CN115386358B - Natural surfactant compound system and preparation method thereof - Google Patents
Natural surfactant compound system and preparation method thereof Download PDFInfo
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- 150000001875 compounds Chemical class 0.000 title claims abstract description 66
- 239000004094 surface-active agent Substances 0.000 title claims abstract description 33
- 238000002360 preparation method Methods 0.000 title claims abstract description 32
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 claims abstract description 66
- 229930182490 saponin Natural products 0.000 claims abstract description 33
- 150000007949 saponins Chemical class 0.000 claims abstract description 33
- 239000001397 quillaja saponaria molina bark Substances 0.000 claims abstract description 32
- 235000018597 common camellia Nutrition 0.000 claims abstract description 26
- 239000001763 2-hydroxyethyl(trimethyl)azanium Substances 0.000 claims abstract description 22
- 235000019743 Choline chloride Nutrition 0.000 claims abstract description 22
- SGMZJAMFUVOLNK-UHFFFAOYSA-M choline chloride Chemical compound [Cl-].C[N+](C)(C)CCO SGMZJAMFUVOLNK-UHFFFAOYSA-M 0.000 claims abstract description 22
- 229960003178 choline chloride Drugs 0.000 claims abstract description 22
- 239000002131 composite material Substances 0.000 claims abstract description 9
- 235000015165 citric acid Nutrition 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 47
- 239000002904 solvent Substances 0.000 claims description 29
- 230000005496 eutectics Effects 0.000 claims description 27
- 241000526900 Camellia oleifera Species 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- 241000209507 Camellia Species 0.000 claims 3
- 240000001548 Camellia japonica Species 0.000 abstract description 23
- 230000000694 effects Effects 0.000 abstract description 14
- 238000006073 displacement reaction Methods 0.000 abstract description 10
- 230000036571 hydration Effects 0.000 abstract description 8
- 238000006703 hydration reaction Methods 0.000 abstract description 8
- 230000015572 biosynthetic process Effects 0.000 abstract description 5
- 239000002994 raw material Substances 0.000 abstract description 4
- 230000005764 inhibitory process Effects 0.000 abstract description 3
- 239000002734 clay mineral Substances 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 29
- 235000017709 saponins Nutrition 0.000 description 28
- 238000002347 injection Methods 0.000 description 22
- 239000007924 injection Substances 0.000 description 22
- 238000011084 recovery Methods 0.000 description 14
- 239000000243 solution Substances 0.000 description 14
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 12
- 238000003756 stirring Methods 0.000 description 12
- 229910052901 montmorillonite Inorganic materials 0.000 description 11
- 238000012360 testing method Methods 0.000 description 11
- 238000002474 experimental method Methods 0.000 description 9
- 230000001965 increasing effect Effects 0.000 description 7
- 238000002329 infrared spectrum Methods 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- 239000012153 distilled water Substances 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000011148 porous material Substances 0.000 description 5
- 239000011734 sodium Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 230000015784 hyperosmotic salinity response Effects 0.000 description 4
- 230000002401 inhibitory effect Effects 0.000 description 4
- IOLCXVTUBQKXJR-UHFFFAOYSA-M potassium bromide Chemical compound [K+].[Br-] IOLCXVTUBQKXJR-UHFFFAOYSA-M 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 239000003945 anionic surfactant Substances 0.000 description 3
- 150000001450 anions Chemical class 0.000 description 3
- 238000005452 bending Methods 0.000 description 3
- 238000013329 compounding Methods 0.000 description 3
- 239000010779 crude oil Substances 0.000 description 3
- 239000002608 ionic liquid Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 2
- 239000003093 cationic surfactant Substances 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229930182470 glycoside Natural products 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 239000011435 rock Substances 0.000 description 2
- 239000009671 shengli Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 238000009736 wetting Methods 0.000 description 2
- 239000000370 acceptor Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- -1 glycoside compound Chemical class 0.000 description 1
- 150000002338 glycosides Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910001507 metal halide Inorganic materials 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003381 solubilizing effect Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000002522 swelling effect Effects 0.000 description 1
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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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- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
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Abstract
本发明公开了一种天然表面活性剂复配体系及其制备方法,其包括如下组分:氯化胆碱、柠檬酸、油茶皂素。本发明提供的复配体系能有效提高了黏土矿物水化膨胀的抑制性,在较大程度上降低了油藏各种复杂情况的发生;本发明提供的复配体系具有低的界面张力,制得的复配体系能有效提高驱油效率,降压效果显著;原料来源广泛,制备工艺简单,对地层无污染。
The invention discloses a natural surfactant compound system and a preparation method thereof, which comprises the following components: choline chloride, citric acid and camellia saponin. The compound system provided by the present invention can effectively improve the inhibition of clay mineral hydration expansion, and reduce the occurrence of various complex situations in oil reservoirs to a large extent; the compound system provided by the present invention has low interfacial tension, making The obtained composite system can effectively improve the oil displacement efficiency, and has a remarkable pressure-reducing effect; the source of raw materials is extensive, the preparation process is simple, and there is no pollution to the formation.
