IP Library Granted Patent US 7,094,363
Granted Patent B2
US 7,094,363 · App. 10/668,295 · Granted Aug 22, 2006

Process for the preparation of a synthesis gas

Assignee: Haldor Topsoe A/S
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Quick Facts
Patent No.
US 7,094,363
App. No.
10/668,295
Granted
Aug 22, 2006
Kind
B2
Abstract

Process and apparatus for the preparation of synthesis gas by catalytic steam and/or CO 2 reforming of a hydrocarbon feedstock comprising the following steps: (a) heating the reaction mixture of hydrocarbon and steam and/or CO 2 in a heated steam reforming unit integrated with the flue gas containing waste heat section from the fired tubular reformer in which reforming of the reaction mixture takes place by contact with a solid reforming catalyst (b) feeding the partially steam reformed mixture to the fired tubular reformer and further reforming the mixture to the desired composition and temperature, wherein the heated steam reforming unit comprises a piping system containing reaction sections with solid reforming catalyst comprising catalyst pellets and/or catalysed structured elements, the piping system being part of the process gas piping system integrated with the flue gas-containing waste heat section.

Claims (9)

1. Process for the preparation of synthesis gas by catalytic steam and/or CO 2 reforming of a hydrocarbon feedstock comprising the following steps:

(a) heating the reaction mixture of hydrocarbon and steam and/or CO 2 in a heated steam reforming unit integrated with the flue gas containing waste heat section from the fired tubular reformer in which reforming of the reaction mixture takes place in the heated steam reforming unit by contact with a solid reforming catalyst to produce a partially steam reformed mixture; and

(b) feeding the partially steam reformed mixture to the fired tubular reformer and further reforming the mixture to the desired composition and temperature, wherein the heated steam reforming unit comprises a piping system containing reaction sections with solid reforming catalyst comprising catalyst pellets and/or catalysed structured elements, the piping system being part of the process gas piping system integrated with the flue gas-containing waste heat section.

2. Process according to claim 1 , wherein the heated steam reforming unit is comprised of heating sections with or without solid reforming catalyst and adiabatic reaction sections containing catalysed structured elements coated with a layer of steam reforming catalyst, both sections being part of the process gas piping system integrated with the flue gas-containing waste heat section.

3. Process according to claim 1 , wherein the heated steam reforming unit is comprised of heated, reaction sections with catalyst pellets, the heated sections being part of the process gas piping system integrated with the flue gas-containing waste heat section.

4. Process according to claim 1 , wherein the reaction mixture of hydrocarbon and steam and/or CO 2 is pre-reformed prior to heating step (a).

5. Process according to claim 1 , wherein the structured element is a monolith or is cross-corrugated.

6. Process according to claim 2 , wherein steam and/or carbon dioxide is added to the adiabatic reaction sections.

7. Process according to claim 1 , wherein the reaction sections also contain steam reforming catalyst attached to the tube wall or catalyst attached to structures attached to the tube wall.

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 Sep 24, 2003
From: CHRISTENSEN, PETER SEIER; ROSTRUP-NIELSEN, THOMAS; ERIKSTRUP, NIELS; AASBERG-PETERSEN, KIM; HANSEN, JENS-HENRIK BAK; DYBKJAER, IB
To: HALDOR TOPSOE A/S
Reel/Frame 014543/0945 →
Priority Claims (1)
DK 2002 01431 · Sep 26, 2002 · national
Continuity (1)
Related Publication 20040065014A1 · Apr 8, 2004