CN108611084A - Complexing agent for Reservoir Acidization and preparation method thereof, application - Google Patents

Complexing agent for Reservoir Acidization and preparation method thereof, application Download PDF

Info

Publication number
CN108611084A
CN108611084A CN201611133607.2A CN201611133607A CN108611084A CN 108611084 A CN108611084 A CN 108611084A CN 201611133607 A CN201611133607 A CN 201611133607A CN 108611084 A CN108611084 A CN 108611084A
Authority
CN
China
Prior art keywords
complexing agent
acid
ethyl
complexing
reservoir
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.)
Pending
Application number
CN201611133607.2A
Other languages
Chinese (zh)
Inventor
余东合
赵立强
修书志
徐昆
罗炯
李年银
张丽娜
范秋菊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Natural Gas Co Ltd
Original Assignee
China Petroleum and Natural Gas Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by China Petroleum and Natural Gas Co Ltd filed Critical China Petroleum and Natural Gas Co Ltd
Priority to CN201611133607.2A priority Critical patent/CN108611084A/en
Publication of CN108611084A publication Critical patent/CN108611084A/en
Pending legal-status Critical Current

Links

Classifications

    • 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
    • C09K8/72Eroding chemicals, e.g. acids
    • C09K8/74Eroding chemicals, e.g. acids combined with additives added for specific purposes
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP 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
    • E21B43/25Methods for stimulating production
    • E21B43/26Methods for stimulating production by forming crevices or fractures

Abstract

The invention discloses a kind of complexing agent for Reservoir Acidization and preparation method thereof, applications, belong to technical field of petrochemical industry.It is in terms of 100% by the gross mass of the complexing agent, which includes the following components'mass percentage:Organic acid and/or acylate, 10%~30%;Gluceptate, 20%~30%;Alkyl imidazoline class compound, 10%~25%;Surfactant, 5%~10%;Water, surplus.The complexing agent retardative property is good, complexing of metal ion ability is strong, corrosion rate is low, can effectively reduce acid-rock reaction rate, realize the deep penetration of acid solution;Calcium, iron, magnesium plasma effectively in complexing reservoir inhibit the generation of precipitation;And effectively reduce corrosion of the acid solution to down-hole string;To realize the Efficient Development of reservoir, increase oil and gas production.

