CN106279509B - Oily double suction resin and preparation method and application are met suitable for the chance water of oil-well cement - Google Patents
Oily double suction resin and preparation method and application are met suitable for the chance water of oil-well cement Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 106
- 239000011347 resin Substances 0.000 title claims abstract description 90
- 229920005989 resin Polymers 0.000 title claims abstract description 90
- 239000004568 cement Substances 0.000 title claims abstract description 24
- 239000003129 oil well Substances 0.000 title claims abstract description 14
- 238000002360 preparation method Methods 0.000 title claims abstract description 14
- 238000010521 absorption reaction Methods 0.000 claims abstract description 57
- 239000002250 absorbent Substances 0.000 claims abstract description 41
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 239000003431 cross linking reagent Substances 0.000 claims abstract description 22
- 239000004530 micro-emulsion Substances 0.000 claims abstract description 19
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 14
- 239000003999 initiator Substances 0.000 claims abstract description 12
- 239000007957 coemulsifier Substances 0.000 claims abstract description 10
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 6
- 239000000178 monomer Substances 0.000 claims description 36
- 239000012153 distilled water Substances 0.000 claims description 26
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical group C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 claims description 22
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical group N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 claims description 22
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical group NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims description 22
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical group CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 22
- GMSCBRSQMRDRCD-UHFFFAOYSA-N dodecyl 2-methylprop-2-enoate Chemical compound CCCCCCCCCCCCOC(=O)C(C)=C GMSCBRSQMRDRCD-UHFFFAOYSA-N 0.000 claims description 16
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 13
- 239000011837 N,N-methylenebisacrylamide Substances 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical group C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 10
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical group [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 8
- 235000019333 sodium laurylsulphate Nutrition 0.000 claims description 8
- 230000003068 static effect Effects 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 3
- 238000001035 drying Methods 0.000 claims description 2
- 238000012703 microemulsion polymerization Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 33
- 238000000034 method Methods 0.000 abstract description 9
- 230000015572 biosynthetic process Effects 0.000 abstract description 8
- 238000003786 synthesis reaction Methods 0.000 abstract description 5
- 230000032798 delamination Effects 0.000 abstract description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 16
- 238000012360 testing method Methods 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- 230000002745 absorbent Effects 0.000 description 4
- 230000008961 swelling Effects 0.000 description 4
- -1 Sodium dialkylsulfate Chemical class 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 230000005465 channeling Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000000593 microemulsion method Methods 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 240000003183 Manihot esculenta Species 0.000 description 2
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000011229 interlayer Substances 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000001878 scanning electron micrograph Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 239000004141 Sodium laurylsulphate Substances 0.000 description 1
- 208000013201 Stress fracture Diseases 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000001588 bifunctional effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013399 early diagnosis Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000008398 formation water Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000008601 oleoresin Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000011555 saturated liquid Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
- C08F220/12—Esters of monohydric alcohols or phenols
- C08F220/14—Methyl esters, e.g. methyl (meth)acrylate
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/12—Polymerisation in non-solvents
- C08F2/16—Aqueous medium
- C08F2/22—Emulsion polymerisation
- C08F2/24—Emulsion polymerisation with the aid of emulsifying agents
- C08F2/26—Emulsion polymerisation with the aid of emulsifying agents anionic
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
- C08F220/12—Esters of monohydric alcohols or phenols
- C08F220/16—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
- C08F220/18—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
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- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/42—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells
- C09K8/46—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells containing inorganic binders, e.g. Portland cement
- C09K8/467—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells containing inorganic binders, e.g. Portland cement containing additives for specific purposes
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- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
- C08F220/12—Esters of monohydric alcohols or phenols
- C08F220/16—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms
- C08F220/18—Esters of monohydric alcohols or phenols of phenols or of alcohols containing two or more carbon atoms with acrylic or methacrylic acids
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Abstract
本发明公开了一种适于油井水泥的遇水遇油双吸树脂及制备方法和应用,制备方法利用双连续微乳液为模板,将蒸馏水、水相单体、水相交联剂、油相单体、油相交联剂、乳化剂、助乳化剂、引发剂依次加入到反应容器中,搅拌混合均匀形成单相无色透明双连续微乳液后进行聚合反应。本发明合成过程稳定,在聚合过程中能够保持微乳液不分层,合成时间短;合成的遇水遇油双吸树脂吸液速率快。当油井井下水泥环发生破坏产生微裂缝时,遇水遇油双吸树脂遇到通过微裂缝的水流或油流能够快速吸水吸油膨胀,在水泥环破坏的地方形成物理封隔。
The invention discloses a water-meets-oil double-absorbing resin suitable for oil well cement and its preparation method and application. The body, the oil phase cross-linking agent, the emulsifier, the co-emulsifier and the initiator are sequentially added into the reaction vessel, stirred and mixed evenly to form a single-phase colorless transparent double continuous microemulsion, and then carry out the polymerization reaction. The synthesis process of the invention is stable, the microemulsion can be kept from delamination during the polymerization process, and the synthesis time is short; the synthesized water-meeting double-absorbent resin has a fast liquid absorption rate. When the downhole cement sheath of an oil well is damaged and micro-cracks occur, the double-absorbent resin that encounters water and oil meets the water flow or oil flow through the micro-cracks and can quickly absorb water and oil to expand, forming a physical seal at the place where the cement sheath is damaged.
