CN106634902B - The molten hydraulic cementing materials of high temperature resistant theobromine and be used for oil-well cement slurry system - Google Patents
The molten hydraulic cementing materials of high temperature resistant theobromine and be used for oil-well cement slurry system Download PDFInfo
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- 239000004568 cement Substances 0.000 title claims abstract description 48
- 239000000463 material Substances 0.000 title claims abstract description 45
- 239000002002 slurry Substances 0.000 title claims abstract description 34
- 239000003129 oil well Substances 0.000 title claims abstract description 30
- YAPQBXQYLJRXSA-UHFFFAOYSA-N theobromine Chemical compound CN1C(=O)NC(=O)C2=C1N=CN2C YAPQBXQYLJRXSA-UHFFFAOYSA-N 0.000 title claims abstract 6
- 229960004559 theobromine Drugs 0.000 title claims abstract 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000004927 clay Substances 0.000 claims abstract description 9
- 239000006028 limestone Substances 0.000 claims abstract description 9
- 239000011863 silicon-based powder Substances 0.000 claims abstract description 9
- 229910052742 iron Inorganic materials 0.000 claims abstract description 5
- 239000002245 particle Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910052791 calcium Inorganic materials 0.000 claims 1
- 239000011575 calcium Substances 0.000 claims 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 11
- 229910000019 calcium carbonate Inorganic materials 0.000 abstract description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 8
- 235000019738 Limestone Nutrition 0.000 abstract description 8
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 abstract description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 7
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 abstract description 7
- 239000010440 gypsum Substances 0.000 abstract description 7
- 229910052602 gypsum Inorganic materials 0.000 abstract description 7
- 239000004816 latex Substances 0.000 abstract description 7
- 229920000126 latex Polymers 0.000 abstract description 7
- 229920001467 poly(styrenesulfonates) Polymers 0.000 abstract description 7
- 239000003921 oil Substances 0.000 abstract description 6
- 239000000725 suspension Substances 0.000 abstract description 4
- 238000004062 sedimentation Methods 0.000 abstract description 2
- 229920006243 acrylic copolymer Polymers 0.000 abstract 1
- 229940008099 dimethicone Drugs 0.000 abstract 1
- 239000004205 dimethyl polysiloxane Substances 0.000 abstract 1
- 235000013870 dimethyl polysiloxane Nutrition 0.000 abstract 1
- 239000008187 granular material Substances 0.000 abstract 1
- 229940059939 kayexalate Drugs 0.000 abstract 1
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 20
- 239000002253 acid Substances 0.000 description 15
- 238000001354 calcination Methods 0.000 description 13
- DZSVIVLGBJKQAP-UHFFFAOYSA-N 1-(2-methyl-5-propan-2-ylcyclohex-2-en-1-yl)propan-1-one Chemical compound CCC(=O)C1CC(C(C)C)CC=C1C DZSVIVLGBJKQAP-UHFFFAOYSA-N 0.000 description 12
- IRLPACMLTUPBCL-KQYNXXCUSA-N 5'-adenylyl sulfate Chemical compound C1=NC=2C(N)=NC=NC=2N1[C@@H]1O[C@H](COP(O)(=O)OS(O)(=O)=O)[C@@H](O)[C@H]1O IRLPACMLTUPBCL-KQYNXXCUSA-N 0.000 description 12
- 239000007864 aqueous solution Substances 0.000 description 12
- 238000012360 testing method Methods 0.000 description 10
- 235000010216 calcium carbonate Nutrition 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 229910052595 hematite Inorganic materials 0.000 description 7
- 239000011019 hematite Substances 0.000 description 7
- 229920002126 Acrylic acid copolymer Polymers 0.000 description 6
- 239000005909 Kieselgur Substances 0.000 description 6
- 239000002174 Styrene-butadiene Substances 0.000 description 6
- PASHVRUKOFIRIK-UHFFFAOYSA-L calcium sulfate dihydrate Chemical compound O.O.[Ca+2].[O-]S([O-])(=O)=O PASHVRUKOFIRIK-UHFFFAOYSA-L 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 238000002156 mixing Methods 0.000 description 6
- 229940006186 sodium polystyrene sulfonate Drugs 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 239000011115 styrene butadiene Substances 0.000 description 6
- 229920003048 styrene butadiene rubber Polymers 0.000 description 6
- 238000011161 development Methods 0.000 description 5