Description

Complexing agent for Reservoir Acidization and preparation method thereof, application
Technical field
The present invention relates to technical field of petrochemical industry, more particularly to a kind of complexing agents and its preparation side for Reservoir Acidization Method, application.
Background technology
Sandstone oil reservoir has the characteristics that low porosity and low permeability, anisotropism are strong, for such oil reservoir, generally use Acidizing Technology pair It is developed.Currently, being acidified common acid fluid system mainly has hydrochloric acid, mud acid (compounding to obtain by hydrochloric acid and hydrofluoric acid) etc., There are numerous prominent questions in the reaction process with sandstone reservoir for existing acid fluid system.For example, mud acid and sandstone reservoir Acid-rock reaction excessive velocities, and due to the excessive corrosion mineral of acid solution, Container Rock Sanding, plugging hole is caused to shout channel;While with The progress of acid-rock reaction, the pH value of acid solution constantly increases, and acid solution and clay mineral etc. easily generate aluminosilicate, metal hydroxide The precipitations such as object, fluosilicate.
Addition may be used into acid solution have slow, scale suppression effect complexing agent to slow down acid solution and rock stratum reacts fast Rate simultaneously prevents fouling.For example, application No. is US61/424,271, entitled " include suitable for handle carbonate containing stratum The patent application of the fluid of complexing agent ", application No. is the 200880124468.4, entitled " acid waters containing complexing agent The patent application of solution and application thereof " and application No. is 200910219440.5, it is entitled that " heavy metal species are complexed The complexing agent that can be used for acidification of oil field process is reported in the patent application of the preparation method of agent ".
In the implementation of the present invention, the inventors discovered that having at least the following problems in the prior art:Existing network When mixture is applied to the acidification of sandstone oil reservoir, there are retardative properties, and poor, complexing of metal ion energy force difference and corrosion rate height etc. are asked Topic.
Invention content
In order to solve the above technical problems, the embodiment of the present invention provides that a kind of retardative property is good, complexing of metal ion energy Power is strong, and the low complexing agent suitable for acidizing sandstone oil reservoir of corrosion rate realizes reservoir to realize the deep penetration of acid solution Efficient Development increases oil and gas production.
Specifically, including technical solution below:
In a first aspect, the embodiment of the present invention provides a kind of complexing agent for Reservoir Acidization, with total matter of the complexing agent Amount is 100% meter, and the complexing agent includes the following components'mass percentage:
Organic acid and/or acylate, 10%~30%;
Gluceptate, 20%~30%;
Alkyl imidazoline class compound, 10%~25%;
Surfactant, 5%~10%;
Water, surplus.
Optionally, the organic acid be selected from least one of formic acid and acetic acid, the acylate be selected from organic salt with And at least one of organic phosphate.
Optionally, the organic salt is selected from ammonium acetate, and the organic phosphate is selected from ethylenediamine tetraacetic methene sodium phosphate.
Optionally, the gluceptate in glucoheptonic acid ammonium, sodium glucoheptonate and glucoheptonic acid potassium at least It is a kind of.
Optionally, the alkyl imidazoline class compound is selected from 1- (2- aminoethyls) -2- alkyl imidazolines, 1- (2- methyl - Thiocarbamide ethyl) at least one of -2- alkyl imidazolines and 1- (2- phenyl-thioureas ethyl) -2- alkyl imidazolines.
Optionally, 1- (2- the aminoethyls) -2- alkyl imidazolines are selected from 1- (2- aminoethyls) -2- ethyl imidazol(e) quinolines;Institute It states 1- (2- methyl-thioureas ethyl) -2- alkyl imidazolines and is selected from 1- (2- methyl-thioureas ethyl) -2- pentadecyl imidazolines;Institute It states 1- (2- phenyl-thioureas ethyl) -2- alkyl imidazolines and is selected from 1- (2- phenyl-thioureas ethyl) -2- pentadecyl imidazolines.
Optionally, the surfactant is selected from perfluoroalkyl ethers lauryl alcohol amine anion surfactant and perfluor alkane At least one of base ether quaternary cationics.
Optionally, the perfluoroalkyl ethers lauryl alcohol amine anion surfactant is selected from perfluoro-ethyl ether lauryl alcohol amine.
Second aspect, the embodiment of the present invention provide a kind of preparation method of above-mentioned complexing agent, which includes: At a temperature of 50 DEG C~60 DEG C, and under stirring conditions, by organic acid and/or acylate, alkyl imidazoline class compound, Water, gluceptate and surfactant are added in container, continue stirring to system is transparent, after clarification up to the complexing Agent.
The third aspect, the embodiment of the present invention provide a kind of application of above-mentioned complexing agent in Reservoir Acidization.
Further, above application is specially:It is used after the complexing agent is mixed with hydrochloric acid, water according to preset ratio In the acid solution of Reservoir Acidization.
