CN108587593A - Slickwater fracturing fluid for low-temperature reservoir - Google Patents

Slickwater fracturing fluid for low-temperature reservoir Download PDF

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Publication number
CN108587593A
CN108587593A CN201711441220.8A CN201711441220A CN108587593A CN 108587593 A CN108587593 A CN 108587593A CN 201711441220 A CN201711441220 A CN 201711441220A CN 108587593 A CN108587593 A CN 108587593A
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methacrylate
acid
fracturing fluid
acrylate
acrylmonomers
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Inventor
赵振峰
范华波
薛小佳
李忠兴
慕立俊
张矿生
吴江
李楷
刘锦
郭钢
郭小勇
胡超
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Petrochina Co Ltd
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Petrochina Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/62Compositions for forming crevices or fractures
    • C09K8/66Compositions based on water or polar solvents
    • C09K8/68Compositions based on water or polar solvents containing organic compounds
    • C09K8/685Compositions based on water or polar solvents containing organic compounds containing cross-linking agents
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/607Compositions for stimulating production by acting on the underground formation specially adapted for clay formations
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/84Compositions based on water or polar solvents
    • C09K8/86Compositions based on water or polar solvents containing organic compounds
    • C09K8/88Compositions based on water or polar solvents containing organic compounds macromolecular compounds
    • C09K8/882Compositions based on water or polar solvents containing organic compounds macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/60Compositions for stimulating production by acting on the underground formation
    • C09K8/84Compositions based on water or polar solvents
    • C09K8/86Compositions based on water or polar solvents containing organic compounds
    • C09K8/88Compositions based on water or polar solvents containing organic compounds macromolecular compounds
    • C09K8/887Compositions based on water or polar solvents containing organic compounds macromolecular compounds containing cross-linking agents
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/12Swell inhibition, i.e. using additives to drilling or well treatment fluids for inhibiting clay or shale swelling or disintegrating
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K2208/00Aspects relating to compositions of drilling or well treatment fluids
    • C09K2208/26Gel breakers other than bacteria or enzymes

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  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
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  • Dispersion Chemistry (AREA)
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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

The invention belongs to the technical field of oil field production increase, and particularly provides slickwater fracturing fluid for a low-temperature reservoir, which comprises the following components in percentage by mass: 0.15-0.25% of thickening agent, 0.03-0.05% of clay stabilizer, 0.20-0.30% of structural stabilizer, 0.05-0.10% of low-temperature activator, 0.02-0.05% of gel breaker and the balance of water.

Description

A kind of low temperature reservoir slippery water fracturing fluid
Technical field
The invention belongs to oilfield stimulation technical fields, and in particular to a kind of low temperature reservoir slippery water fracturing fluid.
Background technology
Pressure break has been rapidly developed as the Main Yield-increasing of oil-gas reservoir, well stimulation and extensive use.Pressure break is exactly profit It presses off stratum to form crack with pressure, proppant is used in combination to support it, to reduce volume increase, the augmented injection of fluid flow resistance Measure.The purpose of pressure break is exactly to form the crack with flow conductivity in the earth formation, and the fracturing fluid of use is largely determined Fracturing effect is determined, while the viscosity of fracturing fluid there are certain requirements, the fluid that it can be known as low viscosity after pressure break is made to be easy The row of returning damages to avoid to the oil-gas Layer in stratum.
Domestic and international most common fracturing fluid is mainly using guanidine glue and its modifier as the aqueous fracturing fluid of thickening agent, at present It is widely applied in each oil field, and achieves good effect of increasing production.But celebrate oil gas field densification oil-gas reservoir pressure break with long The change of work pattern and Environmental Protection Situation are increasingly severe, it is desirable that aqueous fracturing fluid in addition to Low Damage, low frictional resistance, low cost, Except the easy row of returning, easy continuous mixture feature, also there is the characteristics of easily recycling, high recycling rate, drain is returned after being pressed with reduction Pollution to environment and soil, while requiring to reduce industrial water quantity.And guanidine glue and its modifier have natural plant gum easily corrupt Inadequate natural endowment disadvantage, it is difficult to return drain processing by chemical crosslinking the formation of and fracturing fluid system complicated component, frozen glue after breaking gel Degree is big, of high cost, reuses poor feasibility.Since the disadvantages described above of the plant gum fracturing fluids such as guanidine glue can neither alleviate environmentally friendly pressure Power cannot meet above-mentioned site operation requirement again, so extensive at present use polymerization species fracturing fluid to solve the above problems.
