CN105419772B - A kind of thinner of polyacrylamide polymer - Google Patents

A kind of thinner of polyacrylamide polymer Download PDF

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Publication number
CN105419772B
CN105419772B CN201510999126.9A CN201510999126A CN105419772B CN 105419772 B CN105419772 B CN 105419772B CN 201510999126 A CN201510999126 A CN 201510999126A CN 105419772 B CN105419772 B CN 105419772B
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thinner
viscosity
agent
polyacrylamide
polyacrylamide polymer
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CN105419772A (en
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黄亚杰
徐毓珠
汪晋
韩玲
饶翔
李保林
朱志芳
李少明
张诚东
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China Petrochemical Corp
Petroleum Engineering Technology Research Institute of Sinopec Jianghan Oilfield Co
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Petroleum Engineering Technology Research Institute of Sinopec Jianghan Oilfield Co
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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
    • 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
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • 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
    • C09K2208/32Anticorrosion additives

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
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Abstract

The present invention relates to a kind of thinners of polyacrylamide polymer, as mass fraction by as follows at being grouped as:Salinity conditioning agent 2.2 30%, viscosity modifier 0.1 0.5%, surfactant 0.1 0.5%, corrosion inhibiter 0.5 2%, cleaning agent 0.1 1%, surplus are water, and the sum of each component is 100%.Thinner provided by the present invention can realize quick viscosity reduction polyacrylamide polymer, carry out viscosity reduction to polypropylene amine amide polymer fracturing fluid, the liquid viscosity after viscosity reduction tends to water, is easy to the row of returning.

