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CN111305825B - Gas well pressure dynamic simulation method with variable control reserves - Google Patents

Gas well pressure dynamic simulation method with variable control reserves Download PDF

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CN111305825B
CN111305825B CN202010102700.7A CN202010102700A CN111305825B CN 111305825 B CN111305825 B CN 111305825B CN 202010102700 A CN202010102700 A CN 202010102700A CN 111305825 B CN111305825 B CN 111305825B
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谢良春
陈理捷
史俊花
傅榆森
杨智程
陈伟
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China Petroleum And Natural Gas Co ltd Southwest Oil And Gas Field Branch Chuanzhong Oil And Gas Mine
Chongqing Fanfeng Petroleum Engineering Technology Service Co Ltd
Southwest Petroleum University
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Chongqing Fanfeng Petroleum Engineering Technology Service Co Ltd
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Abstract

本发明公开了一种变控制储量的气井压力动态模拟方法,基于物质平衡原理,通过修正不同控制储量阶段的虚拟原始地层压力、虚拟累积产量,沿用单一固定储量系统的不稳定流动压力计算方式,产生多阶段控制储量变异的单井压力动态,用于跟踪拟合实际的单井生产动态,计算结果表明在变储量交界点上计算压力连续,展现和保持了阶段储量的动态特征,本方法为利用现有的封闭边界气藏单井渗流模型分析变储量系统动态提供了简便方法。

Figure 202010102700

The invention discloses a dynamic simulation method of gas well pressure with variable control reserves. Based on the principle of material balance, by correcting the virtual original formation pressure and virtual cumulative production in different control reserves stages, the unstable flow pressure calculation method of a single fixed reserves system is used. The single-well pressure dynamics with multi-stage controlled reserve variation is generated, which is used to track and fit the actual single-well production performance. The calculation results show that the calculated pressure is continuous at the junction of variable reserves, showing and maintaining the dynamic characteristics of the reserves in stages. This method is as follows: Using the existing single-well seepage model in closed-boundary gas reservoirs provides a convenient method to analyze the dynamics of variable reserve systems.

Figure 202010102700

Description

一种变控制储量的气井压力动态模拟方法A dynamic simulation method of gas well pressure with variable control reserves

技术领域technical field

本发明涉及动态模拟领域,尤其涉及一种用于变控制储量的气井压力动态模拟方法。The invention relates to the field of dynamic simulation, in particular to a dynamic simulation method for gas well pressure for variable control reserves.

背景技术Background technique

传统的单井动态分析例如现代产能递减分析理论模型和解释方法中,均是假设单井的控制储量固定,将流压的下降视为两个组成部分:一是流体向井运移的流动压降,二是能量衰竭的地层压力下降;流动压降与瞬时产量相关,地层压力下降与累积产量相关。In traditional single-well dynamic analysis, such as modern productivity decline analysis theoretical models and interpretation methods, it is assumed that the controlled reserves of a single well are fixed, and the drop of flow pressure is regarded as two components: one is the flow pressure drop of fluid migration to the well. , and the second is the formation pressure drop due to energy depletion; the flow pressure drop is related to the instantaneous production, and the formation pressure drop is related to the cumulative production.

现有技术存在以下缺陷:The prior art has the following defects:

(1)直接开发新的变储量系统渗流数学模型的解析解,需要针对不同井型、不同边界、不同储量段数,分别建立渗流模型进行解析求解,这种方式既复杂又低效,无法利用现有的渗流模型成果,某些问题还难以求解;(1) To directly develop the analytical solution of the seepage mathematical model of the new variable reserve system, it is necessary to establish the seepage model separately for different well types, different boundaries, and different number of reserve sections for analytical solutions. This method is complex and inefficient, and cannot utilize the existing Some seepage model results, some problems are still difficult to solve;

(2)新储量贡献影响,气藏的非均质性导致不同储集体存在一定的启动压差,当压差大于启动压差后,该储集体才开始有贡献,呈现出储量增加趋势;(2) Contribution of new reserves. The heterogeneity of gas reservoirs leads to a certain threshold pressure difference between different reservoirs. When the pressure difference is greater than the threshold pressure difference, the reservoir starts to contribute, showing a trend of increasing reserves;

(3)存在井间干扰影响,在连通性强的系统中新井投产及周边邻井的产量变化,导致气井控制储量变化。(3) There is the influence of inter-well interference. In a system with strong connectivity, the production of new wells and the production changes of adjacent adjacent wells lead to changes in the control reserves of gas wells.