Acrylamide copolymer thickener kind used at present is more, wherein with guanidine glue and its thickener of derivative It is most widely used, but generally existing breaks the problems such as glue is not thorough, easily returns glue, breaking glue solution residue content is higher, is easy to form blocking Injury causes matrix permeability and fracture condudtiviy to decline, to influence fracturing transformation effect, while natural plant gum class fracturing fluid Pipeline frictional resistance is higher, causes well head pressure under same displacement higher, and more water horse power is caused to be lost and higher construction risk. Synthesized polymer species thickener includes mainly polyacrylamide, Sodium Polyacrylate, polyacrylate and polyvinyl alcohol etc., is generally had There is the features such as strong, the broken colloidality of thickening capabilities can be good, residue is few, but cost is generally higher, does not utilize field popularization application.It is same with this When, since low temperature reservoir temperature is relatively low, polymer fracturing fluid is particularly prominent due to the larger not degradable disadvantage performance of molecular weight Go out, certain injury is caused to stratum.It is current low to meet therefore, it is necessary to form a kind of new slippery water fracturing fluid system The needs of warm reservoir densification oil-gas reservoir reservoir reconstruction.
Invention content
The purpose of the present invention is developing a kind of low temperature reservoir slippery water fracturing fluid, low viscosity, low frictional resistance, low disclosure satisfy that The fracturing fluid system of the features such as cost, the easily row of returning, easy recycling, while glue can be broken rapidly in low temperature reservoir, it reduces to stratum Injury, so as to more preferably meet low permeability oil and gas field low temperature reservoir reconstruction needs.
For this purpose, the present invention provides a kind of low temperature reservoir slippery water fracturing fluids, by following component and its mass percent Composition:
Thickener 0.15%-0.25%
Clay stabilizer 0.03%-0.05%
Structural stabilizing agent 0.20%-0.30%
Low-temp activation agent 0.05%-0.10%
Gel breaker 0.02%-0.05%
Remaining composition is water.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 30% ~ 50%, emulsifier 1% ~ 2%, cause hydrophobicity acrylmonomers 3% ~ 5% Agent 0.2% ~ 0.5%, latency crosslinking agent and surplus water, wherein the latency crosslinking agent accounts for the hydrophily acrylic The 0.5% ~ 1.8% of monomer and the hydrophobicity acrylmonomers quality sum.
The hydrophily acrylmonomers are by acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics It mixes, the mass ratio of the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics is 14:3:3;
The hydrophobicity acrylmonomers are by octadecyl acrylate, octadecyl methacrylate, methoxy poly (ethylene glycol) methyl One kind or more in acrylate, maleic acid single-long-chain alkyl ester sodium salt, Long carbon chain alkyl dimethyl allyl ammonium chloride Kind mixes;
The emulsifier is by sorbitan fatty acid ester, alkyl phenol polyoxyethylene ether, neopelex, dodecane One or more in base sodium sulfonate or lauryl sodium sulfate mix;
The initiator is by ammonium persulfate, potassium peroxydisulfate, ammonium persulfate-sodium sulfite, potassium peroxydisulfate-sodium sulfite, over cure One or more in sour ammonium-sodium thiosulfate, potassium peroxydisulfate-sodium thiosulfate or water-soluble azo initiator mix;
The latency crosslinking agent is mixed by one or both of hydroxy-ethyl acrylate and hydroxyethyl methacrylate.
