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CN105349130B - It is suitable for the diutan and surfactant composite oil-displacing system of high temperature and high salt oil deposit - Google Patents

It is suitable for the diutan and surfactant composite oil-displacing system of high temperature and high salt oil deposit Download PDF

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CN105349130B
CN105349130B CN201510925450.6A CN201510925450A CN105349130B CN 105349130 B CN105349130 B CN 105349130B CN 201510925450 A CN201510925450 A CN 201510925450A CN 105349130 B CN105349130 B CN 105349130B
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oil
diutan
gum
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宫厚健
徐龙
董明哲
李亚军
桑茜
朱腾
李康宁
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China University of Petroleum East China
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Abstract

本发明公开了一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.1%‑0.5%,表面活性剂0.05%‑0.6%,其余为矿化水。本发明还公开了一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系的制备方法,步骤包括:按配比取各组分,常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下加入表面活性剂和定优胶,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。本发明中定优胶与非离子和两性离子表面活性剂都具有较好的配伍性,既能保持驱替液的洗油能力,又能大幅度的增大波及体积,进而提高原油采收率。

The invention discloses a compound oil displacement system of diyou gum and a surfactant suitable for high-temperature and high-salt oil reservoirs, which is composed of the following components in mass percentage: 0.1%-0.5% of diyou gum and 0.05%-surfactant 0.6%, the rest is mineralized water. The invention also discloses a preparation method of the compound oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt reservoirs. The steps include: taking each component according to the proportion, and mixing NaCl , CaCl Add in water and stir evenly to prepare mineralized water, then add surfactant and diuterene at normal temperature, stir evenly, and then get a composite oil displacement system of diuteramide and surfactant suitable for high-temperature and high-salt oil reservoirs. Diyou gum in the present invention has good compatibility with nonionic and zwitterionic surfactants, which can not only maintain the oil washing ability of the displacement fluid, but also greatly increase the swept volume, thereby improving the oil recovery rate .

Description

适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系Diyou gum and surfactant composite flooding system suitable for high temperature and high salinity reservoirs

技术领域technical field

本发明涉及油田化学领域,尤其是一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。The invention relates to the field of oil field chemistry, in particular to a composite oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs.

背景技术Background technique

石油的开采分为三个阶段:最初是依靠地层的天然能量进行开采,称为一次采油,一般采收率为5%~10%;在天然能量枯竭后,可以通过人工注水或注气继续开采,称为二次采油,采收率可以提高到30%~40%;二次采油后,仍有60%~70%的剩余油残留在地下,只能依靠物理和化学的方法进行开采,称为三次采油。三次采油方法主要有热力驱、混相驱、化学驱和微生物驱等。The exploitation of oil is divided into three stages: initially, it is exploited by relying on the natural energy of the formation, which is called primary oil recovery, and the general recovery rate is 5% to 10%; after the natural energy is exhausted, it can be continued by artificial water injection or gas injection , called secondary oil recovery, the recovery rate can be increased to 30% to 40%; after secondary oil recovery, there are still 60% to 70% of the remaining oil remaining in the ground, which can only be exploited by physical and chemical methods. For tertiary oil recovery. Tertiary oil recovery methods mainly include thermal flooding, miscible flooding, chemical flooding and microbial flooding.

