CN108359417A - A kind of preparation method of drilling well anti-sloughing agent - Google Patents

A kind of preparation method of drilling well anti-sloughing agent Download PDF

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CN108359417A
CN108359417A CN201810361215.4A CN201810361215A CN108359417A CN 108359417 A CN108359417 A CN 108359417A CN 201810361215 A CN201810361215 A CN 201810361215A CN 108359417 A CN108359417 A CN 108359417A
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gel
mixing
pectin
mixture
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刘凡领
万振
吴庆梅
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    • 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
    • C09K8/02Well-drilling compositions
    • C09K8/03Specific additives for general use in well-drilling compositions

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Abstract

The invention discloses a kind of preparation methods of drilling well anti-sloughing agent, belong to technical field of polymer materials.It counts, weighs successively in parts by weight, 35~45 portions of modified starches, 50~60 property-modifying additives, 40~80 parts of paraffin, 10~15 parts of isocyanates, paraffin is added in reactor 22~25 parts of ethyl orthosilicates, heating and melting under conditions of being 45~60 DEG C in temperature, and modified starch is sequentially added into reactor, and isocyanates, ethyl orthosilicate and additive, in temperature be 45~55 DEG C, after rotating speed is stirred 15~35min under conditions of being 260~360r/min, Freezing smashing obtains drilling well anti-sloughing agent.

Description

A kind of preparation method of drilling well anti-sloughing agent
Technical field
The invention discloses a kind of preparation methods of drilling well anti-sloughing agent, belong to technical field of polymer materials.
Background technology
There are many type of anti-sloughing agent, and inorganic, high molecular polymerization species, alcohol can be divided by mainly carrying out classification by its performance Class, organic silicon, lignite class, resinae, oils, vinegar class and synthesis base class etc..Drilling fluid influences the impact force size of the borehole wall To the stability of simultaneously wall, turbulent flow is big to the impact force of the borehole wall, and plug flow or tablet flow pattern are small to the impact force of the borehole wall, these show In the flow pattern of drilling fluid, i.e., on the ratio of dynamic shear force/yield value to plastic viscosity of drilling fluid.Therefore, all inorganic agents that can improve drilling fluid ratio of dynamic shear force/yield value to plastic viscosity should also be known as anti- It collapses agent, this kind of anti-sloughing agent refers mainly to positive colloid, modified asbestos and some high molecular polymers.Since anti-sloughing agent type is various, perhaps More anti-sloughing agents have a variety of mechanism of anti caving.For example, positive colloid has to the compression of electric double layer and changes to drilling fluid flow pattern Into the mechanism of action of both effect, with three aspect of tessellation, high molecular polymer encapsulation action and low leak-off effect Mechanism.Therefore, different evaluation methods, the reduction of drilling fluid filtration is applied to make the anti-sloughing agent with different mechanism of anti caving Hydrone is not easily accessible rock core, to reduce the unstable effect of clay caused by aquation dispersion, most of drops Fluid loss agents are also referred to as anti-sloughing agent.Anti-sloughing agent enters rock core microcrack, is filled in the hole of rock core microcrack, and in microcrack It is adsorbed, hydrone is made to be not easily accessible rock core, it is therefore prevented that withered soil expansion because of caused by hydration, it is anti-to play The effect of collapsing.Gel breaker will be discharged in partial points, and gel breaker size has to be larger than the void size of proppant filling tape.Experiments have shown that Gel breaker size should be in the same size with proppant or best slightly larger than proppant effect.In two kinds of releasing mechanisms, it is believed that infiltration is released It is reliable to put mechanism, and gel breaking time is easily controllable, squeezes releasing mechanism and can not achieve sometimes, because at wellbore or low Pressure is since the flexibility of peel cannot be such that capsule breaker is crushed in formation closure, but the capsule breaker of this mechanism It can be used for high pressure formation.It generally believes under low pressure now mainly based on infiltration release;Under high pressure based on extruding release, simultaneously There is also infiltration releases, but the apparent aggravation of infiltration release under high temperature, based on infiltration release.But traditional drilling well anti-sloughing agent is also Have the shortcomings that permeability resistance is poor, caving-preventing characteristic is insufficient.
Therefore, how to improve that permeability resistance existing for traditional drilling well anti-sloughing agent is poor, disadvantage of caving-preventing characteristic deficiency, to obtain The raising of more high combination property is that it is promoted and applies, meets industrial production demand urgent problem to be solved.
Invention content
The present invention solves the technical problem of:Poor, the anti-collapse property for permeability resistance existing for traditional drilling well anti-sloughing agent The insufficient disadvantage of energy, provides a kind of preparation method of drilling well anti-sloughing agent.