The clay stabilizer is quaternary ammonium salt, and quaternary ammonium salt is by trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl One or both of ammonium bromide mixes base season, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide Mass ratio is 1:1 ~ 1.5, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine And its hydrochloride reacts generation with epoxychloropropane, butane, pentamethylene.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with Methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, methacrylic acid fourth Ester, Hexyl 2-propenoate, hexyl methacrylate, octadecyl acrylate, octadecyl methacrylate or methoxy poly (ethylene glycol) first One or more and aluminium citrate compounding in base acrylate dissolves, the ethylene oxide, propylene oxide and 2- first The mass ratio of base acrylic acid is 1.0-1.5:0. 2 -0.3:1, pure substance and methyl acrylate, methyl methacrylate, propylene Acetoacetic ester, ethyl methacrylate, butyl acrylate, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate, third One or more and citric acid in olefin(e) acid octadecyl ester, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer The mass ratio of aluminium is 6-8:1-2:1.
The low-temp activation agent is mixed by one or more of hydrochloric acid, citric acid, acetic acid, gluconic acid.
The gel breaker is mixed by one kind in ammonium persulfate, potassium peroxydisulfate, hydrogen peroxide, magnesium hypochlorite with L-AA It closes.
Compared with the prior art, the present invention has the following advantages:
(1)Easily swelling, may be implemented continuous mixture;
(2)It can be by adjusting thickener concentration, it can be achieved that whole process takes sand;
(3)It is not susceptible to bacteria effect, is not easy corruption;Heat resistance is good;
(4)Construction friction is low, it can be achieved that huge discharge is continuously constructed;
(5)It returns drain recycling and only needs to do that simple filtration processing is i.e. reusable, and simple for process, utilization rate is high;
(6)Glue can be broken rapidly at low ambient temperatures, reservoir damage is small.
Specific implementation mode
Embodiment 1:
A kind of low temperature reservoir slippery water fracturing fluid, by following component and its mass percentage composition:Thickener 0.15%- 0.25%, clay stabilizer 0.03%-0.05%, structural stabilizing agent 0.20%-0.30%, low-temp activation agent 0.05%-0.10%, broken glue Agent 0.02%-0.05%, remaining composition are water.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 30% ~ 50%, emulsifier 1% ~ 2%, cause hydrophobicity acrylmonomers 3% ~ 5% Agent 0.2% ~ 0.5%, latency crosslinking agent and surplus water, wherein the latency crosslinking agent accounts for the hydrophily acrylic The 0.5% ~ 1.8% of monomer and the hydrophobicity acrylmonomers quality sum.
The hydrophily acrylmonomers are by acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics It mixes, the mass ratio of the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics is 14:3:3;
The hydrophobicity acrylmonomers are by octadecyl acrylate, octadecyl methacrylate, methoxy poly (ethylene glycol) methyl One kind or more in acrylate, maleic acid single-long-chain alkyl ester sodium salt, Long carbon chain alkyl dimethyl allyl ammonium chloride Kind mixes;
The emulsifier is by sorbitan fatty acid ester, alkyl phenol polyoxyethylene ether, neopelex, dodecane One or more in base sodium sulfonate or lauryl sodium sulfate mix;
The initiator is by ammonium persulfate, potassium peroxydisulfate, ammonium persulfate-sodium sulfite, potassium peroxydisulfate-sodium sulfite, over cure One or more in sour ammonium-sodium thiosulfate, potassium peroxydisulfate-sodium thiosulfate or water-soluble azo initiator mix;
The latency crosslinking agent is mixed by one or both of hydroxy-ethyl acrylate and hydroxyethyl methacrylate.
The clay stabilizer is quaternary ammonium salt, and quaternary ammonium salt is by trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl One or both of ammonium bromide mixes base season, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide Mass ratio is 1:1 ~ 1.5, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine And its hydrochloride reacts generation with epoxychloropropane, butane, pentamethylene.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with Methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, butyl acrylate, methacrylic acid fourth Ester, Hexyl 2-propenoate, hexyl methacrylate, octadecyl acrylate, octadecyl methacrylate or methoxy poly (ethylene glycol) first One or more and aluminium citrate compounding in base acrylate dissolves, the ethylene oxide, propylene oxide and 2- first The mass ratio of base acrylic acid is 1.0-1.5:0. 2 -0.3:1, pure substance and methyl acrylate, methyl methacrylate, propylene Acetoacetic ester, ethyl methacrylate, butyl acrylate, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate, third One or more and citric acid in olefin(e) acid octadecyl ester, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer The mass ratio of aluminium is 6-8:1-2:1.
