Crystalline ammonia transition metal molybdotungstate

Patent metadata

Field	Value
Publication number	US-2018318809-A1
Application number	US-201816037667-A
Country	US
Kind code	A1
Filing date	Jul 17, 2018
Priority date	Dec 15, 2015
Publication date	Nov 8, 2018
Grant date	—

Abstract

A hydroprocessing catalyst or catalyst precursor has been developed. The catalyst is a unique crystalline ammonia transition metal molybdotungstate material. The hydroprocessing using the crystalline ammonia transition metal molybdotungstate material or a decomposition product thereof may include hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking.

First claim

1 . A conversion process comprising contacting a feed with a catalyst at conversion conditions to give at least one product, the catalyst comprising the decomposition product of the decomposition by sulfidation of a crystalline ammonia transition metal molybdotungstate material having the formula:
(NH 4 ) 2 .(NH 3 ) a (H 2 O) 2-a MMo x W y O z
where ‘M’ is a metal selected from Mg, Mn, Fe, Co, Ni, Cu, Zn and combinations thereof; ‘a’ varies from 0 to 2; ‘x’ varies from 1.5 to 3; ‘y’ varies 0.01 to 0.5; the sum of (x+y) is ≤3; z is a number which satisfies the sum of the valences of [(M+x+y)+2]; the material having a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A:

TABLE A

d (Å)
I 0 /I

6.99
m

6.30
w

5.81
vs

5.36
m

5.05
w

4.79
m

4.43
w

4.10
w

3.95
w

3.79
m

3.69
m

3.50
m

2 . The process of claim 1 wherein the conversion process is hydroprocessing.

3 . The process of claim 1 wherein the hydroprocessing process is selected from the group consisting of hydrodenitrification, hydrodesulfurization, hydrodemetallation, hydrodesilication, hydrodearomatization, hydroisomerization, hydrotreating, hydrofining, and hydrocracking.

4 . The process of claim 1 wherein the crystalline ammonia transition metal molybdotungstate material is present in a mixture with at least one binder and wherein the mixture comprises up to 25 wt % binder.

5 . The process of claim 4 wherein the binder is selected from the group consisting of silicas, aluminas, and silica-aluminas.

6 . The process of claim 1 wherein the feed comprises sulfur and the decomposition by sulfidation comprises contacting the crystalline ammonia transition metal molybdotungstate material with the sulfur containing feed.

7 . The process of claim 1 wherein the decomposition by sulfidation comprises contacting the crystalline ammonia transition metal molybdotungstate material with a gaseous mixture of H 2 S/H 2 .

8 . The process of claim 1 wherein the sulfidation is conducted at a temperature ranging from about 50° C. to about 600° C.

9 . The process of claim 1 wherein the sulfidation is conducted at a temperature ranging from about 150° C. to about 500° C.

10 . The process of claim 1 wherein the sulfidation is conducted at a temperature ranging from about 250° C. to about 450° C.

11 . A method of making a crystalline ammonia transition metal molybdotungstate material having the formula:
(NH 4 ) 2 .(NH 3 ) a (H 2 O) 2-a MMo x W y O z
where ‘M’ is a metal selected from Mg, Mn, Fe, Co Ni, Cu, Zn and mixtures thereof; ‘a’ varies from 0 to 2; ‘x’ varies from 1.5 to 3; ‘y’ varies 0.01 to 0.5; the sum of (x+y) is ≤3; z is a number which satisfies the sum of the valences of [(M+x+y)+2]; the material having a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A:

TABLE A

d (Å)
I 0 /I

6.99
m

6.30
w

5.81
vs

5.36
m

5.05
w

4.79
m

4.43
w

4.10
w

3.95
w

3.79
m

3.69
m

3.50
m

the method comprising:
(a) forming a reaction mixture containing NH 3 , H 2 O, and sources of M, W, and Mo;
(b) adjusting the pH of the reaction mixture to a pH of from about 8 to about 10; and
(c) recovering the crystalline ammonia transition metal molybdotungstate material.

12 . The method of claim 11 wherein the recovering is by filtration or centrifugation or evaporation of solvent.

13 . The method of claim 11 further comprising adding a binder to the recovered crystalline ammonia transition metal molybdotungstate material.

14 . The method of claim 13 wherein the binder is selected from the group consisting of aluminas, silicas, and alumina-silicas.

15 . The method of claim 11 further comprising adding at least one binder to the crystalline ammonia transition metal molybdotungstate material wherein the combination of material and binder comprises up to 25 wt % binder.

16 . The method of claim 11 further comprising decomposing the recovered crystalline ammonia transition metal molybdotungstate material by sulfidation to generate at least one decomposition product.

Assignees

• Uop Llc

Inventors

• Miller Stuart
• Collins Laura

Classifications

• B01J37/009

  Preparation by separation, e.g. by filtration, decantation, screening · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C10G47/04

  Oxides · CPC title

• B01J37/0009

  Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst · CPC title

• B01J37/20

  Sulfiding · CPC title