Description
技术领域technical field
本发明涉及一种遇水遇油双吸树脂的制备方法,还涉及一种该制备方法制备的遇水遇油双吸树脂,以及该遇水遇油双吸树脂作为油井水泥中吸水吸油膨胀成分中的应用。属于油气井固井及油田化学领域。The present invention relates to a method for preparing a water-meets-oil double-absorbent resin, and also relates to a water-meets-oil double-absorbent resin prepared by the preparation method, and the water-meets-oil double-absorbent resin used as a water-oil-absorbing swelling component in oil well cement in the application. The invention belongs to the fields of oil and gas well cementing and oil field chemistry.
背景技术Background technique
油气井水泥环在高温高压等复杂井下条件,投产后必然面对各种试井、测试及生产等复杂作业,产生的压应力和热应力不可避免地使水泥环产生微间隙和微裂缝,产生地层流体的窜流通道,造成层间封隔失效。The cement sheath of oil and gas wells is subjected to complex downhole conditions such as high temperature and high pressure. After it is put into production, it will inevitably face various complex operations such as well testing, testing and production. The channel of formation fluid channeling causes the failure of interlayer isolation.
把吸水吸油膨胀树脂作为添加剂加入到水泥中,当水泥石内部产生微裂缝或微环隙,无论地层水还是地层油流渗入到微裂缝或微环隙处,此时微裂缝或微环隙处的遇水遇油双吸树脂都会吸水或吸油膨胀,膨胀后的吸水吸油树脂具有一定强度,能够堵塞微裂缝或微环隙,在水泥失效层形成了物理封堵,防止地层流体窜流。因此,开发出能够实现对水泥环内部损伤早期诊断并自动修复、愈合的油井水泥——特别是目前修井技术无法较好解决的薄油水互层修井问题,对提高固井水泥环复杂条件下的长期稳定性有着重要意义。The water-absorbing and oil-absorbing expansion resin is added to the cement as an additive. When micro-cracks or micro-annulus are formed inside the cement stone, whether formation water or formation oil flows into the micro-cracks or micro-annulus, the micro-cracks or micro-annulus The water- and oil-absorbing double-absorbent resin will absorb water or oil and swell. The expanded water-absorbing and oil-absorbing resin has a certain strength and can block micro-cracks or micro-annulus, forming a physical plug in the cement failure layer to prevent formation fluid channeling. Therefore, the development of oil well cement that can realize the early diagnosis of the internal damage of the cement sheath and automatically repair and heal it—especially the workover problem of thin oil-water interlayer that cannot be well solved by the current workover technology, is of great help to improve the complex conditions of the cement sheath. long-term stability is of great importance.
中国专利CN102887978A制备了一种交联接枝木薯淀粉型高吸水吸油性树脂,中国专利CN102603978A制备了一种纤维素基吸水吸油材料,但是木薯淀粉和纤维素在高温条件下热稳定性差,容易降解,不适用于油井水泥高温环境中;中国专利CN102850483A利用乳液共聚制备了吸水吸油双功能树脂,但是该方法制备时间长,不利于工业化生产,该材料中吸水组分并不是连续的,不能够实现快速吸水膨胀,无法实现固井水泥环微裂缝快速封堵。而双连续微乳液体系是热力学稳定体系,能够较高温度下聚合,缩短合成时间;另外,由双连续微乳液法制备的遇水遇油双吸树脂中吸水膨胀组分和吸油膨胀组分都是连续的结构,并且树脂内部多孔,能够实现快速吸水吸油的目的。Chinese patent CN102887978A prepared a cross-linked cassava starch type super absorbent and oil-absorbing resin, and Chinese patent CN102603978A prepared a cellulose-based water-absorbing and oil-absorbing material, but tapioca starch and cellulose have poor thermal stability under high temperature conditions and are easy to degrade , not suitable for high temperature environment of oil well cement; Chinese patent CN102850483A uses emulsion copolymerization to prepare water-absorbing oil-absorbing bifunctional resin, but the preparation time of this method is long, which is not conducive to industrial production, and the water-absorbing component in this material is not continuous and cannot be realized Rapid water absorption and expansion cannot achieve rapid plugging of micro-fractures in the cement sheath. The double continuous microemulsion system is a thermodynamically stable system, which can be polymerized at a higher temperature and shorten the synthesis time; in addition, the water-absorbing and oil-absorbing resins prepared by the double-continuous microemulsion method have both water-absorbing and oil-swelling components. It is a continuous structure, and the resin is porous inside, which can achieve the purpose of rapid water and oil absorption.
