Systems and processes for conversion of ethylene feedstocks to hydrocarbon fuels
US-2017218283-A1 · Aug 3, 2017 · US
US12042787B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12042787-B2 |
| Application number | US-201917297522-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 29, 2019 |
| Priority date | Nov 30, 2018 |
| Publication date | Jul 23, 2024 |
| Grant date | Jul 23, 2024 |
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In the present disclosure, a heterogeneous nickel-based oligomerization catalyst in which nickel in the form of single atom is loaded on an Al-mesoporous silicate support by ion exchange and a method for producing the same, and a method for oligomerizing light olefins, specifically C4 olefins using the catalyst are described.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a heterogeneous oligomerization catalyst, the method comprising: a) providing a Na-type Al-mesoporous silicate having a Si/Al atomic ratio in a range of 5 to 20 as a support, wherein aluminum (Al) forms acid sites on the mesoporous silicate and Na + ions are bound to the acid sites; b) ion exchanging the Na + ions bound to the acid sites of the Na-type Al-mesoporous silicate with nickel ions using a nickel compound having an oxidation number of 2+, wherein the nickel ions are exchanged with the bound Na + ions, thereby being bound to the Al-mesoporous silicate; and c) performing heat treatment of the Al-mesoporous silicate containing the exchanged nickel ion, wherein nickel is supported on the support in a form of single atom of Ni and an amount of nickel supported is in a range of 0.1% to 10% by weight, wherein an acid amount of the catalyst is less than 50 μmol/g, and wherein a molar ratio of nickel (Ni)/aluminum (Al) is in a range of 0.3 to 1. 2. The method according to claim 1 , wherein at least 95% of Na + ions bound to acid sites of the Na-type Al-mesoporous silicate is exchanged with a nickel ion in the step b). 3. The method according to claim 1 , wherein the Al-mesoporous silicate is at least one selected from an AlMCM-based silicate or an AlSBA-based silicate. 4. The method according to claim 3 , wherein the Al-mesoporous silicate is at least one selected from AlMCM-48 or AlMCM-41. 5. The method according to claim 1 , wherein the Al-mesoporous silicate has a specific surface area (BET) of 200 to 1200 m 2 /g, a pore volume of 0.3 to 0.6 cc/g, and an average pore diameter of 18 to 40 Å. 6. The method according to claim 1 , wherein the nickel compound having an oxidation number of 2+is at least one selected from the group consisting of nickel nitrate, nickel sulfate, nickel phosphate, nickel halide, nickel carboxylate, nickel hydroxide, and nickel carbonate. 7. The method according to claim 1 , wherein a nickel concentration in an aqueous solution of the nickel compound having an oxidation number of 2+used during the ion exchange in the step b) is in a range of 0.01 to 10 M. 8. The method according to claim 7 , wherein ion exchange in the step b) is performed at 50° C. to 100° C. 9. The method according to claim 1 , wherein the step c) is carried out at 250° C. to 1000° C. in an oxygen-containing atmosphere. 10. The method according to claim 1 , wherein the step b) is carried out by directly ion exchanging the Na + ions of the Na-type Al-mesoporous silicate with nickel ions without passing through an exchange with ammonium ions. 11. The method according to claim 1 , wherein the oligomerization catalyst has a specific surface area (BET) of 150 to 1000 m 2 /g, a pore volume of 0.2 to 0.5 cc/g, and an average pore diameter of 10 to 35 Å. 12. The method according to claim 1 , wherein a particle size (diameter) of the oligomerization catalyst is in a range of 1 to 500 μm. 13. The method according to claim 1 , wherein the oligomerization catalyst substantially free of nickel oxide (NiO).
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Iron group metals or copper · CPC title
2-50 nm · CPC title
less than 0.5 ml/g · CPC title
more than 1000 m2/g · CPC title
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