CN110055044B - A dual control and flooding system for high-temperature and high-salt heterogeneous reservoirs and its application - Google Patents
A dual control and flooding system for high-temperature and high-salt heterogeneous reservoirs and its application Download PDFInfo
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- 230000009977 dual effect Effects 0.000 title abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000000839 emulsion Substances 0.000 claims abstract description 11
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 claims abstract description 8
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims abstract description 7
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims abstract description 7
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims abstract description 7
- WHNWPMSKXPGLAX-UHFFFAOYSA-N N-Vinyl-2-pyrrolidone Chemical compound C=CN1CCCC1=O WHNWPMSKXPGLAX-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000005642 Oleic acid Substances 0.000 claims abstract description 7
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000008367 deionised water Substances 0.000 claims abstract description 7
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 7
- 239000011261 inert gas Substances 0.000 claims abstract description 7
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims abstract description 7
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 7
- 239000003999 initiator Substances 0.000 claims abstract description 6
- 239000012071 phase Substances 0.000 claims description 23
- 238000003756 stirring Methods 0.000 claims description 14
- 238000002360 preparation method Methods 0.000 claims description 10
- 150000003839 salts Chemical class 0.000 claims description 9
- 238000006073 displacement reaction Methods 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 239000000178 monomer Substances 0.000 claims description 6
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 claims description 6
- 239000004094 surface-active agent Substances 0.000 claims description 6
- 229940051841 polyoxyethylene ether Drugs 0.000 claims description 5
- 229920000056 polyoxyethylene ether Polymers 0.000 claims description 5
- -1 Alkyl phenol Chemical compound 0.000 claims description 4
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- RZXLPPRPEOUENN-UHFFFAOYSA-N Chlorfenson Chemical compound C1=CC(Cl)=CC=C1OS(=O)(=O)C1=CC=C(Cl)C=C1 RZXLPPRPEOUENN-UHFFFAOYSA-N 0.000 claims description 4
- 239000008346 aqueous phase Substances 0.000 claims description 3
- 238000010907 mechanical stirring Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 2
- 229910052786 argon Inorganic materials 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 239000002283 diesel fuel Substances 0.000 claims description 2
- 239000001307 helium Substances 0.000 claims description 2
- 229910052734 helium Inorganic materials 0.000 claims description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 2
- 239000003350 kerosene Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims 5
- 125000005233 alkylalcohol group Chemical group 0.000 claims 1
- 238000006392 deoxygenation reaction Methods 0.000 claims 1
- 239000012467 final product Substances 0.000 claims 1
- 239000007789 gas Substances 0.000 claims 1
- 238000010792 warming Methods 0.000 claims 1
- 239000003921 oil Substances 0.000 abstract description 28
- 239000000243 solution Substances 0.000 abstract description 21
- 239000004005 microsphere Substances 0.000 abstract description 12
- 239000010779 crude oil Substances 0.000 abstract description 10
- 238000011084 recovery Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 239000007762 w/o emulsion Substances 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 230000008878 coupling Effects 0.000 abstract 1
- 238000010168 coupling process Methods 0.000 abstract 1
- 238000005859 coupling reaction Methods 0.000 abstract 1
- 229920000642 polymer Polymers 0.000 description 13
- 239000003513 alkali Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000005755 formation reaction Methods 0.000 description 4