Description

A kind of thinner of polyacrylamide polymer
Technical field
The invention belongs to oilfield prospecting developing fields, and in particular to a kind of thinner of polyacrylamide polymer.
Background technology
World's conventional gas stock number is 436 tcms, and shale gas is then up to 456,000,000,000,000 sides (according to EIA), is One of the important development direction of the following clean energy resource.Chinese shale gas reserves are extremely abundant, are mainly distributed on the Sichuan Basin, E Er The areas such as this more basin, Bohai gulf basin, Song-liao basin, Tarim Basin and the Junggar Basin, domestic relevant unit's assessment Technically recoverable resources are more than 10 tcms.And assessed according to EIA, in each main shale gas resource distribution state of the world, China occupies the first in the world with the mining resources amount of 36.1 tcms.Country's shale gas exploitation at present, frequently with horizontal well " drag reduction water+glue " is segmented Sand Fracturing Technology on a large scale, and polyacrylamide polymer and derivative are in fracturing process It can be attached in shaft column and stratum, block pit shaft or stratum, influence construction progress and well yield.
Moreover, for polyacrylamide polymer and derivative fracturing fluid, usually adopted in subsequent treatment process With ammonium persulfate as broken colloid system come viscosity reduction polymer, ammonium persulfate breaks colloid system, and there are the shortcomings of following several respects: (1) ammonium persulfate gel breaking time is long.The half-life period of ammonium persulfate is 8h at 70 DEG C;The half-life period of ammonium persulfate is at 50 DEG C 152h is decomposed too slow;At a temperature of less than 50 DEG C, ammonium persulfate gel breaking capacity declines rapidly, cannot function as aqueous fracturing fluid Gel breaker.(2) glue is broken to be not thorough.In pressing crack construction process, under the premise of ensureing smoothly to take sand, optimize breaker concentration, soon Fast thoroughly broken glue, but fracturing fluid, in pumping and crack closure, due to fluid loss, polymer concentration can increase 5-7 times, gather The concentration for closing object carrys out bigger difficulty to broken adhesive tape.
Chinese patent CN101104844B discloses a kind of sulfate reducing bacteria with polyacrylamide viscosity reduction function And its application, viscosity reduction is carried out to polyacrylamide using sulfate reducing bacteria, but sulfate reducing bacteria is a kind of anaerobic bacteria, and And need suitable growth and breeding environment, it is important to which the sulfate reducing bacteria of high concentration is limited to high concentration polymer viscosity reduction.In State patent CN103043830A discloses a kind of method of polyacrylamide with chlorine dioxide by acid activator viscosity reduction, environment pH For 4-12, then causes chlorine dioxide decomposition using hydrochloric acid or phosphoric acid and generate free radicals, it is poly- that production generates peroxide viscosity reduction Acrylamide, but the strong acid such as hydrochloric acid to be added in activation process, different degrees of corrosion can be caused to flow string;Moreover, Free radical is discharged by chlorine dioxide and carries out viscosity reduction, and the viscosity reduction time related with temperature oil is long.
In addition, " polyacrylamide viscosity-reducing mechanism is studied in oilfield sewage ", petrochemical industry application;" the change of polyacrylamide Learn viscosity reduction research ", Daqing Petroleum Institute's journal;" chemical viscosity reduction of polyacrylamide is studied ", oil gas field environmental protection is situated between respectively Continue the distinct methods of polyacrylamide viscosity reduction, at present on oil field the most commonly used is oxidizing reduction, using reproducibility object is added in document Redox reaction occurs for matter and strong oxidizer, and release generates free radicals viscosity reduction polyacrylamide, but these methods all with temperature It is related, and viscosity reduction speed is slower.
Invention content
The technical problem to be solved by the present invention is to provide a kind of polypropylene in view of the deficiency of the prior art The thinner of acylamide polymer, has using concentration under low, room temperature that viscosity reduction speed is fast, liquid viscosity tends to water, easily after viscosity reduction The characteristics of row of returning.
The present invention be solve the problems, such as it is set forth above used by technical solution be:
A kind of thinner of polyacrylamide polymer, as mass fraction by as follows at being grouped as:Salinity is adjusted Agent 2.2-30%, viscosity modifier 0.1-0.5%, surfactant 0.1-0.5%, corrosion inhibiter 0.5-2%, cleaning agent 0.1- 1%, surplus is water, and the sum of each component is 100%.
By said program, the polyacrylamide polymer is polyacrylamide polymers and its derivative.
By said program, the one kind of the salinity conditioning agent in sodium chloride, potassium chloride, magnesium chloride, calcium chloride etc. Or several mixtures in any proportion.Preferably, the salinity conditioning agent is as mass fraction by as follows at being grouped as:5- 50%KCl, 5-50%NaCl, 0.5-25%MgCl2And 0.5-25%CaCl2.It is highly preferred that the salinity conditioning agent presses matter Amount score meter is by as follows at being grouped as:30-50%KCl, 30-50%NaCl, 3-20%MgCl2And 3-20%CaCl2
By said program, the viscosity modifier is selected from citric acid.
By said program, the surfactant is fluorine carbon surfactant.
By said program, the corrosion inhibiter is organic phosphate corrosion inhibiter.
