Methanol synthesis from synthesis gases with hydrogen deficiency

Patent metadata

Field	Value
Publication number	US-10364202-B2
Application number	US-201716085112-A
Country	US
Kind code	B2
Filing date	Mar 6, 2017
Priority date	Mar 16, 2016
Publication date	Jul 30, 2019
Grant date	Jul 30, 2019

Abstract

The invention relates to a process and a plant for the methanol synthesis, in particular for the methanol synthesis from a synthesis gas which has a hydrogen deficiency. According to the invention, a purge gas stream therefor is branched off from the synthesis gas circuit of the methanol synthesis, liberated from methanol traces in a washing device, and then treated in a hydrogen separation device which comprises a membrane separation stage and a pressure swing adsorption stage. Depending on the application and magnitude of the hydrogen deficit the membrane separation stage and the pressure swing adsorption stage can be connected in series or in parallel.

First claim

The invention claimed is:

1. A process for producing methanol from a synthesis gas comprising hydrogen and carbon oxides, the process comprising the following steps:
(a) providing a synthesis gas make-up gas stream comprising hydrogen and carbon oxides, wherein the synthesis gas make-up gas stream contains a hydrogen deficit with respect to the stoichiometry specified for methanol synthesis;
(b) combining the synthesis gas make-up gas stream from step (a) with a trimming gas stream containing hydrogen to obtain a synthesis gas make-up gas stream enriched in hydrogen;
(c) combining the synthesis gas make-up gas stream enriched in hydrogen with a synthesis gas cycle gas stream obtained in step (g) to obtain a synthesis gas feed gas stream;
(d) introducing the synthesis gas feed gas stream into at least one methanol synthesis reactor and at least in part catalytically converting the carbon oxides contained in the synthesis gas feed gas stream to methanol by using hydrogen under methanol synthesis conditions;
(e) discharging a product gas stream containing methanol vapor and non-converted synthesis gas constituents from the at least one methanol synthesis reactor;
(f) at least partly separating the methanol from the product gas stream by cooling and condensation;
(g) fractionating the product gas stream after separation of the methanol into the synthesis gas cycle gas stream and a purge gas stream loaded with methanol residues, and recirculating the synthesis gas cycle gas stream to step (c);
(h) introducing the purge gas stream loaded with methanol residues into a washing device, contacting the purge gas stream loaded with methanol residues in the washing device with a washing agent, and discharging a purge gas stream depleted of methanol and a washing agent loaded with methanol from the washing device;
(i) introducing the purge gas stream depleted of methanol into a hydrogen separation device which comprises a membrane separation stage and a pressure swing adsorption stage, wherein at least one gas stream enriched in hydrogen and at least one gas stream depleted of hydrogen is obtained; and
(j) recirculating at least one gas stream enriched in hydrogen as the trimming gas stream containing hydrogen to step (b).

2. The process according to claim 1 , wherein in the hydrogen separation device the membrane separation stage and the pressure swing adsorption stage are connected in series and are in fluid connection with each other.

3. The process according to claim 2 , wherein in the hydrogen separation device first the membrane separation stage and then the pressure swing adsorption stage are traversed by the purge gas stream depleted of methanol.

4. The process according to claim 3 , wherein a first gas stream enriched in hydrogen is obtained as permeate in the membrane separation stage, which as trimming gas stream is combined with the synthesis gas make-up gas stream deficient in hydrogen.

5. The process according to claim 4 , wherein the retentate obtained in the membrane separation stage is charged to the pressure swing adsorption stage, and in the pressure swing adsorption stage a second gas stream enriched in hydrogen is obtained, which as trimming gas stream is combined with the synthesis gas make-up gas stream deficient in hydrogen or is discharged from the process as hydrogen export stream.

6. The process according to claim 5 , wherein the second gas stream enriched in hydrogen is combined first with the first gas stream enriched in hydrogen and subsequently as trimming gas stream with the synthesis gas make-up gas stream deficient in hydrogen.