- 239000008398 formation water Substances 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 239000011837 N,N-methylenebisacrylamide Substances 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009533 lab test Methods 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- FQPSGWSUVKBHSU-UHFFFAOYSA-N methacrylamide Chemical compound CC(=C)C(N)=O FQPSGWSUVKBHSU-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000004530 micro-emulsion Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 239000010729 system oil Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
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Abstract
本发明公开了一种高温高盐非均质性油藏双重调驱体系及其应用,其制备方法包括以下步骤,以烷基醇酰胺、烷基酚聚氧乙烯醚磺酸盐、N,N’‑亚甲基双丙烯酰胺、丙烯酰胺、乙烯基吡咯烷酮和去离子水制备水相溶液,以油酸和油相制备油相溶液,将两者在惰性气体气氛以及引发剂的作用下混合反应制得,本发明制得的双重调驱体系在应用于高温高盐非均质性油藏化学驱时,能够将油水界面张力降低至10‑2~10‑3mN/m,在含水率低于90%时,双重调控体系能够乳化原油形成油包水乳状液,其黏度均高于地下原油黏度;乳状液的液滴尺寸可控,通过贾敏效应改善储层非均质性,同时与微球耦合调控,显著提高高温高盐非均质性油藏采收率。
The invention discloses a high-temperature and high-salt heterogeneous oil reservoir dual control and flooding system and its application. '-Methylenebisacrylamide, acrylamide, vinylpyrrolidone and deionized water to prepare water phase solution, oleic acid and oil phase to prepare oil phase solution, and mix the two under the action of inert gas atmosphere and initiator When the dual control and flooding system prepared by the present invention is applied to the chemical flooding of high-temperature and high-salt heterogeneous reservoirs, the interfacial tension of oil and water can be reduced to 10-2 to 10-3 mN/m, and the water content is low At 90%, the dual control system can emulsify crude oil to form a water-in-oil emulsion, the viscosity of which is higher than that of underground crude oil; the droplet size of the emulsion can be controlled, and the heterogeneity of the reservoir can be improved through the Jamin effect. Microsphere coupling control can significantly improve the recovery of high-temperature and high-salt heterogeneity reservoirs.
Description
技术领域technical field
本发明涉及属于油田化学和油田开发技术领域,具体涉及一种高温高盐油藏双重调驱体系及其应用。The invention relates to the technical fields of oilfield chemistry and oilfield development, in particular to a high-temperature and high-salt oil reservoir dual control and flooding system and its application.
技术背景technical background
目前很多老油田已经进入开发中后期,采出液高含水是长期困扰油田开采的严重问题,如何有效控水稳油是现阶段油田开发的重要任务。化学驱油技术已成为老油田控水稳油及进一步提高原油采收率的主要手段,并且在常规油藏得到了广泛的应用。这些化学驱技术主要包括:聚合物驱、碱驱、表面活性剂驱、聚/表二元驱、聚/碱/表三元复合驱以及多元泡沫复合驱等。然而对于高温高盐且非均质性较强的油藏,这些化学驱技术的应用仍然具有一定的局限性,主要表现为:1)聚合物的耐温抗盐性有限,含聚合物的体系只适合于中低温及低矿化度油藏;2)碱驱在高钙/镁条件下,碱结垢现象严重,对地层造成伤害;3)泡沫驱尽管能够在高温高盐油藏应用,但是在非均质性强的油藏,泡沫会沿着高渗透通道产出;4)部分表面活性剂的耐温抗盐性好,但是在非均质性较强的储层,蹿流现象严重。At present, many old oilfields have entered the middle and late stages of development. High water content in produced fluids is a serious problem that has plagued oilfield development for a long time. How to effectively control water and stabilize oil production is an important task for oilfield development at this stage. Chemical flooding technology has become the main means to control water, stabilize oil and further enhance oil recovery in mature oilfields, and has been widely used in conventional oil reservoirs. These chemical flooding technologies mainly include: polymer flooding, alkali flooding, surfactant flooding, polymer/surface binary flooding, poly/alkali/surface ASP flooding, and multi-component foam composite flooding. However, for high-temperature, high-salt and strong heterogeneity reservoirs, the application of these chemical flooding technologies still has certain limitations, mainly as follows: 1) The temperature and salt resistance of polymers is limited. It is only suitable for low-temperature and low-salinity reservoirs; 2) Alkali flooding under high calcium/magnesium conditions will cause serious alkali scaling and cause damage to formations; 3) Although foam flooding can be applied in high-temperature and high-salt reservoirs, However, in reservoirs with strong heterogeneity, foam will be produced along high-permeability channels; 4) Some surfactants have good temperature and salt resistance, but in reservoirs with strong heterogeneity, the flow phenomenon serious.