The low-temp activation agent is mixed by one or more of hydrochloric acid, citric acid, acetic acid, gluconic acid.
The gel breaker is mixed by one kind in ammonium persulfate, potassium peroxydisulfate, hydrogen peroxide, magnesium hypochlorite with L-AA It closes.
The present invention low temperature reservoir be with the preparation method of slippery water fracturing fluid:It is full of in container at the scene and matches liquid water, Again with thickener is slowly added in the case of pump circulation, then press successively formula rate be added clay stabilizer, low-temp activation agent, Gel breaker continues 20 minutes to ensure that liquid mixes well, forms homogeneous solution, then add structural stabilizing agent, fully follow Slippery water fracturing fluid is formed after ring.
This low temperature reservoir provided by the invention is easily swollen with slippery water fracturing fluid, and continuous mixture may be implemented;It can lead to Adjustment thickener concentration is crossed, it can be achieved that whole process takes sand;It is not susceptible to bacteria effect, is not easy corruption;Heat resistance is good;Construction friction It is low, it can be achieved that huge discharge is continuously constructed;Returning drain recycling, only to need to do simple filtration processing i.e. reusable, simple for process, Utilization rate is high;Glue can be broken rapidly at low ambient temperatures, reservoir damage is small.
Embodiment 2:
It is taken by following component and its mass percent:Thickener 0.15%, trimethyl hydroxypropyl season ammonium chloride or trimethyl hydroxypropyl Season ammonium bromide 0.03%, structural stabilizing agent 0.20%, hydrochloric acid or citric acid 0.05%, gel breaker 0.02%, water surplus.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 30%, emulsifier 1%, initiator 0.2%, are dived at hydrophobicity acrylmonomers 3% The water of volt property crosslinking agent and surplus, wherein the latency crosslinking agent accounts for hydrophily acrylmonomers and described hydrophobic The 0.5% of property acrylmonomers quality sum.The hydrophily acrylmonomers are by acrylamide, methacrylic acid and 2- propylene Amide -2- methyl propane sulfonic acids mix, the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics Mass ratio is 14:3:3;The hydrophobicity acrylmonomers are by one kind in octadecyl acrylate, octadecyl methacrylate Or two kinds mix;The emulsifier is by one kind or two in sorbitan fatty acid ester and alkyl phenol polyoxyethylene ether Kind mixes;The initiator is by one or more mixed in ammonium persulfate, potassium peroxydisulfate, ammonium persulfate-sodium sulfite It closes;The latency crosslinking agent is hydroxy-ethyl acrylate.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with In methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate one or more compoundings dissolving and At the mass ratio of the ethylene oxide, propylene oxide and 2- methacrylic acids is 1.0:0. 2 :1, pure substance and acrylic acid One or more and aluminium citrate in methyl esters, methyl methacrylate, ethyl acrylate, ethyl methacrylate compounds mixed The mass ratio for closing object is 6:2:1.
The gel breaker is mixed by one kind in ammonium persulfate, potassium peroxydisulfate with L-AA.
Specifically operating method is:
At the scene in 50 m3 containers full of matching liquid water, then with thickener 0.15% is slowly added in the case of pump circulation, then Formula rate is pressed successively, trimethyl hydroxypropyl season ammonium chloride 0.03%, hydrochloric acid or citric acid 0.05%, gel breaker 0.02% is added, hold To ensure that liquid mixes well, homogeneous solution is formed, structural stabilizing agent 0.20% is then added within continuous 20 minutes, fully after cycle Form slippery water fracturing fluid.The low temperature reservoir with slippery water fracturing fluid viscosity is 4.5mpas, drag reducing efficiency 68%, low cost compared with Conventional guanidine colloid system reduces by 66%, and it is 98.4% that the row of returning, which leads, easily recycling, and cost reduction 20% is reusable, environmentally protective.
