Adsorption-based Claus tail gas treatment through regeneration temperature ramping

Patent metadata

Field	Value
Publication number	US-11572274-B2
Application number	US-202117166821-A
Country	US
Kind code	B2
Filing date	Feb 3, 2021
Priority date	Feb 3, 2021
Publication date	Feb 7, 2023
Grant date	Feb 7, 2023

Abstract

A system and method for sulfur recovery, including hydrogenating Claus tail gas, quenching the hydrogenated gas, adsorbing water and hydrogen sulfide from the quenched gas, and regenerating adsorbent with carbon dioxide and/or nitrogen and heating the adsorbent in a regeneration temperature ramp to desorb primarily hydrogen sulfide in a first part of the temperature ramp.

First claim

What is claimed is:

1. A method for sulfur recovery, comprising:
hydrogenating Claus tail gas to produce hydrogenated gas comprising hydrogen sulfide, water, and at least of one of carbon dioxide or nitrogen;
processing the hydrogenated gas in a quench tower to produce quenched gas comprising hydrogen sulfide, water, and at least one of carbon dioxide or nitrogen;
feeding the quenched gas to an adsorbing first-stage adsorption vessel;
adsorbing water from the quenched gas onto first adsorbent in the adsorbing first-stage adsorption vessel to produce a first outlet gas, the first outlet gas comprising hydrogen sulfide and at least one of carbon dioxide or nitrogen;
feeding the first outlet gas to an adsorbing second-stage adsorption vessel;
adsorbing hydrogen sulfide from the first outlet gas onto second adsorbent in the adsorbing second-stage adsorption vessel to produce a second byproduct stream comprising at least one of carbon dioxide or nitrogen;
feeding a first portion of the second byproduct stream as regeneration gas to a regenerating first-stage adsorption vessel; and
heating the regenerating first-stage adsorption vessel in a temperature ramp to selectively desorb components from first adsorbent in the regenerating first-stage adsorption vessel to produce a first byproduct stream comprising desorbed components, wherein the components desorbed during a first part of the temperature ramp comprise primarily hydrogen sulfide.

2. The method of claim 1 , wherein the first byproduct stream further comprises at least one of carbon dioxide or nitrogen, and wherein the first adsorbent and the second adsorbent each comprise a molecular sieve.

3. The method of claim 1 , comprising feeding the first byproduct stream to a reaction furnace of a Claus unit during the first part of the temperature ramp, wherein the first part of the temperature ramp comprises an initial part of the temperature ramp.

4. The method of claim 1 , wherein during a second part of the temperature ramp, the components desorbed from the first adsorbent in the regenerating first-stage adsorption vessel comprise water or concentration of hydrogen sulfide in the first byproduct stream is less than a threshold value, or both, and wherein the second part of the temperature ramp is later in time and at greater temperatures than the first part of the temperature ramp.

5. The method of claim 1 , comprising feeding the first byproduct stream to the quench tower during a second part of the temperature ramp.

6. The method of claim 1 , wherein a first-stage adsorption unit comprises the adsorbing first-stage adsorption vessel and the regenerating first-stage adsorption vessel, wherein the adsorbing first-stage adsorption vessel is a first-stage adsorption vessel operationally in an adsorption cycle, wherein the regenerating first-stage adsorption vessel is a first-stage adsorption vessel operationally in a regeneration cycle, and wherein the first adsorbent comprises molecular sieve 3A.

7. The method of claim 6 , wherein the first-stage adsorption unit comprises a first-stage adsorption vessel operationally in standby, and wherein the second adsorbent comprises molecular sieve 4A.

8. The method of claim 1 , comprising feeding a second portion of the second byproduct stream to a regenerating second-stage adsorption vessel and desorbing hydrogen sulfide from second adsorbent in the regenerating second-stage adsorption vessel into the second portion of the second byproduct stream to produce a second outlet gas comprising hydrogen sulfide.

9. The method of claim 8 , comprising providing the second outlet gas as feed gas for a reaction furnace of a Claus unit that generated the Claus tail gas.

