CN105062437B - A kind of oil-in-water emulsified drilling fluid of anti-240 DEG C of high temperature - Google Patents
A kind of oil-in-water emulsified drilling fluid of anti-240 DEG C of high temperature Download PDFInfo
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- 238000005553 drilling Methods 0.000 title claims abstract description 60
- 239000012530 fluid Substances 0.000 title claims abstract description 47
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 36
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 22
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 21
- 238000002360 preparation method Methods 0.000 claims abstract description 15
- 239000003381 stabilizer Substances 0.000 claims abstract description 15
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 14
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 235000011121 sodium hydroxide Nutrition 0.000 claims abstract description 7
- 239000002562 thickening agent Substances 0.000 claims abstract 2
- 239000003921 oil Substances 0.000 claims description 28
- 150000002191 fatty alcohols Chemical class 0.000 claims description 20
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 20
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 20
- 238000002156 mixing Methods 0.000 claims description 18
- 229910052901 montmorillonite Inorganic materials 0.000 claims description 12
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 10
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 10
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 10
- 239000005642 Oleic acid Substances 0.000 claims description 10
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 10
- IPGANOYOHAODGA-UHFFFAOYSA-N dilithium;dimagnesium;dioxido(oxo)silane Chemical compound [Li+].[Li+].[Mg+2].[Mg+2].[O-][Si]([O-])=O.[O-][Si]([O-])=O.[O-][Si]([O-])=O IPGANOYOHAODGA-UHFFFAOYSA-N 0.000 claims description 10
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 10
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 10
- 235000013311 vegetables Nutrition 0.000 claims description 10
- QXNVGIXVLWOKEQ-UHFFFAOYSA-N Disodium Chemical compound [Na][Na] QXNVGIXVLWOKEQ-UHFFFAOYSA-N 0.000 claims description 9
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 9
- 239000011734 sodium Substances 0.000 claims description 9
- 229910052708 sodium Inorganic materials 0.000 claims description 9
- 239000007957 coemulsifier Substances 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 5
- 239000011575 calcium Substances 0.000 claims description 5
- 229910052791 calcium Inorganic materials 0.000 claims description 5
- OOCMUZJPDXYRFD-UHFFFAOYSA-L calcium;2-dodecylbenzenesulfonate Chemical compound [Ca+2].CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O.CCCCCCCCCCCCC1=CC=CC=C1S([O-])(=O)=O OOCMUZJPDXYRFD-UHFFFAOYSA-L 0.000 claims description 5
- YRIUSKIDOIARQF-UHFFFAOYSA-N dodecyl benzenesulfonate Chemical compound CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 YRIUSKIDOIARQF-UHFFFAOYSA-N 0.000 claims description 5
- 229940071161 dodecylbenzenesulfonate Drugs 0.000 claims description 5
- 238000009775 high-speed stirring Methods 0.000 claims description 5
- 239000005543 nano-size silicon particle Substances 0.000 claims description 5
- BTXXTMOWISPQSJ-UHFFFAOYSA-N 4,4,4-trifluorobutan-2-one Chemical compound CC(=O)CC(F)(F)F BTXXTMOWISPQSJ-UHFFFAOYSA-N 0.000 claims description 2
- BQACOLQNOUYJCE-FYZZASKESA-N Abietic acid Natural products CC(C)C1=CC2=CC[C@]3(C)[C@](C)(CCC[C@@]3(C)C(=O)O)[C@H]2CC1 BQACOLQNOUYJCE-FYZZASKESA-N 0.000 claims description 2
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L calcium carbonate Substances [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 2
- 230000018044 dehydration Effects 0.000 abstract description 2
- 238000006297 dehydration reaction Methods 0.000 abstract description 2
- 238000004945 emulsification Methods 0.000 abstract description 2
