EP2666958A1 - Method of fraccing a well - Google Patents
Method of fraccing a well Download PDFInfo
- Publication number
- EP2666958A1 EP2666958A1 EP13150380.7A EP13150380A EP2666958A1 EP 2666958 A1 EP2666958 A1 EP 2666958A1 EP 13150380 A EP13150380 A EP 13150380A EP 2666958 A1 EP2666958 A1 EP 2666958A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- natural gas
- well
- gas
- recovered
- injecting
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 238000000034 method Methods 0.000 title claims abstract description 31
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 128
- 239000003345 natural gas Substances 0.000 claims abstract description 54
- 239000012530 fluid Substances 0.000 claims description 23
- 239000007789 gas Substances 0.000 claims description 19
- 239000003949 liquefied natural gas Substances 0.000 claims description 18
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000002485 combustion reaction Methods 0.000 claims description 6
- 239000003129 oil well Substances 0.000 claims description 6
- 239000000654 additive Substances 0.000 claims description 4
- 230000000996 additive effect Effects 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 230000008016 vaporization Effects 0.000 claims description 3
- 239000006200 vaporizer Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 230000004936 stimulating effect Effects 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229910002092 carbon dioxide Inorganic materials 0.000 description 5
- 239000001569 carbon dioxide Substances 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000003915 liquefied petroleum gas Substances 0.000 description 2
- NMJORVOYSJLJGU-UHFFFAOYSA-N methane clathrate Chemical compound C.C.C.C.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O NMJORVOYSJLJGU-UHFFFAOYSA-N 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- VTVVPPOHYJJIJR-UHFFFAOYSA-N carbon dioxide;hydrate Chemical compound O.O=C=O VTVVPPOHYJJIJR-UHFFFAOYSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- -1 hydrocarbon hydrates Chemical class 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical class C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000011707 mineral Chemical class 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH DRILLING; MINING
- E21B—EARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
- E21B43/2605—Methods for stimulating production by forming crevices or fractures using gas or liquefied gas
Abstract
- injecting natural gas into the well, and
- recovering natural gas from the well.
Description
- The present invention relates to a method for fraccing or hydrofracturing or hydraulically fracturing a well, in particular a production well, for example an oil well or a gas well, with natural gas.
- In the production of natural gas from shale or other "tight-gas" formations, hydraulic fracturing (or "frac") is used to break up the rock around the well bore and reduce the resistance to gas flow. The frac technique generally requires injecting into the well large amounts of fluids that are
- compressible, like nitrogen or carbon dioxide, or
- incompressible, such as water or liquefied petroleum gas.
- The fluids are pumped to high pressure to create large compressive forces around the well bore. These forces break the rock and create tiny fissures for gas flow. To aid in the penetration and stability of theses fissures, small amounts on the order of one to two percent by volume of hydrocarbons, mineral acids and "proppants" are added to the injected fluid.
- Thousands of tons of fluid may be injected during each frac job and much of this fluid is returned to the surface when the flow is reversed (hereafter called "produced fluids") and natural gas is produced from the well.
- If water is used as the fracturing fluid, the produced fluid water is typically brackish with small amounts of the other materials injected into the formation. Reuse of these waters is problematic because of their composition and consequently, the produced fluid water must be treated for environmental concerns and disposed of in surface waters.
- Alternatively, the produced fluid water must be injected into deep saline aquifers. If gases or condensable hydrocarbons such as liquefied petroleum gas are used, their availability and disposal after use can also create difficulties for the producer.
-
US 2012/0012321 A1 discloses a method for producing natural gas from hydrocarbon hydrates while simultaneously storing carbon dioxide in geological formations. More particularly, a method for extracting methane from methane hydrates is revealed, comprising the following steps: - feeding supercritical carbon dioxide to the methane hydrate deposits;
- allowing the carbon dioxide to take effect on the methane hydrate to release methane and store the carbon dioxide as carbon dioxide hydrate; and
- removing the released methane.
- This method known from
US 2012/0012321 A1 can be realised in different variants. For example, hydrofracturing methods can be used to increase the permeability of the hydrate-containing sediment layers. - Starting from the disadvantages and shortcomings as described above and taking the prior art as discussed into account, an object of the present invention is to overcome the problems that earlier methods have experienced.
- This object is accomplished by a method comprising the features of claim 1. Advantageous embodiments and expedient improvements of the present invention are disclosed in the dependent claims.
- In one embodiment of the present invention, a well, in particular a production well, for example an oil well or a gas well, is fracced or hydrofractured or hydraulically fractured to recover natural gas present in the well after injecting natural gas into the well.
- Before being injected into the well, the natural gas, in particular the liquefied natural gas (LNG), for example the methane gas,
- can advantageously be vaporized, in particular rapidly vaporized, for example by means of at least one submersible combustion vaporizer, and/or
- can expediently be mixed with at least one appropriate additive, in particular in order to form a foam or dense fluid to the degree necessary to suspend at least one proppant,
- The natural gas, in particular the high pressure natural gas, is fed into the well, in particular injected into the well, for example at rates ranging from about 10.000 standard cubic feed (scf) per minute to about 100.000 scf per minute.
