CN102183675A - Polyacrylamide aqueous solution fluid ultra low flow velocity measuring method and polyacrylamide aqueous solution viscosity measuring method using same - Google Patents
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Abstract
聚丙烯酰胺水溶液流体的超低流速的测量方法及采用该方法测量聚丙烯酰胺水溶液粘度的方法,属于聚合物参数测量技术领域。它解决了现有技术无法实现对聚丙烯酰胺水溶液超低流速的测量,及无法获取其在地下油田岩芯中的实际流速及粘度的问题。方案一将聚丙烯酰胺水溶液贮池的下端连接玻璃毛细管的入口,玻璃毛细管的出口连接溶液收集瓶,采用显微镜观察玻璃毛细管内的溶液,记录一颗微小颗粒流经玻璃毛细管的观测段所用的时间,计算得到流动速度;方案二在方案一的基础之上,再计算聚丙烯酰胺水溶液流入玻璃毛细管时的入口压力降,最后计算获得聚丙烯酰胺水溶液的粘度。本发明用于测量液体的超低流速及进一步获取超低流速液体的粘度。
A method for measuring the ultra-low flow rate of polyacrylamide aqueous solution fluid and a method for measuring the viscosity of polyacrylamide aqueous solution by using the method belong to the technical field of polymer parameter measurement. It solves the problem that the existing technology cannot realize the measurement of the ultra-low flow rate of the polyacrylamide aqueous solution, and cannot obtain its actual flow rate and viscosity in the underground oil field core. Scheme 1: Connect the lower end of the polyacrylamide aqueous solution reservoir to the inlet of the glass capillary, and connect the outlet of the glass capillary to the solution collection bottle, use a microscope to observe the solution in the glass capillary, and record the time it takes for a tiny particle to flow through the observation section of the glass capillary , to calculate the flow velocity; Scheme 2 is based on Scheme 1, then calculate the inlet pressure drop when the polyacrylamide aqueous solution flows into the glass capillary, and finally calculate the viscosity of the polyacrylamide aqueous solution. The invention is used for measuring the ultra-low flow velocity of the liquid and further obtaining the viscosity of the ultra-low flow velocity liquid.
Description
技术领域technical field
本发明涉及一种聚丙烯酰胺水溶液流体的超低流速的测量方法及采用该方法测量聚丙烯酰胺水溶液粘度的方法,属于聚合物参数测量技术领域。The invention relates to a method for measuring the ultra-low flow rate of polyacrylamide aqueous solution fluid and a method for measuring the viscosity of polyacrylamide aqueous solution by using the method, belonging to the technical field of polymer parameter measurement.
背景技术Background technique
目前在石油开采技术中广泛采用三次采油技术,其中聚合物驱油技术有效的提高了石油的采收率。使用聚合物驱油的油田需要进行油田数值的模拟研究,例如:聚合物的粘度与浓度的关系,聚合物溶液在多孔介质中的流变性和设计参数的优化处理等,其中最重要的参数是聚合物溶液在多孔介质中的粘度。At present, tertiary oil recovery technology is widely used in oil extraction technology, among which polymer flooding technology effectively improves oil recovery. Oilfields that use polymer flooding need to carry out oilfield numerical simulation research, such as: the relationship between the viscosity and concentration of polymers, the rheology of polymer solutions in porous media and the optimization of design parameters, etc. The most important parameters are Viscosity of polymer solutions in porous media.
油田驱油采用的聚合物通常为聚丙烯酰胺水溶液,聚丙烯酰胺水溶液的粘度需要根据流速进行计算获得,聚丙烯酰胺水溶液在地下油田岩芯中的流动速度范围为1-5m/d,即相当于0.012-0.057mm/s,流速非常低。目前使用的对较低液体流速进行测量的仪器是多普勒激光流速计,它测量的流速范围仅为0.1mm/s-1000m/s,这与聚丙烯酰胺水溶液在地下油田岩芯中的实际流速差距非常大,显然无法实现对聚丙烯酰胺水溶液的粘度的获取。The polymer used in oil field flooding is usually polyacrylamide aqueous solution. The viscosity of polyacrylamide aqueous solution needs to be calculated according to the flow velocity. The flow velocity range of polyacrylamide aqueous solution in the underground oilfield core is 1-5m/d, which is equivalent to At 0.012-0.057mm/s, the flow rate is very low. The current instrument used to measure the flow rate of the lower liquid is the Doppler laser current meter, which measures the flow rate range of only 0.1mm/s-1000m/s, which is consistent with the actual polyacrylamide aqueous solution in the core of the underground oil field. The difference in flow rate is very large, and it is obviously impossible to obtain the viscosity of polyacrylamide aqueous solution.