发明内容SUMMARY OF THE INVENTION

本发明的目的在于,针对上述问题,提出一种用于变控制储量的气井压力动态模拟方法。The purpose of the present invention is to provide a dynamic simulation method of gas well pressure for variable control reserves in view of the above problems.

本发明的发明目的是通过以下技术方案实现的:一种用于变控制储量的气井压力动态模拟方法,其特征在于,包括以下步骤:The invention object of the present invention is realized by the following technical scheme: a kind of gas well pressure dynamic simulation method for variable control reserves, is characterized in that, comprises the following steps:

S1:物质平衡状态修正,包括以下步骤:S1: Correction of material balance, including the following steps:

S101:根据总累积产量通过气藏物质平衡方程式迭代计算地层压力,其中,所述的气藏物质平衡方程式为:S101: Iteratively calculate the formation pressure through the gas reservoir material balance equation according to the total cumulative production, wherein the gas reservoir material balance equation is:

Figure BDA0002387405910000021
Figure BDA0002387405910000021

其中,

Figure BDA0002387405910000022
表示累积有效压缩系数,Qp表示总累积产量,G表示控制储量,pi表示原始地层压力,zi表示压力pi下的天然气偏差因子,p表示目前地层压力,z表示压力p下的天然气偏差因子;in,
Figure BDA0002387405910000022
Indicates the cumulative effective compressibility coefficient, Q p represents the total cumulative production, G represents the control reserve, pi represents the original formation pressure, zi represents the natural gas deviation factor at the pressure pi , p represents the current formation pressure, and z represents the natural gas under the pressure p bias factor;

所述的总累积产量为:The total cumulative output described is:

Qp=Gp+WpBw/Bg Q p =G p +W p B w /B g

其中,Gp表示累积产气量,Wp表示累积产水量,Bw表示地层水压力p下的体积系数,Bg表示天然气压力p下的体积系数;Among them, G p represents the cumulative gas production, W p represents the cumulative water production, B w represents the volume factor under formation water pressure p, and B g represents the volume factor under natural gas pressure p;

S102:对比第1阶段结束状态和第2阶段的开始状态,得到第2阶段储量的虚拟总累积产量;S102: Comparing the end state of the first stage with the start state of the second stage, obtain the virtual total cumulative production of the second stage reserves;

第1阶段的结束状态等于第2阶段的开始状态,当第2阶段储量作为孤立系统时,第2阶段开始的虚拟总累积产量

Figure BDA0002387405910000023
产生等效的状态,所述的第1阶段结束的状态方程和第2阶段开始的状态方程为:The end state of stage 1 is equal to the start state of stage 2, and the virtual total cumulative production of the beginning of stage 2 when the reserves of stage 2 act as an isolated system
Figure BDA0002387405910000023
The equivalent state is generated, the state equation at the end of the first stage and the state equation at the beginning of the second stage are:

Figure BDA0002387405910000024
Figure BDA0002387405910000024

Figure BDA0002387405910000025
Figure BDA0002387405910000025

其中,G1表示第1阶段的气藏控制储量,G2表示第2阶段的控制储量,Qp,1表示第1阶段结束时的总累积产量,p1表示第1阶段结束时的地层压力,z1表示压力p1下的天然气偏差因子;Among them, G 1 represents the controlled reserves of the gas reservoir in the first stage, G 2 represents the controlled reserves of the second stage, Q p,1 represents the total cumulative production at the end of the first stage, and p 1 represents the formation pressure at the end of the first stage , z 1 represents the natural gas deviation factor under pressure p 1 ;

其中,G1第1阶段的气藏控制储量,G2表示第2阶段的控制储量,Qp,1表示第1阶段结束时的总累积产量,p1表示第1阶段结束时的地层压力,z1表示压力p1下的天然气偏差因子。Among them, G1 is the controlled reserve of the gas reservoir in the first stage, G2 is the controlled reserve of the second stage, Q p,1 is the total cumulative production at the end of the first stage, p1 is the formation pressure at the end of the first stage, z 1 represents the natural gas bias factor at pressure p 1 .