发明内容Contents of the invention
本发明的目的在于提供一种适用于油井水泥的遇水遇油双吸树脂及制备方法与应用。The object of the present invention is to provide a kind of water and oil double absorption resin suitable for oil well cement, its preparation method and application.
为了实现上述目的,根据本发明提出一种遇水遇油双吸树脂,包括蒸馏水、水相单体、水相交联剂、油相单体、油相交联剂、乳化剂、助乳化剂、引发剂,其中水相单体加量为蒸馏水质量的12.5%~20%,水相交联剂加量为水相单体质量的5%~15%,油相单体加量与蒸馏水和水相单体总质量的质量比为1:1,油相交联剂加量为油相单体质量的0.3%~1%,引发剂加量为水相单体和油相单体质量和的1%~4%,乳化剂加量为蒸馏水和水相单体质量和的15%~20%,助乳化剂加量为乳化剂质量的300%~400%。In order to achieve the above object, according to the present invention, a kind of water and oil double absorption resin is proposed, including distilled water, water phase monomer, water phase crosslinking agent, oil phase monomer, oil phase crosslinking agent, emulsifier, co-emulsifier, initiator The amount of water phase monomer added is 12.5% to 20% of the mass of distilled water, the amount of water phase crosslinking agent added is 5% to 15% of the mass of water phase monomer, and the amount of oil phase monomer added is the same as that of distilled water and water phase. The mass ratio of the total mass of the body is 1:1, the amount of the oil phase crosslinking agent is 0.3% to 1% of the mass of the oil phase monomer, and the amount of the initiator is 1% to 1% of the sum of the mass of the water phase monomer and the oil phase monomer 4%, the amount of emulsifier added is 15% to 20% of the mass sum of distilled water and water phase monomers, and the amount of co-emulsifier added is 300% to 400% of the mass of emulsifier.
优选的,所述水相单体为丙烯酰胺,所述水相交联剂为N,N-亚甲基双丙烯酰胺,所述油相单体为甲基丙烯酸甲酯和甲基丙烯酸十二酯的混合物,甲基丙烯酸甲酯和甲基丙烯酸十二酯的质量比为(20~100):100,所述油相交联剂为二乙烯基苯,所述乳化剂为十二烷基硫酸钠,所述助乳化剂为正丁醇,所述引发剂为偶氮二异丁腈。Preferably, the water phase monomer is acrylamide, the water phase crosslinking agent is N, N-methylenebisacrylamide, and the oil phase monomer is methyl methacrylate and lauryl methacrylate The mixture, the mass ratio of methyl methacrylate and lauryl methacrylate is (20~100): 100, the oil phase crosslinking agent is divinylbenzene, and the emulsifier is sodium lauryl sulfate , the co-emulsifier is n-butanol, and the initiator is azobisisobutyronitrile.
优选的,其通过双连续微乳液法制备的,即采用双连续微乳液聚合法制备过程中,将蒸馏水、水相单体、水相交联剂、油相单体、油相交联剂、乳化剂、助乳化剂、引发剂依次加入到反应容器中,搅拌混合均匀形成单相无色透明双连续微乳液后进行聚合反应。Preferably, it is prepared by the double continuous microemulsion method, that is, in the preparation process of the double continuous microemulsion polymerization method, the distilled water, the water phase monomer, the water phase crosslinking agent, the oil phase monomer, the oil phase crosslinking agent, the emulsifier , co-emulsifier and initiator are sequentially added into the reaction vessel, stirred and mixed evenly to form a single-phase colorless transparent double continuous microemulsion, and then carry out polymerization reaction.
