IP Library Granted Patent US 9,034,086
Granted Patent B2
US 9,034,086 · App. 13/677,493 · Granted May 19, 2015

Ventless tank system

Inventors: Danny Daniels (Tishomingo, OK); Vernon Daniels (Tishomingo, OK)
Assignee: Nitro-Lift Hydrocarbon Recovery Systems, LLC
B01D19/0042
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Quick Facts
Patent No.
US 9,034,086
App. No.
13/677,493
Granted
May 19, 2015
Kind
B2
Abstract

A tank system for capturing fluids from an oil or gas well. The system comprises a series of tanks adapted to step down the temperature and pressure of well products from a fossil fuel well while removing gas products until the liquid products contain less dissolved gas in a tank than they could contain at ambient temperature and pressure. Therefore, no venting of gas takes place during the separation. An oil-gas separator is provided within the tank system to separate organic products from non-organic products. Gas products may be flared or delivered for further processing.

Claims (62)

1. A tank system for managing a brine containing an organic gas comprising:

a first tank body characterized by an internal first pressure, the body comprising:

a main inlet port;

a gas outlet port; and

a liquid outlet port;

a flow interrupter located within the first tank body proximate the main inlet port;

a sand separator located within the first tank body;

a flare line operatively connected to the gas outlet port; and

a secondary tank in communication with the liquid outlet port, wherein the conditions in the secondary tank are such that liquid in the secondary tank has less organic gas dissolved in solution than exists at equilibrium at standard temperature and pressure.

2. The tank system of claim 1 wherein the flow interrupter comprises a deflector plate.

3. The tank system of claim 1 further comprising:

a liquid transmission line disposed between the liquid outlet port and the secondary tank; and

a heat exchanger located on the liquid transmission line to remove heat from the transmission line.

4. The tank system of claim 1 wherein the first tank body further comprises a plurality of liquid outlet ports.

5. The tank system of claim 1 further comprising a low pressure flare line operatively connected to the secondary tank.

6. The tank system of claim 1 wherein the flow interrupter comprises a gas buster line.

7. The tank system of claim 1 further comprising a static tree to discharge static electricity within the first tank body.

8. The tank system of claim 1 further comprising a mist collector located in the first tank body such that entrained liquid within the first tank body is collected.

9. A method for removing an organic gas from a brine stream comprising:

directing the brine stream to a first tank comprising a first liquid outlet port and a first gas outlet port;

separating the brine stream into a slurry stream and a gas stream;

separating sand from the slurry stream to create a liquid stream;

removing the liquid stream at the first liquid outlet port;

removing the gas stream at the first gas outlet port;

directing the liquid stream from the first liquid outlet port into a second tank, the second tank being characterized by a lower pressure than the first tank such that dissolved organic gas desorbs from the liquid stream; and

removing the liquid stream from the second tank at a second liquid outlet port

wherein the liquid stream removed from the second liquid outlet port contains less of the organic gas than exists at equilibrium at standard temperature and pressure.

10. The method of claim 9 wherein the step of separating a product stream into the slurry stream and the gas stream comprises:

providing a deflector plate within the first tank;

causing the brine stream to impact the deflector plate; and

collecting the slurry stream.

11. The method of claim 9 wherein the step of separating the sand from the slurry stream comprises providing a baffle.

12. The method of claim 9 further comprising the step of providing a plurality of liquid outlet ports in the first tank body.

13. The method of claim 9 further comprising removing static electricity from the gas stream with a static tree.

14. The method of claim 9 further comprising removing gas from the brine stream in a third tank prior to directing the brine stream to the first tank body.

15. The method of claim 9 further comprising collecting vapor from within the gas stream and returning the collected vapor to the liquid stream.