- AMTWCFIAVKBGOD-UHFFFAOYSA-N dioxosilane;methoxy-dimethyl-trimethylsilyloxysilane Chemical compound O=[Si]=O.CO[Si](C)(C)O[Si](C)(C)C AMTWCFIAVKBGOD-UHFFFAOYSA-N 0.000 description 5
- 238000004090 dissolution Methods 0.000 description 5
- 238000000227 grinding Methods 0.000 description 5
- 229940083037 simethicone Drugs 0.000 description 5
- 230000008719 thickening Effects 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 4
- 238000011056 performance test Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- QKZIVVMOMKTVIK-UHFFFAOYSA-M anilinomethanesulfonate Chemical group [O-]S(=O)(=O)CNC1=CC=CC=C1 QKZIVVMOMKTVIK-UHFFFAOYSA-M 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000000395 magnesium oxide Substances 0.000 description 2
- 239000002195 soluble material Substances 0.000 description 2
- 239000004575 stone Substances 0.000 description 2
- 239000011398 Portland cement Substances 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005465 channeling Effects 0.000 description 1
- IQYKECCCHDLEPX-UHFFFAOYSA-N chloro hypochlorite;magnesium Chemical compound [Mg].ClOCl IQYKECCCHDLEPX-UHFFFAOYSA-N 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- OLZDXDPSDUSGIS-UHFFFAOYSA-N sulfinylmagnesium Chemical compound [Mg].S=O OLZDXDPSDUSGIS-UHFFFAOYSA-N 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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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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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
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- C04B28/00—Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
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- C—CHEMISTRY; METALLURGY
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- C04B7/00—Hydraulic cements
- C04B7/22—Iron ore cements ; Iron rich cements, e.g. Ferrari cements, Kühl cements
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- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
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- C09K8/42—Compositions for cementing, e.g. for cementing casings into boreholes; Compositions for plugging, e.g. for killing wells
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Abstract
Description
技术领域technical field
本发明涉及水硬性胶凝材料领域,特别涉及一种耐高温可酸溶的水硬性胶凝材料及其在油井水泥浆体系中的应用。The invention relates to the field of hydraulic cementitious materials, in particular to a high-temperature-resistant and acid-soluble hydraulic cementitious material and its application in oil well cement slurry systems.
背景技术Background technique
目前,水硬性酸溶胶凝材料的研究与应用以酸溶水泥为主,酸溶水泥最初用于解决油气井储层段的循环漏失问题。通过水泥胶凝硬化作用,在漏失处形成一定强度的桥联堵塞效果,以此封堵天然、次生裂缝以及发生窜流的通道;又因其可观的酸溶特性,在酸压作业后,结构体可在作业时间内逐渐消融分解,能够大幅降低水泥浆对储层的伤害。At present, the research and application of hydraulic acid soluble gelling materials are mainly based on acid soluble cement, which was initially used to solve the problem of circulation loss in the reservoir section of oil and gas wells. Through the gelation and hardening of cement, a certain strength of bridging plugging effect is formed at the leakage site, so as to block the natural and secondary cracks and the channels where channeling occurs; and because of its considerable acid-soluble characteristics, after acid fracturing operations, The structure can be gradually ablated and decomposed within the operation time, which can greatly reduce the damage of cement slurry to the reservoir.
在固井施工后,侵入储层的硬化水泥残渣,加重了体积压裂的难度,进而影响体积压裂效果与气井最终采收率,而使用酸溶水泥固井可有效解除储层的污染。随着人们储层保护意识的增强,经多年发展研究,酸溶水泥在非常规气藏水平段固井中已成功应用,如美国的Barnett页岩气田使用酸溶水泥浆固井,体积压裂后,投产效果良好。After cementing, the hardened cement residue that invades the reservoir increases the difficulty of volume fracturing, which in turn affects the effect of volume fracturing and the ultimate recovery of gas wells. The use of acid-soluble cement for well cementing can effectively decontaminate the reservoir. With the enhancement of people's awareness of reservoir protection, after years of development and research, acid-soluble cement has been successfully applied in the cementing of the horizontal section of unconventional gas reservoirs. For example, the Barnett shale gas field in the United States uses acid-soluble cement to , and the production effect is good.