By said program, the cleaning agent is iron chloride, frerrous chloride.
The preparation method of the thinner of above-mentioned polyacrylamide polymer, includes the following steps:
(1) following ingredient is weighed as mass fraction:Salinity conditioning agent 1.2-30%, viscosity modifier 0.1-0.5%, Surfactant 0.1-0.5%, corrosion inhibiter 0.5-2%, cleaning agent 0.1-1%, surplus are water, and the sum of each component is 100%;
(2) step (1) described proportioning is pressed, salinity conditioning agent is added into water, fully dissolving is stirred, surface is then added After activating agent and viscosity modifier stir evenly, cleaning agent and corrosion inhibiter are added, stirring is to being completely dissolved to get to polypropylene The thinner of acylamide polymer.
The application process of the thinner of above-mentioned polyacrylamide polymer is:To containing polyacrylamide polymer The thinner is added in solution, thinner addition is the 0.1wt%- of the solution quality for containing polyacrylamide polymer 0.5wt% reacts 30-120s under room temperature, which is reduced to 1.1-1.5mPas.
In application process, the solution containing polyacrylamide polymers is usually fracturing fluid, and polyacrylamide is poly- It closes amount of substance concentration and is usually less than 1%;And the amount of thinner can be taken the circumstances into consideration to adjust according to concentration, cost and time.
The principle of the present invention is:The main ingredient of drag reduction water and glue is polyacrylamide and its derivative, the substance Hydrophily is extremely strong, soluble easily in water, can form hydrogen bond with water, after aquation, electrical function occurs for strand, and strand is made to obtain greatly Stretching, extension play the role of thickening to obtain larger hydrodynamics volume, still, the strand be flexible chain, in mineralising It spends in the salting liquid that conditioning agent is formed, strand can crimp, to reduce viscosity;And the carboxylate radical in viscosity modifier from Electric repulsion between son, makes polymer coils roll up, and apparent size reduces, and unfolding degree reduction in water can effectively drop The viscosity of low polymer solution increases mobility;And so that polyacrylamide polymer is shown in aqueous solution bright for cleaning agent Aobvious viscosity loss, viscosity reduction is extremely serious, can lose most viscosity within a very short time, lose performance completely. In addition, the present invention also added corrosive agent and surfactant, the quick row of returning and protection shaft column can be played the role of.
Compared with prior art, the beneficial effects of the invention are as follows:
First, thinner provided by the present invention can realize quick viscosity reduction polyacrylamide polymer, to high concentration Polypropylene amine amide polymer fracturing fluid carries out viscosity reduction, and the liquid viscosity after viscosity reduction tends to water, is easy to the row of returning.
Second, use condition of the present invention is extensive, and dosage is few, low using concentration, simple and practicable with liquid, room temperature lower short time energy Enough realize quick viscosity reduction, no particular/special requirement will not damage the devices such as tubing string in work progress.
Third, thinner of the present invention carry charge and molecular structure by itself, polymer molecule can be made to wad a quilt with cotton Retrogradation is formed sediment, and so that polyacrylamide polymer is shown apparent viscosity loss in aqueous solution, need not be added any initiation Agent;Moreover, ferric ion and other metal ion synergistics is directly applied to act on to polyacrylamide polymer molecular structure Influence, so that polyacrylamide polymer is rolled up viscosity reduction in aqueous solution, feature is that reaction speed is fast, and the viscosity reduction time is short, this Outer ferric ion performance is stablized, easy to operate in constructing at the scene.
4th, group contained by thinner of the present invention is divided into common medicine agent, and cheap easy purchase, preparation method is simple, Convenient for execute-in-place.
It blocks pipeline for existing in pit shaft caused by a large amount of concentration polyacrylamide polymers, influence construction progress Technical problem, quick thinner provided by the present invention can realize quick viscosity reduction and the row of returning, in shale gas high-efficiency mining process It is with a wide range of applications.
Description of the drawings
Fig. 1 is the apparent viscosity using 25 DEG C of 0.4wt% fracturing fluids used by test.
Fig. 2 is after thinner processing described in embodiment 1, using the apparent of 25 DEG C of 0.4wt% fracturing fluids used by test Viscosity.
Fig. 3 is after thinner processing described in embodiment 2, using the apparent of 25 DEG C of 0.4wt% fracturing fluids used by test Viscosity.
Fig. 4 is after thinner processing described in embodiment 3, using the apparent of 25 DEG C of 0.4wt% fracturing fluids used by test Viscosity.
Specific implementation mode
For a better understanding of the present invention, with reference to the embodiment content that the present invention is furture elucidated, but the present invention is not It is limited only to the following examples.
The performance test of thinner of the present invention, being applied to fracturing fluid, (specific formula of the fracturing fluid is 0.4% thick + 0.05% viscosity tune of+0.02% antifoaming agent of agent (polyacrylamide polymer)+0.3% auxiliary rheological agents of+0.15% synergist Section agent, surplus are water) it is tested, the fracturing fluid pH value partial neutral.Certainly, it is polyacrylamide that the present invention, which is suitable for thickening agent, And its fracturing fluid of derivative, fracturing fluid each component concentration can be different from formula provided by the invention.
