CN1472276A - Efficient thickened oil and super-thickened oil viscosity reducer - Google Patents
Efficient thickened oil and super-thickened oil viscosity reducer Download PDFInfo
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Abstract
Description
技术领域:Technical field:
本发明涉及一种高效稠油、超稠油降粘剂,属稠油、超稠油,尤其是掺活性水替代电加热,掺稀油开采稠油、特稠油的乳化表面活性剂合成技术类。The invention relates to a high-efficiency viscous reducer for heavy oil and super heavy oil, which belongs to heavy oil and super heavy oil, especially the synthesis technology of emulsifying surfactant mixed with active water instead of electric heating and mixed with thin oil to exploit heavy oil and extra heavy oil kind.
背景技术:Background technique:
油田稠油、超稠油的开采方式多年来一直采用往油井内掺稀油的方法,及井筒电加热工艺,二者的目的便是使稠油变稀后,采出地面,由于稠油掺稀油工艺技术存在着价格方面的差异以及可掺稀油减少的趋势;而超稠油电加热开采工艺技术存在着电能消耗过高的问题,从而导致吨油采出成本大幅度增加,因此,目前,国内外正在寻求一种能耗少吨油采出成本低的化学工艺技术替代现技术中的稠油掺稀油以及超稠油井筒电加热工艺技术,本发明经查国内外专利未见报导。The heavy oil and ultra-heavy oil production methods in the oil field have been using the method of mixing thin oil into the oil well for many years, and the electric heating process of the wellbore. There are price differences in thin oil technology and the trend of reducing the amount of thin oil that can be blended; and the electric heating recovery technology of super heavy oil has the problem of high power consumption, which leads to a significant increase in the cost of oil production per ton. Therefore, At present, domestic and foreign are looking for a chemical process technology with low energy consumption and low production cost of tons of oil to replace the existing technology of heavy oil mixed with thin oil and ultra-heavy oil wellbore electric heating process technology. The invention has not been found in domestic and foreign patents. report.
发明内容:Invention content:
本发明目的是为了克服上述缺点而提供的一种高效稠油超稠油降粘剂,该降粘剂采用掺活性水和化学降粘方法替代与改变目前原油在开采过程中因掺稀油以及井筒电加热工艺存在的能源高吨油采出成本大幅度升高的现状,另外,本发明还能将稠油井筒降粘,管道输送与联合站脱水施工结为一体,实现降粘脱水一体化目标,从而可进一步降低开采原油成本。本发明的实现方式是:The object of the present invention is to provide a kind of high-efficiency heavy oil super heavy oil viscosity reducer in order to overcome the above-mentioned shortcoming, this viscosity reducer adopts the method of mixing active water and chemical viscosity reduction to replace and change the current crude oil in the exploitation process due to mixing thin oil and The current situation of high energy per ton oil production cost in wellbore electric heating technology has greatly increased. In addition, the present invention can also integrate heavy oil wellbore viscosity reduction, pipeline transportation and combined station dehydration construction to realize the integration of viscosity reduction and dehydration The goal is to further reduce the cost of extracting crude oil. The realization mode of the present invention is:
为实现上述目的,本发明的高效稠油超稠油降粘剂配制方法由化学药剂烷基酚聚氧乙烯醚,聚氧乙烯聚氧丙烯多乙烯多胺,十二烷基苯磺酸钠做主剂;长链醇和渗透剂做辅剂按照一定的配比所制成的水基降粘剂;该降粘剂配制时有效成份总含量不低于45~60%重量百分比。In order to achieve the above object, the preparation method of the high-efficiency heavy oil super heavy oil viscosity reducer of the present invention is dominated by the chemical agent alkylphenol polyoxyethylene ether, polyoxyethylene polyoxypropylene polyethylene polyamine, and sodium dodecylbenzenesulfonate. agent; long-chain alcohol and penetrating agent as auxiliary agents, water-based viscosity reducer made according to a certain ratio; when the viscosity reducer is prepared, the total active ingredient content is not less than 45-60% by weight.