化学驱油,就是通过注入地下的化学剂与油藏流体发生一系列物理化学反应,从而将石油更有效地驱替出来,提高油藏采收率。早在上世纪六七十年代,人们便开始了化学驱三次采油技术的室内研究。先后出现了碱驱、活性水驱、聚合物驱及其发展而来的二元、三元驱油体系。有碱的三元复合驱体系,即“聚合物+表面活性剂+碱”,虽然在提高采收率方面收到明显效果,但由于在适合化学驱的资源中,80%以上的区块地层水中的钙、镁离子含量高,丰富的钙、镁与三元复合驱中的碱结合产生沉淀。严重的结垢问题成为三元复合驱技术推广的致命伤。逐渐人们开始把目光转向对“聚合物+表面活性剂”无碱二元复合驱油体系的研究。表面活性剂与聚合物二元复合驱油体系,一方面聚合物能够扩大驱油体系的波及体积,另一方面表面活性剂能够提高驱油效率。如果两者配伍良好,对提高原油采收率将有广阔的应用前景。水解聚丙烯酰胺(HPAM)成为一种常用的用来提高水相粘度的重要聚合物,但随着研究的深入,发现其耐温抗盐性较差,在高温高盐条件下,体系的粘度损失严重,并且在地下运移过程中,受地下孔道的剪切作用,分子链会断裂,导致体系粘度的降低。为此,有研究人员提出利用疏水改性聚合物,提高分子的耐温抗盐性能,但由于疏水基团的引入,会导致很难得到分子量像聚丙烯酰胺一样高的产物,或者得到了高分子量的产物,由于大量疏水基团的引入,分子的水溶性又变差。同时,疏水缔合聚合物还存在与表面活性剂配伍性方面的问题。随着油田开发的进行,高温、高盐等苛刻条件下的油藏急需要有合适的驱油体系。因此,开发一种配伍性好,具有耐高温、高盐的新型聚合物/表面活性剂二元驱油体系,对于油田的开发具有重要的意义。Chemical flooding is a series of physical and chemical reactions between the chemical agent injected into the ground and the reservoir fluid, so that the oil can be displaced more effectively and the oil recovery rate can be improved. As early as the 1960s and 1970s, people began the laboratory research on chemical flooding EOR technology. Alkali flooding, active water flooding, polymer flooding and their developed binary and triple flooding systems have appeared successively. Alkaline ASP flooding system, that is, "polymer + surfactant + alkali", although it has achieved obvious effects in enhancing oil recovery, but due to the resources suitable for chemical flooding, more than 80% of the block strata The content of calcium and magnesium ions in the water is high, and the abundant calcium and magnesium combine with the alkali in ASP flooding to produce precipitation. Severe scaling has become a fatal injury to the popularization of ASP flooding technology. Gradually, people began to turn their attention to the research on the "polymer + surfactant" alkali-free binary compound flooding system. In the binary composite flooding system of surfactant and polymer, on the one hand, the polymer can expand the swept volume of the oil flooding system, and on the other hand, the surfactant can improve the oil displacement efficiency. If the two are well compatible, there will be broad application prospects for enhanced oil recovery. Hydrolyzed polyacrylamide (HPAM) has become an important polymer commonly used to increase the viscosity of the water phase. However, with the deepening of research, it was found that its temperature resistance and salt resistance are poor. Under high temperature and high salt conditions, the viscosity of the system The loss is serious, and during the underground migration process, the molecular chains will be broken due to the shear action of the underground channels, resulting in a decrease in the viscosity of the system. For this reason, some researchers have proposed to use hydrophobically modified polymers to improve the temperature and salt resistance of molecules, but due to the introduction of hydrophobic groups, it will be difficult to obtain products with a molecular weight as high as polyacrylamide, or to obtain high molecular weight products. Due to the introduction of a large number of hydrophobic groups, the water solubility of the molecule becomes poor. At the same time, hydrophobically associating polymers also have problems in compatibility with surfactants. With the development of oil fields, the reservoirs under harsh conditions such as high temperature and high salinity urgently need a suitable oil displacement system. Therefore, it is of great significance for the development of oil fields to develop a new polymer/surfactant binary flooding system with good compatibility, high temperature resistance and high salt.

发明内容Contents of the invention

本发明的目的是为克服上述现有技术的不足,提供一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,该体系具有很好的配伍性,同时具有耐温和抗盐的特性。The purpose of the present invention is to overcome the deficiencies of the above-mentioned prior art, and provide a compound oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt reservoirs. Salt resistance properties.

为实现上述目的,本发明采用下述技术方案:To achieve the above object, the present invention adopts the following technical solutions:

一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.1%-0.5%,表面活性剂0.05%-0.6%,其余为矿化水。A compound oil displacement system of diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs, consisting of the following components in mass percentage: 0.1%-0.5% of diyou gum, 0.05%-0.6% of surfactant, and the rest for mineralized water.

优选的,所述复合驱油体系,由以下质量百分比的组分组成:定优胶0.15~0.2%,表面活性剂0.05~0.3%,其余为矿化水。Preferably, the composite oil displacement system is composed of the following components in mass percentage: 0.15-0.2% diyout gum, 0.05-0.3% surfactant, and the rest is mineralized water.

优选的,所述表面活性剂为两性表面活性剂和非离子型表面活性剂的混合物,质量比为75:25~25:75。Preferably, the surfactant is a mixture of an amphoteric surfactant and a nonionic surfactant, and the mass ratio is 75:25˜25:75.

优选的,所述两性表面活性剂和非离子型表面活性剂的质量比为50:50。Preferably, the mass ratio of the amphoteric surfactant to the nonionic surfactant is 50:50.

