Process for preparing methanol

Patent metadata

Field	Value
Publication number	US-12528754-B2
Application number	US-202117920201-A
Country	US
Kind code	B2
Filing date	Apr 9, 2021
Priority date	Apr 20, 2020
Publication date	Jan 20, 2026
Grant date	Jan 20, 2026

Abstract

The invention relates to a process for preparing methanol, in which a synthesis gas comprising carbon oxides and hydrogen is provided, which is passed at elevated pressure and elevated temperature through a catalyst bed of a methanol synthesis catalyst for conversion of the synthesis gas to methanol to obtain a product stream comprising crude methanol and unreacted synthesis gas. Unreacted synthesis gas is recycled to the catalyst bed inlet and combined with the synthesis gas, resulting in a mixed synthesis gas. The mixed synthesis gas at the catalyst bed inlet has a stoichiometry number SN of ≥0.80, the catalyst bed in the conversion of the mixed synthesis gas to methanol has a maximum catalyst bed temperature of ≤280° C., and the mixed synthesis gas at the catalyst bed inlet has a carbon monoxide concentration of ≤20% by volume.

First claim

The invention claimed is:

1 . A process for producing methanol, comprising:
a. providing a synthesis gas including carbon oxides and hydrogen; b. passing the synthesis gas at elevated pressure and elevated temperature through a catalyst bed of a methanol synthesis reactor for conversion of the synthesis gas to methanol thereby producing a product stream comprising crude methanol and unreacted synthesis gas; c. cooling the product stream for condensation and separation of crude methanol comprising at least methanol and water from the cooled product stream; d. recycling at least a portion of the unreacted synthesis gas to the catalyst bed inlet, wherein the unreacted synthesis gas is combined with the synthesis gas thereby producing a mixed synthesis gas, and passing the mixed synthesis gas at elevated pressure and elevated temperature through the catalyst bed of the methanol synthesis catalyst for conversion of the mixed synthesis gas to methanol, wherein the mixed synthesis gas at the catalyst bed inlet has a stoichiometry number SN of ≥0.80, where

SN
=

n
⁡
(

H
2

)

-

n
⁡
(

CO
2

)

n
⁡
(
CO
)

+

n
⁡
(

CO
2

)

,

with
⁢

n
⁢

in

[
mol
]

,

the catalyst bed in the conversion of the mixed synthesis gas to methanol has a maximum catalyst bed temperature of ≤280° C., and the mixed synthesis gas at the catalyst bed inlet has a carbon monoxide concentration of between 9.0% and 13.0% by volume.

2 . The process according to claim 1 , wherein the catalyst bed in the conversion of the mixed synthesis gas to methanol has a maximum catalyst bed temperature of ≤265° C.

3 . The process according to claim 1 , wherein the catalyst bed in the conversion of the mixed synthesis gas to methanol has a maximum catalyst bed temperature of 205° C. to 280° C.

4 . The process according to claim 1 , wherein the catalyst bed in the conversion of the mixed synthesis gas to methanol has a maximum catalyst bed temperature of 205° C. to 265° C.

5 . The process according to claim 1 , wherein the mixed synthesis gas at the catalyst bed inlet has a stoichiometry number SN of ≥2.0.

6 . The process according to claim 1 , wherein the mixed synthesis gas at the catalyst bed inlet has a stoichiometry number SN of 0.80 to 10.0.

7 . The process according to claim 6 , wherein the mixed synthesis gas at the catalyst bed inlet has a stoichiometry number of 0.80 to 2.20.

8 . The process according to claim 7 , wherein the mixed synthesis gas at the catalyst bed inlet has a carbon monoxide concentration of 9.0% to 13.0% by volume.

9 . The process according to claim 1 , wherein the synthesis gas has a stoichiometry number SN of 1.0 to 2.85.

10 . The process according to claim 1 , wherein the mixed synthesis gas at the catalyst bed inlet has a carbon dioxide concentration of ≥20.0% by volume.

11 . The process according to claim 1 , wherein the catalyst bed is divided into a multitude of catalyst bed stages arranged in series, wherein step c) is conducted downstream of each of the catalyst bed stages.

12 . The process according to claim 1 , wherein the synthesis gas is converted to methanol in the catalyst bed at a cooling temperature of the cooling medium used of 190° C. to 250° C.

Assignees

• Air Liquide

Inventors

• Schuhmann Timm
• Wurzel Thomas
• Williams Bryce
• Gronemann Veronika
• Oelmann Tobias
• Haag Stéphane
• Do Nga Thi Quynh

Classifications

• C07C29/153

  characterised by the catalyst used · CPC title

• C07C29/1518

  one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis · CPC title

• Y02P20/584

  Recycling of catalysts · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C07C31/04 Primary

  Methanol · CPC title