Process and apparatus for treating a sour synthesis gas

Patent metadata

Field	Value
Publication number	US-10399852-B2
Application number	US-201715593156-A
Country	US
Kind code	B2
Filing date	May 11, 2017
Priority date	May 11, 2017
Publication date	Sep 3, 2019
Grant date	Sep 3, 2019

Abstract

Processes and apparatuses for treating a sour synthesis gas are provided. The process comprises passing the sour synthesis gas stream to an acid gas removal unit to provide a treated synthesis gas stream and a CO 2 rich stream. At least a portion of the CO 2 rich stream is passed to a thermal oxidizer unit to provide a treated CO 2 gas stream. At least a portion of the treated synthesis gas stream is passed to a pressure swing adsorption unit to obtain a purified hydrogen stream and a tail gas stream. At least a portion of the tail gas stream is passed to the thermal oxidizer unit.

First claim

The invention claimed is:

1. An integrated process for treating a sour synthesis gas and recovering one or more acidic gases comprising CO 2 present in the sour synthesis gas, the process comprising:
(a) passing a sour synthesis gas stream to an acid gas removal unit to provide a treated synthesis gas stream and a CO 2 rich stream;
(b) passing at least a portion of the CO 2 rich stream to a thermal oxidizer unit to provide a treated CO 2 gas stream;
(c) passing at least a portion of the treated synthesis gas stream to a pressure swing adsorption unit to obtain a purified hydrogen stream and a tail gas stream; and
(d) passing at least a portion of the tail gas stream obtained from the pressure swing adsorption unit to the thermal oxidizer unit, further comprising passing a flue gas produced in the thermal oxidizer unit to a waste heat recovery unit, and further comprising passing at least a portion of steam recovered from the waste heat recovery unit to the acid gas removal unit.

2. The process of claim 1 further comprising obtaining a hydrogen sulfide rich stream from the acid gas removal unit and passing the hydrogen sulfide rich stream to a sulfur recovery unit to recover one or more sulfur compounds.

3. The process of claim 1 wherein one or more impurities comprising carbon monoxide and hydrogen present in the CO 2 rich stream are removed via oxidation in the thermal oxidizer unit.

4. The process of claim 1 further comprising obtaining the sour synthesis gas from partial oxidation of a hydrocarbon containing feedstock.

5. The process of claim 1 wherein the tail gas stream being passed to the thermal oxidizer unit is of reduced pressure.

6. The process of claim 1 further comprising controlling one or more operating parameters of the acid gas removal unit and the pressure swing adsorption unit to maximize an amount of purified hydrogen stream produced.

7. The process of claim 1 further comprising minimizing an amount of an external fuel gas being provided to the thermal oxidizer and maximizing the amount of the tail gas stream being provided to the thermal oxidizer unit via one or more control modules.

8. The process of claim 1 further comprising maximizing the amount of steam recovered from the waste heat recovery unit via a steam recovery module.

9. An integrated process for treating a sour synthesis gas and recovering one or more gases comprising CO 2 present in the sour synthesis gas, the process comprising:
(a) passing a sour synthesis gas stream to an acid gas removal unit to provide a treated synthesis gas stream and a CO 2 rich stream;
(b) passing at least a portion of the CO 2 rich stream to a thermal oxidizer unit to provide a treated CO 2 gas stream;
(c) passing a flue gas produced in the thermal oxidizer unit to a waste heat recovery unit;
(d) passing at least a portion of steam recovered from the waste heat recovery unit to the acid gas removal unit; and
(e) passing at least a portion of the treated synthesis gas stream to a pressure swing adsorption unit to obtain a purified hydrogen stream and a tail gas stream.

10. The process of claim 9 further comprising passing at least a portion of the tail gas stream to the thermal oxidizer unit.

11. The process of claim 9 wherein the tail gas stream being passed to the thermal oxidizer unit is of reduced pressure.

12. The process of claim 9 further comprising obtaining a hydrogen sulfide rich stream from the acid gas removal unit and passing the hydrogen sulfide rich stream to a sulfur recovery unit to recover one or more sulfur compounds.

13. The process of claim 9 wherein one or more impurities comprising carbon monoxide and hydrogen present in the CO 2 rich stream are removed via oxidation in the thermal oxidizer unit.

14. The process of claim 9 further comprising obtaining the sour synthesis gas from partial oxidation of a hydrocarbonaceous fuel.

15. An integrated process for treating a sour synthesis gas and recovering one or more gases comprising CO 2 present in the sour synthesis gas, the process comprising:
(a) passing a sour synthesis gas stream to an acid gas removal unit to provide a treated synthesis gas stream and a CO 2 rich stream;
(b) passing at least a portion of the CO 2 rich stream to a thermal oxidizer unit to provide a treated CO 2 gas stream;
(c) passing a flue gas produced in the thermal oxidizer unit to a waste heat recovery unit;
(d) passing at least a portion of steam recovered from the waste heat recovery unit to the acid gas removal unit;
(e) passing at least a portion of the treated synthesis gas stream to a pressure swing adsorption unit to obtain a purified hydrogen stream and a tail gas stream; and
(f) passing at least a portion of the tail gas stream to the thermal oxidizer unit.

16. The process of claim 15 wherein the tail gas stream being passed to the thermal oxidizer unit is of reduced pressure.

17. The process of claim 15 further comprising obtaining a hydrogen sulfide rich stream from the acid gas removal unit and passing the hydrogen sulfide rich stream to a sulfur recovery unit to recover one or more sulfur compounds.

18. The process of claim 15 wherein one or more impurities comprising carbon monoxide and hydrogen present in the CO 2 rich stream are removed via oxidation in the thermal oxidizer unit.

Assignees

• Uop Llc

Inventors

• De Ren Jan
• Beuckels Bart J T
• Whyman William J

Classifications

• B01D2257/408

  Cyanides, e.g. hydrogen cyanide (HCH) · CPC title

• B01D2257/306

  Organic sulfur compounds, e.g. mercaptans · CPC title

• B01D2257/108

  Hydrogen · CPC title

• B01D2256/24

  Hydrocarbons · CPC title

• B01D2252/20468

  containing a pyrrolidone-ring · CPC title