大量室内实验及现场试验证明,聚合物微球能够有效地改善地层非均质性、扩大波及水相波及体积。同时温度和矿化度对其适应性影响较小,用量少成本低,有效期长,特别适用于高温高盐非均质性油藏,但是如果油藏非均质性过强、聚合物微球改善地层非均质性的能力减弱,不能很好的适应油藏。A large number of laboratory experiments and field tests have proved that polymer microspheres can effectively improve formation heterogeneity and expand the swept volume of the swept water phase. At the same time, the influence of temperature and salinity on its adaptability is small, the dosage is low, the cost is low, and the validity period is long. It is especially suitable for high-temperature and high-salt heterogeneous reservoirs. The ability of the ball to improve formation heterogeneity is weakened, and it cannot be well adapted to the reservoir.
发明内容:Invention content:
本发明针对目前油田用化学驱存在的不足,提出一种高温高盐非均质油藏双重调驱体系,既能够弥补常规聚合物微球使用的限制,又能够提高经济效益。Aiming at the shortcomings of current chemical flooding in oil fields, the present invention proposes a dual control and flooding system for high-temperature, high-salt heterogeneous reservoirs, which can not only make up for the limitations of conventional polymer microspheres, but also improve economic benefits.
为达到上述目的,本发明提供以下技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种高温高盐非均质性油藏双重调驱体系,以质量百分比计,采用包括以下原料制成:A dual control and flooding system for high-temperature, high-salt heterogeneous reservoirs, made of the following raw materials in terms of mass percentage:
a、油相:40%~70%,a. Oil phase: 40% to 70%,
油酸:0.5%~2%,Oleic acid: 0.5% to 2%,
b、水溶性单体:b. Water-soluble monomer:
烷基醇酰胺:6%~8%,Alkanolamide: 6% to 8%,
烷基酚聚氧乙烯醚磺酸盐表面活性剂:1%~2%,Alkylphenol polyoxyethylene ether sulfonate surfactant: 1% to 2%,
丙烯酰胺(AM):10%~20%,Acrylamide (AM): 10% to 20%,
乙烯基吡咯烷酮(NVP):1%~3%,Vinylpyrrolidone (NVP): 1% to 3%,
N,N’-亚甲基双丙烯酰胺(MBA):水溶性单体总质量的0.1%~0.4%,N,N'-methylenebisacrylamide (MBA): 0.1% to 0.4% of the total mass of water-soluble monomers,
c、引发剂:水溶性单体总质量的0.01%~0.05%,c. Initiator: 0.01% to 0.05% of the total mass of water-soluble monomers,
d、其余为去离子水;d. The rest is deionized water;
所述调驱体系的制备包括以下步骤:The preparation of the control and flooding system comprises the following steps:
(1)水相溶液配制:将丙烯酰胺、乙烯基吡咯烷酮、N,N’-亚甲基双丙烯酰胺、烷基醇酰胺和烷基醇聚氧乙烯醚磺酸盐表面活性剂加入到去离子水中,搅拌至溶液澄清透明,备用。(1) Water phase solution preparation: add acrylamide, vinylpyrrolidone, N,N'-methylene bisacrylamide, alkanolamide and alkanol polyoxyethylene ether sulfonate surfactants to the deionized water, stir until the solution is clear and transparent, set aside.
(2)油相溶液配制:将油酸加入到油相中,搅拌均匀至溶液澄清透明,备用。(2) Oil phase solution preparation: add oleic acid into the oil phase, stir evenly until the solution is clear and transparent, set aside.
(3)乳液体系的配制:将油相溶液加入到带机械搅拌、惰性气体入口/出口的三口烧瓶中,在800r/min~1000r/min的高速机械搅拌条件下,缓慢将水相溶液加入到油相溶液中,加入完全后开始通入惰性气体30min,使得乳液体系处于脱氧条件,再降低机械搅拌速率至200min~400r/min,加入引发剂后再升温三口烧瓶至45℃~50℃,反应2h~3h,形成聚合物微球尺寸在0.1μm~100μm的双重调控体系。(3) Preparation of emulsion system: Add the oil phase solution into a three-necked flask with mechanical stirring and inert gas inlet/outlet, and slowly add the water phase solution into the In the oil phase solution, after the addition is complete, the inert gas is introduced for 30 minutes, so that the emulsion system is in a deoxygenated condition, and then the mechanical stirring rate is reduced to 200min~400r/min, and the temperature of the three-necked flask is raised to 45℃~50℃ after adding the initiator. After 2h to 3h, a dual control system with a polymer microsphere size of 0.1 μm to 100 μm is formed.
