CN108531153B - High-temperature-resistant petroleum resin dispersoid blocking agent and preparation method and application thereof - Google Patents
High-temperature-resistant petroleum resin dispersoid blocking agent and preparation method and application thereof Download PDFInfo
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- 239000003208 petroleum Substances 0.000 title claims abstract description 117
- 239000011347 resin Substances 0.000 title claims abstract description 117
- 229920005989 resin Polymers 0.000 title claims abstract description 117
- 239000002981 blocking agent Substances 0.000 title abstract description 21
- 238000002360 preparation method Methods 0.000 title abstract description 14
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 77
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 64
- 239000006185 dispersion Substances 0.000 claims abstract description 63
- 125000002091 cationic group Chemical group 0.000 claims abstract description 49
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000003921 oil Substances 0.000 claims abstract description 38
- 239000003129 oil well Substances 0.000 claims abstract description 32
- 239000002994 raw material Substances 0.000 claims abstract description 27
- 239000002105 nanoparticle Substances 0.000 claims abstract description 19
- 239000004094 surface-active agent Substances 0.000 claims abstract description 19
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 claims abstract description 18
- 150000003839 salts Chemical class 0.000 claims abstract description 18
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 18
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 claims abstract description 12
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 claims abstract description 12
- 238000006011 modification reaction Methods 0.000 claims abstract description 10
- 235000012239 silicon dioxide Nutrition 0.000 claims abstract 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical group [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 33
- 238000000034 method Methods 0.000 claims description 15
- 230000000903 blocking effect Effects 0.000 claims description 12
- NAPSCFZYZVSQHF-UHFFFAOYSA-N dimantine Chemical group CCCCCCCCCCCCCCCCCCN(C)C NAPSCFZYZVSQHF-UHFFFAOYSA-N 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 10
- 239000000843 powder Substances 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 9
- 239000011259 mixed solution Substances 0.000 claims description 8
- 239000008398 formation water Substances 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- 239000000243 solution Substances 0.000 claims description 5
- 239000000725 suspension Substances 0.000 claims description 4
- 230000008014 freezing Effects 0.000 claims description 3
- 238000007710 freezing Methods 0.000 claims description 3
- 229910052757 nitrogen Inorganic materials 0.000 claims description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 claims 2
- 230000033558 biomineral tissue development Effects 0.000 claims 2
- 150000001768 cations Chemical class 0.000 claims 1
- 230000015572 biosynthetic process Effects 0.000 description 17
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- 230000000052 comparative effect Effects 0.000 description 7
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- 238000002347 injection Methods 0.000 description 7
- 239000007924 injection Substances 0.000 description 7
- 235000015110 jellies Nutrition 0.000 description 6
- 239000008274 jelly Substances 0.000 description 6
- WBHQBSYUUJJSRZ-UHFFFAOYSA-M sodium bisulfate Chemical compound [Na+].OS([O-])(=O)=O WBHQBSYUUJJSRZ-UHFFFAOYSA-M 0.000 description 6
- 229910000342 sodium bisulfate Inorganic materials 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 238000004581 coalescence Methods 0.000 description 5
- 239000000499 gel Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
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- 238000006460 hydrolysis reaction Methods 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 125000000542 sulfonic acid group Chemical group 0.000 description 3
- 235000020681 well water Nutrition 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 150000001408 amides Chemical class 0.000 description 2
- 239000003708 ampul Substances 0.000 description 2
- 125000000129 anionic group Chemical group 0.000 description 2
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 description 2
- 125000004029 hydroxymethyl group Chemical group [H]OC([H])([H])* 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000002028 premature Effects 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000004088 simulation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000008096 xylene Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000006004 Quartz sand Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 239000002280 amphoteric surfactant Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 238000010538 cationic polymerization reaction Methods 0.000 description 1
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- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000000599 controlled substance Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229910003480 inorganic solid Inorganic materials 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000011146 organic particle Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229940051841 polyoxyethylene ether Drugs 0.000 description 1
- 229920000056 polyoxyethylene ether Polymers 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
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- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/50—Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
- C09K8/504—Compositions based on water or polar solvents
- C09K8/506—Compositions based on water or polar solvents containing organic compounds
- C09K8/508—Compositions based on water or polar solvents containing organic compounds macromolecular compounds
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- C09K8/50—Compositions for plastering borehole walls, i.e. compositions for temporary consolidation of borehole walls
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B33/00—Sealing or packing boreholes or wells
- E21B33/10—Sealing or packing boreholes or wells in the borehole
- E21B33/13—Methods or devices for cementing, for plugging holes, crevices or the like
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
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Abstract
Description
技术领域technical field
本发明涉及一种耐高温石油树脂分散体堵剂及其制备方法与应用,属于油田化学技术领域。The invention relates to a high temperature resistant petroleum resin dispersion plugging agent, a preparation method and application thereof, and belongs to the technical field of oilfield chemistry.