发明内容Contents of the invention
本发明的目的是为了解决现有技术无法实现对聚丙烯酰胺水溶液超低流速的测量,及无法实现其在地下油田岩芯中的实际流速的测量,进而无法获取其粘度的问题,提供一种聚丙烯酰胺水溶液流体的超低流速的测量方法及采用该方法测量聚丙烯酰胺水溶液粘度的方法。The purpose of the present invention is to solve the problem that the existing technology cannot realize the measurement of the ultra-low flow rate of polyacrylamide aqueous solution, and the measurement of its actual flow rate in the underground oil field core, and thus its viscosity cannot be obtained. A method for measuring the ultra-low flow rate of polyacrylamide aqueous solution fluid and a method for measuring the viscosity of polyacrylamide aqueous solution by using the method.
本发明的第一种技术方案为:The first technical scheme of the present invention is:
聚丙烯酰胺水溶液流体的超低流速的测量方法,将聚丙烯酰胺水溶液贮池的下端通过胶管与微米级的玻璃毛细管的入口连接,玻璃毛细管呈水平放置,并且聚丙烯酰胺水溶液贮池的下端高于玻璃毛细管的管中心线;玻璃毛细管的出口连接溶液收集瓶的入口,并且玻璃毛细管和溶液收集瓶放置在恒温箱内;The method of measuring the ultra-low flow rate of the polyacrylamide aqueous solution fluid, the lower end of the polyacrylamide aqueous solution storage tank is connected with the inlet of the micron-sized glass capillary through a rubber tube, the glass capillary is placed horizontally, and the lower end of the polyacrylamide aqueous solution storage tank is high on the tube center line of the glass capillary; the outlet of the glass capillary is connected to the inlet of the solution collection bottle, and the glass capillary and the solution collection bottle are placed in the incubator;
采用显微镜观察玻璃毛细管内的溶液,并在显微镜的视野内选定玻璃毛细管长度为S的一段作为观测段,测量过程为:Use a microscope to observe the solution in the glass capillary, and select a section of the glass capillary whose length is S in the field of view of the microscope as the observation section. The measurement process is:
步骤一:在聚丙烯酰胺水溶液贮池中注入聚丙烯酰胺水溶液;Step 1: Inject the polyacrylamide aqueous solution into the polyacrylamide aqueous solution storage tank;
步骤二:通过显微镜观察玻璃毛细管的观测段,并通过秒表记录聚丙烯酰胺水溶液中的一颗微小颗粒流经观测段所用的时间t,然后计算获得所述微小颗粒的流动速度u:Step 2: Observe the observation section of the glass capillary through a microscope, and record the time t it takes for a tiny particle in the polyacrylamide aqueous solution to flow through the observation section through a stopwatch, and then calculate the flow velocity u of the tiny particle:
u=S/t,u=S/t,
微小颗粒的流动速度u即为聚丙烯酰胺水溶液的流动速度。The flow velocity u of the tiny particles is the flow velocity of the polyacrylamide aqueous solution.