16. The method of claim 9 wherein the liquid stream comprises oil and water.

17. The method of claim 16 further comprising the step of separating the oil from the water.

18. The method of claim 17 wherein the water is separated from the oil in the first tank.

19. A tank system for removing a volatile organic gas from liquid solution comprising:

a first tank body characterized by an internal first pressure comprising:

a first tank inlet port;

a first tank gas outlet port; and

a first tank liquid outlet port;

a second tank body characterized by a second internal pressure comprising:

a second tank inlet port;

a second tank gas outlet port; and

a second tank liquid outlet port;

a first liquid transmission line disposed between the first tank liquid outlet port and the second tank inlet port;

a heat exchanger located on the first liquid transmission line to cool liquid within the first liquid transmission line;

a first gas flare line connected to the first tank gas outlet port; and

a second gas flare line connected to the second tank gas outlet port;

wherein the internal first pressure is greater than the internal second pressure.

20. The system of claim 19 further comprising:

a third tank body characterized by a third internal pressure comprising:

a third tank inlet port;

a third tank gas outlet port; and

a third tank liquid outlet port;

wherein the internal third pressure is higher than the internal first pressure and the liquid solution exiting through the third tank liquid outlet port is directed to the first tank inlet port.

21. The system of claim 19 wherein the liquid solution comprises water.

22. The system of claim 19 wherein the first tank body further comprises a sand separator.

23. The system of claim 19 wherein the first tank body comprises a plurality of first tank liquid outlet ports, wherein each first tank liquid outlet port is characterized by a different height.

Assignments (10)
NOTICE OF SUCCESSOR COLLATERAL AGENT Recorded Oct 14, 2025
From: GOLDMAN SACHS MIDDLE MARKET LENDING CORP. II
To: GOLDMAN SACHS PRIVATE CREDIT CORP.
Reel/Frame 073069/0670 →
RELEASE OF SECURITY INTEREST Recorded May 7, 2024
From: CADENCE BANK
To: NITRO LIFT TECHNOLOGIES, L.L.C; USA DEBUSK LLC
Reel/Frame 067334/0621 →
PATENT SECURITY AGREEMENT Recorded May 1, 2024
From: USA DEBUSK LLC; NITRO LIFT TECHNOLOGIES, L.L.C.
To: GOLDMAN SACHS MIDDLE MARKET LENDING CORP. II
Reel/Frame 067288/0580 →
SECURITY INTEREST Recorded Nov 30, 2023
From: NITRO LIFT TECHNOLOGIES, L.L.C.; USA DEBUSK LLC
To: CADENCE BANK
Reel/Frame 065715/0218 →
PATENT SHORT FORM SECURITY AGREEMENT Recorded Nov 28, 2023
From: NITRO LIFT TECHNOLOGIES, L.L.C.; USA DEBUSK LLC
To: BRIGHTWOOD LOAN SERVICES, LLC
Reel/Frame 065693/0367 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 30, 2023
From: NITRO LIFT HOLDINGS, LLC
To: NITRO LIFT TECHNOLOGIES, L.L.C.
Reel/Frame 065384/0863 →
RELEASE OF SECURITY INTEREST Recorded Oct 26, 2023
From: PETRO CAPITAL ENERGY CREDIT II, LP
To: NITRO-LIFT HYDROCARBON RECOVERY SYSTEMS, LLC
Reel/Frame 065353/0241 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 13, 2023
From: NITRO-LIFT HYDROCARBON RECOVERY SYSTEMS, LLC
To: NITRO LIFT HOLDINGS, LLC
Reel/Frame 064887/0163 →
SECURITY AGREEMENT Recorded Dec 3, 2013
From: NITRO-LIFT HYDROCARBON RECOVERY SYSTEMS, LLC
To: PETRO CAPITAL ENERGY CREDIT, LLC
Reel/Frame 031763/0733 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 25, 2013
From: DANIELS, DANNY; DANIELS, VERNON
To: NITRO-LIFT HYDROCARBON RECOVERY SYSTEMS, LLC
Reel/Frame 031670/0579 →
Continuity (1)
Related Publication 20140130676A1 · May 15, 2014