In order to solve the above-mentioned technical problem, the technical solution adopted in the present invention is:
(1)By cationic starch and water in mass ratio 1:4~1:6 mixing, and 0.6~0.8 times of cationic starch quality is added The initiator of 0.1~0.3 times of acrylamide and starch quality after being stirred, filters, dry, obtains modified starch;
(2)It will(N- amidino groups)Dodecylacrylamide and polyethyleneglycol derivative in mass ratio 2:1~1:1 mixing, and be added Two cyclopentadienyls of 0.08~0.12 times of the paracide and polyethyleneglycol derivative quality that 0.1~0.2 times of polyethyleneglycol derivative quality Iron is stirred, and obtains inorganic agent;
(3)It counts, weighs successively in parts by weight:80~100 parts of polyvinyl alcohol, 40~60 parts of gelatin, 250~350 parts of water, 30~ 40 parts of glutaraldehyde water solutions and 10~25 parts of hydrochloric acid, polyvinyl alcohol is mixed with water, and heating stirring obtains poly-vinyl alcohol solution, will Poly-vinyl alcohol solution cools down, and the poly-vinyl alcohol solution after cooling is mixed with gelatin, and sequentially adds hydrochloric acid and glutaraldehyde water Solution, after being stirred, filtering, stripping and slicing is washed, and vacuum drying obtains gel;
(4)By gel and water in mass ratio 1:5~1:8 mixing, and pH to 2.0~2.6 is adjusted, it is stirred, obtains gel mixing Object, by gel mixture and pretreatment montmorillonite in mass ratio 3:1~5:1 mixing, and be added gel mixture quality 0.1~ 0.2 times of inorganic agent after being stirred, obtains modified gel mixture, adjusts the pH to 5.6~6.6 of modified gel mixture, mistake Filter, it is dry, obtain modified gel;
(5)By pectin and sodium hydroxide solution in mass ratio 1:3~1:4 mixing, and the water of 20~40 times of pectin quality is added, it stirs After mixing mixing, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:3~15:7 mixing, and adjust pH to 6.0~ 6.5, the sodium bicarbonate of 0.1~0.3 times of the modified gel and pectin solution quality of 0.4~0.5 times of pectin solution quality is added, stirs After mixing mixing, sonic oscillation obtains pectin mixture, and pectin mixture is instilled calcium chloride solution with the rate of 1~3mL/min In, after being crosslinked 15~30min, filtering obtains property-modifying additive;
(6)It counts, weighs successively in parts by weight, 35~45 portions of modified starches, 50~60 property-modifying additives, 40~80 parts of paraffin, 10~15 parts of isocyanates, 22~25 parts of ethyl orthosilicates, heating paraffin are melted, and modified starch is added, isocyanates, just Silester and additive, after being stirred, Freezing smashing crosses 320~500 mesh sieve, obtains drilling well anti-sloughing agent.
Step(1)The initiator is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate.
Step(2)The polyethyleneglycol derivative is in polyethylene glycol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate Any one.
Step(4)The preparation method of the pretreatment montmorillonite is by montmorillonite and paraffin in mass ratio 1:3~1:4 is mixed It closes, and polyacrylic acid zinc is added, after being stirred, Freezing smashing obtains pretreatment montmorillonite.
Step(6)The paraffin is the mineral wax mixture that carbon atom number is 24~36.
Step(6)The isocyanates is isofoer diisocyanate, toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride Any one in diisocyanate.
The beneficial effects of the invention are as follows:
(1)Modified gel is added when preparing drilling well anti-sloughing agent in the present invention, and first, modified gel can be with the change of external environment pH And expand or shrink, after being added in product, gel can expand under the stimulation of alkaline environment, to make on the borehole wall Soil be squeezed and bond, and water is made to cannot be introduced into inside the borehole wall, to make the caving-preventing characteristic of product improve, secondly, Inorganic agent and montmorillonite containing imitated vesicle structure inside modified gel, in expanded gel during product use with gel The imitated vesicle structure and montmorillonite in portion expose, and montmorillonite can expand after meeting water, enter the borehole wall to reduce moisture penetration, into And the caving-preventing characteristic of product is made to further increase, and imitated vesicle structure can form certain vapour lock inside gel, to make production The anti-permeability performance of product improves, and then the anti-collapse property of product is made to improve;
(2)Isocyanates and ethyl orthosilicate are added when preparing drilling well anti-sloughing agent by the present invention, on the one hand, the isocyanates of addition Paraffin melting on the outside it can contact and hydrolyze with water afterwards, to generate amine substance and carbon dioxide, carbon dioxide can promote to change The expansion of imitated vesicle structure in property gel, and then the caving-preventing characteristic of product is made to further increase, and during amine substance is water-soluble, make Water is conducive to the hydrolysis of ethyl orthosilicate in alkalinity, and on the other hand, the ethyl orthosilicate of addition can form silica, and by There is certain flocculability in the modified starch of addition, the silica of formation can be combined with tiny mud particles, to well Gap and hole on wall are filled, to make the caving-preventing characteristic of product further increase.
Specific implementation mode
By cationic starch and water in mass ratio 1:4~1:6 are mixed in beaker, and starch quality is added into beaker The initiator of 0.6~0.8 times of 0.1~0.3 times of acrylamide and starch quality, in temperature be 55~85 DEG C, rotating speed be 220~ After being stirred 50~80min under conditions of 300r/min, filter, it is dry, obtain modified starch;It will(N- amidino groups)Dodecyl third Acrylamide and polyethyleneglycol derivative in mass ratio 2:1~1:1 is mixed in flask, and polyethylene glycol is added into flask and derives The ferrocene of 0.08~0.12 times of the paracide and polyethyleneglycol derivative quality that 0.1~0.2 times of amount of substance, in temperature be 55 ~75 DEG C, after rotating speed is stirred 1~2h under conditions of being 200~350r/min, inorganic agent is obtained, is counted in parts by weight, successively It weighs:80~100 parts of polyvinyl alcohol, 40~60 parts of gelatin, 250~350 parts of water, 30~40 parts of mass fractions are 25~28% The hydrochloric acid that glutaraldehyde water solution and 10~25 parts of mass fractions are 15~25%, polyvinyl alcohol is mixed with water, in temperature for 88~ 98 DEG C, under conditions of rotating speed is 250~300r/min after 55~80min of stirring, poly-vinyl alcohol solution is obtained, by poly-vinyl alcohol solution 50~60 DEG C are cooled to, and the poly-vinyl alcohol solution after cooling is mixed with gelatin, and successively to poly-vinyl alcohol solution and gelatin Mixture in hydrochloric acid and glutaraldehyde water solution is added, in temperature be 35~48 DEG C, under conditions of rotating speed is 250~300r/min After being stirred 10~12h, filtering obtains pretreatment gel, will pre-process gel stripping and slicing, deionized water washing by soaking 5~6 is used in combination It, while a deionized water is changed every 10~12h, by the gel piece after washing after being dried in vacuo 3~5h under room temperature, Obtain gel;By gel and water in mass ratio 1:5~1:8 mixing are used in combination the hydrochloric acid that mass fraction is 20~30% to adjust gel and water The pH to 2.0~2.6 of mixture is 30~40 DEG C in temperature, rotating speed is stirred 15 under conditions of being 200~230r/min~ After 25min, gel mixture is obtained, by gel mixture and pretreatment montmorillonite in mass ratio 3:1~5:1 mixing, and to gel Mixture and the inorganic agent that 0.1~0.2 times of gel mixture quality is added in