Hydrocracking catalyst for hydrocarbon oil, method for producing hydrocracking catalyst, and method for hydrocracking hydrocarbon oil with hydrocracking catalyst
US-9221036-B2 · Dec 29, 2015 · US
US2017239648A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017239648-A1 |
| Application number | US-201615048535-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 19, 2016 |
| Priority date | Feb 19, 2016 |
| Publication date | Aug 24, 2017 |
| Grant date | — |
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The present disclosure relates to a process for producing a finely divided metal-doped aluminogallate nanocomposite comprising mixing a carrier solvent with a bulk metal-doped aluminogallate nanocomposite to form a bulk metal-doped aluminogallate slurry and atomizing the bulk metal-doped aluminogallate slurry using a low temperature collision to produce a finely divided metal-doped aluminogallate nanocomposite, the composition of a nickel-doped aluminogallate nanocomposite (GAN), and a method of NO decomposition using the nickel-doped aluminogallate nanocomposite.
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1 : A process for producing a finely divided metal-doped aluminogallate nanocomposite comprising: mixing a carrier solvent with a bulk metal-doped aluminogallate nanocomposite synthesized by a process selected from the group consisting of co-precipitation, sol-gel, and hydrothermal to form a bulk metal-doped aluminogallate slurry, wherein the bulk metal-doped aluminogallate nanocomposite comprises: Ga 2 O 3 ; Al 2 O 3 ; and at least one metal oxide dopant comprising a metal selected from the group consisting of Cr, Mn, Fe, Co, Ni, Cu, Zn, Ag, Au, Pd, Pt, Ru, Rh, In, Ir, Tl, Ge, and Sn; and atomizing the bulk metal-doped aluminogallate slurry using a collision to produce the finely divided metal-doped aluminogallate nanocomposite; wherein the carrier solvent is at least one selected from the group consisting of deionized water, ethanol, butanol, isopropyl alcohol, diacetone alcohol, diglycol, triglycol, acetone, methyl ethyl ketone, ethyl acetate, butyl acetate, toluene, and xylene. 2 : The process of claim 1 , wherein the bulk metal-doped aluminogallate is synthesized by a hydrothermal process comprising: adding a precipitating agent to an aqueous solution comprising a gallium salt, an aluminum salt, and a metal dopant salt to form a metal-doped aluminogallate suspension with a pH of 8-12; and heating the metal-doped aluminogallate suspension to a hydrothermal reaction temperature in a range of 100° C.-350° C., for a reaction time range of 24-100 hrs to form the bulk metal-doped aluminogallate nanocomposite. 3 : The process of claim 1 , wherein the atomizing comprises: injecting the bulk metal-doped aluminogallate slurry into a fluid carrier stream to produce a bulk metal-doped aluminogallate slurry stream; colliding the bulk metal-doped aluminogallate slurry stream with a surface of at least one collision agent within an atomizing unit reaction zone at a flow rate and a sufficient pressure to atomize the bulk metal-doped aluminogallate slurry stream and form the finely divided metal-doped aluminogallate nanocomposite without any heat induced phase transitions. 4 : The process of claim 1 , wherein the bulk metal-doped aluminogallate slurry comprises: 20-45 mol % Ga 2 O 3 ; 35-60 mol % Al 2 O 3 ; and 2-30 mol % metal oxide dopant relative to the total molar composition of the bulk metal-doped aluminogallate nanocomposite. 5 : The process of claim 1 , wherein the metal oxide dopant is nickel oxide. 6 : The process of claim 3 , wherein the atomizing unit is a wet jet atomizer. 7 : The process of claim 3 , wherein the sufficient pressure is 50 MPa-400 MPa. 8 : The process of claim 3 , wherein prior to the colliding the bulk metal-doped aluminogallate slurry stream passes through a nozzle having a nozzle diameter of 50 μm-300 μm. 9 : The process of claim 3 , wherein the flow rate of the bulk metal-doped aluminogallate slurry is 2 L/hr to 840 L/hr. 10 : The process of claim 3 , wherein the at least one collision agent is at least a portion of the bulk metal-doped aluminogallate slurry. 11 : The process of claim 3 , wherein the at least one collision agent is a ceramic ball. 12 : The process of claim 2 , wherein the bulk metal-doped aluminogallate slurry, the finely divided metal-doped aluminogallate nanocomposite or both are not calcined or milled. 13 - 20 . (canceled) 21 : The process of claim 1 , wherein the carrier solvent is ethanol.
Aluminium · CPC title
in the presence of water, e.g. steam · CPC title
Nickel · CPC title
Processes characterised by a specific catalyst · CPC title
to form a gel or a cogel · CPC title
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