CN112480889B - Preparation method of retarder for slag cementing fluid - Google Patents
Preparation method of retarder for slag cementing fluid Download PDFInfo
- Publication number
- CN112480889B CN112480889B CN202011411704.XA CN202011411704A CN112480889B CN 112480889 B CN112480889 B CN 112480889B CN 202011411704 A CN202011411704 A CN 202011411704A CN 112480889 B CN112480889 B CN 112480889B
- Authority
- CN
- China
- Prior art keywords
- retarder
- component
- slag
- cementing fluid
- acid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000002893 slag Substances 0.000 title claims abstract description 51
- 239000012530 fluid Substances 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 24
- 239000010455 vermiculite Substances 0.000 claims abstract description 38
- 229910052902 vermiculite Inorganic materials 0.000 claims abstract description 38
- 235000019354 vermiculite Nutrition 0.000 claims abstract description 38
- 238000006243 chemical reaction Methods 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 18
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 12
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 12
- USHAGKDGDHPEEY-UHFFFAOYSA-L potassium persulfate Chemical compound [K+].[K+].[O-]S(=O)(=O)OOS([O-])(=O)=O USHAGKDGDHPEEY-UHFFFAOYSA-L 0.000 claims abstract description 12
- 239000000843 powder Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 239000003999 initiator Substances 0.000 claims abstract description 7
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000008367 deionised water Substances 0.000 claims abstract description 6
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 6
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims abstract description 6
- 239000011976 maleic acid Substances 0.000 claims abstract description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 6
- 239000001301 oxygen Substances 0.000 claims abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 6
- HELHAJAZNSDZJO-OLXYHTOASA-L sodium L-tartrate Chemical compound [Na+].[Na+].[O-]C(=O)[C@H](O)[C@@H](O)C([O-])=O HELHAJAZNSDZJO-OLXYHTOASA-L 0.000 claims abstract description 6
- 239000001433 sodium tartrate Substances 0.000 claims abstract description 6
- 229960002167 sodium tartrate Drugs 0.000 claims abstract description 6
- 235000011004 sodium tartrates Nutrition 0.000 claims abstract description 6
- MNCGMVDMOKPCSQ-UHFFFAOYSA-M sodium;2-phenylethenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C=CC1=CC=CC=C1 MNCGMVDMOKPCSQ-UHFFFAOYSA-M 0.000 claims abstract description 6
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims abstract description 6
- RRHXZLALVWBDKH-UHFFFAOYSA-M trimethyl-[2-(2-methylprop-2-enoyloxy)ethyl]azanium;chloride Chemical compound [Cl-].CC(=C)C(=O)OCC[N+](C)(C)C RRHXZLALVWBDKH-UHFFFAOYSA-M 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims abstract 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 27
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 10
- 239000000178 monomer Substances 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 239000012263 liquid product Substances 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 238000000227 grinding Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 claims 1
- 230000008719 thickening Effects 0.000 abstract description 17
- 239000000203 mixture Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 6
- 239000004568 cement Substances 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- 239000002002 slurry Substances 0.000 description 8
- 239000012190 activator Substances 0.000 description 7
- 239000010410 layer Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000003381 stabilizer Substances 0.000 description 6
- 239000000725 suspension Substances 0.000 description 6
- 238000010276 construction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 5
- 230000002035 prolonged effect Effects 0.000 description 5
- 239000007789 gas Substances 0.000 description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 230000002159 abnormal effect Effects 0.000 description 3
- DPXJVFZANSGRMM-UHFFFAOYSA-N acetic acid;2,3,4,5,6-pentahydroxyhexanal;sodium Chemical group [Na].CC(O)=O.OCC(O)C(O)C(O)C(O)C=O DPXJVFZANSGRMM-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 description 3
- 239000000701 coagulant Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 238000005755 formation reaction Methods 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 235000019812 sodium carboxymethyl cellulose Nutrition 0.000 description 3
- 229920001027 sodium carboxymethylcellulose Polymers 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- 239000010936 titanium Substances 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000979 retarding effect Effects 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 235000019325 ethyl cellulose Nutrition 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000004482 other powder Substances 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 239000000375 suspending agent Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
