考虑变粘酸动态过程的酸压模拟方法Acid fracturing simulation method considering the dynamic process of variable viscosity
技术领域Technical field
本发明涉及压裂领域,具体涉及考虑变粘酸动态过程的酸压模拟方法。The invention relates to the field of fracturing, and in particular to an acid fracturing simulation method considering the dynamic process of variable viscosity.
背景技术Background technique
变粘酸是由斯伦贝谢公司在1997率先合成的一种粘度可变的酸液,用于通过水力压裂、酸化方式进行油气增产的压裂液中,在国外有大量使老油田恢复产能、新油田提高可采储量的成功运用。现有的变粘酸的初始黏度在170
-1的剪切速率下可为30mpa·s左右,随着酸液与地层基质的反应,pH值升高,当pH值升至2左右时,酸液体系的粘度急剧上升,可达到1000mpa·s。之后随着酸岩反应的继续进行,pH值达到4左右时,激发另一化学反应,将残酸的粘度降低到20mpa·s或更低。酸液消耗过程中的高粘状态使得后注入的酸液转入渗透率相对较低的地层,并阻止了孔洞的发育、减缓了活性酸向天然裂缝的滤失,从而实现了均质及深度酸化的目的。而最终残酸粘度的下降,又有利于压裂液或酸液的返排。
Viscosity is a kind of acid with variable viscosity first synthesized by Schlumberger in 1997. It is used in fracturing fluids for increasing oil and gas production through hydraulic fracturing and acidification. There are a large number of foreign oilfields to restore old oilfields. Successful use of production capacity and new oilfields to increase recoverable reserves. The initial viscosity of the existing variable mucous acid can be about 30 mpa·s at a shear rate of 170 -1 . As the acid liquid reacts with the formation matrix, the pH value increases. When the pH value rises to about 2, the acid The viscosity of the liquid system rises sharply and can reach 1000mpa·s. Then as the acid rock reaction continues, when the pH value reaches about 4, another chemical reaction is triggered to reduce the viscosity of the residual acid to 20 mpa·s or lower. The high viscosity during the acid consumption process makes the later injected acid transfer to the formation with relatively low permeability, and prevents the development of pores and slows the loss of active acid to natural fractures, thereby achieving homogeneity and depth The purpose of acidification. The final decrease in the viscosity of the residual acid is conducive to the flowback of fracturing fluid or acid fluid.
在压裂增产领域内,酸液滤失是影响酸压缝长的主要因素之一,滤失速度越小,酸压缝长越长。变粘酸在反应过程中粘度不断发生变化,因而滤失速度也不断发生变化,最终影响酸压裂缝形态。现有的酸压模拟技术是基于常规酸液所得出的,未考虑变粘酸的动态滤失过程,导致变粘酸酸压模拟缝长与实际情况符合率不高。In the field of fracturing stimulation, acid fluid loss is one of the main factors affecting the length of acid fracturing fractures. The smaller the fluid loss rate, the longer the acid fracturing fracture length. The viscosity of variable viscous acid changes continuously during the reaction process, so the fluid loss rate also changes continuously, which ultimately affects the morphology of acid fracturing cracks. The existing acid fracturing simulation technology is based on conventional acid, and does not consider the dynamic fluid loss process of the variable viscous acid, resulting in a low rate of conformity with the actual situation of the simulated seam length of the variable viscous acid fracturing.
发明内容Summary of the invention
本发明的目的在于提供考虑变粘酸动态过程的酸压模拟方法,以解决现有技术中酸压模拟技术未考虑变粘酸的动态滤失过程,导致变粘酸酸压模拟缝长与实际情况符合率不高的问题,实现能够模拟得到考虑变粘酸动态降率后的酸压裂缝形态的目的。The purpose of the present invention is to provide an acid fracturing simulation method that considers the dynamic process of changing viscous acid to solve the problem that the acid fracturing simulation technology in the prior art does not consider the dynamic fluid loss process of changing viscous acid. The problem of the low coincidence rate of the situation can achieve the goal of being able to simulate the acid fracturing fracture morphology after considering the dynamic reduction rate of the variable viscous acid.