本发明所述高效稠油超稠油的降粘剂制备方法,其特征是,在摄氏50~80度常压搅拌条件下首先将十二烷基苯磺酸钠配制成10~20%浓度的溶液,再依次向上述体系缓慢加入烷基酚聚氧乙稀醚,聚氧乙烯聚氧丙多乙烯多胺,长链醇及渗透剂,所加入各原料的重量比为10∶20∶10∶4∶5~20∶10∶3∶1∶2,同时以60~120转/分钟转速,连续搅拌60~90分钟,即可得到本水基降粘剂。The preparation method of the high-efficiency heavy oil super heavy oil viscosity reducer of the present invention is characterized in that, under the condition of normal pressure stirring at 50-80 degrees Celsius, firstly, sodium dodecylbenzenesulfonate is prepared into a 10-20% concentration solution, and then slowly add alkylphenol polyoxyethylene ether, polyoxyethylene polyoxypropylene polyethylene polyamine, long-chain alcohol and penetrating agent to the above system in sequence, and the weight ratio of the added raw materials is 10:20:10: 4: 5-20: 10: 3: 1: 2, while stirring at 60-120 rpm for 60-90 minutes, the water-based viscosity reducer can be obtained.
本发明所述的高效稠油超稠油降粘剂使用时,首先在摄氏20~50度水中加入该降粘剂,配制好的降粘剂重量百分比为:0.1~1%的水溶液,然后再将此溶液加入到摄氏45~90度的原油中,水溶液与原油的混合时的比例为4∶6~1∶9混合液,然后在30~120转/分钟下搅拌1~3分钟;即可形成低粘度的水包型乳状液。所述的长链醇为月桂醇(十二醇),渗透剂为烷基醇聚氧乙烯醚。When using the high-efficiency heavy oil super heavy oil viscosity reducer described in the present invention, first add the viscosity reducer in water at 20-50 degrees Celsius, the weight percentage of the prepared viscosity reducer is: 0.1-1% aqueous solution, and then Add this solution to the crude oil at 45-90 degrees Celsius, the ratio of the aqueous solution to the crude oil is 4:6-1:9 mixed liquid, and then stir at 30-120 rpm for 1-3 minutes; Forms a low viscosity water-in-water emulsion. The long-chain alcohol is lauryl alcohol (lauryl alcohol), and the penetrating agent is alkyl alcohol polyoxyethylene ether.
本发明与现有技术相比具有显著效果。Compared with the prior art, the present invention has remarkable effect.
由于本发明中水基降粘剂采用了主剂及辅剂原料并按一定比例复配成有机合成表面活性剂,对稠油和超稠油具有良好降粘效果,该降粘剂还具有自动破乳脱水性能,用于超稠油降粘其降粘率达99%以上。另外如用于井站或联会站的脱水工序,在联会站或井站使用时,可实现自动破乳脱水,即使在不加任何破乳剂情况下,当罐内原油在摄氏85度温度下沉降72小时,含水率仍可降至4%以下,另外该降粘剂与现有破乳剂具有良好的配比性,有助于快速脱水。降粘剂成本低,应用后与井筒电加热相比能使采出油成本下降15~20元/吨油。Since the water-based viscosity reducer in the present invention adopts the main agent and auxiliary agent raw materials and is compounded into an organic synthetic surfactant in a certain proportion, it has a good viscosity reduction effect on heavy oil and super heavy oil, and the viscosity reducer also has automatic Demulsification and dehydration performance, used for viscosity reduction of super heavy oil, its viscosity reduction rate can reach more than 99%. In addition, if it is used in the dehydration process of the well station or the union station, when it is used in the union station or the well station, it can realize automatic demulsification and dehydration. Even without adding any demulsifier, when the crude oil in the tank is at a temperature of 85 degrees Celsius After 72 hours of subsidence, the water content can still be reduced to less than 4%. In addition, the viscosity reducer has a good ratio with the existing demulsifier, which is helpful for rapid dehydration. The cost of the viscosity reducer is low, and after application, it can reduce the cost of produced oil by 15-20 yuan/ton of oil compared with wellbore electric heating.