Description
技术领域technical field
本发明属于驱油剂制备技术领域,具体涉及到一种天然表面活性剂复配体系及其制备方法。The invention belongs to the technical field of oil displacement agent preparation, and in particular relates to a natural surfactant compound system and a preparation method thereof.
背景技术Background technique
低渗透油藏资源在我国占有重要战略地位,据我国第三次油气资源调查结果显示,低渗透油藏资源量占全国总资源量的49%。低渗透砂岩油藏由于其具有极差的油层物性以及毛管中较高的界面阻力效应使得储层具有流动性能差、注水阻力大等特点,油藏中天然能量不足,即使注水有效,也会因储层物性差、孔喉细、界面阻力高等导致注入阻力升高、甚至储层中注不进水,而高压注水会使地面设备和井下套管处于高压状态,损坏设备和井下套管,也会因高压使地层破裂,降低注入效率。因此长时间高压注水是不可行的,降低界面阻力与注入压力,探索低渗透油藏注水降压增注手段是改善注水开发效果的关键,而降压增注的原理多是依据降低界面张力,较少考虑细微孔喉中对渗流影响更为显著的固-液界面产生的阻力效应。Low-permeability reservoir resources occupy an important strategic position in my country. According to the results of the third survey of oil and gas resources in my country, the resources of low-permeability reservoirs account for 49% of the total resources in the country. Low-permeability sandstone reservoirs have the characteristics of poor fluidity and high water injection resistance due to their extremely poor oil layer physical properties and high interfacial resistance effect in the capillary. The natural energy in the reservoir is insufficient. Poor physical properties of the reservoir, thin pore throat, high interface resistance, etc. lead to increased injection resistance, and even no water can be injected into the reservoir, while high-pressure water injection will make the surface equipment and downhole casing under high pressure, damage the equipment and downhole casing, and cause The formation will be broken due to high pressure, reducing the injection efficiency. Therefore, long-term high-pressure water injection is not feasible. Reducing interfacial resistance and injection pressure, and exploring ways to reduce pressure and increase injection in low-permeability reservoirs are the key to improving the development effect of water injection. The principle of reducing pressure and increasing injection is mostly based on reducing interfacial tension. Less consideration is given to the resistance effect produced by the solid-liquid interface in the fine pore throat, which has a more significant impact on seepage.
表面活性剂驱属于三次采油,指的是通过向地层中注入表面活性剂,降低油水间的界面张力,进而达到提高油藏采收效率的效果,是一种能有效提高油藏采收率,具有极高发展潜力的化学驱油技术,在国内外均具有广泛的应用,应用最为普遍的为阴离子表面活性剂,应用最少的为阳离子表面活性剂,目前三次采油中的表面活性剂大多使用多元复配体系,如专利CN109207136A公开了一种应用于高矿化度油藏下的阴离子与阳离子表面活性剂复配体系,使得复配体系达到超低界面张力(10-3mN/m)的效果,再如专利CN103773346A公开了一种高效驱油的阳离子和阴非离子表面活性剂复配体系,此复配体系界面张力可达到超低界面张力,最终采收率提高7.5%。但目前的表面活性剂仍存在较多问题,如表面活性较差、提高采收率效果不理想,大多阴离子表面活性剂与无机碱共同使用,会对地层、管道设备等造成腐蚀,且各种驱油用表活剂还存在成本较高等问题。Surfactant flooding belongs to tertiary oil recovery, which refers to the injection of surfactants into the formation to reduce the interfacial tension between oil and water, thereby achieving the effect of improving the recovery efficiency of the reservoir. The chemical flooding technology with extremely high development potential has been widely used at home and abroad. The most widely used is anionic surfactant, and the least used is cationic surfactant. At present, most surfactants in tertiary oil recovery use multiple Compound system, such as patent CN109207136A discloses a compound system of anionic and cationic surfactants applied in high salinity oil reservoirs, so that the compound system can achieve the effect of ultra-low interfacial tension (10 -3 mN/m) , Another example is patent CN103773346A which discloses a compound system of cationic and anionic non-ionic surfactants for high-efficiency oil displacement. The interfacial tension of this compound system can reach ultra-low interfacial tension, and the ultimate recovery rate is increased by 7.5%. However, there are still many problems with the current surfactants, such as poor surface activity and unsatisfactory effect of enhancing oil recovery. Most anionic surfactants are used together with inorganic alkalis, which will cause corrosion to formations and pipeline equipment, and various Surfactants for oil displacement also have problems such as high cost.
