Claus process for sulfur recovery with intermediate water vapor removal by adsorption

Patent metadata

Field	Value
Publication number	US-9701537-B1
Application number	US-201614988032-A
Country	US
Kind code	B1
Filing date	Jan 5, 2016
Priority date	Jan 5, 2016
Publication date	Jul 11, 2017
Grant date	Jul 11, 2017

Abstract

A method to recover sulfur comprising the steps of feeding an acid gas stream to a combustion furnace, condensing the cooled furnace stream to produce a first gas stream, feeding the first gas stream to a first adsorber comprises a molecular sieve, feeding the first hot dry gas stream to a first catalytic reactor, cooling the first catalytic outlet stream in a first condenser, feeding the second gas stream to a second adsorber, feeding the second hot dry gas stream to a second catalytic reactor, cooling the second catalytic outlet stream in a second condenser, introducing the third gas stream to a third adsorber, feeding the third hot dry gas stream to a third catalytic reactor to produce a third catalytic outlet stream, and cooling the third catalytic outlet stream in a third condenser to produce a third sulfur stream and a tail gas stream.

First claim

What is claimed is:

1. A method to recover sulfur from hydrogen sulfide in an acid gas stream, the method comprising the steps of:
feeding the acid gas stream to a combustion furnace to produce a furnace outlet stream, the combustion furnace configured to convert the hydrogen sulfide to elemental sulfur, wherein the furnace outlet stream comprises elemental sulfur, hydrogen sulfide, sulfur dioxide, and water vapor;
introducing the furnace outlet stream to a waste heat boiler to produce a cooled furnace outlet stream, the waste heat boiler configured to reduce a temperature of the furnace outlet stream;
condensing the cooled furnace stream in a sulfur condenser to produce a liquid sulfur stream and a first gas stream, the sulfur condenser configured to reduce a temperature of the cooled furnace stream to a temperature below a dew point of elemental sulfur and above a dew point of water;
feeding the first gas stream to a first adsorber to produce a first dry gas stream and a first water stream, wherein the first adsorber comprises a molecular sieve, wherein the first dry gas stream is in the absence of water vapor, wherein the first dry gas stream comprises hydrogen sulfide and sulfur dioxide;
heating the first dry gas stream in a first reheater to produce a first hot dry gas stream, wherein the first hot dry gas stream is at a first temperature;
feeding the first hot dry gas stream to a first catalytic reactor to produce a first catalytic outlet stream, wherein the first catalytic outlet stream comprises elemental sulfur, hydrogen sulfide, sulfur dioxide, and water vapor;
cooling the first catalytic outlet stream in a first condenser to produce a first sulfur stream and a second gas stream, the first condenser configured to condense the elemental sulfur in the first catalytic outlet stream such that the first sulfur stream comprises liquid sulfur, wherein a temperature in the first condenser is between the dew point of sulfur and the dew point of water, wherein the second gas stream comprises hydrogen sulfide, sulfur dioxide, and water vapor;
feeding the second gas stream to a second adsorber to produce a second dry gas stream and a second water stream, wherein the second adsorber comprises a molecular sieve, wherein the second dry gas stream comprises hydrogen sulfide and sulfur dioxide, wherein the second dry gas stream is in the absence of water vapor;
heating the second dry gas stream in a second reheater to produce a second hot dry gas stream, wherein the second hot dry gas stream is at a second temperature, wherein the second temperature is lower than the first temperature;
feeding the second hot dry gas stream to a second catalytic reactor to produce a second catalytic outlet stream, wherein the second catalytic outlet stream comprises elemental sulfur, hydrogen sulfide, sulfur dioxide, and water vapor;
cooling the second catalytic outlet stream in a second condenser to produce a second sulfur stream and a third gas stream, the second condenser configured to condense the elemental sulfur in the second catalytic outlet stream such that the second sulfur stream comprises liquid sulfur, wherein a temperature in the second condenser is between the dew point of sulfur and the dew point of water, wherein the third gas stream comprises hydrogen sulfide, sulfur dioxide, and water vapor;
introducing the third gas stream to a third adsorber to produce a third dry gas stream and a third water stream, wherein the third adsorber comprises a molecular sieve, wherein the third dry gas stream comprises hydrogen sulfide and sulfur dioxide, wherein the third dry gas stream is in the absence of water vapor;
heating the third dry gas stream in a third reheater to produce a third hot dry gas stream, wherein the third hot dry gas stream is at a third temperature, wherein the third temperature is lower than the second temperature;
feeding the third hot dry gas stream to a third catalytic reactor to produce a third catalytic outlet stream, wherein the third catalytic outlet stream comprises elemental sulfur, hydrogen sulfide, sulfur dioxide, and water vapor; and
cooling the third catalytic outlet stream in a third condenser to produce a third sulfur stream and a tail gas stream, the third condenser configured to condense the elemental sulfur in the third catalytic outlet stream such that the third sulfur stream comprises liquid sulfur, wherein a temperature in the third condenser is between the dew point of sulfur and the dew point of water, wherein the tail gas stream comprises hydrogen sulfide, sulfur dioxide, and water vapor.