7. The process according to claim 1 , wherein the membrane separation stage and the pressure swing adsorption stage are connected in parallel in the hydrogen separation device, wherein a part of the purge gas stream depleted of methanol is charged to the membrane separation stage and the remaining part of the purge gas stream depleted of methanol is charged to the pressure swing adsorption stage.

8. The process according to claim 7 , wherein a first gas stream enriched in hydrogen is obtained as permeate in the membrane separation stage, which as trimming gas stream is combined with the synthesis gas make-up gas stream deficient in hydrogen.

9. The process according to claim 7 , wherein a second gas stream enriched in hydrogen is obtained in the pressure swing adsorption stage, which as trimming gas stream is combined with the synthesis gas make-up gas stream deficient in hydrogen or is discharged from the process as hydrogen export stream.

10. The process according to claim 1 , wherein the provision of the synthesis gas make-up gas stream is effected by means of a synthesis gas generation stage which comprises an autothermal reformer.

11. A plant for producing methanol from a synthesis gas containing hydrogen, carbon oxides and optionally inert components, comprising the following plant components:
(a) a synthesis gas generation stage for providing a synthesis gas make-up gas stream containing hydrogen, carbon oxides and optionally inert components, which contains a hydrogen deficit with respect to the stoichiometry specified for the methanol synthesis,
(b) a first mixing device for combining the synthesis gas make-up gas stream deficient in hydrogen with a trimming gas stream containing hydrogen to obtain a synthesis gas make-up gas stream enriched in hydrogen,
(c) a second mixing device for combining the synthesis gas make-up gas stream enriched in hydrogen with a synthesis gas cycle gas stream to obtain a synthesis gas feed gas stream,
(d) at least one methanol synthesis reactor, a conduit for introducing the synthesis gas feed gas stream into the at least one methanol synthesis reactor,
(e) a conduit for discharging a product gas stream containing methanol vapor and non-converted synthesis gas constituents from the at least one methanol synthesis reactor,
(f) a separating device for at least partly separating the methanol from the product gas stream by cooling and condensation,
(g) a fractionating device for fractionating the product gas stream after separation of the methanol into a synthesis gas cycle gas stream and a purge gas stream loaded with methanol residues, and a conduit for recirculating the synthesis gas cycle gas stream to the second mixing device,
(h) a washing device, a conduit for introducing the purge gas stream loaded with methanol residues into the washing device, a conduit for introducing the washing agent, a conduit for discharging a purge gas stream depleted of methanol from the washing device, and a conduit for discharging a washing agent loaded with methanol from the washing device,
(i) a hydrogen separation device, comprising a membrane separation stage and a pressure swing adsorption stage, a conduit for introducing the purge gas stream depleted of methanol into the hydrogen separation device, a conduit for discharging a gas stream enriched in hydrogen from the hydrogen separation device, and a conduit for discharging a gas stream depleted of hydrogen from the hydrogen separation device,
(j) a conduit for recirculating a gas stream enriched in hydrogen as trimming gas stream containing hydrogen to the first mixing device.

12. The plant according to claim 11 , wherein in the hydrogen separation device the membrane separation stage and the pressure swing adsorption stage are connected in series and are in fluid connection with each other.

13. The plant according to claim 12 , wherein in the hydrogen separation device first the membrane separation stage and then the pressure swing adsorption stage are traversed by the purge gas stream depleted of methanol.

Assignees

• Air Liquide

Inventors

• Kopetsch Hans
• Gronemann Veronika
• Oelmann Tobias

Classifications

• C07C31/04

  Methanol · CPC title

• B01D53/047

  Pressure swing adsorption · CPC title

• B01J2219/00452

  Means for the recovery of reactants or products · CPC title

• B01J19/0053

  Details of the reactor · CPC title

• C07C29/152 Primary

  characterised by the reactor used · CPC title