Method for the preparation of synthesis gas

Patent metadata

Field	Value
Publication number	US-11370660-B2
Application number	US-201816623835-A
Country	US
Kind code	B2
Filing date	Jul 20, 2018
Priority date	Jul 25, 2017
Publication date	Jun 28, 2022
Grant date	Jun 28, 2022

Abstract

Method for the preparation of synthesis gas based on a combination of the ATR process or partial oxidation of hydrocarbon fee stock using oxygen from the electrolysis of water and an air separation unit to produce the synthesis gas.

First claim

The invention claimed is:

1. Method for the preparation of gas for the synthesis of methanol, comprising the steps of:
(a) separating atmospheric air into a separate oxygen containing stream and into a separate nitrogen containing stream;
(b) preparing a separate hydrogen containing stream and a separate oxygen containing stream by electrolysis of water and/or steam;
(c) partial oxidizing or autothermal reforming in an autothermal reformer at least a part of a hydrocarbon feed stock with at least a part of the oxygen containing stream obtained by the separation of atmospheric air in step (a) and at least a part of the oxygen containing stream obtained by the electrolysis of water and/or steam in step (b) to a process gas comprising hydrogen, carbon monoxide and carbon dioxide;
(d) introducing at least part of the separate hydrogen containing stream from step (b) into the process gas from step (c), wherein the resulting mixture of hydrogen in the separate hydrogen containing stream with the process gas from step (c) form the gas for the synthesis of methanol, the gas having a module M, where M=(H 2 —CO 2 )/(CO+CO 2 ), of between 1.9 and 2.2; and
(e) adjusting the module M by tailoring the amount of hydrogen mixed with the process gas and/or by adding CO 2 to the hydrocarbon feed stock upstream of partial oxidizing or autothermal reforming and/or downstream of step (c).

2. The method of claim 1 , comprising the further step of steam reforming, in a heat exchange reformer, a part of the hydrocarbon feed stock not reformed in the autothermal reformer, by indirect heat transfer with part or all the process stream leaving the autothermal reforming step (c).

3. The method of claim 1 , comprising the further step of steam reforming, in a heat exchange reformer, a part of the hydrocarbon feed stock not reformed in the autothermal reformer and/or a second hydrocarbon feed stock by indirect heat transfer with part or all the process gas leaving the autothermal reforming step (c), and mixing the heat exchange steam reformed process gas with autothermal reformed process gas.

4. The method of claim 1 , comprising a further step of primary steam reforming the hydrocarbon feed stock upstream step (c).

5. The method of claim 1 , wherein the hydrocarbon feed stock comprises natural gas, methane, LNG, naphtha or mixtures thereof either as such or pre-reformed and/or desulfurized.

6. The method of claim 1 , wherein the separating of atmospheric air in step (a) and/or the electrolysis of water and/or steam in step (b) is powered at least in part by renewable energy.

7. The method of claim 1 , wherein the separating of atmospheric air in step (a) is performed by cryogenic separation.

8. The method of claim 1 , wherein the module M is between 2 to 2.1.

9. The method of claim 1 , wherein the gas for the synthesis of methanol is, in a further step, converted to a methanol product.

Assignees

• Haldor Topsoe As
• Topsoe As

Inventors

• Aasberg-Petersen Kim
• Han Pat A

Classifications

• Y02P20/133

  Renewable energy sources, e.g. sunlight · CPC title

• Y02E60/36

  Hydrogen production from non-carbon containing sources, e.g. by water electrolysis · CPC title

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title

• C01B3/382 Primary

  Processes with two or more reaction steps, of which at least one is catalytic, e.g. steam reforming and partial oxidation · CPC title

• C10K3/06

  by mixing with gases · CPC title