Embodiment 3:
It is taken by following component and its mass percent:Thickener 0.25%, clay stabilizer 0.05%, structural stabilizing agent 0.30%, vinegar Acid or gluconic acid 0.1%, gel breaker 0.05%, water surplus.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 50%, emulsifier 2%, initiator 0.5%, are dived at hydrophobicity acrylmonomers 5% The water of volt property crosslinking agent and surplus, wherein the latency crosslinking agent accounts for hydrophily acrylmonomers and described hydrophobic The 1.8% of property acrylmonomers quality sum.The hydrophily acrylmonomers are by acrylamide, methacrylic acid and 2- propylene Amide -2- methyl propane sulfonic acids mix, the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics Mass ratio is 14:3:3;The hydrophobicity acrylmonomers are by methoxy polyethylene glycol methacrylate-styrene polymer, maleic acid One or both of single-long-chain alkyl ester sodium salt mixes;The emulsifier is by neopelex, dodecane One or both of base sodium sulfonate mixes;The initiator is thio by potassium peroxydisulfate-sodium sulfite, ammonium persulfate- One or more in sodium sulphate mix;The latency crosslinking agent is hydroxyethyl methacrylate.
The clay stabilizer is quaternary ammonium salt, and quaternary ammonium salt is by trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl Base season, ammonium bromide mixed, trimethyl hydroxypropyl season ammonium chloride and the mass ratio of trimethyl hydroxypropyl season ammonium bromide be 1:1, three Methylhydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine and its hydrochloride and epoxy chlorine Propane, butane, pentamethylene reaction generate.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with In butyl acrylate, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate one or more compoundings dissolving and At the mass ratio of the ethylene oxide, propylene oxide and 2- methacrylic acids is 1.5:0.3:1, pure substance and acrylic acid fourth The mixing of one or more and aluminium citrate compounding in ester, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate The quality of object is 8:1:1.
The gel breaker is mixed by one kind in hydrogen peroxide, magnesium hypochlorite with L-AA.
Specifically operating method is:
At the scene in 50 m3 containers full of matching liquid water, then with thickener 0.25% is slowly added in the case of pump circulation, then Press formula rate successively and clay stabilizer 0.05%, acetic acid or gluconic acid 0.1%, gel breaker 0.05% be added, continue 20 minutes with Ensure that liquid mixes well, form homogeneous solution, then add structural stabilizing agent 0.30%, fully forms slippery water after cycle Fracturing fluid.The low temperature reservoir with slippery water fracturing fluid viscosity is 4.2mpas, drag reducing efficiency 69%, the more conventional guanidine colloid of low cost System reduces by 65%, and it is 98.7% that the row of returning, which leads, easily recycling, and cost reduction 25% is reusable, environmentally protective.
Embodiment 4:
It is taken by following component and its mass percent:Thickener 0.20%, clay stabilizer 0.04%, structural stabilizing agent 0.25%, vinegar Mixture 0.75%, the gel breaker 0.35% of acid and hydrochloric acid, water surplus.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 40%, hydrophobicity acrylmonomers 4%, emulsifier 1.5%, initiator 0.35%, The water of latency crosslinking agent and surplus, wherein the latency crosslinking agent account for the hydrophily acrylmonomers and it is described dredge The 1.15% of aqueous acrylamide base monomer mass sum.The hydrophily acrylmonomers are by acrylamide, methacrylic acid and 2- third Acrylamide -2- methyl propane sulfonic acids mix, the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics Mass ratio be 14:3:3;The hydrophobicity acrylmonomers are Long carbon chain alkyl dimethyl allyl ammonium chloride;Described Emulsifier is lauryl sodium sulfate;The initiator is by potassium peroxydisulfate-sodium thiosulfate or water-soluble azo initiator One or more mix;The latency crosslinking agent by hydroxy-ethyl acrylate and hydroxyethyl methacrylate mixing and At.