本发明还提供了上述遇水遇油双吸树脂的制备方法,将蒸馏水、水相单体、水相交联剂、油相单体、油相交联剂、乳化剂、助乳化剂、引发剂依次加入到反应容器中,排出反应容器中的氧气,在400-600转/分的转速下搅拌混合成单相无色透明双连续微乳液,在40-80℃水浴中静止反应,所得产物经干燥粉碎后得到遇水遇油双吸树脂。The present invention also provides a preparation method for the above-mentioned water-meets-oil double-absorbent resin, wherein distilled water, water phase monomers, water phase crosslinking agents, oil phase monomers, oil phase crosslinking agents, emulsifiers, co-emulsifiers, and initiators are sequentially Add it into the reaction vessel, discharge the oxygen in the reaction vessel, stir and mix it at a speed of 400-600 rpm to form a single-phase colorless transparent double continuous microemulsion, react statically in a water bath at 40-80°C, and the obtained product is dried After being pulverized, a water-meets-oil double-absorbent resin is obtained.
优选的,所述搅拌转速为500转/分。Preferably, the stirring speed is 500 rpm.
优选的,所述水浴温度为60℃,静止反应3h。Preferably, the temperature of the water bath is 60° C., and the static reaction is performed for 3 hours.
优选的,所述干燥为在80℃下干燥24h。Preferably, the drying is at 80° C. for 24 hours.
本发明另外提供了上述遇水遇油双吸树脂作为油井水泥中吸水吸油膨胀成分的应用。The present invention further provides the application of the above-mentioned water-meets-oil double-absorbent resin as a water-absorbing and oil-absorbing swelling component in oil well cement.
本发明的制备方法利用双连续微乳液为模板,在这种微乳液中,水相和油相都是连续的,在水相和油相中分别加入水相聚合单体和油相聚合单体,在引发剂的作用下发生聚合反应,得到具有双连续结构的遇水遇油双吸树脂,即遇水遇油双吸树脂中的遇水膨胀组分和遇油膨胀组分都是连续的结构,并且树脂内部多孔,因此能够避免树脂不吸水或不吸油,并且能够达到快速吸水吸油的目的。The preparation method of the present invention utilizes a double continuous microemulsion as a template. In this microemulsion, the water phase and the oil phase are continuous, and the water phase polymerized monomer and the oil phase polymerized monomer are respectively added into the water phase and the oil phase. , a polymerization reaction occurs under the action of an initiator to obtain a water-in-oil double-absorbent resin with a bicontinuous structure, that is, the water-swellable component and the oil-swellable component in the water-in-oil double-absorbent resin are continuous Structure, and the resin is porous inside, so it can prevent the resin from not absorbing water or oil, and can achieve the purpose of rapid water and oil absorption.
本发明合成过程稳定,在聚合过程中能够保持微乳液不分层,合成时间短;合成的遇水遇油双吸树脂吸液速率快。本发明的制备方法制备的遇水遇油双吸树脂添加到油井水泥中,当油井井下水泥环发生破坏时,无论油流或水流通过水泥环裂缝,遇水遇油双吸树脂都能吸油或吸水膨胀,在水泥环破坏的地方形成物理封隔,封堵裂缝,阻止井下不同层位间流体窜流。在油井水泥中应用遇水遇油双吸树脂,要求树脂的吸液倍率在5~6之间。如果树脂吸液倍率过低,树脂吸液膨胀后不能达到有效封堵裂缝的作用;如果树脂吸液倍率过高,树脂吸液膨胀产生的膨胀力过大,可能会破坏水泥石的完整性。The synthesis process of the invention is stable, the microemulsion can be kept from delamination during the polymerization process, and the synthesis time is short; the synthesized water-meeting double-absorbent resin has a fast liquid absorption rate. The water-meets-oil double-absorbent resin prepared by the preparation method of the present invention is added to the oil well cement, and when the downhole cement sheath of the oil well is damaged, the water-meets-oil double-absorbent resin can absorb oil or It absorbs water and swells, forming a physical seal at the place where the cement sheath is damaged, sealing the cracks, and preventing fluid channeling between different layers in the well. In the application of water and oil double absorption resin in oil well cement, the liquid absorption ratio of the resin is required to be between 5 and 6. If the resin absorption rate is too low, the resin cannot effectively seal the crack after the resin absorbs liquid expansion; if the resin absorption rate is too high, the expansion force generated by the resin absorption expansion is too large, which may damage the integrity of the cement stone.
