IP Library Granted Patent US 11,124,424
Granted Patent B2
US 11,124,424 · App. 16/623,139 · Granted Sep 21, 2021

Process for the co-production of methanol and ammonia in parallel

Inventor: Pat A. Han (Smørum, DK)
Assignee: Haldor Topsoe A/S
C01C1/0488C01B3/025C01B3/382C01C1/024C07C29/1518C25B1/04C01B2203/0216C01B2203/0283C01B2203/046C01B2203/061C01B2203/068
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Quick Facts
Patent No.
US 11,124,424
App. No.
16/623,139
Granted
Sep 21, 2021
Kind
B2
Abstract

A process for co-production of methanol and ammonia in parallel based on autothermal reforming with oxygen enriched air from electrolysis of water and separation of air and preparation of ammonia with hydrogen from the electrolysis of water and nitrogen from the separation of air.

Claims (11)

1. Process for the co-production of methanol and ammonia in parallel, comprising the steps of:

(a) providing a hydrocarbon feed stock;

(b) preparing a separate hydrogen stream and a separate oxygen stream by electrolysis of water;

(c) preparing a separate oxygen stream and a separate nitrogen stream by separation of air;

(d) introducing at least part of the separate oxygen stream from step (b) and at least part of the separate oxygen from step (c) into an autothermal reformer;

(e) in the autothermal reformer, autothermal reforming the hydrocarbon feed stock from step (a) to a methanol synthesis gas comprising hydrogen and carbon oxides;

(f) converting the methanol synthesis gas to raw methanol in a methanol synthesis stage; and in parallel

(g) introducing the at least part of the separate hydrogen stream from step (b) and the separate nitrogen stream from step (c) into an ammonia synthesis loop, and converting the nitrogen and hydrogen stream to ammonia.

2. Process of claim 1 , wherein module (M=(H 2 −CO 2 )/(CO+CO 2 )) of the methanol synthesis gas from step (e) is adjusted to a value of between 1.9 and 2.2 by adding a part of the separate hydrogen stream from step (b) into the methanol synthesis gas from step (e).

3. Process of claim 1 , wherein the separate hydrogen stream from step (b) and the separate nitrogen stream from step (c) are introduced into the ammonia synthesis loop in amounts to provide a molar ratio of the hydrogen to the nitrogen of 2.7-3.3.

4. Process of claim 1 , wherein the electrolysis of water and/or the separation of air is powered by renewable energy.

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 Feb 27, 2020
From: HAN, PAT A.
To: HALDOR TOPSOE A/S
Reel/Frame 051946/0443 →
Priority Claims (6)
DK PA 2017 00425 · Jul 25, 2017 · national
DK PA 2017 00522 · Sep 25, 2017 · national
DK PA 2018 00237 · May 28, 2018 · national
DK PA 2018 00345 · Jul 6, 2018 · national
DK PA 2018 00351 · Jul 6, 2018 · national
DK PA 2018 00352 · Jul 6, 2018 · national
Continuity (1)
Related Publication 20200207632A1 · Jul 2, 2020