Images
Classifications
-
- 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
- C09K8/42—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
-
- 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
- C08F212/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring
- C08F212/02—Monomers containing only one unsaturated aliphatic radical
- C08F212/04—Monomers containing only one unsaturated aliphatic radical containing one ring
- C08F212/14—Monomers containing only one unsaturated aliphatic radical containing one ring substituted by heteroatoms or groups containing heteroatoms
- C08F212/30—Sulfur
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
本发明涉及一种矿渣固井液用缓凝剂的制备方法,包括:(1)在反应容器中将苯乙烯磺酸钠、马来酸、甲基丙烯酰氧乙基三甲基氯化铵混合,溶解在去离子水中,调节反应溶液pH值为7~8;通入氮气除氧,升至70℃时加入引发剂过硫酸钾;将产物冷却、提纯、干燥,得到A组分;(2)将天然蛭石平铺于磁盘上,置于微波炉内,高火条件下处理1 min,再将其加入到盐酸中,水浴70℃下搅拌,得到酸改性蛭石粉末,即B组分;(3)将酒石酸钠与柠檬酸混合,得到C组分;(4)将A组分、B组分、C组分以3:1:1的质量比混合。本发明原理可靠,操作简便,制备的缓凝剂能有效控制矿渣固井液的稠化时间,不影响其沉降稳定性,可广泛用于以矿渣胶凝材料为支撑的固井工程。
The invention relates to a preparation method of a retarder for slag cementing fluid, comprising: (1) mixing sodium styrene sulfonate, maleic acid and methacryloyloxyethyltrimethylammonium chloride in a reaction vessel Mix, dissolve in deionized water, adjust the pH value of the reaction solution to 7~8; pass nitrogen to remove oxygen, add initiator potassium persulfate when the temperature rises to 70 °C; cool, purify and dry the product to obtain component A; ( 2) Spread the natural vermiculite on the disk, put it in a microwave oven, and treat it under high fire for 1 min, then add it to hydrochloric acid, and stir it in a water bath at 70°C to obtain acid-modified vermiculite powder, namely component B (3) mixing sodium tartrate and citric acid to obtain C component; (4) mixing A component, B component and C component with a mass ratio of 3:1:1. The invention is reliable in principle and simple in operation, and the prepared retarder can effectively control the thickening time of slag cementing fluid without affecting its settlement stability, and can be widely used in cementing engineering supported by slag cementing material.
Description
技术领域technical field
本发明涉及油田化学领域一种固井液用缓凝剂的制备方法,特别是涉及一种固井矿渣胶凝材料用缓凝剂的制备方法,能有效控制矿渣固井液的稠化时间,并可改善矿渣固井液的沉降稳定性。The invention relates to a method for preparing a retarder for cementing fluid in the field of oilfield chemistry, in particular to a method for preparing a retarder for cementing slag cementing materials, which can effectively control the thickening time of the slag cementing fluid, And can improve the settlement stability of slag cementing fluid.
背景技术Background technique
传统固井是指当钻井作业达到一定井深后,在已钻成井眼中下入套管柱,然后在套管和井壁之间的环空内注入水泥浆达到某预定位置,并使其在预定时间内迅速凝结、硬化,形成优质、完整、具有良好层间封隔能力的水泥环的过程。近几年来,随着油田勘探开发难度和井下开采复杂程度的增加,固井难度逐渐加大。传统水泥浆固井技术存在易向地层流失、强度发展缓慢、密度大易发生漏失等问题。因此,具有与水泥相似水硬性的胶凝材料矿渣,由于其活性强、早强高、顶替效率强、成本低廉等特点,受到了相关研究人员的广泛关注,矿渣固井液技术也应运而生。Traditional cementing means that when the drilling operation reaches a certain well depth, the casing string is run in the drilled wellbore, and then the cement slurry is injected into the annulus between the casing and the well wall to reach a predetermined position, and make it in the predetermined position. The process of rapidly setting and hardening within a short period of time to form a high-quality, complete cement sheath with good interlayer isolation ability. In recent years, with the increase in the difficulty of oilfield exploration and development and the complexity of underground mining, the difficulty of cementing has gradually increased. Traditional cement slurry cementing technology has problems such as easy formation loss, slow strength development, high density and easy leakage. Therefore, cementitious material slag with hydraulic properties similar to cement has attracted extensive attention from relevant researchers due to its strong activity, high early strength, high replacement efficiency, and low cost, and slag cementing fluid technology has also emerged as the times require. .
矿渣固井液是以矿渣为无机胶凝材料制备的一种新型固井液,以氢氧化钠、碳酸钠、硅酸钠及其复配物为激活剂,以羧甲基纤维素钠、羟乙基纤维素等为悬浮剂。矿渣固井液可替代水泥浆,充满套管与套管或地层间的环形空间,凝固硬化后支撑套管、加固井壁,有效封隔油气水层,用于解决低压易漏地层、长封固段固井作业,提高简化井身结构等非目的层的封固、填充作业。Slag cementing fluid is a new type of well cementing fluid prepared from slag as inorganic cementitious material. Sodium hydroxide, sodium carbonate, sodium silicate and their complexes are used as activators. Ethyl cellulose and the like are suspending agents. The slag cementing fluid can replace the cement slurry, fill the annular space between the casing and the casing or the formation, support the casing after solidification and hardening, strengthen the well wall, effectively seal the oil, gas and water layers, and is used to solve the problem of low-pressure leaky formations, long The cementing operation in the sealing section improves the sealing and filling operations of non-target layers such as simplified well structure.