本发明所述的一种适用于油井水泥的遇水遇油双吸树脂的吸液倍数测定方法如下:A method for measuring the liquid absorption multiple of a water-meets-oil double-absorbent resin suitable for oil well cement according to the present invention is as follows:
称取一定质量的遇水遇油双吸树脂粉末,记为W1,放入白色无纺布袋中,称量树脂和布袋的总质量,记为W2,然后放入盛有蒸馏水或甲苯的烧杯中,考虑井下温度,在75℃条件下进行吸液测试,每隔5min取出无纺布袋,悬挂至基本无液滴低落,称量无纺布袋和吸液后树脂的总质量,记为W3,计算遇水遇油双吸树脂的吸液倍率,其公式为:吸液倍率(g/g)=(W3-W2)/W1。Weigh a certain amount of water-in-oil double-absorbent resin powder, record it as W1, put it into a white non-woven bag, weigh the total mass of the resin and the bag, record it as W2, and then put it into a beaker filled with distilled water or toluene In the process, considering the downhole temperature, the liquid absorption test was carried out at 75°C, and the non-woven bag was taken out every 5 minutes, and hung until there was basically no liquid drop, and the total mass of the non-woven bag and the resin after liquid absorption was weighed, recorded as W3, calculate the liquid absorption rate of the water-in-oil double-absorbent resin, the formula is: liquid absorption rate (g/g)=(W3-W2)/W1.
本发明所述的一种适用于油井水泥的遇水遇油双吸树脂的吸液速率测定方法如下:A method for measuring the liquid absorption rate of a water-meets-oil double-absorbent resin suitable for oil well cement according to the present invention is as follows:
吸液速率是指给定时间的吸液倍率(W4)和饱和吸液倍率(W5)的比值,为了实现快速吸液膨胀,本发明中给定的时间为10分钟。吸液速率=W4/W5。The liquid absorption rate refers to the ratio of the liquid absorption rate (W4) and the saturated liquid absorption rate (W5) at a given time. In order to realize rapid liquid absorption expansion, the given time in the present invention is 10 minutes. Liquid absorption rate = W4/W5.
本发明的附加方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过本发明的实践了解到。Additional aspects and advantages of the invention will be set forth in the description which follows, and in part will be obvious from the description, or may be learned by practice of the invention.
附图说明Description of drawings
图1为遇水遇油双吸树脂的照片图,其中A为实施例2所得的树脂,B为实施例9所得的树脂;Fig. 1 is the photogram of water encountering oil double absorption resin, wherein A is the resin obtained in embodiment 2, and B is the resin obtained in embodiment 9;
图2为遇水遇油双吸树脂的扫描电镜图,其中A为实施例2所得的树脂,B为实施例4所得的树脂。Fig. 2 is the scanning electron micrograph of water-meets-oil double-absorption resin, wherein A is the resin obtained in Example 2, and B is the resin obtained in Example 4.
具体实施方式Detailed ways
以下结合具体实例,对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific examples.
实施例1:Example 1:
在反应容器中加入8g蒸馏水、1g丙烯酰胺、0.1g N,N-亚甲基双丙烯酰胺、4.5g甲基丙烯酸甲酯、4.5g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、5.5g正丁醇、0.3g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 8g of distilled water, 1g of acrylamide, 0.1g of N,N-methylenebisacrylamide, 4.5g of methyl methacrylate, 4.5g of lauryl methacrylate, 0.05g of divinylbenzene, 1.8 1g sodium lauryl sulfate, 5.5g n-butanol, 0.3g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix at a speed of 500 rpm to form a single-phase colorless transparent double continuous The microemulsion was statically reacted in a water bath at 60°C for 3 hours, and the product was dried at 80°C for 24 hours, and then pulverized to obtain a water-meets-oil double-absorbent resin.
实施例2:Example 2:
在反应容器中加入7.5g蒸馏水、1.5g丙烯酰胺、0.15g N,N-亚甲基双丙烯酰胺、4.5g甲基丙烯酸甲酯、4.5g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、5.9g正丁醇、0.315g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 7.5g distilled water, 1.5g acrylamide, 0.15g N,N-methylenebisacrylamide, 4.5g methyl methacrylate, 4.5g lauryl methacrylate, 0.05g divinylbenzene to the reaction vessel , 1.8g sodium lauryl sulphate, 5.9g n-butanol, 0.315g azobisisobutyronitrile, nitrogen discharge oxygen in the reaction vessel, stirring and mixing at a speed of 500 rpm to form a single-phase colorless and transparent Double continuous microemulsion, react statically in a water bath at 60°C for 3 hours, dry the product at 80°C for 24 hours, and pulverize to obtain a water-meets-oil double absorbent resin.