- 239000003208 petroleum Substances 0.000 abstract description 2
- 239000002199 base oil Substances 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 239000006260 foam Substances 0.000 description 12
- 239000004113 Sepiolite Substances 0.000 description 8
- 229960000892 attapulgite Drugs 0.000 description 8
- 239000004927 clay Substances 0.000 description 8
- 229910052625 palygorskite Inorganic materials 0.000 description 8
- 229920005989 resin Polymers 0.000 description 8
- 239000011347 resin Substances 0.000 description 8
- 229910052624 sepiolite Inorganic materials 0.000 description 8
- 235000019355 sepiolite Nutrition 0.000 description 8
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000005755 formation reaction Methods 0.000 description 5
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical class [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- AJLXXPFSLLWHKQ-UHFFFAOYSA-N formaldehyde (2-hydroxyphenyl)methanesulfonic acid Chemical compound C=O.S(=O)(=O)(O)CC1=C(C=CC=C1)O AJLXXPFSLLWHKQ-UHFFFAOYSA-N 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- ULUAUXLGCMPNKK-UHFFFAOYSA-N Sulfobutanedioic acid Chemical compound OC(=O)CC(C(O)=O)S(O)(=O)=O ULUAUXLGCMPNKK-UHFFFAOYSA-N 0.000 description 3
- RSWGJHLUYNHPMX-ONCXSQPRSA-N abietic acid Chemical compound C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C(O)=O RSWGJHLUYNHPMX-ONCXSQPRSA-N 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000018109 developmental process Effects 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- JMGZBMRVDHKMKB-UHFFFAOYSA-L disodium;2-sulfobutanedioate Chemical compound [Na+].[Na+].OS(=O)(=O)C(C([O-])=O)CC([O-])=O JMGZBMRVDHKMKB-UHFFFAOYSA-L 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- ITCAUAYQCALGGV-XTICBAGASA-M sodium;(1r,4ar,4br,10ar)-1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylate Chemical compound [Na+].C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C([O-])=O ITCAUAYQCALGGV-XTICBAGASA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/02—Well-drilling compositions
- C09K8/04—Aqueous well-drilling compositions
- C09K8/26—Oil-in-water emulsions
- C09K8/28—Oil-in-water emulsions containing organic additives
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
Abstract
本发明涉及一种抗240℃高温的水包油乳化钻井液,属石油钻井的钻井液技术领域。其原料组成包括70份水,30份基础油,0.1~0.4份烧碱,2.0~4.0份增粘剂,4.0~6.0份主乳化剂,1.0~3.0份辅乳化剂,2~5份降滤失剂,0.5~2.0份高温稳定剂和1.0~3.0份流型调节剂。其制备方法为:先将水投于10000转/分的高速搅拌机中,再依次投入增粘剂、辅乳化剂、主乳化剂、降滤失剂、高温稳定剂和流型调节剂,待所有组分原料添加完成并全部混合完毕后,在常温常压下再高速搅拌60分钟制作完毕。本发明在高温条件下具有较好的乳化稳定性、携岩能力、失水造壁性和润滑性。The invention relates to an oil-in-water emulsified drilling fluid resistant to a high temperature of 240 DEG C, belonging to the technical field of drilling fluids for petroleum drilling. Its raw material composition includes 70 parts of water, 30 parts of base oil, 0.1 to 0.4 parts of caustic soda, 2.0 to 4.0 parts of tackifier, 4.0 to 6.0 parts of primary emulsifier, 1.0 to 3.0 parts of auxiliary emulsifier, and 2 to 5 parts of fluid loss reducer agent, 0.5 to 2.0 parts of high temperature stabilizer and 1.0 to 3.0 parts of flow regulator. The preparation method is as follows: first put water into a high-speed mixer at 10,000 rpm, and then put in the thickener, auxiliary emulsifier, main emulsifier, fluid loss reducer, high temperature stabilizer and flow pattern regulator in turn, and wait for all After the component raw materials are added and all mixed, stir at a high speed for another 60 minutes at normal temperature and pressure to complete the preparation. The invention has good emulsification stability, rock-carrying ability, dehydration wall-building property and lubricity under high-temperature conditions.
Description
技术领域technical field
本发明涉及一种抗240℃高温的水包油乳化钻井液,属石油钻井的钻井液技术领域。The invention relates to an oil-in-water emulsified drilling fluid resistant to a high temperature of 240 DEG C, belonging to the technical field of drilling fluids for petroleum drilling.
