Hydroprocessing catalyst prepared with waste catalyst fines and its use
US-9211536-B2 · Dec 15, 2015 · US
US2019388877A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2019388877-A1 |
| Application number | US-201916388463-A |
| Country | US |
| Kind code | A1 |
| Filing date | Apr 18, 2019 |
| Priority date | Jun 26, 2018 |
| Publication date | Dec 26, 2019 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A hydroprocessing catalyst has been developed. The catalyst is a crystalline transition metal molybdotungstate material. The hydroprocessing using the crystalline ammonia transition metal molybdotungstate material may include hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking.
Opening claim text (preview).
1 . A crystalline transition metal molybdotungstate material having the formula: (NH 4 ) m M(OH) n Mo x W y O z where ‘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 0.5; ‘y’ varies from 0.4 to 1.75; and ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; 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 (%) 10.45 vs 9.79 m 8.05 w 6.97 w 5.83 m 5.03 m 4.96 m 4.87 m 4.49 m 2 . The crystalline transition metal molybdotungstate material of claim 1 wherein the 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 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 crystalline transition metal molybdotungstate material of claim 1 wherein M is nickel or zinc. 5 . The crystalline transition metal molybdotungstate material of claim 1 wherein M is nickel. 6 . A method of making a crystalline transition metal molybdotungstate material having the formula: (NH 4 ) m M(OH) n Mo x W y O z where ‘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 0.5; ‘y’ varies from 0.4 to 1.75; and ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; 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 (%) 10.45 vs 9.79 m 8.05 w 6.97 w 5.83 m 5.03 m 4.96 m 4.87 m 4.49 m the method comprising: a. forming a reaction mixture containing H 2 O, sources of NH 3 , M, W, and Mo; b. reacting the reaction mixture at a temperature from about 60° C. to about 120° C.; c. recovering the crystalline transition metal molybdotungstate material. 7 . The method of claim 6 further comprising removing at least some of the H 2 O, NH 3 , or a combination thereof to form an intermediate before reacting the reaction mixture. 8 . The method of claim 6 wherein the reacting is conducted at a temperature of from 60° C. to about 120° C. for a period of time of 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 drying the recovered crystalline transition metal molybdotungstate material at a temperature from about 100° C. to about 350° C. for about 30 minutes to about 48 hours. 11 . The method of claim 6 further comprising adding a binder to the recovered crystalline transition metal molybdotungstate material. 12 . The method of claim 11 wherein the binder is selected from the group consisting of aluminas, silicas, and alumina-silicas. 13 . The method of claim 6 further comprising decomposing the recovered crystalline transition metal molybdotungstate material by sulfidation to form metal sulfides. 14 . A conversion process comprising contacting a material with a sulfiding agent to convert at least a portion of the material to metal sulfides and contacting the metal sulfides with a feed at conversion conditions to generate at least one product, wherein the material comprises a crystalline transition metal molybdotungstate material having the formula: (NH 4 ) m M(OH) n Mo x W y O z where ‘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 0.5; ‘y’ varies from 0.4 to 1.75; and ‘z’ is a number which satisfies the sum of the valency of the cationic species present in the material; the material further characterized by a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A: TABLE A
by unit-cell parameters, atom positions or structure diagrams · CPC title
by peak-intensities or a ratio thereof only · CPC title
one element only · CPC title
containing elements as dopants · CPC title
Complex oxides containing nickel and at least one other metal element · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.