本发明方法的第二种技术方案为:The second technical scheme of the inventive method is:
测量聚丙烯酰胺水溶液粘度的方法,将聚丙烯酰胺水溶液贮池的下端通过胶管同时与微米级的玻璃毛细管的入口和液位计相连通,玻璃毛细管呈水平放置,并且聚丙烯酰胺水溶液贮池的下端高于玻璃毛细管的管中心线,液位计的下端与聚丙烯酰胺水溶液贮池的下端位于同一水平线上,玻璃毛细管的出口连接溶液收集瓶的入口,并且玻璃毛细管和溶液收集瓶放置在恒温箱内;The method of measuring the viscosity of the polyacrylamide aqueous solution is to connect the lower end of the polyacrylamide aqueous solution storage tank with the inlet of the micron-sized glass capillary and the liquid level gauge through the rubber tube, the glass capillary is placed horizontally, and the polyacrylamide aqueous solution storage tank The lower end is higher than the tube center line of the glass capillary, the lower end of the liquid level gauge is on the same level as the lower end of the polyacrylamide aqueous solution storage tank, the outlet of the glass capillary is connected to the inlet of the solution collection bottle, and the glass capillary and the solution collection bottle are placed in a constant temperature inside the box;
采用显微镜观察玻璃毛细管内的溶液,并在显微镜的视野内选定玻璃毛细管长度为S的一段作为观测段,测量过程为:Use a microscope to observe the solution in the glass capillary, and select a section of the glass capillary whose length is S in the field of view of the microscope as the observation section. The measurement process is:
步骤一:在聚丙烯酰胺水溶液贮池中注入聚丙烯酰胺水溶液;Step 1: Inject the polyacrylamide aqueous solution into the polyacrylamide aqueous solution storage tank;
步骤二:通过显微镜观察玻璃毛细管的观测段,并通过秒表记录聚丙烯酰胺水溶液中的一颗微小颗粒流经观测段所用的时间t,然后计算获得所述微小颗粒的流动速度u:Step 2: Observe the observation section of the glass capillary through a microscope, and record the time t it takes for a tiny particle in the polyacrylamide aqueous solution to flow through the observation section through a stopwatch, and then calculate the flow velocity u of the tiny particle:
u=S/t,u=S/t,
微小颗粒的流动速度u即为聚丙烯酰胺水溶液的流动速度;The flow velocity u of the tiny particles is the flow velocity of the polyacrylamide aqueous solution;
步骤三:计算聚丙烯酰胺水溶液流入玻璃毛细管时的入口压力降P;Step 3: Calculate the inlet pressure drop P when the polyacrylamide aqueous solution flows into the glass capillary;
步骤四:计算获得聚丙烯酰胺水溶液的粘度μ。Step 4: Calculate and obtain the viscosity μ of the polyacrylamide aqueous solution.
本发明的优点是:本发明方法采用微米级的玻璃毛细管作为多孔介质物理模型,来模拟井下油田的岩芯,应用常规的物理仪器,将它们组合在一起即实现了聚丙烯酰胺水溶液流体的超低流速的测量,解决了多普勒激光流速计无法测量超低流速的问题。它简单易行,价格低廉,精度高。The advantage of the present invention is that: the method of the present invention adopts micron-sized glass capillary as the physical model of porous medium to simulate the rock core of the downhole oil field, and combines them with conventional physical instruments to realize the ultra-thin polyacrylamide aqueous solution fluid. The measurement of low flow velocity solves the problem that the Doppler laser flow meter cannot measure ultra-low flow velocity. It is simple, easy, inexpensive and highly accurate.
本发明方法通过测量聚丙烯酰胺水溶液中微小颗粒的流速,再计算来获得聚丙烯酰胺水溶液的粘度,实现方法简单,可以达到的测速范围为0.01mm/s-0.1mm/s,精度的估算值为0.5%,能够满足聚丙烯酰胺水溶液在地下油田岩芯中的流动速度的测量需要。The method of the present invention obtains the viscosity of the polyacrylamide aqueous solution by measuring the flow velocity of tiny particles in the polyacrylamide aqueous solution, and then calculating, the realization method is simple, the speed measurement range that can be achieved is 0.01mm/s-0.1mm/s, and the estimated value of the precision is The content is 0.5%, which can meet the requirement of measuring the flow velocity of the polyacrylamide aqueous solution in the core of the underground oil field.
附图说明Description of drawings
图1为实施方式二所述方法的流程图;Fig. 1 is the flowchart of the method described in Embodiment 2;
图2为实施方式二所述方法采用的装置示意图。Fig. 2 is a schematic diagram of the device used in the method described in Embodiment 2.
