IP Library Granted Patent US 7,935,323
Granted Patent B2
US 7,935,323 · App. 12/253,824 · Granted May 3, 2011

System and method for hydrogen sulfide decontamination

Assignee: Cody Liners Ltd.
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Quick Facts
Patent No.
US 7,935,323
App. No.
12/253,824
Granted
May 3, 2011
Kind
B2
Abstract

The invention describes a system and method for hydrogen sulfide decontamination of natural gas using a scavenging reagent. The system uses a scavenging reagent within two reactors wherein the consumption of scavenging reagent is optimized by the control of flow of clean and partially-consumed scavenging reagent within and between the two reactors.

Claims (31)

1. A system for removing hydrogen sulfide from natural gas comprising:

a first reactor receiving a partially-consumed scavenging reagent and a sour natural gas, said partially-consumed scavenging reagent reacting with said sour natural gas in said first reactor to produce a partially-sweetened natural gas and a consumed scavenging reagent;

a separator operatively connected to said first reactor, said separator receiving said consumed scavenging reagent and said partially-sweetened natural gas, said consumed scavenging reagent being separated from said partially-sweetened natural gas via said separator;

a second reactor operatively connected to the separator, said second reactor receiving a clean scavenging reagent and said partially-sweetened natural gas, said clean scavenging reagent reacting with said partially-sweetened natural gas in said second reactor to produce a sweetened natural gas;

a scavenging reagent delivery system operatively connected to the first reactor and said second reactor, said scavenging reagent delivery system delivering said clean scavenging reagent to said second reactor and delivering said partially-consumed scavenging reagent to said first reactor; and

a control system controlling a flow of said partially-consumed scavenging reagent to said first reactor and a flow of said clean scavenging reagent to said second reactor based on a hydrogen sulfide concentration within said partially-sweetened natural gas.

2. A system as in claim 1 , wherein the control system includes an H 2 S sensor operatively connected between said separator and said second reactor for measuring H 2 S concentration exiting said separator and wherein the control system is responsive to the H 2 S concentration exiting said separator to increase or decrease the relative flow of said partially-consumed scavenging reagent to said first reactor and to increase or decrease the flow of said clean scavenger reagent to said second reactor.

3. A system as in claim 1 , wherein the second reactor includes a level controller operatively connected to the control system, said level controller controlling a level of scavenging reagent within said second reactor.

4. A system for removing hydrogen sulfide from natural gas comprising:

a first reactor receiving a partially-consumed scavenging reagent and a sour natural gas, said partially-consumed scavenging reagent reacting with said sour natural gas in said first reactor to produce a partially-sweetened natural gas and a consumed scavenging reagent, said first reactor separating said consumed scavenging reagent from said partially-sweetened natural gas;

a second reactor operatively connected to said first reactor, said second reactor receiving a clean scavenging reagent and said partially-sweetened natural gas, said clean scavenging reagent reacting with said partially-sweetened natural gas in said second reactor to produce a sweetened natural gas;

a scavenging reagent delivery system operatively connected to said first reactor and said second reactor, said scavenging reagent delivery system delivering clean scavenging reagent to said second reactor and delivering said partially-consumed scavenging reagent to said first reactor; and

a control system controlling a flow of said partially-consumed scavenging reagent to said first reactor and a flow of said clean scavenging reagent to said second reactor based on a hydrogen sulfide concentration within said partially-sweetened natural gas, wherein said control system includes an H 2 S sensor operatively connected between said first reactor and said second reactor, said H 2 S sensor measuring a H 2 S concentration of said partially-sweetened natural gas exiting said first reactor and wherein said control system is responsive to the H 2 S concentration of said partially-sweetened natural gas exiting said first reactor to increase or decrease said flow of partially-consumed scavenging reagent to said first reactor and to increase or decrease said flow of said clean scavenging reagent to said second reactor.

5. A system as in claim 4 , wherein said second reactor includes a level controller operatively connected to said control system, said level controller controlling a level of scavenging reagent within said second reactor.

