CN110157403A - A low-permeability oil displacement agent - Google Patents
A low-permeability oil displacement agent Download PDFInfo
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- CN110157403A CN110157403A CN201910379995.XA CN201910379995A CN110157403A CN 110157403 A CN110157403 A CN 110157403A CN 201910379995 A CN201910379995 A CN 201910379995A CN 110157403 A CN110157403 A CN 110157403A
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- 238000006073 displacement reaction Methods 0.000 title claims abstract description 47
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 47
- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 38
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 38
- 239000003093 cationic surfactant Substances 0.000 claims abstract description 13
- AISMNBXOJRHCIA-UHFFFAOYSA-N trimethylazanium;bromide Chemical compound Br.CN(C)C AISMNBXOJRHCIA-UHFFFAOYSA-N 0.000 claims abstract description 11
- 150000001875 compounds Chemical class 0.000 claims abstract description 5
- 235000019422 polyvinyl alcohol Nutrition 0.000 claims abstract 10
- 239000004698 Polyethylene Substances 0.000 claims abstract 4
- -1 poly ethylene Polymers 0.000 claims abstract 4
- 229920000573 polyethylene Polymers 0.000 claims abstract 4
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical group [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 9
- 238000013329 compounding Methods 0.000 claims description 7
- 125000001165 hydrophobic group Chemical group 0.000 claims description 3
- CPELXLSAUQHCOX-UHFFFAOYSA-M Bromide Chemical compound [Br-] CPELXLSAUQHCOX-UHFFFAOYSA-M 0.000 claims description 2
- HNTGIJLWHDPAFN-UHFFFAOYSA-N 1-bromohexadecane Chemical compound CCCCCCCCCCCCCCCCBr HNTGIJLWHDPAFN-UHFFFAOYSA-N 0.000 claims 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 claims 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims 1
- 239000000654 additive Substances 0.000 claims 1
- 230000000996 additive effect Effects 0.000 claims 1
- 239000003921 oil Substances 0.000 description 51
- 238000011084 recovery Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 230000035699 permeability Effects 0.000 description 12
- 239000004094 surface-active agent Substances 0.000 description 9
- 238000004945 emulsification Methods 0.000 description 8
- 239000000839 emulsion Substances 0.000 description 8
- 239000010779 crude oil Substances 0.000 description 7
- 230000001804 emulsifying effect Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000003607 modifier Substances 0.000 description 5
- 238000011161 development Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- LWBFNUKTNRHYKJ-UHFFFAOYSA-N Br.CCCCCCCCCCCCCCCC Chemical compound Br.CCCCCCCCCCCCCCCC LWBFNUKTNRHYKJ-UHFFFAOYSA-N 0.000 description 3
- 239000008398 formation water Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 230000002269 spontaneous effect Effects 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 1
- SWLVFNYSXGMGBS-UHFFFAOYSA-N ammonium bromide Chemical compound [NH4+].[Br-] SWLVFNYSXGMGBS-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 125000001273 sulfonato group Chemical class [O-]S(*)(=O)=O 0.000 description 1
- PUVAFTRIIUSGLK-UHFFFAOYSA-M trimethyl(oxiran-2-ylmethyl)azanium;chloride Chemical compound [Cl-].C[N+](C)(C)CC1CO1 PUVAFTRIIUSGLK-UHFFFAOYSA-M 0.000 description 1
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- 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
- C09K8/58—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
- C09K8/584—Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
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Abstract
Description
技术领域technical field
本发明涉及一种驱油组合物,尤其涉及一种适用于低渗透油藏的驱油组合物,属于油藏开采技术领域。The invention relates to an oil-displacement composition, in particular to an oil-displacement composition suitable for low-permeability reservoirs, and belongs to the technical field of reservoir exploitation.
背景技术Background technique
21世纪以来,伴随国民经济的快速增长,世界各国对石油的需求量急剧攀升。以低渗透、特低渗透油藏为代表的复杂油藏已成为我国石油资源产量接替的重要组成部分,在今后相当一段时期内将是我国石油工业增储上产的重要资源基础。Since the 21st century, with the rapid growth of the national economy, the demand for oil in countries around the world has risen sharply. Complex oil reservoirs represented by low-permeability and ultra-low-permeability reservoirs have become an important part of my country's oil resource output replacement, and will be an important resource base for my country's oil industry to increase reserves and production for a considerable period of time in the future.
