IP Library Granted Patent US 11,247,955
Granted Patent B2
US 11,247,955 · App. 17/269,607 · Granted Feb 15, 2022

Process for the preparation of methanol

Inventors: Emil Andreas T{umlaut over (j)}arnehov (Limhamn, SE); Lars Storm Pedersen (Farum, DK); Michael Hultqvist (Bagsværd, DK); Søren Grønborg Eskesen (Espergærde, DK); Louise Wissing Jensen (Kgs. Lyngby, DK)
Assignee: Haldor Topsoe A/S
C07C29/1518C07C29/152C07C29/80C25B1/04
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Quick Facts
Patent No.
US 11,247,955
App. No.
17/269,607
Granted
Feb 15, 2022
Kind
B2
Abstract

Process for the preparation of a methanol product comprising the steps of a) providing a first process stream consisting essentially of carbon dioxide; b) providing a second process stream consisting of hydrogen by electrolyzing water in an electrolysis unit; c) mixing the first and second process in amount to obtain a methanol synthesis gas with a mole ratio of H2 and CO2 of between 2.5 and 3.5; d) catalytic converting the methanol synthesis gas into raw methanol in at least one methanol reactor; e) purifying the raw methanol in a distillation unit; and recovering waste heat generated in the electrolysis unit in step (b) by transferring the waste heat to a circulating heat transfer medium by indirect heat exchange with the waste heat and by indirect heat exchange of the heated heat transfer medium with steam used for the distillation of the raw methanol, wherein the heated transfer medium is compressed upstream the indirect heat exchange with steam.

Claims (10)

1. A process for the preparation of a methanol product comprising the steps of:

a) providing a first process stream consisting essentially of carbon dioxide;

b) providing a second process stream consisting of hydrogen by electrolyzing water in an electrolysis unit;

c) mixing the first and second process stream in amount to obtain a methanol synthesis gas with a mole ratio of H 2 and CO 2 of between 2.5 and 3.5;

d) catalytic converting the methanol synthesis gas into raw methanol in at least one methanol reactor;

e) purifying the raw methanol in a distillation unit; and

recovering waste heat generated in the electrolysis unit in step (b) by transferring the waste heat to a circulating heat transfer medium by indirect heat exchange with the waste heat and by indirect heat exchange of the heated heat transfer medium with steam used for the distillation of the raw methanol, wherein the heated transfer medium is compressed upstream the indirect heat exchange with steam.

2. Process of claim 1 , wherein the heat transfer medium has a boiling point lower than the waste heat from the electrolysis at a pressure prevailing in the indirect heat exchange with the waste heat and a boiling point higher than the temperature in the indirect heat exchange with the steam at a pressure prevailing in the indirect heat exchange with the steam.

3. The process of claim 1 , wherein the distillation unit comprises two or more distillation towers operated in series.

4. The process of claim 1 , wherein at least a part of the water electrolyzed in the electrolysis unit is distillation water withdrawn from the methanol distillation unit.

Assignments (2)
CHANGE OF NAME Recorded Oct 3, 2023
From: HALDOR TOPSØE A/S
To: TOPSOE A/S
Reel/Frame 065108/0028 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 4, 2021
From: TJÄRNEHOV, EMIL ANDREAS; PEDERSEN, LARS STORM; HULTQVIST, MICHAEL; ESKESEN, SØREN GRØNBORG; JENSEN, LOUISE WISSING
To: HALDOR TOPSOE A/S
Reel/Frame 058023/0418 →
Priority Claims (1)
DK PA 2018 00573 · Sep 13, 2018 · national
Continuity (1)
Related Publication 20210363079A1 · Nov 25, 2021