矿渣固井液缓凝剂作为最重要的三种外加剂之一,对延迟凝固时间,维持浆体可泵送状态具有重要作用,是确保固井施工顺利和固井质量的关键环节。目前用于水泥浆的缓凝剂往往不适用于矿渣固井液,研发出适用于矿渣固井液的缓凝剂迫在眉睫。Slag cementing fluid retarder, as one of the three most important admixtures, plays an important role in delaying the solidification time and maintaining the pumpable state of the slurry, and is a key link to ensure smooth cementing construction and cementing quality. The retarders currently used for cement slurry are often not suitable for slag cementing fluids, and it is imminent to develop a retarder suitable for slag cementing fluids.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种矿渣固井液用缓凝剂的制备方法,该方法原理可靠,操作简便,制备的缓凝剂解决了目前矿渣固井液沉降稳定性差、过度分散、稠度降低等问题,可以有效控制调节矿渣固井液的稠化时间,同时不影响其沉降稳定性,可广泛用于以矿渣胶凝材料固井技术为支撑的固井工程。The purpose of the present invention is to provide a preparation method of a retarder for slag cementing fluid, the method is reliable in principle, easy to operate, and the prepared retarder solves the problems of poor settlement stability, excessive dispersion, and reduced consistency of the current slag cementing fluid. It can effectively control and adjust the thickening time of slag cementing fluid without affecting its settlement stability, and can be widely used in cementing projects supported by slag cementing material cementing technology.
为达到以上技术目的,本发明采用以下技术方案。In order to achieve the above technical purpose, the present invention adopts the following technical solutions.
一种矿渣固井液用缓凝剂的制备方法,依次包括以下步骤:A preparation method of a retarder for slag cementing fluid, comprising the following steps in sequence:
(1)、制备缓凝剂A组分:(1) Preparation of component A of retarder:
1)在反应容器中将苯乙烯磺酸钠SSS、马来酸MA、甲基丙烯酰氧乙基三甲基氯化铵DMC以质量比为10~8:7~5:3~1的比例混合,溶解在去离子水中,用氢氧化钠调节反应溶液的pH值为7~8;1) In the reaction vessel, mix sodium styrene sulfonate SSS, maleic acid MA, and methacryloyloxyethyltrimethylammonium chloride DMC in a mass ratio of 10~8:7~5:3~1 Mix, dissolve in deionized water, and adjust the pH of the reaction solution to 7~8 with sodium hydroxide;
2)向反应容器中通入10min氮气除氧,待反应体系温度升至70℃时,缓慢加入引发剂过硫酸钾,过硫酸钾的质量为单体总质量的1.0~3.0%;2) Pour nitrogen into the reaction vessel to remove oxygen for 10 minutes, and when the temperature of the reaction system rises to 70°C, slowly add the initiator potassium persulfate, and the quality of potassium persulfate is 1.0~3.0% of the total monomer mass;
3)反应进行4h后,将粘稠液体产物冷却至室温,用丙酮进行提纯、干燥和粉碎,得到缓凝剂A组分;3) After the reaction is carried out for 4 hours, the viscous liquid product is cooled to room temperature, purified, dried and pulverized with acetone to obtain component A of the retarder;
(2)、制备缓凝剂B组分:(2) Preparation of component B of retarder:
1)以天然蛭石(VER)为原料,均匀平铺于磁盘上,置于微波炉内,在微波高火的条件下处理 1 min,得到微波膨胀蛭石;1) Using natural vermiculite (VER) as the raw material, evenly spread it on the disk, place it in a microwave oven, and treat it for 1 min under the condition of microwave high fire to obtain microwave-expanded vermiculite;
2)取一定量微波膨胀蛭石粉体,按固液质量比 1:20~25加入到2mol/L 的盐酸溶液中,在水浴 70℃下搅拌2h;2) Take a certain amount of microwave-expanded vermiculite powder, add it to a 2mol/L hydrochloric acid solution at a solid-liquid mass ratio of 1:20~25, and stir at 70°C in a water bath for 2h;
3)洗涤、抽滤、干燥,研磨至200目,得到酸改性蛭石粉末,即缓凝剂B组分;3) Washing, suction filtration, drying, and grinding to 200 mesh to obtain acid-modified vermiculite powder, namely component B of retarder;
(3)、制备缓凝剂C组分:(3), preparation of retarder C component:
将酒石酸钠与柠檬酸以20~80:80~20的质量比混合,得到缓凝剂C组分;Mix sodium tartrate and citric acid in a mass ratio of 20~80:80~20 to obtain component C of the retarder;
(4)、制备缓凝剂:(4) Preparation of retarder:
将A组分、B组分、C组分以3:1:1的质量比混合,得到矿渣固井液用缓凝剂。The A component, the B component and the C component are mixed in a mass ratio of 3:1:1 to obtain a retarder for slag cementing fluid.