本发明通过下述技术方案实现:The present invention is realized through the following technical solutions:
考虑变粘酸动态过程的酸压模拟方法,包括以下步骤:Consider the acid fracturing simulation method of the dynamic process of changing viscosity, including the following steps:
(a)分别测定变粘酸粘度与剪切速率、温度、钙离子浓度、pH值、表活剂浓度关系,建立变粘本构方程;(a) Determine the relationship between the viscosity of variable viscosity and the shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration, and establish the variable viscosity constitutive equation;
(b)模拟变粘酸酸液在裂缝系统中的流动及反应过程,得到裂缝系统内压力剖面;(b) Simulate the flow and reaction process of the variable viscous acid liquid in the fracture system to obtain the pressure profile in the fracture system;
(c)以裂缝系统内压力剖面为内边界条件,地面压力为外边界条件,模拟计算变粘酸在基质中的反应过程;(c) Using the internal pressure profile of the fracture system as the inner boundary condition, and the ground pressure as the outer boundary condition, simulate and calculate the reaction process of variable viscosity in the matrix;
(d)模拟酸液在基质系统中的粘度变化情况,并计算得到滤失速度;(d) Simulate the viscosity change of the acid liquid in the matrix system, and calculate the fluid loss rate;
(e)将得到的滤失速度带入至步骤(b)的裂缝系统内压力剖面。(e) Bring the obtained fluid loss rate to the pressure profile in the fracture system of step (b).
进一步的,所述步骤(a)中变粘本构方程的建立方法包括:Further, the method for establishing the variable viscosity constitutive equation in the step (a) includes:
①实验测定变粘酸在不同剪切速率下的剪切应力,通过线性回归得到变粘酸的流变指数;①Measure the shear stress of mucous acid under different shear rates through experiments, and obtain the rheological index of mucous acid through linear regression;
②实验测定变粘酸在不同pH值下的粘度,拟合得到粘度与pH值的关系;②Experimentally determine the viscosity of variable mucic acid at different pH values, and get the relationship between viscosity and pH value by fitting;
③实验测定变粘酸在不同钙离子浓度下的粘度,拟合得到粘度与钙离子浓度的关系;③Experimentally determine the viscosity of variable mucic acid at different calcium ion concentrations, and fit the relationship between the viscosity and the calcium ion concentration;
④实验测定变粘酸在不同表面活性剂浓度下的粘度,拟合得到粘度与表面活性剂浓度的关系;④Experimentally determine the viscosity of variable mucic acid at different surfactant concentrations, and fit the relationship between the viscosity and the surfactant concentration;
⑤建立受剪切速率、温度、钙离子浓度、pH值、表活剂浓度共同影响的变粘本构方程。⑤Establish a variable viscosity constitutive equation affected by shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration.
进一步的,步骤①中流变指数n的回归公式为:η=Hγ
n-1,其中η为剪切应力,Pa;H为流体粘度,mPa·s;γ为剪切速率,s
-1。
Further, the regression formula of the rheological index n in step ① is: η=Hγ n-1 , where η is the shear stress, Pa; H is the fluid viscosity, mPa·s; γ is the shear rate, s -1 .