背景技术Background technique
渤海湾地区南堡油田潜山构造带由于地层压力低,埋藏较深,地层温度较高,钻井液易发生漏失及储层伤害等问题。为及时准确地发现新的油气藏,更有效地开发油气资源,多实施欠平衡钻井作业,以最大限度地发现和保护储层。目前国内外针对低压易漏地层普遍采用的钻井液体系包括气体类钻井液、油基类钻井液、水包油钻井液、泡沫类钻井液以及微泡钻井液等等,根据不同钻井液体系的特点,其密度范围也不一样,其中气体类的密度范围最小,其次为泡沫类和微泡类,随后分别为油基类以及水包油类。在钻井过程中,由于泡沫及微泡对压力比较敏感,当钻到一定深度时,其泡沫破裂后无法起到降低密度的作用,而现阶段泡沫稳定性是一个世界难题。同时泡沫类和微泡类钻井液体系由于自身体系不连贯,因此会影响到电测以及数据传输。而空气、充气以及泡沫钻井还需要现场配备特殊的设备,因此在实用性上存在一定的局限性。Due to the low formation pressure, deep burial and high formation temperature in the buried hill structural belt of Nanpu Oilfield in the Bohai Bay area, drilling fluid leakage and reservoir damage are prone to occur. In order to discover new oil and gas reservoirs in a timely and accurate manner and develop oil and gas resources more effectively, more underbalanced drilling operations are implemented to maximize the discovery and protection of reservoirs. At present, the drilling fluid systems commonly used in low-pressure and leaky formations at home and abroad include gas drilling fluid, oil-based drilling fluid, oil-in-water drilling fluid, foam drilling fluid and micro-foam drilling fluid, etc., according to different drilling fluid systems The density range is different, among which the density range of gas is the smallest, followed by foam and microbubble, followed by oil-based and oil-in-water respectively. During the drilling process, because foam and micro-foam are sensitive to pressure, when drilling to a certain depth, the foam cannot reduce the density after the foam ruptures. At this stage, foam stability is a worldwide problem. At the same time, the foam and micro-foam drilling fluid systems will affect the electrical measurement and data transmission due to their incoherent systems. However, air, air and foam drilling also need to be equipped with special equipment on site, so there are certain limitations in practicability.
相对而言,油基类钻井液以及水包油钻井液应用相对广泛,由于油基类钻井液对环境的污染较大,后续钻屑的处理成本压力大以及成本等方面的问题(尤其对于易漏失地层),存在一定的局限性,因此综合考虑,水包油钻井液体系具有性能稳定、稳定井壁能力强,密度低于普通水基钻井液,能有效防止低压易漏失地层的漏失,具有良好的储层保护性能等特点,同时其环境污染较小、后续钻屑处理相对较易、且较油基钻井液成本低,适合于欠平衡钻井作业。Relatively speaking, oil-based drilling fluids and oil-in-water drilling fluids are relatively widely used. Due to oil-based drilling fluids polluting the environment, the cost pressure of subsequent drilling cuttings is high and cost problems (especially for easy Lost formations), there are certain limitations. Therefore, comprehensively considered, the oil-in-water drilling fluid system has stable performance, strong ability to stabilize the wellbore wall, and a lower density than ordinary water-based drilling fluids. Good reservoir protection performance and other characteristics, at the same time, it has less environmental pollution, relatively easy follow-up cuttings treatment, and lower cost than oil-based drilling fluid, so it is suitable for underbalanced drilling operations.
华北油田于1992年利用水包柴油钻井液钻成了我国陆上第一口中曲率半径水平井——任平1井,抗温能力120℃;大港油田于1999年研制出了水包原油钻井液体系,在大港油田西G2井的欠平衡钻井中进行了应用,抗温能力达150℃。胜利油田研制的盐水水包原油钻井液体系在江汉油田第一口中曲率水平井中成功应用,抗温100℃。大庆油田于2000年首次使用水包柴油钻井液体系进行欠平衡钻井,在宋深101井三开欠平衡井段得到了成功应用,抗温达150℃。大庆油田2008年研制出了可实现密度0.90g/cm3、抗温可达近200℃的水包油钻井液,现场应用井温在180℃左右。2009~2013年冀东油田在南堡潜山实施欠平衡钻井,使用了抗高温水包油钻井液体系,应用井温度在150~200℃左右。虽然水包油钻井液在国内都进行了成功的应用,但用于240℃以上的高温水包油钻井液体系未见报道,而冀东油田潜山储层所钻遇的地层温度越来越高,PG2区块潜山储层温度在200℃以上。虽然水包油钻井液体系的抗温能力在逐步提高,但对于像南堡油田潜山高温深井储层的勘探和开发,需要达到抗240℃高温的水包油钻井液,现有的水包油钻井液还无法满足其要求。In 1992, Huabei Oilfield drilled the first medium-curvature-radius horizontal well on land in my country—Well Renping 1, with water-in-diesel drilling fluid, which has a temperature resistance of 120°C; The liquid system has been applied in the underbalanced drilling of Well G2 in Dagang Oilfield, and its temperature resistance can reach 150°C. The crude oil-in-brine drilling fluid system developed by Shengli Oilfield was successfully applied in the first medium-curvature horizontal well in Jianghan Oilfield, with a temperature resistance of 100°C. Daqing Oilfield used the water-in-diesel drilling fluid system for underbalanced drilling for the first time in 2000. It was successfully applied in the third underbalanced section of Well Songshen 101, and the temperature resistance reached 150°C. In 2008, Daqing Oilfield developed an oil-in-water drilling fluid with a density of 0.90g/cm 3 and a temperature resistance of nearly 200°C. The field application well temperature is around 180°C. From 2009 to 2013, Jidong Oilfield implemented underbalanced drilling in the Nanpu buried hill, using a high-temperature resistant oil-in-water drilling fluid system, and the applied well temperature was around 150-200 °C. Although the oil-in-water drilling fluid has been successfully applied in China, there is no report on the high-temperature oil-in-water drilling fluid system above 240 °C, and the formation temperature encountered in the buried hill reservoir of Jidong Oilfield is getting higher and higher. High, the buried hill reservoir temperature in block PG2 is above 200°C. Although the temperature resistance of the oil-in-water drilling fluid system is gradually improving, for the exploration and development of high-temperature deep well reservoirs in buried hills like Nanpu Oilfield, oil-in-water drilling fluids that can withstand high temperatures of 240 °C are required. Oil drilling fluid can not meet its requirements.