背景技术Background technique
油井出水是油田采油过程中的一种重要的现象,油井出水原因一般为:(1)注入水及边水推进;(2)底水推进;(3)上层水、下层水窜入;(4)夹层水进入,夹层水又指油层间的层间水,即在上下两个油层之间的水层。油井出水造成的危害很多,如:(1)油井出砂,使胶结疏松的砂岩层受到破坏,造成出砂,严重时使油层塌陷或导致油井停产;(2)油井停喷,见水后含水量不断增加,井筒液柱重量随之增大,导致自喷井不能自喷;(3)形成死油区,油井过早见水,会导致在地下形成一些死油区,大大降低了油藏的采收率;(4)设备腐蚀,会腐蚀油井设备及破坏井身结构,增加修井作业任务和难度,缩短油井寿命;(5)增加采油成本,增大地面注水量,相应增加了地面水源使用量、注水设施的使用及电能消耗。Oil well water production is an important phenomenon in the process of oil production. The reasons for oil well water production are generally: (1) injection water and edge water propulsion; (2) bottom water propulsion; (3) upper layer water and lower layer water intrusion; (4) ) interlayer water enters, and interlayer water refers to the interlayer water between the oil layers, that is, the water layer between the upper and lower oil layers. There are many hazards caused by water production in oil wells, such as: (1) sand production in oil wells, which damages the cemented and loose sandstone layers, resulting in sand production, and in severe cases, oil layer collapse or oil well production shutdown; With the continuous increase of the water volume, the weight of the wellbore liquid column increases, resulting in the failure of the self-blowing well; (3) the formation of dead oil areas, the premature water breakthrough of the oil wells will lead to the formation of some dead oil areas underground, which greatly reduces the oil reservoir. (4) Equipment corrosion will corrode oil well equipment and damage well structure, increase the task and difficulty of workover operations, and shorten the life of oil wells; (5) Increase oil production costs, increase ground water injection, and correspondingly increase the surface Water usage, usage of water injection facilities and electricity consumption.
调剖堵水作为油田控水的常规措施,可以起到提高油层压力,提高注入水的波及系数,从而提高原油采收率的作用。但随着油田的开发,油藏特征及环境不断变化,尤其是油藏进入高含水开采期后,长期水驱使油藏开发矛盾更为突出,现有调剖堵水技术,特别是能有效应用的技术总是落后于油田开发的需要。对于我国的某些高温深井油藏,油藏温度高达130℃,针对上述油田,现有技术普遍使用的是聚丙烯酰胺类高温冻胶堵剂和固体颗粒型堵剂。聚丙烯酰胺类高温冻胶堵剂成胶时间过快,易造成近井地带堵塞,高温下冻胶稳定性差,且作业过程水基冻胶体系进入油层易造成伤害等缺点。固体颗粒型堵剂主要是由水泥、粉煤灰等无机固体颗粒及其它有机颗粒组成,以悬浮体的形式注入到地层,通过有机颗粒的架桥和无机颗粒的充填,来调整吸水剖面和水相渗透率,用以封堵高渗透层及出水层,达到调整吸水剖面、堵水的目的,但这是一种非选择性堵剂,并且这种颗粒型堵剂稳定性差,易结块伤害储层,仅适用于近井地带封堵。并且,针对高温深井油藏,中国专利文献CN101423753A也公开了一种稠油油井热采专用调剖剂。该调剖剂由下列原料组成:阴离子型聚丙烯酰胺,烷基酚聚氧乙烯醚,石油树脂,乌落托品,二甲苯,烧碱和水。该发明的调剖剂可以在温度为200℃、矿化度大于20000mg/L的条件下长时间使用,但该调剖剂能否在更高的矿化度条件下应用未知,阴离子型聚丙烯酰胺成胶时间快,调剖剂乳液整体稳定性欠佳,易造成近井地带堵塞,并存在聚丙烯酰胺类高温冻胶堵剂的缺陷;并且所用原料中二甲苯属于有毒物质,污染环境,长期接触对人体伤害也很大,在油田上属于管制药品。Profile control and water plugging, as a routine measure for water control in oilfields, can increase the reservoir pressure, increase the sweep coefficient of injected water, and thus improve oil recovery. However, with the development of the oil field, the characteristics and environment of the oil reservoir are constantly changing, especially after the oil reservoir enters the high water cut production period, the long-term water flooding makes the development contradiction of the oil reservoir more prominent. technology is always behind the needs of oilfield development. For some high-temperature deep well reservoirs in my country, the reservoir temperature is as high as 130°C. For the above oilfields, polyacrylamide-based high-temperature gel plugging agents and solid particle plugging agents are commonly used in the prior art. The polyacrylamide high-temperature jelly plugging agent takes too long to gel, which is easy to cause blockage in the area near the wellbore, poor jelly stability under high temperature, and the water-based jelly system enters the oil layer during the operation, which is easy to cause damage. The solid particle plugging agent is mainly composed of inorganic solid particles such as cement and fly ash and other organic particles. Phase permeability is used to block the high permeability layer and the water outlet layer to achieve the purpose of adjusting the water absorption profile and plugging water, but this is a non-selective plugging agent, and this granular plugging agent has poor stability and is easy to agglomerate and damage. Reservoir, only suitable for plugging near wellbore. In addition, for high temperature deep well oil reservoirs, Chinese patent document CN101423753A also discloses a special profile control agent for thermal recovery of heavy oil wells. The profile control agent is composed of the following raw materials: anionic polyacrylamide, alkylphenol polyoxyethylene ether, petroleum resin, urotropine, xylene, caustic soda and water. The profile control agent of the invention can be used for a long time at a temperature of 200 ° C and a salinity of more than 20,000 mg/L, but it is unknown whether the profile control agent can be used in a higher salinity condition. The gelling time of amide is fast, the overall stability of the profile control agent emulsion is not good, it is easy to cause blockage in the area near the wellbore, and there are defects of polyacrylamide high-temperature gel blocking agent; and the xylene in the raw material used is a toxic substance, which pollutes the environment. Long-term exposure is also very harmful to the human body, and it is a controlled drug in the oil field.
因此,研制一种新型的耐温抗盐堵剂,在高温和高矿化度下稳定能力强,能够顺利到达油藏油井深部实现堵水,并且具有油水选择性和优异的封堵效果,对于解决高温油藏的油井出水问题具有重要的意义。Therefore, a new type of temperature-resistant and salt-resistant plugging agent was developed, which has strong stability under high temperature and high salinity, can smoothly reach the deep part of the oil well to achieve water plugging, and has oil-water selectivity and excellent plugging effect. It is of great significance to solve the problem of oil well water production in high temperature reservoirs.