具体实施方式Detailed ways
具体实施方式一:结合图2说明本实施方式,本实施方式中所述的聚丙烯酰胺水溶液流体的超低流速的测量方法,将聚丙烯酰胺水溶液贮池1的下端通过胶管与微米级的玻璃毛细管2的入口连接,玻璃毛细管2呈水平放置,并且聚丙烯酰胺水溶液贮池1的下端高于玻璃毛细管2的管中心线;玻璃毛细管2的出口连接溶液收集瓶3的入口,并且玻璃毛细管2和溶液收集瓶3放置在恒温箱4内;Specific embodiment one: this embodiment is described in conjunction with Fig. 2, the measuring method of the ultra-low flow rate of polyacrylamide aqueous solution fluid described in this embodiment, the lower end of polyacrylamide aqueous solution reservoir 1 is passed through rubber hose and micron-sized glass The inlet of the capillary 2 is connected, the glass capillary 2 is placed horizontally, and the lower end of the polyacrylamide aqueous solution storage tank 1 is higher than the tube center line of the glass capillary 2; the outlet of the glass capillary 2 is connected to the inlet of the solution collection bottle 3, and the glass capillary 2 Place in the incubator 4 with the solution collection bottle 3;
采用显微镜观察玻璃毛细管2内的溶液,并在显微镜的视野内选定玻璃毛细管2长度为S的一段作为观测段,测量过程为:Use a microscope to observe the solution in the glass capillary 2, and select a section of the glass capillary 2 whose length is S in the field of view of the microscope as the observation section, and the measurement process is:
步骤一:在聚丙烯酰胺水溶液贮池1中注入聚丙烯酰胺水溶液;Step 1: Inject the polyacrylamide aqueous solution into the polyacrylamide aqueous solution storage tank 1;
步骤二:通过显微镜观察玻璃毛细管2的观测段,并通过秒表记录聚丙烯酰胺水溶液中的一颗微小颗粒流经观测段所用的时间t,然后计算获得所述微小颗粒的流动速度u:Step 2: Observe the observation section of the glass capillary 2 through a microscope, and record the time t it takes for a tiny particle in the polyacrylamide aqueous solution to flow through the observation section through a stopwatch, and then calculate the flow velocity u of the tiny particle:
u=S/t,u=S/t,
微小颗粒的流动速度u即为聚丙烯酰胺水溶液的流动速度。The flow velocity u of the tiny particles is the flow velocity of the polyacrylamide aqueous solution.
具体实施方式二:本实施方式为对实施方式一的进一步说明,所述聚丙烯酰胺水溶液中的一颗微小颗粒为处于玻璃毛细管2的管中心处的微小颗粒。其它与实施方式一相同。Embodiment 2: This embodiment is a further description of Embodiment 1. A tiny particle in the polyacrylamide aqueous solution is a tiny particle at the center of the glass capillary 2 . Others are the same as the first embodiment.
玻璃毛细管2的管中心处的微小颗粒的流动速度最快,在众多颗粒中容易找到。The tiny particles at the tube center of the glass capillary 2 have the fastest flow speed and are easy to find among numerous particles.