the mixture of pretreatment montmorillonite, in temperature be 22 ~28 DEG C, after rotating speed is stirred 30~70min under conditions of being 200~300r/min, modified gel mixture is obtained, quality is used After the sodium hydroxide solution that score is 10~12% adjusts the pH to 5.6~6.6 of modified gel mixture, filtering obtains filter cake, will Under conditions of filter cake is 60~80 DEG C in temperature after dry 1~2h, modified gel is obtained;It is 12~18% by pectin and mass fraction Sodium hydroxide solution in mass ratio 1:3~1:4 mixing, and be added into the mixture of pectin and sodium hydroxide pectin quality 20~ 40 times of water is 30~45 DEG C in temperature, after rotating speed is stirred 30~60min under conditions of being 200~300r/min, obtains fruit Sol solution, by pectin solution and lecithin in mass ratio 15:3~15:7 mixing, and adjust pectin solution and lecithin mixture PH to 6.0~6.5, then the modification of 0.4~0.5 times of pectin solution quality is added into the mixture of pectin solution and lecithin 0.1~0.3 sodium bicarbonate of gel and pectin solution quality is 30~35 DEG C in temperature, and rotating speed is the condition of 200~250r/min Under be stirred 15~25min after, obtain pretreatment pectin mixture, will pre-process pectin mixture in frequency be 45~55kW Under the conditions of after 5~10min of sonic oscillation, obtain pectin mixture, pectin mixture instilled into quality with the rate of 1~3mL/min In the calcium chloride solution that score is 20~30%, after being crosslinked 20~30min under room temperature, filtering obtains filter cake to get modification Additive;It counts, weighs successively in parts by weight, 35~45 portions of modified starches, 50~60 property-modifying additives, 40~80 parts of paraffin, Paraffin is added in reactor for 10~15 parts of isocyanates, 22~25 parts of ethyl orthosilicates, the condition for being 45~60 DEG C in temperature Lower heating and melting, and modified starch is sequentially added into reactor, isocyanates, ethyl orthosilicate and additive are in temperature 45~55 DEG C, after rotating speed is stirred 15~35min under conditions of being 260~360r/min, it is anti-collapse to obtain drilling well for Freezing smashing Agent.The initiator is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate.The polyethyleneglycol derivative is poly- second Any one in glycol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate.The preparation method of the pretreatment montmorillonite is will Montmorillonite and paraffin in mass ratio 1:3~1:4 mixing, and polyacrylic acid zinc is added, after being stirred, Freezing smashing, excessively 320~ 500 mesh sieve, and obtain pretreatment montmorillonite.The paraffin is the mineral wax mixture that carbon atom number is 24~36.The isocyanates is Any one in isofoer diisocyanate, toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride diisocyanate.
Example 1
By cationic starch and water in mass ratio 1:6 are mixed in beaker, and the propylene of 0.8 times of starch quality is added into beaker The initiator of 0.3 times of amide and starch quality is 85 DEG C in temperature, and rotating speed is stirred 80min under conditions of being 300r/min Afterwards, it filters, it is dry, obtain modified starch;It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed Together in flask, and the paracide and polyethyleneglycol derivative matter of 0.2 times of polyethyleneglycol derivative quality is added into flask The ferrocene of 0.12 times of amount after rotating speed is stirred 2h under conditions of being 350r/min, obtains inorganic agent, by weight in 75 DEG C of temperature Number meter is measured, is weighed successively:100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water that 40 parts of mass fractions are 28% The hydrochloric acid that solution and 25 parts of mass fractions are 25%, polyvinyl alcohol is mixed with water, in temperature be 98 DEG C, rotating speed 300r/min Under conditions of after stirring 80min, obtain poly-vinyl alcohol solution, poly-vinyl alcohol solution be cooled to 60 DEG C, and by the poly- second after cooling Enolate solution is mixed with gelatin, and into the mixture of poly-vinyl alcohol solution and gelatin, addition hydrochloric acid and glutaraldehyde are water-soluble successively Liquid is 48 DEG C in temperature, and after rotating speed is stirred 12h under conditions of being 300r/min, filtering obtains pretreatment gel, will locate in advance Gel stripping and slicing is managed, deionized water washing by soaking is used in combination 6 days, while a deionized water is changed every 12h, by the gel piece after washing After being dried in vacuo 5h under room temperature, gel is obtained;By gel and water in mass ratio 1:8 mixing, it is 30% that mass fraction, which is used in combination, Hydrochloric acid adjusts the pH to 2.6 of gel and aqueous mixtures, is 40 DEG C in temperature, rotating speed is stirred under conditions of being 230r/min After 25min, gel mixture is obtained, by gel mixture and pretreatment montmorillonite in mass ratio 5:1 mixing, and to gel mixture It it is 28 DEG C in temperature, rotating speed is with the inorganic agent that 0.2 times of gel mixture quality is added in the mixture of pretreatment montmorillonite After being stirred 70min under conditions of 300r/min, modified gel mixture is obtained, the sodium hydroxide for being 12% with mass fraction is molten After liquid adjusts the pH to 6.6 of modified gel mixture, filtering obtains filter cake, dry 2h under conditions of being 80 DEG C in temperature by filter cake Afterwards, modified gel is obtained;It is 18% sodium hydroxide solution in mass ratio 1 by pectin and mass fraction:4 mixing, and to pectin and hydrogen-oxygen Change the water that 40 times of pectin quality is added in the mixture of sodium, is 45 DEG C in temperature, rotating speed stirs mixed under conditions of being 300r/min After closing 60min, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:7 mixing, and adjust pectin solution and lecithin The 6.5 of lipoprotein mixture, then be added into the mixture of pectin solution and lecithin 0.5 times of pectin solution quality modified gel and 0.3 sodium bicarbonate of pectin solution quality is 35 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 250r/min, obtains Pectin mixture is pre-processed, pretreatment pectin mixture after sonic oscillation 10min, is obtained into pectin under conditions of frequency is 55kW Mixture is instilled pectin mixture in the calcium chloride solution that mass fraction is 30% with the rate of 3mL/min, in room temperature condition After lower crosslinking 30min, filtering obtains filter cake to get property-modifying additive;It counts, weighs successively in parts by weight, 45 portions of modified starches, Paraffin is added in reactor, is in temperature by 60 property-modifying additives, 80 parts of paraffin, 15 parts of isocyanates, 25 parts of ethyl orthosilicates Heating and melting under conditions of 60 DEG C, and modified starch is sequentially added into reactor, isocyanates, ethyl orthosilicate and addition Agent is 55 DEG C in temperature, and after rotating speed is stirred 35min under conditions of being 360r/min, Freezing smashing obtains drilling well anti-sloughing agent. The initiator is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate.The polyethyleneglycol derivative is poly- second two Any one in alcohol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate.The preparation method of the pretreatment montmorillonite is that will cover De- stone and paraffin in mass ratio 1:4 mixing, and polyacrylic acid zinc is added, after being stirred, Freezing smashing is crossed 500 mesh sieve, is obtained pre- Handle montmorillonite.The paraffin is the mineral wax mixture that carbon atom number is 36.The isocyanates is different Fu Er ketone diisocyanate Any one in ester, toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride diisocyanate.
