Hydroprocessing catalyst prepared with waste catalyst fines and its use
US-9211536-B2 · Dec 15, 2015 · US
US2020001282A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020001282-A1 |
| Application number | US-201916388357-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 18, 2019 |
| Priority date | Jun 29, 2018 |
| Publication date | Jan 2, 2020 |
| Grant date | — |
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A hydroprocessing catalyst or catalyst precursor has been developed. The catalyst is a poorly crystalline transition metal molybdotungstate material or a metal sulfide decomposition product thereof. The hydroprocessing using the crystalline ammonia transition metal molybdotungstate material may include hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking.
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1 . A poorly crystalline transition metal molybdotungstate material having the formula: A m M(OH) n (Mo) x (W) y O z .(NH 3 ) h (H 2 O) i where ‘A’ is selected from NH 4 + , H 3 O + or combinations thereof, m varies from 0.001 to 2; ‘n’ varies from 0.001 to 2; ‘M’ is a metal selected from Mn, Fe, Co, Ni, V, Cu, Zn and combinations thereof; ‘x’ varies from 0.001 to 2; ‘y’ varies from 0.4 to 3; ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; ‘h’ varies from 0 to m; and ‘i’ varies from 0 to m; the material further characterized by a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A: TABLE A d (Å) I/I 0 (%) 6.5 w 3.75 vs 3.3 vs 2.73 m 2.45 w 1.91 w 2 . The poorly crystalline transition metal molybdotungstate material of claim 1 wherein the poorly crystalline transition metal molybdotungstate material is present in a mixture with at least one binder and wherein the mixture comprises up to 25 wt-% binder. 3 . The poorly crystalline transition metal molybdotungstate material of claim 2 wherein the binder is selected from the group consisting of silicas, aluminas, and silica-aluminas. 4 . The poorly crystalline transition metal molybdotungstate material of claim 1 wherein M is nickel or zinc. 5 . The poorly crystalline transition metal molybdotungstate material of claim 1 wherein M is nickel. 6 . A method of making a poorly crystalline transition metal molybdotungstate material having the formula: A m M(OH) n (Mo) x (W) y O z .(NH 3 ) h (H 2 O) i where ‘A’ is selected from NH 4 + , H 3 O + or combinations thereof, m varies from 0.001 to 2; ‘n’ varies from 0.001 to 2; ‘M’ is a metal selected from Mn, Fe, Co, Ni, V, Cu, Zn and combinations thereof; ‘x’ varies from 0.001 to 2; ‘y’ varies from 0.4 to 3; ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; ‘h’ varies from 0 to m; and ‘i’ varies from 0 to m; the material further characterized by a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A: TABLE A d (Å) I/I 0 (%) 6.5 w 3.75 vs 3.3 vs 2.73 m 2.45 w 1.91 w the method comprising: b. forming a reaction mixture containing NH 4 + , H 3 O + or combinations thereof, and sources of M, W, and Mo; c. reacting the mixture from about 90° C. to about 350° C. in an autogenous environment to form a reaction product; d. recovering the reaction product; and e. drying the recovered product at a temperature from about 100° C. to about 350° C. for about 30 minutes to about 48 hours to generate the poorly crystalline transition metal molybdotungstate material. 7 . The method of claim 6 further comprising removing at least some of the NH 4 + , H 3 O + , or a combination thereof to form an intermediate before reacting the mixture at a temperature from about 90° C. to about 350° C. in an autogenous environment 8 . The method of claim 6 wherein the reacting is conducted for a period from about 30 minutes to 14 days. 9 . The method of claim 6 wherein the recovering is by filtration or centrifugation. 10 . The method of claim 6 further comprising adding a binder to the poorly crystalline transition metal molybdotungstate material. 11 . The method of claim 10 wherein the binder is selected from the group consisting of aluminas, silicas, and alumina-silicas. 12 . The method of claim 6 further comprising decomposing the transition metal molybdotungstate material by sulfidation to form metal sulfides. 13 . A conversion process comprising contacting a material with a sulfiding agent to convert at least a portion of the material to a metal sulfide and contacting the metal sulfide with a feed at conversion conditions to give at least one product, the material comprising a poorly crystalline transition metal molybdotungstate material having the formula: A m M(OH) n (Mo) x (W) y O z .(NH 3 ) h (H 2 O) i where ‘A’ is selected from NH 4 + , H 3 O + or combinations thereof, m varies from 0.001 to 2; ‘n’ varies from 0.001 to 2; ‘M’ is a metal selected from Mn, Fe, Co, Ni, V, Cu, Zn and combinations thereof; ‘x’ varies from 0.001 to 2; ‘y’ varies from 0.4 to 3; ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; ‘h’ varies from 0 to m; and ‘i’ varies from 0 to m; the material further characterized by a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A: TABLE A d (Å) I/I 0 (%)
in combination with chromium, molybdenum, or tungsten metals, or compounds thereof · CPC title
containing also molybdenum · CPC title
Precipitation · CPC title
Mixed salts · CPC title
by d-values or two theta-values, e.g. as X-ray diagram · CPC title
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