附图说明:Description of drawings:
图1,本发明井下部分施工流程图Fig. 1, the downhole part construction flow chart of the present invention
图2,本发明地面部分施工流程示意图Fig. 2, the schematic diagram of the construction process of the ground part of the present invention
图中:1、空心抽油杆,2、油管,3、套管,4、抽油泵,7、工作筒,8、搅拌器,9、空心螺杆泵,12、1#药罐,13、2#药罐,14、3#水罐,15、4#油罐,16、5#油罐,17、抽油机,18、油层组成。In the figure: 1. Hollow sucker rod, 2. Oil pipe, 3. Casing pipe, 4. Oil well pump, 7. Work cylinder, 8. Agitator, 9. Hollow screw pump, 12. 1# medicine tank, 13, 2 #medicine tank, 14, 3# water tank, 15, 4# oil tank, 16, 5# oil tank, 17, pumping unit, 18, composition of oil layer.
具体实施方式:Detailed ways:
本发明由以下实施例给出:The invention is given by the following examples:
下面结合附图对本发明做进一步描述:The present invention will be further described below in conjunction with accompanying drawing:
实施例1,降粘剂用于稠油超稠油降粘剂施工的方法。首先在20~50℃的水中加入该降粘剂;降粘剂的重量百分比为0.1~1%的水溶液,然后,在药罐内搅拌将加热后的降粘剂从室心抽油杆1中将此水溶液输入到45~90℃的井下混合装置中的工作筒7和搅拌器8内,使掺入降粘剂的原油得到充分搅拌,此时,水溶液与原油比例为4:6~1∶9又经搅拌器8,30~120转/分钟的搅拌,1~3分钟后即可使油管2内的原油形成低粘度的水包油乳状液,此时水包油乳状液还会在抽油井上举升过程中产生混合效果,形成低粘度的油水乳化液,从而达到对井筒内油管2以及套管3与油管2之间环形空间的稠油降粘目的。Example 1, the method of using the viscosity reducer in the construction of heavy oil and super heavy oil viscosity reducer. First add the viscosity reducer to water at 20-50°C; the weight percentage of the viscosity reducer is an aqueous solution of 0.1-1%, and then stir the heated viscosity reducer from the ventricular sucker rod 1 in the medicine tank Input this aqueous solution into the mandrel 7 and agitator 8 in the downhole mixing device at 45-90°C, so that the crude oil mixed with viscosity reducer can be fully stirred. At this time, the ratio of aqueous solution to crude oil is 4:6-1: 9. Stirring by the stirrer 8 at 30-120 rpm, the crude oil in the oil pipe 2 can form a low-viscosity oil-in-water emulsion after 1-3 minutes. At this time, the oil-in-water emulsion will still be pumped The mixing effect is produced during the lifting process of the oil well, forming a low-viscosity oil-water emulsion, so as to achieve the purpose of reducing the viscosity of the heavy oil in the wellbore tubing 2 and the annular space between the casing 3 and the tubing 2.
实施例2,图2使用降粘剂进行低粘度油水乳化液预脱水工艺时,从抽油机17采出的低粘度油水乳化液经管道进入4#油罐15,5#油罐16中,在温度60~65℃状况下自动沉降1~3小时后经系统脱除20%~30%的活性水经管线流入3#水罐14中去,并再次沉降0.5~2小时,此时,予脱污水含油为300~800PPm,其机械杂质含量5000~8000PPm,即能达到满足回掺要求,依靠水位差又将活性水压入1#药罐12中,从而实现管道循环输送与脱水一体化功能,节约了油水乳化液成本及清水资源。Embodiment 2, when Fig. 2 uses the viscosity reducer to carry out the pre-dehydration process of the low-viscosity oil-water emulsion, the low-viscosity oil-water emulsion extracted from the pumping unit 17 enters the 4# oil tank 15 and the 5# oil tank 16 through the pipeline, After automatic settlement at a temperature of 60-65°C for 1-3 hours, 20%-30% of the active water removed by the system flows into the 3# water tank 14 through the pipeline, and settles again for 0.5-2 hours. At this time, give The oil content of the decontaminated sewage is 300-800PPm, and its mechanical impurity content is 5000-8000PPm, which can meet the requirements of back-mixing. Relying on the water level difference, the active water is pressed into the 1# medicine tank 12, so as to realize the integrated function of pipeline circulation transportation and dehydration , saving the cost of oil-water emulsion and water resources.