The advantageous effect of technical solution provided in an embodiment of the present invention:
The embodiment of the present invention is optimized by component to complexing agent and proportioning, has obtained a kind of retardative property The New Chelating Agents good, complexing of metal ion ability is strong, corrosion rate is low.For same sandstone reservoir, the present invention is added and implements The slow rate of the more conventional mud acid of acid fluid system of the complexing agent of example is up to 40% or more, to which acid-rock reaction speed be greatly lowered Rate is conducive to the deep penetration of acid solution.There is stronger complexing power to calcium, iron, magnesium ion, effectively inhibit secondary, precipitate three times Generation.Corrosion of the acid solution to down-hole string can be effectively reduced simultaneously, realizes the Efficient Development of reservoir, increases oil and gas production.
The acidification of the complexing agent provided in an embodiment of the present invention sandstone reservoir strong especially suitable for low porosity and low permeability, anisotropism Construction, additionally it is possible to be used for 150 DEG C or more of temperature reservoirs.
Specific implementation mode
To keep technical scheme of the present invention and advantage clearer, embodiment of the present invention is made below further detailed Description.Unless otherwise defined, all technical terms used in the embodiment of the present invention all have usually manages with those skilled in the art The identical meaning of solution.
In a first aspect, the embodiment of the present invention provides a kind of complexing agent for Reservoir Acidization, with the gross mass of the complexing agent For 100% meter, complexing agent includes the following components'mass percentage:
Organic acid and/or acylate, 10%~30%;
Gluceptate, 20%~30%;
Alkyl imidazoline class compound, 10%~25%;
Surfactant, 5%~10%;
Water, surplus.
It is novel that an embodiment of the present invention provides a kind of retardative properties is good, complexing of metal ion ability is strong, corrosion rate is low Complexing agent effectively reduces acid-rock reaction rate, realizes the depth of acid solution by the mutual cooperation between each component, synergistic effect It penetrates;The generation that calcium, iron, magnesium plasma effectively in complexing reservoir inhibit secondary, precipitate three times;And acid solution is effectively reduced to well The corrosion of lower tubular column;To realize the Efficient Development of reservoir, increase oil and gas production.
Specifically, in complexing agent provided in an embodiment of the present invention, organic acid, the acidity of acylate are weaker, in acid Ionization substep during karst erosion carries out, and the speed of release hydrogen ions is slower, to slow down acid-rock reaction rate.
In the embodiment of the present invention, organic acid can be at least one of low-carbons carboxylic acids such as formic acid, acetic acid, and acylate can To be selected from least one of organic salt, organic phosphate etc..Wherein, organic salt is specifically as follows ammonium acetate, organic phosphate tool Body can be ethylenediamine tetraacetic methene sodium phosphate.
In a kind of specific embodiment, using formic acid, acetic acid, ammonium acetate and organic phosphate according to mass ratio 4:2: 2:The mixture of 2 ratio compounding.
Gluceptate has multiple hydroxyls and multiple carboxyls in molecular structure, can form multiple match with metal ion Position body, plays complexing, and complexing power goes out far above common ethylenediamine tetra-acetic acid (EDTA), diethylene triamine pentacetic acid (DTPA) (DTPA), the complexing power of the aminocarboxylics acids such as Hedta (HEDTA).
It will be appreciated by persons skilled in the art that in commercially available gluceptate, gluceptate is in addition to small molecule Outside form exists, also exist with multimeric forms, poly gluceptate has better complexing power.
Gluceptate can be selected from the soluble gluceptate such as glucoheptonic acid ammonium, sodium glucoheptonate, glucoheptonic acid potassium At least one of, in a kind of specific embodiment, gluceptate is glucoheptonic acid ammonium, sodium glucoheptonate and glucoheptose Sour potassium is according to mass ratio 4:3:The mixture of 3 ratio compounding.
Alkyl imidazoline class compound can be adsorbed on metal surface, and certain oxidizing substances in acid solution are complexed, To realize preferable rust inhibition, and then reduce extent of corrosion of the acid solution to down-hole string.
Alkyl imidazoline class compound can be selected from 1- (2- aminoethyls) -2- alkyl imidazolines, 1- (2- methyl-thiourea second Base) at least one of -2- alkyl imidazolines and 1- (2- phenyl-thioureas ethyl) -2- alkyl imidazolines.Wherein, 1- (2- ammonia Ethyl) -2- alkyl imidazolines are specifically as follows 1- (2- aminoethyls) -2- ethyl imidazol(e) quinolines, 1- (2- methyl-thioureas ethyl) -2- Alkyl imidazoline is specifically as follows 1- (2- methyl-thioureas ethyl) -2- pentadecyl imidazolines, 1- (2- phenyl-thioureas ethyl) - 2- alkyl imidazolines are specifically as follows 1- (2- phenyl-thioureas ethyl) -2- pentadecyl imidazolines.
