IP Library Granted Patent US 7,547,332
Granted Patent B2
US 7,547,332 · App. 11/359,466 · Granted Jun 16, 2009

Apparatus for the preparation of synthesis gas

Assignee: Haldor Topsoe A/S
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Quick Facts
Patent No.
US 7,547,332
App. No.
11/359,466
Granted
Jun 16, 2009
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 (10)

1. Apparatus for the preparation of synthesis gas comprising:

a. an adiabatic pre-reformer for optional pre-reforming of a mixture of hydrocarbon and steam and/or CO 2 ;

b. a fired tubular reformer with a flue gas-containing waste heat section for heating of a mixture of hydrocarbon and steam and/or CO 2 or of the pre-reformed mixture; and

c. a heated steam reforming unit integrated with the flue gas containing waste heat section from the fired tubular reformer wherein the heated steam reforming unit comprises a piping system of a flue gas heated coil system, the piping system containing reaction sections of solid reforming catalyst comprising catalyst pellets and/or catalyzed structured elements, the piping system comprising heating sections and adiabatic reaction sections, the adiabatic reaction sections being situated outside the flue gas containing waste heat section, the piping system being part of the process gas piping system integrated with the flue gas-containing waste heat section.

2. Apparatus according to claim 1 wherein solid catalyst is placed in the heated reaction sections and/or in the adiabatic reaction sections of the heated steam reforming unit.

3. Apparatus according to claim 2 wherein the solid catalyst comprises catalyzed hardware in the form of catalyst pellets and/or structured elements with a catalytic layer of steam reforming catalyst.

4. Apparatus according to claim 2 wherein the solid catalyst comprises high surface structured elements or catalyst attached to the tube wall as a film.

5. Apparatus 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 catalyzed 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.

6. Apparatus 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.

7. Apparatus according to claim 1 wherein the structured element is a monolith or is cross-corrugated.

Assignments (1)
CHANGE OF NAME Recorded Oct 3, 2023
From: HALDOR TOPSØE A/S
To: TOPSOE A/S
Reel/Frame 065108/0028 →
Priority Claims (1)
DK 2002 01431 · Sep 26, 2003 · national
Continuity (2)
Division 1066829500 · Sep 24, 2003
Related Publication 20060143984A1 · Jul 6, 2006