实施例3:Example 3:
在反应容器中加入7g蒸馏水、2g丙烯酰胺、0.2g N,N-亚甲基双丙烯酰胺、4.5g甲基丙烯酸甲酯、4.5g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、6.2g正丁醇、0.33g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 7g of distilled water, 2g of acrylamide, 0.2g of N,N-methylenebisacrylamide, 4.5g of methyl methacrylate, 4.5g of lauryl methacrylate, 0.05g of divinylbenzene, 1.8 1g sodium lauryl sulfate, 6.2g n-butanol, 0.33g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix under the rotating speed of 500 rpm to form a single-phase colorless transparent double continuous The microemulsion was statically reacted in a water bath at 60°C for 3 hours, and the product was dried at 80°C for 24 hours, and then pulverized to obtain a water-meets-oil double-absorbent resin.
实施例4:Example 4:
在反应容器中加入6.5g蒸馏水、2.5g丙烯酰胺、0.25g N,N-亚甲基双丙烯酰胺、4.5g甲基丙烯酸甲酯、4.5g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、6.4g正丁醇、0.345g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 6.5g distilled water, 2.5g acrylamide, 0.25g N,N-methylenebisacrylamide, 4.5g methyl methacrylate, 4.5g lauryl methacrylate, 0.05g divinylbenzene to the reaction vessel , 1.8g sodium lauryl sulfate, 6.4g n-butanol, 0.345g azobisisobutyronitrile, vent the oxygen in the reaction vessel with nitrogen gas, and stir and mix at a speed of 500 rpm to form a single-phase colorless and transparent Double continuous microemulsion, react statically in a water bath at 60°C for 3 hours, dry the product at 80°C for 24 hours, and pulverize to obtain a water-meets-oil double absorbent resin.
实施例5:Example 5:
在反应容器中加入8g蒸馏水、1g丙烯酰胺、0.1g N,N-亚甲基双丙烯酰胺、3g甲基丙烯酸甲酯、6g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、5.5g正丁醇、0.3g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 8g of distilled water, 1g of acrylamide, 0.1g of N,N-methylenebisacrylamide, 3g of methyl methacrylate, 6g of lauryl methacrylate, 0.05g of divinylbenzene, 1.8g of Sodium dialkylsulfate, 5.5g n-butanol, 0.3g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix at a speed of 500 rpm to form a single-phase colorless transparent double continuous microemulsion , reacted statically in a water bath at 60°C for 3h, dried the product at 80°C for 24h, and pulverized to obtain a double-absorbent resin when meeting water and oil.
实施例6:Embodiment 6:
在反应容器中加入8g蒸馏水、1g丙烯酰胺、0.1g N,N-亚甲基双丙烯酰胺、1.5g甲基丙烯酸甲酯、7.5g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、5.5g正丁醇、0.3g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 8g of distilled water, 1g of acrylamide, 0.1g of N,N-methylenebisacrylamide, 1.5g of methyl methacrylate, 7.5g of dodecyl methacrylate, 0.05g of divinylbenzene, 1.8 1g sodium lauryl sulfate, 5.5g n-butanol, 0.3g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix at a speed of 500 rpm to form a single-phase colorless transparent double continuous The microemulsion was statically reacted in a water bath at 60°C for 3 hours, and the product was dried at 80°C for 24 hours, and then pulverized to obtain a water-meets-oil double-absorbent resin.
实施例7:Embodiment 7:
在反应容器中加入8g蒸馏水、1g丙烯酰胺、0.1g N,N-亚甲基双丙烯酰胺、6g甲基丙烯酸甲酯、3g甲基丙烯酸十二酯、0.05g二乙烯基苯、1.8g十二烷基硫酸钠、5.5g正丁醇、0.3g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 8g of distilled water, 1g of acrylamide, 0.1g of N,N-methylenebisacrylamide, 6g of methyl methacrylate, 3g of lauryl methacrylate, 0.05g of divinylbenzene, 1.8g of Sodium dialkylsulfate, 5.5g n-butanol, 0.3g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix at a speed of 500 rpm to form a single-phase colorless transparent double continuous microemulsion , reacted statically in a water bath at 60°C for 3h, dried the product at 80°C for 24h, and pulverized to obtain a double-absorbent resin when meeting water and oil.