发明内容SUMMARY OF THE INVENTION
针对现有技术存在的不足,本发明提供一种耐高温石油树脂分散体堵剂。本发明堵剂注入地层后,其中的阳离子聚丙烯酰胺会在地层的高温下发生改性反应,引入与碳原子相连接的磺酸基,得到磺酸基改性的阳离子聚丙烯酰胺,该改性阳离子聚丙烯酰胺水解度低,热稳定性好,其能够有效分散、稳定石油树脂悬浮液,有效提高石油树脂分散体堵剂的耐高温性、抗盐性和稳定性,从而使石油树脂能够顺利到达油藏油井深部实现堵水。本发明的堵剂耐温性能和抗盐性能优异,在高温和高矿化度下分散稳定性好,并且具有油水选择性,能在130℃的高温油藏环境中起到有效封堵作用。In view of the deficiencies in the prior art, the present invention provides a high temperature resistant petroleum resin dispersion blocking agent. After the plugging agent of the present invention is injected into the formation, the cationic polyacrylamide in the cationic polyacrylamide will undergo a modification reaction at the high temperature of the formation, and a sulfonic acid group connected with carbon atoms is introduced to obtain a cationic polyacrylamide modified by the sulfonic acid group. The cationic polyacrylamide has low hydrolysis degree and good thermal stability. It can effectively disperse and stabilize the petroleum resin suspension, and effectively improve the high temperature resistance, salt resistance and stability of the petroleum resin dispersion blocking agent, so that the petroleum resin can be It successfully reached the deep part of the oil well in the reservoir to achieve water plugging. The plugging agent of the invention has excellent temperature resistance and salt resistance, good dispersion stability under high temperature and high salinity, and has oil-water selectivity, and can play an effective plugging role in a high temperature oil reservoir environment of 130°C.
本发明还提供一种耐高温石油树脂分散体堵剂的制备方法及其应用。本发明制备方法简单,改性阳离子聚丙烯酰胺是在注入地层后反应产生,避免了地面上一系列复杂的合成工艺,降低了成本以及危险(主要为人身安全)。The invention also provides a preparation method and application of a high temperature resistant petroleum resin dispersion blocking agent. The preparation method of the invention is simple, and the modified cationic polyacrylamide is reacted after being injected into the formation, which avoids a series of complex synthesis processes on the ground and reduces costs and dangers (mainly personal safety).
本发明的技术方案如下:The technical scheme of the present invention is as follows:
一种耐高温石油树脂分散体堵剂,包括如下质量百分比的原料制成:石油树脂5%~15%,表面活性剂0.1%~0.5%,阳离子聚丙烯酰胺0.05%~0.4%,三乙醇胺0.1%~0.4%,亚硫酸氢钠0.1%-0.5%,二氧化硅纳米颗粒1%~3%,pH调节剂0.1%~0.5%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion plugging agent, comprising the following raw materials by mass percentage: 5% to 15% of petroleum resin, 0.1% to 0.5% of surfactant, 0.05% to 0.4% of cationic polyacrylamide, and 0.1% of triethanolamine %~0.4%, sodium bisulfite 0.1%-0.5%, silica nanoparticles 1%~3%, pH adjuster 0.1%~0.5%, the balance is water; the sum of the mass percentages of each raw material is 100% .
根据本发明优选的,所述石油树脂分散体堵剂,包括如下百分比的原料制成:石油树脂5%~10%,表面活性剂0.1%~0.3%,阳离子聚丙烯酰胺0.05%~0.3%,三乙醇胺0.1%~0.2%,亚硫酸氢钠0.15%-0.4%,二氧化硅纳米颗粒1%~2%,pH调节剂0.2%~0.4%,余量为水;各原料的质量百分比之和为100%。Preferably according to the present invention, the petroleum resin dispersion plugging agent is made from the following percentages of raw materials: 5% to 10% of petroleum resin, 0.1% to 0.3% of surfactant, 0.05% to 0.3% of cationic polyacrylamide, Triethanolamine 0.1%-0.2%, sodium bisulfite 0.15%-0.4%, silica nanoparticles 1%-2%, pH adjuster 0.2%-0.4%, the balance is water; the sum of the mass percentages of each raw material is 100%.
根据本发明优选的,所述石油树脂为C5或C9的石油树脂,相对分子质量为1000~5000,软化点为100℃~120℃。Preferably according to the present invention, the petroleum resin is C5 or C9 petroleum resin, the relative molecular mass is 1000-5000, and the softening point is 100°C-120°C.
根据本发明优选的,所述表面活性剂为两性表面活性剂;优选的,所述表面活性剂为十八烷基二甲基氧化铵。Preferably according to the present invention, the surfactant is an amphoteric surfactant; preferably, the surfactant is octadecyl dimethyl ammonium oxide.
根据本发明优选的,所述阳离子聚丙烯酰胺的重均分子量为700×104~800×104,阳离子度为20-40%。Preferably according to the present invention, the weight-average molecular weight of the cationic polyacrylamide is 700×10 4 to 800×10 4 , and the cationic degree is 20-40%.
根据本发明优选的,所述二氧化硅纳米颗粒的粒径为10-14nm。Preferably according to the present invention, the particle size of the silica nanoparticles is 10-14 nm.
根据本发明优选的,所述pH调节剂为氢氧化钠。Preferably according to the present invention, the pH adjusting agent is sodium hydroxide.
