IP Library Granted Patent US 10,196,266
Granted Patent B2
US 10,196,266 · App. 15/323,157 · Granted Feb 5, 2019

Process for producing hydrogen

Inventor: Kristian Lindell (Kävlinge, SE)
Assignee: Haldor Topsoe A/S
C01B3/48C01B3/382C01B3/56C10G2/30C01B2203/0233C01B2203/0283C01B2203/042C01B2203/043C01B2203/062C01B2203/1058C01B2203/1082C01B2203/127C01B2203/1241C01B2203/1247C01B2203/142
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Quick Facts
Patent No.
US 10,196,266
App. No.
15/323,157
Granted
Feb 5, 2019
Kind
B2
Abstract

Process for producing hydrogen in which tail gas from a separate plant for production of gasoline or diesel is added downstream the steam methane reforming stage and upstream the water gas shift stage of a hydrogen production plant.

Claims (9)

1. Process for producing hydrogen from a hydrocarbon feedstock comprising: passing a feedstock comprising at least one of natural gas and naphtha through sequential stages of steam methane reforming, water gas shift, and hydrogen separation, in which at least a portion of a tail gas from a separate plant for production of gasoline or diesel is combined into a reformed stream by adding the tail gas downstream the steam methane reforming stage and upstream the water gas shift stage, such that reformed gas including the added tail gas is treated in the water gas shift stage.

2. Process according to claim 1 in which the hydrocarbon feedstock is subjected to a pre-reforming stage prior to passing through the steam reforming stage.

3. Process according to claim 2 in which the hydrocarbon feedstock is subjected to hydrogenation and sulfur removal prior to passing through the pre-reforming stage.

4. Process according to claim 1 , in which the steam reforming stage is conducted by conventional steam methane reforming where heat for reforming is provided by radiant heat transfer, convection reforming, or combinations of both.

5. Process according to claim 1 , in which the water gas shift stage is high temperature water gas shift.

6. Process according to claim 1 , in which the hydrogen separation stage is conducted via a PSA-unit.

7. Process according to claim 1 , in which at least a portion of synthesis gas from said separate plant for production of gasoline or diesel is also added downstream the steam methane reforming stage and upstream the water gas shift stage.

8. Process according to claim 1 , wherein said tail gas comprises carbon monoxide, hydrogen, carbon dioxide and methane.

9. Process according to claim 8 , wherein said tail gas includes a minimum of 5 vol. % of carbon monoxide, hydrogen, and carbon dioxide.

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 7, 2017
From: LINDELL, KRISTIAN
To: HALDOR TOPSOE A/S
Reel/Frame 041189/0716 →
Priority Claims (1)
DK 2014 00374 · Jul 9, 2014 · national
Continuity (1)
Related Publication 20170137286A1 · May 18, 2017
Cited By (1)
US 12,565,423