Example 2
By cationic starch and water in mass ratio 1:6 are mixed in beaker, and the propylene of 0.8 times of starch quality is added into beaker The initiator of 0.3 times of amide and starch quality is 85 DEG C in temperature, and rotating speed is stirred 80min under conditions of being 300r/min Afterwards, it filters, it is dry, obtain modified starch;It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed Together in flask, and the paracide and polyethyleneglycol derivative matter of 0.2 times of polyethyleneglycol derivative quality is added into flask The ferrocene of 0.12 times of amount after rotating speed is stirred 2h under conditions of being 350r/min, obtains inorganic agent, by weight in 75 DEG C of temperature Number meter is measured, is weighed successively:100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water that 40 parts of mass fractions are 28% The hydrochloric acid that solution and 25 parts of mass fractions are 25%, polyvinyl alcohol is mixed with water, in temperature be 98 DEG C, rotating speed 300r/min Under conditions of after stirring 80min, obtain poly-vinyl alcohol solution, poly-vinyl alcohol solution be cooled to 60 DEG C, and by the poly- second after cooling Enolate solution is mixed with gelatin, and into the mixture of poly-vinyl alcohol solution and gelatin, addition hydrochloric acid and glutaraldehyde are water-soluble successively Liquid is 48 DEG C in temperature, and after rotating speed is stirred 12h under conditions of being 300r/min, filtering obtains pretreatment gel, will locate in advance Gel stripping and slicing is managed, deionized water washing by soaking is used in combination 6 days, while a deionized water is changed every 12h, by the gel piece after washing After being dried in vacuo 5h under room temperature, gel is obtained;It is 18% sodium hydroxide solution in mass ratio 1 by pectin and mass fraction:4 It mixes, and the water of 40 times of pectin quality is added into the mixture of pectin and sodium hydroxide, be 45 DEG C in temperature, rotating speed is After being stirred 60min under conditions of 300r/min, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:7 is mixed It closes, and adjusts the 6.5 of pectin solution and lecithin mixture, then addition pectin is molten into the mixture of pectin solution and lecithin 0.3 sodium bicarbonate of liquid quality is 35 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 250r/min, must pre-process Pretreatment pectin mixture after sonic oscillation 10min, is obtained pectin mixing by pectin mixture under conditions of frequency is 55kW Object instills pectin mixture in the calcium chloride solution that mass fraction is 30% with the rate of 3mL/min, in handing under room temperature After joining 30min, filtering obtains filter cake to get property-modifying additive;It counts, weighs successively in parts by weight, 45 portions of modified starches, 60 change Property additive, 80 parts of paraffin, 15 parts of isocyanates, 25 parts of ethyl orthosilicates, by paraffin be added reactor in, in temperature be 60 DEG C Under conditions of heating and melting, and modified starch is sequentially added into reactor, isocyanates, ethyl orthosilicate and additive, in Temperature is 55 DEG C, and after rotating speed is stirred 35min under conditions of being 360r/min, Freezing smashing obtains drilling well anti-sloughing agent.It is described to draw Hair agent is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate.The polyethyleneglycol derivative is polyethylene glycol-to first Any one in benzene sulfonate or polyethylene glycol salicylate.The preparation method of the pretreatment montmorillonite is by montmorillonite and stone Wax in mass ratio 1:4 mixing, and polyacrylic acid zinc is added, after being stirred, Freezing smashing crosses 500 mesh sieve, it is de- must to pre-process illiteracy Stone.The paraffin is the mineral wax mixture that carbon atom number is 36.The isocyanates is isofoer diisocyanate, toluene two Any one in isocyanates or dicyclohexyl methyl hydride diisocyanate.