以上物质市场上均有售。The above substances are available in the market.
本发明制备的矿渣固井液用缓凝剂外观为白色粉末,无味。该缓凝剂在水中的溶解性良好,缓凝效果良好,能够明显延长固井液的稠化时间,并保持良好的沉降稳定性。The appearance of the retarder for slag cementing fluid prepared by the invention is white powder and tasteless. The retarder has good solubility in water and good retardation effect, can significantly prolong the thickening time of the cementing fluid, and maintain good settlement stability.
与现有技术相比,本发明取得的有益效果如下:Compared with the prior art, the beneficial effects obtained by the present invention are as follows:
1、本发明采用自由基水溶液聚合方式并使用无机过氧化物类的过硫酸钾作为引发剂,操作过程简单易行,合成聚合物的成功率高,且能保证一定的转化率。1. The present invention adopts the free radical aqueous solution polymerization mode and uses the potassium persulfate of inorganic peroxides as the initiator, the operation process is simple and easy, the success rate of synthesizing the polymer is high, and a certain conversion rate can be guaranteed.
2、引入了大分子和不易降解的官能团单体,所得聚合物耐温性能得到显著提高,能够有效延长固井液的稠化时间。2. Introducing macromolecules and non-degradable functional monomers, the temperature resistance of the obtained polymer is significantly improved, and the thickening time of the cementing fluid can be effectively prolonged.
3、采用的新型单体使聚合物在一定温度下发生分子间或分子内缔合,由于聚合物分子中较高的SSS含量,保证了聚合物分子链的强亲水性,相容稳定性能提升。3. The new monomer used enables the polymer to undergo intermolecular or intramolecular association at a certain temperature. Due to the high SSS content in the polymer molecule, the strong hydrophilicity of the polymer molecular chain is ensured, and the compatibility and stability are improved. .
4、本发明采用的蛭石,一种天然、无毒的矿物质,由大量具有一定的结构单元层组成,在高温作用下会膨胀。通过微波改性方法并未破坏蛭石结构,而是疏通了蛭石层间孔隙,且随着蛭石层间距离的增大,膨胀蛭石的吸附性能提高,使得蛭石能够更好地与其他粉体吸附,同时具有良好的吸水性和稳定的化学性能。4. The vermiculite used in the present invention, a natural, non-toxic mineral, is composed of a large number of layers with certain structural units, and will expand under the action of high temperature. The microwave modification method did not destroy the vermiculite structure, but dredged the pores between the vermiculite layers. With the increase of the distance between the vermiculite layers, the adsorption performance of the expanded vermiculite improved, so that the vermiculite could better interact with the vermiculite. Other powder adsorption, while having good water absorption and stable chemical properties.
5、本发明中蛭石酸化是用无机强酸将蛭石结构中的四面体阳离子和八面体阳离子溶出,达到提高蛭石比表面积、改善层电荷、增加表面活性官能团的目的。酸化的蛭石有更好的相容性,能够更好地与有机基体相结合。5. In the present invention, acidification of vermiculite is to dissolve the tetrahedral cations and octahedral cations in the vermiculite structure with strong inorganic acid, so as to achieve the purpose of increasing the specific surface area of vermiculite, improving the layer charge and increasing the surface active functional groups. The acidified vermiculite has better compatibility and can be better combined with the organic matrix.
6、本发明的缓凝剂采用三种组分结合的方式,弥补了原有缓凝剂剂材料单一、性能缺失的不足。6. The retarder of the present invention adopts the combination of three components, which makes up for the shortcomings of the original retarder with single material and lack of performance.
7、本发明的缓凝剂,专用于固井用矿渣固井液控制缓凝效果,填补了现有技术的缺陷和不足。7. The retarder of the present invention is specially used for controlling the retarding effect of slag cementing fluid for well cementing, and fills the defects and deficiencies of the prior art.
附图说明Description of drawings
图1为矿渣固井液用缓凝剂在70℃下的稠化曲线图。Figure 1 shows the thickening curve of retarder for slag cementing fluid at 70°C.
图2为矿渣固井液用缓凝剂在80℃下的稠化曲线图。Fig. 2 is the thickening curve diagram of retarder for slag cementing fluid at 80°C.
图3为矿渣固井液用缓凝剂在90℃下的稠化曲线图。Fig. 3 is the thickening curve diagram of retarder for slag cementing fluid at 90°C.
具体实施方式Detailed ways
下面结合附图和实施例,进一步说明本发明。The present invention will be further described below with reference to the accompanying drawings and embodiments.