对比第1阶段结束和第2阶段开始的状态方程式,得到:Comparing the equations of state at the end of stage 1 and the beginning of stage 2, we get:

Figure BDA0002387405910000026
Figure BDA0002387405910000026

即:which is:

Figure BDA0002387405910000031
Figure BDA0002387405910000031

得到第2阶段储量的虚拟总累积产量:To get the virtual total cumulative production of the Phase 2 reserves:

Figure BDA0002387405910000032
Figure BDA0002387405910000032

S103:当气藏的控制储量发生变化时,更新一次新储量系统开始时的气、水的虚拟累积产量,所述的气、水的虚拟累积产量为:S103: When the control reserves of the gas reservoir change, update the virtual cumulative production of gas and water at the beginning of the new reserve system, and the virtual cumulative production of gas and water is:

Figure BDA0002387405910000033
Figure BDA0002387405910000033

Figure BDA0002387405910000034
Figure BDA0002387405910000034

其中,

Figure BDA0002387405910000035
为第2阶段开始的虚拟累积产气量,
Figure BDA0002387405910000036
为第2阶段开始的虚拟累积产水量,Gp,1为第1阶段结束时的真实累积产气量、Wp,1为第1阶段结束时的真实累积产水量;in,
Figure BDA0002387405910000035
is the virtual cumulative gas production at the beginning of the second stage,
Figure BDA0002387405910000036
is the virtual cumulative water production at the beginning of the second stage, G p,1 is the real cumulative gas production at the end of the first stage, and W p,1 is the real cumulative water production at the end of the first stage;

S104:当进入第2阶段后,累积产气量Gp、累积产水量Wp修正为基于虚拟累积产量

Figure BDA0002387405910000037
计算,其中所述的累积产气量和累积产水量为:S104: After entering the second stage, the cumulative gas production Gp and the cumulative water production Wp are corrected to be based on the virtual cumulative production
Figure BDA0002387405910000037
Calculated, where the cumulative gas production and cumulative water production are:

Figure BDA0002387405910000038
Figure BDA0002387405910000038

Figure BDA0002387405910000039
Figure BDA0002387405910000039

其中,qsc(t)表示气产量,qw(t)表示水产量,t1表示第1阶段的结束时间,t表示当前生产时间;Among them, q sc (t) represents the gas production, q w (t) represents the water production, t 1 represents the end time of the first stage, and t represents the current production time;

利用计算所得的修正累积产量Gp、Wp代入总累积产量计算虚拟总累积产量Qp,以第2阶段的控制储量G2为当前储量G,通过气藏物质平衡方程式迭代计算第2阶段的地层压力p随总累积产量的变化,再将压力p转换为气井压力动态计算所需的拟压力ψ形式。Substitute the calculated corrected cumulative production G p , W p into the total cumulative production to calculate the virtual total cumulative production Q p , take the second-stage controlled reserve G 2 as the current reserve G, and iteratively calculate the second stage’s The formation pressure p changes with the total cumulative production, and then the pressure p is converted into the pseudo-pressure ψ form required for the dynamic calculation of the gas well pressure.