进一步的,所述的油相为煤油、白油、柴油中的至少一种。Further, the oil phase is at least one of kerosene, white oil and diesel oil.
进一步的,所述惰性气体为氦气、氮气或氩气中的一种。Further, the inert gas is one of helium, nitrogen or argon.
进一步的,所述的烷基醇酰胺结构简式为:Further, the simplified structural formula of the alkyl alcohol amide is:
CnH2n+1CON(CH2CH2OH)C n H 2n+1 CON(CH 2 CH 2 OH)
其中,n为11~15。Among them, n is 11-15.
进一步的,所述的烷基酚聚氧乙烯醚磺酸盐结构简式为:Further, the simplified structural formula of the alkylphenol polyoxyethylene ether sulfonate is:
其中,m为8~10,o为10~40。Among them, m is 8-10, and o is 10-40.
本发明还公布了一种高温高盐非均质性油藏双重调驱体系的应用,其主要应用于高温高盐非均质性油藏的化学驱中。The invention also discloses the application of a dual control and flooding system for high-temperature and high-salt heterogeneity reservoirs, which is mainly used in chemical flooding of high-temperature and high-salt heterogeneity reservoirs.
与现有调驱体系相比,本发明有如下有益效果:Compared with the existing control and drive system, the present invention has the following beneficial effects:
1、双重调驱体系能够将油水界面张力降低至10-2~10-3mN/m,在含水率低于90%时,双重调控体系能够乳化原油并形成油包水的乳状液。1. The dual control and flooding system can reduce the oil-water interfacial tension to 10 -2 ~ 10 -3 mN/m, and when the water cut is lower than 90%, the dual control system can emulsify crude oil and form a water-in-oil emulsion.
2、该乳状液在含水率不同时黏度也不同,且其黏度均高于地下原油黏度,当含水率在30%-90%范围内时,乳状液的黏度是原油黏度的数倍,表现出良好的流度自控能力。2. The viscosity of the emulsion is different when the water content is different, and its viscosity is higher than that of underground crude oil. When the water content is in the range of 30%-90%, the viscosity of the emulsion is several times that of crude oil, showing Good mobility self-control ability.
3、乳状液的液滴尺寸可控,通过贾敏效应改善储层非均质性,同时与微球耦合调控,进一步改善油藏的非均质性、显著提高高温高盐非均质性油藏采收率。3. The droplet size of the emulsion is controllable, and the heterogeneity of the reservoir is improved through the Jamin effect. At the same time, it is coupled with microspheres to further improve the heterogeneity of the reservoir and significantly increase the heterogeneity of high-temperature and high-salt oil. Tibetan recovery rate.
附图说明:Description of drawings:
图1、聚合物微球调驱实验效果图;Figure 1. Effect diagram of polymer microsphere control and flooding experiment;
图2、双重调驱体系调驱试验效果图。Fig. 2. The effect diagram of the control and drive test of the dual control and drive system.
具体实施方式:Detailed ways:
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention.
下面结合实施例和附图对本发明进行进一步说明,但不限制本发明。The present invention will be further described below in conjunction with the embodiments and accompanying drawings, but the present invention is not limited.
实施例1:Example 1:
(一)高温高盐非均质性油藏双重调驱体系的制备(1) Preparation of dual control and flooding system for high-temperature and high-salt heterogeneous reservoirs
实验需分别配制油相溶液与水相溶液,油相溶液为白油与油酸的混合体系,水相溶液为去离子水、丙烯酰胺、乙烯基吡咯烷酮、烷基醇酰胺与N,N-亚甲基双丙烯酰胺的混合体系。The experiment needs to prepare the oil phase solution and the water phase solution respectively. The oil phase solution is a mixed system of white oil and oleic acid, and the water phase solution is deionized water, acrylamide, vinylpyrrolidone, alkanolamide and N,N-ethylene oxide. Mixed systems of methacrylamide.