低渗透油藏目前面临诸多问题,同中高渗储层相比,低渗透油田在开发效果上有很大差异。我国大部分低渗油藏采用注水开发的方式。但是由于低孔低渗,在开发过程中普遍存在注水压力高“注不进、采不出”的现象,最终导致油田采收率较低。此外,我国部分油田位处西北地区,水资源匮乏,不利于注水开发的实施。Low permeability reservoirs are currently facing many problems. Compared with medium and high permeability reservoirs, the development effect of low permeability oilfields is quite different. Most low-permeability reservoirs in my country are developed by waterflooding. However, due to low porosity and low permeability, the phenomenon of high water injection pressure and "no injection or production" is common in the development process, which ultimately leads to low oil recovery. In addition, some oilfields in my country are located in the northwest region, and water resources are scarce, which is not conducive to the implementation of water flooding development.
表面活性剂由于具有低界面张力、乳化原油、改变润湿性等一系列性能,可以有效降压增注,启动低渗基质里的剩余油,在特低渗低渗油藏开发过程中具有巨大的应用前景。据统计,世界上80%的原油是以乳状液形式采出的,近年来室内研究及现场实践表明,在低渗油藏中,表面活性剂的乳化作用对采收率的贡献率大于其界面活性对采收率的贡献率。Surfactants have a series of properties such as low interfacial tension, emulsifying crude oil, and changing wettability, which can effectively reduce pressure and increase injection, start the remaining oil in low-permeability matrix, and play a huge role in the development of ultra-low permeability and low permeability reservoirs. application prospects. According to statistics, 80% of the world's crude oil is produced in the form of emulsion. In recent years, laboratory research and field practice have shown that in low-permeability reservoirs, the contribution rate of surfactant emulsification to recovery is greater than that of its interface. Contribution rate of activity to recovery factor.
目前现场应用的乳化效果较好的表面活性剂为OP系列和石油磺酸盐系列。但他们分别有污染环境、耐温性差的缺点。At present, the surfactants with good emulsifying effect in field application are OP series and petroleum sulfonate series. However, they have the disadvantages of polluting the environment and poor temperature resistance.
因此针对低渗透油藏常规表面活性剂驱用量大、耐温性能差、乳液稳定性差的状况,有必要提供一种在较低粘度下具有优秀乳化性能,可在低渗储层中自发形成较为稳定的乳状液,进一步提高低渗透油藏的采收率的自乳化驱油体系。Therefore, it is necessary to provide a low-permeability reservoir with excellent emulsifying performance at a low viscosity, which can spontaneously form a relatively low-permeability reservoir. Stable emulsion, a self-emulsification flooding system that further improves the recovery of low-permeability reservoirs.
发明内容Contents of the invention
为了解决上述技术问题,本发明的目的在于提供一种驱油效果良好的表面活性剂驱油剂。In order to solve the above technical problems, the object of the present invention is to provide a surfactant oil displacement agent with good oil displacement effect.
为了实现上述技术目的,本发明提供了一种低渗透油藏(渗透率小于50mD)驱油剂,该低渗透油藏驱油剂是由改性聚乙烯醇和C12-C18的三甲基溴化铵阳离子表面活性剂复配而成;其中,改性聚乙烯醇与C12-C18的三甲基溴化铵阳离子表面活性剂的复配质量比为1:9-9:1。In order to achieve the above-mentioned technical purpose, the present invention provides a kind of low permeability reservoir (permeability is less than 50mD) oil displacement agent, this low permeability reservoir oil displacement agent is made of modified polyvinyl alcohol and C12-C18 trimethyl bromide Ammonium cationic surfactant is compounded; wherein, the compounding mass ratio of modified polyvinyl alcohol and C12-C18 trimethylammonium bromide cationic surfactant is 1:9-9:1.