实施例8:Embodiment 8:
在反应容器中加入8g蒸馏水、1g丙烯酰胺、0.15g N,N-亚甲基双丙烯酰胺、3g甲基丙烯酸甲酯、6g甲基丙烯酸十二酯、0.072g二乙烯基苯、1.8g十二烷基硫酸钠、5.5g正丁醇、0.4g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 8g of distilled water, 1g of acrylamide, 0.15g of N,N-methylenebisacrylamide, 3g of methyl methacrylate, 6g of lauryl methacrylate, 0.072g of divinylbenzene, 1.8g of Sodium dialkylsulfate, 5.5g n-butanol, 0.4g azobisisobutyronitrile, the oxygen in the reaction vessel is exhausted by nitrogen gas, stirring and mixing at a speed of 500 rpm to form a single-phase colorless transparent double continuous microemulsion , reacted statically in a water bath at 60°C for 3h, dried the product at 80°C for 24h, and pulverized to obtain a double-absorbent resin when meeting water and oil.
实施例9:Embodiment 9:
在反应容器中加入7.5g蒸馏水、1.5g丙烯酰胺、0.075g N,N-亚甲基双丙烯酰胺、1.5g甲基丙烯酸甲酯、7.5g甲基丙烯酸十二酯、0.03g二乙烯基苯、1.5g十二烷基硫酸钠、6g正丁醇、0.11g偶氮二异丁腈,通氮气排出反应容器中的氧气,在500转/分的转速下搅拌混合成单相无色透明双连续微乳液,在60℃水浴中静止反应3h,产物在80℃下干燥24h,粉碎后得到遇水遇油双吸树脂。Add 7.5g distilled water, 1.5g acrylamide, 0.075g N,N-methylenebisacrylamide, 1.5g methyl methacrylate, 7.5g lauryl methacrylate, 0.03g divinylbenzene to the reaction vessel , 1.5g sodium lauryl sulfate, 6g n-butanol, 0.11g azobisisobutyronitrile, blow nitrogen to discharge the oxygen in the reaction vessel, stir and mix at a speed of 500 rpm to form a single-phase colorless transparent double Continuous microemulsion, static reaction in a water bath at 60°C for 3 hours, the product was dried at 80°C for 24 hours, and pulverized to obtain a double-absorbent resin when meeting water and oil.
实施例1~实施例4所得遇水遇油双吸树脂的吸液倍率和吸液速率如表1所示。The liquid absorption ratio and liquid absorption rate of the water-oil double-absorbent resins obtained in Examples 1 to 4 are shown in Table 1.
表1实施例1~实施例4所得树脂吸液倍率和吸液速率测试结果Table 1 embodiment 1~embodiment 4 gained resin liquid absorption rate and liquid absorption rate test result
从表1可知,实施例1~实施例4中,随着水相单体丙烯酰胺加量的增加,遇水遇油双吸树脂中的吸水组分增加,因此使树脂的吸水倍率增加、吸油倍率减少,为了达到树脂的吸水倍率和吸油倍率均在5~6倍,优选丙烯酰胺加量为蒸馏水质量的12.5%~28.6%;此外,树脂的吸水速率和吸油速率均随丙烯酰胺加量的增加而降低,这是由于在丙烯酰胺加量较少时,树脂内部会形成多孔结构,增加了液体和树脂的接触面积和液体在树脂内部的传输速率,但是这种多孔结构会随着丙烯酰胺加量的增加而减少,因此丙烯酰胺加量增加会降低树脂的吸液速率,为了达到树脂快速吸液的目的,使树脂的吸液速率达到95%以上,优选丙烯酰胺加量为蒸馏水质量的12.5%~20%。综合以上所述,优选丙烯酰胺加量为蒸馏水质量的12.5%~20%。It can be seen from Table 1 that in Examples 1 to 4, as the amount of acrylamide added to the water phase monomer increases, the water-absorbing component in the water-meets-oil double-absorbent resin increases, thus increasing the water-absorbing ratio of the resin and increasing the oil-absorbing ratio. The ratio is reduced. In order to achieve the water absorption ratio and oil absorption ratio of the resin at 5 to 6 times, it is preferred that the amount of acrylamide added is 12.5% to 28.6% of the quality of distilled water; This is because when the amount of acrylamide is less, a porous structure will be formed inside the resin, increasing the contact area between the liquid and the resin and the transmission rate of the liquid inside the resin, but this porous structure will increase with the acrylamide The increase of the amount of acrylamide decreases, so the increase of the amount of acrylamide will reduce the liquid absorption rate of the resin. In order to achieve the purpose of rapid liquid absorption of the resin, the liquid absorption rate of the resin should reach more than 95%. The preferred amount of acrylamide is distilled water. 12.5% to 20%. Based on the above, the preferred amount of acrylamide added is 12.5% to 20% of the mass of distilled water.