根据本发明优选的,所述水是矿化度为(20-25)×104mg/L的地层水,其中Na+含量为(7-8)×104mg/L、Ca2+含量为(0.5-1.5)×104mg/L、Mg2+含量为(0.1-0.2)×104mg/L、HCO3 -含量为(0.01-0.02)×104mg/L、Cl-含量为(13-14)×104mg/L;优选的,所述水是矿化度为22.3×104mg/L的地层水,其中Na+含量为7.3×104mg/L、Ca2+含量为1.1×104mg/L、Mg2+含量为0.15×104mg/L、HCO3 -含量为0.018×104mg/L、Cl-含量为13.7×104mg/L。Preferably according to the present invention, the water is formation water with a salinity of (20-25)×10 4 mg/L, wherein the Na + content is (7-8)×10 4 mg/L, and the Ca 2+ content (0.5-1.5)×10 4 mg/L, Mg 2+ content (0.1-0.2)×10 4 mg/L, HCO 3 -content (0.01-0.02)×10 4 mg/L, Cl -content is (13-14)×10 4 mg/L; preferably, the water is formation water with a salinity of 22.3×10 4 mg/L, wherein the Na + content is 7.3×10 4 mg/L, Ca 2 The + content was 1.1×10 4 mg/L, the Mg 2+ content was 0.15×10 4 mg/L, the HCO 3 - content was 0.018×10 4 mg/L, and the Cl - content was 13.7×10 4 mg/L.
上述耐高温石油树脂分散体堵剂的制备方法,包括步骤:The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent, comprising the steps:
将表面活性剂溶于水中,加入石油树脂粉末,充分分散得石油树脂分散液;将阳离子聚丙烯酰胺、三乙醇胺、亚硫酸氢钠和pH调节剂溶于水中,加入二氧化硅纳米颗粒,充分分散得混合液;将混合液和石油树脂分散液混合均匀,即得石油树脂分散体堵剂。Dissolve the surfactant in water, add petroleum resin powder, and fully disperse the petroleum resin dispersion; dissolve the cationic polyacrylamide, triethanolamine, sodium bisulfite and pH adjuster in water, add silica nanoparticles, and fully Disperse to obtain a mixed solution; mix the mixed solution and the petroleum resin dispersion evenly to obtain the petroleum resin dispersion blocking agent.
根据本发明优选的,所述石油树脂粉末是采用冷冻粉碎方法,即以液氮为冷源,将石油树脂粉粹成粒径为0.5微米~10微米的粉末。According to the preferred embodiment of the present invention, the petroleum resin powder adopts a freezing pulverization method, that is, using liquid nitrogen as a cold source, the petroleum resin powder is pulverized into a powder with a particle size of 0.5 micrometers to 10 micrometers.
根据本发明优选的,所述石油树脂分散液中石油树脂的质量浓度为25-30%。Preferably according to the present invention, the mass concentration of the petroleum resin in the petroleum resin dispersion liquid is 25-30%.
上述耐高温石油树脂分散体堵剂应用于高温油藏油井进行调剖堵水。The above-mentioned high temperature resistant petroleum resin dispersion plugging agent is used for profile control and water plugging of oil wells in high temperature oil reservoirs.
根据本发明优选的,所述应用方法为:将石油树脂分散体堵剂注入高温油藏油井中,随着油藏油井中从上到下的温度逐渐升高,石油树脂分散体堵剂中的阳离子聚丙烯酰胺与三乙醇胺、亚硫酸氢钠发生磺酸基改性反应得到磺酸基改性阳离子聚丙烯酰胺,所述磺酸基改性阳离子聚丙烯酰胺的重均分子量为710×104~810×104,其能够有效分散、稳定石油树脂悬浮液,有效提高石油树脂分散体堵剂的耐高温性、抗盐性和稳定性,从而达到将石油树脂分散体堵剂注入油藏油井深部而不堵塞近井地带的目的,进入油藏油井深部后的石油树脂开始软化变粘从而聚结封堵水流通道达到堵水的目的。According to the preferred method of the present invention, the application method is as follows: injecting the petroleum resin dispersion plugging agent into the high-temperature oil reservoir oil well, and as the temperature in the oil reservoir oil well gradually increases from top to bottom, the The sulfonic acid group modification reaction of the cationic polyacrylamide with triethanolamine and sodium bisulfite obtains the sulfonic acid group modified cationic polyacrylamide, and the weight average molecular weight of the sulfonic acid group modified cationic polyacrylamide is 710×10 4 ~810×10 4 , it can effectively disperse and stabilize the petroleum resin suspension, effectively improve the high temperature resistance, salt resistance and stability of the petroleum resin dispersion plugging agent, so as to achieve the injection of the petroleum resin dispersion plugging agent into the oil reservoir oil well The purpose of not blocking the near-well zone in the deep part, the petroleum resin after entering the deep part of the oil well begins to soften and become sticky, so as to coalesce and block the water flow channel to achieve the purpose of water blocking.