优选的,所述两性表面活性剂活性剂为十二烷基聚氧乙烯醚甜菜碱、十二烷基二甲基羟丙基磺基甜菜碱、十二烷基甜菜碱或十二烷基二甲基甜菜碱中的一种。Preferably, the amphoteric surfactant active agent is lauryl polyoxyethylene ether betaine, dodecyl dimethyl hydroxypropyl sultaine, dodecyl betaine or dodecyl di One of the methyl betaines.

优选的,所述非离子表面活性剂活性剂为聚乙二醇单辛基苯基醚(TX-100)或烷基酚聚氧乙烯(10)醚(OP-10)。Preferably, the nonionic surfactant active agent is polyethylene glycol monooctyl phenyl ether (TX-100) or alkylphenol polyoxyethylene (10) ether (OP-10).

优选的,所述矿化水由NaCl、CaCl2和MgCl2配制而成,总矿化度为244121mg·L-1,其中Na+、Mg2+、Ca2+和Cl-的浓度分别为95373、102、411和148235mg·L-1Preferably, the mineralized water is prepared from NaCl, CaCl 2 and MgCl 2 , the total salinity is 244121 mg·L -1 , and the concentrations of Na + , Mg 2+ , Ca 2+ and Cl - are respectively 95373 , 102, 411 and 148235 mg·L -1 ;

本发明还公开了一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系的制备方法,步骤包括:The present invention also discloses a preparation method of the compound oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt reservoirs, the steps comprising:

按配比取各组分,常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下加入表面活性剂和定优胶,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。Take each component according to the proportion, add NaCl, CaCl 2 and MgCl 2 into water at room temperature and stir evenly to prepare mineralized water, then add surfactant and diuterene at room temperature, and stir evenly to obtain a product suitable for high temperature and high salt Diyou gum and surfactant compound flooding system in oil reservoir.

根据本发明,所述适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系应用在石油开采的三次采油过程中。According to the present invention, the diutan gum and surfactant compound oil displacement system suitable for high temperature and high salt reservoirs are applied in the tertiary oil recovery process of oil production.

本发明的有益效果是:The beneficial effects of the present invention are:

(1)本发明选用定优胶具有非常好的增粘效果,其表观粘度要明显地高于黄原胶体系,更高于HPAM体系,且与表面活性剂复配后,耐盐效果好。这主要是因为定优胶的主链为由-O-键连接的糖环单元,同时分子链上每个重复单元中还含有一个由两个糖元长度的侧链,-COO-基团位于分子主链的重复单元中,而侧链中没有带电荷的基团,所以当定优胶的大分子链在表面活性剂和矿化水中溶解后,定优胶的分子链能够与表面活性剂相互缠绕,定优胶的侧链会对主链和表面活性剂上的带电基团起到一定的保护作用,从而使定优胶分子与表面活性剂分子产生协同作用,在高于90℃条件下,驱油体系仍能保持一定的粘度,从而使得其耐盐性大大的提高,黄原胶分子虽然也是由糖元的主链和侧链组成,但是其侧链上含有两个-COO-基团,更容易受到盐的影响,使其耐盐性能大打折扣。(1) The present invention selects Diyou gum to have a very good viscosifying effect, and its apparent viscosity is significantly higher than that of the xanthan gum system, higher than that of the HPAM system, and after compounding with surfactants, the salt-resistant effect is good . This is mainly because the main chain of Diutan gum is a sugar ring unit connected by -O- bonds, and each repeating unit on the molecular chain also contains a side chain with a length of two sugars, and the -COO- group is located in the In the repeating unit of the molecular main chain, there is no charged group in the side chain, so when the macromolecular chain of diuter gum is dissolved in surfactant and mineralized water, the molecular chain of diuter gum can be combined with surfactant Intertwined with each other, the side chains of Diutan gum will protect the main chain and the charged groups on the surfactant to a certain extent, so that Diutan gum molecules and surfactant molecules have a synergistic effect. Under low conditions, the oil displacement system can still maintain a certain viscosity, which greatly improves its salt tolerance. Although the xanthan gum molecule is also composed of the main chain and side chain of glycogen, its side chain contains two -COO- The group is more susceptible to the influence of salt, which greatly reduces its salt resistance.