发明内容Contents of the invention
本发明的目的在于,针对现有水包油钻井液达不到抗240℃高温的不足,提供一种在高温条件下具有较好的乳化稳定性、携岩能力、失水造壁性和润滑性等性能,能满足高温深井裂缝性储层以及低压衰竭储层勘探开发的抗240℃高温的水包油乳化钻井液。The purpose of the present invention is to provide an oil-in-water drilling fluid with good emulsification stability, rock-carrying ability, dehydration and wall-building properties and lubrication under high temperature conditions. It is an oil-in-water emulsified drilling fluid that can resist high temperature of 240℃ and can satisfy the exploration and development of high-temperature deep well fractured reservoirs and low-pressure depleted reservoirs.
本发明是通过如下的技术方案来实现上述目的的The present invention achieves the above-mentioned purpose through the following technical solutions
一种抗240℃高温的水包油乳化钻井液,其特征在于,它由下述重量份的原料制成:An oil-in-water emulsified drilling fluid resistant to 240°C high temperature is characterized in that it is made of the following raw materials in parts by weight:
水 70份,70 parts of water,
5#白油 30份,30 parts of 5# white oil,
烧碱 0.1~0.4份,Caustic soda 0.1~0.4 parts,
增粘剂 2.0~4.0份,Tackifier 2.0~4.0 parts,
主乳化剂 4.0~6.0份,Main emulsifier 4.0~6.0 parts,
辅乳化剂 1.0~3.0份,Co-emulsifier 1.0~3.0 parts,
降滤失剂 2~5份,2 to 5 parts of fluid loss reducer,
高温稳定剂 0.5~2.0份,High temperature stabilizer 0.5~2.0 parts,
流型调节剂 1.0~3.0份;Flow regulator 1.0~3.0 parts;
该抗240℃高温的水包油乳化钻井液的制备方法为:先将水投于10000转/分的高速搅拌机中,再投入增粘剂搅拌20分钟,再投入辅乳化剂搅拌2分钟,然后再投入主乳化剂搅拌30分钟,再投入降滤失剂、高温稳定剂搅拌20分钟,最后投入流型调节剂搅拌20分钟;待所有组分原料添加完成并全部混合完毕后,在常温常压下再高速搅拌60分钟制作完毕。The preparation method of the oil-in-water emulsified drilling fluid resistant to 240°C high temperature is as follows: first put water into a high-speed mixer at 10,000 rpm, then put in a viscosifier and stir for 20 minutes, then put in an auxiliary emulsifier and stir for 2 minutes, and then Then put in the main emulsifier and stir for 30 minutes, then put in the fluid loss reducer and high temperature stabilizer and stir for 20 minutes, and finally put in the flow regulator and stir for 20 minutes; Stir at high speed for another 60 minutes to complete the preparation.
所述的一种240℃高温的水包油乳化钻井液的原料的最佳重量配比为:The optimal weight ratio of the raw materials of the 240°C high temperature oil-in-water emulsified drilling fluid is:
水 70份,70 parts of water,
5#白油 30份,30 parts of 5# white oil,
烧碱 0.2份,0.2 parts of caustic soda,
增粘剂 3.0份,3.0 parts of tackifier,
主乳化剂 5.0份,5.0 parts of main emulsifier,
辅乳化剂 1.0份,Co-emulsifier 1.0 part,
降滤失剂 3份,3 parts of fluid loss reducer,
高温稳定剂 1份,1 part high temperature stabilizer,
流型调节剂 1.5份。Flow regulator 1.5 parts.