10. The method of claim 1 , wherein a significant portion of the water in the quenched gas is adsorbed onto the first adsorbent in the adsorbing first-stage adsorption vessel, wherein the first adsorbent in the adsorbing first-stage adsorption vessel adsorbs water while passes hydrogen sulfide, carbon dioxide, and nitrogen to form the first outlet gas during an adsorption cycle, and wherein the second adsorbent adsorbs hydrogen sulfide while passes carbon dioxide and nitrogen to form the second byproduct stream during an adsorption cycle.

11. The method of claim 1 , comprising feeding a third portion of the second byproduct stream to a thermal oxidizer, wherein the hydrogenated gas does not comprise sulfur-containing compounds other than hydrogen sulfide, wherein the first outlet gas does not comprise water, and wherein the second byproduct stream does not comprise hydrogen sulfide.

12. The method of claim 1 , wherein hydrogenating the Claus tail gas comprises converting sulfur-containing compounds in the Claus tail gas into hydrogen sulfide in a hydrogenation reactor to produce the hydrogenated gas comprising hydrogen sulfide, water, and at least one of carbon dioxide or nitrogen.

13. The method of claim 1 , wherein hydrogenating the Claus tail gas comprises feeding the Claus tail gas comprising sulfur-containing compounds to a hydrogenation reactor and converting the sulfur-containing compounds in the hydrogenation reactor to hydrogen sulfide to produce the hydrogenated gas comprising hydrogen sulfide, water, and at least one of carbon dioxide or nitrogen.

14. The method of claim 1 , wherein processing the hydrogenated gas in a quench tower comprises feeding the hydrogenated gas to the quench tower, condensing water in the hydrogenated gas in the quench tower, and removing water condensate from the quench tower to produce the quenched gas, and wherein the quenched gas comprises the hydrogenated gas without the water condensate removed.

15. A system for treating Claus tail gas, comprising:
a hydrogenation reactor to receive the Claus tail gas and hydrogenate sulfur-containing compounds in the Claus tail gas into hydrogen sulfide to produce hydrogenated gas comprising hydrogen sulfide, water, and at least one of carbon dioxide or water;
a quench tower to receive the hydrogenated gas and condense water in the hydrogenated gas to produce quenched gas comprising hydrogen sulfide, water, and at least of one carbon dioxide or nitrogen, wherein condensed water is recovered as water condensate from the quench tower;
a first first-stage adsorption vessel to receive in an adsorption cycle the quenched gas and adsorb water from the quenched gas onto first adsorbent to produce a first outlet gas comprising hydrogen sulfide and at least one of carbon dioxide or nitrogen;
a first second-stage adsorption vessel to receive in an adsorption cycle the first outlet gas and adsorb hydrogen sulfide from the first outlet gas onto second adsorbent to produce a second byproduct stream comprising at least one of carbon dioxide or nitrogen; and
a second first-stage adsorption vessel to receive in a regeneration cycle a first portion of the second byproduct stream as regeneration gas and heat first adsorbent in second first-stage adsorption vessel per a temperature ramp to selectively desorb components from the first adsorbent in the second first-stage adsorption vessel to produce a first byproduct stream comprising desorbed components and at least one of carbon dioxide or nitrogen, wherein the components desorbed during a first part of the temperature ramp comprise primarily hydrogen sulfide.

16. The system of claim 15 , wherein the second first-stage adsorption vessel to discharge the first byproduct stream to a reaction furnace of a Claus unit during the first part of the temperature ramp, and wherein the first part of the temperature ramp comprises an initial part of the temperatur

Assignees

• Saudi Arabian Oil Co

Inventors

• Lithoxoos Georgios
• Othman Rashid M
• Alami Ismail A
• Duval Sebastien A

Classifications

• C01B17/167 Primary

  Separation · CPC title

• B01D53/261

  by adsorption · CPC title

• B01D2259/4062

  using six beds · CPC title

• B01D2253/308

  Pore size · CPC title

• B01D53/0423

  Beds in columns · CPC title