在本发明的低渗透油藏驱油剂中,采用的改性聚乙烯醇是对本身无疏水性能的聚乙烯醇进行疏水改性,构筑一种既具有亲水基团同时又具有疏水基团的高分子表面活性剂。改性获得的高分子表面活性剂的用量少,分子量大具有良好的分散油滴性能。更为经济友好。In the low-permeability reservoir oil displacement agent of the present invention, the modified polyvinyl alcohol used is to hydrophobically modify the polyvinyl alcohol itself without hydrophobic properties, to construct a kind of polyvinyl alcohol with both hydrophilic groups and hydrophobic groups. polymeric surfactants. The polymer surfactant obtained by modification has a small dosage, high molecular weight and good performance of dispersing oil droplets. More economically friendly.
本发明的低渗透油藏驱油剂采用的高分子表面活性剂为改性聚乙烯醇,通过改性聚乙烯醇与C12-C18的三甲基溴化铵阳离子表面活性剂的协同作用,使得到的复配物具有自乳化驱油性能,无需外力即可自发乳化。The macromolecular surfactant adopted in the low-permeability reservoir oil displacement agent of the present invention is modified polyvinyl alcohol, and through the synergistic effect of modified polyvinyl alcohol and C12-C18 trimethylammonium bromide cationic surfactant, the The obtained compound has self-emulsifying oil displacement performance and can be emulsified spontaneously without external force.
在本发明的一具体实施方式中,改性聚乙烯醇和C12-C18的三甲基溴化铵阳离子表面活性剂的复配质量比为1:9、3:7、5:5、7:3或9:1。In a specific embodiment of the present invention, the compounding mass ratio of the trimethylammonium bromide cationic surfactant of modified polyvinyl alcohol and C12-C18 is 1:9, 3:7, 5:5, 7:3 or 9:1.
在本发明的一具体实施方式中,采用的C12-C18的三甲基溴化铵阳离子表面活性剂为十六烷基三甲基溴化铵。In a specific embodiment of the present invention, the C12-C18 trimethylammonium bromide cationic surfactant used is cetyltrimethylammonium bromide.
即,该低渗透油藏驱油剂是由改性聚乙烯醇和十六烷基三甲基溴化铵复配而成;其中,改性聚乙烯醇和十六烷基三甲基溴化铵的复配质量比可以为1:9-9:1。That is, the low-permeability reservoir oil displacement agent is compounded by modified polyvinyl alcohol and cetyl trimethyl ammonium bromide; wherein, the modified polyvinyl alcohol and cetyl trimethyl ammonium bromide The compounding mass ratio can be 1:9-9:1.
在本发明的一具体实施方式中,采用的改性聚乙烯醇的分子量为2000-3000。该分子量的改性聚乙烯醇具有较好的油滴分散性能以及乳化性能。比如,采用的改性聚乙烯醇的分子量可以为2200。In a specific embodiment of the present invention, the molecular weight of the modified polyvinyl alcohol used is 2000-3000. The modified polyvinyl alcohol with this molecular weight has better oil drop dispersing performance and emulsifying performance. For example, the molecular weight of the modified polyvinyl alcohol used can be 2200.
在本发明的一具体实施方式中,改性聚乙烯醇同时具有疏水基团和亲水基团。In a specific embodiment of the present invention, the modified polyvinyl alcohol has both hydrophobic groups and hydrophilic groups.
在本发明的一具体实施方式中,改性聚乙烯醇是由改性剂对聚乙烯醇进行疏水改性得到的。In a specific embodiment of the present invention, the modified polyvinyl alcohol is obtained by hydrophobically modifying polyvinyl alcohol with a modifier.
比如,采用的改性剂可以为溴代十六烷或2,3-环氧丙基三甲基氯化铵。For example, the modifier used may be hexadecane bromide or 2,3-epoxypropyltrimethylammonium chloride.
优选地,采用的改性剂为溴代十六烷。即改性聚乙烯醇是由溴代十六烷改性聚乙烯醇得到的。该改性聚乙烯醇的结构式如下式所示:Preferably, the modifier used is hexadecane bromide. That is, the modified polyvinyl alcohol is obtained by modifying polyvinyl alcohol with hexadecane bromide. The structural formula of this modified polyvinyl alcohol is as shown in the following formula:
其中,x≥1的整数,y≥1的整数,m≥1的整数,n≥1的整数,40≤x+y+m+n≤70。Wherein, an integer of x≥1, an integer of y≥1, an integer of m≥1, an integer of n≥1, 40≤x+y+m+n≤70.