深共晶溶剂(DES)是一类特殊的溶剂,是由氢键供体和氢键受体组成的混合物。这两种物质的相互作用导致液体的特性与成分特性显著不同(在温度为23±2℃)。DES的主要特征是它的熔点低于其中任何一个组分。因此,DES在室温下通常为黏性液体,而其成分均为结晶固体。与其它离子液体相比,DES是生物可降解的且无毒的,制备简单,价格便宜,原料来源广。与传统的离子液体不同,DES很容易以纯净的形式制备。DES也被称为绿色溶剂,因为它们的蒸气压可忽略不计,不易燃、不易爆炸、毒性低、电化学以及热稳定性好。DES是熔盐,主要是通过盐的阴离子形成大量的氢键网络或金属卤化物相互作用,而不是像离子液体那样依靠阴阳离子之间的静电力作用,DES中具有大量的氢键网络,其在抑制黏土水化膨胀方面具有巨大的潜力。Deep eutectic solvents (DES) are a special class of solvents that are mixtures of hydrogen bond donors and hydrogen bond acceptors. The interaction of these two substances causes the properties of the liquid to be significantly different from those of the components (at a temperature of 23±2°C). The main feature of DES is that it has a lower melting point than any of its components. Therefore, DES is usually a viscous liquid at room temperature, while its components are all crystalline solids. Compared with other ionic liquids, DES is biodegradable and non-toxic, easy to prepare, cheap, and has a wide source of raw materials. Unlike conventional ionic liquids, DES is easily prepared in pure form. DES are also known as green solvents because of their negligible vapor pressure, non-flammability, non-explosive properties, low toxicity, and good electrochemical and thermal stability. DES is a molten salt, which mainly forms a large number of hydrogen bond networks or metal halide interactions through the anions of the salt, rather than relying on the electrostatic force between anions and cations like ionic liquids. DES has a large number of hydrogen bond networks. It has great potential in inhibiting the hydration expansion of clay.
我国拥有世界最大的油茶种植面积,总面积约有5500万亩,主要分布在我国湖南、江西等地,油茶皂素又称油茶皂甙,是油茶中含有的一种天然糖甙化合物,是在油茶榨油后废料中提取的一种天然非离子表面活性剂,主要由糖体和皂苷元、有机酸组成,亲水亲油平衡值(HLB)为16,具有良好的发泡、稳泡、乳化、润湿和增溶等作用,其原材料来源广泛,成本极低,属于废料利用,且油茶皂素属于天然表面活性剂,无毒无害,可以应用到原油开采领域,但单一油茶皂素的表面活性有限,还不足以达到高效提高原油采收率的效果。China has the world's largest planting area of camellia oleifera, with a total area of about 55 million mu, mainly distributed in Hunan, Jiangxi and other places in China. Camellia oleifera saponin, also known as camellia oleifera saponin, is a natural glycoside compound contained in camellia oleifera. A natural non-ionic surfactant extracted from waste after oil extraction, mainly composed of glycosides, saponins, and organic acids, with a hydrophilic-lipophilic balance (HLB) of 16, and has good foaming, foam stabilizing, and emulsifying properties , wetting and solubilizing effects, its raw materials have a wide range of sources, the cost is extremely low, it belongs to waste utilization, and camellia saponin is a natural surfactant, non-toxic and harmless, and can be applied to the field of crude oil exploitation, but the single camellia saponin The limited surface activity is not enough to achieve the effect of high oil recovery efficiency.
发明内容Contents of the invention
本部分的目的在于概述本发明的实施例的一些方面以及简要介绍一些较佳实施例。在本部分以及本申请的说明书摘要和发明名称中可能会做些简化或省略以避免使本部分、说明书摘要和发明名称的目的模糊,而这种简化或省略不能用于限制本发明的范围。The purpose of this section is to outline some aspects of embodiments of the invention and briefly describe some preferred embodiments. Some simplifications or omissions may be made in this section, as well as in the abstract and titles of this application, to avoid obscuring the purpose of this section, abstract and titles, and such simplifications or omissions should not be used to limit the scope of the invention.
鉴于上述和/或现有技术中存在的问题,提出了本发明。In view of the problems mentioned above and/or in the prior art, the present invention is proposed.
因此,本发明的目的是,克服现有技术中的不足,提供一种天然表面活性剂复配体系。Therefore, the purpose of the present invention is to overcome the deficiencies in the prior art and provide a kind of natural surfactant complex system.
为解决上述技术问题,本发明提供了如下技术方案:一种天然表面活性剂复配体系,其包括如下组分:氯化胆碱、柠檬酸、油茶皂素。In order to solve the above technical problems, the present invention provides the following technical proposal: a natural surfactant compound system, which includes the following components: choline chloride, citric acid, and camellia saponin.
本发明的另一个目的是为了一种天然表面活性剂的复配体系的制备方法。Another object of the present invention is a method for preparing a compound system of natural surfactants.
为解决上述技术问题,本发明提供了如下技术方案:一种天然表面活性剂的复配体系的制备方法,其包括如下步骤:In order to solve the above-mentioned technical problems, the present invention provides the following technical solutions: a preparation method of a compound system of natural surfactant, which comprises the steps of:
制备深共晶溶剂:混合氯化胆碱和柠檬酸,制得深共晶溶剂;Preparation of deep eutectic solvent: mixing choline chloride and citric acid to obtain a deep eutectic solvent;
制备复合体系:将深共晶溶剂和油茶皂素混合,加入水,制得复合体系,所述复合体系即天然表面活性剂复配体系。Preparation of the composite system: mixing the deep eutectic solvent and camellia oleifera saponin, adding water to prepare the composite system, which is the natural surfactant composite system.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备天然深共晶溶剂中,按照摩尔比,氯化胆碱:柠檬酸=0.5~2:1。As a preferred version of the preparation method of the compound system of the natural surfactant of the present invention, wherein: in the preparation of the natural deep eutectic solvent, according to the molar ratio, choline chloride:citric acid=0.5~2:1 .