Example 3
By cationic starch and water in mass ratio 1:6 are mixed in beaker, and the propylene of 0.8 times of starch quality is added into beaker The initiator of 0.3 times of amide and starch quality is 85 DEG C in temperature, and rotating speed is stirred 80min under conditions of being 300r/min Afterwards, it filters, it is dry, obtain modified starch;It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed Together in flask, and the paracide and polyethyleneglycol derivative matter of 0.2 times of polyethyleneglycol derivative quality is added into flask The ferrocene of 0.12 times of amount after rotating speed is stirred 2h under conditions of being 350r/min, obtains inorganic agent, by weight in 75 DEG C of temperature Number meter is measured, is weighed successively:100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water that 40 parts of mass fractions are 28% The hydrochloric acid that solution and 25 parts of mass fractions are 25%, polyvinyl alcohol is mixed with water, in temperature be 98 DEG C, rotating speed 300r/min Under conditions of after stirring 80min, obtain poly-vinyl alcohol solution, poly-vinyl alcohol solution be cooled to 60 DEG C, and by the poly- second after cooling Enolate solution is mixed with gelatin, and into the mixture of poly-vinyl alcohol solution and gelatin, addition hydrochloric acid and glutaraldehyde are water-soluble successively Liquid is 48 DEG C in temperature, and after rotating speed is stirred 12h under conditions of being 300r/min, filtering obtains pretreatment gel, will locate in advance Gel stripping and slicing is managed, deionized water washing by soaking is used in combination 6 days, while a deionized water is changed every 12h, by the gel piece after washing After being dried in vacuo 5h under room temperature, gel is obtained;By gel and water in mass ratio 1:8 mixing, it is 30% that mass fraction, which is used in combination, Hydrochloric acid adjusts the pH to 2.6 of gel and aqueous mixtures, is 40 DEG C in temperature, rotating speed is stirred under conditions of being 230r/min After 25min, gel mixture is obtained, by gel mixture and pretreatment montmorillonite in mass ratio 5:1 mixing, and to gel mixture It it is 28 DEG C in temperature, rotating speed is with the inorganic agent that 0.2 times of gel mixture quality is added in the mixture of pretreatment montmorillonite After being stirred 70min under conditions of 300r/min, modified gel mixture is obtained, the sodium hydroxide for being 12% with mass fraction is molten After liquid adjusts the pH to 6.6 of modified gel mixture, filtering obtains filter cake, dry 2h under conditions of being 80 DEG C in temperature by filter cake Afterwards, modified gel is obtained;It counts, weighs successively in parts by weight, 45 portions of modified starches, 80 parts of paraffin, 15 parts of isocyanates, 25 parts just Paraffin is added in reactor silester, heating and melting under conditions of being 60 DEG C in temperature, and is sequentially added into reactor Modified starch, isocyanates, ethyl orthosilicate and additive are 55 DEG C in temperature, and rotating speed stirs under conditions of being 360r/min After mixing 35min, Freezing smashing obtains drilling well anti-sloughing agent.The initiator is potassium peroxydisulfate, is appointed in ammonium persulfate or sodium peroxydisulfate Meaning is a kind of.The polyethyleneglycol derivative is any one in polyethylene glycol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate. The preparation method of the pretreatment montmorillonite is by montmorillonite and paraffin in mass ratio 1:4 mixing, and polyacrylic acid zinc is added, it stirs After mixing mixing, Freezing smashing crosses 500 mesh sieve, obtains pretreatment montmorillonite.The paraffin is the paraffin mixing that carbon atom number is 36 Object.The isocyanates is isofoer diisocyanate, in toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride diisocyanate Any one.
Example 4
It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed in flask, and to flask The ferrocene of middle 0.12 times of the paracide and polyethyleneglycol derivative quality that 0.2 times of polyethyleneglycol derivative quality is added, in 75 DEG C of temperature obtains inorganic agent, counts in parts by weight, weigh successively after rotating speed is stirred 2h under conditions of being 350r/min: 100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water solution and 25 parts of mass fractions that 40 parts of mass fractions are 28% For 25% hydrochloric acid, polyvinyl alcohol is mixed with water, is 98 DEG C in temperature, rotating speed stirs 80min under conditions of being 300r/min Afterwards, poly-vinyl alcohol solution is obtained, poly-vinyl alcohol solution is cooled to 60 DEG C, and the poly-vinyl alcohol solution after cooling is mixed with gelatin It closes, and hydrochloric acid and glutaraldehyde water solution is added into the mixture of poly-vinyl alcohol solution and gelatin successively, be 48 DEG C in temperature, turn Speed be 300r/min under conditions of be stirred 12h after, filtering, obtain pretreatment gel, will pre-process gel stripping and slicing, and spend from Sub- water washing by soaking 6 days, while a deionized water is changed every 12h, the gel piece after washing is done in vacuum under room temperature After dry 5h, gel is obtained;By gel and water in mass ratio 1:8 mixing are used in combination the hydrochloric acid that mass fraction is 30% to adjust gel mixed with water The pH to 2.6 for closing object is 40 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 230r/min, obtains gel mixing Object, by gel mixture and pretreatment montmorillonite in mass ratio 5:1 mixing, and to gel mixture and pre-process the mixed of montmorillonite The inorganic agent that 0.2 times of gel mixture quality is added in object is closed, is 28 DEG C in temperature, rotating speed stirs under conditions of being 300r/min After mixing 70min, modified gel mixture is obtained, the sodium hydroxide solution for being 12% with mass fraction adjusts modified gel mixture PH to 6.6 after, filtering obtains filter cake, under conditions of being 80 DEG C in temperature by filter cake after dry 2h, obtains modified gel;By pectin It is 18% sodium hydroxide solution in mass ratio 1 with mass fraction:4 mixing, and fruit is added into the mixture of pectin and sodium hydroxide The water that 40 times of colloid amount is 45 DEG C in temperature, after rotating speed is stirred 60min under conditions of being 300r/min, obtains pectin solution, By pectin solution and lecithin in mass ratio 15:7 mixing, and adjust the 6.5 of pectin solution and lecithin mixture, then to pectin 0.3 bicarbonate of modified gel and pectin solution quality of 0.5 times of pectin solution quality is added in the mixture of solution and lecithin Sodium is 35 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 250r/min, obtains pretreatment pectin mixture, will be pre- Handle pectin mixture and after sonic oscillation 10min, obtain pectin mixture under conditions of frequency is 55kW, by pectin mixture with The rate of 3mL/min instills in the calcium chloride solution that mass fraction is 30%, and after being crosslinked 30min under room temperature, filtering obtains Filter cake is to get property-modifying additive;It counts, weighs successively in parts by weight, 60 property-modifying additives, 80 parts of paraffin, 15 parts of isocyanates, 25 parts of ethyl orthosilicates, by paraffin be added reactor in, in temperature be 60 DEG C under conditions of heating and melting, and into reactor according to Secondary addition isocyanates, ethyl orthosilicate and additive are 55 DEG C in temperature, and rotating speed is stirred under conditions of being 360r/min After 35min, Freezing smashing obtains drilling well anti-sloughing agent.The initiator is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate Kind.The polyethyleneglycol derivative is any one in polyethylene glycol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate.It is described The preparation method for pre-processing montmorillonite is by montmorillonite and paraffin in mass ratio 1:4 mixing, and polyacrylic acid zinc is added, stirring is mixed After conjunction, Freezing smashing crosses 500 mesh sieve, obtains pretreatment montmorillonite.The paraffin is the mineral wax mixture that carbon atom number is 36.Institute It is isofoer diisocyanate to state isocyanates, any one in toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride diisocyanate Kind.