实施例3,掺降粘剂现场试验数据:掺降粘剂活性水替代井筒电加热技术降粘试验9井次7口井试验参数结果如下:如表: Example 3, field test data of viscosity reducer: mixed with viscosity reducer active water instead of wellbore electric heating technology viscosity reduction test 9 wells and 7 wells The test parameter results are as follows: as shown in the table:
通过采用掺活性水降粘技术,看出几项主要技术参数(包括抽油机上、下行电流井口产出液温度及粘度等),均明显降低,从而较大幅度降低了开采过程中因为油稠而产生的高摩阻,高负荷不利因素,并为低温管道输送创造了很好条件。By adopting the viscosity reduction technology mixed with active water, it can be seen that several main technical parameters (including the temperature and viscosity of the wellhead output fluid of the pumping unit's up and down currents, etc.) have been significantly reduced, thereby greatly reducing the oil viscosity caused by oil viscosity during the production process. The resulting high friction, high load unfavorable factors, and create good conditions for low temperature pipeline transportation.
自动脱出的污水实现了循环再利用目的,进一步降低了开采成本。The automatically detached sewage achieves the purpose of recycling and further reduces the mining cost.
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| CN100363456C (en) * | 2004-11-17 | 2008-01-23 | 中国石油化工股份有限公司 | A thick oil emulsifying viscosity reducer |
| CN101210173A (en) * | 2006-12-28 | 2008-07-02 | 富顺集团控股有限公司 | High-efficiency pour point depressant for thermal oil recovery process |
| CN101235279A (en) * | 2007-02-02 | 2008-08-06 | 富顺集团控股有限公司 | Efficient viscosity reducer for thermal oil recovery process |
| CN100465192C (en) * | 2006-11-09 | 2009-03-04 | 西南石油大学 | Preparation method of molybdenum acetylacetonate cyclodextrin inclusion compound and its application in viscosity reduction of heavy oil |
| CN101921583A (en) * | 2010-08-20 | 2010-12-22 | 中国石油天然气股份有限公司 | Viscosity reducer containing polymer or gel for oil well produced fluid |
| CN101348585B (en) * | 2007-07-18 | 2011-05-25 | 中国石油天然气集团公司 | A drag reducer for oil-water two-phase flow |
| CN101092558B (en) * | 2007-07-20 | 2011-06-22 | 于毅 | Viscosity reducting, de-waxing, deoiling auxiliary agent in use for extracting petroleum, and preparation method |
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| CN102952566A (en) * | 2011-08-18 | 2013-03-06 | 中国石油化工股份有限公司 | Dehydration method of oilfield produced fluid |
| CN101210174B (en) * | 2006-12-28 | 2013-04-24 | 李向东 | Nano oil displacement agent for thermodynamic oil extraction process |
| CN101735115B (en) * | 2008-11-18 | 2013-06-05 | 长江大学 | Salt resistance and calcium resistant deep extra-heavy oil emulsifier and viscosity dropping agent |
| CN106190079A (en) * | 2016-08-10 | 2016-12-07 | 上海亚润能源技术有限公司 | A kind of multi-functional viscous crude inorganic agent and preparation method thereof |
| CN108276510A (en) * | 2018-01-31 | 2018-07-13 | 西安石油大学 | A method of preparing crude Treatment agent using organic glass is discarded |
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| CN100363456C (en) * | 2004-11-17 | 2008-01-23 | 中国石油化工股份有限公司 | A thick oil emulsifying viscosity reducer |
