Crystalline transition metal molybdotungstate

Patent metadata

Field	Value
Publication number	US-10392571-B2
Application number	US-201816037849-A
Country	US
Kind code	B2
Filing date	Jul 17, 2018
Priority date	Dec 15, 2015
Publication date	Aug 27, 2019
Grant date	Aug 27, 2019

Abstract

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

First claim

The invention claimed is:

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 transition metal molybdotungstate material having the formula:
(NH 4 ) a MMo x W y O z

where ‘a’ varies from 0.1 to 3; ‘M’ is a metal selected from Mg, Mn, Fe, Co, Ni, Cu, Zn, and combinations thereof; ‘x’ is from 0.1 to 5; ‘y’ is from 1 to 10; the sum of (x+y) is ≤10.1 and z is a number which satisfies the sum of the valences of a, M, x and y; the material having a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A:

TABLE A

d (Å)
I0/I %

9.67-9.49
vs

9.09-8.94
m

8.18-8.13
m

8.22-10.91
w

5.05-5.0
m

4.96-4.91
m

4.80-4.76
m

4.51-4.47
w

4.09-4.05
w

3.84-3.81
w

3.74-3.68
m

3.60-3.55
w.

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

3. The process of claim 1 wherein the conversion 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 transition metal molybdotungstate material, or the decomposition product, or both 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 transition metal molybdotungstate material with the sulfur containing feed.

7. The process of claim 1 wherein the decomposition by sulfidation comprises contacting the crystalline 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 catalyst comprising the decomposition product of the decomposition by sulfidation of a crystalline transition metal molybdotungstate material having the formula:
(NH 4 ) a MMo x W y O z

where ‘a’ varies from 0.1 to 3; ‘M’ is a metal selected from Mg, Mn, Fe, Co, Ni, Cu, Zn, and combinations thereof; ‘x’ is from 0.1 to 5; ‘y’ is from 1 to 10; the sum of (x+y) is ≤10.1 and z is a number which satisfies the sum of the valences of a, M, x and y; the material having a x-ray powder diffraction pattern showing peaks at the d-spacings listed in Table A:

TABLE A

d (Å)
I0/I %

9.67-9.49
vs

9.09-8.94
m

8.18-8.13
m

8.22-10.91
w

5.05-5.0
m

4.96-4.91
m

4.80-4.76
m

4.51-4.47
w

4.09-4.05
w

3.84-3.81
w

3.74-3.68
m

3.60-3.55
w

the method comprising:
(a) forming a reaction mixture containing NH 3 , H 2 O, and sources of M, Mo and W;
(b) adjusting the pH of the reaction mixture to a pH of from around 8.5 to about 10;
(c) heating the reaction mixture at temperatures from about 30° C. to about 100° C. until the resultant pH is from about 8 and about 9;
(d) recovering the crystalline transition metal molybdotungstate material; and
(e) decomposing the recovered crystalline transition metal molybdotungstate material by sulfidation to generate at least one decomposition product.

12. The method of claim 11 wherein the reacting is conducted at a temperature of from about 30° C. to about 130° C. for a period of time from about 30 minutes to 14 days.

13. The method of claim 11 wherein the recovering is by filtration, centrifugation or drying.

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

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

Assignees

• Uop Llc

Inventors

• Miller Stuart
• Collins Laura

Classifications

• B01J2523/00

  Constitutive chemical elements of heterogeneous catalysts · CPC title

• B01J27/19

  Molybdenum · 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

• B01J21/04

  Alumina · CPC title