S2:阶段初始压力修正:S2: Stage initial pressure correction:

当S103发生时,更新一次阶段的虚拟初始地层压力,将前期的累积产气量在新储量系统中作注入,计算虚拟初始压力的拟压力为:When S103 occurs, the virtual initial formation pressure of the first stage is updated, and the cumulative gas production in the previous period is injected into the new reserve system, and the pseudo pressure for calculating the virtual initial pressure is:

Figure BDA0002387405910000041
Figure BDA0002387405910000041

其中,ψi,2表示新储量系统即第2阶段虚拟初始压力的拟压力,Gp1表示前期即第1阶段终点的累积产气量,ψ1表示前期终点时刻地层压力的拟压力,ct表示系统的综合压缩系数。Among them, ψ i,2 represents the pseudo pressure of the new reserve system, that is, the virtual initial pressure of the second stage, G p1 represents the cumulative gas production in the early stage, that is, the end point of the first stage, ψ 1 represents the pseudo pressure of the formation pressure at the end point of the previous stage, and c t represents the The overall compressibility of the system.

S3:井底压力动态计算:S3: Dynamic calculation of bottom hole pressure:

利用虚拟初始地层压力的拟压力,通过叠加原理计算第2阶段的变流量作用下的井底流压拟压力:Using the pseudo pressure of the virtual initial formation pressure, the bottom hole flow pressure pseudo pressure under the action of the variable flow rate in the second stage is calculated by the superposition principle:

Figure BDA0002387405910000042
Figure BDA0002387405910000042

式中,t为时间,hour;q为流量,m3/d;qj=q(tj),q0=0,q(tj)为流量序列,j=1,2,…,N;PD为含表皮和井储的任意油藏模型的无因次压力解,B为原始压力下的气体体积系数;μ表示原始压力下的气体粘度,mPa.s;k表示储层渗透率,um2;h表示储层厚度,m。In the formula, t is time, hour; q is flow rate, m 3 /d; q j =q(t j ), q 0 =0, q(t j ) is flow sequence, j=1,2,...,N ; P D is the dimensionless pressure solution of any reservoir model with skin and well reservoir, B is the gas volume coefficient at the original pressure; μ is the gas viscosity at the original pressure, mPa.s; k is the reservoir permeability , um 2 ; h represents the thickness of the reservoir, m.

由井底流压拟压力式计算的拟压力ψwf(t)再反变换为井底流压Pwf(t),用于实测压力的动态拟合。控制储量变化超过2段以上时,处理方式与2阶段情况类似。The pseudo pressure ψ wf (t) calculated by the bottom hole flow pressure pseudo pressure formula is then inversely transformed into the bottom hole flow pressure P wf (t), which is used for dynamic fitting of the measured pressure. When the change of the controlled reserves exceeds 2 stages, the treatment method is similar to that of the 2 stage.

本发明的有益效果:本方法利用现有的封闭边界气藏单井渗流模型分析变储量系统动态提供了简便方法。Beneficial effects of the invention: The method provides a convenient method for analyzing the dynamics of a variable reserve system by using the existing single-well seepage model of a closed boundary gas reservoir.

附图说明Description of drawings

图1为本发明的方法流程框图;Fig. 1 is the method flow chart of the present invention;

图2为xc1井压力指数分析曲线图;Fig. 2 is the analysis curve of pressure index of well xc1;

图3为xc1井阶段变储量Blasingame诊断曲线拟合图;Fig. 3 is the fitting diagram of the Blasingame diagnostic curve of variable reserves in well xc1;

图4为xc1井阶段变储量双对数压力拟合曲线图;Fig. 4 is the fitting curve of double logarithmic pressure of variable reserves in well xc1;

图5为xc1井注气产量曲线图;Fig. 5 is the gas injection production curve diagram of well xc1;

图6为xc1井井底流压拟合曲线图;Fig. 6 is the fitting curve of bottom hole flow pressure in xc1 well;

图7为xc1井地层压力预测曲线图。Fig. 7 is the prediction curve of formation pressure of well xc1.

具体实施方式Detailed ways

为了对本发明的技术特征、目的和效果有更加清楚的理解,先对照附图说明本发明的具体实施方式。In order to have a clearer understanding of the technical features, purposes and effects of the present invention, the specific embodiments of the present invention are first described with reference to the accompanying drawings.