步骤②中拟合得到的粘度μ与pH值的关系公式为:μ(pH)=μ
0+μ
max(pH)erf(b·pH+c),其中μ
max为最大黏度,μ
0为初始黏度,mPa·s;pH为体系pH值,无量纲;b、c均为拟合系数,无量纲;
The formula for the relationship between the viscosity μ and the pH value obtained by fitting in step ② is: μ(pH)=μ 0 + μ max (pH)erf(b·pH+c), where μ max is the maximum viscosity, and μ 0 is the initial Viscosity, mPa·s; pH is the system pH value, dimensionless; b and c are fitting coefficients, dimensionless;
步骤③中拟合得到的粘度与钙离子浓度的关系公式为:The formula for the relationship between the viscosity and the calcium ion concentration obtained by fitting in step ③ is:
其中Ca
2+为钙离子浓度,d、e、W
1均为拟合系数;
Among them, Ca 2+ is the concentration of calcium ions, and d, e, and W 1 are all fitting coefficients;
步骤④中拟合得到粘度与表面活性剂浓度的关系公式为:The formula for the relationship between viscosity and surfactant concentration obtained by fitting in step ④ is:
其中,VES表示表面活性剂,f、g、W
2均为拟合系数;
Among them, VES means surfactant, f, g, and W 2 are all fitting coefficients;
步骤⑤所建立的本构方程为:The constitutive equation established in step ⑤ is:
其中,α为与变粘酸性质有关的常数,无量纲;T为地层温度,K;T
0为实验温度,K。
Among them, α is a constant related to the properties of variable viscosity, dimensionless; T is the formation temperature, K; T 0 is the experimental temperature, K.
进一步的,所述步骤(b)中得到的裂缝系统内压力剖面方程为:Further, the pressure profile equation in the fracture system obtained in the step (b) is:
其中,w
a为裂缝宽度,m;v
x、v
y分别为变粘酸在x、y方向的流速,m/s;μ
a为粘度,mPa·s;k为基质渗透率,Md;p为基质压力,MPa;p
e为储层压力,MPa;v
lm为变粘酸在裂缝壁面上不同位置的动态滤失速度,m/s。
Among them, w a is the crack width, m; v x and v y are the flow velocity of the variable viscous acid in the x and y directions, m/s; μ a is the viscosity, mPa·s; k is the matrix permeability, Md; p Is the matrix pressure, MPa; p e is the reservoir pressure, MPa; v lm is the dynamic fluid loss velocity of variable viscous acid at different positions on the fracture wall, m/s.
进一步的,步骤(c)中模拟计算变粘酸在基质中的反应过程包括:计算剪切速率及流场、 计算pH值及酸浓度场、计算钙离子浓度场、计算表面活性剂浓度场、计算温度场、计算酸与岩石反应后的孔隙度场、边界条件及迭代计算。Further, in step (c), the simulation calculation of the reaction process of mucous acid in the matrix includes: calculating the shear rate and flow field, calculating the pH value and the acid concentration field, calculating the calcium ion concentration field, calculating the surfactant concentration field, Calculate the temperature field, calculate the porosity field after the acid reacts with the rock, boundary conditions and iterative calculations.
进一步的,剪切速率及流场通过流动方程计算,所述流动方程包括:Further, the shear rate and the flow field are calculated by the flow equation, and the flow equation includes:
其中K为渗透率,mD;P为压力,MPa;φ为孔隙度,无量纲;t为时间,s;
为梯度算符;
Where K is permeability, mD; P is pressure, MPa; φ is porosity, dimensionless; t is time, s; Is the gradient operator;
pH值及酸浓度场通过酸液浓度方程计算,所述酸液浓度方程包括:The pH value and the acid concentration field are calculated by the acid concentration equation, and the acid concentration equation includes:
其中C
f为酸液在孔隙内部的摩尔浓度,mol/l;D
e为氢离子扩散系数,m
2/s;C
s为酸液在孔隙表面的摩尔浓度mol/l;a
v为孔隙比表面,m
2/m
3;
Where C f is the molar concentration of the acid in the pores, mol/l; De is the hydrogen ion diffusion coefficient, m 2 /s; C s is the molar concentration of the acid on the pore surface, mol/l; a v is the pore ratio Surface, m 2 /m 3 ;
钙离子浓度场通过钙离子平衡方程计算,所述钙离子平衡方程包括:The calcium ion concentration field is calculated by the calcium ion balance equation, and the calcium ion balance equation includes:
