IP Library Granted Patent US 10,722,833
Granted Patent B2
US 10,722,833 · App. 16/128,585 · Granted Jul 28, 2020

Purification process

Inventors: Colin Baptist (North Yorkshire, GB); Claire Cahill (Cleveland, GB); Matthew John Cousins (Lancashire, GB); David Davis (County Durham, GB); Michelle Taylor Wilson (Cleveland, GB); Christopher John Young (Cleveland, GB)
Assignee: Johnson Matthey Public Limited Company
B01D53/02B01D15/00B01D15/10B01D15/1871C01B7/0718C01B7/093C07C7/12B01D2256/16B01D2256/24B01D2257/204B01D2257/206B01D2257/2045B01D2257/2064B01D2259/402B01D2259/414Y02P20/154
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Quick Facts
Patent No.
US 10,722,833
App. No.
16/128,585
Granted
Jul 28, 2020
Kind
B2
Abstract

A process is described for removing halogen compounds, particularly chlorine compounds, from a process fluid, comprising the steps of (i) passing a process fluid containing hydrogen halide over a first sorbent to remove hydrogen halide and generate a hydrogen halide depleted process fluid and then, (ii) passing the hydrogen halide depleted process fluid over a second different sorbent to remove organic halide compounds therefrom. A purification system suitable for removing hydrogen halide and organic halide compounds from process fluids is also described.

Claims (26)

1. A process for removing a halogen compound from a process fluid, comprising the steps of:

(i) passing a process fluid containing hydrogen halide over a first sorbent comprising an alkalized alumina to remove hydrogen halide and generate a hydrogen halide depleted process fluid; and then

(ii) passing the hydrogen halide depleted process fluid over a second sorbent comprising zeolite 13X to remove an organic halide compound.

2. The process of claim 1 , wherein the process fluid is a hydrogen gas stream comprising 50% vol or greater of hydrogen.

3. The process of claim 1 , wherein the process fluid is a liquid stream comprising a hydrocarbon or a gas stream comprising a hydrocarbon.

4. The process of claim 1 , wherein the process fluid is a liquid stream comprising a hydrocarbon.

5. The process of claim 1 , wherein the halogen compound is a bromine compound or a chlorine compound.

6. The process of claim 5 , wherein the halogen compound is a chlorine compound.

7. The process of claim 1 , wherein the hydrogen halide content of the process fluid fed to the first sorbent is in the range of from 0.1 to 20 ppm.

8. The process of claim 1 , wherein the first sorbent comprises acidic sites that form one or more organic halide compounds.

9. The process of claim 1 , wherein the process fluid from step (ii) is passed over a third sorbent to remove residual or formed hydrogen halide.

10. The process of claim 9 , wherein the third sorbent is the same as the first sorbent.

11. The process of claim 1 , wherein the temperature is in a range of from 0° C. to 300° C.

12. The process of claim 11 , wherein the temperature is in a range of from 0° C. to 200° C.

13. The process of claim 12 , wherein the temperature in a range of from 10° C. to 100° C.

14. The process of claim 1 , wherein the pressure is in a range of from 1 to 100 bar abs.

15. The process of claim 14 , wherein the pressure is in a range of from 1 to 40 bar abs.

16. A purification system for removing a halogen compound from a process fluid, the system comprising:

a first sorbent that removes hydrogen halide from said process fluid to generate a hydrogen halide depleted process fluid; and

a second sorbent downstream of said first sorbent that removes the organic halide compound from the hydrogen halide depleted process fluid,

wherein:

the first sorbent comprises pellets, granules or extrudates comprising an alkalised alumina, and the second sorbent comprises pellets, granules or extrudates comprising zeolite 13X.

17. The purification system of claim 16 , wherein the first sorbent comprises acidic sites and forms one or more organic halide compounds.

18. The purification system of claim 16 , further comprising a third sorbent downstream of the second sorbent, wherein the third sorbent removes hydrogen halide from the process fluid.

19. The purification system of claim 18 , wherein the third sorbent is the same as the first sorbent.

20. The purification system of claim 16 , wherein the first and second sorbents are in the same vessel.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 26, 2025
From: JOHNSON MATTHEY PLC
To: JOHNSON MATTHEY DAVY TECHNOLOGIES LIMITED
Reel/Frame 072941/0488 →
Priority Claims (1)
GB 1116801.01 · Sep 29, 2011 · national
Continuity (2)
Continuation 14346880
Related Publication 20190009206A1 · Jan 10, 2019