Surfactant can reduce the interfacial tension of grease, increase the wet degree of water of rock, while can also realize residual acid The preferably row of returning.
In the embodiment of the present invention, surfactant can be selected from perfluoroalkyl ethers lauryl alcohol amine anion surfactant with And at least one of perfluoroalkyl ethers quaternary cationics.Wherein, perfluoroalkyl ethers lauryl alcohol amine anion It is multiple that surfactant is specifically as follows perfluoro-methyl ether lauryl alcohol amine, perfluoro-ethyl ether lauryl alcohol amine or a variety of perfluoroalkyl ethers The mixture matched.
In complexing agent provided in an embodiment of the present invention, dosage arbitrary value, act in the range of restriction of each component For example, the mass percent of organic acid and/or acylate can be 10%, 12%, 14%, 15%, 16%, 18%, 20%, 22%, 24%, 25%, 26%, 28%, 30% etc.;The mass percent of gluceptate can be 20%, 22%, 24%, 25%, 26%, 28%, 30% etc.;The mass percent of alkyl imidazoline class compound can be 10%, 12%, 14%, 15%, 16%, 18%, 20%, 22%, 24%, 25% etc.;The mass percent of surfactant can be 5%, 6%, 7%, 8%, 9%, 10% etc..
Second aspect, the embodiment of the present invention provide a kind of preparation method of above-mentioned complexing agent, which includes: At a temperature of 50 DEG C~60 DEG C, and under stirring conditions, by organic acid and/or acylate, alkyl imidazoline class compound, Water, gluceptate and surfactant are added in container, continue stirring to system is transparent, after clarification up to complexing agent.
It should be noted that in above-mentioned preparation method, the charging sequence of water and gluceptate in no particular order, and has Machine acid and/or acylate, alkyl imidazoline class compound should sequentially add before water and gluceptate, surfactant It is eventually adding.And surfactant should be slowly added to, it is made to come into full contact with and be uniformly mixed with solution under the action of stirring.
When system is transparent, clarification, after no precipitation, can continue to stand a period of time, such as used again after 1 hour.
The third aspect, the embodiment of the present invention provide a kind of application of above-mentioned complexing agent in Reservoir Acidization.By above-mentioned network Mixture injects reservoir after being mixed with acid solution (such as hydrochloric acid, mud acid etc.) with acidizing treatment.
In a kind of specific embodiment, by above-mentioned complexing agent, hydrochloric acid and water according to mass ratio 1:1:8 ratio is mixed It closes, injects reservoir.
The technical solution of the embodiment of the present invention is described in further detail below by specific data.
Experimental method used in following embodiment is conventional method unless otherwise specified.
Material used in following embodiment, reagent etc., be not specified production firm and specification person be can be by purchased in market The conventional products of acquisition.
In following embodiment, the group of each component becomes in complexing agent:
A:The combination (hereinafter referred to as organic acid) of organic acid and acylate is:40% formic acid, 20% acetic acid, 20% acetic acid Ammonium, 20% ethylenediamine tetraacetic methene sodium phosphate, the above percentage are mass percent, are to be incited somebody to action in terms of 100% by the gross mass of organic acid Formic acid, acetic acid, ammonium acetate and ethylenediamine tetraacetic methene sodium phosphate are mixed with other components as a whole after mixing.
B:Gluceptate:40% glucoheptonic acid ammonium, 30% sodium glucoheptonate, 30% glucoheptonic acid potassium, the above percentage It is in terms of 100%, by glucoheptonic acid ammonium, sodium glucoheptonate and glucoheptose by the gross mass of gluceptate for mass percent Sour potassium is mixed with other components as a whole after mixing.
C:Alkyl imidazoline class compound:1- (2- aminoethyls) -2- ethyl imidazol(e) quinolines.
D:Surfactant:Perfluoro-ethyl ether lauryl alcohol amine.
Unless otherwise instructed, the mass percent of the hydrochloric acid described in following embodiment is pure hydrochloric acid, i.e. hydrogen chloride Mass percent.
Embodiment 1
The present embodiment provides three kinds for Reservoir Acidization complexing agents and corresponding preparation method, and to its retardative property into Row test.
The formula of the complexing agent of the present embodiment is as shown in table 1.
The formula for the complexing agent that 1 embodiment 1 of table provides
Each percentage is mass percent in table 1, and by the gross mass of complexing agent I in terms of 100%.
The preparation method of the complexing agent of the present embodiment is as follows:
At a temperature of 50 DEG C, and under stirring conditions, according to the proportioning of each component in table 1, successively by organic acid, alkane Base imidazolines, water, gluceptate and surfactant are added in container, continue stirring to system it is transparent, Clarification, and up to complexing agent after standing 1 hour.
By hydrochloric acid, the complexing agent of the present embodiment and water example 10 in mass ratio:10:80 ratio is compounded to obtain complex acid System, using the core of two blocks of the AE of H Oil Fields and XL as sample, (total rock of the core sample of AE and XL blocks analyzes knot Fruit is as shown in table 2), the sour karst erosion experiment of 2h is carried out under 90 DEG C of water bath conditions.Complex acid under different organic acids component Slow rate test result such as table 3.
