Ni—MgO—ZnO solid catalysts for syngas preparation and process for the preparation thereof

US9950315B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9950315-B2
Application numberUS-201514842301-A
CountryUS
Kind codeB2
Filing dateSep 1, 2015
Priority dateSep 2, 2014
Publication dateApr 24, 2018
Grant dateApr 24, 2018

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

The present invention provides a process and catalyst for the production of synthesis gas (a mixture of CO and H 2 ) by reforming of methane with carbon dioxide. The process provides a direct single step selective vapor phase dry reforming of methane with carbon dioxide to produce synthesis gas over Ni—MgO—ZnO catalyst between temperature range of 600° C. to 800° C. at 1 atmospheric pressure. The process provides a methane conversion of 5-95% with H 2 to CO mole ratio of 0.83-1.2.

First claim

Opening claim text (preview).

We claim: 1. A process for the preparation of a Ni—MgO—ZnO solid catalyst, the catalyst comprising: a) Ni in the range of 2-10%, b) MgO in the range of 2-10% and c) ZnO in the range of 90-95%, wherein the said process comprises the steps of: i. dissolving Zinc nitrate hexahydrate and Magnesium nitrate hexahydrate in water, ii. adding Nickel nitrate hexahydrate in water to the mixture as obtained in step (i) followed by stirring to obtain a homogenous mixture; iii. adding a solution of CTAB (cetyltrimethylammonium bromide) in ethanol to the mixture as obtained in step (ii) with stirring for period in the range of 1 to 2 hours followed by adding hydrazine hydrate with adjusting the pH of the solution in the range of 8-12 to obtain a solution, iv. stirring the solution as obtained in step (iii) for a period in the range of 1-3 hours followed by autoclaving for period in the range of 12 to 48 hours at a temperature in the range of 160 to 180° C. to obtain a precipitate; v. filtering the precipitate as obtained in step (iv) with water and drying at a temperature ranging between 60 to 110° C. for a time period ranging between 12-20 hours followed by calcining at a temperature in the range of 400-750° C. for a time period of 4-8 hours to obtain the Ni—MgO—ZnO catalyst. 2. The process as claimed in claim 1 , wherein the Ni to Ni—MgO—ZnO of the catalyst varied in the range of 2 to 10%.

Assignees

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Classifications

  • Natural gas or methane · CPC title

  • the reforming step being a carbon dioxide reforming step · CPC title

  • Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

  • characterised by the catalyst · CPC title

  • Cross-Sectional Technologies · mapped topic

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What does patent US9950315B2 cover?
The present invention provides a process and catalyst for the production of synthesis gas (a mixture of CO and H 2 ) by reforming of methane with carbon dioxide. The process provides a direct single step selective vapor phase dry reforming of methane with carbon dioxide to produce synthesis gas over Ni—MgO—ZnO catalyst between temperature range of 600° C. to 800° C. at 1 atmospheric pressure. T…
Who is the assignee on this patent?
Council Scient Ind Res
What technology area does this patent fall under?
Primary CPC classification B01J23/80. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Apr 24 2018 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).