Example 5
By cationic starch and water in mass ratio 1:6 are mixed in beaker, and the propylene of 0.8 times of starch quality is added into beaker The initiator of 0.3 times of amide and starch quality is 85 DEG C in temperature, and rotating speed is stirred 80min under conditions of being 300r/min Afterwards, it filters, it is dry, obtain modified starch;It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed Together in flask, and the paracide and polyethyleneglycol derivative matter of 0.2 times of polyethyleneglycol derivative quality is added into flask The ferrocene of 0.12 times of amount after rotating speed is stirred 2h under conditions of being 350r/min, obtains inorganic agent, by weight in 75 DEG C of temperature Number meter is measured, is weighed successively:100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water that 40 parts of mass fractions are 28% The hydrochloric acid that solution and 25 parts of mass fractions are 25%, polyvinyl alcohol is mixed with water, in temperature be 98 DEG C, rotating speed 300r/min Under conditions of after stirring 80min, obtain poly-vinyl alcohol solution, poly-vinyl alcohol solution be cooled to 60 DEG C, and by the poly- second after cooling Enolate solution is mixed with gelatin, and into the mixture of poly-vinyl alcohol solution and gelatin, addition hydrochloric acid and glutaraldehyde are water-soluble successively Liquid is 48 DEG C in temperature, and after rotating speed is stirred 12h under conditions of being 300r/min, filtering obtains pretreatment gel, will locate in advance Gel stripping and slicing is managed, deionized water washing by soaking is used in combination 6 days, while a deionized water is changed every 12h, by the gel piece after washing After being dried in vacuo 5h under room temperature, gel is obtained;By gel and water in mass ratio 1:8 mixing, it is 30% that mass fraction, which is used in combination, Hydrochloric acid adjusts the pH to 2.6 of gel and aqueous mixtures, is 40 DEG C in temperature, rotating speed is stirred under conditions of being 230r/min After 25min, gel mixture is obtained, by gel mixture and pretreatment montmorillonite in mass ratio 5:1 mixing, and to gel mixture It it is 28 DEG C in temperature, rotating speed is with the inorganic agent that 0.2 times of gel mixture quality is added in the mixture of pretreatment montmorillonite After being stirred 70min under conditions of 300r/min, modified gel mixture is obtained, the sodium hydroxide for being 12% with mass fraction is molten After liquid adjusts the pH to 6.6 of modified gel mixture, filtering obtains filter cake, dry 2h under conditions of being 80 DEG C in temperature by filter cake Afterwards, modified gel is obtained;It is 18% sodium hydroxide solution in mass ratio 1 by pectin and mass fraction:4 mixing, and to pectin and hydrogen-oxygen Change the water that 40 times of pectin quality is added in the mixture of sodium, is 45 DEG C in temperature, rotating speed stirs mixed under conditions of being 300r/min After closing 60min, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:7 mixing, and adjust pectin solution and lecithin The 6.5 of lipoprotein mixture, then be added into the mixture of pectin solution and lecithin 0.5 times of pectin solution quality modified gel and 0.3 sodium bicarbonate of pectin solution quality is 35 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 250r/min, obtains Pectin mixture is pre-processed, pretreatment pectin mixture after sonic oscillation 10min, is obtained into pectin under conditions of frequency is 55kW Mixture is instilled pectin mixture in the calcium chloride solution that mass fraction is 30% with the rate of 3mL/min, in room temperature condition After lower crosslinking 30min, filtering obtains filter cake to get property-modifying additive;It counts, weighs successively in parts by weight, 45 portions of modified starches, Paraffin is added in reactor for 60 property-modifying additives, 80 parts of paraffin, 25 parts of ethyl orthosilicates, under conditions of temperature is 60 DEG C Heating and melting, and modified starch is sequentially added into reactor, ethyl orthosilicate and additive are 55 DEG C in temperature, and rotating speed is After being stirred 35min under conditions of 360r/min, Freezing smashing obtains drilling well anti-sloughing agent.The initiator is potassium peroxydisulfate, mistake Any one in ammonium sulfate or sodium peroxydisulfate.The polyethyleneglycol derivative is polyethylene glycol-p-methyl benzenesulfonic acid ester or poly- second two Any one in alcohol salicylate.The preparation method of the pretreatment montmorillonite is by montmorillonite and paraffin in mass ratio 1:4 is mixed It closes, and polyacrylic acid zinc is added, after being stirred, Freezing smashing crosses 500 mesh sieve, obtains pretreatment montmorillonite.The paraffin is carbon The mineral wax mixture that atomicity is 36.