实施例7、实施例1、实施例5、实施例6所得遇水遇油双吸树脂的吸液倍率和吸液速率如表2所示。The liquid absorption ratio and liquid absorption rate of the obtained water and oil double-absorbent resins obtained in Example 7, Example 1, Example 5, and Example 6 are shown in Table 2.
表2实施例7、实施例1、实施例5、实施例6所得树脂吸液倍率和吸液速率测试结果Table 2 embodiment 7, embodiment 1, embodiment 5, embodiment 6 gained resin liquid absorption rate and liquid absorption rate test result
从表2可知,从实施例7、实施例1、实施例5到实施例6中,油相单体甲基丙烯酸甲酯和甲基丙烯酸十二酯的质量比逐渐降低,遇水遇油双吸树脂的吸油倍率先增加后降低。这是由于甲基丙烯酸十二酯属于长链软组分单体,其加量增加可以增加树脂的吸油倍率,但是加量过大时,树脂较软,不利于树脂吸油,优选甲基丙烯酸甲酯和甲基丙烯酸十二酯的质量比为(20~100):100。As can be seen from Table 2, from Example 7, Example 1, Example 5 to Example 6, the mass ratio of the oil phase monomer methyl methacrylate and lauryl methacrylate gradually decreases, and when water meets oil, the mass ratio decreases gradually. The oil absorption times of the absorbent resin first increased and then decreased. This is because lauryl methacrylate is a long-chain soft component monomer, and its addition can increase the oil absorption ratio of the resin, but when the addition is too large, the resin is soft, which is not conducive to the oil absorption of the resin. Methyl methacrylate is preferred. The mass ratio of ester to lauryl methacrylate is (20-100):100.
实施例8、实施例9所得遇水遇油双吸树脂的吸液倍率和吸液速率如表3所示。Table 3 shows the liquid absorption ratio and liquid absorption rate of the water and oil double-absorbent resin obtained in Example 8 and Example 9.
表3实施例8、实施例9所得树脂吸液倍率和吸液速率测试结果Table 3 embodiment 8, embodiment 9 gained resin liquid absorption rate and liquid absorption rate test result
图1为实施例2和实施例9所得遇水遇油双吸树脂的照片图,从A中可以看出由实施例2所得的遇水遇油树脂为白色块状固体,从B中可以看出由实施例9所得的遇水遇油树脂为无色透明块状固体。两个实施例的制备过程均稳定,未发生分层现象。Fig. 1 is the photogram of embodiment 2 and embodiment 9 met water encounter oil double absorption resin, can find out from A that the water encounter oil resin obtained by embodiment 2 is a white massive solid, can see from B The water-meets-oleoresin obtained in Example 9 is a colorless transparent massive solid. The preparation processes of the two examples were stable without delamination.
图2所示为实施例2和实施例4所得遇水遇油双吸树脂的扫描电镜图,从图中可以看出,在微观下,由双连续微乳液方法制备的遇水遇油双吸树脂中仅较少颗粒状物质生成,而中国专利CN102850483A中制备的吸水吸油双功能树脂的扫描电镜图中吸水膨胀组分均是颗粒状并且以非连续形式分散在吸油膨胀组分中,本专利制备的遇水遇油双吸树脂具有遇水膨胀组分和遇油膨胀组分都是连续的结构;此外,在丙烯酰胺加量较少时,树脂内部形成的微孔较多,而丙烯酰胺加量较多时,树脂内部形成的微孔较少,因此优选丙烯酰胺加量为蒸馏水质量的12.5%~20%,有利于增加树脂内部微孔数量,增加树脂吸液速率。Fig. 2 shows the scanning electron micrographs of the obtained water-meets-oil double-absorbent resins obtained in Example 2 and Example 4. As can be seen from the figure, microscopically, the water-meets-oil double-absorbents prepared by the double continuous microemulsion method Only less granular substances are produced in the resin, while the water-absorbing and swelling components of the water-absorbing and oil-absorbing dual-functional resin prepared in the Chinese patent CN102850483A are all granular and dispersed in the oil-absorbing and swelling components in a discontinuous form. The prepared double-absorbent resin with water and oil has a continuous structure of water-swellable components and oil-swellable components; in addition, when the amount of acrylamide is small, more micropores are formed inside the resin, while acrylamide When the amount added is large, the micropores formed inside the resin are less, so the preferred amount of acrylamide added is 12.5% to 20% of the mass of distilled water, which is beneficial to increase the number of micropores inside the resin and increase the liquid absorption rate of the resin.
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