本发明的技术特点和有益效果如下:The technical characteristics and beneficial effects of the present invention are as follows:
1、聚丙烯酰胺在高温高盐下易水解,且热氧化作用及高盐条件下聚丙烯酰胺的溶解度会变差而导致其稳定性也会变差;为了改善上述缺陷,本发明利用阳离子聚合物中碳阳离子在高温作用下与碱性物质易发生结合、转移、异构化等反应的特点,在阳离子聚丙烯酰胺中添加了三乙醇胺、亚硫酸氢钠以及二氧化硅纳米颗粒,当堵剂进入地层后,温度逐渐升高,在高温、强碱条件下,阳离子聚丙烯酰胺首先与三乙醇胺反应,羟甲基取代酰胺基上的一个氢,生成物再与亚硫酸氢钠反应,使得一部分羟甲基上的羟基又被磺酸钠基团取代,在纳米颗粒的作用下提高了生成物的高温稳定性,降低了其水解度,最终生成的改性阳离子聚丙烯酰胺(平均分子量为700×104~800×104)耐温性能大大提高,稳定能力强。在表面活性剂的润湿作用下,石油树脂分散在表面活性剂溶液中,当改性阳离子聚丙烯酰胺生成后,极大的提高了石油树脂分散体分散稳定性以及耐温抗盐性能,明显改善了其它颗粒型堵剂存在的缺陷。本发明制备的石油树脂分散体注入地层后,由于改性阳离子聚丙烯酰胺的存在,结合表面活性剂助剂,使石油树脂悬浮液耐温和抗盐性能优异,分散稳定性好,能够顺利到达油藏油井深部,并在130℃的高温油藏环境中起到有效封堵作用。1. Polyacrylamide is easily hydrolyzed at high temperature and high salt, and the solubility of polyacrylamide under thermal oxidation and high-salt conditions will deteriorate, resulting in poor stability; in order to improve the above defects, the present invention utilizes cationic polymerization. Carbocations are easy to combine, transfer, and isomerize with alkaline substances under the action of high temperature. Triethanolamine, sodium bisulfite and silica nanoparticles are added to cationic polyacrylamide. After the agent enters the formation, the temperature gradually rises. Under the conditions of high temperature and strong alkali, the cationic polyacrylamide first reacts with triethanolamine, hydroxymethyl replaces one hydrogen on the amide group, and the product reacts with sodium bisulfite, so that Part of the hydroxyl groups on the hydroxymethyl group are replaced by sodium sulfonate groups, which improves the high temperature stability of the product and reduces its degree of hydrolysis under the action of nanoparticles. The final modified cationic polyacrylamide (average molecular weight is 700×10 4 ~800×10 4 ) The temperature resistance is greatly improved and the stability is strong. Under the wetting action of the surfactant, the petroleum resin is dispersed in the surfactant solution. When the modified cationic polyacrylamide is formed, the dispersion stability and the temperature and salt resistance of the petroleum resin dispersion are greatly improved. The defects of other granular plugging agents are improved. After the petroleum resin dispersion prepared by the invention is injected into the formation, due to the existence of the modified cationic polyacrylamide, combined with the surfactant auxiliary, the petroleum resin suspension has excellent temperature resistance and salt resistance, good dispersion stability, and can reach the oil smoothly. It can effectively block the deep oil wells in the high temperature reservoir environment of 130 °C.
2、本发明石油树脂分散体堵剂在高温和高盐下稳定性好,能够注入油藏油井深部而不会堵塞近井地带,进入油藏油井深部后的石油树脂开始软化变粘从而聚结封堵水流通道达到堵水的目。石油树脂在地层温度下具有较高的粘度,利用其软化聚结呈液态后的高粘特性,粘连吸附在孔隙岩石表面对地层孔隙进行封堵,并且在高温高盐下封堵效果好,封堵时间长;本发明中石油树脂不溶于乙醇和水,能溶于油中,可实现选择性堵水不堵油,能有效的封堵高渗透层。而水基冻胶无油水选择性,聚合物在交联剂作用下在孔隙内成胶,对水层封堵效果与石油树脂相比较差,高温高盐下易于脱水而失效,且易对储层造成污染,其可对油层进行封堵,但会造成水驱采收率降低。2. The petroleum resin dispersion plugging agent of the present invention has good stability under high temperature and high salt, and can be injected into the deep part of the oil well in the oil reservoir without blocking the near-well zone. The petroleum resin after entering the deep part of the oil well in the oil reservoir begins to soften and become sticky to coalesce Block the water flow channel to achieve the purpose of blocking water. Petroleum resin has high viscosity at formation temperature. Using its high viscosity after softening and coalescing to liquid state, it can be adhered and adsorbed on the surface of pore rock to seal the pores of the formation, and the sealing effect is good under high temperature and high salt. The plugging time is long; the petroleum resin in the present invention is insoluble in ethanol and water, but can be dissolved in oil, which can realize selective water plugging but not oil plugging, and can effectively plug high-permeability layers. The water-based gel has no oil-water selectivity, and the polymer forms gel in the pores under the action of the cross-linking agent. Compared with the petroleum resin, the sealing effect on the water layer is poor. The formation can cause contamination, which can plug the oil layer, but it will reduce the recovery rate of water flooding.
3、本发明原料廉价易得,制备方法简单;本发明石油树脂分散体堵剂注入地层后,其中的阳离子聚丙烯酰胺在地层高温作用下反应产生改性阳离子聚丙烯酰胺,避免了地面上一系列复杂的合成工艺,降低了成本以及危险(主要为人身安全)。3. The raw materials of the present invention are cheap and easy to obtain, and the preparation method is simple; after the petroleum resin dispersion plugging agent of the present invention is injected into the formation, the cationic polyacrylamide in it reacts under the action of the high temperature of the formation to produce modified cationic polyacrylamide, which avoids the occurrence of the cationic polyacrylamide on the ground. A series of complex synthesis processes reduce costs and risks (mainly personal safety).
4、本发明制备的石油树脂分散体经高温反应后具有良好的稳定性,在高温和高矿化度下分散体稳定时间可达22h,本发明的堵剂同时具有较高的封堵率,在高矿化度(22×104mg/L)、高温(130℃)下,封堵率高达98.3%。4. The petroleum resin dispersion prepared by the present invention has good stability after high temperature reaction, and the dispersion stability time can reach 22h at high temperature and high salinity. The blocking agent of the present invention also has a high blocking rate, At high salinity (22×10 4 mg/L) and high temperature (130°C), the blocking rate is as high as 98.3%.