(2)在高温高盐条件下,定优胶体系的线性粘弹区非常的明显,其粘弹性要明显地强于黄原胶和HPAM。从定优胶的结构来看,其分子链上有大量的-OH和一定数量的-COO-基团,这样的亲水基结构与非离子和两性离子表面活性剂都具有较好的配伍性。(2) Under the condition of high temperature and high salt, the linear viscoelastic region of Diutan gum system is very obvious, and its viscoelasticity is obviously stronger than that of xanthan gum and HPAM. From the perspective of the structure of Diutan Gum, there are a large number of -OH and a certain number of -COO- groups on its molecular chain. Such a hydrophilic group structure has good compatibility with nonionic and zwitterionic surfactants. .

(3)定优胶与所用表面活性剂复配体系之间产生协同作用,两者复合能够产生优于两者单一体系的效果,在保持体系较高粘度的同时,又保持了表面活性剂较低的界面张力,使得定优胶/表面活性剂二元体系在驱油过程中,既能保持驱替液的洗油能力,又能大幅度的增大其波及体积,进而提高原油采收率。(3) There is a synergistic effect between diyou gum and the surfactant compound system used, and the compounding of the two can produce an effect better than that of the two single systems. The low interfacial tension makes Diyou gum/surfactant binary system not only maintain the oil washing ability of the displacement fluid, but also greatly increase its swept volume during the oil displacement process, thereby improving oil recovery .

附图说明Description of drawings

图1是定优胶分子结构图;Fig. 1 is the molecular structure diagram of diyout gum;

图2是在矿化度为244121mg·L-1,温度分别为25和90℃条件下,0.175%的聚合物溶液粘度随剪切速率的变化图;图中diutan gum、xanthan gum和HPAM分别指定优胶、黄原胶和部分水解聚丙烯酰胺;Figure 2 is a graph showing the variation of viscosity of 0.175% polymer solution with shear rate under the condition of salinity of 244121 mg·L -1 and temperature of 25 and 90°C respectively; in the figure diutan gum, xanthan gum and HPAM are designated respectively Eucalyptus, xanthan gum and partially hydrolyzed polyacrylamide;

图3是矿化度为244121mg·L-1,90℃条件下,0.175%的聚合物溶液体系复合模量(图A)储能模量G′和损耗模量G″(图B)随应力的变化图;Fig. 3 is the composite modulus of 0.175% polymer solution system with a salinity of 244121 mg·L -1 at 90°C (Fig. A), storage modulus G′ and loss modulus G″ (Fig. B) with stress change map;

图4是矿化度为244121mg·L-1,90℃条件下,0.175%聚合物/0.3%十二烷基甜菜碱/0.2%OP-10复合体系表观粘度(A)和剪切应力(B)随剪切速率的变化图;Figure 4 shows the apparent viscosity (A) and shear stress ( B) Variation graph with shear rate;

图5是矿化度为244121mg·L-1,90℃条件下,0.15%聚合物/0.05%十二烷基二甲基羟丙基磺基甜菜碱/0.05%TX-100复合体系溶液复合模量随应力的变化图(图A)及储能模量G′和损耗模量G″随振荡频率的变化图(图B);Figure 5 is a composite model of the solution of the 0.15% polymer/0.05% dodecyldimethylhydroxypropyl sulfobetaine/0.05% TX-100 composite system with a salinity of 244121mg·L -1 and 90°C The change diagram of the quantity with the stress (figure A) and the change diagram of the storage modulus G' and the loss modulus G" with the oscillation frequency (figure B);

图6是矿化度为244121mg·L-1,90℃条件下,0.175%聚合物/0.1%十二烷基二甲基甜菜碱/0.1%OP-10复合体系界面张力随表面活性剂浓度的变化图;Figure 6 shows the interfacial tension of the 0.175% polymer/0.1% dodecyl dimethyl betaine/0.1% OP-10 composite system with a salinity of 244121 mg·L -1 at 90°C with the concentration of surfactant change map;

图7是矿化度为244121mg·L-1,90℃条件下,0.175%聚合物/0.15%十二烷基聚氧乙烯醚甜菜碱/0.15%TX-100复合体系的累计采收率随注入PV数的变化图。Fig. 7 shows the cumulative recovery of the composite system of 0.175% polymer/0.15% polyoxyethylene lauryl ether betaine/0.15% TX-100 at 90°C with a salinity of 244121 mg·L -1 Change graph of PV number.

具体实施方式Detailed ways

下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.