The clay stabilizer is quaternary ammonium salt, and quaternary ammonium salt is by trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl Base season, ammonium bromide mixed, trimethyl hydroxypropyl season ammonium chloride and the mass ratio of trimethyl hydroxypropyl season ammonium bromide be 1:1.5 Trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine and its hydrochloride and epoxy Chloropropane, butane, pentamethylene reaction generate.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with One or more compoundings in octadecyl acrylate, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer are molten It solves, the mass ratio of the ethylene oxide, propylene oxide and 2- methacrylic acids is 1.25:0.25:1, pure substance and third One or more and citric acid in olefin(e) acid octadecyl ester, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer The mass ratio of the mixture of aluminium compounding is 7:1.5:1.
The gel breaker is mixed by ammonium sulfate and L-AA.
Specifically operating method is:
At the scene in 50 m3 containers full of matching liquid water, then with thickener 0.20% is slowly added in the case of pump circulation, then Formula rate is pressed successively, clay stabilizer 0.04%, the mixture 0.75% of acetate and hydrochloride, gel breaker 0.35% is added, continue 20 Minute to ensure that liquid mixes well, forms homogeneous solution, then adds structural stabilizing agent 0.25%, is fully formed after cycle Slippery water fracturing fluid.The low temperature reservoir with slippery water fracturing fluid viscosity is 4.1mpas, drag reducing efficiency 70%, low cost are more conventional Guanidine colloid system reduces by 68%, and it is 98.9% that the row of returning, which leads, easily recycling, and cost reduction 27% is reusable, environmentally protective.
Embodiment 5:
It is taken by following component and its mass percent:Thickener 0.19%, clay stabilizer 0.35%, structural stabilizing agent 0.27%, lemon The mixture 0.70% of lemon acid and gluconic acid, gel breaker 0.38%, water surplus.
The thickener is acrylamide copolymer, and the acrylamide copolymer is by following component and its matter Measure percentage composition:Hydrophily acrylmonomers 38%, hydrophobicity acrylmonomers 3.7%, emulsifier 1.7%, initiator 0.40%, the water of latency crosslinking agent and surplus, wherein the latency crosslinking agent account for the hydrophily acrylmonomers and The 1.3% of the hydrophobicity acrylmonomers quality sum.The hydrophily acrylmonomers are by acrylamide, methacrylic acid It is mixed with 2- acrylamide-2-methyl propane sulfonics, the acrylamide, methacrylic acid and 2- acrylamide -2- methyl The mass ratio of propane sulfonic acid is 14:3:3;The hydrophobicity acrylmonomers are by octadecyl methacrylate, Long carbon chain alkyl two One or both of methacrylic chlorination ammonium mixes;The emulsifier is lauryl sodium sulfate;Described draws Hair agent is mixed by one or more in ammonium persulfate-sodium sulfite or potassium peroxydisulfate-sodium thiosulfate;The latency Crosslinking agent is hydroxyethyl methacrylate.
The clay stabilizer is quaternary ammonium salt, and quaternary ammonium salt is by trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl Base season, ammonium bromide mixed, trimethyl hydroxypropyl season ammonium chloride and the mass ratio of trimethyl hydroxypropyl season ammonium bromide be 1: 1.25, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine and its hydrochloride Generation is reacted with epoxychloropropane, butane, pentamethylene.
The structural stabilizing agent by ethylene oxide, propylene oxide and 2- methacrylic acids reaction purification after pure substance with One or more compoundings in octadecyl acrylate, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer are molten It solves, the mass ratio of the ethylene oxide, propylene oxide and 2- methacrylic acids is 1.2:0.2:1, pure substance and propylene One or more and aluminium citrate in sour octadecyl ester, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer The mixture quality ratio of compounding is 7:1.3:1.
The gel breaker is mixed by hydrogen peroxide and L-AA.
Specifically operating method is:
At the scene in 50 m3 containers full of matching liquid water, then with thickener 0.19% is slowly added in the case of pump circulation, then Clay stabilizer 0.35%, citric acid and gluconic acid is added in formula rate mixture 0.70%, gel breaker 0.38% are pressed successively, Continue 20 minutes to ensure that liquid mixes well, form homogeneous solution, then add structural stabilizing agent 0.27%, fully recycles Slippery water fracturing fluid is formed afterwards.The low temperature reservoir with slippery water fracturing fluid viscosity is 4.0mpas, drag reducing efficiency 71%, low cost More conventional guanidine colloid system reduces by 67%, and it is 98.6% that the row of returning, which leads, easily recycling, and cost reduction 28% is reusable, environmentally protective.