所述的增粘剂为凹凸棒石粘土、海泡石混合制得,凹凸棒石粘土与海泡石的比例为3~4︰1~2。The tackifier is prepared by mixing attapulgite clay and sepiolite, and the ratio of attapulgite clay to sepiolite is 3-4:1-2.
所述的主乳化剂由脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠、松香酸钠、脂肪醇聚氧乙烯醚AEO9在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠︰松香酸钠︰脂肪醇聚氧乙烯醚AEO9的比例为1~3︰2~3︰1~2。The main emulsifier is mixed and stirred by fatty alcohol polyoxyethylene ether sulfosuccinic monoester disodium, sodium rosinate, fatty alcohol polyoxyethylene ether AEO9 at a temperature of 80°C and a high-speed stirring of 10,000 rpm for 20 minutes. The ratio of fatty alcohol polyoxyethylene ether sulfosuccinic monoester disodium: abietic acid sodium: fatty alcohol polyoxyethylene ether AEO9 is 1~3:2~3:1~2.
所述的辅乳化剂由十二烷基苯磺酸钙、植物油酸、5#白油在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,十二烷基苯磺酸钙︰植物油酸︰5#白油的比例为3~5︰2~4︰5~7。The co-emulsifier is prepared by mixing and stirring calcium dodecylbenzenesulfonate, vegetable oleic acid, and 5# white oil for 20 minutes at a temperature of 80°C and at a high speed of 10,000 rpm. Dodecylbenzenesulfonate The ratio of calcium acid: vegetable oleic acid: 5# white oil is 3~5: 2~4: 5~7.
所述的降滤失剂由吸水树脂和磺甲基酚醛树脂混合后在105℃温度下烘干后,磨成200目的粉末制得,吸水树脂︰磺化酚醛树脂的比例为0.5~2︰3~5。The fluid loss reducer is prepared by mixing water-absorbing resin and sulfomethylphenol-formaldehyde resin, drying at 105°C, and grinding them into 200-mesh powder. The ratio of water-absorbing resin:sulfonated phenol-formaldehyde resin is 0.5~2:3 ~5.
所述的高温稳定剂为纳米碳酸钙、纳米二氧化硅、纳米蒙脱石中的一种。The high-temperature stabilizer is one of nano-calcium carbonate, nano-silicon dioxide, and nano-montmorillonite.
所述的流型调节剂为纳米蒙脱石、硅酸锂镁混合后制得,纳米蒙脱石︰硅酸锂镁的比例为0.5~2.0:5~8。The flow regulator is prepared by mixing nano-montmorillonite and lithium-magnesium silicate, and the ratio of nano-montmorillonite:lithium-magnesium silicate is 0.5-2.0:5-8.
本发明与现有技术相比的有益效果在于Compared with the prior art, the present invention has the beneficial effect of
1、抗温能力达到240℃,性能稳定,流动性好,滤失量小,稳定井壁能力较强,满足高温深井欠平衡钻探需要;1. The temperature resistance can reach 240 ℃, stable performance, good fluidity, small filtration loss, strong ability to stabilize the well wall, and meet the needs of underbalanced drilling in high-temperature deep wells;
2、密度低于普通水基钻井液,欠平衡钻进时对储层损害极小,有利于解放油气层,提高油气井产能;2. The density is lower than that of ordinary water-based drilling fluid, and the damage to the reservoir is minimal during underbalanced drilling, which is conducive to liberating oil and gas layers and increasing the productivity of oil and gas wells;
3、有助于防止井漏的产生和机械钻速的提高,不影响电测和核磁测井;3. Helps prevent lost circulation and increase ROP without affecting electrical and nuclear magnetic logging;
4、较之泡沫和充气钻井液体系而言,其在使用过程中不需要配备复杂设备,且性能上容易监测、控制和调整;4. Compared with foam and aerated drilling fluid systems, it does not need to be equipped with complex equipment during use, and its performance is easy to monitor, control and adjust;
5、润滑作用好,可减少对泥浆泵的损害;5. The lubricating effect is good, which can reduce the damage to the mud pump;
6、较纯油基钻井液成本低,对橡胶件的损害小,对环境污染小。6. Compared with pure oil-based drilling fluid, the cost is lower, the damage to rubber parts is small, and the environmental pollution is small.