本实施例中采用的表面活性剂均为市售产品,产品纯度级别为化学纯;采用的定优胶为美国斯比凯克公司提供,纯度98%,分子量为5.2×106g·mol-1,特性粘度为5450mL·g-1。室内模拟驱油实验所用原油油样为河南油田普通稠油,原油酸值为1.361mgKOH/g,粘度254mPas。The surfactants used in this example are all commercially available products, and the purity level of the products is chemically pure; the diyout gum used is provided by CPK Company of the United States, with a purity of 98% and a molecular weight of 5.2×10 6 g·mol - 1 , the intrinsic viscosity is 5450mL·g -1 . The crude oil sample used in the indoor simulated oil displacement experiment is ordinary heavy oil from Henan Oilfield, with an acid value of 1.361 mgKOH/g and a viscosity of 254 mPas.

实施例1Example 1

一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.15%,表面活性剂0.1%,其中十二烷基二甲基羟丙基磺基甜菜碱占0.05%,TX-100占0.05%,其余为矿化水,所述矿化水由NaCl、CaCl2和MgCl2配制而成,总矿化度为244121mg·L-1,其中Na+、Mg2+、Ca2+和Cl-的浓度分别为95373、102、411和148235mg·L-1A compound oil displacement system of Diutan gum and surfactant suitable for high-temperature and high-salt oil reservoirs. Hydroxypropyl sulfobetaine accounts for 0.05%, TX-100 accounts for 0.05%, and the rest is mineralized water. The mineralized water is formulated from NaCl, CaCl 2 and MgCl 2 , and the total mineralization degree is 244121mg·L -1 , where the concentrations of Na + , Mg 2+ , Ca 2+ and Cl - are 95373, 102, 411 and 148235 mg·L -1 , respectively.

制备方法如下:常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下将0.05g的十二烷基二甲基羟丙基磺基甜菜碱、0.05g的TX-100和0.15g的定优胶加入到99.75g矿化水中,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。The preparation method is as follows: add NaCl, CaCl 2 and MgCl 2 into water at normal temperature and stir to prepare mineralized water, then add 0.05g of dodecyl dimethyl hydroxypropyl sulfobetaine, 0.05g of Add TX-100 and 0.15g of Diutan gum into 99.75g of mineralized water, and stir evenly to obtain a combined oil displacement system of Diutan gum and surfactant suitable for high-temperature and high-salt reservoirs.

室内模拟驱油实验,在水驱至填砂管不出油后,利用该体系进一步进行驱油实验,当该体系的注入量为0.5PV时,采收率可在水驱基础上提高36.8%。In the laboratory simulation oil displacement experiment, after water flooding until the sand-packed pipe does not produce oil, the system is used for further oil displacement experiments. When the injection volume of the system is 0.5PV, the recovery rate can be increased by 36.8% on the basis of water flooding .

实施例2Example 2

一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.2%,表面活性剂0.3%,其中十二烷基聚氧乙烯醚甜菜碱占0.15%,TX-100占0.15%,其余为矿化水,所述矿化水由NaCl、CaCl2和MgCl2配制而成,总矿化度为244121mg·L-1,其中Na+、Mg2+、Ca2+和Cl-的浓度分别为95373、102、411和148235mg·L-1A compound oil displacement system of Diutan gum and surfactant suitable for high-temperature and high-salt oil reservoirs, which is composed of the following components in mass percentage: 0.2% Diutan gum, 0.3% surfactant, wherein dodecyl polyoxygen Vinyl ether betaine accounts for 0.15%, TX-100 accounts for 0.15%, and the rest is mineralized water. The mineralized water is prepared from NaCl, CaCl 2 and MgCl 2. The total mineralization degree is 244121mg·L -1 , of which The concentrations of Na + , Mg 2+ , Ca 2+ and Cl - were 95373, 102, 411 and 148235 mg·L -1 , respectively.

制备方法如下:常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下将0.15g的十二烷基聚氧乙烯醚甜菜碱、0.15g的TX-100和0.2g的定优胶加入到99.5g矿化水中,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。The preparation method is as follows: add NaCl, CaCl 2 and MgCl 2 into water at normal temperature and stir to prepare mineralized water, then add 0.15g of lauryl polyoxyethylene ether betaine, 0.15g of TX-100 and Add 0.2g of Diyou gum to 99.5g of mineralized water, and stir evenly to obtain a composite oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs.

室内模拟驱油实验,在水驱至填砂管不出油后,利用该体系进一步进行驱油实验,当该体系的注入量为0.5PV时,采收率可在水驱基础上提高44.2%。In the laboratory simulation oil displacement experiment, after water flooding until the sand-packed pipe does not produce oil, the system is used for further oil displacement experiments. When the injection volume of the system is 0.5PV, the recovery rate can be increased by 44.2% on the basis of water flooding .