2. The method of claim 1 , wherein a total conversion can be determined.

3. The method of claim 2 , wherein the total conversion exceeds 99% by weight.

4. The method of claim 1 , wherein the molecular sieve is molecular sieve 3A.

5. The method of claim 1 , wherein the first temperature is 235° C.

6. The method of claim 1 , wherein the second temperature is 215° C.

7. The method of claim 1 , wherein the third temperature is 205° C.

8. A system to recover sulfur from hydrogen sulfide in an acid gas stream, the system comprising:
a combustion furnace, the combustion furnace configured to convert the hydrogen sulfide to elemental sulfur to produce a furnace outlet stream, wherein the furnace outlet stream comprises elemental sulfur, hydrogen sulfide, sulfur dioxide, and water vapor;
a waste heat boiler fluidly connected to the combustion furnace, the waste heat boiler configured to remove heat from the furnace outlet stream to produce a cooled furnace stream;
a sulfur condenser fluidly connected to the waste heat boiler, the sulfur condenser configured to condense the elemental sulfur in cooled furnace stream to produce a liquid sulfur stream and a first gas stream, wherein the gas stream is in the absence of elemental sulfur, wherein the first gas stream comprises water vapor;
a first adsorber fluidly connected to the sulfur condenser, the first adsorber configured to remove water vapor from the first gas stream to produce a first dry gas stream and a first water stream, wherein the first adsorber comprises a molecular sieve, wherein the first dry gas stream comprises hydrogen sulfide and sulfur dioxide and is in the absence of water vapor;
a first Claus catalytic stage fluidly connected to the first adsorber, the first Claus catalytic stage configured to produce a first sulfur stream and a second gas stream;
a second adsorber fluidly connected to the first Claus catalytic stage, the second adsorber configured to remove water vapor from the second gas to produce a second dry gas stream, wherein the second adsorber comprises a molecular sieve, wherein the second dry gas stream comprises hydrogen sulfide and sulfur dioxide and is in the absence of water vapor;
a second Claus catalytic stage fluidly connected to the second adsorber, the second Claus catalytic stage configured to produce a second sulfur stream and a third gas stream;
a third adsorber fluidly connected to the second Claus catalytic stage, the third adsorber configured to remove water vapor from the third gas to produce a third dry gas stream, wherein the third adsorber comprises a molecular sieve, wherein the third dry gas stream comprises hydrogen sulfide and sulfur dioxide and is in the absence of water vapor; and
a third Claus catalytic stage fluidly connected to the third adsorber, the third Claus catalytic stage configured to produce a third sulfur stream and a tail gas stream.

9. The system of claim 8 , wherein a total conversion can be determined.

10. The system of claim 9 , wherein the total conversion exceeds 99% by weight.

11. The system of claim 8 , wherein the molecular sieve is molecular sieve 3A.

Assignees

• Saudi Arabian Oil Co

Inventors

• Ercan Cemal
• Othman Rashid M
• Wang Yuguo

Classifications

• C01B17/0456 Primary

  the hydrogen sulfide-containing gas being a Claus process tail gas · CPC title

• B01J19/245

  placed in series · CPC title

• B01D53/8615

  Mixtures of hydrogen sulfide and sulfur oxides · CPC title

• C01B17/0408

  Pretreatment of the hydrogen sulfide containing gases · CPC title

• C01B17/0404

  by processes comprising a dry catalytic conversion of hydrogen sulfide-containing gases, e.g. the Claus process · CPC title