表面活性剂浓度场通过表面活性剂平衡方程计算,所述表面活性剂平衡方程包括:The surfactant concentration field is calculated by the surfactant balance equation, and the surfactant balance equation includes:
其中,C
SDVA—表活剂质量浓度,wt%;D
e,SDVA—表活剂的有效扩散系数,m
2/s;
Among them, C SDVA -surface active agent mass concentration, wt%; De, SDVA -surface active agent effective diffusion coefficient, m 2 /s;
温度场通过酸岩反应放热的热传递模型计算,所述酸岩反应放热的热传递模型包括:The temperature field is calculated by the heat transfer model of the acid rock reaction exothermic heat, and the heat transfer model of the acid rock reaction exothermic heat includes:
其中,T
f—酸液温度,K;T
s—岩石温度,K;C
Pf—酸液比热容,J/kg K;C
Ps—岩石比热容, J/kg K;k
ef—酸液导热系数,W/m K;k
es—岩石导热系数,W/m K;h
c—酸液与岩石对流换热系数,W/m
2K;△H
r—反应焓,J/mol;ρ
f—酸液密度;ρ
s—岩石密度;
Among them, T f — acid temperature, K; T s — rock temperature, K; C Pf — acid specific heat capacity, J/kg K; C Ps — rock specific heat capacity, J/kg K; k ef — acid thermal conductivity, W/m K; k es — thermal conductivity of rock, W/m K; h c — convection heat transfer coefficient between acid and rock, W/m 2 K; △H r — reaction enthalpy, J/mol; ρ f — acid Liquid density; ρ s —rock density;
酸与岩石反应后的孔隙度场通过如下公式计算:
The porosity field after the acid reacts with the rock is calculated by the following formula:
进一步的,所述步骤(d)中滤失速度的计算方法为:Further, the calculation method of the filtration rate in the step (d) is:
(1)将步骤(c)中得到的剪切速率、温度、钙离子浓度、pH值、表活剂浓度带入步骤⑤所建立的本构方程中,得到基质系统中的粘度u
eff分布情况;
(1) Bring the shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration obtained in step (c) into the constitutive equation established in step ⑤ to obtain the viscosity u eff distribution in the matrix system ;
(2)将u
eff带入所述流动方程,得到不同位置的酸液流动速度,其中内边界上的流速即是裂缝壁面上的滤失速度。
(2) Bring u eff into the flow equation to obtain the acid flow velocity at different positions, where the flow velocity on the inner boundary is the fluid loss velocity on the fracture wall.
进一步的,所述步骤(e)中,将得到的滤失速度带入至步骤(b)的裂缝系统内压力剖面,直至注酸循环结束。Further, in the step (e), the fluid loss rate obtained is brought into the pressure profile in the fracture system of the step (b) until the acid injection cycle ends.
本发明与现有技术相比,具有如下的优点和有益效果:Compared with the prior art, the present invention has the following advantages and beneficial effects:
本发明考虑变粘酸动态过程的酸压模拟方法,克服了现有技术未考虑变粘酸的动态滤失过程、导致变粘酸酸压模拟缝长与实际情况符合率不高的缺陷,充分考虑了变粘酸与岩石反应的动态过程,通过模拟不同时刻下地层中的剪切速率、温度、钙离子浓度、pH值、表活剂浓度场,从而计算瞬态下的酸液粘度变化情况,并且得到酸液的动态滤失速度,最终模拟得到考虑变粘酸动态降率后的酸压裂缝形态,显著提高了变粘酸酸压模拟时的缝长准确性。The present invention considers the acid fracturing simulation method of the dynamic process of changing viscous acid, overcomes the defect that the prior art does not consider the dynamic fluid loss process of changing viscous acid, which leads to the shortcomings that the length of the simulated seam length of the variable viscous acid fracturing is not high in accordance with the actual situation. Considering the dynamic process of the reaction between variable viscous acid and rock, by simulating the shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration field in the formation at different times to calculate the transient acid viscosity change , And obtain the dynamic fluid loss rate of the acid liquid, and finally simulate the acid fracturing fracture morphology considering the dynamic reduction rate of the variable viscous acid, which significantly improves the accuracy of the fracture length during the simulation of the variable viscous acid fracturing.