在本发明的一具体实施方式中,改性剂的用量为聚乙烯醇的质量的12.5%-17.5%。比如,改性剂的用量为聚乙烯醇的质量的13%、14%、15%、16%和17%。In a specific embodiment of the present invention, the amount of modifier used is 12.5%-17.5% of the mass of polyvinyl alcohol. For example, the amount of modifier used is 13%, 14%, 15%, 16% and 17% of the mass of polyvinyl alcohol.
在本发明的一具体实施方式中,改性聚乙烯醇是通过以下步骤制备得到的:In a specific embodiment of the present invention, modified polyvinyl alcohol is prepared through the following steps:
在55℃-75℃下,将改性剂与聚乙烯醇混合,反应40h-50h(优选48h),得到改性聚乙烯醇。Mix the modifying agent with polyvinyl alcohol at 55°C-75°C, and react for 40h-50h (preferably 48h) to obtain modified polyvinyl alcohol.
在本发明的低渗透油藏驱油剂中,以C12-C18的三甲基溴化铵阳离子表面活性剂,与改性聚乙烯醇复配。CTAB是油田现场及实验室研究中常见的化学试剂,对于其在石油领域的应用已经有足够的研究支撑。此外CTAB具有16碳链的结构同改性聚乙烯醇的疏水部分相似,因而具有一定的协同效应,有利于自发乳化的发生。In the low-permeability reservoir oil displacement agent of the present invention, C12-C18 trimethylammonium bromide cationic surfactant is compounded with modified polyvinyl alcohol. CTAB is a common chemical reagent in oilfield field and laboratory research, and there is enough research support for its application in the petroleum field. In addition, CTAB has a 16-carbon chain structure similar to the hydrophobic part of modified polyvinyl alcohol, so it has a certain synergistic effect, which is conducive to the occurrence of spontaneous emulsification.
本发明的低渗透油藏驱油剂在具体用于乳化低渗透油藏时,按照本领域常规的驱油剂实施方式进行实施即可。其中,该低渗透油藏驱油剂的添加量为3000mg/L。When the oil displacement agent for low-permeability oil reservoirs of the present invention is specifically used for emulsifying low-permeability oil reservoirs, it can be implemented according to the conventional implementation methods of oil displacement agents in the field. Wherein, the addition amount of the low-permeability reservoir oil displacement agent is 3000mg/L.
本发明的低渗透油藏驱油剂可以通过以下步骤制备得到:The low-permeability reservoir oil displacement agent of the present invention can be prepared through the following steps:
向模拟地层水中加入改性聚乙烯醇和C12-C18的三甲基溴化铵阳离子表面活性剂,混合搅拌30min,静置,得到低渗透油藏驱油剂。Add modified polyvinyl alcohol and C12-C18 trimethylammonium bromide cationic surfactant to the simulated formation water, mix and stir for 30 minutes, and let stand to obtain a low-permeability reservoir oil displacement agent.
本发明的低渗透油藏驱油剂的原料来源广,价格便宜,并且可同低渗透油藏自发形成乳化驱油体系。The low-permeability reservoir oil-displacing agent of the invention has wide sources of raw materials and is cheap, and can spontaneously form an emulsified oil-displacement system with the low-permeability reservoir.
本发明的低渗透油藏驱油剂的物理模拟驱油效果良好,能够在低渗透岩心常规水驱后进一步提高原油采收率,采收率可以提高60%左右。The physical simulation oil displacement effect of the low-permeability reservoir oil displacement agent of the present invention is good, and the oil recovery rate can be further improved after conventional water flooding of the low-permeability rock core, and the recovery rate can be increased by about 60%.
本发明的低渗透油藏驱油剂是一种自乳化驱油体系,无需外力即可自发乳化,为筛选适宜油田的提高采收率方法提供了依据。The low-permeability reservoir oil displacement agent of the present invention is a self-emulsification oil displacement system, which can be emulsified spontaneously without external force, and provides a basis for screening suitable methods for enhancing oil recovery in oil fields.