Embodiment 1
A kind of thinner of polyacrylamide polymer, as mass fraction by as follows at being grouped as:Salinity is adjusted Agent 2.2%, viscosity modifier citric acid 0.5%, fluorocarbon surfactant 0.1%, organic phosphate corrosion inhibiter KD- GH022%, cleaning agent FeCl31%, surplus is water, and the sum of each component is 100%.Wherein, the salinity conditioning agent presses matter Amount score meter is by as follows at being grouped as:45.5%KCl, 45.5%NaCl, 4.5%MgCl2And 4.5%CaCl2
The preparation method of the thinner of above-mentioned polyacrylamide polymer, includes the following steps:By said ratio, measure Water pours into stirring container, and the whirlpool that adjusting agitator speed to liquid is formed can see propeller-blade axis top and be Only, salinity conditioning agent is added into water, is sufficiently stirred until be completely dissolved, adds fluorocarbon surfactant and citric acid, 4-5min is stirred, FeCl is eventually adding3And corrosion inhibiter, it is sufficiently stirred until being completely dissolved to get to polyacrylamide Type of Collective The thinner of object.
The application process of the thinner of above-mentioned polyacrylamide polymer is:To the polyacrylamide of concentration 0.4wt% The thinner of embodiment 1 is added in the fracturing fluid of Type of Collective object, thinner addition is the 0.4wt% of the fracturing fluid quality, is filled Divide stirring, it is 1.09mPas that 53s is reacted under room temperature to measure fracturing fluid viscosity.Test result is as depicted in figs. 1 and 2, and drop is added The apparent viscosity of the fracturing fluid is 86mPas when stick, and after 1 thinner 53s of example is added, apparent viscosity will be 1.09mPa s。
Embodiment 2
A kind of thinner of polyacrylamide polymer, as mass fraction by as follows at being grouped as:Salinity is adjusted Agent 30%, viscosity modifier citric acid 0.1%, fluorocarbon surfactant 0.5%, organic phosphate corrosion inhibiter KD- GH020.5%, cleaning agent FeCl30.1%, surplus is water, and the sum of each component is 100%.Wherein, the salinity conditioning agent As mass fraction by as follows at being grouped as:33.3%KCl, 33.3%NaCl, 16.7%MgCl2And 16.7%CaCl2
The preparation method of the thinner of above-mentioned polyacrylamide polymer, includes the following steps:By said ratio, measure Water pours into stirring container, and the whirlpool that adjusting agitator speed to liquid is formed can see propeller-blade axis top and be Only, salinity conditioning agent is added into water, is sufficiently stirred until be completely dissolved, adds fluorocarbon surfactant and citric acid, 4-5min is stirred, FeCl is eventually adding3And corrosion inhibiter, it is sufficiently stirred until being completely dissolved to get to polyacrylamide Type of Collective The thinner of object.
The application process of the thinner of above-mentioned polyacrylamide polymer is:To the polyacrylamide of concentration 0.4wt% The thinner of embodiment 2 is added in the fracturing fluid of Type of Collective object, thinner addition is the 0.4% of the fracturing fluid quality, fully It stirs, it is 1.21mPas that reaction 117s, which measures fracturing fluid viscosity, under room temperature.Test result is as shown in figures 1 and 3, and viscosity reduction is added The apparent viscosity of the fracturing fluid is 86mPas when agent, and after 2 thinner 117s of example is added, apparent viscosity will be 1.21mPa·s。
Embodiment 3
A kind of thinner of polyacrylamide polymer, as mass fraction by as follows at being grouped as:Salinity is adjusted Agent 16%, viscosity modifier citric acid 0.5%, fluorocarbon surfactant 0.2%, organic phosphate corrosion inhibiter KD- GH021.5%, cleaning agent FeCl30.4%, surplus is water, and the sum of each component is 100%.Wherein, the salinity conditioning agent As mass fraction by as follows at being grouped as:31.3%KCl, 31.3%NaCl, 18.8%MgCl2And 18.8%CaCl2
The preparation method of the thinner of above-mentioned polyacrylamide polymer, includes the following steps:By said ratio, measure Water pours into stirring container, and the whirlpool that adjusting agitator speed to liquid is formed can see propeller-blade axis top and be Only, salinity conditioning agent is added into water, is sufficiently stirred until be completely dissolved, adds fluorocarbon surfactant and citric acid, 4-5min is stirred, FeCl is eventually adding3And corrosion inhibiter, it is sufficiently stirred until being completely dissolved to get to polyacrylamide Type of Collective The thinner of object.
The application process of the thinner of above-mentioned polyacrylamide polymer is:To the polyacrylamide of concentration 0.4wt% The thinner of embodiment 3 is added in the fracturing fluid of Type of Collective object, thinner addition is the 0.4wt% of the fracturing fluid quality, is filled Divide stirring, it is 1.13mPas that 83s is reacted under room temperature to measure fracturing fluid viscosity.Test result is as shown in Figure 1 and Figure 4, and drop is added The apparent viscosity of the fracturing fluid is 86mPas when stick, and after 3 thinner 86s of example is added, apparent viscosity will be 1.13mPa s。
The above is only a preferred embodiment of the present invention, it is noted that come for those of ordinary skill in the art It says, without departing from the concept of the premise of the invention, several modifications and variations can also be made, these belong to the present invention's Protection domain.