The total rock of the core sample of 2 AE and XL blocks of table is analyzed
Corrosion situation of the complexing acid system of 3 different organic acids content of table to sandstone mineral
In table 3, for slow rate on the basis of the corrosion rate of regular mud acid, i.e. the corrosion inhibition rate of regular mud acid is 0.
As can be seen from Table 3, the complexing acid system under different organic acids content is big to the slow rate of the above block In 40%, there is stronger slow property;Acid system is complexed to the corrosion rate of block between 20%~32%, there is certain corrosion Ability (the corrosion rate of regular mud acid is 35% or so).
Embodiment 2
The present embodiment provides three kinds of complexing agents for Reservoir Acidization and corresponding preparation methods, and to it to metal ion Complex performance tested.
The formula of the complexing agent of the present embodiment is as shown in table 4.
The formula for the complexing agent that 4 embodiment 2 of table provides
Each percentage is mass percent in table 4, and by the gross mass of complexing agent I in terms of 100%.
The preparation method of the complexing agent of the present embodiment is as follows:
At a temperature of 55 DEG C, and under stirring conditions, according to the proportioning of each component in table 4, successively by organic acid, alkane Base imidazolines, water, gluceptate and surfactant are added in container, continue stirring to system it is transparent, Clarification, and up to complexing agent after standing 1 hour.
Measure the metal of blank group (not plus complexing agent) and experimental group (complexing agent is added) respectively using indicator titration method The complexing power of the New Chelating Agents to calcium ion, iron ion and magnesium ion of the present embodiment is obtained by calculation in ion complexation value. Influence of the different glucoheptonic acid salt contents to complexing of metal ion ability, is shown in Table 5.
Influence of the complexing agent of the different glucoheptonic acid salt contents of table 5 to complexing of metal ion ability
As can be seen from Table 5, poly- glucoheptonic acid salt content is preferably 25%~30%, complexing provided in this embodiment Agent is 272mg/g, 167mg/g, 455mg/g respectively to the highest complexing value of calcium, magnesium, iron three classes ion.
Embodiment 3
The present embodiment provides four kinds for Reservoir Acidization complexing agents and corresponding preparation method, and to its corrosive nature into Row measures.
The formula of the complexing agent of the present embodiment is as shown in table 6.
The formula for the complexing agent that 6 embodiment 3 of table provides
The preparation method of the complexing agent of the present embodiment is as follows:
At a temperature of 60 DEG C, and under stirring conditions, according to the proportioning of each component in table 6, successively by organic acid, alkane Base imidazolines, water, gluceptate and surfactant are added in container, continue stirring to system it is transparent, Clarification, and up to complexing agent after standing 1 hour.
By hydrochloric acid, the complexing agent of the present embodiment and water example 10 in mass ratio:10:80 ratio is compounded to obtain complex acid System carries out static corrosion test at 90 DEG C, and N80 steel discs are put into above-mentioned complexing acid system and impregnate 4h.Different alkyl miaows Influence of the oxazoline compound content to steel disc rate of corrosion is shown in Table 7.
Influence of the complexing acid system of the different alkyl imidazoline kind compound contents of table 7 to corrosion rate
As can be seen from Table 7, the complexing acid system of different alkyl imidazoline kind compound contents, is being not added with other 100g/m is respectively less than to the corrosion rate of steel disc in the case of corrosion inhibiter2·h.With the increase of alkyl imidazoline content, complexing Acid is gradually reduced the corrosion rate of steel disc, and the content of alkyl imidazoline class compound is preferably 20%~25%.
The conventional acid fluid system for being not added with corrosion inhibiter is measured the corrosion rate of N80 steel discs simultaneously, test condition: 90 DEG C, corrode 4h.It the results are shown in Table 8.
The acid fluid system that table 8 is not added with corrosion inhibiter measures the corrosion rate of steel disc
In table 8, the formula of mud acid:10%HCl+2%HF+87% water;
Concentration of hydrochloric acid is 10%;
MH acid:10%HCl+3%SA601+4%SA701+83% water.
As can be seen from Table 8, the corrosion rate of the acid fluid system of the complexing agent of the present embodiment is added to far below normal Acid solution such as hydrochloric acid, mud acid, MH acid are advised to the corrosion rate of steel disc.
The above is merely for convenience of it will be understood by those skilled in the art that technical scheme of the present invention, not limiting The present invention.All within the spirits and principles of the present invention, any modification, equivalent replacement, improvement and so on should be included in this Within the protection domain of invention.