目前酸溶性胶凝材料主要分为以下三类:(1)镁氧水泥,广泛应用于完井与修井作业(李早元,靳东旭,周超,等.镁氧水泥用于油井堵漏及暂闭的室内研究[J].西南石油大学学报(自然科学版),2011,33(5):152-156),氯氧镁水泥虽表现出优异的可酸溶特性,但抗温能力差,在井下高温水湿环境中,水泥石内部的晶型将随时间逐渐发生不利于强度发展的不可逆转变;硫氧镁水泥虽缓解了强度衰退的趋势,但其整体强度依然表现不佳。(2)G级水泥中掺入少量碳酸钙的硅酸盐水泥浆体系,该体系在各油田虽有不少现场应用案例,但其高温沉降稳定性较差,水泥石强度偏低,酸溶率不理想,技术尚不成熟。(3)酸溶性固化剂,由于相应配套处理剂种类复杂,成本较高,使其在油气田开发中至今难以推广。At present, acid-soluble cementitious materials are mainly divided into the following three categories: (1) Magnesia cement, which is widely used in well completion and workover operations (Li Zaoyuan, Jin Dongxu, Zhou Chao, etc. Magnesia cement is used for oil well plugging and temporary closure Indoor research on [J]. Southwest Petroleum University Journal (Natural Science Edition), 2011,33(5):152-156), although magnesium oxychloride cement exhibits excellent acid-soluble properties, but poor temperature resistance, in In the underground high temperature and water humidity environment, the crystal form inside the cement stone will gradually undergo irreversible changes that are not conducive to the strength development over time; although the magnesium oxysulfide cement has alleviated the trend of strength decline, its overall strength is still not good. (2) Portland cement slurry system with a small amount of calcium carbonate added to grade G cement. Although this system has many field application cases in various oil fields, its high-temperature settlement stability is poor, and the strength of cement stone is low. The rate is not ideal, and the technology is not yet mature. (3) Acid-soluble curing agent, due to the complex types of corresponding supporting treatment agents and high cost, it is difficult to popularize it in the development of oil and gas fields.
发明内容Contents of the invention
本发明的目的在于提供一种耐高温可酸溶的水硬性胶凝材料,通过该材料中颗粒的合理级配设计,在保证酸溶解除效果的前提下,赋予胶凝材料的硬化体更加稳定的高温强度发育,弥补现有胶凝材料抗温性差、水湿环境中强度衰退等不足。The purpose of the present invention is to provide a high-temperature resistant and acid-soluble hydraulic gelling material. Through the reasonable gradation design of the particles in the material, the hardened body of the gelling material is more stable under the premise of ensuring the effect of acid dissolution. The development of high-temperature strength can make up for the shortcomings of existing cementitious materials such as poor temperature resistance and strength decline in water-humid environments.
本发明的另一目的还在于提供上述耐高温可酸溶的水硬性胶凝材料在油井水泥浆体系中的应用。由水硬性胶凝材料配制的油井水泥浆体系,工艺便捷,成本低廉,性能优异,通过材料颗粒自身的物理悬浮能力,在井下80℃~130℃的高温环境中,保持良好的沉降稳定性,突破了现有酸溶性胶凝材料的浆体高温沉降稳定性差的局限。该项发明有望应用于油气井储层暂闭、堵水、非常规气藏固井等领域。Another object of the present invention is to provide the application of the above-mentioned high-temperature resistant and acid-soluble hydraulic cementitious material in oil well cement slurry system. The oil well cement slurry system prepared by hydraulic cementitious materials has convenient process, low cost and excellent performance. Through the physical suspension ability of material particles, it can maintain good settlement stability in the high temperature environment of 80℃~130℃ underground. The invention breaks through the limitation of poor high-temperature sedimentation stability of the slurry of the existing acid-soluble gelling material. The invention is expected to be applied to fields such as temporary closure of oil and gas well reservoirs, water shutoff, unconventional gas reservoir cementing and the like.
为达到以上技术目的,本发明提供以下技术方案。In order to achieve the above technical objectives, the present invention provides the following technical solutions.