附图说明Description of drawings
图1为实施例1中的低渗透油藏驱油剂的界面张力随复配比例变化曲线。Fig. 1 is the variation curve of the interfacial tension of the low-permeability reservoir oil-displacing agent in Example 1 as a function of the compounding ratio.
具体实施方式Detailed ways
为了对本发明的技术特征、目的和有益效果有更加清楚的理解,现对本发明的技术方案进行以下详细说明,但不能理解为对本发明的可实施范围的限定。In order to have a clearer understanding of the technical features, purposes and beneficial effects of the present invention, the technical solution of the present invention is described in detail below, but it should not be construed as limiting the scope of implementation of the present invention.
实施例1Example 1
本实施例提供了一种低渗透油藏自乳化驱油剂,其是通过以下步骤制备得到的:This embodiment provides a self-emulsifying oil displacement agent for low permeability reservoirs, which is prepared through the following steps:
使用模拟地层水配制自乳化驱油体系,总浓度为3000mg/L,其中,改性PVA-1570(分子量为2200)(由溴代十六烷改性聚乙烯醇得到的)浓度为2100mg/L,CTAB(十六烷基三甲基溴化铵)浓度为900mg/L,搅拌30min,静置,得到自乳化高分子复合驱油剂。Use simulated formation water to prepare self-emulsification oil displacement system, the total concentration is 3000mg/L, among which, the concentration of modified PVA-1570 (molecular weight is 2200) (obtained from bromide cetane modified polyvinyl alcohol) is 2100mg/L , the CTAB (cetyltrimethylammonium bromide) concentration was 900mg/L, stirred for 30min, and left to stand to obtain a self-emulsifying polymer composite oil displacement agent.
对本实施例的上述驱油剂进行表面张力测试。仪器采用TX-500C界面张力仪,油相采用某油田脱气脱水原油,水相为该油田实际地层水。测试温度为45℃,在5000转/分钟的条件下测定油水界面张力。结果显示,当复配质量比为7:3时体系具备自乳化性能,且乳液稳定性良好。A surface tension test was performed on the above-mentioned oil displacing agent of this embodiment. The instrument uses TX-500C interfacial tensiometer, the oil phase is degassed and dehydrated crude oil from an oilfield, and the water phase is the actual formation water of the oilfield. The test temperature is 45°C, and the oil-water interfacial tension is measured under the condition of 5000 rpm. The results showed that when the compounding mass ratio was 7:3, the system had self-emulsifying properties, and the emulsion stability was good.
由图1可以看出,改性PVA-1570、CTAB的复配体系分别在质量比为9:1、7:3时达到低界面张力状态(≤10-2mN/m)。It can be seen from Figure 1 that the compound system of modified PVA-1570 and CTAB reaches a state of low interfacial tension (≤10 -2 mN/m) when the mass ratio is 9:1 and 7:3 respectively.
将本实施例的驱油剂进行性能测试,结果如表1所示。The performance test of the oil displacement agent of this embodiment is shown in Table 1.
表1Table 1
由表1可以看出,该自乳化体系虽为高分子表面活性剂复配体系,但体系粘度极低,近似于水的粘度。过高的粘度会使化学剂在低渗透油藏中驱替困难,出现地层堵塞等现象。而该体系粘度低,更有利于其在低渗透油藏提高采收率中的应用。It can be seen from Table 1 that although the self-emulsifying system is a compound system of polymer surfactant, the viscosity of the system is extremely low, which is close to the viscosity of water. Excessively high viscosity will make it difficult for chemical agents to displace in low-permeability reservoirs, resulting in formation plugging and other phenomena. The low viscosity of the system is more conducive to its application in enhanced oil recovery of low permeability reservoirs.
利用自乳化驱油体系进行岩心驱替实验,岩心长度10.0cm,渗透率15mD,饱和水18mL,后饱和油10mL。进行水驱-化学驱-水驱,采收率如表2。The self-emulsification flooding system was used to carry out the core displacement experiment, the core length was 10.0cm, the permeability was 15mD, the saturated water was 18mL, and the post-saturated oil was 10mL. After water flooding-chemical flooding-water flooding, the recovery factors are shown in Table 2.