Example 6
By cationic starch and water in mass ratio 1:6 are mixed in beaker, and the propylene of 0.8 times of starch quality is added into beaker The initiator of 0.3 times of amide and starch quality is 85 DEG C in temperature, and rotating speed is stirred 80min under conditions of being 300r/min Afterwards, it filters, it is dry, obtain modified starch;It will(N- amidino groups)Dodecylacrylamide presses quality 1 with polyethyleneglycol derivative:1 is mixed Together in flask, and the paracide and polyethyleneglycol derivative matter of 0.2 times of polyethyleneglycol derivative quality is added into flask The ferrocene of 0.12 times of amount after rotating speed is stirred 2h under conditions of being 350r/min, obtains inorganic agent, by weight in 75 DEG C of temperature Number meter is measured, is weighed successively:100 parts of polyvinyl alcohol, 60 parts of gelatin, 350 parts of water, the glutaraldehyde water that 40 parts of mass fractions are 28% The hydrochloric acid that solution and 25 parts of mass fractions are 25%, polyvinyl alcohol is mixed with water, in temperature be 98 DEG C, rotating speed 300r/min Under conditions of after stirring 80min, obtain poly-vinyl alcohol solution, poly-vinyl alcohol solution be cooled to 60 DEG C, and by the poly- second after cooling Enolate solution is mixed with gelatin, and into the mixture of poly-vinyl alcohol solution and gelatin, addition hydrochloric acid and glutaraldehyde are water-soluble successively Liquid is 48 DEG C in temperature, and after rotating speed is stirred 12h under conditions of being 300r/min, filtering obtains pretreatment gel, will locate in advance Gel stripping and slicing is managed, deionized water washing by soaking is used in combination 6 days, while a deionized water is changed every 12h, by the gel piece after washing After being dried in vacuo 5h under room temperature, gel is obtained;By gel and water in mass ratio 1:8 mixing, it is 30% that mass fraction, which is used in combination, Hydrochloric acid adjusts the pH to 2.6 of gel and aqueous mixtures, is 40 DEG C in temperature, rotating speed is stirred under conditions of being 230r/min After 25min, gel mixture is obtained, by gel mixture and pretreatment montmorillonite in mass ratio 5:1 mixing, and to gel mixture It it is 28 DEG C in temperature, rotating speed is with the inorganic agent that 0.2 times of gel mixture quality is added in the mixture of pretreatment montmorillonite After being stirred 70min under conditions of 300r/min, modified gel mixture is obtained, the sodium hydroxide for being 12% with mass fraction is molten After liquid adjusts the pH to 6.6 of modified gel mixture, filtering obtains filter cake, dry 2h under conditions of being 80 DEG C in temperature by filter cake Afterwards, modified gel is obtained;It is 18% sodium hydroxide solution in mass ratio 1 by pectin and mass fraction:4 mixing, and to pectin and hydrogen-oxygen Change the water that 40 times of pectin quality is added in the mixture of sodium, is 45 DEG C in temperature, rotating speed stirs mixed under conditions of being 300r/min After closing 60min, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:7 mixing, and adjust pectin solution and lecithin The 6.5 of lipoprotein mixture, then be added into the mixture of pectin solution and lecithin 0.5 times of pectin solution quality modified gel and 0.3 sodium bicarbonate of pectin solution quality is 35 DEG C in temperature, after rotating speed is stirred 25min under conditions of being 250r/min, obtains Pectin mixture is pre-processed, pretreatment pectin mixture after sonic oscillation 10min, is obtained into pectin under conditions of frequency is 55kW Mixture is instilled pectin mixture in the calcium chloride solution that mass fraction is 30% with the rate of 3mL/min, in room temperature condition After lower crosslinking 30min, filtering obtains filter cake to get property-modifying additive;It counts, weighs successively in parts by weight, 45 portions of modified starches, Paraffin is added in reactor for 60 property-modifying additives, 80 parts of paraffin, 15 parts of isocyanates, adds under conditions of being 60 DEG C in temperature Heat is melted, and modified starch is sequentially added into reactor, isocyanates and additive, is 55 DEG C in temperature, rotating speed is After being stirred 35min under conditions of 360r/min, Freezing smashing obtains drilling well anti-sloughing agent.The initiator is potassium peroxydisulfate, mistake Any one in ammonium sulfate or sodium peroxydisulfate.The polyethyleneglycol derivative is polyethylene glycol-p-methyl benzenesulfonic acid ester or poly- second two Any one in alcohol salicylate.The preparation method of the pretreatment montmorillonite is by montmorillonite and paraffin in mass ratio 1:4 is mixed It closes, and polyacrylic acid zinc is added, after being stirred, Freezing smashing crosses 500 mesh sieve, obtains pretreatment montmorillonite.The paraffin is carbon The mineral wax mixture that atomicity is 36.The isocyanates is isofoer diisocyanate, toluene di-isocyanate(TDI) or two rings Any one in hexyl methane diisocyanate.
Comparative example:The anti-collapse prescription of drilling equipment Manufacturing Co., Ltd of Taiyuan City production.
The drilling well anti-sloughing agent and comparative example product of example 1 to 6 gained of example are subjected to performance detection, specific detection method is such as Under:
1. penetration depth:Reagent is added, it is high to measure filter pressing loss, high temperature in the room temperature of different experiments slurry by aging 16h at 120 DEG C Press state filter loss and high temperature and pressure casting bed penetration depth;
2. core permeability:It is 625.4 × 10-3 μm 2 that water, which surveys permeability, and experimental temperature is 120 DEG C, is forced into 4.2MPa, confining pressure To 0.7MPa, leak-off 1h;
3. sealing ratiod:It is obtained with comparing core permeability before and after leak-off.
Specific testing result is as shown in table 1:
Table 1:The specific testing result amount of drilling well anti-sloughing agent
Detection project Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Comparative example
Penetration depth(DHTHP 4.0 4.9 5.6 6.0 9.9 10.0 10.5
Core permeability(10-3 μm2 69.7 72.3 93.1 103.2 169.3 275.9 310.6
Sealing ratiod(%) 96.98 90.23 84.12 73.60 70.01 64.53 50.19
By 1 testing result of table, it is found that drilling well anti-sloughing agent prepared by technical solution of the present invention has, permeability resistance is high, caving-preventing characteristic is strong The characteristics of, it has broad prospects in the development of high polymer material technology industry.