(1)油、水相溶液的配制(1) Preparation of oil and water phase solutions
油相溶液:量取白油60mL,油酸2g,超声搅拌混合均匀。Oil phase solution: Measure 60mL of white oil and 2g of oleic acid, and mix them evenly by ultrasonic stirring.
水相溶液:量取去离子水40mL,丙烯酰胺15g,乙烯基吡咯烷酮2g和N,N-亚甲基双丙烯酰胺0.4g,烷基醇酰胺8g,超声搅拌至完全溶解。Aqueous phase solution: Measure 40 mL of deionized water, 15 g of acrylamide, 2 g of vinylpyrrolidone, 0.4 g of N,N-methylenebisacrylamide, and 8 g of alkanolamide, and stir ultrasonically until completely dissolved.
(2)反相微乳液的制备(2) Preparation of inverse microemulsion
a、将油相溶液加入三口烧瓶中,在900r/min的搅拌速度下将水相溶液缓慢加入油相溶液中,滴加的时间控制在30min,滴加完毕后连接氮气源再搅拌30min;a. Add the oil phase solution into the three-necked flask, and slowly add the water phase solution into the oil phase solution at a stirring speed of 900r/min. The time for dropping is controlled at 30 minutes. After the dropping is completed, connect the nitrogen source and stir for another 30 minutes;
b、降低搅拌速度至400r/min,缓慢加入1%的偶氮二异丁基脒盐酸盐溶液2mL,完全加入后,将体系温度升高至48℃,持续反应3小时,即得高温高盐非均质性油藏双重调驱体系。b. Reduce the stirring speed to 400r/min, and slowly add 2mL of 1% azobisisobutylamidine hydrochloride solution. After the addition is complete, raise the system temperature to 48°C and continue the reaction for 3 hours to obtain high temperature and high temperature. Dual control and flooding system in salt heterogeneous reservoirs.
(二)性能测试:(2) Performance test:
1、双重调控体系的降低界面张力的能力1. The ability of the dual control system to reduce interfacial tension
配制矿化度为50000mg/L(Ca2+、Mg2+浓度为500mg/L)及100000mg/L(Ca2+、Mg2+浓度为1500mg/L)的模拟地层水各100mL,随后加入1g上述体系,搅拌均匀,在90℃条件下利用TX500C旋转界面张力仪测试双重调控体系与不同原油间的稳定界面张力值。实验结果如表1所示,双重调控体系能够将油水界面张力值降低至10-2~10-3mN/m,本发明表现出良好的洗油性能。Prepare 100mL of simulated formation water with a salinity of 50000mg/L (Ca2+, Mg2+ concentration is 500mg/L) and 100000mg/L (Ca2+, Mg2+ concentration is 1500mg/L), then add 1g of the above system, stir evenly, at 90 The TX500C rotating interfacial tensiometer was used to test the stable interfacial tension value between the dual control system and different crude oils under the condition of ℃. The experimental results are shown in Table 1. The dual control system can reduce the oil-water interfacial tension to 10 -2 ~ 10 -3 mN/m, and the present invention shows good oil washing performance.