耐高温可酸溶的水硬性胶凝材料,由以下各组分按重量份组成:A high-temperature-resistant and acid-soluble hydraulic gelling material consists of the following components by weight:
所述耐高温可酸溶的水硬性胶凝材料的制备过程如下:The preparation process of the high-temperature resistant and acid-soluble hydraulic gelling material is as follows:
采用干法生产,将100份石灰石、10~15份黏土、2~4份赤铁矿、1~3份硅藻土、0.1~2份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1小时,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至50~80℃,冷却速率18~20℃/min,再加入1~2份石膏、30~35份硅粉、0~50份铁矿粉、30~45份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。Produced by dry method, crush 100 parts of limestone, 10-15 parts of clay, 2-4 parts of hematite, 1-3 parts of diatomaceous earth, and 0.1-2 parts of phosphogypsum with a crusher until the particle size is less than 25mm. , after mixing, send it to the rotary kiln for calcination for 1 hour, the calcination temperature is 1350-1450°C, enter the cooling machine for cooling, rapidly cool to 50-80°C, and the cooling rate is 18-20°C/min, then add 1-2 parts of gypsum, 30- 35 parts of silicon powder, 0-50 parts of iron ore powder, and 30-45 parts of calcium carbonate are mixed and ground, so that the particle size of the product is controlled at 1-100 μm, and a high-temperature-resistant and acid-soluble hydraulic gelling material is obtained.
所述石灰石中CaCO3的纯度至少为65%。 The purity of CaCO3 in said limestone is at least 65%.
所述黏土中SiO2的含量不低于60%,同时煅烧前应经过严格烘干,使其含水量少于1%。The content of SiO 2 in the clay is not less than 60%, and it should be strictly dried before calcination to make the water content less than 1%.
所述赤铁矿中Fe2O3的含量为50%~70%。 The content of Fe2O3 in the hematite is 50%-70%.
所述硅粉是约为400目(38μm)的颗粒。The silicon powder is about 400 mesh (38 μm) particles.
所述碳酸钙是两种约为1500目(7μm)与10000目(1.3μm)的不同粒径混合物,以形成更佳的级配效果。The calcium carbonate is a mixture of two different particle sizes of about 1500 mesh (7 μm) and 10000 mesh (1.3 μm) to form a better gradation effect.
上述的几种原料均可从市场采购。The above-mentioned several raw materials can be purchased from the market.
将所述耐高温可酸溶的水硬性胶凝材料用于油井水泥浆体系,所述油井水泥浆体系由以下各组分按重量份组成:The high-temperature-resistant and acid-soluble hydraulic cementitious material is used in an oil well cement slurry system, and the oil well cement slurry system is composed of the following components by weight:
所述油井水泥浆体系的制备过程如下:The preparation process of the oil well cement slurry system is as follows:
称取0~1.5份聚苯乙烯磺酸钠、3~6份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.5~0.8份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1~1.5份丁苯乳胶、0.01~0.5份二甲基硅油,溶解在35~50份水中,配制水溶液,将水溶液放置在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得本发明配制的耐高温可酸溶的油井水泥浆体系。Weigh 0-1.5 parts of sodium polystyrene sulfonate, 3-6 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.5-0.8 parts of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1-1.5 parts of styrene-butadiene latex, 0.01-0.5 parts of dimethyl silicone oil, dissolved in 35-50 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, and the stirrer at a low speed (4000±200 rpm /min) rotation, and add 100 parts of hydraulic cementitious materials in 15 seconds, then continue to stir for 35 seconds under high-speed (12000 ± 500 rpm) rotation, to obtain the high temperature resistant acid-soluble oil well prepared by the present invention cement slurry system.
本发明提供了一种耐高温可酸溶的水硬性胶凝材料,并配制出能够用于非常规气藏固井、储层暂闭等领域的油井水泥浆体系。通过颗粒合理的级配,实现了浆体良好的物理悬浮作用,使体系突破性地适应了80℃~130℃的高温环境,无需外加剂的额外调节;更为密实的堆积程度,赋予了水硬性胶凝材料的硬化体更加稳定的高温强度发育;加入不同粒径的酸溶性材料,增大了硬化体的酸溶反应速率,保证了其可观的解除(酸压作业)效果。本发明弥补了现有酸溶性胶凝材料的抗温性差、沉降稳定性不佳、水湿环境中强度衰退等不足。The invention provides a high-temperature-resistant and acid-soluble hydraulic gelling material, and prepares an oil well cement slurry system that can be used in the fields of unconventional gas reservoir cementing, reservoir temporary closure, and the like. Through the reasonable gradation of the particles, good physical suspension of the slurry is achieved, making the system adapt to the high temperature environment of 80 ℃ ~ 130 ℃ in a breakthrough, without additional adjustment of admixtures; the denser accumulation degree gives water The hardened body of the hard gelling material develops more stable high-temperature strength; adding acid-soluble materials with different particle sizes increases the acid-soluble reaction rate of the hardened body, ensuring its considerable release (acid fracturing) effect. The invention makes up for the deficiencies of the existing acid-soluble gelling materials, such as poor temperature resistance, poor settlement stability, and strength decline in a water-humid environment.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)该胶凝材料耐高温性能优良,灰样基于合理的级配设计,依托颗粒自身的物理作用实现了良好的悬浮。现有酸溶胶凝体系很难适应80℃以上的温度环境,而本发明胶凝材料能在80℃~130℃的井下温度环境中保持较好的稳定性,无需特殊的外加剂调节,失水量低,工程应用性能均可调节。(1) The gelling material has excellent high temperature resistance, and the gray sample is based on a reasonable gradation design, relying on the physical function of the particles themselves to achieve good suspension. The existing acid-sol gelling system is difficult to adapt to the temperature environment above 80°C, but the gelling material of the present invention can maintain good stability in the downhole temperature environment of 80°C-130°C, without special admixture adjustment, and the water loss Low, engineering application performance can be adjusted.