实施例1Example 1
缓凝剂制备过程:Retarder preparation process:
(1)、A组分的制备:(1) Preparation of component A:
1)在反应容器中将苯乙烯磺酸钠SSS、马来酸MA、甲基丙烯酰氧乙基三甲基氯化铵DMC以质量比为10:7:3的比例混合,溶解在去离子水中,用氢氧化钠调节反应溶液的PH值为7~8;1) In the reaction vessel, mix sodium styrene sulfonate SSS, maleic acid MA, and methacryloyloxyethyltrimethylammonium chloride DMC in a mass ratio of 10:7:3, and dissolve them in deionized water. In water, the pH value of the reaction solution is adjusted with sodium hydroxide to be 7~8;
2)向反应容器中通入10min氮气除氧,待反应体系温度升至70℃时,缓慢加入引发剂过硫酸钾,过硫酸钾的质量为单体总质量的1.0%;2) Pour nitrogen into the reaction vessel for 10 minutes to remove oxygen, and when the temperature of the reaction system rises to 70°C, slowly add initiator potassium persulfate, and the quality of potassium persulfate is 1.0% of the total monomer mass;
3)反应进行4h后,将粘稠液体产物冷却至室温,用丙酮进行提纯、干燥和粉碎,得到缓凝剂组分A;3) After the reaction is carried out for 4 hours, the viscous liquid product is cooled to room temperature, purified with acetone, dried and pulverized to obtain the retarder component A;
(2)、B组分的制备:(2) Preparation of component B:
1)以天然蛭石(VER)为原料,均匀平铺于磁盘上,置于微波炉内,在微波高火的条件下处理 1 min,得到微波膨胀蛭石;1) Using natural vermiculite (VER) as the raw material, evenly spread it on the disk, place it in a microwave oven, and treat it for 1 min under the condition of microwave high fire to obtain microwave-expanded vermiculite;
2)取一定量微波膨胀蛭石粉体,按固液比 1:20加入到2mol/L 盐酸的酸溶液中,在水浴 70℃下磁力搅拌2h;2) Take a certain amount of microwave-expanded vermiculite powder, add it to an acid solution of 2mol/L hydrochloric acid at a solid-to-liquid ratio of 1:20, and stir magnetically for 2h at 70°C in a water bath;
3)搅拌后在自然环境中静置2h,洗涤、抽滤,然后将其放在干燥箱内在 105℃条件下干燥24 h后,研磨至 200 目,得到酸改性蛭石粉末即缓凝剂组分B;3) After stirring, let it stand in the natural environment for 2 hours, wash it, filter it with suction, and then put it in a drying oven at 105 °C for 24 hours, and then grind it to 200 mesh to obtain acid-modified vermiculite powder, which is a retarder. component B;
(3)、C组分的制备:(3) Preparation of component C:
酒石酸钠与柠檬酸以20:80的比例混合,得到缓凝剂组分C;Sodium tartrate and citric acid are mixed in a ratio of 20:80 to obtain retarder component C;
(4)、缓凝剂的制备:(4) Preparation of retarder:
A、B、C组分以3:1:1的比例混合,制得矿渣固井液用缓凝剂。The components A, B and C are mixed in a ratio of 3:1:1 to obtain a retarder for slag cementing fluid.
将制得的缓凝剂(命名为H1)加入矿渣固井液配方中,在温度70℃,压力25MPa的稠化条件下进行试验,以验证该缓凝剂的缓凝性能。The prepared retarder (named H1) was added to the slag cementing fluid formula, and the experiment was carried out under the thickening conditions of
矿渣固井液配方:矿渣150份+激活剂12份+悬浮稳定剂2份+缓凝剂3份+水100份。Slag cementing fluid formula: 150 parts of slag + 12 parts of activator + 2 parts of suspension stabilizer + 3 parts of retarder + 100 parts of water.
注:上述矿渣为提钛尾渣,激活剂为氢氧化钠,悬浮稳定剂为羧甲基纤维素钠。Note: The above slag is titanium extraction tailings, the activator is sodium hydroxide, and the suspension stabilizer is sodium carboxymethyl cellulose.
如图1所示,矿渣固井液的稠化时间在高温高压环境下得到了明显的延长,能够满足油气井固井现场施工对固井液泵注时间的要求,且稠化曲线表明该缓凝剂的加入在高温高压条件下并未出现异常的“鼓包”和“包芯”现象,水泥浆稠度维持在一个比较稳定的值周围,表明该缓凝剂对维持矿渣固井液的沉降稳定性具有良好效果。As shown in Figure 1, the thickening time of slag cementing fluid has been significantly prolonged under high temperature and high pressure environment, which can meet the requirements of oil and gas well cementing site construction for cementing fluid pumping time, and the thickening curve shows that the slow The addition of the coagulant does not appear abnormal "bulging" and "core wrapping" phenomena under the conditions of high temperature and high pressure, and the consistency of the cement slurry is maintained at a relatively stable value, indicating that the retarder can maintain the stability of the settlement of the slag cementing fluid. Sex has a good effect.
