Catalyst coating liquid manufacturing method and catalyst body thereby
US-9486780-B2 · Nov 8, 2016 · US
US10384199B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10384199-B2 |
| Application number | US-201515302079-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 17, 2015 |
| Priority date | Jul 17, 2014 |
| Publication date | Aug 20, 2019 |
| Grant date | Aug 20, 2019 |
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A process and system for modifying heterogeneous catalysts by contacting them with chemical compounds to functionalize the surface of the heterogeneous catalyst. A polymetallic catalyst including bimetallic catalyst is functionalized on its surface by employing a precursor of an inorganic compound. The precursor of the inorganic compound is an organometallic compound, and the metal based inorganic compound is aluminum oxide. A process and system for surface modification functionalization of the heterogeneous catalysts at conditions including room temperature and atmospheric pressure.
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We claim: 1. A modified heterogeneous catalyst comprising at least one modifying layer on surface of a heterogeneous catalyst, wherein the surface of the heterogeneous catalyst is modified, which causes surface functionalization of the heterogeneous catalyst, and wherein the heterogeneous catalyst is bimetallic catalyst or polymetallic catalyst. 2. A modified heterogeneous catalyst as claimed in claim 1 , wherein the modifying layer on the surface of the heterogeneous catalyst has a thickness ranging from about 6 nm to about 12 nm and wherein the modifying layer is aluminium oxide. 3. The modified heterogeneous catalyst as claimed in claim 1 , wherein the polymetallic catalyst is selected from a group comprising platinum-tin-iridium catalyst, platinum-tin-rhodium catalyst, platinum-tin-ruthenium catalyst, platinum-tin catalyst, platinum-rhenium catalyst and platinum-germanium catalyst. 4. The modified heterogeneous catalyst as claimed in claim 1 , wherein the modifying layer of the heterogeneous catalyst prevents carbon deposition of more than 2 wt % on surface of the heterogeneous catalyst per kg of a feed in a reaction selected from a group comprising oxidative dehydrogenation reaction and naphtha reforming reaction.
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