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备天然深共晶溶剂中,按照摩尔比,氯化胆碱:柠檬酸=1:1。As a preferred version of the preparation method of the compound system of natural surfactant of the present invention, wherein: in the preparation of natural deep eutectic solvent, according to the molar ratio, choline chloride:citric acid=1:1.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备复合体系中,按照摩尔比,深共晶溶剂:油茶皂素=0.5~2:1。As a preferred scheme of the preparation method of the natural surfactant compound system of the present invention, wherein: in preparing the compound system, according to the molar ratio, deep eutectic solvent: camellia saponin = 0.5-2:1.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备复合体系中,按照摩尔比,深共晶溶剂:油茶皂素=1:1。As a preferred scheme of the preparation method of the natural surfactant compound system of the present invention, wherein: in preparing the compound system, according to the molar ratio, the deep eutectic solvent: camellia saponin=1:1.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备深共晶溶剂中,氯化胆碱和柠檬酸在加热环境下进行混合。As a preferred solution of the preparation method of the natural surfactant complex system of the present invention, wherein: in the preparation of the deep eutectic solvent, choline chloride and citric acid are mixed under a heating environment.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备深共晶溶剂中,氯化胆碱和柠檬酸搅拌,在60~100℃下加热1~3h。As a preferred version of the preparation method of the compound system of natural surfactants according to the present invention, wherein: in the preparation of the deep eutectic solvent, choline chloride and citric acid are stirred, and heated at 60-100°C for 1- 3h.
作为本发明所述的天然表面活性剂的复配体系的制备方法的一种优选方案,其中:制备深共晶溶剂中,所述氯化胆碱和柠檬酸搅拌,在80℃下加热2h。As a preferred solution of the preparation method of the natural surfactant compound system of the present invention, wherein: in the preparation of the deep eutectic solvent, the choline chloride and citric acid are stirred and heated at 80° C. for 2 hours.
本发明有益效果:Beneficial effects of the present invention:
1.本发明提供的复配体系能有效提高了黏土矿物水化膨胀的抑制性,在较大程度上降低了油藏各种复杂情况的发生;1. The compound system provided by the present invention can effectively improve the inhibition of hydration expansion of clay minerals, and reduce the occurrence of various complex situations in oil reservoirs to a large extent;
2.本发明提供的复配体系具有低的界面张力,在天然表活剂的基础上再次降低,随时间变化十分稳定,在高矿化度环境下仍能维持低的界面张力;2. The compound system provided by the present invention has low interfacial tension, which is lowered again on the basis of natural surfactants, is very stable over time, and can still maintain low interfacial tension in a high salinity environment;
3.本发明提供的复配体系能有效提高驱油效率,降压效果显著;3. The compound system provided by the present invention can effectively improve the oil displacement efficiency, and the pressure-reducing effect is remarkable;
4.本发明提供的复配体系采用天然表面活性剂复配,属于废料利用,原料来源广泛,制备工艺简单,对地层无污染。4. The compounding system provided by the present invention adopts natural surfactant compounding, belongs to waste material utilization, has wide sources of raw materials, simple preparation process, and no pollution to the formation.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其它的附图。其中:In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following will briefly introduce the accompanying drawings that need to be used in the description of the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. For Those of ordinary skill in the art can also obtain other drawings based on these drawings without any creative effort. in:
图1为本发明实施中图不同体系抑制蒙脱石水化膨胀实验结果。Fig. 1 is the experimental result of inhibiting the hydration expansion of montmorillonite by different systems in Fig. 1 during the implementation of the present invention.
图2为本发明实施中DES、油茶皂素及复配体系红外光谱图;Fig. 2 is the infrared spectrogram of DES, camellia saponin and compound system in the implementation of the present invention;
图中,图a为DES、油茶皂素及复配体系红外光谱谱图,图b为DES红外光谱谱图,图c为油茶皂素红外光谱谱图,图d为DES+油茶皂素复配体系红外光谱谱图;In the figure, picture a is the infrared spectrum spectrum of DES, camellia saponin and compound system, picture b is the infrared spectrum spectrum of DES, picture c is the infrared spectrum spectrum of camellia saponin, and picture d is the compound system of DES+ camellia saponin Infrared Spectrum;
具体实施方式Detailed ways
为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合说明书实施例对本发明的具体实施方式做详细的说明。In order to make the above objects, features and advantages of the present invention more obvious and comprehensible, the specific implementation manners of the present invention will be described in detail below in conjunction with the embodiments of the specification.