Claims (10)

1. a kind of complexing agent for Reservoir Acidization, which is characterized in that by the gross mass of the complexing agent be 100% in terms of, it is described Complexing agent includes the following components'mass percentage:
Organic acid and/or acylate, 10%~30%;
Gluceptate, 20%~30%;
Alkyl imidazoline class compound, 10%~25%;
Surfactant, 5%~10%;
Water, surplus.
2. complexing agent according to claim 1, which is characterized in that the organic acid in formic acid and acetic acid at least one Kind, the acylate is selected from least one of organic salt and organic phosphate.
3. complexing agent according to claim 1, which is characterized in that the gluceptate is selected from glucoheptonic acid ammonium, Portugal heptan At least one of sodium saccharate and glucoheptonic acid potassium.
4. complexing agent according to claim 1, which is characterized in that the alkyl imidazoline class compound is selected from 1- (2- ammonia Ethyl) -2- alkyl imidazolines, 1- (2- methyl-thioureas ethyl) -2- alkyl imidazolines and 1- (2- phenyl-thioureas ethyl) -2- At least one of alkyl imidazoline.
5. complexing agent according to claim 4, which is characterized in that 1- (2- the aminoethyls) -2- alkyl imidazolines are selected from 1- (2- aminoethyls) -2- ethyl imidazol(e) quinolines;
1- (2- methyl-thioureas the ethyl) -2- alkyl imidazolines are selected from 1- (2- methyl-thioureas ethyl) -2- pentadecyl miaows Oxazoline;
1- (2- phenyl-thioureas the ethyl) -2- alkyl imidazolines are selected from 1- (2- phenyl-thioureas ethyl) -2- pentadecyl miaows Oxazoline.
6. complexing agent according to claim 1, which is characterized in that the surfactant is selected from perfluoroalkyl ethers lauryl alcohol At least one of amine anion surfactant and perfluoroalkyl ethers quaternary cationics.
7. complexing agent according to claim 6, which is characterized in that the perfluoroalkyl ethers lauryl alcohol amine anionic surface is lived Property agent be selected from perfluoro-ethyl ether lauryl alcohol amine.
8. a kind of preparation method of claim 1~7 any one of them complexing agent, which is characterized in that including:50 DEG C~60 At a temperature of DEG C, and under stirring conditions, by organic acid and/or acylate, alkyl imidazoline class compound, water, Portugal heptan Sugar lime and surfactant are added in container, continue stirring to system is transparent, after clarification up to the complexing agent.
9. a kind of application of claim 1~7 any one of them complexing agent in Reservoir Acidization.
10. application according to claim 9, which is characterized in that mix the complexing agent and hydrochloric acid, water according to preset ratio The acid solution for Reservoir Acidization is obtained after conjunction.
CN201611133607.2A 2016-12-10 2016-12-10 Complexing agent for Reservoir Acidization and preparation method thereof, application Pending CN108611084A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611133607.2A CN108611084A (en) 2016-12-10 2016-12-10 Complexing agent for Reservoir Acidization and preparation method thereof, application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611133607.2A CN108611084A (en) 2016-12-10 2016-12-10 Complexing agent for Reservoir Acidization and preparation method thereof, application