(2)该胶凝体系是水硬性材料,井下水湿环境中的长期稳定性较好,无强度衰退现象。(2) The gelling system is a hydraulic material, and has good long-term stability in the underground water-humid environment without strength decline.
(3)选用不同粒径的酸溶材料,既增大了硬化体的酸溶反应速率,又改善了硬化体的密实程度,有利于其强度的稳定发育。(3) The selection of acid-soluble materials with different particle sizes not only increases the acid-soluble reaction rate of the hardened body, but also improves the compactness of the hardened body, which is conducive to the stable development of its strength.
(4)该胶凝材料配制而成的油井水泥浆体系应用前景广泛,成本低廉,工艺便捷,可应用于非常规油气藏固井、储层暂闭等领域。(4) The oil well cement slurry system prepared by the cementitious material has broad application prospects, low cost and convenient process, and can be applied to unconventional oil and gas reservoir cementing, reservoir temporary closure and other fields.
附图说明Description of drawings
图1是实施例3合成产物的稠化曲线(实验温度130℃、压力70MPa)。Fig. 1 is the thickening curve (experimental temperature 130 ℃, pressure 70MPa) of the synthetic product of embodiment 3.
图2为G级水泥净浆和实施例3的硬化体的实时酸溶率测试结果。Fig. 2 is the test result of the real-time acid solubility rate of G grade cement paste and the hardened body of Example 3.
具体实施方案specific implementation plan
下面通过实施例和附图对本发明做进一步说明。The present invention will be further described below through embodiment and accompanying drawing.
一、耐高温可酸溶的水硬性胶凝材料及油井水泥浆体系的制备(以下各组分均为重量份)One, the preparation of high temperature resistant and acid-soluble hydraulic cementitious material and oil well cement slurry system (the following components are parts by weight)
实施例1Example 1
采用干法生产,将100份石灰石、15份粘土、3份赤铁矿、3份硅藻土、1份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1h,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至65℃,冷却速率18~20℃/min,再加入2份石膏、30份硅粉、35份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。It is produced by dry method. 100 parts of limestone, 15 parts of clay, 3 parts of hematite, 3 parts of diatomaceous earth and 1 part of phosphogypsum are crushed by a crusher to a block with a particle size of less than 25mm, mixed and sent to a rotary kiln for calcination 1h, the calcination temperature is 1350-1450°C, enter the cooling machine for cooling, rapidly cool to 65°C, and the cooling rate is 18-20°C/min, then add 2 parts of gypsum, 30 parts of silicon powder, and 35 parts of calcium carbonate for mixing and grinding. The particle size of the product is controlled at 1-100 μm to obtain a high-temperature-resistant and acid-soluble hydraulic gelling material.
称取1份聚苯乙烯磺酸钠、3份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.5份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1.5份丁苯乳胶、0.01份二甲基硅油,溶解在37份水中,配制水溶液,将水溶液放在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得耐高温可酸溶的油井水泥浆体系。Weigh 1 part of sodium polystyrene sulfonate, 3 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.5 part of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1.5 parts Dissolve styrene-butadiene latex and 0.01 part of simethicone in 37 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, turn the stirrer at a low speed (4000±200 rpm), and add it within 15 seconds 100 parts of hydraulic cementitious material, and then continue stirring for 35 seconds under high-speed (12000±500 rpm) rotation to obtain a high-temperature-resistant and acid-soluble oil well cement slurry system.