表2Table 2
由表2可以看出,该自乳化驱油剂具有低界面张力,高乳液稳定时间,并且自发与原油乳化,提高油水混合能力。可以看出本实施例的自乳化驱油剂可以明显提高采收率。首先对含油低渗透岩心进行水驱,采收率是41%,然后进行自乳化驱(即三次采油)此时可以把采收率提高12%,后续再进行二次水驱,提高采收率3%。总采收率为56%。It can be seen from Table 2 that the self-emulsifying oil displacement agent has low interfacial tension, high emulsion stability time, and spontaneously emulsifies with crude oil, improving the oil-water mixing ability. It can be seen that the self-emulsifying oil displacement agent of this example can significantly increase the recovery factor. First, carry out water flooding on the oil-bearing low-permeability core, and the recovery rate is 41%, and then carry out self-emulsification flooding (that is, tertiary oil recovery). At this time, the recovery rate can be increased by 12%, and then the secondary water flooding is carried out to increase the recovery rate 3%. The total recovery rate is 56%.
当本实施例的驱油剂用量为3000mg/L时,当NaCl浓度为10000-20000mg/L时,自发乳化效果最好,油样加入瞬间即可自发进入水相,形成乳状液。乳状液稳定性强,静置30min后依然保持较好乳化效果。When the amount of oil displacing agent used in this example is 3000mg/L, when the NaCl concentration is 10000-20000mg/L, the spontaneous emulsification effect is the best, and the oil sample can spontaneously enter the water phase immediately after adding, forming an emulsion. The emulsion has strong stability, and it still maintains a good emulsifying effect after standing for 30 minutes.
用移液枪将本实施例的驱油剂溶液置于试管中,并于45℃恒温箱中静置2h。后将试管取出,用移液枪取45℃恒温原油(水油比9:1),距离试管1cm处悬空滴加原油,观察原油滴加后试管内溶液的变化情况。油滴自发进入水相,形成乳液,说明乳化剂具有自发乳化性能。Put the oil displacing agent solution of this example into a test tube with a pipette gun, and let it stand in a thermostat at 45° C. for 2 hours. Finally, take out the test tube, use a pipette gun to take crude oil at a constant temperature of 45°C (water-oil ratio 9:1), add crude oil dropwise at a distance of 1 cm from the test tube, and observe the change of the solution in the test tube after the crude oil is added dropwise. The oil droplets spontaneously entered the water phase to form an emulsion, which indicated that the emulsifier had spontaneous emulsifying properties.
以上实施例说明,本发明的低渗透油藏驱油剂对于低渗透油藏具有更好的提高采收率效果。此外,驱替过程中可以明显看到采出液以乳液形式存在,从而扩展其应用范围,提供了一种可以将高分子表面活性剂用于低渗油藏三次采油的新思路。The above examples illustrate that the oil displacement agent for low-permeability reservoirs of the present invention has a better effect of enhancing oil recovery for low-permeability reservoirs. In addition, it can be clearly seen that the produced fluid exists in the form of emulsion during the displacement process, thereby expanding its application range and providing a new idea for using polymer surfactants in low-permeability reservoirs for tertiary oil recovery.
