IP Library Granted Patent US 8,535,419
Granted Patent B2
US 8,535,419 · App. 12/752,674 · Granted Sep 17, 2013

Modular amine plant

Inventors: Glen Wind (Houston, TX); John Kenton Thompson (The Woodlands, TX); Lance Perryman (Whimberly, TX)
Assignee: Zephyr Gas Services LLC
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Quick Facts
Patent No.
US 8,535,419
App. No.
12/752,674
Granted
Sep 17, 2013
Kind
B2
Abstract

A modular amine plant having a front-end module and a back-end module in fluid communication with each other. The front-end module having pre-fabricated connections for the association of various equipment including: a filter, an absorption tower, and a flash tank. The back-end module having pre-fabricated connections for the association of other various equipment including: a heat exchanger, a distillation tower, and a reboiler. The modular amine plant capable of being installed at a site in less than about 5 days. The modular amine plant further having moment forces sufficient to withstand wind speeds of about 100 miles per hour.

Claims (25)

1. A method of installing a modular amine plant comprising:

providing to a site a front-end module having a filter affixed to the front-end skid, an absorption tower affixed to the front-end skid, and a flash tank affixed to the front-end skid, wherein the filter, absorption tower, and flash tank are in adaptable fluid communication with each other prior to arrival at the site;

providing to the site a back-end module in adaptable fluid communication with the front-end module, the back-end module having a heat exchanger affixed to the back-end skid, a distillation tower affixed to the back-end skid, and a reboiler affixed to the back-end skid, wherein the heat exchanger, the distillation tower, and the reboiler are in adaptable fluid communication with each other prior to arrival at the site; and

starting up the modular amine plant in less than about 5 days.

2. A method of installing a modular amine plant comprising:

providing to a site a front-end module having a filter affixed to the front-end module, an absorption tower affixed to the front-end module, a scrubber affixed to the front-end module, and a flash tank affixed to the front-end module, wherein the filter, absorption tower, and flash tank are in adaptable fluid communication with each other prior to arrival at the site;

providing a back-end module in adaptable fluid communication with the front-end having:

a distillation skid having a distillation tower affixed to the distillation skid, a heat exchanger affixed to the distillation skid, a condenser affixed to the distillation skid, wherein the heat exchanger and the distillation tower are in substantial fluid communication with each other prior to arrival at the site;

a reboiler skid having a reboiler affixed to the reboiler skid;

a pump skid having a main pump affixed to the pump skid; and

starting up the modular amine plant in less than about 5 days.

3. The method of claim 2 , wherein the modular amine plant is set up in less than about 2 days.

4. The method of claim 1 , wherein the modular amine plant has moment forces sufficient to withstand wind speeds of at least about 120 miles per hour.

5. The method of claim 4 , wherein a total footprint of the back-end module is less than about 3,000 ft 2 .

6. The method of claim 2 , wherein the modular amine plant has moment forces sufficient to withstand wind speeds of at least about 120 miles per hour.

7. The method of claim 6 , wherein a total footprint of the back-end module is less than about 3,000 ft 2 .

8. The method of claim 1 , wherein the modular amine plant is sized to accommodate an amine-water circulation rate selected from the group consisting of about 3 gallons per minute, about 7.5 gallons per minute, about 30 gallons per minute, about 60 gallons per minute, about 100 gallons per minute, about 110 gallons per minute, about 200 gallons per minute, about 300 gallons per minute, about 400 gallons per minute, about 500 gallons per minute, about 600 gallons per minute, and about 700 gallons per minute, plus or minus ten percent.

9. The method of claim 2 , wherein the modular amine plant is sized to accommodate an amine-water circulation rate selected from the group consisting of about 3 gallons per minute, about 7.5 gallons per minute, about 30 gallons per minute, about 60 gallons per minute, about 100 gallons per minute, about 110 gallons per minute, about 200 gallons per minute, about 300 gallons per minute, about 400 gallons per minute, about 500 gallons per minute, about 600 gallons per minute, and about 700 gallons per minute, plus or minus ten percent.

10. A method of installing a modular amine plant comprising:

providing to a site a front-end module having a filter affixed to the front-end skid, an absorption tower affixed to the front-end skid, and a flash tank affixed to the front-end skid, wherein the filter, absorption tower, and flash tank are in adaptable fluid communication with each other prior to arrival at the site;

providing to the site a back-end module in adaptable fluid communication with the front-end module, the back-end module having a heat exchanger affixed to the back-end skid, a distillation tower affixed to the back-end skid, and a reboiler affixed to the back-end skid, wherein the heat exchanger, the distillation tower, and the reboiler are in adaptable fluid communication with each other prior to arrival at the site; and

starting up the modular amine plant in less than about 7 days.

11. The method of claim 10 , wherein the modular amine plant has moment forces sufficient to withstand wind speeds of at least about 120 miles per hour.

12. The method of claim 11 , wherein a total footprint of the back-end module is less than about 3,000 ft 2 .

13. The method of claim 10 , wherein the modular amine plant is sized to accommodate an amine-water circulation rate selected from the group consisting of about 3 gallons per minute, about 7.5 gallons per minute, about 30 gallons per minute, about 60 gallons per minute, about 100 gallons per minute, about 110 gallons per minute, about 200 gallons per minute, about 300 gallons per minute, about 400 gallons per minute, about 500 gallons per minute, about 600 gallons per minute, and about 700 gallons per minute, plus or minus ten percent.

Assignments (4)
MERGER Recorded Jul 29, 2015
From: ZEPHYR GAS SERVICES LLC
To: CDM RESOURCE MANAGEMENT LLC
Reel/Frame 036207/0218 →
MERGER Recorded Dec 8, 2011
From: ZEPHYR GAS SERVICES, LP
To: REGENCY ZEPHYR LLC
Reel/Frame 027349/0671 →
CHANGE OF NAME Recorded Dec 8, 2011
From: REGENCY ZEPHYR LLC
To: ZEPHYR GAS SERVICES LLC
Reel/Frame 027350/0927 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 26, 2010
From: WIND, GLEN; THOMPSON, JOHN KENTON; PERRYMAN, LANCE
To: ZEPHYR GAS SERVICES, LP
Reel/Frame 024289/0324 →
Continuity (3)
Provisional Application 61165896 · Apr 1, 2009
Provisional Application 61309053 · Mar 1, 2010
Related Publication 20100251897A1 · Oct 7, 2010