表1双重调控体系降低界面张力的能力Table 1 The ability of dual regulation system to reduce interfacial tension
2、双重调控体系的乳化能力2. The emulsifying ability of the dual regulation system
配制矿化度为50000mg/L(Ca2+、Mg2+浓度为500mg/L)及100000mg/L(Ca2+、Mg2+浓度为1500mg/L)的模拟地层水各100mL,随后加入1g上述体系,搅拌均匀,按照不同比例与原油混合,放入带磁力搅拌器的三口烧瓶中,在温度为90℃,搅拌速率为400r/min的速度下搅拌1h,搅拌结束后测定乳液类型,利用高温高压安东帕流变仪测试乳状液的黏度。实验结果如表2所示:含水率小于或等于90%时,油水乳化形成油包水型乳状液,且其黏度均大于原油黏度;当含水率在30%-90%范围内时,乳状液的黏度是原油黏度的数倍,表现出良好的流度自控能力。Prepare 100mL of simulated formation water with a salinity of 50000mg/L (Ca2+, Mg2+ concentration is 500mg/L) and 100000mg/L (Ca2+, Mg2+ concentration is 1500mg/L), then add 1g of the above system, stir evenly, according to different The ratio is mixed with crude oil, put into a three-necked flask with a magnetic stirrer, and stirred for 1 hour at a temperature of 90°C and a stirring rate of 400r/min. Test the viscosity of the emulsion. The experimental results are shown in Table 2: when the water content is less than or equal to 90%, the oil-water emulsification forms a water-in-oil emulsion, and its viscosity is greater than that of crude oil; when the water content is in the range of 30%-90%, the emulsion The viscosity is several times that of crude oil, showing good mobility self-control ability.
表2双重调驱体系与原油(黏度为9.8mPa·s)的乳化性能Table 2. Emulsification performance of dual control and flooding system and crude oil (viscosity 9.8mPa·s)
3、双重调控体系的调驱的能力3. The ability to adjust and drive the dual regulation system
体系准备:配制矿化度为100000mg/L(Ca2+、Mg2+浓度为1500mg/L)的模拟地层水100mL,随后加入1g上述体系,搅拌均匀。System preparation: Prepare 100mL of simulated formation water with a salinity of 100000mg/L (Ca2+, Mg2+ concentration is 1500mg/L), then add 1g of the above system and stir evenly.
为了对比研究聚合物微球体系与双重调控体系的性能,取实施例1中的双重调控体系50mL,利用乙醇破乳后烘干获得聚合物微球,并取1g该聚合物微球加入到100mL上述模拟地层水中做对比实验。In order to compare and study the performance of the polymer microsphere system and the dual control system, take 50mL of the dual control system in Example 1, use ethanol to break the emulsion and dry to obtain the polymer microspheres, and take 1g of the polymer microspheres and add them to 100mL The above simulated formation water was used for comparative experiments.
实验温度:90℃Experimental temperature: 90°C
驱油性能:通过双并联岩心实验,在渗透率级差为15,低渗岩心渗透率为300mD的条件下,先水驱至含水率为98%时,注入0.5PV体系,再进行后续水驱,实验结果如图1和图2所示。Oil displacement performance: Through double parallel core experiments, under the condition of permeability difference of 15 and low permeability core permeability of 300mD, water flooding to water cut of 98%, injection of 0.5PV system, and subsequent water flooding, The experimental results are shown in Figure 1 and Figure 2.
实验结果表明,对于单一的聚合物微球体系,聚合物微球驱及后续水驱能够提高高渗岩心采收率18.6%,提高低渗采收率18.5%;而双重调控体系能够提高高渗岩心采收率16.3%,提高低渗岩心采收率31.6%,证明了在非均质性强的地层上的驱替性能明显优于聚合物微球体系。The experimental results show that for a single polymer microsphere system, polymer microsphere flooding and subsequent water flooding can increase the recovery rate of high-permeability cores by 18.6%, and improve the recovery rate of low-permeability cores by 18.5%; The core recovery rate is 16.3%, and the low-permeability core recovery rate is increased by 31.6%, which proves that the displacement performance in the formation with strong heterogeneity is obviously better than that of the polymer microsphere system.
上述具体实施方案已结合附图对本发明的方法进行详述,但是本发明并不限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,并不是限制性的,本领域的普通技术人员在本发明的启示下,只要在不超过本发明的主旨范围内,可对实验条件与分析方法及对象进行灵活的变更,这些均属于本发明的保护范围之内。The above-mentioned specific embodiments have been described in detail in conjunction with the accompanying drawings to the method of the present invention, but the present invention is not limited to the above-mentioned specific embodiments. The above-mentioned specific embodiments are only illustrative and not restrictive. Those of ordinary skill in the art Under the enlightenment of the present invention, personnel can flexibly change the experimental conditions, analysis methods and objects as long as they do not exceed the gist of the present invention, and these all belong to the protection scope of the present invention.
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