实施例3Example 3

一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.175%,表面活性剂0.2%,其中十二烷基二甲基甜菜碱占0.1%,OP-10占0.1%,其余为矿化水,所述矿化水由NaCl、CaCl2和MgCl2配制而成,总矿化度为244121mg·L-1,其中Na+、Mg2+、Ca2+和Cl-的浓度分别为95373、102、411和148235mg·L-1A compound oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs, which is composed of the following components in mass percentage: 0.175% of Diyou gum, 0.2% of surfactant, and dodecyl dimethyl Betaine-based betaine accounts for 0.1%, OP-10 accounts for 0.1%, and the rest is mineralized water. The mineralized water is prepared from NaCl, CaCl 2 and MgCl 2. The total mineralization degree is 244121mg·L -1 , of which Na The concentrations of + , Mg 2+ , Ca 2+ and Cl - were 95373, 102, 411 and 148235 mg·L -1 , respectively.

制备方法如下:常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下将0.1g的十二烷基二甲基甜菜碱、0.1g的OP-10和0.175g的定优胶加入到99.625g矿化水中,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。The preparation method is as follows: add NaCl, CaCl 2 and MgCl 2 into water at normal temperature and stir to prepare mineralized water, then add 0.1g of dodecyl dimethyl betaine, 0.1g of OP-10 and 0.175 Add 99.625g of Diyou gum into 99.625g of mineralized water, and stir evenly to obtain the Diyou gum and surfactant composite flooding system suitable for high-temperature and high-salt oil reservoirs.

室内模拟驱油实验,在水驱至填砂管不出油后,利用该体系进一步进行驱油实验,当该体系的注入量为0.5PV时,采收率可在水驱基础上提高37.2%。In the laboratory simulation oil displacement experiment, after water flooding until the sand-packed pipe does not produce oil, the system is used for further oil displacement experiments. When the injection volume of the system is 0.5PV, the recovery rate can be increased by 37.2% on the basis of water flooding .

实施例4Example 4

一种适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系,由以下质量百分比的组分组成:定优胶0.5%,表面活性剂0.5%,其中十二烷基甜菜碱占0.3%,OP-10占0.2%,其余为矿化水,所述矿化水由NaCl、CaCl2和MgCl2配制而成,总矿化度为244121mg·L-1,其中Na+、Mg2+、Ca2+和Cl-的浓度分别为95373、102、411和148235mg·L-1A compound oil displacement system of Diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs, which consists of the following components in mass percentage: 0.5% Diyou gum, 0.5% surfactant, wherein Accounted for 0.3%, OP-10 accounted for 0.2%, the rest is mineralized water, the mineralized water is prepared from NaCl, CaCl 2 and MgCl 2 , the total salinity is 244121mg·L -1 , of which Na + , Mg The concentrations of 2+ , Ca 2+ and Cl - were 95373, 102, 411 and 148235 mg·L -1 , respectively.

制备方法如下:常温下将NaCl、CaCl2和MgCl2加入水中搅拌均匀制备成矿化水,然后在常温下将0.3g的十二烷基甜菜碱、0.2g的OP-10和0.5g的定优胶加入到99g矿化水中,搅拌均匀,即得适合于高温高盐油藏的定优胶和表面活性剂复合驱油体系。The preparation method is as follows: add NaCl, CaCl 2 and MgCl 2 into water at normal temperature and stir to prepare mineralized water, then add 0.3g of dodecyl betaine, 0.2g of OP-10 and 0.5g of fixed Diyou gum was added to 99g of mineralized water and stirred evenly to obtain a combined oil displacement system of diyou gum and surfactant suitable for high-temperature and high-salt oil reservoirs.

室内模拟驱油实验,在水驱至填砂管不出油后,利用该体系进一步进行驱油实验,当该体系的注入量为0.5PV时,采收率可在水驱基础上提高34.7%。In the laboratory simulation oil displacement experiment, after water flooding until the sand-packed pipe does not produce oil, the system is used for further oil displacement experiments. When the injection volume of the system is 0.5PV, the recovery rate can be increased by 34.7% based on water flooding .