在下面的描述中阐述了很多具体细节以便于充分理解本发明,但是本发明还可以采用其他不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本发明内涵的情况下做类似推广,因此本发明不受下面公开的具体实施例的限制。In the following description, a lot of specific details are set forth in order to fully understand the present invention, but the present invention can also be implemented in other ways different from those described here, and those skilled in the art can do it without departing from the meaning of the present invention. By analogy, the present invention is therefore not limited to the specific examples disclosed below.
其次,此处所称的“一个实施例”或“实施例”是指可包含于本发明至少一个实现方式中的特定特征、结构或特性。在本说明书中不同地方出现的“在一个实施例中”并非均指同一个实施例,也不是单独的或选择性的与其他实施例互相排斥的实施例。Second, "one embodiment" or "an embodiment" referred to herein refers to a specific feature, structure or characteristic that may be included in at least one implementation of the present invention. "In one embodiment" appearing in different places in this specification does not all refer to the same embodiment, nor is it a separate or selective embodiment that is mutually exclusive with other embodiments.
实施例1Example 1
分别称取0.381g氯化胆碱与0.519g柠檬酸,摩尔比为1:1,在恒温水浴锅中以200r/min搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES);Take by weighing 0.381g choline chloride and 0.519g citric acid respectively, the molar ratio is 1:1, stir and heat 2h with 200r/min in constant temperature water bath, experiment temperature is 80 ℃, mix well, obtain deep eutectic solvent ( DES);
将制得的DES与油茶皂素以1:1的摩尔比进行复配,加入100mL水,搅拌均匀、充分,得到复配体系;Compound the prepared DES and camellia saponin at a molar ratio of 1:1, add 100mL of water, and stir evenly and fully to obtain a compound system;
称取过200目筛的钠基蒙脱土10g,将钠基蒙脱土在压力机(YLJ600压力机)中10MPa下压10min,制得人造岩心。Weigh 10 g of sodium-based montmorillonite passed through a 200-mesh sieve, and press the sodium-based montmorillonite in a press (YLJ600 press) at 10 MPa for 10 minutes to prepare an artificial rock core.
将人造岩心分别置于蒸馏水、3wt%KCl和3vol%复配体系溶液的培养皿中浸泡24h,使溶液完全浸没人造岩心表面,并拍照记录人造岩心在三种不同溶液中不同浸泡时间的水化膨胀的情况。Soak the artificial core in a petri dish of distilled water, 3wt% KCl and 3vol% compound system solution for 24 hours, so that the solution is completely submerged on the surface of the artificial core, and take pictures to record the hydration of the artificial core in three different solutions for different soaking times Inflated situation.
将拍摄到的图片记录在图1中。Record the captured pictures in Figure 1.
由图1可得,比较了钠基蒙脱土在不同体系(蒸馏水、3%KCl、1%复配体系)溶液中的水化膨胀效果,在不同的时间节点上,1%复配体系浸泡后的岩心有着更加明显的膨胀被抑制的效果,K+可嵌入到钠基蒙脱土晶格的六角孔穴中,且很难发生交换,从而有效阻止了水分子进入蒙脱土的孔穴结构中,抑制了蒙脱土的水化膨胀。复配体系中的表活剂分子会优先进入钠基蒙脱土晶格的六角孔穴中并吸附在蒙脱土的表面上,DES也通过盐的阴离子形成大量的氢键网络,另外复配体系的疏水性增强,更有效抑制了蒙脱土的水化膨胀。It can be seen from Figure 1 that the hydration swelling effect of sodium-based montmorillonite in different systems (distilled water, 3% KCl, 1% compound system) was compared. At different time points, the 1% compound system soaked The resulting core has a more obvious effect of inhibiting expansion, K + can be embedded in the hexagonal pores of the Na-based montmorillonite lattice, and it is difficult to exchange, thus effectively preventing water molecules from entering the pore structure of the montmorillonite , inhibiting the hydration swelling of montmorillonite. The surfactant molecules in the complex system will preferentially enter the hexagonal pores of the Na-based montmorillonite lattice and be adsorbed on the surface of the montmorillonite. DES also forms a large number of hydrogen bond networks through the anions of the salt. In addition, the complex system The hydrophobicity of montmorillonite is enhanced, and the hydration swelling of montmorillonite is more effectively inhibited.