Claims (4)

1. a kind of thinner of polyacrylamide polymer, it is characterised in that as mass fraction by as follows at being grouped as:Mine Change degree conditioning agent 2.2-30%, viscosity modifier 0.1-0.5%, surfactant 0.1-0.5%, corrosion inhibiter 0.5-2%, cleaning agent 0.1-1%, surplus are water, and the sum of each component is 100%;
The salinity conditioning agent is as mass fraction by as follows at being grouped as:30-50%KCl, 30-50%NaCl, 3-20%MgCl2 And 3-20%CaCl2;The cleaning agent is one or both of iron chloride or frerrous chloride;The viscosity modifier is lemon Lemon acid, the surfactant are fluorocarbon surfactant.
2. a kind of thinner of polyacrylamide polymer according to claim 1, it is characterised in that the corrosion inhibiter For organic phosphate corrosion inhibiter.
3. a kind of preparation method of the thinner of polyacrylamide polymer described in claim 1, it is characterised in that including Following steps:
(1)Following ingredient is weighed as mass fraction:Salinity conditioning agent 2.2-30%, viscosity modifier 0.1-0.5%, surface is lived Property agent 0.1-0.5%, corrosion inhibiter 0.5-2%, cleaning agent 0.1-1%, surplus is water, the sum of each component be 100%;
(2)By step(1)Salinity conditioning agent is added into water for the proportioning, stirs fully dissolving, surface-active is then added After agent and viscosity modifier stir evenly, cleaning agent and corrosion inhibiter are added, stirring is to being completely dissolved to get to polyacrylamide The thinner of Type of Collective object.
4. the application process of the thinner of polyacrylamide polymer described in claim 1, it is characterised in that containing poly- The thinner is added in the solution of acrylamide copolymer, the addition of thinner is the 0.1wt%- of the solution quality 0.5wt%, under room temperature after reaction 30-120s, the viscosity of the solution is reduced to 1.1-1.5mPas.
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CN105921053A (en) * 2016-05-31 2016-09-07 徐州工业职业技术学院 Gas-producing wet coal ash material stirring method and system
CN107762474B (en) * 2017-11-10 2020-05-08 中国石油天然气股份有限公司 Low-permeability heavy oil reservoir fracturing method
CN108641698A (en) * 2018-04-23 2018-10-12 谢新昇 A kind of preparation method of polydactyl acid base heavy crude thinner
MX2019012623A (en) 2018-10-22 2020-12-01 Chevron Usa Inc Treating fluid comprising hydrocarbons, water, and polymer.
CN112028292A (en) * 2019-06-04 2020-12-04 惠博普(武汉)生物环保科技有限公司 Viscosity reduction treatment method for polymer-containing sewage in oil field
CN113774692B (en) * 2021-11-01 2023-03-21 滨州东方地毯有限公司 Polyacrylamide paste for carpet and preparation method thereof
CN114890768B (en) * 2022-06-08 2023-03-10 济南大学 Iron tailing road base material, preparation method and application thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1931736A (en) * 2006-09-25 2007-03-21 哈尔滨工业大学 Degrading and viscosity reducing process for sewage containing oil and polymer
CN102627378A (en) * 2012-04-24 2012-08-08 湖北君集水处理有限公司 Oil field alkali-surfactant-polymer flooding oil extraction wastewater treatment method
CN102977237A (en) * 2012-12-25 2013-03-20 山东大学 Acrylamide polymer degradation method
CN103043831A (en) * 2013-01-21 2013-04-17 陕西延长石油(集团)有限责任公司研究院 Treatment method of continental shale gas well fracturing operation waste liquid
WO2014179682A1 (en) * 2013-05-03 2014-11-06 Oyj, Kemira Breakers containing iron compounds and their methods of use

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1931736A (en) * 2006-09-25 2007-03-21 哈尔滨工业大学 Degrading and viscosity reducing process for sewage containing oil and polymer
CN102627378A (en) * 2012-04-24 2012-08-08 湖北君集水处理有限公司 Oil field alkali-surfactant-polymer flooding oil extraction wastewater treatment method
CN102977237A (en) * 2012-12-25 2013-03-20 山东大学 Acrylamide polymer degradation method
CN103043831A (en) * 2013-01-21 2013-04-17 陕西延长石油(集团)有限责任公司研究院 Treatment method of continental shale gas well fracturing operation waste liquid
WO2014179682A1 (en) * 2013-05-03 2014-11-06 Oyj, Kemira Breakers containing iron compounds and their methods of use

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
聚合物在油田污水中降粘降解机理研究;王莹;《中国博士学位论文全文数据库 工程科技I辑》;20120215(第02期);第31页第1段,第32页第1段,第33页第2段,第37页末段和图4.15 *
采油污水中聚丙烯酰胺的化学降解特性研究;雒维国 等;《环境污染治理技术与设备》;20041231;第5卷(第12期);第38-42页 *

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Patentee after: China Petrochemical Co., Ltd.

Address before: 430035 Hubei city of Wuhan province Gutian two Road No. 37 HSBC Nanniwan Avenue headquarters block fifth B

Patentee before: PETROLEUM ENGINEERING TECHNOLOGY RESEARCH INSTITUTE, JIANGHAN OILFIELD BRANCH OF CHINA PETROCHEMICAL CORPORATION