如图2所示,定优胶具有非常好的增粘效果,温度为25℃、剪切速率为7s-1时,定优胶与油田常用HPAM的表观粘度相当,要明显地高于黄原胶的粘度,而当温度升高到90℃时,定优胶体系的表观粘度要明显地高于黄原胶体系,更高于HPAM体系。这个结果充分说明生物胶体系在增粘效果方面要明显地强于HPAM体系,同时,定优胶的效果也要好于黄原胶。这主要是因为定优胶的主链为由-O-键连接的糖环单元,同时分子链上每个重复单元中还含有一个由两个糖元长度的侧链,分子主链重复单元中,含有一个-COO-基团,而侧链中没有带电荷的基团,所以,当定优胶的大分子链在表面活性剂和矿化水中溶解后,分子链与表面活性剂相互缠绕,侧链会对主链上的带电基团起到一定的保护作用,在高于90℃条件下,驱由体系仍能保持一定的粘度,从而使得其耐盐性大大的提高,黄原胶分子虽然也是由糖元的主链和侧链组成,但是其侧链上含有两个-COO-基团,更容易受到盐的影响,使其耐盐性能大打折扣。As shown in Figure 2, Diutan gum has a very good viscosity-increasing effect. When the temperature is 25°C and the shear rate is 7s -1 , the apparent viscosity of Diuter gum is equivalent to that of HPAM commonly used in oilfields, which is significantly higher than that of yellow rubber. The viscosity of raw gum, and when the temperature rises to 90 ℃, the apparent viscosity of diutan gum system is obviously higher than that of xanthan gum system, higher than that of HPAM system. This result fully shows that the viscosifying effect of the bio-glue system is obviously stronger than that of the HPAM system, and the effect of Diyou gum is also better than that of xanthan gum. This is mainly because the main chain of Diutan gum is a sugar ring unit connected by -O- bonds, and each repeating unit on the molecular chain also contains a side chain with a length of two sugar elements, and the repeating unit of the main chain of the molecule , contains a -COO- group, and there is no charged group in the side chain, so when the macromolecular chain of Diutan Gum is dissolved in the surfactant and mineralized water, the molecular chain and the surfactant are intertwined, The side chain will protect the charged groups on the main chain to a certain extent. At a temperature higher than 90°C, the drive system can still maintain a certain viscosity, which greatly improves its salt resistance. Xanthan gum molecules Although it is also composed of the main chain and side chain of glycogen, its side chain contains two -COO- groups, which are more susceptible to the influence of salt, which greatly reduces its salt tolerance.

如图3所示,在高温高盐条件下,定优胶体系的线性粘弹区非常的明显,其粘弹性要明显地强于黄原胶和HPAM,说明定优胶具有非常好的耐温抗盐性能,在高温高盐条件下,仍具有十分明显的粘弹性,这对于驱油体系来说,是十分重要的性质。从定优胶的结构来看,其分子链上有大量的-OH和一定数量的-COO-基团,这样的亲水基结构与非离子和两性离子表面活性剂都具有较好的配伍性。As shown in Figure 3, under the condition of high temperature and high salt, the linear viscoelastic zone of Diyou gum system is very obvious, and its viscoelasticity is obviously stronger than that of xanthan gum and HPAM, which shows that Diyou gum has very good temperature resistance Salt resistance, under high temperature and high salt conditions, still has very obvious viscoelasticity, which is a very important property for oil displacement systems. From the perspective of the structure of Diutan Gum, there are a large number of -OH and a certain number of -COO- groups on its molecular chain. Such a hydrophilic group structure has good compatibility with nonionic and zwitterionic surfactants. .

如图4和图5所示,定优胶与两性及非离子表面活性剂复配后,体系仍然具有定优胶体系的耐温和抗盐性能,表现出较强的粘弹特性。As shown in Figure 4 and Figure 5, after Diutan gum is compounded with amphoteric and non-ionic surfactants, the system still has the temperature and salt resistance performance of Diutan gum system, showing strong viscoelastic properties.

如图6所示,定优胶与表面活性剂复配,在表面活性剂浓度为0.1%~0.3%时,复合体系的界面张力最低,达到10-2mN·m-1数量级,虽然没有达到10-3~10-4这样超低的数量级,但是在90℃高温、矿化度为244121mg·L-1条件下达到这样低的界面张力已经实属不易。As shown in Figure 6, when Diyou gum is compounded with surfactants, when the concentration of surfactants is 0.1% to 0.3%, the interfacial tension of the composite system is the lowest, reaching the order of 10 -2 mN·m -1 , although it has not reached 10 -3 to 10 -4 is an ultra-low order of magnitude, but it is not easy to achieve such a low interfacial tension at a high temperature of 90°C and a salinity of 244121mg·L -1 .