实施例2Example 2
缓凝剂制备过程:Retarder preparation process:
(1)、A组分的制备:(1) Preparation of component A:
1)在反应容器中将苯乙烯磺酸钠SSS、马来酸MA、甲基丙烯酰氧乙基三甲基氯化铵DMC以质量比为9:6:2的比例混合,溶解在去离子水中,用氢氧化钠调节反应溶液的PH值为7~8;1) In the reaction vessel, mix sodium styrene sulfonate SSS, maleic acid MA, and methacryloyloxyethyltrimethylammonium chloride DMC in a mass ratio of 9:6:2, and dissolve them in deionized water. In water, the pH value of the reaction solution is adjusted with sodium hydroxide to be 7~8;
2)向反应容器中通入10min氮气除氧,待反应体系温度升至70℃时,缓慢加入引发剂过硫酸钾,过硫酸钾的质量为单体总质量的2.0%;2) Pour nitrogen into the reaction vessel for 10 minutes to remove oxygen, and when the temperature of the reaction system rises to 70°C, slowly add the initiator potassium persulfate, and the quality of potassium persulfate is 2.0% of the total monomer mass;
3)反应进行4h后,将粘稠液体产物冷却至室温,用丙酮进行提纯、干燥和粉碎,得到缓凝剂组分A;3) After the reaction is carried out for 4 hours, the viscous liquid product is cooled to room temperature, purified with acetone, dried and pulverized to obtain the retarder component A;
(2)、B组分的制备:(2) Preparation of component B:
1)以天然蛭石(VER)为原料,均匀平铺于磁盘上,置于微波炉内,在微波高火的条件下处理 1 min,得到微波膨胀蛭石;1) Using natural vermiculite (VER) as the raw material, evenly spread it on the disk, place it in a microwave oven, and treat it for 1 min under the condition of microwave high fire to obtain microwave-expanded vermiculite;
2)取一定量微波膨胀蛭石粉体,按固液比 1:23加入到2mol/L 盐酸的酸溶液中,在水浴 70℃下磁力搅拌2h;2) Take a certain amount of microwave-expanded vermiculite powder, add it to an acid solution of 2mol/L hydrochloric acid at a solid-to-liquid ratio of 1:23, and stir magnetically for 2h at 70°C in a water bath;
3)搅拌后在自然环境中静置2h,洗涤、抽滤,然后将其放在干燥箱内在 105℃条件下干燥24 h,研磨至 200 目,得到酸改性蛭石粉末即缓凝剂组分B;3) After stirring, let it stand in the natural environment for 2 hours, wash it, filter it with suction, and then put it in a drying oven at 105 °C for 24 hours, and grind it to 200 mesh to obtain acid-modified vermiculite powder, namely the retarder group. point B;
(3)、C组分的制备:(3) Preparation of component C:
酒石酸钠与柠檬酸以50:50的比例混合,得到缓凝剂组分C;Sodium tartrate and citric acid are mixed in a ratio of 50:50 to obtain retarder component C;
(4)、缓凝剂的制备:(4) Preparation of retarder:
A、B、C组分以3:1:1的比例混合,制得矿渣固井液用缓凝剂。The components A, B and C are mixed in a ratio of 3:1:1 to obtain a retarder for slag cementing fluid.
将制得的缓凝剂(命名为H2)加入矿渣固井液配方中,在温度80℃,压力30MPa的稠化条件下进行试验,以验证该缓凝剂的缓凝性能。The prepared retarder (named H2) was added to the slag cementing fluid formula, and the experiment was carried out under the thickening conditions of
矿渣固井液配方:矿渣120份+激活剂10份+悬浮稳定剂1.5份+缓凝剂4份+水100份。Slag cementing fluid formula: 120 parts of slag + 10 parts of activator + 1.5 parts of suspension stabilizer + 4 parts of retarder + 100 parts of water.
注:上述矿渣为提钛尾渣,激活剂为氢氧化钠,悬浮稳定剂为羧甲基纤维素钠。Note: The above slag is titanium extraction tailings, the activator is sodium hydroxide, and the suspension stabilizer is sodium carboxymethyl cellulose.
如图2所示,矿渣固井液的稠化时间在高温高压环境下得到了明显的延长,能够满足油气井固井现场施工对固井液泵注时间的要求,且稠化曲线表明该缓凝剂的加入在高温高压条件下并未出现异常的“鼓包”和“包芯”现象,水泥浆稠度维持在一个比较稳定的值周围,表明该缓凝剂对维持矿渣固井液的沉降稳定性具有良好效果。As shown in Figure 2, the thickening time of slag cementing fluid has been significantly prolonged under high temperature and high pressure environment, which can meet the requirements of oil and gas well cementing site construction for cementing fluid pumping time. The addition of the coagulant does not appear abnormal "bulging" and "core wrapping" phenomena under the conditions of high temperature and high pressure, and the consistency of the cement slurry is maintained at a relatively stable value, indicating that the retarder can maintain the stability of the settlement of the slag cementing fluid. Sex has a good effect.