附图说明Description of the drawings
此处所说明的附图用来提供对本发明实施例的进一步理解,构成本申请的一部分,并不构成对本发明实施例的限定。在附图中:The drawings described here are used to provide a further understanding of the embodiments of the present invention, constitute a part of the application, and do not constitute a limitation to the embodiments of the present invention. In the attached picture:
图1为本发明具体实施例中剪切速率与剪切应力的关系图;Figure 1 is a graph of the relationship between shear rate and shear stress in a specific embodiment of the present invention;
图2为本发明具体实施例中变粘酸在不同pH值下的粘度示意图;Fig. 2 is a schematic diagram of the viscosity of variable mucic acid at different pH values in a specific embodiment of the present invention;
图3为本发明具体实施例中变粘酸在不同钙离子浓度下的粘度示意图;Figure 3 is a schematic diagram of the viscosity of mucic acid under different calcium ion concentrations in specific embodiments of the present invention;
图4为本发明具体实施例中变粘酸在不同表面活性剂浓度下的粘度示意图;Figure 4 is a schematic diagram of the viscosity of variable mucic acid at different surfactant concentrations in specific embodiments of the present invention;
图5为本发明具体实施例中变粘酸在裂缝系统内的流速剖面示意图;Fig. 5 is a schematic diagram of the flow velocity profile of variable viscous acid in the fracture system in a specific embodiment of the present invention;
图6为本发明具体实施例中变粘酸在裂缝系统内的压力剖面示意图;Fig. 6 is a schematic diagram of the pressure profile of the variable viscosity in the fracture system in a specific embodiment of the present invention;
图7为本发明具体实施例中裂缝系统内酸浓度场示意图;Fig. 7 is a schematic diagram of the acid concentration field in the fracture system in a specific embodiment of the present invention;
图8为本发明具体实施例中裂缝系统内钙离子浓度场示意图;8 is a schematic diagram of the calcium ion concentration field in the fracture system in a specific embodiment of the present invention;
图9为本发明具体实施例中裂缝系统内表面活性剂浓度场示意图;Fig. 9 is a schematic diagram of the surfactant concentration field in the fracture system in a specific embodiment of the present invention;
图10为本发明具体实施例中变粘酸与岩石反应后的孔隙度场示意图;Fig. 10 is a schematic diagram of the porosity field after the reaction of the variable viscous acid with the rock in the specific embodiment of the present invention;
图11为本发明具体实施例中基质系统中的粘度u
eff分布示意图;
Figure 11 is a schematic diagram of the viscosity u eff distribution in the matrix system in a specific embodiment of the present invention;
图12为本发明具体实施例中变粘酸在裂缝壁面上的滤失速度示意图;Fig. 12 is a schematic diagram of the fluid loss rate of variable viscose acid on the crack wall surface in a specific embodiment of the present invention;
图13为本发明具体实施例模拟完成后的裂缝形态图。Fig. 13 is a diagram of the crack morphology after the simulation of the specific embodiment of the present invention is completed.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚明白,下面结合实施例和附图,对本发明作进一步的详细说明,本发明的示意性实施方式及其说明仅用于解释本发明,并不作为对本发明的限定。In order to make the objectives, technical solutions, and advantages of the present invention clearer and clearer, the present invention will be further described in detail below with reference to the embodiments and drawings. The exemplary embodiments and descriptions of the present invention are only used to explain the present invention, not As a limitation of the present invention.
考虑变粘酸动态过程的酸压模拟方法,具体方法如下:Consider the acid fracturing simulation method of the dynamic process of variable viscosity, the specific method is as follows:
(一)、分别测定粘度与剪切速率、温度、钙离子浓度、pH值、表活剂浓度关系,建立变粘本构方程:(1) Determine the relationship between viscosity and shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration respectively, and establish a variable viscosity constitutive equation:
①实验测定变粘酸在不同剪切速率下的剪切应力,实验结果如图1所示,通过线性回归得到变粘酸的流变指数n:σ=4.669·γ
0.449。
①The experimental determination of the shear stress of mucous acid at different shear rates is shown in Figure 1. The rheological index n of mucous acid is obtained by linear regression: σ=4.669·γ 0.449 .