具体实施方式Detailed ways
下面通过具体实施例对本发明做进一步说明,但不限于此。The present invention will be further described below through specific embodiments, but not limited thereto.
实施例中所用原料均为常规原料,可市购获得;所述方法如无特殊说明均为现有技术。The raw materials used in the examples are all conventional raw materials, which are commercially available; the methods are all prior art unless otherwise specified.
实施例中,所用石油树脂为C9石油树脂,广州力本有限公司有售,平均相对分子质量为3500,软化点为120℃;阳离子聚丙烯酰胺,重均分子量为750×104,阳离子度为30%,安徽巨成精细化工有限公司有售;所用二氧化硅纳米颗粒平均粒径为12nm,Sigma-Aldrich公司有售。In the embodiment, the petroleum resin used is C9 petroleum resin, available from Guangzhou Liben Co., Ltd., the average relative molecular mass is 3500, and the softening point is 120°C ; 30%, available from Anhui Jucheng Fine Chemical Co., Ltd.; the silica nanoparticles used have an average particle size of 12 nm, available from Sigma-Aldrich.
所用水是矿化度为22.3×104mg/L的地层水,其中Na+含量为7.3×104mg/L、Ca2+含量为1.1×104mg/L、Mg2+含量为0.15×104mg/L、HCO3 -含量为0.018×104mg/L、Cl-含量为13.7×104mg/L。The water used is formation water with a salinity of 22.3×10 4 mg/L, of which the Na + content is 7.3×10 4 mg/L, the Ca 2+ content is 1.1×10 4 mg/L, and the Mg 2+ content is 0.15 ×10 4 mg/L, HCO 3 -content is 0.018×10 4 mg/L, Cl -content is 13.7×10 4 mg/L.
所用石油树脂粉末:采用冷冻粉碎方法,即以液氮为冷源,将石油树脂粉碎成粒径为0.5微米~2微米的石油树脂粉末。The petroleum resin powder used: adopt the freezing pulverization method, that is, use liquid nitrogen as the cold source to pulverize the petroleum resin into petroleum resin powder with a particle size of 0.5 micrometers to 2 micrometers.
实施例1Example 1
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.2%,阳离子聚丙烯酰胺0.1%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high-temperature resistant petroleum resin dispersion blocking agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.2%, cationic polyacrylamide 0.1%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,包括步骤:The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent, comprising the steps:
向25g矿化度为22.3×104mg/L的地层水中加入0.2g十八烷基二甲基氧化铵,充分溶解搅拌均匀,缓慢加入10g石油树脂粉末(加入过程控制在5~10min),充分搅拌分散均匀得混合液A;向13g矿化度为22.3×104mg/L的地层水中加入0.2g亚硫酸氢钠、0.2g三乙醇胺,搅拌均匀,使其充分溶解,加入50g质量浓度为0.2%的阳离子聚丙烯酰胺水溶液,并加入0.3g氢氧化钠和1.1g二氧化硅纳米颗粒,充分分散搅拌均匀得混合液B;将混合液A和混合液B充分混合,即得石油树脂分散体堵剂。Add 0.2 g of octadecyl dimethyl ammonium oxide to 25 g of formation water with a salinity of 22.3×10 4 mg/L, fully dissolve and stir evenly, slowly add 10 g of petroleum resin powder (the addition process is controlled within 5-10 minutes), Fully stir and disperse evenly to obtain mixed solution A; add 0.2 g of sodium bisulfite and 0.2 g of triethanolamine to 13 g of formation water with a salinity of 22.3×10 4 mg/L, stir evenly, make it fully dissolved, and add 50 g of mass concentration It is a 0.2% cationic polyacrylamide aqueous solution, and 0.3 g of sodium hydroxide and 1.1 g of silica nanoparticles are added, and the mixture is fully dispersed and stirred to obtain a mixed solution B; the mixed solution A and the mixed solution B are fully mixed to obtain the petroleum resin. Dispersion blocking agent.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置15h后,石油树脂仍稳定分散,未发生聚结现象,说明本发明的堵剂在使用后形成的磺酸基改性阳离子聚丙烯酰胺能够提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, cationic polyacrylamide undergoes modification reaction to generate sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; It is still stably dispersed and no coalescence occurs, indicating that the sulfonic acid group-modified cationic polyacrylamide formed by the plugging agent of the present invention after use can improve the stability of the petroleum resin under high temperature and high salt conditions.
实施例2Example 2
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.25%,阳离子聚丙烯酰胺0.1%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion blocking agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.25%, cationic polyacrylamide 0.1%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,与实施例1一致,所不同的是:表面活性剂十八烷基二甲基氧化铵的用量为0.25g,其它步骤和条件与实施例1相同。The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent is consistent with Example 1, the difference is: the consumption of the surfactant octadecyl dimethyl ammonium oxide is 0.25g, and other steps and conditions are the same as those in Example 1. same.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置16h后,石油树脂仍稳定分散,未发生聚结现象,说明表面活性剂的用量在本发明范围之内时,提高表面活性剂的用量,可以提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, the cationic polyacrylamide undergoes a modification reaction to form a sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; the above-mentioned high-temperature-treated plugging agent is placed at 130 ° C for 16 hours, and the petroleum resin It is still stably dispersed and no coalescence occurs, indicating that when the amount of surfactant is within the scope of the present invention, increasing the amount of surfactant can improve the stability of petroleum resin under high temperature and high salt conditions.