- Once the well is pressurized and fracturing has begun, the flow of the high pressure natural gas can preferably be stopped and/or preferably be reversed. The natural gas produced and recovered from the well can be treated and made ready for use in other applications; in particular,
- the natural gas which is recovered as both the compressed or pressurized natural gas and natural gas present in the well can be separated from at least one other produced fluid; and/or
- the recovered natural gas can be fed directly to at least one pipeline where the recovered natural gas is sent to at least one storage facility or fed to at least one other industrial operation; and/or
- the recovered natural gas can be combusted and the combustion products can be run through at least one heat exchanger, at least one expander and/or at least one turbine to produce electricity and/or steam.
- Finally, the present invention relates to a method for using natural gas, in particular liquefied natural gas (LNG), for example methane gas, for stimulating a well, in particular a production well, for example an oil well or a gas well.
- The present invention addresses the problems associated with the disposal of producing fluid by using liquefied natural gas (LNG) as a fluid source. The produced fluid will have roughly the same composition of natural gas and can be introduced into at least one pipeline without further processing.
- The present invention provides for a method for fraccing or hydrofracturing or hydraulically fracturing a well, in particular an oil well or a gas well, to recover natural gas.
- Natural gas, in particular liquefied natural gas (LNG), can be shipped to the well site in large quantities, such as about thousand tons.
- The liquefied natural gas can be rapidly vaporized utilizing a high-speed vaporization technique such as by at least one submersible combustion vaporizer or other known technique.
- The vaporized liquefied natural gas, which can, at least essentially, be methane gas, can be mixed with small amounts of additives to form a foam or dense fluid to the degree necessary to suspend at least one proppant.
- The foam or dense fluid can then be compressed or pressurized, in particular by conventional techniques, to pressures between about 1.000 pounds per square inch (psi) [= about 6,9 Megapascal (MPa)] and about 10.000 psi [= about 69,0 MPa] for injection into the well, in particular at rates ranging from about 10.000 standard cubic feed (scf) [= about 283,2 cubic metres (m3)] per minute to about 100.000 scf [= about 2.832 m3] per minute.
- Once the well has been fully pressurized and the fracturing process initiated, the flow of the pressurized natural gas can be stopped and/or can be reversed. The natural gas, in particular the methane gas, which is recovered as both the pressurized dense fluid and the gas present in the fractured well can be separated from other produced fluids.
- The recovered natural gas, in particular the recovered methane gas, can be fed directly to at least one pipeline where the gas can be sent to at least one storage facility or fed to at least one other industrial operation.
- Additionally or alternatively, the recovered natural gas can be combusted and the combustion products can be run through at least one heat exchanger, at least one expander and/or at least one turbine to produce electricity and/or steam.
- The method of the present invention using natural gas from liquefied natural gas (LNG) has numerous advantages over water or inert gas as fracturing fluids:
- Large amounts of water-based fracturing fluids, for example, can remain in the reservoir and reduce natural gas flow from the well.
- The vaporized liquefied natural gas is essentially the same composition as the in-situ natural gas present in the well and when the flow is reversed, the produced fluids can be treated by the same equipment and in the same manner as the produced natural gas.
- Further, no additional safety issues are created when the vaporized liquefied natural gas is fed into well.
Claims (15)
- A method of fraccing or hydrofracturing or hydraulically fracturing a well, comprising- injecting natural gas into the well, and- recovering natural gas from the well.
- The method according to claim 1, wherein the well is a production well, in particular an oil well or a gas well.
- The method according to claim 1 or 2, wherein the natural gas is liquefied natural gas (LNG).
- The method according to at least one of claims 1 to 3, wherein the natural gas is, at least essentially, methane gas.
- The method according to at least one of claims 1 to 4, comprising the additional step of compressing or pressurizing the natural gas before the step of injecting it into the well.
- The method according to claim 5, wherein the natural gas is compressed or pressurized to pressures between about 1.000 pounds per square inch (psi) and about 10.000 psi for injection into the well.
- The method according to at least one of claims 1 to 6, comprising the additional step of vaporizing, in particular rapidly vaporizing, the natural gas before the step of injecting it into the well, in particular before the step of compressing or pressurizing the natural gas.
- The method according to claim 7, wherein the natural gas is vaporized by at least one submersible combustion vaporizer.
- The method according to at least one of claims 1 to 8, comprising the additional step of mixing the natural gas with at least one amount of at least one additive before the step of injecting the natural gas into the well, in particular comprising the additional step of mixing the vaporized natural gas with at least one small amount of at least one additive before the step of compressing or pressurizing the natural gas.
- The method according to at least one of claims 1 to 9, wherein the natural gas is injected into the well at rates ranging from about 10.000 standard cubic feed (scf) per minute to about 100.000 scf per minute.
- The method according to at least one of claims 1 to 10, comprising the additional step of stopping and/or reversing the flow of the compressed or pressurized natural gas before the step of recovering natural gas from the well.
- The method according to at least one of claims 1 to 11, wherein the natural gas which is recovered as both the compressed or pressurized natural gas and natural gas present in the well is separated from at least one other produced fluid.