一种用于变控制储量的气井压力动态模拟方法,其特征在于,包括以下步骤:A method for dynamic simulation of gas well pressure for variable control reserves, characterized in that it comprises the following steps:

S1:物质平衡状态修正,包括以下步骤:S1: Correction of material balance, including the following steps:

S101:根据总累积产量通过气藏物质平衡方程式迭代计算地层压力,其中,所述的气藏物质平衡方程式为:S101: Iteratively calculate the formation pressure through the gas reservoir material balance equation according to the total cumulative production, wherein the gas reservoir material balance equation is:

Figure BDA0002387405910000051
Figure BDA0002387405910000051

其中,

Figure BDA0002387405910000052
表示累积有效压缩系数,Qp表示总累积产量,G表示控制储量,pi表示原始地层压力,zi表示压力pi下的天然气偏差因子,p表示目前地层压力,z表示压力p下的天然气偏差因子;in,
Figure BDA0002387405910000052
Indicates the cumulative effective compressibility coefficient, Q p represents the total cumulative production, G represents the control reserve, pi represents the original formation pressure, zi represents the natural gas deviation factor at the pressure pi , p represents the current formation pressure, and z represents the natural gas under the pressure p bias factor;

所述的总累积产量为:The total cumulative output described is:

Qp=Gp+WpBw/Bg Q p =G p +W p B w /B g

其中,Gp表示累积产气量,Wp表示累积产水量,Bw表示地层水压力p下的体积系数,Bg表示天然气压力p下的体积系数;Among them, G p represents the cumulative gas production, W p represents the cumulative water production, B w represents the volume factor under formation water pressure p, and B g represents the volume factor under natural gas pressure p;

S102:对比第1阶段的结束状态和第2阶段的开始状态,得到第2阶段储量的虚拟总累积产量;S102: Comparing the end state of the first stage with the start state of the second stage, obtain the virtual total cumulative production of the second stage reserves;

第1阶段的结束状态等于第2阶段的开始状态,当第2阶段储量作为孤立系统时,第2阶段开始的虚拟总累积产量

Figure BDA0002387405910000053
产生等效的状态,所述的第1阶段结束的状态式和第2阶段开始的状态方程为:The end state of stage 1 is equal to the start state of stage 2, and the virtual total cumulative production of the beginning of stage 2 when the reserves of stage 2 act as an isolated system
Figure BDA0002387405910000053
To generate an equivalent state, the state equation at the end of the first stage and the state equation at the beginning of the second stage are:

Figure BDA0002387405910000054
Figure BDA0002387405910000054

Figure BDA0002387405910000055
Figure BDA0002387405910000055

其中,G1表示第1阶段的气藏控制储量,G2表示第2阶段的控制储量,Qp,1表示第1阶段结束时的总累积产量,p1表示第1阶段结束时的地层压力,z1表示压力p1下的天然气偏差因子。Among them, G 1 represents the controlled reserves of the gas reservoir in the first stage, G 2 represents the controlled reserves of the second stage, Q p,1 represents the total cumulative production at the end of the first stage, and p 1 represents the formation pressure at the end of the first stage , z 1 represents the natural gas bias factor at pressure p 1 .

对比第1阶段结束和第2阶段开始的状态方程,得到第2阶段储量的虚拟总累积产量为:Comparing the equations of state at the end of stage 1 and the beginning of stage 2, the virtual total cumulative production of reserves in stage 2 is obtained as:

Figure BDA0002387405910000061
Figure BDA0002387405910000061

S103:当气藏的控制储量发生变化时,更新一次新储量系统开始时的气、水的虚拟累积产量,所述的气、水的虚拟累积产量为:S103: When the control reserves of the gas reservoir change, update the virtual cumulative production of gas and water at the beginning of the new reserve system, and the virtual cumulative production of gas and water is:

Figure BDA0002387405910000062
Figure BDA0002387405910000062

Figure BDA0002387405910000063
Figure BDA0002387405910000063

其中,

Figure BDA0002387405910000064
为第2阶段开始的虚拟累积产气量,
Figure BDA0002387405910000065
为第2阶段开始的虚拟累积产水量,Gp,1为第1阶段结束时的真实累积产气量、Wp,1为第1阶段结束时的真实累积产水量;in,
Figure BDA0002387405910000064
is the virtual cumulative gas production at the beginning of the second stage,
Figure BDA0002387405910000065
is the virtual cumulative water production at the beginning of the second stage, G p,1 is the real cumulative gas production at the end of the first stage, and W p,1 is the real cumulative water production at the end of the first stage;

