Highly active catalyst for dehydrogenation of alkanes and method of preparation thereof

Patent metadata

Field	Value
Publication number	US-10947172-B2
Application number	US-201916657726-A
Country	US
Kind code	B2
Filing date	Oct 18, 2019
Priority date	Nov 21, 2018
Publication date	Mar 16, 2021
Grant date	Mar 16, 2021

Abstract

The invention discloses a novel method for preparation of highly active and selective dehydrogenation catalyst, comprising of metal oxide of group VIB elements of periodic table, and at least one metal oxide from group IA and/or group VIII, supported on alumina or silica or mixture thereof, wherein the accessibility to active sites and dispersion of metal oxides is enhanced by the addition of carbonaceous material such as coke derived from coal or petroleum coke or any other form of carbon, during catalyst preparation and its combustion thereof during calcination.

First claim

The invention claimed is:

1. A process for preparation of a catalyst for dehydrogenation of alkane, wherein the process comprises:
(a) wet grinding of carbonaceous material to obtain a grinded paste of the carbonaceous material;
(b) adding alumina to an organic acid solution under stirring for 15-20 minutes to form alumina gel and ageing the gel for 15-20 minutes;
(c) preparing aqueous solution of salts of metals of Groups IA and/or VIB and/or VIII using suitable metal salts;
(d) adding the grinded paste of the carbonaceous material obtained in step (a) and the aqueous solution of salts of metals obtained in step (c) to the alumina gel obtained in step (b) to obtain a homogeneous catalyst slurry;
(e) drying the catalyst slurry obtained in step (d) at 100-150° C. for 12-16 hours to get a dry cake of catalyst;
(f) crushing the dry cake of catalyst obtained in step (e) and sieving to obtain catalyst particles of 0.5-1.0 mm for fixed bed operation and particles of 20-200μ for fluidized bed operation;
(g) calcining the catalyst particles obtained in step (f) at 600-650° C. at a ramp rate of 2.0° C./min for 2 hours in presence of air; and
(h) reducing the catalyst obtained in step (g) in a fixed bed/fixed-fluidized bed reactor using hydrogen gas, at 600-800° C. at a controlled flow rate to obtain final catalyst.

2. The process as claimed in claim 1 , wherein the carbonaceous material is selected from the group comprising of petroleum coke, activated charcoal, graphite powder, and a combination thereof.

3. The process as claimed in claim 1 , wherein in step (a) the carbonaceous material is grinded to a particle size ranging from 1 to 5μ.

4. The process as claimed in claim 1 , wherein in step (b) the organic acid is formic acid.

5. The process as claimed in claim 1 , wherein in step (b) the organic acid solution is prepared by adding 10% by volume of formic acid in distilled water.

6. The process as claimed in claim 1 , wherein the metal of Group VIB is selected from group consisting of chromium, molybdenum, and tungsten.

7. The process as claimed in claim 1 , wherein the metal of Group VIII is selected from group consisting of iron, cobalt, rhodium, iridium, nickel, palladium, and platinum, and the metal of Group IA is selected from group consisting of lithium, sodium, potassium, rubidium, and cesium.

Assignees

• Indian Oil Corp Ltd

Inventors

• Thakur Ram Mohan
• Doosa Hima Bindu
• Gupta Kamlesh
• Bhattacharyya Debasis
• Mazumdar Sanjiv Kumar
• RAMAKUMAR Sankara Sri Venkata

Classifications

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• B01J23/6527

  Tungsten · CPC title

• B01J37/0036

  Grinding · CPC title

• B01J21/18 Primary

  Carbon · CPC title

• B01J23/04

  Alkali metals · CPC title