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Citations (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4545911A (en) * | 1982-04-30 | 1985-10-08 | Mobil Oil Corporation | Polymeric pyrrolidinium methanesulfonate viscosifiers for aqueous fluids |
US4609708A (en) * | 1982-04-30 | 1986-09-02 | Mobil Oil Corporation | Method for manufacture of polymeric pyrrolidinium methanesulfonate viscosifiers |
US5100952A (en) * | 1989-05-11 | 1992-03-31 | Mobil Oil Corporation | Organically crosslinked polyvinyl alcohol copolymeric gels for use under harsh reservoir conditions |
CN1615392A (en) * | 2001-12-21 | 2005-05-11 | 罗狄亚化学公司 | Use of charged amphiphilic statistic polymers for thickening phases comprising giant micelles of surfactants and aqueous compositions comprising same |
US20050230112A1 (en) * | 2004-04-19 | 2005-10-20 | Reddy B R | Sealant compositions comprising colloidally stabilized latex and methods of using the same |
CN101314710A (en) * | 2008-07-18 | 2008-12-03 | 中国石油大学(华东) | Foam regulating and displacing agent, oil displacement system and oil displacement method |
CN101927139A (en) * | 2010-07-12 | 2010-12-29 | 孙安顺 | Self-emulsifier and use thereof in tertiary oil recovery |
CN102286273A (en) * | 2011-09-05 | 2011-12-21 | 中国石油大学(华东) | Oil-in-water emulsifier as well as preparation and use methods thereof |
CN103525886A (en) * | 2013-10-11 | 2014-01-22 | 北京国海能源技术研究院 | Clean type liquid guanidine gum and preparation method thereof |
CN103834379A (en) * | 2014-01-03 | 2014-06-04 | 中国石油大学(华东) | Wormlike micelle foam system and method for enhancing oil recovery by using same |
CN104080960A (en) * | 2011-12-28 | 2014-10-01 | 普拉德研究及开发股份有限公司 | Multicomponent degradable materials and use |
CN104498016A (en) * | 2014-12-17 | 2015-04-08 | 唐山冀油瑞丰化工有限公司 | Foam agent used in carbon-dioxide flooding and preparation method of foam agent |
CN104694103A (en) * | 2013-12-09 | 2015-06-10 | 青岛惠城石化科技有限公司 | A Surfactant Compound System with Reservoir Adaptability |
CN105331348A (en) * | 2015-12-04 | 2016-02-17 | 西安石油大学 | Homogeneous-phase microemulsion oil-displacing agent applied to low-permeation oil field and preparation method of homogeneous-phase microemulsion oil-displacing agent |
CN105331347A (en) * | 2015-11-16 | 2016-02-17 | 厦门大学 | Modified PVA polyvinyl alcohol polymer surfactant for displacement of reservoir oil |
CN105368430A (en) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | Oil-displacing agent, preparing method of oil-displacing agent and intensified oil production method |
CN106398675A (en) * | 2015-07-30 | 2017-02-15 | 中国石油化工股份有限公司 | Emulsification viscosity reduction agent, preparation method and applications thereof, and thick oil emulsification viscosity reduction method |
CN106634924A (en) * | 2016-12-21 | 2017-05-10 | 中国石油大学(华东) | Nanometer fluid for compact oil reservoir imbibition oil discharging and preparation method thereof |
CN106867496A (en) * | 2015-12-14 | 2017-06-20 | 中国石油化工股份有限公司 | Online injection type oil displacement agent containing hydrophobic associated polymer emulsion and preparation method thereof |
CN108179023A (en) * | 2017-12-07 | 2018-06-19 | 中海油天津化工研究设计院有限公司 | A kind of viscous crude Produced Liquid reverse-phase emulsifier and preparation method thereof |
CN108192586A (en) * | 2018-01-12 | 2018-06-22 | 中国石油大学(华东) | A kind of betaine type amphipathic polymer supermolecule oil displacement system and its construction method |
CN109142640A (en) * | 2018-09-28 | 2019-01-04 | 中国石油大学(北京) | A kind of self-emulsifying screening technique of low-permeability oil deposit self-emulsifying oil displacement system |
CN109354648A (en) * | 2018-10-23 | 2019-02-19 | 安徽天润化学工业股份有限公司 | A kind of soluble salt viscosity amphiphilic polymer oil displacing agent and preparation method thereof |
CN109652048A (en) * | 2018-12-28 | 2019-04-19 | 中国石油大学(北京) | A kind of compound oil displacement agent and its preparation method and application |
-
2019
- 2019-05-08 CN CN201910379995.XA patent/CN110157403B/en active Active