具体实施方式detailed description
下面通过具体的实施例对该240℃高温的水包油乳化钻井液进行详细描述:The 240°C high-temperature oil-in-water emulsified drilling fluid is described in detail below through specific examples:
实施例1:Example 1:
按制取要求先确定每份的重量,再按下述重量份称取原料。First determine the weight of each part according to the preparation requirements, and then weigh the raw materials according to the following parts by weight.
水70份;70 parts of water;
5#白油30份;30 parts of 5# white oil;
烧碱0.2份;0.2 parts of caustic soda;
增粘剂3.0份,由凹凸棒石粘土、海泡石混合制得,凹凸棒石粘土与海泡石的比例为3.5:1.5;3.0 parts of tackifiers are prepared by mixing attapulgite clay and sepiolite, and the ratio of attapulgite clay to sepiolite is 3.5:1.5;
主乳化剂5.0份,由脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠、松香酸钠、脂肪醇聚氧乙烯醚AEO9在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠:松香酸钠:脂肪醇聚氧乙烯醚AEO9的比例为2︰2.5︰1.5;5.0 parts of the main emulsifier, made of fatty alcohol polyoxyethylene ether sulfosuccinic acid monoester disodium, rosin acid sodium, fatty alcohol polyoxyethylene ether AEO9 at a temperature of 80 ° C and 10,000 rpm under high-speed stirring for 20 Prepared in minutes, the ratio of fatty alcohol polyoxyethylene ether sulfosuccinic monoester disodium: sodium rosinate: fatty alcohol polyoxyethylene ether AEO9 is 2: 2.5: 1.5;
辅乳化剂1.0份,由十二烷基苯磺酸钙、植物油酸、5#白油在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,十二烷基苯磺酸钙︰植物油酸︰5#白油的比例为3.5︰3︰6;1.0 parts of co-emulsifier, prepared by mixing calcium dodecylbenzenesulfonate, vegetable oleic acid, and 5# white oil at a temperature of 80°C and stirring at a high speed of 10,000 rpm for 20 minutes. Dodecylbenzenesulfonate The ratio of calcium acid: vegetable oleic acid: 5# white oil is 3.5: 3: 6;
降滤失剂3份,由吸水树脂和磺甲基酚醛树脂混合后在105℃温度下烘干后,磨成200目的粉末制得,吸水树脂︰磺化酚醛树脂的比例为1︰4;3 parts of fluid loss reducer, made by mixing water-absorbent resin and sulfomethylphenol-formaldehyde resin, drying at 105°C, and grinding them into 200-mesh powder. The ratio of water-absorbent resin:sulfonated phenol-formaldehyde resin is 1:4;
高温稳定剂1份,为纳米二氧化硅;1 part of high temperature stabilizer, which is nano silicon dioxide;
流型调节剂1.5份,由纳米蒙脱石和硅酸锂镁混合后制得,纳米蒙脱石与硅酸锂镁的比例为1︰7;1.5 parts of flow regulator, made by mixing nano-montmorillonite and lithium magnesium silicate, the ratio of nano-montmorillonite to lithium magnesium silicate is 1:7;
该抗240℃高温的水包油乳化钻井液的制备方法为:先将水投于10000转/分的高速搅拌机中,再投入增粘剂搅拌20分钟,再投入辅乳化剂搅拌2分钟,然后再投入主乳化剂搅拌30分钟,再投入降滤失剂、高温稳定剂搅拌20分钟,最后投入流型调节剂搅拌20分钟;待所有组分原料添加完成并全部混合完毕后,在常温常压下再高速搅拌60分钟制作完毕。The preparation method of the oil-in-water emulsified drilling fluid resistant to 240°C high temperature is as follows: first put water into a high-speed mixer at 10,000 rpm, then put in a viscosifier and stir for 20 minutes, then put in an auxiliary emulsifier and stir for 2 minutes, and then Then put in the main emulsifier and stir for 30 minutes, then put in the fluid loss reducer and high temperature stabilizer and stir for 20 minutes, and finally put in the flow regulator and stir for 20 minutes; Stir at high speed for another 60 minutes to complete the preparation.
实施例2:Example 2:
按制取要求先确定每份的重量,再按下述重量份称取原料。First determine the weight of each part according to the preparation requirements, and then weigh the raw materials according to the following parts by weight.