- The method according to at least one of claims 1 to 12, wherein the recovered natural gas is fed directly to at least one pipeline where the recovered natural gas is sent to at least one storage facility or fed to at least one other industrial operation.
- The method according to at least one of claims 1 to 13, wherein the recovered natural gas is combusted and the combustion products are run through at least one heat exchanger, at least one expander and/or at least one turbine to produce electricity and/or steam.
- Use of the method according to at least one of claims 1 to 14 for stimulating a well, in particular a production well, for example an oil well or a gas well, with natural gas, in particular with liquefied natural gas (LNG), for example with methane gas.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201261650588P | 2012-05-23 | 2012-05-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2666958A1 true EP2666958A1 (en) | 2013-11-27 |
Family
ID=47520838
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP13150380.7A Withdrawn EP2666958A1 (en) | 2012-05-23 | 2013-01-07 | Method of fraccing a well |
Country Status (3)
Country | Link |
---|---|
US (1) | US20130312976A1 (en) |
EP (1) | EP2666958A1 (en) |
WO (1) | WO2013177114A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112832728A (en) * | 2021-01-08 | 2021-05-25 | 中国矿业大学 | Shale reservoir fracturing method based on methane multistage combustion and explosion |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140262285A1 (en) * | 2013-03-12 | 2014-09-18 | Rustam H. Sethna | Methods for fraccing oil and gas wells |
US10344204B2 (en) | 2015-04-09 | 2019-07-09 | Diversion Technologies, LLC | Gas diverter for well and reservoir stimulation |
US10012064B2 (en) | 2015-04-09 | 2018-07-03 | Highlands Natural Resources, Plc | Gas diverter for well and reservoir stimulation |
US10982520B2 (en) | 2016-04-27 | 2021-04-20 | Highland Natural Resources, PLC | Gas diverter for well and reservoir stimulation |
CA3036517C (en) * | 2016-11-11 | 2021-01-26 | Halliburton Energy Services, Inc. | Liquefied natural gas (lng) re-fracturing |
US11390798B2 (en) | 2017-07-28 | 2022-07-19 | Hallburton Energy Services, Inc. | Acidizing and interfacial tension reducing hydrolysable oils for subterranean treatments |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060065400A1 (en) * | 2004-09-30 | 2006-03-30 | Smith David R | Method and apparatus for stimulating a subterranean formation using liquefied natural gas |
US20120012321A1 (en) | 2009-02-04 | 2012-01-19 | Leibniz-Institut Fuer Meereswissenschaften | Method for Producing Natural Gas from Hydrocarbon Hydrates While Simultaneously Storing Carbon Dioxide in Geological Formations |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5711376A (en) * | 1995-12-07 | 1998-01-27 | Marathon Oil Company | Hydraulic fracturing process |
JP4759571B2 (en) * | 2004-12-16 | 2011-08-31 | フルオー・テクノロジーズ・コーポレイシヨン | Configurations and methods for LNG regasification and BTU control |
US8356487B2 (en) * | 2007-09-07 | 2013-01-22 | SPX Cooling Technologies | Control system and method for vaporizer with heating tower |
US8846585B2 (en) * | 2010-09-17 | 2014-09-30 | Clearwater International, Llc | Defoamer formulation and methods for making and using same |
EA024378B1 (en) * | 2011-01-17 | 2016-09-30 | Миллениум Стимьюлэйшн Сервисез Лтд. | Method for hydraulic fracturing a downhole formation |
US8342246B2 (en) * | 2012-01-26 | 2013-01-01 | Expansion Energy, Llc | Fracturing systems and methods utilyzing metacritical phase natural gas |
WO2013163476A1 (en) * | 2012-04-25 | 2013-10-31 | Anderson Kenneth W | Systems and methods for converting liquid natural gas to compressed natural gas and to low pressure natural gas |
-
2013
- 2013-01-07 EP EP13150380.7A patent/EP2666958A1/en not_active Withdrawn
- 2013-05-20 US US13/897,699 patent/US20130312976A1/en not_active Abandoned
- 2013-05-21 WO PCT/US2013/041952 patent/WO2013177114A1/en active Application Filing
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20060065400A1 (en) * | 2004-09-30 | 2006-03-30 | Smith David R | Method and apparatus for stimulating a subterranean formation using liquefied natural gas |
US20120012321A1 (en) | 2009-02-04 | 2012-01-19 | Leibniz-Institut Fuer Meereswissenschaften | Method for Producing Natural Gas from Hydrocarbon Hydrates While Simultaneously Storing Carbon Dioxide in Geological Formations |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112832728A (en) * | 2021-01-08 | 2021-05-25 | 中国矿业大学 | Shale reservoir fracturing method based on methane multistage combustion and explosion |
CN112832728B (en) * | 2021-01-08 | 2022-03-18 | 中国矿业大学 | Shale reservoir fracturing method based on methane multistage combustion and explosion |
Also Published As
Publication number | Publication date |
---|---|
US20130312976A1 (en) | 2013-11-28 |
WO2013177114A1 (en) | 2013-11-28 |
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