6. A method for removing hydrogen sulfide from natural gas comprising the following steps in any order:

providing a partially-consumed scavenging reagent;

providing a sour natural gas;

providing a clean scavenging reagent;

reacting said partially-consumed scavenging reagent with said sour natural gas to produce a partially-sweetened natural gas and a consumed scavenging reagent;

separating said consumed scavenging reagent from said partially-sweetened natural gas; and

reacting said clean scavenging reagent with said partially-sweetened natural gas to produce a sweetened natural gas, wherein said clean scavenging reagent from is used as said partially-consumed scavenging reagent.

7. A method as in claim 6 , wherein a flow of said partially-consumed scavenging reagent and a flow of said clean scavenging reagent is controlled based on a hydrogen sulfide concentration within said partially-sweetened natural gas.

8. A method as in claim 7 , wherein said scavenging reagent consumption is effectively 100% in the step of reacting said partially-consumed scavenging reagent with said sour natural gas.

9. A system in accordance with claim 1 , wherein said reaction of said clean scavenging reagent with said partially-sweetened natural gas in said second reactor produces said partially-consumed scavenging reagent, said second reactor separating said partially-consumed scavenging reagent from said sweetened natural gas, said partially-consumed scavenging reagent being delivered from said second reactor to said first reactor via said scavenging reagent delivery control system.

10. A system in accordance with claim 4 , wherein said reaction of said clean scavenging reagent with said partially-sweetened natural gas in said second reactor produces said partially-consumed scavenging reagent, said second reactor separating said partially-consumed scavenging reagent from said sweetened natural gas, said partially-consumed scavenging reagent being delivered from said second reactor to said first reactor via said scavenging reagent delivery system.

11. A method in accordance with claim 6 , further comprising the steps of:

providing a first reactor;

providing a second reactor;

providing a separator, said partially-consumed scavenging reagent reacting with said sour natural gas in said first reactor to produce said partially-sweetened natural gas and said consumed scavenging reagent, said consumed scavenging reagent being separated from said partially-sweetened natural gas via said separator, said clean scavenging reagent reacting with said partially-sweetened natural gas in said second reactor to produce said sweetened natural gas and said partially-consumed scavenging reagent;

separating said sweetened natural gas from said partially-consumed scavenging reagent with said second reactor; and

delivering said partially-consumed scavenging reagent from said second reactor to said first reactor.

Assignments (8)
RELEASE OF SECURITY INTEREST IN PATENTS Recorded Jul 17, 2025
From: JPMORGAN CHASE BANK, N.A.
To: CHAMPIONX LLC; APERGY ESP SYSTEMS, LLC; APERGY BMCS ACQUISITION CORP; HARBISON-FISCHER, INC.; NORRIS RODS, INC.,; NORRIS RODS, INC.,; NORRISEAL-WELLMARK, INC.; PCS FERGUSON, INC.; QUARTZDYNE, INC.; US SYNTHETIC CORPORATION
Reel/Frame 072004/0019 →
RELEASE OF SECURITY INTEREST Recorded Jun 7, 2022
From: BANK OF AMERICA, N.A.
To: CHAMPIONX USA INC.
Reel/Frame 060304/0267 →
CHANGE OF ADDRESS Recorded Mar 23, 2022
From: ECOLAB USA INC.
To: ECOLAB USA INC.
Reel/Frame 059485/0168 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 23, 2022
From: ECOLAB USA INC.
To: CHAMPIONX USA INC.
Reel/Frame 059485/0204 →
SECURITY INTEREST Recorded Jun 5, 2020
From: CHAMPIONX USA INC.
To: BANK OF AMERICA, N.A.
Reel/Frame 052848/0368 →
SECURITY INTEREST Recorded Jun 5, 2020
From: CHAMPIONX USA INC.
To: JPMORGAN CHASE BANK, N.A.
Reel/Frame 053250/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 10, 2015
From: CODY LINERS LTD.
To: ECOLAB USA INC.
Reel/Frame 037258/0712 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 20, 2008
From: SCHULZ, MARC; MCKEARY, LEONARD
To: CODY LINERS LTD.
Reel/Frame 021700/0818 →
Continuity (2)
Provisional Application 60981333 · Oct 19, 2007
Related Publication 20090100753A1 · Apr 23, 2009