实施例3Example 3
缓凝剂制备过程:Retarder preparation process:
(1)、A组分的制备:(1) Preparation of component A:
1)在反应容器中将苯乙烯磺酸钠SSS、马来酸MA、甲基丙烯酰氧乙基三甲基氯化铵DMC以质量比为8:5:1的比例混合,溶解在去离子水中,用氢氧化钠调节反应溶液的PH值为7~8;1) In the reaction vessel, mix sodium styrene sulfonate SSS, maleic acid MA, and methacryloyloxyethyltrimethylammonium chloride DMC in a mass ratio of 8:5:1, and dissolve them in deionized water. In water, the pH value of the reaction solution is adjusted with sodium hydroxide to be 7~8;
2)向反应容器中通入10min氮气除氧,待反应体系温度升至70℃时,缓慢加入引发剂过硫酸钾,过硫酸钾的质量为单体总质量的3.0%;2) Pour nitrogen into the reaction vessel for 10 minutes to remove oxygen, and when the temperature of the reaction system rises to 70°C, slowly add initiator potassium persulfate, and the quality of potassium persulfate is 3.0% of the total monomer mass;
3)反应进行4h后,将粘稠液体产物冷却至室温,用丙酮进行提纯、干燥和粉碎,得到缓凝剂组分A;3) After the reaction is carried out for 4 hours, the viscous liquid product is cooled to room temperature, purified with acetone, dried and pulverized to obtain the retarder component A;
(2)、B组分的制备:(2) Preparation of component B:
1)以天然蛭石(VER)为原料,均匀平铺于磁盘上,置于微波炉内,在微波高火的条件下处理 1 min,得到微波膨胀蛭石;1) Using natural vermiculite (VER) as the raw material, evenly spread it on the disk, place it in a microwave oven, and treat it for 1 min under the condition of microwave high fire to obtain microwave-expanded vermiculite;
2)取一定量微波膨胀蛭石粉体,按固液比 1:25加入到2mol/L 盐酸的酸溶液中,在水浴 70℃下磁力搅拌2h;2) Take a certain amount of microwave-expanded vermiculite powder, add it to an acid solution of 2mol/L hydrochloric acid at a solid-to-liquid ratio of 1:25, and stir magnetically for 2h at 70°C in a water bath;
3)搅拌后在自然环境中静置2h,洗涤、抽滤,然后将其放在干燥箱内在 105℃条件下干燥24 h,研磨至 200 目,得到酸改性蛭石粉末即缓凝剂组分B;3) After stirring, let it stand in the natural environment for 2 hours, wash it, filter it with suction, and then put it in a drying oven at 105 °C for 24 hours, and grind it to 200 mesh to obtain acid-modified vermiculite powder, namely the retarder group. point B;
(3)、C组分的制备:(3) Preparation of component C:
酒石酸钠与柠檬酸以80:20的比例混合,得到缓凝剂组分C;Sodium tartrate and citric acid are mixed in a ratio of 80:20 to obtain retarder component C;
(4)、缓凝剂的制备:(4) Preparation of retarder:
A、B、C组分以3:1:1的比例混合,制得矿渣固井液用缓凝剂。The components A, B and C are mixed in a ratio of 3:1:1 to obtain a retarder for slag cementing fluid.
将制得的缓凝剂(命名为H3)加入矿渣固井液配方中,在温度90℃,压力40MPa的稠化条件下进行试验,以验证该缓凝剂的缓凝性能。The prepared retarder (named H3) was added to the slag cementing fluid formula, and the experiment was carried out under the thickening conditions of
矿渣固井液配方:矿渣150份+激活剂10份+悬浮稳定剂2份+缓凝剂6份+水100份。Slag cementing fluid formula: 150 parts of slag + 10 parts of activator + 2 parts of suspension stabilizer + 6 parts of retarder + 100 parts of water.
注:上述矿渣为提钛尾渣,激活剂为氢氧化钠,悬浮稳定剂为羧甲基纤维素钠。Note: The above slag is titanium extraction tailings, the activator is sodium hydroxide, and the suspension stabilizer is sodium carboxymethyl cellulose.
