Composite fracturing prepad fluid and application thereof in hydraulic fracturing of tight reservoir

A composite fracturing and pre-fluid technology, applied in the drilling composition, production fluid, wellbore/well components, etc., can solve the problems of loss of oil and gas diversion channels, low matrix permeability, and high water injection cost. Achieve redistribution, promote percolation, and enhance spontaneous imbibition performance

Inactive Publication Date: 2020-12-08
CHINA UNIV OF PETROLEUM (BEIJING) +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the large particle size of conventional proppant particles, these induced secondary micro-fractures cannot enter the fractures to achieve effective support after construction, thus losing the oil and gas flow channels provided by these fractures
On the other hand, due to the low matrix permeability in tight reservoirs, the original wettability of rocks is mostly neutral wet or oil-wet, which leads to the direction of capillary force opposite to the direction of water flooding, resulting in low recovery and high cost of water flooding in conventional water flooding methods. If the value is too high, at present, the method of adding surfactants that can achieve the effect of wettability reversal to the fracturing pre-fluid is often used to enhance the spontaneous imbibition of tight reservoirs for mining.

Method used

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  • Composite fracturing prepad fluid and application thereof in hydraulic fracturing of tight reservoir
  • Composite fracturing prepad fluid and application thereof in hydraulic fracturing of tight reservoir
  • Composite fracturing prepad fluid and application thereof in hydraulic fracturing of tight reservoir

Examples

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Embodiment 1

[0043] This embodiment provides a kind of composite fracturing prefluid, and this composite fracturing prefluid is obtained by fly ash (through 325 mesh sieves, that is, the particle size is greater than or equal to 325 mesh, and the density of the flyash is 1.5g / cm 3 , breakage rate under 28MPa closing pressure is 2.8%), microemulsion and drag reducer are prepared by adding water, wherein, in the composite fracturing prefluid, fly ash accounts for 0.1wt%, and microemulsion accounts for 0.1wt% , the drag reducer (conventional drag reducer in this field) accounts for 0.8wt%.

[0044]Wherein, in the microemulsion, based on 100g of the microemulsion, it includes: 15g of MOA-7, 12g of MOA-9, 1.5g of OP-10, 5g of sodium octyl succinate sulfonate, 30g of iso Propanol, 20g of cyclohexane, 5g of limonene, 5g of ammonium chloride and the remainder of water.

Embodiment 2

[0046] This embodiment provides a composite fracturing prefluid, which is obtained from quartz sand (through a 230 mesh sieve, that is, the particle size is greater than or equal to 230 mesh, and the density of the quartz sand is 2.7g / cm 3 , the breaking rate under 28MPa closing pressure is 8.5%), microemulsion and drag reducer are prepared by adding water, wherein, in the composite fracturing prefluid, quartz sand accounts for 0.1wt%, microemulsion accounts for 0.15wt%, The drag reducer (conventional drag reducer in this field) accounts for 0.6wt%.

[0047] Wherein, in the microemulsion, based on 100 g of the microemulsion, it includes: 10 g of sodium α-alkenyl sulfonate, 5 g of sodium dodecylbenzene sulfonate, 10 g of propylene glycol, 10 g of cyclohexane, 10g of sodium sulfate and the remainder of water.

Embodiment 3

[0049] This embodiment provides a composite fracturing prefluid, which is obtained by ceramsite (passing through a 200 mesh screen, that is, the particle size is greater than or equal to 200 mesh, and the density of the ceramsite is 2.9g / cm 3 , the breaking rate under 28MPa closing pressure is 3.5%), microemulsion and drag reducer are prepared by adding water, wherein, in the composite fracturing prefluid, quartz sand accounts for 0.2wt%, microemulsion accounts for 1.0wt%, The drag reducer (conventional drag reducer in this field) accounts for 0.8wt%.

[0050] Wherein, in the microemulsion, based on 100g of the microemulsion, it includes: 10g of dodecyltrimethylammonium bromide, 10g of tetradecyltrimethylammonium chloride, 10g of tetradecyl Trimethyl ammonium bromide, ethylene glycol of 5g, propylene glycol of 25g, pinene of 20g, limonene of 5g, potassium chloride of 5g and the water of surplus.

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Abstract

The invention provides a composite fracturing prepad fluid and an application thereof in hydraulic fracturing of a tight reservoir. The composite fracturing prepad fluid composition is prepared from apropping agent and microemulsion, the compounding weight ratio of the propping agent to the microemulsion is (0.1-2): (0.02-1.5); the microemulsion is prepared from the following components in percentage by weight: 8 to 35 weight percent of surfactant, 10 to 30 weight percent of alcohol, 3 to 25 weight percent of oil, 1 to 10 weight percent of salt and the balance of water based on 100 weight percent of the microemulsion. The composite fracturing prepad fluid not only can improve the effective fracture flow conductivity of artificial microfractures after hydraulic fracturing construction of the tight reservoir, but also enhances the spontaneous imbibition performance of a tight reservoir matrix, and is helpful for improving the final recovery ratio of the tight reservoir.

Description

technical field [0001] The invention belongs to the technical field of petroleum exploitation, and in particular relates to a composite fracturing prefluid suitable for hydraulic fracturing of tight reservoirs to enhance oil recovery and its application in hydraulic fracturing of tight reservoirs. Background technique [0002] For tight reservoirs with a permeability lower than 0.1 mD, hydraulic fracturing technology can form an artificial fracture network near the wellbore, improve the seepage capacity near the wellbore, and thus increase the efficient production of formation fluids. On the one hand, in the process of hydraulic fracturing, not only primary fractures will be formed around the wellbore, but also induced secondary micro-fractures formed by the extension of primary fractures will be formed in the area away from the wellbore. Due to the large particle size of conventional proppant particles, these induced secondary micro-fractures cannot enter the fractures to a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C09K8/80E21B43/26
CPCC09K8/80E21B43/26
Inventor 梁天博周福建袁帅姚二冬杨凯左洁李奔曲鸿雁李秀辉胡晓东李源
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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