具体实施方式三:下面结合图1和图2说明本实施方式,Specific embodiment three: the present embodiment is described below in conjunction with Fig. 1 and Fig. 2,
本实施方式中所述的采用实施方式一所述聚丙烯酰胺水溶液流体的超低流速的测量方法测量聚丙烯酰胺水溶液粘度的方法,将聚丙烯酰胺水溶液贮池1的下端通过胶管同时与微米级的玻璃毛细管2的入口和液位计5相连通,玻璃毛细管2呈水平放置,并且聚丙烯酰胺水溶液贮池1的下端高于玻璃毛细管2的管中心线,液位计5的下端与聚丙烯酰胺水溶液贮池1的下端位于同一水平线上,玻璃毛细管2的出口连接溶液收集瓶3的入口,并且玻璃毛细管2和溶液收集瓶3放置在恒温箱4内;The method for measuring the viscosity of the polyacrylamide aqueous solution described in this embodiment using the method for measuring the ultra-low flow rate of the polyacrylamide aqueous solution fluid described in Embodiment 1 is to pass the lower end of the polyacrylamide aqueous solution storage tank 1 through the rubber tube and simultaneously contact with the micron level The inlet of the glass capillary 2 communicates with the liquid level gauge 5, the glass capillary 2 is placed horizontally, and the lower end of the polyacrylamide aqueous solution storage tank 1 is higher than the tube center line of the glass capillary 2, and the lower end of the liquid level gauge 5 is connected to the polypropylene The lower end of the amide aqueous solution reservoir 1 is located on the same horizontal line, the outlet of the glass capillary 2 is connected to the inlet of the solution collection bottle 3, and the glass capillary 2 and the solution collection bottle 3 are placed in the incubator 4;
采用显微镜观察玻璃毛细管2内的溶液,并在显微镜的视野内选定玻璃毛细管2长度为S的一段作为观测段,测量过程为:Use a microscope to observe the solution in the glass capillary 2, and select a section of the glass capillary 2 whose length is S in the field of view of the microscope as the observation section, and the measurement process is:
步骤一:在聚丙烯酰胺水溶液贮池1中注入聚丙烯酰胺水溶液;Step 1: Inject the polyacrylamide aqueous solution into the polyacrylamide aqueous solution storage tank 1;
步骤二:通过显微镜观察玻璃毛细管2的观测段,并通过秒表记录聚丙烯酰胺水溶液中的一颗微小颗粒流经观测段所用的时间t,然后计算获得所述微小颗粒的流动速度u:Step 2: Observe the observation section of the glass capillary 2 through a microscope, and record the time t it takes for a tiny particle in the polyacrylamide aqueous solution to flow through the observation section through a stopwatch, and then calculate the flow velocity u of the tiny particle:
u=S/t,u=S/t,
微小颗粒的流动速度u即为聚丙烯酰胺水溶液的流动速度;The flow velocity u of the tiny particles is the flow velocity of the polyacrylamide aqueous solution;
步骤三:计算聚丙烯酰胺水溶液流入玻璃毛细管2时的入口压力降P;Step 3: Calculate the inlet pressure drop P when the polyacrylamide aqueous solution flows into the glass capillary 2;
步骤四:计算获得聚丙烯酰胺水溶液的粘度μ。Step 4: Calculate and obtain the viscosity μ of the polyacrylamide aqueous solution.
本实施方式中所述的微米级的玻璃毛细管2用于模拟地下油田中的多孔介质,聚丙烯酰胺水溶液贮池1的下端高于玻璃毛细管2的管中心线是为了产生液体压力降,显微镜能够观察玻璃毛细管2中聚丙烯酰胺水溶液中微小颗粒的流动状态。恒温箱4使玻璃毛细管2处于恒温状态,以使玻璃毛细管2内溶液的密度保持稳定。The micron-scale glass capillary 2 described in this embodiment is used to simulate the porous medium in the underground oil field, and the lower end of the polyacrylamide aqueous solution storage tank 1 is higher than the tube centerline of the glass capillary 2 in order to produce liquid pressure drop, and the microscope can Observe the flow state of tiny particles in the polyacrylamide aqueous solution in the glass capillary 2. The incubator 4 keeps the glass capillary 2 in a constant temperature state, so that the density of the solution in the glass capillary 2 remains stable.
工作原理:working principle:
聚丙烯酰胺水溶液贮池1中的聚丙烯酰胺水溶液在液位计5产生的压力降作用下,会在玻璃毛细管2中流动,由于聚丙烯酰胺水溶液中的微小颗粒随着液体一起流动,而微小颗粒可以通过显微镜进行观察,因此将微小颗粒的流动速度做为聚丙烯酰胺水溶液的流动速度。这种方法使粘度μ的获得变得更加简单,易于实现。The polyacrylamide aqueous solution in the polyacrylamide aqueous solution storage tank 1 will flow in the glass capillary 2 under the action of the pressure drop generated by the liquid level gauge 5, because the tiny particles in the polyacrylamide aqueous solution flow together with the liquid, and the tiny The particles can be observed through a microscope, so the flow velocity of the tiny particles is taken as the flow velocity of the polyacrylamide aqueous solution. This method makes the acquisition of viscosity μ easier and easier to implement.