The foregoing examples are only illustrative of the present invention, does not constitute the limitation to protection scope of the present invention, all Be with the present invention it is same or analogous design all belong to the scope of protection of the present invention within.

Claims (7)

1. a kind of low temperature reservoir slippery water fracturing fluid, it is characterised in that:By following component and its mass percentage composition:
Thickener 0.15%-0.25%
Clay stabilizer 0.03%-0.05%
Structural stabilizing agent 0.20%-0.30%
Low-temp activation agent 0.05%-0.10%
Gel breaker 0.02%-0.05%
Remaining composition is water.
2. low temperature reservoir slippery water fracturing fluid as described in claim 1, it is characterised in that:The thickener is acryloyl Amine polymer, the acrylamide copolymer is by following component and its mass percentage composition:Hydrophily acrylic list Body 30% ~ 50%, hydrophobicity acrylmonomers 3% ~ 5%, emulsifier 1% ~ 2%, initiator 0.2% ~ 0.5%, latency crosslinking agent and The water of surplus, wherein the latency crosslinking agent accounts for the hydrophily acrylmonomers and the hydrophobicity acrylmonomers The 0.5% ~ 1.8% of quality sum.
3. low temperature reservoir slippery water fracturing fluid as claimed in claim 2, it is characterised in that:
The hydrophily acrylmonomers are mixed by acrylamide, methacrylic acid with 2- acrylamide-2-methyl propane sulfonics It forms, the mass ratio of the acrylamide, methacrylic acid and 2- acrylamide-2-methyl propane sulfonics is 14:3:3;
The hydrophobicity acrylmonomers are by octadecyl acrylate, octadecyl methacrylate, methoxy poly (ethylene glycol) methyl One kind or more in acrylate, maleic acid single-long-chain alkyl ester sodium salt, Long carbon chain alkyl dimethyl allyl ammonium chloride Kind mixes;
The emulsifier is by sorbitan fatty acid ester, alkyl phenol polyoxyethylene ether, neopelex, dodecane One or more in base sodium sulfonate or lauryl sodium sulfate mix;
The initiator is by ammonium persulfate, potassium peroxydisulfate, ammonium persulfate-sodium sulfite, potassium peroxydisulfate-sodium sulfite, over cure One or more in sour ammonium-sodium thiosulfate, potassium peroxydisulfate-sodium thiosulfate or water-soluble azo initiator mix;
The latency crosslinking agent is mixed by one or both of hydroxy-ethyl acrylate and hydroxyethyl methacrylate.
4. low temperature reservoir slippery water fracturing fluid as claimed in claim 3, it is characterised in that:The clay stabilizer is season Ammonium salt class, quaternary ammonium salt are mixed by one or both of trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide Form, trimethyl hydroxypropyl season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide mass ratio be 1:1 ~ 1.5, trimethyl hydroxypropyl Season ammonium chloride and trimethyl hydroxypropyl season ammonium bromide by trimethyl tertiary amine, dimethylamine and its hydrochloride and epoxychloropropane, butane, Pentamethylene reaction generates.
5. low temperature reservoir slippery water fracturing fluid as claimed in claim 4, it is characterised in that:The structural stabilizing agent is by ring Pure substance after oxidative ethane, propylene oxide and the reaction purification of 2- methacrylic acids and methyl acrylate, methyl methacrylate, third Olefin(e) acid ethyl ester, ethyl methacrylate, butyl acrylate, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate, One or more and lemon in octadecyl acrylate, octadecyl methacrylate or methoxy polyethylene glycol methacrylate-styrene polymer Sour aluminium compounding dissolves, and the mass ratio of the ethylene oxide, propylene oxide and 2- methacrylic acids is 1.0-1.5:0. 2 -0.3:1, pure substance and methyl acrylate, methyl methacrylate, ethyl acrylate, ethyl methacrylate, acrylic acid fourth Ester, butyl methacrylate, Hexyl 2-propenoate, hexyl methacrylate, octadecyl acrylate, octadecyl methacrylate or first The mass ratio of one or more and aluminium citrate in oxygroup polyethylene glycol methacrylate-styrene polymer is 6-8:1-2:1.
