IP Library Granted Patent US 10,569,251
Granted Patent B2
US 10,569,251 · App. 15/342,902 · Granted Feb 25, 2020

Desulphurisation material comprising copper supported on zinc oxide

Inventors: Norman Macleod (Tyne and Wear, GB); Gordon Edward Wilson (Cleveland, GB)
Assignee: Johnson Matthey Public Limited Company
B01J20/0244B01D53/14B01D53/52B01D53/82B01J20/28004B01J20/28059B01J20/28071B01J23/80B01J35/002B01J35/023B01J35/1014B01J35/1038B01J37/0063B01J37/04B01D53/86B01D2253/1124B01D2253/25B01D2253/304B01D2253/306B01D2253/311B01D2255/20761B01D2255/20792B01D2256/24B01D2256/245B01D2257/304B01D2257/306B01D2257/308Y10T428/2982
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Quick Facts
Patent No.
US 10,569,251
App. No.
15/342,902
Granted
Feb 25, 2020
Kind
B2
Abstract

A particulate desulfurization material includes one or more copper compounds supported on a zinc oxide support material, wherein the desulfurization material has a copper content in the range 0.1 to 5.0% by weight and a tapped bulk density ≥1.55 kg/l. The material is obtained by (i) mixing a powdered copper compound with a particulate zinc support material comprising zinc oxide and one or more precursors that form zinc oxide upon calcination, and one or more binders to form a copper-containing composition, (ii) shaping the copper-containing composition by granulation, and (iii) drying and calcining the resulting granulated material.

Claims (17)

1. A particulate desulphurisation material comprising one or more copper compounds supported on a particulate zinc oxide support material and not including a compound of nickel, wherein the desulphurisation material is in the form of granules formed from one or more powdered copper compounds, zinc oxide, and one or more binders, and has a copper content, expressed as CuO, in the range of from 0.1 to 5.0% by weight and a tapped bulk density of 1.55 kg/1 or greater.

2. The desulphurisation material of claim 1 , wherein the desulphurisation material has a particle size in the range of from 1 to 10 mm.

3. The desulphurisation material of claim 1 , wherein the desulphurisation material has a pore volume of 0.22 cm 3 /g or less.

4. The desulphurisation material of claim 1 , wherein the desulphurisation material has a BET surface area of 23 m 2 /g or less.

5. The desulphurisation material of claim 1 , wherein the one or more copper compounds are copper metal, copper oxide, copper hydroxide, or copper hydroxycarbonate.

6. The desulphurisation material of claim 1 , wherein the one or more binders are a clay binder, cement binder, or a mixture thereof.

7. The desulphurisation material of claim 1 , wherein the desulphurisation material further comprises a second support material that is one or more refractory oxide at a level up to 20% by weight.

8. The desulphurisation material of claim 1 , wherein the desulphurisation material further comprises a second metal compound that is one or more compounds of iron, manganese, or cobalt.

9. The desulphurisation material of claim 1 , wherein the zinc oxide support material includes zinc oxide formed by calcining one or more zinc oxide precursors.

10. The desulphurisation material of claim 1 , wherein the desulphurisation material has a particle size in the range of from 1.5 to 7.5 mm.

11. The desulphurisation material of claim 1 , wherein the desulphurisation material has a particle size in the range of from 2.5 to 5.0 mm.

12. A process for desulphurizing a process fluid stream comprising contacting the stream, and optionally hydrogen, with the desulphurization material of claim 1 .

13. The process of claim 12 , wherein the process stream comprises a hydrocarbon gas and hydrogen.

14. The process of claim 12 , wherein the process fluid stream is mixed with hydrogen and contacted with a hydrodesulphurisation catalyst to form a treated process stream, and then the treated process stream is contacted with the desulphurisation material.

15. The process of claim 12 , wherein the desulphurisation material is contacted with the process fluid at a temperature in the range of from 250 to 450° C.

16. The process of claim 12 , wherein the desulphurisation material is contacted with the process fluid at a temperature in the range of from 300-400° C.

17. The process of claim 12 , wherein the desulphurisation material is contacted with the process fluid at a temperature in the range of from 320-400° C.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 26, 2025
From: JOHNSON MATTHEY PLC
To: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
Reel/Frame 072941/0488 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 3, 2016
From: MACLEOD, NORMAN; WILSON, GORDON EDWARD
To: JOHNSON MATTHEY PUBLIC LIMITED COMPANY
Reel/Frame 040217/0551 →
Priority Claims (1)
GB 1112606.7 · Jul 22, 2011 · national
Continuity (2)
Division 14233217
Related Publication 20170072381A1 · Mar 16, 2017