水70份;70 parts of water;
5#白油30份;30 parts of 5# white oil;
烧碱0.1份;0.1 parts of caustic soda;
增粘剂2.0份,由凹凸棒石粘土、海泡石混合制得,凹凸棒石粘土与海泡石的比例为3︰1;2.0 parts of tackifier, made by mixing attapulgite clay and sepiolite, the ratio of attapulgite clay to sepiolite is 3:1;
主乳化剂4.0份,由脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠、松香酸钠、脂肪醇聚氧乙烯醚AEO9在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠:松香酸钠:脂肪醇聚氧乙烯醚AEO9的比例为1︰2︰1;4.0 parts of the main emulsifier, made of fatty alcohol polyoxyethylene ether sulfosuccinic acid monoester disodium, rosin acid sodium, fatty alcohol polyoxyethylene ether AEO9 at a temperature of 80 ° C and 10,000 rpm under high-speed stirring for 20 Prepared in minutes, the ratio of fatty alcohol polyoxyethylene ether sulfosuccinic monoester disodium: sodium rosinate: fatty alcohol polyoxyethylene ether AEO9 is 1: 2: 1;
辅乳化剂1.0份,由十二烷基苯磺酸钙、植物油酸、5#白油在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,十二烷基苯磺酸钙:植物油酸:5#白油的比例为3︰2︰5;1.0 parts of co-emulsifier, prepared by mixing calcium dodecylbenzenesulfonate, vegetable oleic acid, and 5# white oil at a temperature of 80°C and stirring at a high speed of 10,000 rpm for 20 minutes. Dodecylbenzenesulfonate The ratio of calcium acid: vegetable oleic acid: 5# white oil is 3: 2: 5;
降滤失剂2份,由吸水树脂和磺甲基酚醛树脂混合后在105℃温度下烘干后,磨成200目的粉末制得,吸水树脂︰磺化酚醛树脂的比例为0.5︰3;2 parts of fluid loss reducer, made by mixing water-absorbing resin and sulfomethylphenol-formaldehyde resin, drying at 105°C, and grinding them into 200-mesh powder. The ratio of water-absorbing resin:sulfonated phenol-formaldehyde resin is 0.5:3;
高温稳定剂0.5份,为纳米二氧化硅;0.5 part of high-temperature stabilizer is nano silicon dioxide;
流型调节剂1.0份,由纳米蒙脱石和硅酸锂镁混合后制得,纳米蒙脱石和硅酸锂镁的比例为0.5︰5;1.0 parts of flow regulator, made by mixing nano-montmorillonite and lithium magnesium silicate, the ratio of nano-montmorillonite and lithium magnesium silicate is 0.5:5;
该抗240℃高温的水包油乳化钻井液的制备方法为:先将水投于10000转/分的高速搅拌机中,再投入增粘剂搅拌20分钟,再投入辅乳化剂搅拌2分钟,然后再投入主乳化剂搅拌30分钟,再投入降滤失剂、高温稳定剂搅拌20分钟,最后投入流型调节剂搅拌20分钟;待所有组分原料添加完成并全部混合完毕后,在常温常压下再高速搅拌60分钟制作完毕。The preparation method of the oil-in-water emulsified drilling fluid resistant to 240°C high temperature is as follows: first put water into a high-speed mixer at 10,000 rpm, then put in a viscosifier and stir for 20 minutes, then put in an auxiliary emulsifier and stir for 2 minutes, and then Then put in the main emulsifier and stir for 30 minutes, then put in the fluid loss reducer and high temperature stabilizer and stir for 20 minutes, and finally put in the flow regulator and stir for 20 minutes; Stir at high speed for another 60 minutes to complete the preparation.
实施例3:Example 3:
按制取要求先确定每份的重量,再按下述重量份称取原料。First determine the weight of each part according to the preparation requirements, and then weigh the raw materials according to the following parts by weight.
