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Shell impregnated catalyst and process for producing a shell impregnated catalyst body

a catalyst and shell technology, applied in the direction of physical/chemical process catalysts, metal/metal-oxide/metal-hydroxide catalysts, bulk chemical production, etc., can solve the problems of increasing the requirements for efficiency, lifetime and also catalyst costs, and reducing the reactivity of the carrier. e.g. shell impregnation is difficult by known means

Inactive Publication Date: 2017-06-22
HALDOR TOPSOE AS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The new method described in the patent allows for the improvement of the structural stability and lifetime of catalysts used for steam reforming without affecting their strength or integrity. By impregnating the carrier with an alkaline-earth metal, the carriers reactivity and basicity are increased without changing their structure. This change in affinity for reaction with a particular metal can be controlled, leading to the distribution of metal in the catalyst body being controlled.

Problems solved by technology

New catalysts are under constant development as the requirements for efficiency, lifetime and also costs of the catalyst are ever increasing.
On the other hand, however, the requirements to the structural stability and lifetime of the catalyst are high as it is critical for loading and running the reactors with the catalyst.
Due to these requirements to strength of the carrier, the carrier for e.g. steam reforming catalysts is most often sintered at high temperatures, which reduces the reactivity of the carrier rendering e.g. shell impregnation difficult by known means.

Method used

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  • Shell impregnated catalyst and process for producing a shell impregnated catalyst body
  • Shell impregnated catalyst and process for producing a shell impregnated catalyst body
  • Shell impregnated catalyst and process for producing a shell impregnated catalyst body

Examples

Experimental program
Comparison scheme
Effect test

example i

[0066]Carrier:

[0067]A magnesium alumina spinel carrier containing 92 wt % MgAl2O4 and 8 wt % Al2O3 with a pore volume of 260 ml / kg, a porosity of 46% and a BET surface area of 20 m2 / g.

[0068]Impregnation of the carrier with an alkaline earth metal: The carrier is impregnated by incipient wetness with a Ca(NO3)2 solution at room temperature for half an hour to obtain 3 wt % Ca0 on the carrier. After impregnation the calcium nitrate is decomposed at 550° C.

[0069]Impregnation of the modified carrier with a nickel metal precursor:

[0070]The carrier is impregnated by incipient wetness at room temperature with a nickel nitrate solution containing 7 wt % Ni. After impregnation the nickel nitrate is decomposed at 450° C.

example ii

[0071]Carrier: A carrier as described in example I is used.

[0072]Impregnation of the carrier with an alkaline earth metal: The carrier is impregnated by incipient wetness at room temperature with a Ca(NO3)2 solution as described in example I, Carrier.

[0073]Impregnation of the modified carrier with a nickel metal precursor:

[0074]The carrier is impregnated by incipient wetness at room temperature with a 0.6 M (M stands for molar concentration and this abbreviate is used throughout the document) nickel acetate solution. After impregnation the nickel acetate is decomposed at 450° C.

example iii

[0075]Carrier: A carrier as described in example I is used.

[0076]Impregnation of the carrier with an alkaline earth metal: The carrier is impregnated by incipient wetness with a Ca(NO3)2 solution as described in example I carrier Impregnation of the modified carrier with a nickel metal precursor:

[0077]The carrier is impregnated by incipient wetness at 80° C. with a nickel citrate solution containing 9 wt % Ni. The solution was prepared by dissolving 7.6 g nickelhydroxycarbonate containing 42% Ni and 11.4 g citric acid in 15 ml water at 80° C. After impregnation the nickel citrate is decomposed at 450° C.

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Abstract

The present application relates to a process for producing a catalyst,said process comprising the steps of: providing a carrier and following modifying said carrier by a first impregnation with at least one alkaline earth metal in a first metal precursor solution. The first metal precursor is decomposed to form at least one metal oxide or metal hydroxide thereby obtaining a modified carrier and a second impregnation is carried out by incipient wetness by a second precursor solution comprising at least one metal Me in a second solution. Finally the second precursor is decomposed thereby obtaining a catalyst body having an enrichment of the at least one metal Me in the outer shell of the catalyst body, said at least one metal being present in a concentration having either as an egg-shell profile or a hammock profile.

Description

[0001]The invention relates to a catalyst and a process for producing a catalyst for syngas generation.[0002]New catalysts are under constant development as the requirements for efficiency, lifetime and also costs of the catalyst are ever increasing.[0003]For various reasons it may be beneficial to reduce the amount of metals in the catalyst, for example it may be relevant to minimize the amount of the metal in the catalyst due to environmental considerations. In catalysts for reactions limited by mass transfer such as steam reforming reactions or catalytic partial oxidation at high temperatures the reactive metal is only needed in the surface zone of a catalyst body, i.e. in such catalyst bodies it may be relevant to have a significant metal concentration in the surface zone only. This surface concentrated metal layer also limits unwanted side reactions such as ammonia production in steam reforming of nitrogen rich feedstocks.[0004]On the other hand, however, the requirements to th...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01J23/78B01J37/02C01B3/40B01J35/08B01J35/00B01J23/58B01J35/10
CPCB01J23/78C01B2203/1241B01J37/0205B01J35/1009B01J35/1014B01J35/1038B01J35/1042B01J35/08B01J35/0006C01B3/40C01B2203/0233C01B2203/0244C01B2203/0261C01B2203/1058C01B2203/1064B01J23/58C01B3/32B01J35/613B01J35/633Y02P20/52B01J23/005B01J37/0201B01J37/0203B01J35/397B01J35/19B01J35/51B01J35/612B01J35/635
Inventor OVESEN, CHARLOTTE VINDINGCANO, FERNANDO MORALESHYLDTOFT, JENS HENRIKBORSON, MICHAEL
Owner HALDOR TOPSOE AS