实施例2Example 2
采用干法生产,将100份石灰石、15份粘土、2份赤铁矿、3份硅藻土、1份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1h,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至68℃,冷却速率18~20℃/min,再加入2份石膏、30份硅粉、40份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。It is produced by dry method, crushing 100 parts of limestone, 15 parts of clay, 2 parts of hematite, 3 parts of diatomaceous earth, and 1 part of phosphogypsum into lumps with a particle size of less than 25mm, mixed and sent to the rotary kiln for calcination 1h, the calcination temperature is 1350-1450°C, enter the cooling machine for cooling, rapidly cool to 68°C, and the cooling rate is 18-20°C/min, then add 2 parts of gypsum, 30 parts of silicon powder, and 40 parts of calcium carbonate for mixing and grinding. The particle size of the product is controlled at 1-100 μm to obtain a high-temperature-resistant and acid-soluble hydraulic gelling material.
称取1份聚苯乙烯磺酸钠、3.5份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.5份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1.5份丁苯乳胶、0.05份二甲基硅油,溶解在50份水中,配制水溶液,将水溶液放在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得耐高温可酸溶的油井水泥浆体系。Weigh 1 part of sodium polystyrene sulfonate, 3.5 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.5 part of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1.5 parts Dissolve styrene-butadiene latex and 0.05 parts of simethicone in 50 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, turn the stirrer at a low speed (4000±200 rpm), and add it within 15 seconds 100 parts of hydraulic cementitious material, and then continue stirring for 35 seconds under high-speed (12000±500 rpm) rotation to obtain a high-temperature-resistant and acid-soluble oil well cement slurry system.
实施例3Example 3
采用干法生产,将100份石灰石、15份粘土、4份赤铁矿、3份硅藻土、1.5份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1h,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至60℃,冷却速率18~20℃/min,再加入2份石膏、30份硅粉、35份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。Produced by dry method, crush 100 parts of limestone, 15 parts of clay, 4 parts of hematite, 3 parts of diatomaceous earth, and 1.5 parts of phosphogypsum into lumps with a particle size of less than 25mm, mix them and send them to the rotary kiln for calcination 1h, the calcination temperature is 1350-1450°C, enter the cooling machine for cooling, rapidly cool to 60°C, and the cooling rate is 18-20°C/min, then add 2 parts of gypsum, 30 parts of silicon powder, and 35 parts of calcium carbonate for mixing and grinding. The particle size of the product is controlled at 1-100 μm to obtain a high-temperature-resistant and acid-soluble hydraulic gelling material.
称取1份聚苯乙烯磺酸钠、3份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.6份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1.5份丁苯乳胶、0.01份二甲基硅油,溶解在37份水中,配制水溶液,将水溶液放在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得耐高温可酸溶的油井水泥浆体系。Weigh 1 part of sodium polystyrene sulfonate, 3 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.6 part of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1.5 parts Dissolve styrene-butadiene latex and 0.01 part of simethicone in 37 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, turn the stirrer at a low speed (4000±200 rpm), and add it within 15 seconds 100 parts of hydraulic cementitious material, and then continue stirring for 35 seconds under high-speed (12000±500 rpm) rotation to obtain a high-temperature-resistant and acid-soluble oil well cement slurry system.
实施例4Example 4
采用干法生产,将100份石灰石、15份粘土、4份赤铁矿、3份硅藻土、1.5份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1h,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至60℃,冷却速率18~20℃/min,再加入1份石膏、35份硅粉、30份铁矿粉、30份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。Produced by dry method, crush 100 parts of limestone, 15 parts of clay, 4 parts of hematite, 3 parts of diatomaceous earth, and 1.5 parts of phosphogypsum into lumps with a particle size of less than 25mm, mix them and send them to the rotary kiln for calcination 1h, calcination temperature 1350~1450℃, enter into the cooling machine for cooling, rapid cooling to 60℃, cooling rate 18~20℃/min, then add 1 part of gypsum, 35 parts of silicon powder, 30 parts of iron ore powder, 30 parts of calcium carbonate Grinding is carried out after mixing, so that the particle size of the product is controlled at 1-100 μm, and a high-temperature-resistant and acid-soluble hydraulic gelling material is obtained.