水70份;70 parts of water;
5#白油30份;30 parts of 5# white oil;
烧碱0.4份;0.4 parts of caustic soda;
增粘剂4.0份,由凹凸棒石粘土、海泡石混合制得,凹凸棒石粘土与海泡石的比例为4︰2;4.0 parts of tackifier, made by mixing attapulgite clay and sepiolite, the ratio of attapulgite clay to sepiolite is 4:2;
主乳化剂6.0份,由脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠、松香酸钠、脂肪醇聚氧乙烯醚AEO9在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,脂肪醇聚氧乙烯醚磺基琥珀酸单酯二钠:松香酸钠:脂肪醇聚氧乙烯醚AEO9的比例为3:3:2;6.0 parts of the main emulsifier, made of fatty alcohol polyoxyethylene ether sulfosuccinic acid monoester disodium, rosin acid sodium, fatty alcohol polyoxyethylene ether AEO9 at a temperature of 80 ° C and 10,000 rpm under high-speed stirring for 20 Prepared in minutes, the ratio of fatty alcohol polyoxyethylene ether sulfosuccinate disodium: sodium abietate: fatty alcohol polyoxyethylene ether AEO9 is 3:3:2;
辅乳化剂3.0份,由十二烷基苯磺酸钙、植物油酸、5#白油在80℃的温度、10000转/分的高速搅拌下混合搅拌20分钟制得,十二烷基苯磺酸钙:植物油酸:5#白油的比例为5︰4︰7;3.0 parts of co-emulsifier, prepared by mixing calcium dodecylbenzenesulfonate, vegetable oleic acid, and 5# white oil at a temperature of 80°C and stirring at a high speed of 10,000 rpm for 20 minutes. Dodecylbenzenesulfonate The ratio of calcium acid: vegetable oleic acid: 5# white oil is 5:4:7;
降滤失剂5.0份,由吸水树脂和磺甲基酚醛树脂混合后在105℃温度下烘干后,磨成200目的粉末制得,吸水树脂︰磺化酚醛树脂的比例为2︰5;5.0 parts of fluid loss reducer, made by mixing water-absorbing resin and sulfomethylphenol-formaldehyde resin, drying at 105°C, and grinding them into 200-mesh powder. The ratio of water-absorbing resin:sulfonated phenol-formaldehyde resin is 2:5;
高温稳定剂2.0份,为纳米二氧化硅;2.0 parts of high-temperature stabilizers are nano silicon dioxide;
流型调节剂3.0份,由纳米蒙脱石和硅酸锂镁混合后制得,纳米蒙脱石和硅酸锂镁的比例为2︰8;3.0 parts of flow regulator, made by mixing nano-montmorillonite and lithium magnesium silicate, the ratio of nano-montmorillonite and lithium magnesium silicate is 2:8;
该抗240℃高温的水包油乳化钻井液的制备方法为:先将水投于10000转/分的高速搅拌机中,再投入增粘剂搅拌20分钟,再投入辅乳化剂搅拌2分钟,然后再投入主乳化剂搅拌30分钟,再投入降滤失剂、高温稳定剂搅拌20分钟,最后投入流型调节剂搅拌20分钟;待所有组分原料添加完成并全部混合完毕后,在常温常压下再高速搅拌60分钟制作完毕。The preparation method of the oil-in-water emulsified drilling fluid resistant to 240°C high temperature is as follows: first put water into a high-speed mixer at 10,000 rpm, then put in a viscosifier and stir for 20 minutes, then put in an auxiliary emulsifier and stir for 2 minutes, and then Then put in the main emulsifier and stir for 30 minutes, then put in the fluid loss reducer and high temperature stabilizer and stir for 20 minutes, and finally put in the flow regulator and stir for 20 minutes; Stir at high speed for another 60 minutes to complete the preparation.
以上各实施例配制400ml的本发明钻井液,通过240℃热滚老化16小时,各实施例配制的本发明钻井液的性能测试数据如下表:Above each embodiment prepares the drilling fluid of the present invention of 400ml, by 240 ℃ of thermal rolling aging 16 hours, the performance test data of the drilling fluid of the present invention prepared by each embodiment is as follows table:
上述实施例中,实施例一为本发明的最佳实施例,其在240℃高温热滚老化16h后无油析出,说明乳状液热稳定性强,同时本发明所配制的钻井液具有较好的流变性和失水造壁性,能够有效的携岩和形成致密泥饼稳定井壁,满足高温深井裂缝性储层以及低压衰竭储层的勘探开发。Among the above-mentioned examples, Example 1 is the best example of the present invention, and no oil is precipitated after aging at 240°C for 16 hours, indicating that the emulsion has strong thermal stability, and at the same time, the drilling fluid prepared by the present invention has better The rheology and water loss wall-building properties can effectively carry rocks and form dense mud cakes to stabilize the well wall, meeting the exploration and development of high-temperature deep well fractured reservoirs and low-pressure depleted reservoirs.
以上所述只是该发明的具体实施方式,上述举例说明不对本发明的实质内容构成限制,所属技术领域的普通技术人员在阅读了本说明书后可以对上述的具体实施方式做修改或变形,而不背离本发明的实质和范围。The above is only the specific implementation of the invention, and the above illustrations do not limit the essence of the present invention. Those of ordinary skill in the art can modify or deform the above specific implementation after reading this specification, without depart from the spirit and scope of the invention.
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