图7给出了不同驱油体系的采收率随着注入PV数的变化,其中原油选用的为河南油田普通稠油,原油酸值为1.361mgKOH/g,粘度254mPas,可以看出在二元复合驱油体系中,定优胶/表面活性剂体系的采收率也均高于黄原胶/表面活性剂体系和HPAM/表面活性剂体系的采收率。这主要是因为在考察的体系中,定优胶/表面活性剂体系的粘度最高,在驱油过程中能够有效地提高驱替液波及体积,更大程度减少孔道中的残余油,提高原油采收率。在高温高盐条件下,定优胶/表面活性剂体系仍具有较高的原油采收率,主要还是归功于定优胶与所用表面活性剂复配体系之间的协同作用,两者复合能够产生优于两者单一体系的效果,即在保持体系较高粘度的同时,又保持了表面活性剂较低的界面张力,使得定优胶/表面活性剂体系在驱油过程中,既能保持驱替液的洗油能力,又能大幅度的增大其波及体积,进而提高原油采收率。Figure 7 shows the variation of the recovery factor of different oil displacement systems with the injected PV number. The crude oil is ordinary heavy oil in Henan Oilfield, the acid value of the crude oil is 1.361mgKOH/g, and the viscosity is 254mPas. In the composite flooding system, the recovery factor of diutan gum/surfactant system is also higher than that of xanthan gum/surfactant system and HPAM/surfactant system. This is mainly because the dipitan gum/surfactant system has the highest viscosity among the investigated systems, which can effectively increase the swept volume of the displacement fluid during the oil displacement process, reduce residual oil in the pores to a greater extent, and improve oil recovery. yield. Under high-temperature and high-salt conditions, the diutan gum/surfactant system still has a high oil recovery, which is mainly due to the synergistic effect between the diutan gum and the surfactant compound system used. The combination of the two can It produces an effect better than that of the two single systems, that is, while maintaining a high viscosity of the system, it also maintains a low interfacial tension of the surfactant, so that the dipitan gum/surfactant system can maintain both The oil washing ability of the displacement fluid can greatly increase its swept volume, thereby enhancing the oil recovery rate.

以上实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围。The above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: it can still be described in the foregoing embodiments Modifications are made to the recorded technical solutions, or equivalent replacements are made to some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions depart from the scope of the technical solutions of the embodiments of the present invention.

Claims (4)

1. a kind of diutan for being suitable for high temperature and high salt oil deposit and surfactant composite oil-displacing system, it is characterized in that, by following The component composition of mass percent:Diutan 0.1%-0.5%, surfactant 0.05%-0.6%, remaining is mineralized water;Table Face activating agent is amphoteric surfactant and nonionic surface active agent mass ratio is 75:25~25:75 mixture;Both sexes Surfactant activity agent is alkylpolyoxyethylene glycine betaine, dodecyl dimethyl hydroxypropyl sulfobetaines, ten One kind in dialkyl group glycine betaine or dodecyldimethylammonium hydroxide inner salt;Nonionic surfactant activating agent is polyethyleneglycol Octyl phenyl ether or alkylphenol-polyethenoxy (10) ether;Mineralized water is by NaCl, CaCl2And MgCl2It is formulated, total salinity is 244121mg·L-1, wherein Na+、Mg2+、Ca2+And Cl-Concentration be respectively 95373,102,411 and 148235mgL-1
2. a kind of diutan for being suitable for high temperature and high salt oil deposit as claimed in claim 1 and surfactant combination flooding oil body System, it is characterized in that, it is made up of the component of following mass percent:Diutan 0.15~0.2%, surfactant 0.05~ 0.3%, remaining is mineralized water.
3. a kind of diutan for being suitable for high temperature and high salt oil deposit as claimed in claim 1 and surfactant composite oil-displacing system Preparation method, it is characterized in that, step is as follows:Each component is taken by proportioning, by NaCl, CaCl under normal temperature2And MgCl2It is added to the water Stir and be prepared into mineralized water, then add surfactant and diutan at normal temperatures, stir, produce and be suitable for height The diutan and surfactant composite oil-displacing system of warm high salinity reservoir.
4. the diutan for being suitable for high temperature and high salt oil deposit and surfactant complex oil displacing as described in claim any one of 1-2 Application of the system during the tertiary oil recovery of oil exploitation.
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