实施例3Example 3
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.3%,阳离子聚丙烯酰胺0.1%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion blocking agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.3%, cationic polyacrylamide 0.1%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,与实施例1一致,所不同的是:表面活性剂十八烷基二甲基氧化铵的用量为0.3g,其它步骤和条件与实施例1相同。The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent is consistent with Example 1, the difference is: the consumption of the surfactant octadecyl dimethyl ammonium oxide is 0.3g, and other steps and conditions are the same as those in Example 1. same.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置17h后,石油树脂仍稳定分散,未发生聚结现象,说明表面活性剂的用量在本发明范围之内时,提高表面活性剂的用量,可以提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, the cationic polyacrylamide undergoes a modification reaction to form a sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; the above-mentioned high-temperature-treated plugging agent is placed at 130 ° C for 17 hours, and the petroleum resin It is still stably dispersed and no coalescence occurs, indicating that when the amount of surfactant is within the scope of the present invention, increasing the amount of surfactant can improve the stability of petroleum resin under high temperature and high salt conditions.
实施例4Example 4
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.2%,阳离子聚丙烯酰胺0.15%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion plugging agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.2%, cationic polyacrylamide 0.15%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,与实施例1一致,所不同的是:加入50g质量浓度为0.3%的阳离子聚丙烯酰胺水溶液,其它步骤和条件与实施例1相同。The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent is the same as that in Example 1, the difference is that 50 g of cationic polyacrylamide aqueous solution with a mass concentration of 0.3% is added, and other steps and conditions are the same as those in Example 1.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置18h后,石油树脂仍稳定分散,未发生聚结现象,说明阳离子聚丙烯酰胺的用量在本发明范围之内时,提高其用量,可以提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, the cationic polyacrylamide undergoes a modification reaction to form a sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; the above-mentioned high-temperature-treated plugging agent is placed at 130 ℃ for 18 hours, and the petroleum resin It is still stably dispersed and no agglomeration occurs, indicating that when the dosage of cationic polyacrylamide is within the scope of the present invention, increasing its dosage can improve the stability of petroleum resin under high temperature and high salt conditions.
实施例5Example 5
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.25%,阳离子聚丙烯酰胺0.3%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion blocking agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.25%, cationic polyacrylamide 0.3%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,与实施例2一致,所不同的是:加入50g质量浓度为0.6%的阳离子聚丙烯酰胺水溶液,其它步骤和条件与实施例2相同。The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion plugging agent is the same as that of Example 2, the difference is that 50g of cationic polyacrylamide aqueous solution with a mass concentration of 0.6% is added, and other steps and conditions are the same as those of Example 2.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置22h后,石油树脂仍稳定分散,未发生聚结现象,说明阳离子聚丙烯酰胺的用量在本发明范围之内时,提高其用量,可以提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, cationic polyacrylamide undergoes a modification reaction to generate sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; It is still stably dispersed and no agglomeration occurs, indicating that when the dosage of cationic polyacrylamide is within the scope of the present invention, increasing its dosage can improve the stability of petroleum resin under high temperature and high salt conditions.
实施例6Example 6
一种耐高温石油树脂分散体堵剂,包括如下百分比的原料制成:C9石油树脂10%,十八烷基二甲基氧化铵0.3%,阳离子聚丙烯酰胺0.15%,三乙醇胺0.2%,亚硫酸氢钠0.2%,二氧化硅纳米颗粒1.1%,氢氧化钠0.3%,余量为水;各原料的质量百分比之和为100%。A high temperature resistant petroleum resin dispersion blocking agent, comprising the following percentages of raw materials: C9 petroleum resin 10%, octadecyl dimethyl ammonium oxide 0.3%, cationic polyacrylamide 0.15%, triethanolamine 0.2%, 0.2% of sodium hydrogen sulfate, 1.1% of silica nanoparticles, 0.3% of sodium hydroxide, and the balance of water; the sum of the mass percentages of each raw material is 100%.
上述耐高温石油树脂分散体堵剂的制备方法,与实施例3一致,所不同的是:加入50g质量浓度为0.3%的阳离子聚丙烯酰胺水溶液,其它步骤和条件与实施例3相同。The preparation method of the above-mentioned high temperature resistant petroleum resin dispersion blocking agent is the same as that in Example 3, the difference is that 50 g of cationic polyacrylamide aqueous solution with a mass concentration of 0.3% is added, and other steps and conditions are the same as those in Example 3.
模拟高温油藏油井条件:将上述得到的石油树脂分散体堵剂在90℃下,搅拌5h,得高温处理后的堵剂。堵剂中,阳离子聚丙烯酰胺发生改性反应生成磺酸基改性阳离子聚丙烯酰胺,其重均分子量为750×104;上述高温处理后的堵剂在130℃下放置18h后,石油树脂仍稳定分散,未发生聚结现象,说明阳离子聚丙烯酰胺的用量在本发明范围之内时,提高其用量,可以提高石油树脂高温和高盐条件下的稳定性。Simulate oil well conditions in high temperature oil reservoirs: stir the above obtained petroleum resin dispersion plugging agent at 90°C for 5 hours to obtain a plugging agent after high temperature treatment. In the plugging agent, the cationic polyacrylamide undergoes a modification reaction to form a sulfonic acid group-modified cationic polyacrylamide, and its weight average molecular weight is 750×10 4 ; the above-mentioned high-temperature-treated plugging agent is placed at 130 ℃ for 18 hours, and the petroleum resin It is still stably dispersed and no coalescence occurs, indicating that when the dosage of cationic polyacrylamide is within the scope of the present invention, increasing its dosage can improve the stability of the petroleum resin under high temperature and high salt conditions.
对比例1Comparative Example 1
一种堵剂的制备方法,如实施例1所述,所不同的是:不加入氢氧化钠,其它步骤和条件与实施例1一致。A preparation method of a plugging agent is as described in Example 1, except that sodium hydroxide is not added, and other steps and conditions are consistent with Example 1.