实施例2(油水界面张力测试)Embodiment 2 (oil-water interfacial tension test)
分别称取0.4g氯化胆碱与0.6g柠檬酸,摩尔比为1:1,在恒温水浴锅中以3000rpm中搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES),加入100mL蒸馏水制得DES溶液;Weigh 0.4g choline chloride and 0.6g citric acid respectively, the molar ratio is 1:1, stir and heat in a constant temperature water bath with 3000rpm for 2h, the experimental temperature is 80°C, mix well to obtain a deep eutectic solvent (DES ), add 100mL distilled water to make DES solution;
称取1g油茶皂素,加入100mL水,搅拌均匀、充分,制得表面活性剂溶液;Weigh 1g of camellia saponin, add 100mL of water, stir evenly and fully to prepare surfactant solution;
使用旋滴式界面张力仪(上海中晨数字技术设备有限公司JJ2000B2)分别测定质量浓度均为1wt%的DES与表面活性剂溶液的油水界面张力,转速为6000r/min,实验温度为40℃,实验用油为胜利油田某区块原油;Use the spin-drop type interfacial tensiometer (Shanghai Zhongchen Digital Technology Equipment Co., Ltd. JJ2000B2) to measure the oil-water interfacial tension of DES and the surfactant solution whose mass concentration is 1wt%, the rotating speed is 6000r/min, and the experimental temperature is 40°C. The oil used in the experiment was crude oil from a certain block of Shengli Oilfield;
分别称取0.127g氯化胆碱与0.173g柠檬酸,摩尔比为1:1,按照氯化胆碱和柠檬酸和按照摩尔比1:1制得的DES,与油茶皂素分别按摩尔比为2:8、4:6、5:5、6:4、8:2、进行复配,加入100mL水得到复配体系,使用旋滴式界面张力仪测定复配体系的油水界面张力。Take by weighing 0.127g choline chloride and 0.173g citric acid respectively, the molar ratio is 1:1, according to choline chloride and citric acid and according to the DES that the molar ratio 1:1 makes, and camellia saponin respectively by molar ratio For 2:8, 4:6, 5:5, 6:4, 8:2, carry out compounding, add 100mL water to obtain the compound system, use the spin-drop type interfacial tensiometer to measure the oil-water interfacial tension of the compound system.
DES和油茶皂素按照不同摩尔比制得的复配体系经旋滴式界面张力仪测得的油水界面张力如表1所示。The oil-water interfacial tension of DES and camellia saponin prepared in different molar ratios is shown in Table 1.
由表1可得,实验表明单独的质量浓度为1wt%的DES与油茶皂素均具有高的油水界面张力,而DES与油茶皂素以5:5的摩尔比制备的复配体系极大程度降低了油水界面张力,最低达到1.12×10-2mN/m的低界面张力,且随时间变化不大。It can be obtained from Table 1 that the experiment shows that DES and camellia saponin with a mass concentration of 1wt% alone have high oil-water interfacial tension, while the compound system prepared with a molar ratio of 5:5 between DES and camellia saponin has a great degree of The interfacial tension of oil and water is reduced, reaching the lowest low interfacial tension of 1.12×10 -2 mN/m, and it does not change much with time.
表1不同体系的油水界面张力测试结果Table 1 Test results of oil-water interfacial tension of different systems
实施例3(耐盐性测试)Embodiment 3 (salt tolerance test)
分别称取0.127g氯化胆碱与0.173g柠檬酸,摩尔比为1:1,在恒温水浴锅中按照3000rpm搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES);Weigh 0.127g of choline chloride and 0.173g of citric acid respectively, the molar ratio is 1:1, stir and heat in a constant temperature water bath at 3000rpm for 2h, the experimental temperature is 80°C, and mix well to obtain a deep eutectic solvent (DES) ;
将制得的DES与油茶皂素以1:1的摩尔比进行复配,加入100mL水,搅拌均匀、充分,得到复配体系;Compound the prepared DES and camellia saponin at a molar ratio of 1:1, add 100mL of water, and stir evenly and fully to obtain a compound system;
在复配体系中分别加入500mg、1000mg、1500mg、2500mg、4000mg的CaCl2,测试复配体系的耐盐性,使每组复配体系中Ca2+浓度为50mg/L、100mg/L、150mg/L、250mg/L、400mg/L、;Add 500mg, 1000mg, 1500mg, 2500mg, and 4000mg of CaCl 2 to the compound system to test the salt tolerance of the compound system, so that the Ca 2+ concentration in each compound system is 50mg/L, 100mg/L, 150mg /L, 250mg/L, 400mg/L,;
使用旋滴式界面张力仪分别测定加入不同量CaCl2后的油水界面张力,转速为6000r/min,实验温度为40℃,实验用油为胜利油田某区块原油。The interfacial tension of oil and water after adding different amounts of CaCl 2 was measured using a spin-drop interfacial tensiometer. The rotational speed was 6000r/min, and the experimental temperature was 40°C. The oil used in the experiment was crude oil from a block in Shengli Oilfield.
由表2可得,在高浓度Ca2+下,复配体系的最低界面张力仍有2.70×10-2mN/m,复配体系的界面张力随Ca2+浓度的增加变化不大,且随时间变化十分稳定,表现出极好的耐盐性。It can be seen from Table 2 that the minimum interfacial tension of the compound system is still 2.70×10 -2 mN/m under high concentration of Ca 2+ , and the interfacial tension of the compound system does not change much with the increase of Ca 2+ concentration, and Very stable over time and exhibits excellent salt tolerance.