Patent Citations (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4609708A (en) * | 1982-04-30 | 1986-09-02 | Mobil Oil Corporation | Method for manufacture of polymeric pyrrolidinium methanesulfonate viscosifiers |
US4545911A (en) * | 1982-04-30 | 1985-10-08 | Mobil Oil Corporation | Polymeric pyrrolidinium methanesulfonate viscosifiers for aqueous fluids |
US5100952A (en) * | 1989-05-11 | 1992-03-31 | Mobil Oil Corporation | Organically crosslinked polyvinyl alcohol copolymeric gels for use under harsh reservoir conditions |
CN1615392A (en) * | 2001-12-21 | 2005-05-11 | 罗狄亚化学公司 | Use of charged amphiphilic statistic polymers for thickening phases comprising giant micelles of surfactants and aqueous compositions comprising same |
US20050230112A1 (en) * | 2004-04-19 | 2005-10-20 | Reddy B R | Sealant compositions comprising colloidally stabilized latex and methods of using the same |
CN101314710A (en) * | 2008-07-18 | 2008-12-03 | 中国石油大学(华东) | Foam regulating and displacing agent, oil displacement system and oil displacement method |
CN101927139A (en) * | 2010-07-12 | 2010-12-29 | 孙安顺 | Self-emulsifier and use thereof in tertiary oil recovery |
CN102286273A (en) * | 2011-09-05 | 2011-12-21 | 中国石油大学(华东) | Oil-in-water emulsifier as well as preparation and use methods thereof |
CN104080960A (en) * | 2011-12-28 | 2014-10-01 | 普拉德研究及开发股份有限公司 | Multicomponent degradable materials and use |
CN103525886A (en) * | 2013-10-11 | 2014-01-22 | 北京国海能源技术研究院 | Clean type liquid guanidine gum and preparation method thereof |
CN104694103A (en) * | 2013-12-09 | 2015-06-10 | 青岛惠城石化科技有限公司 | A Surfactant Compound System with Reservoir Adaptability |
CN103834379A (en) * | 2014-01-03 | 2014-06-04 | 中国石油大学(华东) | Wormlike micelle foam system and method for enhancing oil recovery by using same |
CN105368430A (en) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | Oil-displacing agent, preparing method of oil-displacing agent and intensified oil production method |
CN104498016A (en) * | 2014-12-17 | 2015-04-08 | 唐山冀油瑞丰化工有限公司 | Foam agent used in carbon-dioxide flooding and preparation method of foam agent |
CN106398675A (en) * | 2015-07-30 | 2017-02-15 | 中国石油化工股份有限公司 | Emulsification viscosity reduction agent, preparation method and applications thereof, and thick oil emulsification viscosity reduction method |
CN105331347A (en) * | 2015-11-16 | 2016-02-17 | 厦门大学 | Modified PVA polyvinyl alcohol polymer surfactant for displacement of reservoir oil |
CN105331348A (en) * | 2015-12-04 | 2016-02-17 | 西安石油大学 | Homogeneous-phase microemulsion oil-displacing agent applied to low-permeation oil field and preparation method of homogeneous-phase microemulsion oil-displacing agent |
CN106867496A (en) * | 2015-12-14 | 2017-06-20 | 中国石油化工股份有限公司 | Online injection type oil displacement agent containing hydrophobic associated polymer emulsion and preparation method thereof |
CN106634924A (en) * | 2016-12-21 | 2017-05-10 | 中国石油大学(华东) | Nanometer fluid for compact oil reservoir imbibition oil discharging and preparation method thereof |
CN108179023A (en) * | 2017-12-07 | 2018-06-19 | 中海油天津化工研究设计院有限公司 | A kind of viscous crude Produced Liquid reverse-phase emulsifier and preparation method thereof |
CN108192586A (en) * | 2018-01-12 | 2018-06-22 | 中国石油大学(华东) | A kind of betaine type amphipathic polymer supermolecule oil displacement system and its construction method |
CN109142640A (en) * | 2018-09-28 | 2019-01-04 | 中国石油大学(北京) | A kind of self-emulsifying screening technique of low-permeability oil deposit self-emulsifying oil displacement system |
CN109354648A (en) * | 2018-10-23 | 2019-02-19 | 安徽天润化学工业股份有限公司 | A kind of soluble salt viscosity amphiphilic polymer oil displacing agent and preparation method thereof |
CN109652048A (en) * | 2018-12-28 | 2019-04-19 | 中国石油大学(北京) | A kind of compound oil displacement agent and its preparation method and application |
Non-Patent Citations (13)
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN116082539A (en) * | 2021-11-05 | 2023-05-09 | 中国石油天然气集团有限公司 | A kind of anti-high temperature modified polyvinyl alcohol and its preparation method and application |
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