称取1份聚苯乙烯磺酸钠、5份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.7份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1.5份丁苯乳胶、0.5份二甲基硅油,溶解在44份水中,配制水溶液,将水溶液放在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得耐高温可酸溶的油井水泥浆体系。Weigh 1 part of sodium polystyrene sulfonate, 5 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.7 part of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1.5 parts Dissolve styrene-butadiene latex and 0.5 parts of simethicone in 44 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, turn the stirrer at a low speed (4000±200 rpm), and add it within 15 seconds 100 parts of hydraulic cementitious material, and then continue stirring for 35 seconds under high-speed (12000±500 rpm) rotation to obtain a high-temperature-resistant and acid-soluble oil well cement slurry system.
实施例5Example 5
采用干法生产,将100份石灰石、15份粘土、3份赤铁矿、3份硅藻土、1.5份磷石膏用破碎机破碎至粒径小于25mm的块料,混合后送入回转窑煅烧1h,煅烧温度1350~1450℃,进入冷却机进行冷却,急冷至62℃,冷却速率18~20℃/min,再加入1份石膏、35份硅粉、50份铁矿粉、30份碳酸钙进行混合后粉磨,使产物的粒度控制在1~100μm,即得耐高温可酸溶的水硬性胶凝材料。It is produced by dry method, crushing 100 parts of limestone, 15 parts of clay, 3 parts of hematite, 3 parts of diatomaceous earth, and 1.5 parts of phosphogypsum into lumps with a particle size of less than 25mm, mixed and sent to the rotary kiln for calcination 1h, calcination temperature 1350~1450℃, enter into the cooling machine for cooling, rapid cooling to 62℃, cooling rate 18~20℃/min, then add 1 part of gypsum, 35 parts of silicon powder, 50 parts of iron ore powder, 30 parts of calcium carbonate Grinding is carried out after mixing, so that the particle size of the product is controlled at 1-100 μm, and a high-temperature-resistant and acid-soluble hydraulic gelling material is obtained.
称取1.5份聚苯乙烯磺酸钠、6份2-丙烯酰胺-2-甲基丙磺酸AMPS、0.8份2-丙烯酰胺-2-甲基丙磺酸丙烯酸共聚物AA/AMPS、1.5份丁苯乳胶、0.5份二甲基硅油,溶解在48份水中,配制水溶液,将水溶液放在高速搅拌器中,搅拌器以低速(4000±200转/分)转动,并在15秒内加完100份水硬性胶凝材料,随后高速(12000±500转/分)转动下继续搅拌35秒,即得耐高温可酸溶的油井水泥浆体系。Weigh 1.5 parts of sodium polystyrene sulfonate, 6 parts of 2-acrylamide-2-methylpropanesulfonic acid AMPS, 0.8 parts of 2-acrylamide-2-methylpropanesulfonic acid acrylic acid copolymer AA/AMPS, 1.5 parts Dissolve styrene-butadiene latex and 0.5 parts of simethicone in 48 parts of water to prepare an aqueous solution, put the aqueous solution in a high-speed stirrer, turn the stirrer at a low speed (4000±200 rpm), and add it within 15 seconds 100 parts of hydraulic cementitious material, and then continue stirring for 35 seconds under high-speed (12000±500 rpm) rotation to obtain a high-temperature-resistant and acid-soluble oil well cement slurry system.
二、耐高温可酸溶的水硬性胶凝材料所配制的油井水泥浆体系的性能测试2. Performance test of oil well cement slurry system prepared by high temperature resistant and acid soluble hydraulic cementitious material
1、油井水泥浆应用性能测试1. Application performance test of oil well cement slurry
按照油井水泥标准GB/T19139-2012《油井水泥试验方法》,对耐高温水硬性可酸溶的胶凝体系进行应用性能测试,测试结果见表1。According to the oil well cement standard GB/T19139-2012 "Oil well cement test method", the application performance test of the high temperature resistant hydraulic acid soluble gelling system is carried out. The test results are shown in Table 1.
表1油井水泥浆应用性能测试结果Table 1 Test results of application performance of oil well cement slurry
由性能测试结果可以看出,浆体密度于1.60~2.20g/cm3可调,失水量表现较低,高温沉降稳定性良好,流动度适中,且稠化时间线性可调节,基本满足现场施工要求。It can be seen from the performance test results that the slurry density is adjustable from 1.60 to 2.20g/cm 3 , the water loss performance is low, the high temperature settlement stability is good, the fluidity is moderate, and the thickening time is linearly adjustable, which basically meets the needs of on-site construction. Require.