Claims (6)

1. a kind of preparation method of drilling well anti-sloughing agent, which is characterized in that specifically preparation process is:
(1)By cationic starch and water in mass ratio 1:4~1:6 mixing, and 0.6~0.8 times of cationic starch quality is added The initiator of 0.1~0.3 times of acrylamide and starch quality after being stirred, filters, dry, obtains modified starch;
(2)It will(N- amidino groups)Dodecylacrylamide and polyethyleneglycol derivative in mass ratio 2:1~1:1 mixing, and be added Two cyclopentadienyls of 0.08~0.12 times of the paracide and polyethyleneglycol derivative quality that 0.1~0.2 times of polyethyleneglycol derivative quality Iron is stirred, and obtains inorganic agent;
(3)It counts, weighs successively in parts by weight:80~100 parts of polyvinyl alcohol, 40~60 parts of gelatin, 250~350 parts of water, 30~ 40 parts of glutaraldehyde water solutions and 10~25 parts of hydrochloric acid, polyvinyl alcohol is mixed with water, and heating stirring obtains poly-vinyl alcohol solution, will Poly-vinyl alcohol solution cools down, and the poly-vinyl alcohol solution after cooling is mixed with gelatin, and sequentially adds hydrochloric acid and glutaraldehyde water Solution, after being stirred, filtering, stripping and slicing is washed, and vacuum drying obtains gel;
(4)By gel and water in mass ratio 1:5~1:8 mixing, and pH to 2.0~2.6 is adjusted, it is stirred, obtains gel mixing Object, by gel mixture and pretreatment montmorillonite in mass ratio 3:1~5:1 mixing, and be added gel mixture quality 0.1~ 0.2 times of inorganic agent after being stirred, obtains modified gel mixture, adjusts the pH to 5.6~6.6 of modified gel mixture, mistake Filter, it is dry, obtain modified gel;
(5)By pectin and sodium hydroxide solution in mass ratio 1:3~1:4 mixing, and the water of 20~40 times of pectin quality is added, it stirs After mixing mixing, pectin solution is obtained, by pectin solution and lecithin in mass ratio 15:3~15:7 mixing, and adjust pH to 6.0~ 6.5, the sodium bicarbonate of 0.1~0.3 times of the modified gel and pectin solution quality of 0.4~0.5 times of pectin solution quality is added, stirs After mixing mixing, sonic oscillation obtains pectin mixture, and pectin mixture is instilled calcium chloride solution with the rate of 1~3mL/min In, after being crosslinked 15~30min, filtering obtains property-modifying additive;
(6)It counts, weighs successively in parts by weight, 35~45 portions of modified starches, 50~60 property-modifying additives, 40~80 parts of paraffin, 10~15 parts of isocyanates, 22~25 parts of ethyl orthosilicates, heating paraffin are melted, and modified starch is added, isocyanates, just Silester and additive, after being stirred, Freezing smashing crosses 320~500 mesh sieve, obtains drilling well anti-sloughing agent.
2. a kind of preparation method of drilling well anti-sloughing agent according to claim 1, it is characterised in that:Step(1)The initiation Agent is potassium peroxydisulfate, any one in ammonium persulfate or sodium peroxydisulfate.
3. a kind of preparation method of drilling well anti-sloughing agent according to claim 1, it is characterised in that:Step(2)The poly- second Diol, derivatives are any one in polyethylene glycol-p-methyl benzenesulfonic acid ester or polyethylene glycol salicylate.
4. a kind of preparation method of drilling well anti-sloughing agent according to claim 1, it is characterised in that:Step(4)The pre- place The preparation method for managing montmorillonite is by montmorillonite and paraffin in mass ratio 1:3~1:4 mixing, and polyacrylic acid zinc is added, it stirs After mixing, Freezing smashing obtains pretreatment montmorillonite.
5. a kind of preparation method of drilling well anti-sloughing agent according to claim 1, it is characterised in that:Step(6)The paraffin The mineral wax mixture for being 24~36 for carbon atom number.
6. a kind of preparation method of drilling well anti-sloughing agent according to claim 1, it is characterised in that:Step(6)The isocyanide Acid esters is isofoer diisocyanate, any one in toluene di-isocyanate(TDI) or dicyclohexyl methyl hydride diisocyanate.
CN201810361215.4A 2018-04-20 2018-04-20 A kind of preparation method of drilling well anti-sloughing agent Pending CN108359417A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113372889A (en) * 2021-06-23 2021-09-10 成都西油华巍科技有限公司 High water loss plugging agent

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CN102676141A (en) * 2012-04-20 2012-09-19 中国海洋石油总公司 Deformable plugging and anti-sloughing agent for drilling fluid
CN103725266A (en) * 2013-12-23 2014-04-16 河南海洋化工有限公司 Anti-collapse inhibitor for drilling fluid and preparation method of anti-collapse inhibitor
CN104194741A (en) * 2014-08-05 2014-12-10 新乡市富邦科技有限公司 High-temperature-resistant salt-resistant anti-collapse filtrate reducer for drilling fluid and preparation method of high-temperature-resistant salt-resistant anti-collapse filtrate reducer

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102676141A (en) * 2012-04-20 2012-09-19 中国海洋石油总公司 Deformable plugging and anti-sloughing agent for drilling fluid
CN103725266A (en) * 2013-12-23 2014-04-16 河南海洋化工有限公司 Anti-collapse inhibitor for drilling fluid and preparation method of anti-collapse inhibitor
CN104194741A (en) * 2014-08-05 2014-12-10 新乡市富邦科技有限公司 High-temperature-resistant salt-resistant anti-collapse filtrate reducer for drilling fluid and preparation method of high-temperature-resistant salt-resistant anti-collapse filtrate reducer

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113372889A (en) * 2021-06-23 2021-09-10 成都西油华巍科技有限公司 High water loss plugging agent
CN113372889B (en) * 2021-06-23 2022-11-08 成都西油华巍科技有限公司 High water loss plugging agent

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