6. low temperature reservoir slippery water fracturing fluid as claimed in claim 5, it is characterised in that:The low-temp activation agent is by salt One or more of acid, citric acid, acetic acid, gluconic acid mix.
7. low temperature reservoir slippery water fracturing fluid as claimed in claim 6, it is characterised in that:The gel breaker is by persulfuric acid One kind in ammonium, potassium peroxydisulfate, hydrogen peroxide, magnesium hypochlorite is mixed with L-AA.
CN201711441220.8A 2017-12-27 2017-12-27 Slickwater fracturing fluid for low-temperature reservoir Pending CN108587593A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110295036A (en) * 2019-06-14 2019-10-01 中国石油天然气股份有限公司 Slickwater fracturing fluid for medium-high temperature compact reservoir and preparation method thereof
CN110437818A (en) * 2019-08-23 2019-11-12 西南石油大学 A kind of broken glue activator and preparation method thereof suitable for 20-50 DEG C of reservoir fracturing
CN111234796A (en) * 2020-01-21 2020-06-05 中国石油天然气股份有限公司 Surfactant and preparation method thereof
CN111378424A (en) * 2020-03-25 2020-07-07 大庆油田有限责任公司 Continuous sand-carrying slick water system
CN116200183A (en) * 2023-03-02 2023-06-02 四川申和新材料科技有限公司 High-efficiency variable-viscosity fracturing fluid for deep coal bed gas development and integrated construction method

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101595199A (en) * 2007-01-23 2009-12-02 哈利伯顿能源服务公司 The Tackified polymeric that makes that is used for downhole well applications breaks the composition and the method for glue at extremely low temperature
CN103666437A (en) * 2012-09-18 2014-03-26 中国石油天然气股份有限公司 Fracturing fluid
CN105008661A (en) * 2013-02-27 2015-10-28 阿科玛股份有限公司 Promoters for peroxides in aqueous treatment fluids
CN106146730A (en) * 2015-03-25 2016-11-23 中国石油天然气股份有限公司 Acrylamide polymer thickener, preparation method thereof and fracturing fluid

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101595199A (en) * 2007-01-23 2009-12-02 哈利伯顿能源服务公司 The Tackified polymeric that makes that is used for downhole well applications breaks the composition and the method for glue at extremely low temperature
CN103666437A (en) * 2012-09-18 2014-03-26 中国石油天然气股份有限公司 Fracturing fluid
CN105008661A (en) * 2013-02-27 2015-10-28 阿科玛股份有限公司 Promoters for peroxides in aqueous treatment fluids
CN106146730A (en) * 2015-03-25 2016-11-23 中国石油天然气股份有限公司 Acrylamide polymer thickener, preparation method thereof and fracturing fluid

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110295036A (en) * 2019-06-14 2019-10-01 中国石油天然气股份有限公司 Slickwater fracturing fluid for medium-high temperature compact reservoir and preparation method thereof
CN110437818A (en) * 2019-08-23 2019-11-12 西南石油大学 A kind of broken glue activator and preparation method thereof suitable for 20-50 DEG C of reservoir fracturing
CN111234796A (en) * 2020-01-21 2020-06-05 中国石油天然气股份有限公司 Surfactant and preparation method thereof
CN111378424A (en) * 2020-03-25 2020-07-07 大庆油田有限责任公司 Continuous sand-carrying slick water system
CN116200183A (en) * 2023-03-02 2023-06-02 四川申和新材料科技有限公司 High-efficiency variable-viscosity fracturing fluid for deep coal bed gas development and integrated construction method
CN116200183B (en) * 2023-03-02 2024-05-28 四川申和新材料科技有限公司 High-efficiency variable-viscosity fracturing fluid for deep coal bed gas development and integrated construction method

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Application publication date: 20180928