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Catalyst for the production of hydrogen

Assignee: Imperial Chemical Industries Ltd
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Filing: 1981-06-11
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Granted: 1984-07-17
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Expires: 2001-06-11
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Abstract

Abstract A catalyst for producing hydrogen by reacting in the gaseous phase a hydrocarbon, hydrocarbon derivative or carbon monoxide with steam and/or if appropriate, carbon dioxide is in the form of hollow pieces each having walls 0.5 to 2 mm thick and comprising a primary support of low pore volume and a secondary support of relatively high surface area. The hollow pieces preferably are partitioned rings and are especially useful in hydrocarbon steam reforming because they can afford high catalytic activity at relatively low active metal content, high mechanical strength and low pressure drop.

Inventors

  • 👤 Martyn V. Twigg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 18:16
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/755; B01J23/76; B01J23/83; B01J35/00; B01J35/30; B01J35/34; B01J35/37; B01J35/50; B01J35/55; B01J35/56; B01J37/00; B01J37/02; B01J37/024; C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B3/40; B01J2235/00; B01J2235/15; C01B2203/00; C01B2203/10; C01B2203/1041; C01B2203/1047; C01B2203/1052; C01B2203/1076; C01B2203/1082; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 124 words
A catalyst for producing a gas containing hydrogen by reacting in the gaseous phase a hydrocarbon, hydrocarbon derivative or carbon monoxide with steam and/or, where appropriate, carbon dioxide, in the form of hollow cylinders having walls 0.5 to 3 mm thick, each said cylinder comprising a primary support made of refractory material having a pore volume less than 0.3 cm 3 g -1 and a surface area less than 10 m 2 g -1 and a coating thereon of a secondary support made of refractory oxidic material having a pore volume greater than 0.3 cm 3 g -1 and an internal surface area in the range 15-300 m 2 g -1 , said secondary support having deposited thereon a catalyst comprising nickel and/or cobalt.
Claim 2
Dependent Claim 124 words
A catalyst for producing a gas containing hydrogen by reacting in the gaseous phase a hydrocarbon, hydrocarbon derivative or carbon monoxide with steam and/or, where appropriate, carbon dioxide, in the form of hollow cylinders having walls 0.5 to 3 mm thick, each said cylinder comprising a primary support made of refractory material having a pore volume less than 0.3 cm 3 g -1 and a surface area less than 10 m 2 g -1 and a coating thereon of a secondary support made of refractory oxidic material having a pore volume greater than 0.3 cm 3 g -1 and an internal surface area in the range 15-300 m 2 g -1 , said secondary support having deposited thereon a catalyst comprising nickel and/or cobalt.
Claim 3
Dependent Claim 24 words
A catalyst according to claim 1 in which the pore volume of the primary support is less than 0.18 cm 3 g -1 .
Claim 4
Dependent Claim 27 words
A catalyst according to claim 1 in which the surface area of the primary support is in the range 0.01 to 2.0 m 2 g -1 .
Claim 5
Dependent Claim 30 words
A catalyst according to claim 1, 2 or 3 in which the surface area of the secondary support is in the range 50 to 200 m 2 g -1 .
Claim 6
Dependent Claim 20 words
A catalyst according to claim 1 in the form of hollow cylinders having 5 or 7 inwardly projecting radial partitions.
Claim 7
Dependent Claim 47 words
A catalyst according to claim 1 in the form of hollow cylinders having through passages defined by partitions having the cross-section of chords intersecting one another in pairs at points distanced from the circumference and centre of the circle in a plane perpendicular to the cylinder axis.
Claim 8
Dependent Claim 25 words
A catalyst according to claim 1 in which the secondary support comprises 0.1 to 5.0% W /W of an oxide of a rare earth metal.
Claim 9
Dependent Claim 35 words
A catalyst according to claim 1 and intended for a process starting from a hydrocarbon, in which the nickel and/or cobalt is present to the extent of 1 to 6% W /W calculated as monoxide.
Claim 10
Dependent Claim 24 words
A catalyst as in claim 1 wherein the nickel and/or cobalt content in within the range 0.2 to 35% W /W calculated as monoxide.
Claim 11
Dependent Claim 24 words
A catalyst as in claim 1 wherein the nickel and/or cobalt content is within the range 1 to 25% W /W calculated as monoxide.
Claim 12
Dependent Claim 24 words
A catalyst as in claim 1 wherein the nickel and/or cobalt content is within the range 0.5 to 8.0% W /W calculated as monoxide.
Claim 13
Dependent Claim 24 words
A catalyst as in claim 1 wherein the nickel and/or cobalt content is within the range 1 to 6% W /W calculated as monoxide.
Claim 14
Dependent Claim 24 words
A catalyst as in claim 1 wherein the nickel and/or cobalt content is within the range 1 to 4% W /W calculated as monoxide.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1987-07-17 1988-01-16 1988-07-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1991-07-17 1992-01-16 1992-07-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1995-07-17 1996-01-16 1996-07-17 $7700.00 Window Closed / Lapsed

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