模拟高温油藏油井条件:将上述得到的堵剂在90℃下,搅拌5h,得高温处理后的堵剂。上述高温处理后的堵剂在130℃下放置3h后,石油树脂出现聚结现象,说明改性后的阳离子型聚丙烯酰胺可以有效的提高石油树脂在高温高盐下的稳定性。Simulation of high temperature reservoir oil well conditions: the above obtained plugging agent was stirred at 90°C for 5 hours to obtain the plugging agent after high temperature treatment. After the above-mentioned high-temperature-treated plugging agent was placed at 130 °C for 3 hours, the petroleum resin coalesced, indicating that the modified cationic polyacrylamide could effectively improve the stability of the petroleum resin under high temperature and high salt.
本对比例制备的堵剂稳定时间短,不能注入油藏油井的深部,过早出现聚结现象,封堵近井地带。The plugging agent prepared in this comparative example has a short stable time and cannot be injected into the deep part of the oil well in the oil reservoir, and premature coalescence occurs, blocking the area near the wellbore.
对比例2Comparative Example 2
在50g自来水中加入0.05g间苯二酚、0.1g乌洛托品,搅拌均匀,使充分溶解或分散,再将50g用自来水配制的质量浓度为15%的水解度为20%的阴离子聚丙烯酰胺溶液与上述溶液混合,搅拌均匀,将得到的成胶液置于安瓿瓶中,密封处理。然后将其置于130℃的烘箱中,分别放置20、60、90天,计算安瓿瓶中冻胶的脱水率。Add 0.05g of resorcinol and 0.1g of urotropine to 50g of tap water, stir evenly to fully dissolve or disperse, and then add 50g of anionic polypropylene with a mass concentration of 15% and a degree of hydrolysis of 20% prepared with tap water. The amide solution is mixed with the above solution, stirred evenly, and the obtained gel-forming solution is placed in an ampoule bottle and sealed. Then it was placed in an oven at 130°C for 20, 60, and 90 days, respectively, and the dehydration rate of the jelly in the ampoule was calculated.
表1水基冻胶脱水率Table 1 Dehydration rate of water-based jelly
本对比例中冻胶脱水较为严重,将会影响其在地层中的封堵能力,使其封堵能力大幅度降低。In this comparative example, the dehydration of the jelly is more serious, which will affect its plugging ability in the formation and greatly reduce its plugging ability.
应用例Application example
封堵能力考察:Blocking ability inspection:
以“实施例1-6”中获得的高温处理后的堵剂为研究对象,考察本发明所提供的石油树脂分散体的封堵能力。以“对比例2”中得到的成胶液为研究对象,考察聚丙烯酰胺类堵剂的封堵能力并以此作为对比。具体模拟实验过程如下:将内径为2.5cm、长度为20cm的七根填砂管填充石英砂粒制得模拟岩心,分别记作1#、2#、3#、4#、5#、6#、7#,水驱至压力稳定后得到原始渗透率k1,然后将“实施例1-6”中的高温处理后的堵剂以及“对比例2”中得到的成胶液分别反向注入上述七根填砂管中,注入体积为0.25PV(岩心孔隙体积),然后注入0.25PV水进行顶替(注入的目的是将堵剂顶替到填砂管的中部,模拟地层条件下的注入地层深部),之后将七根填砂管置于130℃烘箱中分别老化30天和80天,最后分别水驱至压力稳定,测得模拟岩心的堵后渗透率k2,并按公式E=(k1-k2)/k1*100%,计算岩心封堵率E,实验结果如下表所示。Taking the blocking agent after high temperature treatment obtained in "Example 1-6" as the research object, the blocking ability of the petroleum resin dispersion provided by the present invention was investigated. Taking the glue-forming liquid obtained in "Comparative Example 2" as the research object, the blocking ability of the polyacrylamide-based plugging agent was investigated and used as a comparison. The specific simulation experiment process is as follows: seven sand-packing pipes with an inner diameter of 2.5cm and a length of 20cm are filled with quartz sand grains to obtain simulated cores, which are denoted as 1#, 2#, 3#, 4#, 5#, 6#, 7#, the original permeability k 1 is obtained after the water is flooded to a stable pressure, and then the plugging agent after high temperature treatment in "Example 1-6" and the gel-forming liquid obtained in "Comparative Example 2" are reversely injected into the above-mentioned In the seven sand-packing pipes, the injection volume is 0.25PV (core pore volume), and then 0.25PV of water is injected for displacement (the purpose of injection is to displace the plugging agent in the middle of the sand-packing pipe, simulating the injection into the deep formation under the formation conditions) , and then put the seven sand-packing pipes in an oven at 130 °C for 30 days and 80 days, respectively, and finally water-flood until the pressure is stable, and measure the permeability k 2 of the simulated core after plugging. -k 2 )/k 1 *100%, calculate the core plugging rate E, and the experimental results are shown in the following table.
表2封堵能力测试数据Table 2 Plugging ability test data
以上实验结果表明:本发明提供的石油树脂分散体堵剂在130℃高温条件下具有优异的封堵性能,与对比例2相比无论是其20天后的封堵效果还是90天后的封堵效果,都不如本发明石油树脂分散体堵剂封堵效果好,石油树脂分散体堵剂具有长期较为稳定的封堵效果。The above experimental results show that: the petroleum resin dispersion plugging agent provided by the present invention has excellent plugging performance under the high temperature condition of 130 ° C. Compared with Comparative Example 2, whether it is the plugging effect after 20 days or the plugging effect after 90 days. , are not as good as the plugging effect of the petroleum resin dispersion plugging agent of the present invention, and the petroleum resin dispersion plugging agent has a relatively stable plugging effect for a long time.
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