S104:当进入第2阶段后,累积产气量Gp、累积产水量Wp修正为基于虚拟累积产量

Figure BDA0002387405910000066
计算,其中所述的累积产气量和累积产水量为:S104: After entering the second stage, the cumulative gas production Gp and the cumulative water production Wp are corrected to be based on the virtual cumulative production
Figure BDA0002387405910000066
Calculated, where the cumulative gas production and cumulative water production are:

Figure BDA0002387405910000067
Figure BDA0002387405910000067

Figure BDA0002387405910000068
Figure BDA0002387405910000068

其中,qsc(t)表示气产量,qw(t)表示水产量,t1表示第1阶段的结束时间,t表示当前生产时间。Among them, q sc (t) represents the gas production, q w (t) represents the water production, t 1 represents the end time of the first stage, and t represents the current production time.

利用计算所得的修正累积产量Gp、Wp代入总累积产量计算虚拟总累积产量Qp,以第2阶段的控制储量G2为当前储量G,通过气藏物质平衡方程式迭代计算第2阶段的地层压力p随总累积产量的变化,再将压力p转换为气井压力动态计算所需的拟压力ψ形式。Substitute the calculated corrected cumulative production G p , W p into the total cumulative production to calculate the virtual total cumulative production Q p , take the second-stage controlled reserve G 2 as the current reserve G, and iteratively calculate the second stage’s The formation pressure p changes with the total cumulative production, and then the pressure p is converted into the pseudo-pressure ψ form required for the dynamic calculation of the gas well pressure.

S2:阶段初始压力修正:S2: Stage initial pressure correction:

当S103发生时,更新一次阶段的虚拟初始地层压力,将前期的累积产气量在新储量系统中作注入,计算虚拟初始压力的拟压力为:When S103 occurs, the virtual initial formation pressure of the first stage is updated, and the cumulative gas production in the previous period is injected into the new reserve system, and the pseudo pressure for calculating the virtual initial pressure is:

Figure BDA0002387405910000071
Figure BDA0002387405910000071

其中,ψi,2表示新储量系统即第2阶段虚拟初始压力的拟压力,Gp1表示前期即第1阶段终点的累积产气量,ψ1表示前期终点时刻地层压力的拟压力,ct表示系统的综合压缩系数。Among them, ψ i,2 represents the pseudo pressure of the new reserve system, that is, the virtual initial pressure of the second stage, G p1 represents the cumulative gas production in the early stage, that is, the end point of the first stage, ψ 1 represents the pseudo pressure of the formation pressure at the end point of the previous stage, and c t represents the The overall compressibility of the system.

S3:井底压力动态计算:S3: Dynamic calculation of bottom hole pressure:

利用虚拟初始地层压力的拟压力,通过叠加原理计算第2阶段的变流量作用下的井底流压拟压力:Using the pseudo pressure of the virtual initial formation pressure, the bottom hole flow pressure pseudo pressure under the action of the variable flow rate in the second stage is calculated by the superposition principle:

Figure BDA0002387405910000072
Figure BDA0002387405910000072

式中,t为时间,hour;q为流量,m3/d;qj=q(tj),q0=0,q(tj)为流量序列,j=1,2,…,N;PD为含表皮和井储的任意油藏模型的无因次压力解,B为原始压力下的气体体积系数;μ表示原始压力下的气体粘度,mPa.s;k表示储层渗透率,um2;h表示储层厚度,m。In the formula, t is time, hour; q is flow rate, m 3 /d; q j =q(t j ), q 0 =0, q(t j ) is flow sequence, j=1,2,...,N ; P D is the dimensionless pressure solution of any reservoir model with skin and well reservoir, B is the gas volume coefficient at the original pressure; μ is the gas viscosity at the original pressure, mPa.s; k is the reservoir permeability , um 2 ; h represents the thickness of the reservoir, m.

由井底流压拟压力式计算的拟压力ψwf(t)再反变换为井底流压Pwf(t),用于实测压力的动态拟合。控制储量变化超过2段以上时,处理方式与2阶段情况类似。The pseudo pressure ψ wf (t) calculated by the bottom hole flow pressure pseudo pressure formula is then inversely transformed into the bottom hole flow pressure P wf (t), which is used for dynamic fitting of the measured pressure. When the change of the controlled reserves exceeds 2 stages, the treatment method is similar to that of the 2 stage.

本实施例为一个某储气库气井所提供的分析结果,具体如下:The present embodiment is an analysis result provided by a gas well in a certain gas storage, and the details are as follows:

某储气库气井xc1井在第2轮注气期间表现出变控制储量现象,如图2所示压力指数曲线呈现2段斜率,反映出初期控制储量小、后期控制储量大,阶段控制储量分析结果如表1所示。The gas well xc1 of a gas storage shows the phenomenon of variable controlled reserves during the second round of gas injection. As shown in Figure 2, the pressure index curve presents a 2-stage slope, reflecting that the initial controlled reserves are small and the later controlled reserves are large. The results are shown in Table 1.

表1.xc1井阶段控制储量分析结果Table 1. Analysis results of controlled reserves in Well xc1

Figure BDA0002387405910000073
Figure BDA0002387405910000073

Figure BDA0002387405910000081
Figure BDA0002387405910000081

在2014年8月20日附近发生控制储量变化。变控制储量的定产压降的Blasingame图版拟合曲线如图3、双对数压降图版拟合曲线如图4。根据xc1井的注气产量曲线如图5,计算出井底流压拟合曲线如图6,可见模拟曲线能够较好的跟踪注气压力动态,预测出地层压力变化如图7,在控制储量变化的2014年8月20日附近,计算的流压、地层压力连续,在该日期后的地层压力上升变缓,对应为控制储量增加的现象。A change in controlled reserves occurred around August 20, 2014. The fitting curve of the Blasingame chart for the constant production pressure drop of variable control reserves is shown in Figure 3, and the fitting curve of the double logarithmic pressure drop chart is shown in Figure 4. According to the gas injection production curve of Well xc1 as shown in Figure 5, the bottom hole flow pressure fitting curve is calculated as shown in Figure 6. It can be seen that the simulated curve can better track the gas injection pressure dynamics, and the formation pressure change is predicted as shown in Figure 7. Around August 20, 2014, the calculated flow pressure and formation pressure were continuous, and after this date, the formation pressure increased slowly, which corresponds to the phenomenon of controlled reserves increasing.

本实施例中,具体方法原理分析如下:In this embodiment, the specific method principle is analyzed as follows:

通过修正不同控制储量阶段的虚拟原始地层压力、虚拟累积产量的简化方式,即可保持沿用固定储量系统的不稳定流动压力计算模式;By revising the virtual original formation pressure and virtual cumulative production in different control reserve stages, the unstable flow pressure calculation mode of the fixed reserve system can be maintained;

计算结果表明本案方法在变储量交界点上计算的压力连续,展现和保持了阶段储量的动态特征,可用于跟踪拟合实际的气井生产动态。The calculation results show that the pressure calculated by the method in this case is continuous at the junction of variable reserves, showing and maintaining the dynamic characteristics of the reserves in stages, which can be used to track and fit the actual gas well production performance.

以上显示和描述了本发明的基本原理和主要特征和本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above. Those skilled in the art should understand that the present invention is not limited by the above-mentioned embodiments, and the descriptions in the above-mentioned embodiments and the description are only to illustrate the principle of the present invention. Without departing from the spirit and scope of the present invention, the present invention will have Various changes and modifications fall within the scope of the claimed invention. The claimed scope of the present invention is defined by the appended claims and their equivalents.