②实验测定变粘酸在不同pH值下的粘度,实验结果如图2所示,通过以下公式拟合得到粘度与pH值的关系公式:②Experimental measurement of the viscosity of variable mucous acid at different pH values. The experimental results are shown in Figure 2. The relationship formula between viscosity and pH value is obtained by fitting the following formula:
μ(pH)=μ
0+μ
max(pH)erf(b·pH+c),其中b—拟合系数,取0.609;c—拟合系数,取0.136。
μ(pH)=μ 0 +μ max (pH)erf(b·pH+c), where b—fitting coefficient, taking 0.609; c—fitting coefficient, taking 0.136.
③实验测定变粘酸在不同钙离子浓度下的粘度,实验结果如图3所示,通过以下公式拟合得到粘度与钙离子浓度的关系公式:③The experiment measures the viscosity of mucic acid under different calcium ion concentrations. The experimental results are shown in Figure 3. The relationship between viscosity and calcium ion concentration is obtained by fitting the following formula:
其中,d—拟合系数,取2.302;e—拟合系数,取15.203;W
1——拟合系数,取18.012。
Among them, d—fitting coefficient, taken as 2.302; e—fitting coefficient, taken as 15.203; W 1 ——fitting coefficient, taken as 18.012.
④实验测定变粘酸在不同表活剂浓度下的粘度,实验结果如图4所示,通过以下公式拟合得到粘度与表活剂浓度的关系公式:④Experimentally determine the viscosity of variable mucous acid at different surfactant concentrations. The experimental results are shown in Figure 4. The relationship formula between viscosity and surfactant concentration is obtained by fitting the following formula:
其中,f—拟合系数,取1.000;g—拟合系数,取6.702;W
2—拟合系数,取4.334。
Among them, f—fitting coefficient, taken as 1.000; g—fitting coefficient, taken as 6.702; W 2 —fitting coefficient, taken as 4.334.
⑤在上述实验结果的基础上,联袂变粘酸在不同环境下的粘度结果,建立受剪切速率、温度、钙离子浓度、pH值、表活剂浓度共同影响的变粘本构方程:⑤On the basis of the above experimental results, the viscosity results of mucous acid in different environments are combined to establish a constitutive equation for variable viscosity that is affected by shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration:
(二)模拟计算酸液在裂缝系统中的流动及反应过程,如图5所示,并计算得到如图6 所示的裂缝系统内压力剖面。(2) Simulate and calculate the flow and reaction process of acid in the fracture system, as shown in Figure 5, and calculate the pressure profile in the fracture system as shown in Figure 6.
(三)以裂缝系统内压力剖面为内边界条件,地面压力为外边界条件,计算转向酸在基质系统中的物理化学反应过程:(3) Taking the internal pressure profile of the fracture system as the inner boundary condition and the ground pressure as the outer boundary condition, calculate the physical and chemical reaction process of the steering acid in the matrix system:
①通过流动方程计算剪切速率及流场,其中流动方程如下:①Calculate the shear rate and flow field through the flow equation, where the flow equation is as follows:
②通过酸液浓度方程计算pH值及酸浓度场,计算结果如图7所示,其中酸液浓度方程如下:
②Calculate the pH value and acid concentration field through the acid concentration equation. The calculation result is shown in Figure 7. The acid concentration equation is as follows:
③钙离子平衡方程计算钙离子浓度场,计算结果如图8所示,其中钙离子平衡方程如下:③Calcium ion balance equation calculates the calcium ion concentration field. The calculation result is shown in Figure 8. The calcium ion balance equation is as follows:
式中C
Ca
2+—钙离子摩尔浓度(mol/l);D
e,Ca
2+—钙离子的有效扩散系数(m2/s)。
In the formula, C Ca 2+-the molar concentration of calcium ions (mol/l); De, Ca 2+-the effective diffusion coefficient of calcium ions (m2/s).
