Stimulation with natural gas

Patent metadata

Field	Value
Publication number	US-9790775-B2
Application number	US-201414209598-A
Country	US
Kind code	B2
Filing date	Mar 13, 2014
Priority date	Mar 15, 2013
Publication date	Oct 17, 2017
Grant date	Oct 17, 2017

Abstract

Apparatus, systems, and methods in which a fracturing fluid source is in fluid communication with a wellbore extending into a subterranean formation. A compressor has an input in fluid communication with a natural gas source, and has an output in fluid communication with the wellbore. The compressor is operable to compress natural gas received at the input for delivery at the output. A liquefied gas source is also in fluid communication with the wellbore.

First claim

What is claimed is:

1. An apparatus, comprising:
a fracturing fluid source in fluid communication with a wellbore extending into a subterranean formation, the fracturing fluid source comprising fracturing fluid and water;
a natural gas source;
a compressor having an input in fluid communication with the natural gas source, having an output in fluid communication with the wellbore, and operable to compress natural gas received at the input for delivery at the output;
a heat recovery system to receive thermal energy from the compressor, the thermal energy to alter temperature of the fracturing fluid, water, or compressed natural gas,
wherein a pressure of the fracturing fluid is at a higher pressure relative to a pressure of the compressed natural gas; and
a liquefied gas source in fluid communication with the wellbore.

2. The apparatus of claim 1 wherein the liquefied gas source comprises a liquefied gas selected from the group consisting of:
liquefied natural gas;
liquefied carbon dioxide; and
liquefied nitrogen.

3. The apparatus of claim 2 further comprising a cryogenic pump operable to pressurize the liquefied gas received from the liquefied gas source before communication to the wellbore.

4. The apparatus of claim 3 wherein the cryogenic pump pressurizes the liquefied gas at a pressure substantially equal to or greater than an outlet pressure of the compressor.

5. The apparatus of claim 1 further comprising a foaming device in fluid communication with the compressor, the fracturing fluid source, and the wellbore, wherein the foaming device is operable to form a foamed fluid comprising compressed natural gas received from the compressor and fracturing fluid received from the fracturing fluid source for delivery to the wellbore.

6. The apparatus of claim 5 wherein the foaming device is further operable to receive a polymer also utilized to form the foamed fluid.

7. The apparatus of claim 5 wherein the foaming device is further operable to receive a cross-linked polymer stabilizer also utilized to form the foamed fluid.

8. The apparatus of claim 1 wherein the natural gas source comprises a pressure vessel containing a natural gas product selected from the group consisting of:
liquefied natural gas;
compressed natural gas; and
gas hydrates.

9. The apparatus of claim 1 further comprising a fracturing pump in fluid communication between the fracturing fluid source and the wellbore, wherein the fracturing pump comprises a combustion engine in fluid communication with the natural gas source.

10. The apparatus of claim 1 further comprising a cooler in fluid communication between the compressor output and the wellbore and operable to cool the compressed natural gas received from the compressor.

11. The apparatus of claim 1 further comprising an injector in fluid communication between the compressor and the wellbore and operable to inject a pressurized cooling chemical into the compressed natural gas before delivery to the wellbore, wherein the cooling chemical is selected from the group consisting of:
liquefied natural gas;
liquefied nitrogen; and
liquefied carbon dioxide.

12. The apparatus of claim 1 further comprising an injector in fluid communication between the natural gas source and the compressor and operable to inject a pressurized cooling chemical into natural gas received from the natural gas source before delivery to the compressor, wherein the cooling chemical is selected from the group consisting of:
methanol;
ethanol;
liquefied natural gas;
liquefied nitrogen; and
liquefied carbon dioxide.

13. The apparatus of claim 1 wherein the compressor input is a fluid input and the apparatus further comprises a power generator having an output shaft operatively coupled to a mechanical input of the compressor, wherein the power generator comprises a combustion engine fueled by the natural gas source.

14. The apparatus of claim 1 further comprising a mixer disposed in the wellbore, wherein the mixer is in fluid communication with the fracturing fluid source and the compressor.

15. The apparatus of claim 14 wherein the mixer is in fluid communication with a tubular disposed within the wellbore and an annulus defined between the tubular and the wellbore, and wherein the fracturing fluid source and the compressor are in fluid communication with respective ones of the tubular and the annulus.

16. The apparatus of claim 15 wherein the mixer comprises a plurality of orifices extending through walls of the tubular and collectively operable to enable mixing of fluids received from the fracturing fluid source and the compressor.

17. The apparatus of claim 15 further comprising a packer disposed in the annulus and forming an uphole portion of the annulus and a downhole portion of the annulus, wherein the packer is disposed further downhole than the plurality of orifices.

18. A method, comprising:
conducting natural gas from a natural gas source located at a wellsite to a compressor located at the wellsite;
compressing the natural gas via operation of the compressor;
mixing the compressed natural gas with a fracturing fluid received from a fracturing fluid source located at the wellsite, thereby forming a pressurized mixture,
wherein a pressure of the fracturing fluid is at a higher pressure relative to a pressure of the compressed natural gas;
receiving thermal energy from the compressor to alter temperature of the fracture fluid or compressed natural gas; and
fracturing a subterranean formation by introducing the pressurized mixture into a wellbore extending from the wellsite into the subterranean formation.

19. The method of claim 18 wherein the mixing occurs at the wellsite.

20. The method of claim 18 wherein the mixing occurs in the wellbore at a depth of at least about 60 meters.

Assignees

• Schlumberger Technology Corp

Inventors

• Joseph Jijo
• Hutchins Richard D
• Huey William Troy
• Clinkscales Joel
• Enkababian Philippe
• Pena Alejandro
• Waters George
• Ayala Salvador
• Brown J Ernest

Classifications

• C10L3/06

  Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04 {(liquefying by pressure and cold treatment F25J)} · CPC title

• C09K8/62

  Compositions for forming crevices or fractures · CPC title

• E21B43/26 Primary

  by forming crevices or fractures · CPC title

• E21B43/2607 Primary

  Surface equipment specially adapted for fracturing operations · CPC title

• E21B43/2605

  using gas or liquefied gas · CPC title