| CN100465192C (en) * | 2006-11-09 | 2009-03-04 | 西南石油大学 | Preparation method of molybdenum acetylacetonate cyclodextrin inclusion compound and its application in viscosity reduction of heavy oil |
| CN101210173B (en) * | 2006-12-28 | 2013-04-24 | 李向东 | Highly effective pour depressant for thermodynamic oil extraction process |
| CN101210173A (en) * | 2006-12-28 | 2008-07-02 | 富顺集团控股有限公司 | High-efficiency pour point depressant for thermal oil recovery process |
| CN101210174B (en) * | 2006-12-28 | 2013-04-24 | 李向东 | Nano oil displacement agent for thermodynamic oil extraction process |
| CN101235279A (en) * | 2007-02-02 | 2008-08-06 | 富顺集团控股有限公司 | Efficient viscosity reducer for thermal oil recovery process |
| CN101235279B (en) * | 2007-02-02 | 2013-04-24 | 李向东 | Highly effective viscosity-reducing agent for thermodynamic oil extraction process |
| CN101348585B (en) * | 2007-07-18 | 2011-05-25 | 中国石油天然气集团公司 | A drag reducer for oil-water two-phase flow |
| CN101092558B (en) * | 2007-07-20 | 2011-06-22 | 于毅 | Viscosity reducting, de-waxing, deoiling auxiliary agent in use for extracting petroleum, and preparation method |
| CN101735115B (en) * | 2008-11-18 | 2013-06-05 | 长江大学 | Salt resistance and calcium resistant deep extra-heavy oil emulsifier and viscosity dropping agent |
| CN102575152A (en) * | 2009-08-26 | 2012-07-11 | 油流技术控股有限公司 | Treatment of Oil |
| CN101921583B (en) * | 2010-08-20 | 2012-12-12 | 中国石油天然气股份有限公司 | Viscosity reducer for oil well production fluid containing polymer or gel |
| CN101921583A (en) * | 2010-08-20 | 2010-12-22 | 中国石油天然气股份有限公司 | Viscosity reducer containing polymer or gel for oil well produced fluid |
| CN102952566B (en) * | 2011-08-18 | 2014-12-31 | 中国石油化工股份有限公司 | Dehydration method of oilfield produced fluid |
| CN102952566A (en) * | 2011-08-18 | 2013-03-06 | 中国石油化工股份有限公司 | Dehydration method of oilfield produced fluid |
| CN106190079A (en) * | 2016-08-10 | 2016-12-07 | 上海亚润能源技术有限公司 | A kind of multi-functional viscous crude inorganic agent and preparation method thereof |
| CN108276510A (en) * | 2018-01-31 | 2018-07-13 | 西安石油大学 | A method of preparing crude Treatment agent using organic glass is discarded |
| CN110272727A (en) * | 2018-03-14 | 2019-09-24 | 中国石油天然气股份有限公司 | Viscosity reducer and preparation method thereof |
| CN108441199A (en) * | 2018-03-23 | 2018-08-24 | 北京捷贝通石油技术股份有限公司 | A kind of environment-friendly highly efficient heavy crude thinner |
| CN110305646A (en) * | 2018-03-27 | 2019-10-08 | 中国石油天然气股份有限公司 | Viscosity reducer and its preparation method and application |
| CN108558154A (en) * | 2018-03-30 | 2018-09-21 | 中石化石油工程技术服务有限公司 | The immediate processing method of oily sludge |
| CN109135703A (en) * | 2018-09-17 | 2019-01-04 | 佛山市禅城区诺高环保科技有限公司 | A kind of preparation method of heavy crude thinner |
| CN118703188A (en) * | 2024-06-13 | 2024-09-27 | 中国石油大学(北京) | A CO2-stimulated crude oil emulsion with long-term stability and rapid demulsification for oil viscosity reduction |
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