具体实施方式四:本实施方式为对实施方式三的进一步说明,所述聚丙烯酰胺水溶液中的一颗微小颗粒为处于玻璃毛细管2的管中心处的微小颗粒。其它与实施方式三相同。Embodiment 4: This embodiment is a further description of Embodiment 3. A tiny particle in the polyacrylamide aqueous solution is a tiny particle at the center of the glass capillary 2 . Others are the same as the third embodiment.
玻璃毛细管2的管中心处的微小颗粒的流动速度最快,在众多颗粒中容易找到。The tiny particles at the tube center of the glass capillary 2 have the fastest flow speed and are easy to find among numerous particles.
具体实施方式五:本实施方式为对实施方式三或四的进一步说明,Embodiment 5: This embodiment is a further description of Embodiment 3 or 4.
步骤三中所述计算聚丙烯酰胺水溶液流入玻璃毛细管2时的入口压力降P的方法为:The method for calculating the inlet pressure drop P when the polyacrylamide aqueous solution flows into the glass capillary 2 described in step 3 is:
采用测高仪测量获得聚丙烯酰胺水溶液贮池1内的初始液面高度与玻璃毛细管2的管中心线的高度差h,则聚丙烯酰胺水溶液的压力降P为:The height difference h between the initial liquid level height in the polyacrylamide aqueous solution storage tank 1 and the tube centerline of the glass capillary 2 is measured by an altimeter, then the pressure drop P of the polyacrylamide aqueous solution is:
P=ρgh,P = ρgh,
式中ρ为聚丙烯酰胺水溶液的密度、g为重力加速度。In the formula, ρ is the density of the polyacrylamide aqueous solution, and g is the acceleration due to gravity.
其它与实施方式三或四相同。Others are the same as the third or fourth embodiment.
本实施方式中高度差h的获得可以通过液位计5分别测量聚丙烯酰胺水溶液液面的初始高度和玻璃毛细管2的管中心线的高度后,作差获得。In this embodiment, the height difference h can be obtained by measuring the initial height of the liquid level of the polyacrylamide aqueous solution and the height of the centerline of the glass capillary 2 respectively by the liquid level gauge 5 and then making a difference.
具体实施方式六:本实施方式为对实施方式五的进一步说明,Specific implementation mode six: this implementation mode is a further description of implementation mode five,
步骤四中所述计算获得聚丙烯酰胺水溶液的粘度μ的方法为:The method for calculating the viscosity μ of polyacrylamide aqueous solution described in step 4 is:
首先计算聚丙烯酰胺水溶液的剪切速率 First calculate the shear rate of the polyacrylamide aqueous solution
式中d为玻璃毛细管2的内径;In the formula, d is the inner diameter of the glass capillary 2;
然后计算聚丙烯酰胺水溶液的剪切应力τ:Then calculate the shear stress τ of the polyacrylamide aqueous solution:
τ=Pd/4L,τ=Pd/4L,
式中L为玻璃毛细管2的总长度;In the formula, L is the total length of the glass capillary 2;
根据剪切速率和剪切应力τ计算粘度μ:According to the shear rate and the shear stress τ to calculate the viscosity μ:
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JPWO2022065369A1 (en) * | 2020-09-28 | 2022-03-31 |
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CN102818751A (en) * | 2012-08-29 | 2012-12-12 | 河南省交通科学技术研究院有限公司 | Copper mould, tin plate and method for testing flowing value of pavement seam filling adhesive |
CN102818751B (en) * | 2012-08-29 | 2014-04-09 | 河南省交通科学技术研究院有限公司 | Copper mould, tin plate and method for testing flowing value of pavement seam filling adhesive |
CN104865161A (en) * | 2014-06-10 | 2015-08-26 | 中国石油天然气股份有限公司 | Method for measuring liquid viscosity by capillary and device for the method |
JPWO2022065369A1 (en) * | 2020-09-28 | 2022-03-31 | ||
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