如图3所示,矿渣固井液的稠化时间在高温高压环境下得到了明显的延长,能够满足油气井固井现场施工对固井液泵注时间的要求,且稠化曲线表明该缓凝剂的加入在高温高压条件下并未出现异常的“鼓包”和“包芯”现象,水泥浆稠度维持在一个比较稳定的值周围,表明该缓凝剂对维持矿渣固井液的沉降稳定性具有良好效果。As shown in Figure 3, the thickening time of slag cementing fluid has been significantly prolonged under high temperature and high pressure environment, which can meet the requirements of oil and gas well cementing site construction for cementing fluid pumping time. The addition of the coagulant does not appear abnormal "bulging" and "core wrapping" phenomena under the conditions of high temperature and high pressure, and the consistency of the cement slurry is maintained at a relatively stable value, indicating that the retarder can maintain the stability of the settlement of the slag cementing fluid. Sex has a good effect.
如图1-图3所示,矿渣固井液的稠化时间均得到了明显的延长,稠度未发生下降明显的现象,能够满足固井现场施工要求,且稠化曲线表明该缓凝剂适用于矿渣固井液,能避免和解决稳定性差、沉降严重的问题。As shown in Figure 1-Figure 3, the thickening time of slag cementing fluid has been significantly prolonged, and the consistency has not decreased significantly, which can meet the construction requirements of the cementing site, and the thickening curve shows that the retarder is suitable for For slag cementing fluid, it can avoid and solve the problems of poor stability and serious settlement.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011411704.XA CN112480889B (en) | 2020-12-04 | 2020-12-04 | Preparation method of retarder for slag cementing fluid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011411704.XA CN112480889B (en) | 2020-12-04 | 2020-12-04 | Preparation method of retarder for slag cementing fluid |
Publications (2)
Publication Number | Publication Date |
---|---|
CN112480889A CN112480889A (en) | 2021-03-12 |
CN112480889B true CN112480889B (en) | 2022-09-20 |
Family
ID=74939798
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202011411704.XA Active CN112480889B (en) | 2020-12-04 | 2020-12-04 | Preparation method of retarder for slag cementing fluid |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112480889B (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106632842B (en) * | 2015-10-30 | 2020-07-14 | 中石化石油工程技术服务有限公司 | Preparation method and application method of oil well cement retarder |
US11028311B2 (en) * | 2019-04-26 | 2021-06-08 | Baker Hughes Oilfield Operations Llc | Methods of cementing a wellbore |
-
2020
- 2020-12-04 CN CN202011411704.XA patent/CN112480889B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN112480889A (en) | 2021-03-12 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6209646B1 (en) | Controlling the release of chemical additives in well treating fluids | |
CN101857799B (en) | Curable leaking stoppage spacer fluid and preparation method thereof | |
CN102191027B (en) | High-temperature-resistant dispersed fluid loss agent for oil well cement and preparation method thereof | |
CN103740340B (en) | Expansion consolidation type plugging agent | |
CN102443383A (en) | High-water-loss, hardenable and plugging agent | |
CN115466603B (en) | A kind of anti-240 ℃ anti-salt plugging type water-based drilling fluid and its preparation method and application | |
CN105802596B (en) | A kind of early strong low hydration heat mortar architecture suitable for deep water shallow cementing | |
CN105176505A (en) | Well cementing cement slurry stabilizer, preparation method and applications thereof | |
CN114716984A (en) | Cementing and plugging type wall fixing agent for water-based drilling fluid and preparation method and application thereof | |
MX2013012179A (en) | Use of methylhydroxyethyl cellulose as cement additive. | |
CN106167695B (en) | Oil well chemical plugging agent | |
CN112480889B (en) | Preparation method of retarder for slag cementing fluid | |
CN112300346B (en) | Amphoteric ion grafted copolymer fluid loss agent and preparation method and application thereof | |
CN103319650A (en) | Phosphoaluminate cement system fluid loss additive and preparation method thereof | |
CN105567196A (en) | Toughness enhancing latex additive with weak slow setting and water loss controlling effects and preparation method of latex additive | |
CN101240163A (en) | Oil well cement swelling agent | |
CN102863593B (en) | Sludge cake curing agent, and preparation and application method thereof | |
CN104045271A (en) | Plugging agent for oil field or natural gas extraction and preparation method thereof | |
CN104152136B (en) | Method for preparing ultra-low-density fracturing and propping agent by using white clay | |
CN115074097B (en) | A fluid capable of deep profile control inorganic particle gel and its preparation method and application | |
CN101462851B (en) | Retardation cement mortar | |
CN106967397B (en) | A thermal viscosification and settlement stabilizer suitable for oil well cement slurry, its preparation method and application | |
CN106517852B (en) | A kind of modified aluminate cement retarder and preparation method thereof of the pre- aluminum ions AMPS copolymer of chelating and borate compounding | |
CN104946215A (en) | Method for preparing drilling fluid using guar gum fracturing fluid waste water | |
CN104293327A (en) | Novel drilling fluid for exploring oil shale |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |