CN110439517A - A kind of flooding method suitable for heavy crude reservoir - Google Patents
A kind of flooding method suitable for heavy crude reservoir Download PDFInfo
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- 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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Abstract
本发明涉及原油采集技术领域,公开了一种适用于稠油油藏的驱油方法。将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油2‑4次,Pickering乳状液体系与泡沫体系总段塞注入量为0.4‑0.8PV;泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂;Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂和聚合物。本发明适驱油方法适用于黏度低于5000mPa·s的原油,适用原油粘度范围较宽,且对于高粘度稠油油藏的采收率有大幅提高。The invention relates to the technical field of crude oil collection, and discloses an oil displacement method suitable for heavy oil reservoirs. The Pickering emulsion system and the foam system were alternately flooded by slug combination for 2-4 times, and the total slug injection volume of the Pickering emulsion system and the foam system was 0.4-0.8PV; the emulsifier of the foam system included magnetic nano-Fe 3 O 4 @ SiO2 particles and foaming agent; the emulsifier of the Pickering emulsion system includes magnetic nano-Fe3O4@SiO2 particles, surfactants and polymers. The suitable oil displacement method of the present invention is suitable for crude oil with a viscosity lower than 5000mPa·s, has a wide range of suitable crude oil viscosity, and greatly improves the recovery factor for high-viscosity heavy oil reservoirs.
Description
技术领域technical field
本发明涉及原油采集技术领域,尤其是涉及一种适用于稠油油藏的驱油方法。The invention relates to the technical field of crude oil collection, in particular to an oil displacement method suitable for heavy oil reservoirs.
背景技术Background technique
随着工业的发展,石油的社会需求量与石油资源严重不足的矛盾日益加剧。如何从已开发的油田中开采出更多得的油成为研究重点。随着科技的进步,一些特殊的油藏也越来越多的被开发,如低渗透油藏、特低渗透油藏、高温高盐油藏等。可流动稠油的黏度通常高达几千至几万mPa·s,由于水与稠油流度比差异太大,容易造成水的指进,从而导致无效驱替和低采收率。Exxon公司最早提出Pickering乳状液采油法,并被用来开发黏度在20-3000mPa·s范围内的稠油。经室内和现场试验证明,Pickering乳状液可以进行长时间注入,而且在流动过程中可以保持稳定,显著提高采收率。Son等也使用Pickering乳状液进行驱油,同时提出乳液和水交替注入具有更好的驱油效果。但是,这些方法中对高浓度原油存在原油采收率低的缺点。中国专利公开号CN101949282公开了一种渣油沥青乳状液驱油方法,将渣油或沥青加热至流动状态,配置一定浓度的表面活性剂水溶液并加热至80℃,然后将流动态的渣油或沥青按配比加入热的表面活性剂溶液中,搅拌使其乳化,在现场水驱油至含水率98%以上,随后注入渣油或沥青乳状液进行驱替,再后续水驱,但是此渣油沥青乳状液只适用于普通稠油油藏(原油粘度小于300mPa.s),适用稠油粘度范围较窄,对于高粘度稠油油藏原油采收率则会大大降低。With the development of industry, the contradiction between the social demand for oil and the serious shortage of oil resources has become increasingly serious. How to extract more oil from the developed oil fields has become the focus of research. With the advancement of science and technology, some special reservoirs are being developed more and more, such as low permeability reservoirs, ultra-low permeability reservoirs, high temperature and high salinity reservoirs and so on. The viscosity of flowable heavy oil is usually as high as thousands to tens of thousands of mPa·s. Due to the large difference in the mobility ratio of water and heavy oil, it is easy to cause water fingering, resulting in ineffective displacement and low recovery. Exxon Company first proposed the Pickering emulsion oil recovery method, and was used to develop heavy oil with a viscosity in the range of 20-3000mPa·s. Indoor and field tests have proved that the Pickering emulsion can be injected for a long time, and can remain stable during the flow process, significantly improving the recovery factor. Son et al. also used Pickering emulsion for oil displacement, and at the same time proposed that the alternating injection of emulsion and water has a better oil displacement effect. However, these methods have the disadvantage of low oil recovery for high-concentration crude oil. Chinese Patent Publication No. CN101949282 discloses a residual oil bitumen emulsion flooding method. The residual oil or bitumen is heated to a flow state, and a certain concentration of surfactant aqueous solution is prepared and heated to 80° C., and then the flow state residual oil or Asphalt is added to the hot surfactant solution according to the proportion, stirred to emulsify it, and the oil is flooded with water on site to a water content above 98%, and then the residual oil or bitumen emulsion is injected for displacement, followed by water flooding, but the residual oil Asphalt emulsion is only suitable for ordinary heavy oil reservoirs (crude oil viscosity is less than 300mPa.s), and the viscosity range of heavy oil is narrow, and the oil recovery rate for high viscosity heavy oil reservoirs will be greatly reduced.
发明内容Contents of the invention
本发明是为了克服现有技术高浓度稠油采收率低的问题,提供一种适用于稠油油藏的驱油方法,适用于黏度低于5000mPa·s的原油,适用原油粘度范围较宽,且对于高粘度稠油油藏的采收率有大幅提高。The present invention aims to overcome the problem of low recovery of high-concentration heavy oil in the prior art, and provides an oil displacement method suitable for heavy oil reservoirs, suitable for crude oil with a viscosity lower than 5000mPa·s, and suitable for a wide range of crude oil viscosity , and the recovery factor for high-viscosity heavy oil reservoirs has been greatly improved.
为了实现上述目的,本发明采用以下技术方案:一种适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油2-4次。In order to achieve the above object, the present invention adopts the following technical solutions: an oil displacement method suitable for heavy oil reservoirs, in which the Pickering emulsion system and the foam system are alternately displaced 2-4 times in the form of slug combination.
本发明采用Pickering乳状液体系和泡沫体系以段塞组合方式交替注入岩芯,乳状液体系和泡沫体系可以分散到高粘度稠油中。这种分散作用一方面抑制了低粘度驱油体系的指进,使得波及效果较好;另一方面由于分散到原油中的液滴对稠油有优异的稀释降粘作用,可大幅度降低前沿相接触的稠油的粘度,从而提高了稠油的流度。另外,乳状液的连续相中还有表面活性剂,在流动的扰动下,稠油可以形成明显的拉丝现象,通过这种机理可以将稠油乳化成水包油的乳化液滴,进而提高洗油效率。体系中的聚合物可以降低后续水流的流度,增加后续水流的波及体积。对原油粘度低于5000mPa·s的原油的采收率有大幅提高。The invention adopts the Pickering emulsion system and the foam system to alternately inject the rock core in a slug combination mode, and the emulsion system and the foam system can be dispersed into the high-viscosity heavy oil. On the one hand, this dispersion effect inhibits the fingering of the low-viscosity oil displacement system, making the sweeping effect better; The viscosity of the heavy oil in contact with each other increases the fluidity of the heavy oil. In addition, there are surfactants in the continuous phase of the emulsion. Under the disturbance of the flow, the heavy oil can form an obvious stringing phenomenon. Through this mechanism, the heavy oil can be emulsified into oil-in-water emulsion droplets, thereby improving the washing effect. oil efficiency. The polymer in the system can reduce the fluidity of the subsequent water flow and increase the swept volume of the subsequent water flow. The recovery factor of crude oil whose viscosity is lower than 5000mPa·s is greatly improved.
作为优选,所述Pickering乳状液体系与泡沫体系总段塞注入量为0.4-0.8PV。Preferably, the total slug injection volume of the Pickering emulsion system and the foam system is 0.4-0.8 PV.
作为优选,所述沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂。Preferably, the emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and a foaming agent.
作为优选,所述泡沫体系的制备方法包括以下步骤:将起泡剂和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,以2000-5000r/min高速搅拌1-3min,即得。Preferably, the preparation method of the foam system includes the following steps: adding foaming agent and foam stabilizer magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, and stirring at a high speed of 2000-5000r/min for 1-3min, that is have to.
作为优选,所述Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂和聚合物。Preferably, the emulsifier of the Pickering emulsion system includes magnetic nano-Fe3O4@SiO2 particles, surfactants and polymers.
作为优选,所述聚合物选自聚丙烯酰胺、黄原胶、聚乙二醇、褐藻酸钠、硬葡聚糖、羧甲基纤维素中的任一种。Preferably, the polymer is selected from any one of polyacrylamide, xanthan gum, polyethylene glycol, sodium alginate, sclerodextran, and carboxymethyl cellulose.
作为优选,所述表面活性剂选自石油羧酸盐、石油磺酸盐、重烷基苯磺酸盐、木质素磺酸盐、生物表面活性剂中的任一种。Preferably, the surfactant is selected from any one of petroleum carboxylate, petroleum sulfonate, heavy alkylbenzene sulfonate, lignin sulfonate, and biological surfactants.
作为优选,所述油相选自煤油、植物油、白油、汽油、柴油中的任一种。Preferably, the oil phase is selected from any one of kerosene, vegetable oil, white oil, gasoline and diesel oil.
作为优选,所述磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:Preferably, the preparation method of the magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液;将氢氧化钠溶液加热至60-80℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: Dissolve sodium hydroxide in water to form a sodium hydroxide solution; mix equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed solution of iron salt; heat the sodium hydroxide solution to 60 -80°C, add the iron salt mixed solution dropwise into the sodium hydroxide solution, stop heating when the solution turns black, cool to room temperature, separate the black product generated by the reaction, wash with water, and dry to obtain Fe3O4 nanoparticles ;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成胶体溶液,加热至40-60℃,向胶体溶液中滴加Na2SiO3溶液并同时滴加H2SiO4溶液控制pH为9-10,反应3-4h,升温至80-95℃再反应1-2h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to form a colloidal solution, heat to 40-60°C, add Na 2 SiO 3 solution and H 2 dropwise to the colloidal solution Control the pH of the SiO 4 solution to 9-10, react for 3-4 hours, raise the temperature to 80-95°C and react for 1-2 hours, wash with deionized water under the action of a magnet, add the cleaned particles to boiling water and boil, and deionize water under the action of a magnet Washing and vacuum drying to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂加入乙醇水溶液中进行水解,然后向水解液中加入Fe3O4@SiO2颗粒,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: Add aminosilane coupling agent to ethanol aqueous solution for hydrolysis, then add Fe 3 O 4 @SiO 2 particles to the hydrolyzed solution, stir and react, wash with absolute ethanol under the action of a magnet, and dry to obtain alkanes Base Fe 3 O 4 @SiO 2 particles;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,在70-80℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: Mix the mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, stir and emulsify at 70-80°C to obtain an emulsion, cool until the paraffin solidifies, and deionize the water under the action of a magnet Washing and drying to obtain paraffin emulsion; mixing paraffin emulsion with perfluorooctanoic acid solution, reacting at room temperature, washing with ethanol under the action of a magnet, and drying to obtain.
作为优选,所述Pickering乳状液体系的制备方法包括以下步骤:As preferably, the preparation method of described Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,超声分散均匀;取油相加入水相溶液组成上下分层的油水体系,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form a water phase solution, and disperse evenly by ultrasonic; take the oil phase and add the water phase solution to form an oil-water system with upper and lower layers, and homogenize in a homogenizer A homogeneously mixed oil-water system is obtained, let it stand at room temperature, and then separate the precipitated oil phase and water phase.
本发明先利用氧化还原法制备Fe3O4纳米颗粒,Fe3O4纳米颗粒作为乳化剂能够对溶液起到较好的乳化效果。另外本发明利用Fe3O4纳米颗粒为载体通过Na2SiO3水解在Fe3O4纳米颗粒表面覆盖一层二氧化硅得到Fe3O4@SiO2颗粒,然后对Fe3O4@SiO2颗粒进行烷基化处理,使无机Fe3O4@SiO2颗粒表面负载氨基活性基团,利用氨基活性基团分别与石蜡和全氟辛酸反应,将石蜡和全氟辛酸接枝到Fe3O4@SiO2颗粒表面上,形成亲水亲油磁性纳米颗粒,磁性纳米颗粒配置形成乳状液在高温高盐条件下具有良好的稳定性,保持乳状液体系的驱油效果。In the present invention, Fe 3 O 4 nanoparticles are firstly prepared by a redox method, and the Fe 3 O 4 nanoparticles are used as an emulsifier, which can have a better emulsifying effect on the solution. In addition, the present invention uses Fe 3 O 4 nanoparticles as a carrier to cover a layer of silicon dioxide on the surface of Fe 3 O 4 nanoparticles through Na 2 SiO 3 hydrolysis to obtain Fe 3 O 4 @SiO 2 particles, and then to Fe 3 O 4 @SiO 2 particles were subjected to alkylation treatment, so that the surface of the inorganic Fe 3 O 4 @SiO 2 particles was loaded with amino active groups, and the amino active groups were used to react with paraffin and perfluorooctanoic acid respectively, and the paraffin and perfluorooctanoic acid were grafted onto Fe 3 O 4 @SiO 2 On the surface of the particles, hydrophilic and lipophilic magnetic nanoparticles are formed. The emulsion formed by the configuration of the magnetic nanoparticles has good stability under high temperature and high salt conditions, and maintains the oil displacement effect of the emulsion system.
因此,本发明具有如下有益效果:(1)适用于黏度低于5000mPa·s的原油,适用原油粘度范围较宽,且对于高粘度稠油油藏的采收率有大幅提高;(2)乳状液体系具有较强的稳定性,能适用于高温高盐环境。Therefore, the present invention has the following beneficial effects: (1) suitable for crude oil with a viscosity lower than 5000mPa·s, suitable for a wide range of crude oil viscosity, and greatly improved recovery for high-viscosity heavy oil reservoirs; (2) milky The liquid system has strong stability and can be applied to high-temperature and high-salt environments.
具体实施方式Detailed ways
下面通过具体实施例,对本发明的技术方案做进一步说明。The technical solutions of the present invention will be further described below through specific examples.
本发明中,若非特指,所采用的原料和设备等均可从市场购得或是本领域常用的,实施例中的方法,如无特别说明,均为本领域的常规方法。In the present invention, unless otherwise specified, the raw materials and equipment used can be purchased from the market or commonly used in the field. The methods in the examples, unless otherwise specified, are conventional methods in the field.
实施例1Example 1
磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:The preparation method of magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成浓度为80g/L氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液,FeCl3溶液为FeCl3和HCl的混合水溶液,FeCl3浓度为2mol/L,HCl浓度为0.5mol/L;FeSO4溶液为FeSO4和HCl的混合水溶液;FeSO4浓度为1mol/L;HCl浓度为0.5mol/L;将氢氧化钠溶液加热至70℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,铁盐混合溶液添加量为氢氧化钠溶液的15wt%,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: dissolving sodium hydroxide in water to form a sodium hydroxide solution with a concentration of 80g/L; mixing equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed iron salt solution, FeCl 3 solution It is a mixed aqueous solution of FeCl 3 and HCl, the concentration of FeCl 3 is 2mol/L, and the concentration of HCl is 0.5mol/L; the FeSO 4 solution is a mixed aqueous solution of FeSO 4 and HCl; the concentration of FeSO 4 is 1mol/L; the concentration of HCl is 0.5mol /L; heat the sodium hydroxide solution to 70°C, dropwise add the iron salt mixed solution to the sodium hydroxide solution, the amount of the iron salt mixed solution added is 15wt% of the sodium hydroxide solution, and stop heating when the solution turns black , cooled to room temperature, separated the black product generated by the reaction, washed with water and dried to obtain Fe 3 O 4 nanoparticles;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成浓度为25g/L胶体溶液,加热至50℃,向胶体溶液中滴加浓度为2mol/L Na2SiO3溶液并同时滴加浓度为0.4mol/LH2SiO4溶液控制pH为9.5,Na2SiO3与Fe3O4纳米颗粒的质量比为1:0.5,反应3h,升温至90℃再反应1h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to form a colloidal solution with a concentration of 25g/L, heat to 50°C, and drop Na 2 SiO with a concentration of 2mol/L into the colloidal solution 3 solution and at the same time dropwise add a concentration of 0.4mol/L H 2 SiO 4 solution to control the pH to 9.5, the mass ratio of Na 2 SiO 3 to Fe 3 O 4 nanoparticles is 1:0.5, react for 3h, heat up to 90°C and react for 1h , wash with deionized water under the action of a magnet, add the cleaned particles into boiling water to boil, wash with deionized water under the action of a magnet, and dry in vacuum to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂KH-550加入乙醇水溶液中进行水解,氨基硅烷偶联剂KH-550与无水乙醇体积比为1:30,然后向水解液中加入Fe3O4@SiO2颗粒,Fe3O4@SiO2颗粒在水解液中的初始浓度为10g/L,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: add aminosilane coupling agent KH-550 into ethanol aqueous solution for hydrolysis, the volume ratio of aminosilane coupling agent KH - 550 to absolute ethanol is 1:30, and then add Fe3 to the hydrolyzate O 4 @SiO 2 particles, the initial concentration of Fe 3 O 4 @SiO 2 particles in the hydrolyzed solution is 10g/L, stirred and reacted, washed with absolute ethanol under the action of a magnet, and dried to obtain alkylated Fe 3 O 4 @SiO 2 pellets;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,烷基化Fe3O4@SiO2颗粒在混合液中的浓度为30g/L,石蜡在混合液中的浓度为100g/L,在75℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,石蜡乳滴与全氟辛酸的质量比为1:0.1,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: a mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, the concentration of alkylated Fe 3 O 4 @SiO 2 particles in the mixed solution is 30g/L, The concentration of paraffin in the mixed liquid is 100g/L. Stir and emulsify at 75°C to obtain an emulsion, cool until the paraffin is solidified, wash with deionized water under the action of a magnet, and dry to obtain paraffin emulsion; mix the paraffin emulsion with PFOA solution, paraffin wax The mass ratio of emulsion droplets to perfluorooctanoic acid is 1:0.1, react at room temperature, wash with ethanol under the action of a magnet, and dry to obtain the product.
泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂十二烷基硫酸钠;泡沫体系的制备方法包括以下步骤:将起泡剂十二烷基硫酸钠和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,表面活性剂的浓度为0.2g/L,磁性纳米Fe3O4@SiO2颗粒浓度为2g/L,以3000r/min高速搅拌2min,即得。The emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and foaming agent sodium lauryl sulfate; the preparation method of foam system comprises the following steps: mixing the foaming agent sodium lauryl sulfate and foam stabilizer Add magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, the concentration of surfactant is 0.2g/L, the concentration of magnetic nano-Fe 3 O 4 @SiO 2 particles is 2g/L, stir at 3000r/min for 2min, Instantly.
Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂石油羧酸盐和聚合物聚丙烯酰胺。Pickering乳状液体系的制备方法包括以下步骤:The emulsifiers of the Pickering emulsion system include magnetic nano-Fe3O4@SiO2 particles, surfactant petroleum carboxylate and polymer polyacrylamide. The preparation method of Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,水相溶液中磁性纳米Fe3O4@SiO2颗粒浓度为2g/L,表面活性剂的浓度为0.2g/L,聚合物的浓度为1000mg/L;超声分散均匀;取煤油加入水相溶液组成上下分层的油水体系,水相和油相的体积比为1:4,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form an aqueous phase solution. The concentration of magnetic nano - Fe3O4 @ SiO2 particles in the aqueous phase solution is 2g/L, and the concentration of surfactant is 0.2g/L, the concentration of the polymer is 1000mg/L; ultrasonic dispersion is uniform; kerosene is added to the water phase solution to form a layered oil-water system, the volume ratio of the water phase and the oil phase is 1:4, as for the homogenizer Homogenize to obtain a uniformly mixed oil-water system, let it stand at room temperature, and then separate the precipitated oil phase and water phase to obtain the product.
适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油3次(先Pickering乳状液体系驱,然后泡沫体系驱,再Pickering乳状液体系驱);Pickering乳状液体系与泡沫体系总段塞注入量为0.6PV;Pickering乳状液体系段塞注入量为0.4PV,泡沫体系段塞注入量为0.2PV。The oil displacement method suitable for heavy oil reservoirs, the Pickering emulsion system and the foam system are alternately displaced by slug combination three times (Pickering emulsion system flooding first, then foam system flooding, then Pickering emulsion system flooding); The total slug injection volume of Pickering emulsion system and foam system is 0.6PV; the slug injection volume of Pickering emulsion system is 0.4PV, and the slug injection volume of foam system is 0.2PV.
实施例2Example 2
磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:The preparation method of magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成浓度为80g/L氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液,FeCl3溶液为FeCl3和HCl的混合水溶液,FeCl3浓度为2mol/L,HCl浓度为0.5mol/L;FeSO4溶液为FeSO4和HCl的混合水溶液;FeSO4浓度为1mol/L;HCl浓度为0.5mol/L;将氢氧化钠溶液加热至75℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,铁盐混合溶液添加量为氢氧化钠溶液的15wt%,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: dissolving sodium hydroxide in water to form a sodium hydroxide solution with a concentration of 80g/L; mixing equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed iron salt solution, FeCl 3 solution It is a mixed aqueous solution of FeCl 3 and HCl, the concentration of FeCl 3 is 2mol/L, and the concentration of HCl is 0.5mol/L; the FeSO 4 solution is a mixed aqueous solution of FeSO 4 and HCl; the concentration of FeSO 4 is 1mol/L; the concentration of HCl is 0.5mol /L; heat the sodium hydroxide solution to 75°C, dropwise add the iron salt mixed solution to the sodium hydroxide solution, the amount of the iron salt mixed solution added is 15wt% of the sodium hydroxide solution, stop heating until the solution turns black , cooled to room temperature, separated the black product generated by the reaction, washed with water and dried to obtain Fe 3 O 4 nanoparticles;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成浓度为25g/L胶体溶液,加热至55℃,向胶体溶液中滴加浓度为2mol/L Na2SiO3溶液并同时滴加浓度为0.4mol/LH2SiO4溶液控制pH为10,Na2SiO3与Fe3O4纳米颗粒的质量比为1:0.5,反应4h,升温至95℃再反应1h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to prepare a colloidal solution with a concentration of 25g/L, heat to 55°C, and drop Na 2 SiO with a concentration of 2mol/L into the colloidal solution 3 solution and at the same time dropwise add a concentration of 0.4mol/L H 2 SiO 4 solution to control the pH to 10, the mass ratio of Na 2 SiO 3 to Fe 3 O 4 nanoparticles is 1:0.5, react for 4h, heat up to 95°C and react for 1h , wash with deionized water under the action of a magnet, add the cleaned particles into boiling water to boil, wash with deionized water under the action of a magnet, and dry in vacuum to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂KH-550加入乙醇水溶液中进行水解,氨基硅烷偶联剂KH-550与无水乙醇体积比为1:30,然后向水解液中加入Fe3O4@SiO2颗粒,Fe3O4@SiO2颗粒在水解液中的初始浓度为10g/L,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: add aminosilane coupling agent KH-550 into ethanol aqueous solution for hydrolysis, the volume ratio of aminosilane coupling agent KH - 550 to absolute ethanol is 1:30, and then add Fe3 to the hydrolyzate O 4 @SiO 2 particles, the initial concentration of Fe 3 O 4 @SiO 2 particles in the hydrolyzed solution is 10g/L, stirred and reacted, washed with absolute ethanol under the action of a magnet, and dried to obtain alkylated Fe 3 O 4 @SiO 2 pellets;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,烷基化Fe3O4@SiO2颗粒在混合液中的浓度为30g/L,石蜡在混合液中的浓度为100g/L,在80℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,石蜡乳滴与全氟辛酸的质量比为1:0.1,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: a mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, the concentration of alkylated Fe 3 O 4 @SiO 2 particles in the mixed solution is 30g/L, The concentration of paraffin in the mixed solution is 100g/L. Stir and emulsify at 80°C to obtain an emulsion, cool until the paraffin solidifies, wash with deionized water under the action of a magnet, and dry to obtain paraffin emulsion; mix the paraffin emulsion with PFOA solution, and the paraffin wax The mass ratio of emulsion droplets to perfluorooctanoic acid is 1:0.1, react at room temperature, wash with ethanol under the action of a magnet, and dry to obtain the product.
泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂十二烷基硫酸钠;泡沫体系的制备方法包括以下步骤:将起泡剂十二烷基硫酸钠和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,表面活性剂的浓度为0.3g/L,磁性纳米Fe3O4@SiO2颗粒浓度为2g/L,以4000r/min高速搅拌3min,即得。The emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and foaming agent sodium lauryl sulfate; the preparation method of foam system comprises the following steps: mixing the foaming agent sodium lauryl sulfate and foam stabilizer Add magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, the concentration of surfactant is 0.3g/L, the concentration of magnetic nano-Fe 3 O 4 @SiO 2 particles is 2g/L, stir at 4000r/min for 3min, Instantly.
Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂石油磺酸盐和聚合物黄原胶。Pickering乳状液体系的制备方法包括以下步骤:The emulsifiers of the Pickering emulsion system include magnetic nano-Fe3O4@SiO2 particles, surfactant petroleum sulfonate and polymer xanthan gum. The preparation method of Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,水相溶液中磁性纳米Fe3O4@SiO2颗粒浓度为2.5g/L,表面活性剂的浓度为0.3g/L,聚合物的浓度为1200mg/L;超声分散均匀;取植物油加入水相溶液组成上下分层的油水体系,水相和油相的体积比为1:4,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form an aqueous phase solution. The concentration of magnetic nano - Fe3O4 @ SiO2 particles in the aqueous phase solution is 2.5g/L, and the concentration of surfactant The concentration of the polymer is 0.3g/L, the concentration of the polymer is 1200mg/L; the ultrasonic dispersion is uniform; the vegetable oil is added to the water phase solution to form a layered oil-water system, the volume ratio of the water phase and the oil phase is 1:4, as for the homogenizer Homogenize in a medium to obtain a uniformly mixed oil-water system, let it stand at room temperature, and then separate the precipitated oil phase and water phase to obtain.
适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油4次(Pickering乳状液体系驱-泡沫体系驱-Pickering乳状液体系驱-泡沫体系驱);Pickering乳状液体系与泡沫体系总段塞注入量为0.8PV;Pickering乳状液体系段塞注入量为0.4PV,泡沫体系段塞注入量为0.4PV。The oil displacement method suitable for heavy oil reservoirs, the Pickering emulsion system and the foam system are alternately displaced by slug combination four times (Pickering emulsion system flooding-foam system flooding-Pickering emulsion system flooding-foam system flooding) The total slug injection volume of Pickering emulsion system and foam system is 0.8PV; the slug injection volume of Pickering emulsion system is 0.4PV, and the slug injection volume of foam system is 0.4PV.
实施例3Example 3
磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:The preparation method of magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成浓度为80g/L氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液,FeCl3溶液为FeCl3和HCl的混合水溶液,FeCl3浓度为2mol/L,HCl浓度为0.5mol/L;FeSO4溶液为FeSO4和HCl的混合水溶液;FeSO4浓度为1mol/L;HCl浓度为0.5mol/L;将氢氧化钠溶液加热至65℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,铁盐混合溶液添加量为氢氧化钠溶液的15wt%,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: dissolving sodium hydroxide in water to form a sodium hydroxide solution with a concentration of 80g/L; mixing equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed iron salt solution, FeCl 3 solution It is a mixed aqueous solution of FeCl 3 and HCl, the concentration of FeCl 3 is 2mol/L, and the concentration of HCl is 0.5mol/L; the FeSO 4 solution is a mixed aqueous solution of FeSO 4 and HCl; the concentration of FeSO 4 is 1mol/L; the concentration of HCl is 0.5mol /L; heat the sodium hydroxide solution to 65°C, dropwise add the iron salt mixed solution to the sodium hydroxide solution, the amount of the iron salt mixed solution added is 15wt% of the sodium hydroxide solution, stop heating until the solution turns black , cooled to room temperature, separated the black product generated by the reaction, washed with water and dried to obtain Fe 3 O 4 nanoparticles;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成浓度为25g/L胶体溶液,加热至45℃,向胶体溶液中滴加浓度为2mol/L Na2SiO3溶液并同时滴加浓度为0.4mol/LH2SiO4溶液控制pH为9,Na2SiO3与Fe3O4纳米颗粒的质量比为1:0.5,反应3h,升温至85℃再反应1h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to prepare a colloidal solution with a concentration of 25g/L, heat to 45°C, and drop Na 2 SiO with a concentration of 2mol/L into the colloidal solution 3 solution and at the same time dropwise add the concentration of 0.4mol/L H 2 SiO 4 solution to control the pH to 9, the mass ratio of Na 2 SiO 3 to Fe 3 O 4 nanoparticles is 1:0.5, react for 3h, heat up to 85°C and react for 1h , wash with deionized water under the action of a magnet, add the cleaned particles into boiling water to boil, wash with deionized water under the action of a magnet, and dry in vacuum to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂KH-550加入乙醇水溶液中进行水解,氨基硅烷偶联剂KH-550与无水乙醇体积比为1:30,然后向水解液中加入Fe3O4@SiO2颗粒,Fe3O4@SiO2颗粒在水解液中的初始浓度为10g/L,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: add aminosilane coupling agent KH-550 into ethanol aqueous solution for hydrolysis, the volume ratio of aminosilane coupling agent KH - 550 to absolute ethanol is 1:30, and then add Fe3 to the hydrolyzate O 4 @SiO 2 particles, the initial concentration of Fe 3 O 4 @SiO 2 particles in the hydrolyzed solution is 10g/L, stirred and reacted, washed with absolute ethanol under the action of a magnet, and dried to obtain alkylated Fe 3 O 4 @SiO 2 pellets;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,烷基化Fe3O4@SiO2颗粒在混合液中的浓度为30g/L,石蜡在混合液中的浓度为100g/L,在70℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,石蜡乳滴与全氟辛酸的质量比为1:0.1,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: a mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, the concentration of alkylated Fe 3 O 4 @SiO 2 particles in the mixed solution is 30g/L, The concentration of paraffin in the mixed solution is 100g/L. Stir and emulsify at 70°C to obtain an emulsion, cool until the paraffin is solidified, wash with deionized water under the action of a magnet, and dry to obtain paraffin emulsion; mix the paraffin emulsion with PFOA solution, paraffin wax The mass ratio of emulsion droplets to perfluorooctanoic acid is 1:0.1, react at room temperature, wash with ethanol under the action of a magnet, and dry to obtain the product.
泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂十二烷基硫酸钠;泡沫体系的制备方法包括以下步骤:将起泡剂十二烷基硫酸钠和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,表面活性剂的浓度为0.15g/L,磁性纳米Fe3O4@SiO2颗粒浓度为1g/L,以3000r/min高速搅拌2min,即得。The emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and foaming agent sodium lauryl sulfate; the preparation method of foam system comprises the following steps: mixing the foaming agent sodium lauryl sulfate and foam stabilizer Add magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, the concentration of surfactant is 0.15g/L, the concentration of magnetic nano-Fe 3 O 4 @SiO 2 particles is 1g/L, stir at 3000r/min for 2min, Instantly.
Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂重烷基苯磺酸盐和聚合物聚乙二醇。Pickering乳状液体系的制备方法包括以下步骤:The emulsifiers of the Pickering emulsion system include magnetic nano-Fe3O4@SiO2 particles, surfactant heavy alkylbenzene sulfonate and polymer polyethylene glycol. The preparation method of Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,水相溶液中磁性纳米Fe3O4@SiO2颗粒浓度为1g/L,表面活性剂的浓度为0.15g/L,聚合物的浓度为800mg/L;超声分散均匀;取白油加入水相溶液组成上下分层的油水体系,水相和油相的体积比为1:3,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form an aqueous phase solution. The concentration of magnetic nano - Fe3O4 @ SiO2 particles in the aqueous phase solution is 1g/L, and the concentration of surfactant is 0.15g/L, the concentration of the polymer is 800mg/L; ultrasonic dispersion is uniform; take white oil and add water phase solution to form an oil-water system with upper and lower layers. The volume ratio of water phase and oil phase is 1:3. As for the homogenizer Homogenize in a medium to obtain a uniformly mixed oil-water system, let it stand at room temperature, and then separate the precipitated oil phase and water phase to obtain.
适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油2次(先Pickering乳状液体系驱油,然后泡沫体系驱油);Pickering乳状液体系与泡沫体系总段塞注入量为0.4PV;Pickering乳状液体系段塞注入量为0.2PV,泡沫体系段塞注入量为0.2PV。The oil displacement method suitable for heavy oil reservoirs, the Pickering emulsion system and the foam system are alternately displaced twice in a slug combination (first the Pickering emulsion system drives oil, then the foam system drives oil); the Pickering emulsion system and the foam system drive oil twice; The total slug injection volume of the foam system is 0.4PV; the slug injection volume of the Pickering emulsion system is 0.2PV, and the slug injection volume of the foam system is 0.2PV.
实施例4Example 4
磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:The preparation method of magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成浓度为80g/L氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液,FeCl3溶液为FeCl3和HCl的混合水溶液,FeCl3浓度为2mol/L,HCl浓度为0.5mol/L;FeSO4溶液为FeSO4和HCl的混合水溶液;FeSO4浓度为1mol/L;HCl浓度为0.5mol/L;将氢氧化钠溶液加热至80℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,铁盐混合溶液添加量为氢氧化钠溶液的15wt%,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: dissolving sodium hydroxide in water to form a sodium hydroxide solution with a concentration of 80g/L; mixing equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed iron salt solution, FeCl 3 solution It is a mixed aqueous solution of FeCl 3 and HCl, the concentration of FeCl 3 is 2mol/L, and the concentration of HCl is 0.5mol/L; the FeSO 4 solution is a mixed aqueous solution of FeSO 4 and HCl; the concentration of FeSO 4 is 1mol/L; the concentration of HCl is 0.5mol /L; heat the sodium hydroxide solution to 80°C, dropwise add the iron salt mixed solution to the sodium hydroxide solution, the amount of the iron salt mixed solution added is 15wt% of the sodium hydroxide solution, stop heating until the solution turns black , cooled to room temperature, separated the black product generated by the reaction, washed with water and dried to obtain Fe 3 O 4 nanoparticles;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成浓度为25g/L胶体溶液,加热至60℃,向胶体溶液中滴加浓度为2mol/L Na2SiO3溶液并同时滴加浓度为0.4mol/LH2SiO4溶液控制pH为10,Na2SiO3与Fe3O4纳米颗粒的质量比为1:0.5,反应4h,升温至95℃再反应1h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to prepare a colloidal solution with a concentration of 25g/L, heat to 60°C, and add Na 2 SiO with a concentration of 2mol/L to the colloidal solution dropwise 3 solution and at the same time dropwise add a concentration of 0.4mol/L H 2 SiO 4 solution to control the pH to 10, the mass ratio of Na 2 SiO 3 to Fe 3 O 4 nanoparticles is 1:0.5, react for 4h, heat up to 95°C and react for 1h , wash with deionized water under the action of a magnet, add the cleaned particles into boiling water to boil, wash with deionized water under the action of a magnet, and dry in vacuum to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂KH-550加入乙醇水溶液中进行水解,氨基硅烷偶联剂KH-550与无水乙醇体积比为1:30,然后向水解液中加入Fe3O4@SiO2颗粒,Fe3O4@SiO2颗粒在水解液中的初始浓度为10g/L,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: add aminosilane coupling agent KH-550 into ethanol aqueous solution for hydrolysis, the volume ratio of aminosilane coupling agent KH - 550 to absolute ethanol is 1:30, and then add Fe3 to the hydrolyzate O 4 @SiO 2 particles, the initial concentration of Fe 3 O 4 @SiO 2 particles in the hydrolyzed solution is 10g/L, stirred and reacted, washed with absolute ethanol under the action of a magnet, and dried to obtain alkylated Fe 3 O 4 @SiO 2 pellets;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,烷基化Fe3O4@SiO2颗粒在混合液中的浓度为30g/L,石蜡在混合液中的浓度为100g/L,在80℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,石蜡乳滴与全氟辛酸的质量比为1:0.1,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: a mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, the concentration of alkylated Fe 3 O 4 @SiO 2 particles in the mixed solution is 30g/L, The concentration of paraffin in the mixed solution is 100g/L. Stir and emulsify at 80°C to obtain an emulsion, cool until the paraffin solidifies, wash with deionized water under the action of a magnet, and dry to obtain paraffin emulsion; mix the paraffin emulsion with PFOA solution, and the paraffin wax The mass ratio of emulsion droplets to perfluorooctanoic acid is 1:0.1, react at room temperature, wash with ethanol under the action of a magnet, and dry to obtain the product.
泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂十二烷基硫酸钠;泡沫体系的制备方法包括以下步骤:将起泡剂十二烷基硫酸钠和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,表面活性剂的浓度为0.3g/L,磁性纳米Fe3O4@SiO2颗粒浓度为3g/L,以5000r/min高速搅拌1min,即得。The emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and foaming agent sodium lauryl sulfate; the preparation method of foam system comprises the following steps: mixing the foaming agent sodium lauryl sulfate and foam stabilizer Add magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, the concentration of surfactant is 0.3g/L, the concentration of magnetic nano-Fe 3 O 4 @SiO 2 particles is 3g/L, stir at 5000r/min for 1min, Instantly.
Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂木质素磺酸盐和聚合物褐藻酸钠。Pickering乳状液体系的制备方法包括以下步骤:The emulsifiers of the Pickering emulsion system include magnetic nano-Fe3O4@SiO2 particles, surfactant lignosulfonate and polymer sodium alginate. The preparation method of Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,水相溶液中磁性纳米Fe3O4@SiO2颗粒浓度为3g/L,表面活性剂的浓度为0.3g/L,聚合物的浓度为1500mg/L;超声分散均匀;取汽油加入水相溶液组成上下分层的油水体系,水相和油相的体积比为1:5,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form an aqueous phase solution. The concentration of magnetic nano - Fe3O4 @ SiO2 particles in the aqueous phase solution is 3g/L, and the concentration of surfactant is 0.3g/L, the concentration of the polymer is 1500mg/L; the ultrasonic dispersion is uniform; take gasoline and add the water phase solution to form a layered oil-water system, the volume ratio of the water phase and the oil phase is 1:5, as for the homogenizer Homogenize to obtain a uniformly mixed oil-water system, let it stand at room temperature, and then separate the precipitated oil phase and water phase to obtain the product.
适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油4次(Pickering乳状液体系驱-泡沫体系驱-Pickering乳状液体系驱-泡沫体系驱);Pickering乳状液体系与泡沫体系总段塞注入量为0.8PV;Pickering乳状液体系段塞注入量为0.4PV,泡沫体系段塞注入量为0.4PV。The oil displacement method suitable for heavy oil reservoirs, the Pickering emulsion system and the foam system are alternately displaced by slug combination four times (Pickering emulsion system flooding-foam system flooding-Pickering emulsion system flooding-foam system flooding) The total slug injection volume of Pickering emulsion system and foam system is 0.8PV; the slug injection volume of Pickering emulsion system is 0.4PV, and the slug injection volume of foam system is 0.4PV.
实施例5Example 5
磁性纳米Fe3O4@SiO2颗粒的制备方法包括以下步骤:The preparation method of magnetic nano Fe3O4@SiO2 particles comprises the following steps:
1)Fe3O4纳米颗粒制备:将氢氧化钠溶于水中配置成浓度为80g/L氢氧化钠溶液;将等体积的FeCl3溶液和FeSO4溶液混合得铁盐混合溶液,FeCl3溶液为FeCl3和HCl的混合水溶液,FeCl3浓度为2mol/L,HCl浓度为0.5mol/L;FeSO4溶液为FeSO4和HCl的混合水溶液;FeSO4浓度为1mol/L;HCl浓度为0.5mol/L;将氢氧化钠溶液加热至60℃,逐滴将铁盐混合溶液滴加到氢氧化钠溶液中,铁盐混合溶液添加量为氢氧化钠溶液的15wt%,待溶液变黑停止加热,冷却至室温,分离反应生成的黑色产物,经过水洗、干燥得Fe3O4纳米颗粒;1) Preparation of Fe 3 O 4 nanoparticles: dissolving sodium hydroxide in water to form a sodium hydroxide solution with a concentration of 80g/L; mixing equal volumes of FeCl 3 solution and FeSO 4 solution to obtain a mixed iron salt solution, FeCl 3 solution It is a mixed aqueous solution of FeCl 3 and HCl, the concentration of FeCl 3 is 2mol/L, and the concentration of HCl is 0.5mol/L; the FeSO 4 solution is a mixed aqueous solution of FeSO 4 and HCl; the concentration of FeSO 4 is 1mol/L; the concentration of HCl is 0.5mol /L; heat the sodium hydroxide solution to 60°C, add the iron salt mixed solution dropwise to the sodium hydroxide solution, the amount of the iron salt mixed solution added is 15wt% of the sodium hydroxide solution, and stop heating when the solution turns black , cooled to room temperature, separated the black product generated by the reaction, washed with water and dried to obtain Fe 3 O 4 nanoparticles;
2)Fe3O4@SiO2颗粒制备:将Fe3O4纳米颗粒加入水中配置成浓度为25g/L胶体溶液,加热至40℃,向胶体溶液中滴加浓度为2mol/L Na2SiO3溶液并同时滴加浓度为0.4mol/LH2SiO4溶液控制pH为9,Na2SiO3与Fe3O4纳米颗粒的质量比为1:0.5,反应3h,升温至80℃再反应2h,在磁体作用下去离子水清洗,清洗后的颗粒加入沸水中煮沸,在磁体作用下去离子水清洗,真空干燥得到Fe3O4@SiO2颗粒;2) Preparation of Fe 3 O 4 @SiO 2 particles: Add Fe 3 O 4 nanoparticles into water to form a colloidal solution with a concentration of 25g/L, heat to 40°C, and add Na 2 SiO with a concentration of 2mol/L to the colloidal solution dropwise 3 solution and at the same time drop the concentration of 0.4mol/L H 2 SiO 4 solution to control the pH to 9, the mass ratio of Na 2 SiO 3 and Fe 3 O 4 nanoparticles is 1:0.5, react for 3h, heat up to 80°C and react for 2h , wash with deionized water under the action of a magnet, add the cleaned particles into boiling water to boil, wash with deionized water under the action of a magnet, and dry in vacuum to obtain Fe 3 O 4 @SiO 2 particles;
3)烷基化处理:将氨基硅烷偶联剂KH-550加入乙醇水溶液中进行水解,氨基硅烷偶联剂KH-550与无水乙醇体积比为1:30,然后向水解液中加入Fe3O4@SiO2颗粒,Fe3O4@SiO2颗粒在水解液中的初始浓度为10g/L,搅拌反应,在磁铁作用下无水乙醇清洗,干燥得烷基化Fe3O4@SiO2颗粒;3) Alkylation treatment: add aminosilane coupling agent KH-550 into ethanol aqueous solution for hydrolysis, the volume ratio of aminosilane coupling agent KH - 550 to absolute ethanol is 1:30, and then add Fe3 to the hydrolyzate O 4 @SiO 2 particles, the initial concentration of Fe 3 O 4 @SiO 2 particles in the hydrolyzed solution is 10g/L, stirred and reacted, washed with absolute ethanol under the action of a magnet, and dried to obtain alkylated Fe 3 O 4 @SiO 2 pellets;
4)接枝:将烷基化Fe3O4@SiO2颗粒、石蜡和去离子水混合的混合液,烷基化Fe3O4@SiO2颗粒在混合液中的浓度为30g/L,石蜡在混合液中的浓度为100g/L,在70℃下搅拌乳化得乳状液,冷却至石蜡固化,磁铁作用下去离子水清洗,干燥得石蜡乳滴;将石蜡乳滴与全氟辛酸溶液混合,石蜡乳滴与全氟辛酸的质量比为1:0.1,室温反应,磁铁作用下乙醇清洗,干燥,即得。4) Grafting: a mixture of alkylated Fe 3 O 4 @SiO 2 particles, paraffin and deionized water, the concentration of alkylated Fe 3 O 4 @SiO 2 particles in the mixed solution is 30g/L, The concentration of paraffin in the mixed solution is 100g/L. Stir and emulsify at 70°C to obtain an emulsion, cool until the paraffin is solidified, wash with deionized water under the action of a magnet, and dry to obtain paraffin emulsion; mix the paraffin emulsion with PFOA solution, paraffin wax The mass ratio of emulsion droplets to perfluorooctanoic acid is 1:0.1, react at room temperature, wash with ethanol under the action of a magnet, and dry to obtain the product.
泡沫体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒和起泡剂十二烷基硫酸钠;泡沫体系的制备方法包括以下步骤:将起泡剂十二烷基硫酸钠和稳泡剂磁性纳米Fe3O4@SiO2颗粒加入去离子水中,表面活性剂的浓度为0.1g/L,磁性纳米Fe3O4@SiO2颗粒浓度为0.5g/L,以2000r/min高速搅拌3min,即得。The emulsifier of the foam system includes magnetic nano Fe 3 O 4 @SiO 2 particles and foaming agent sodium lauryl sulfate; the preparation method of foam system comprises the following steps: mixing the foaming agent sodium lauryl sulfate and foam stabilizer Add magnetic nano-Fe 3 O 4 @SiO 2 particles into deionized water, the concentration of surfactant is 0.1g/L, the concentration of magnetic nano-Fe 3 O 4 @SiO 2 particles is 0.5g/L, stir at 2000r/min for 3min , that is.
Pickering乳状液体系的乳化剂包括磁性纳米Fe3O4@SiO2颗粒、表面活性剂生物表面活性剂和聚合物硬葡聚糖。Pickering乳状液体系的制备方法包括以下步骤:The emulsifiers of the Pickering emulsion system include magnetic nano-Fe3O4@SiO2 particles, surfactant biosurfactant and polymer scleroglucan. The preparation method of Pickering emulsion system comprises the following steps:
将磁性纳米Fe3O4@SiO2颗粒、表面活性剂、聚合物和去离子水混合组成水相溶液,水相溶液中磁性纳米Fe3O4@SiO2颗粒浓度为0.5g/L,表面活性剂的浓度为0.1g/L,聚合物的浓度为500mg/L;超声分散均匀;取柴油加入水相溶液组成上下分层的油水体系,水相和油相的体积比为1:3,至于均质机中进行均质得混合均匀的油水体系,室温静置,然后分离析出的油相和水相,即得。Mix magnetic nano-Fe3O4@SiO2 particles, surfactants, polymers and deionized water to form an aqueous phase solution. The concentration of magnetic nano - Fe3O4 @ SiO2 particles in the aqueous phase solution is 0.5g/L, and the concentration of surfactant The concentration of the polymer is 0.1g/L, the concentration of the polymer is 500mg/L; the ultrasonic dispersion is uniform; the diesel oil is added to the water phase solution to form a layered oil-water system, the volume ratio of the water phase and the oil phase is 1:3, as for the homogenizer Homogenize in a medium to obtain a uniformly mixed oil-water system, let it stand at room temperature, and then separate the precipitated oil phase and water phase to obtain.
适用于稠油油藏的驱油方法,将Pickering乳状液体系和泡沫体系以段塞组合方式交替驱油2次(先Pickering乳状液体系驱油,然后泡沫体系驱油);Pickering乳状液体系与泡沫体系总段塞注入量为0.4PV;Pickering乳状液体系段塞注入量为0.3PV,泡沫体系段塞注入量为0.1PV。The oil displacement method suitable for heavy oil reservoirs, the Pickering emulsion system and the foam system are alternately displaced twice in a slug combination (first the Pickering emulsion system drives oil, then the foam system drives oil); the Pickering emulsion system and the foam system drive oil twice; The total slug injection volume of the foam system is 0.4PV; the slug injection volume of the Pickering emulsion system is 0.3PV, and the slug injection volume of the foam system is 0.1PV.
试验测试:Experimental test:
选取渗透率约为1000mD的岩心,抽真空,饱和地层水,称湿重,计算岩心孔隙度;岩心装入夹持器,连接管线,驱替原油,造束缚水,老化30h。用地层水驱替岩心中的原油,直到出口端不见出油,记录出口的出油量,计算水驱采收率;转注一定段塞尺寸的磁性Pickering乳状液,注入完毕以后,转注一定段塞尺寸的泡沫体系,再往岩心中注地层水,直到出口端不见油,停止注入,记录出口的出油量,计算磁性Pickering乳状液提高原油采收率。Select a core with a permeability of about 1000mD, vacuumize, saturate the formation water, weigh the wet weight, and calculate the porosity of the core; put the core into a holder, connect the pipeline, displace crude oil, create bound water, and age for 30 hours. Use formation water to displace the crude oil in the rock core until no oil comes out at the outlet, record the oil output at the outlet, and calculate the water flooding recovery; transfer a certain slug size of magnetic Pickering emulsion, after the injection is completed, transfer a certain slug Then inject formation water into the core of the rock until there is no oil at the outlet, stop the injection, record the oil output at the outlet, and calculate the enhanced oil recovery of the magnetic Pickering emulsion.
由实验数据可以得到本发明对粘度高达4000mPa·s的原油进行驱油,提高原油采收率保持在20%以上,证明本发明对高粘度稠油油藏的采收率有大幅提高,适用于高粘度原油采收。From the experimental data, it can be obtained that the present invention can drive oil with a viscosity as high as 4000mPa·s, and the enhanced oil recovery rate can be kept above 20%. High viscosity crude oil recovery.
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明,任何熟悉本专业的技术人员,在不脱离本发明技术方案范围内,当可利用上述揭示的技术内容作出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案内容,依据本发明的技术实质对以上实施例所作的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。The above description is only a preferred embodiment of the present invention, and does not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with this field Those skilled in the art, without departing from the scope of the technical solution of the present invention, may use the technical content disclosed above to make some changes or modify them into equivalent embodiments with equivalent changes, but as long as they do not depart from the technical solution of the present invention, the Technical Essence Any simple modifications, equivalent changes and modifications made to the above embodiments still fall within the scope of the technical solution of the present invention.
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