Publications (1)

Publication Number Publication Date
CN108611084A true CN108611084A (en) 2018-10-02

Family

ID=63643559

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611133607.2A Pending CN108611084A (en) 2016-12-10 2016-12-10 Complexing agent for Reservoir Acidization and preparation method thereof, application

Country Status (1)

Country Link
CN (1) CN108611084A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116410725A (en) * 2021-12-29 2023-07-11 中国石油天然气股份有限公司 Corrosion inhibition type foam discharging agent for gas field, preparation method and application

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103074050A (en) * 2011-10-26 2013-05-01 中国石油化工股份有限公司 Anti-scaling multi-hydrogen retarded acid for highly argillaceous sandstone reservoir
US20150292308A1 (en) * 2014-04-14 2015-10-15 Flex-Chem Holding Company, Llc Stimulation of wells in nano-darcy shale formations
CN105086989A (en) * 2014-05-19 2015-11-25 中国石油化工股份有限公司 Shale gas reservoir pre-fracture composite acid solution, preparation method and application thereof
CN105482801A (en) * 2015-11-25 2016-04-13 中国海洋石油总公司 Oil and water well polyacid blocking remover

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103074050A (en) * 2011-10-26 2013-05-01 中国石油化工股份有限公司 Anti-scaling multi-hydrogen retarded acid for highly argillaceous sandstone reservoir
US20150292308A1 (en) * 2014-04-14 2015-10-15 Flex-Chem Holding Company, Llc Stimulation of wells in nano-darcy shale formations
CN105086989A (en) * 2014-05-19 2015-11-25 中国石油化工股份有限公司 Shale gas reservoir pre-fracture composite acid solution, preparation method and application thereof
CN105482801A (en) * 2015-11-25 2016-04-13 中国海洋石油总公司 Oil and water well polyacid blocking remover

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
从鑫等: "螯合剂的生产工艺研究进展", 《山东化工》 *
赵福麟主编: "《油田化学》", 30 September 2010, 中国石油大学出版社 *
邢红忠等: "改性咪唑啉缓蚀剂抗H2S/CO2腐蚀性能研究", 《腐蚀研究》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116410725A (en) * 2021-12-29 2023-07-11 中国石油天然气股份有限公司 Corrosion inhibition type foam discharging agent for gas field, preparation method and application

Similar Documents

Publication Publication Date Title
DK2737002T3 (en) BELL SERVICE FLUID AND METHOD OF SERVICING A BELL WITH THE FLUID
US10035949B2 (en) Fluoro-inorganics for well cleaning and rejuvenation
CN107973422B (en) Composite corrosion and scale inhibitor, corrosion and scale inhibition method for oil field water and oil extraction method
CN107418549A (en) A kind of compound acidification corrosion inhibitor of 120 ~ 140 DEG C of heatproof
CN107892910A (en) Inexpensive multifunctional acid liquid system
CN108467718B (en) Preparation of clay anti-swelling agent with anti-corrosion effect for water injection
Al-Harbi et al. Evaluation of organic hydrofluoric acid mixtures for sandstone acidising
CA2849248C (en) Method of fracturing with phenothiazine stabilizer
CN104109530A (en) Iron ion stabilizing agent used for acidifying and preparation method
Shafiq et al. An effective acid combination for enhanced properties and corrosion control of acidizing sandstone formation
CN105295886A (en) Composite retarded acid
CN108219763A (en) A kind of acidizing sandstone oil reservoir slow type MH acid system and its construction technology
CN107973418B (en) Composite corrosion and scale inhibitor, corrosion and scale inhibition method for oil field water and oil extraction method
EP2951267A1 (en) Process for treating subterranean oil-bearing formations comprising carbonate rocks
Shafiq et al. Comparison of buffer effect of different acids during sandstone acidizing
CN108611084A (en) Complexing agent for Reservoir Acidization and preparation method thereof, application
CN114058350B (en) Chlorite blocking remover, preparation method, application and blocking removing method thereof
CN103937480A (en) Organic alkali/surfactant binary composite oil displacement system as well as preparation method and application thereof
CN101570687B (en) Oilfield injection friction-reducing agent and application thereof
CN107973423B (en) Composite corrosion and scale inhibitor, corrosion and scale inhibition method for oil field water and oil extraction method
CN106350047B (en) A kind of oil gas field corrosion inhibiter and preparation method thereof
CN104877650A (en) Complex water-based deep-water disposal fluid
CN109837546B (en) Ammonium persulfate corrosion inhibitor used in production oil pipeline of offshore oil field and application thereof
CN112358861A (en) Corrosion inhibition bactericide for shale gas field
CN102604626A (en) Acid fracturing fluid for high sulfur content gas reservoir

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20181002