表2复配体系的耐盐性测试结果Salt tolerance test result of compound system of table 2
实施例4(润湿性测试)Embodiment 4 (wettability test)
分别称取0.127g氯化胆碱与0.173g柠檬酸,摩尔比为1:1,在恒温水浴锅中按照3000rpm搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES);Weigh 0.127g of choline chloride and 0.173g of citric acid respectively, the molar ratio is 1:1, stir and heat in a constant temperature water bath at 3000rpm for 2h, the experimental temperature is 80°C, and mix well to obtain a deep eutectic solvent (DES) ;
将制得的DES与油茶皂素以1:1的摩尔比进行复配,加入100mL水,搅拌均匀、充分,得到复配体系;Compound the prepared DES and camellia saponin at a molar ratio of 1:1, add 100mL of water, and stir evenly and fully to obtain a compound system;
将实验所取的岩心顶端通过岩心刨磨机进行打磨至表面光滑,岩心经过蒸馏水浸泡48h后,使用金属注射器将蒸馏水与油通过固定滴技术测量岩心顶端的接触角并记录;The top of the core taken in the experiment was polished to a smooth surface by a core planer. After the core was soaked in distilled water for 48 hours, the contact angle of the top of the core was measured and recorded by using a metal syringe to measure the contact angle of the core with distilled water and oil through the fixed drop technique;
将岩心放置于制得的复配体系中浸泡48h,并测定出此时的水与油相接触角,通过润湿角改变判定出复配体系对岩心润湿性的改变。The core was placed in the prepared compound system and soaked for 48 hours, and the contact angle between water and oil was measured at this time, and the change of the wettability of the core by the compound system was judged by the change of wetting angle.
实验结果:实验结果见表3,实验表明岩心在经过复配体系处理后,水相与油相接触角均变大,水相接触角由7.7°变为64.4°,疏水性增强,油相接触角由27.7°变为64.4°,亲油性减弱,说明复配体系中表活剂吸附在岩心表面,有效改变了岩心表面的界面性,减少了岩石表面对油滴的吸附,岩心的亲油性显著降低,岩心表面发生润湿性反转。Experimental results: The experimental results are shown in Table 3. The experiment shows that after the core is treated with the compound system, the contact angle between the water phase and the oil phase becomes larger, the water phase contact angle changes from 7.7° to 64.4°, the hydrophobicity is enhanced, and the oil phase contacts The antennae changed from 27.7° to 64.4°, and the lipophilicity weakened, indicating that the surfactant in the compound system was adsorbed on the surface of the core, which effectively changed the interfacial properties of the core surface and reduced the adsorption of oil droplets on the rock surface, and the lipophilicity of the core was significant. decrease, wettability reversal occurs on the core surface.
表3复配体系润湿性测试结果Table 3 wettability test results of compound system
实施例5(红外光谱测试)Embodiment 5 (infrared spectrum test)
分别称取0.127g氯化胆碱与0.173g柠檬酸,摩尔比为1:1,在恒温水浴锅中搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES),随后加入0.717g油茶皂素,使其溶解于DES中,搅拌均匀、充分,DES与油茶皂素摩尔比为1:1,制得复配体系。Weigh 0.127g choline chloride and 0.173g citric acid respectively, the molar ratio is 1:1, stir and heat in a constant temperature water bath for 2h, the experimental temperature is 80°C, mix well to obtain a deep eutectic solvent (DES), and then Add 0.717g camellia saponin, dissolve it in DES, stir evenly and fully, and the molar ratio of DES to camellia saponin is 1:1 to obtain a compound system.
分别使用深共晶溶剂、油茶皂素与按照上述比例制备的+复配体系制备样品压片,将制备好的溴化钾空白片置于红外光谱仪样品仓内的样品架上,确定采集参比背景光谱,背景谱图采集完毕后,将溴化钾空白片取出,将待测样品片放入光谱仪内,关上仓盖,得到样品的红外光谱图,将得到的油茶皂素、DES以及复配体系的红外光谱谱图记为图2。Use the deep eutectic solvent, camellia oleifera saponin and the compound system prepared according to the above ratio to prepare sample compression tablets, place the prepared potassium bromide blank on the sample holder in the sample chamber of the infrared spectrometer, and determine the collection reference After the background spectrum is collected, take out the potassium bromide blank sheet, put the sample sheet to be tested into the spectrometer, close the cover, and obtain the infrared spectrum of the sample. The infrared spectrum of the system is marked in Figure 2.
由图2可得,相比单独油茶皂素,复配体系在波长2500cm-1-3500cm-1范围出现宽且长的-OH伸缩震动峰,说明DES中大量氢键加入到了复配体系,使得体系降低界面张力能力大大提高,DES的加入,也使复配体系在波长为2010cm-1处存在C≡C的伸缩震动峰,波长1732cm-1处为C=O伸缩震动峰,波长1478cm-1、1409cm-1对应的为C-H面内弯曲震动峰,波长1196cm-1对应的为C-C伸缩震动峰,波长1082cm-1、955cm-1对应的为C-H面内弯曲震动峰,波长1006cm-1、866cm-1、783cm-1对应的为C-H面外弯曲震动峰,相比单独油茶皂素,复配体系的疏水性增强,对钠基蒙脱石水敏性膨胀的抑制性也随之增强。It can be seen from Figure 2 that compared with Camellia oleifera saponin alone, the compound system has a wide and long -OH stretching vibration peak in the wavelength range of 2500cm -1 -3500cm -1 , indicating that a large number of hydrogen bonds in DES have been added to the compound system, making The ability of the system to reduce interfacial tension is greatly improved, and the addition of DES also makes the compound system have a stretching vibration peak of C≡C at a wavelength of 2010cm -1 , and a stretching vibration peak of C=O at a wavelength of 1732cm -1 , and a wavelength of 1478cm -1 , 1409cm -1 corresponds to the CH in-plane bending vibration peak, the wavelength 1196cm -1 corresponds to the CC stretching vibration peak, the wavelengths 1082cm -1 , 955cm -1 correspond to the CH in-plane bending vibration peak, and the wavelength 1006cm -1 , 866cm -1 and 783cm -1 correspond to the CH out-of-plane bending vibration peaks. Compared with camellia saponin alone, the hydrophobicity of the compound system is enhanced, and the inhibition of the water-sensitive expansion of sodium montmorillonite is also enhanced.