图1为实施例3的稠化实验结果,实验条件为130℃、50MPa。实验结果:稠化时间为272min,过渡时间为5min,接近直角稠化,浆体性能良好,达到预期效果,满足工程应用。Figure 1 shows the results of the thickening experiment of Example 3, and the experimental conditions are 130°C and 50MPa. Experimental results: The thickening time is 272 minutes, the transition time is 5 minutes, close to right-angle thickening, the slurry performance is good, the expected effect is achieved, and the engineering application is satisfied.
2、硬化体的抗压强度测试2. Compressive strength test of hardened body
表2为实施例在130℃,20MPa水浴养护条件下的抗压强度测试结果。Table 2 shows the compressive strength test results of the examples under the conditions of 130°C and 20MPa water bath curing.
表2硬化体的抗压强度测试结果The compressive strength test result of table 2 hardened body
本发明配制的油井水泥浆的硬化体在130℃高温下的抗压强度依然稳定,60d养护后无强度衰退显现,强度整体表现稳定;相比之下,G级水泥净浆所养护的硬化体,在养护3d后,出现了较为明显的强度衰退,硬化体已逐渐丧失结构强度。The compressive strength of the hardened body of the oil well cement slurry prepared by the present invention is still stable at a high temperature of 130°C, no strength decline appears after 60 days of curing, and the overall strength performance is stable; in contrast, the hardened body cured by G-grade cement paste , after 3 days of curing, there is a more obvious strength decline, and the hardened body has gradually lost its structural strength.
3、硬化体的酸溶率测试3. Acid solubility test of hardened body
(1)利用剩余质量法,将硬化体浸泡于10%盐酸中2h,测试其2h内的酸溶率。(1) Using the residual mass method, soak the hardened body in 10% hydrochloric acid for 2 hours, and test its acid solubility within 2 hours.
表3为130℃养护龄期为3d的硬化体置于10%足量盐酸中的2h酸溶实验结果。Table 3 shows the results of the 2h acid dissolution experiment of the hardened body with a curing age of 3d at 130°C in 10% sufficient hydrochloric acid.
表3硬化体的酸溶率测试结果Table 3 Acid solubility test results of hardened body
由酸溶实验发现:本发明的硬化体2h的酸溶率最高可达84.7%,其中高密度体系受加重剂的影响,酸溶率表现稍低;相比之下,G级水泥净浆的硬化体酸溶率仅为50.5%,由此可见,本发明的胶凝材料所配置的油井水泥浆养护形成的硬化体,具有较为优异的可酸溶特性。It is found by the acid dissolution experiment that the acid solubility rate of the hardened body of the present invention can reach up to 84.7% in 2 hours, wherein the high density system is affected by the weighting agent, and the acid solubility rate performance is slightly lower; in contrast, the G grade cement slurry The acid-soluble rate of the hardened body is only 50.5%, so it can be seen that the hardened body formed by curing the oil well cement slurry with the cementitious material of the present invention has relatively excellent acid-soluble properties.
(2)选取20min、40min、60min、80min、100min、120min这6个时间点,对G级水泥净浆的硬化体和本发明的硬化体(实施例3)进行实时酸溶率测试,实验结果见图2。(2) Choose these 6 time points of 20min, 40min, 60min, 80min, 100min, 120min, carry out the real-time acid-soluble rate test to the hardened body of G grade cement paste and the hardened body (embodiment 3) of the present invention, experimental result See Figure 2.
结果表明,G级水泥净浆硬化体的反应速率始终较为缓慢,2h的最终酸溶率仅为50.5%;而实施例3的硬化体在20~60min反应速率急剧加快,60~80min反应速率减缓,80~120min反应逐渐停止,2h的最终酸溶率为84.7%,在保证封堵质量的同时,大幅改善了酸溶效果。The results show that the reaction rate of the hardened body of G-grade cement paste is always relatively slow, and the final acid-soluble rate is only 50.5% in 2 hours; while the reaction rate of the hardened body of Example 3 is accelerated sharply at 20-60 minutes, and the reaction rate is slowed down at 60-80 minutes , The reaction gradually stopped after 80-120 minutes, and the final acid-dissolution rate was 84.7% in 2 hours. While ensuring the plugging quality, the acid-dissolution effect was greatly improved.
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