and wherein the synthesis gas consists of H 2 and CO x , wherein x=1-1.4.

14. The process according to claim 13 , wherein the gaseous mixture originating from step (b) is separated in step (c) in DME and a gaseous mixture comprising synthesis gas and wherein the synthesis gas consists of H 2 and CO x , wherein x=1-1.1.

15. The process according to claim 1 , wherein the direct DME catalyst system is a bifunctional DME synthesis catalyst or a combination of a methanol synthesis catalyst and a methanol dehydration catalyst.

Assignees

• Stichting Energieonderzoek Centrum Nederland
• TNO

Inventors

• Berkel Franciscus Petrus Felix Van
• Dijk Hendricus Adrianus Johannes Van
• Cobden Paul Dean
• Haije Willem Gerrit
• Vente Jaap Ferdinand

Classifications

• Y02P20/582

  Recycling of unreacted starting or intermediate materials · CPC title

• B01J8/0492

  Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title

• B01J20/165

  Natural alumino-silicates, e.g. zeolites · CPC title

• C01B2203/06

  Integration with other chemical processes · CPC title

• C07C41/01 Primary

  Preparation of ethers · CPC title