实施例6(驱替实验)Embodiment 6 (displacement experiment)
分别称取0.127g氯化胆碱与0.173g柠檬酸,摩尔比为1:1,在恒温水浴锅中按照3000rpm搅拌加热2h,实验温度为80℃,混合均匀,得到深共晶溶剂(DES),随后加入0.717g油茶皂素,使其溶解于DES中,搅拌均匀、充分,DES与油茶皂素摩尔比为1:1,制得复配体系。Weigh 0.127g of choline chloride and 0.173g of citric acid respectively, the molar ratio is 1:1, stir and heat in a constant temperature water bath at 3000rpm for 2h, the experimental temperature is 80°C, and mix well to obtain a deep eutectic solvent (DES) , then add 0.717g camellia saponin, dissolve it in DES, stir evenly and fully, and the molar ratio of DES to camellia saponin is 1:1, and a compound system is obtained.
将岩心样品在常温下饱和蒸馏水,实时监测注入端与出口端的压力,并对饱和水前后的岩心称重,计算出岩心的渗透率与孔隙度,随后将岩心进行饱和油,实验岩心基本参数见表4;The core sample is saturated with distilled water at room temperature, the pressure at the injection port and the outlet port is monitored in real time, and the core is weighed before and after water saturation, and the permeability and porosity of the core are calculated, and then the core is saturated with oil. The basic parameters of the experimental core are shown in Table 4;
将配置好的复配体系置于高压容器中,岩心饱和油后装入岩心夹持器并连接到岩心驱替装置,首先一次注水至出口端不再出油且入口端压力稳定后,注入复配体系溶液至压力稳定,之后再次注水至压力稳定,记录每个驱替阶段的入口端压力及油/水产出量,分析其降压增注效果与采收率提高情况。Put the configured compound system in a high-pressure container, fill the core holder with oil saturated and connect it to the core displacement device, first inject water until the outlet end no longer produces oil and the pressure at the inlet end is stable, then inject the complex Prepare the system solution until the pressure is stable, then reinject water until the pressure is stable, record the inlet pressure and oil/water output of each displacement stage, and analyze the effect of depressurization and enhanced injection and the improvement of recovery factor.
对于岩心进行渗透率和孔隙度的实验中。实验设置围压为20MPa,回压为3MPa,实验温度为25℃,注入速度均为0.05mL/min。Permeability and porosity experiments were performed on cores. The experimental settings were that the confining pressure was 20MPa, the back pressure was 3MPa, the experimental temperature was 25°C, and the injection rate was 0.05mL/min.
实验结果:实验结果见表5,实验表明在注入复配体系后,二次注水注入压力稳定后相比一次注水后的注入压力降低效果十分显著,在岩心样品1-1中,降压率达到17.42%,岩心样品1-2中,降压率达到19.66%;在岩心样品1-1中,注入复配体系后提高5.7%的采收率,二次注水提高0.5%的采收率,最终采收率为42.6%,岩心样品1-2中,注入复配体系后提高6.5%的采收率,二次注水提高0.7%的采收率,最终采收率为45.4%,有效提升了岩心样品的驱油效率。Experimental results: The experimental results are shown in Table 5. The experiment shows that after the injection of the compound system, the injection pressure of the second water injection is stabilized, compared with the injection pressure after the first water injection. The effect of reducing the injection pressure is very significant. 17.42%, in the core sample 1-2, the depressurization rate reached 19.66%; in the core sample 1-1, the recovery rate increased by 5.7% after injecting the compound system, and the recovery rate was increased by 0.5% after the second water injection, and finally The recovery rate was 42.6%. In the core sample 1-2, the recovery rate increased by 6.5% after injecting the compound system, and the recovery rate was increased by 0.7% after the second water injection, and the final recovery rate was 45.4%. The oil displacement efficiency of the sample.
表4实验岩心基本参数Table 4 Basic parameters of experimental cores
表5驱替各阶段稳定注入压力与采收率测试结果Table 5 Test results of stable injection pressure and recovery factor at each stage of displacement
应说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围当中。It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention without limitation, although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be carried out Modifications or equivalent replacements without departing from the spirit and scope of the technical solution of the present invention shall be covered by the claims of the present invention.
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