④通过表面活性剂平衡方程计算表面活性剂浓度场,计算结果如图9所示,其中表面活性剂平衡方程如下:④Calculate the surfactant concentration field by the surfactant balance equation. The calculation result is shown in Figure 9. The surfactant balance equation is as follows:
C
SDVA—表活剂质量浓度,wt%;D
e,SDVA—表活剂的有效扩散系数,m
2/s。
C SDVA —mass concentration of surfactant, wt%; De, SDVA —effective diffusion coefficient of surfactant, m 2 /s.
⑤考虑酸岩反应放热的热传递模型计算温度场。所述酸岩反应放热的热传递模型包括:⑤Calculate the temperature field with the heat transfer model considering the heat released by the acid rock reaction. The heat transfer model of the acid rock reaction exothermic heat includes:
其中,T
f—酸液温度,K;T
s—岩石温度,K;C
Pf—酸液比热容,J/kg K;C
Ps—岩石比热容,J/kg K;k
ef—酸液导热系数,W/m K;k
es—岩石导热系数,W/m K;h
c—酸液与岩石对流换热系数,W/m
2K;△H
r—反应焓,J/mol;ρ
f—酸液密度;ρ
s—岩石密度;
Among them, T f — acid temperature, K; T s — rock temperature, K; C Pf — acid specific heat capacity, J/kg K; C Ps — rock specific heat capacity, J/kg K; k ef — acid thermal conductivity, W/m K; k es — thermal conductivity of rock, W/m K; h c — convection heat transfer coefficient between acid and rock, W/m 2 K; △H r — reaction enthalpy, J/mol; ρ f — acid Liquid density; ρ s —rock density;
⑥计算酸与岩石反应后的孔隙度场,计算结果如图10所示。⑥Calculate the porosity field after the acid reacts with the rock. The calculation result is shown in Figure 10.
⑦边界条件(以裂缝系统内压力剖面为内边解条件,地面压力为外边界条件,等等)及迭代计算步骤,均为现有技术,在此不做赘述。⑦The boundary conditions (using the internal pressure profile of the fracture system as the internal solution condition, the ground pressure as the external boundary condition, etc.) and the iterative calculation steps are all existing technologies and will not be repeated here.
(四)、模拟酸液在基质系统中的粘度变化情况,并计算得到滤失速度:(4) Simulate the viscosity change of the acid liquid in the matrix system, and calculate the fluid loss rate:
将上述步骤(三)中得到的剪切速率、温度、钙离子浓度、pH值、表活剂浓度带入步骤(一)中第⑤小步,计算得到基质系统中的粘度分布情况u
eff。
Bring the shear rate, temperature, calcium ion concentration, pH value, and surfactant concentration obtained in step (3) into step ⑤ in step (1), and calculate the viscosity distribution u eff in the matrix system.
再将u
eff带入步骤(三)的流动方程中,得到不同位置的酸液流动速度,其中内边界上的流速即是如图12所示的裂缝壁面上的滤失速度。
Then bring u eff into the flow equation of step (3) to obtain the acid flow velocity at different positions, where the flow velocity on the inner boundary is the fluid loss velocity on the crack wall as shown in FIG. 12.
(五)将滤失速度带入第二步,循环结束,直至注酸结束,得到的模拟结束后的裂缝形态如图13所示。(5) Bring the fluid loss rate into the second step, and the cycle ends until the end of acid injection. The fracture morphology obtained after the simulation is completed is shown in Figure 13.
以上所述的具体实施方式,对本发明的目的、技术方案和有益效果进行了进一步详细说明,所应理解的是,以上所述仅为本发明的具体实施方式而已,并不用于限定本发明的保护范围,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The specific embodiments described above further describe the purpose, technical solutions and beneficial effects of the present invention in detail. It should be understood that the above are only specific embodiments of the present invention, and are not intended to limit the scope of the present invention. The protection scope, any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included in the protection scope of the present invention.