Claims (4)

1. A dynamic simulation method for gas well pressure with variable control reserves is characterized by comprising the following steps:
s1: correcting the material balance state, calculating the virtual total accumulated yield by using the corrected accumulated yield, and calculating the formation pressure by using a gas reservoir material balance equation and the current reserve;
s2: correcting the initial pressure of the stage, namely calculating virtual initial pressure pseudo pressure by using the accumulated gas production rate of the 1 st stage end point calculated in the step S1;
s3: and (4) dynamically calculating the bottom hole pressure, namely calculating the bottom hole flow pressure simulated pressure under the variable flow action in the 2 nd stage by using the simulated pressure of the virtual initial pressure obtained in the step S2 and a superposition principle, and then inversely transforming the bottom hole flow pressure into the bottom hole flow pressure.
2. The method for dynamically simulating the pressure of a gas well with variable control reserve as claimed in claim 1, wherein the step S1 specifically comprises the following steps:
s101: and (3) iteratively calculating the formation pressure through a gas reservoir material balance equation according to the total accumulated yield, wherein the gas reservoir material balance equation is as follows:
Figure FDA0003224973860000011
wherein,
Figure FDA0003224973860000012
representing the cumulative effective compression factor, QpRepresenting the total cumulative yield, G representing the control reserve, piRepresenting the original formation pressure, ziDenotes the pressure piA natural gas deviation factor below, p represents the current formation pressure, and z represents the natural gas deviation factor under the pressure p;
the total cumulative yield is:
Qp=Gp+WpBw/Bg
wherein G ispRepresents cumulative gas production, WpIndicating cumulative water production, BwRepresents the volume coefficient under the formation water pressure p, BgRepresents the volume coefficient under the pressure p of the natural gas;
s102: comparing the ending state of the 1 st stage with the starting state of the 2 nd stage to obtain the virtual total accumulated yield of the reserves of the 2 nd stage;
the ending state of stage 1 is equal to the starting state of stage 2, and when the stage 2 reserves are taken as the isolated system, the virtual total cumulative production of stage 2 is started
Figure FDA0003224973860000013
Generating equivalent states, wherein the state equation at the end of the 1 st stage and the state equation at the beginning of the 2 nd stage are as follows:
Figure FDA0003224973860000014
Figure FDA0003224973860000021
wherein G is1Indicating the gas reservoir control reserve, G, of stage 12Indicating the control reserve, Q, of stage 2p,1Denotes the total cumulative yield at the end of stage 1, p1Denotes the formation pressure at the end of phase 1, z1Denotes the pressure p1A natural gas deviation factor of;
comparing the state equations at the end of stage 1 and the beginning of stage 2 to obtain the virtual total cumulative yield of stage 2 reserves as:
Figure FDA0003224973860000022
s103: when the control storage amount of the gas reservoir changes, updating the virtual accumulated yield of the gas and the water when a one-time new storage amount system starts, wherein the virtual accumulated yield of the gas and the water is as follows:
Figure FDA0003224973860000023
Figure FDA0003224973860000024
wherein,
Figure FDA0003224973860000025
for the virtual cumulative gas production beginning at stage 2,
Figure FDA0003224973860000026
for the virtual cumulative water production starting at stage 2, Gp,1Is the true cumulative gas production, W, at the end of stage 1p,1Is the true cumulative water production at the end of stage 1;
s104: after entering stage 2, the gas production is accumulated GpCumulative water production WpModified to be based on virtual cumulative yield
Figure FDA0003224973860000027
Calculating, wherein the cumulative gas production and the cumulative water production are as follows:
Figure FDA0003224973860000028
Figure FDA0003224973860000029
wherein q issc(t) gas production, qw(t) represents the water yield, t1Represents the end time of the 1 st stage, t represents the current production time;
using calculated modificationsPositive cumulative yield Gp、WpCalculating a virtual total cumulative yield Q by substituting the total cumulative yieldpWith control of reserves G in stage 22And (3) iteratively calculating the change of the formation pressure p in the 2 nd stage along with the total accumulated production through a gas reservoir material balance equation for the current reserve G, and converting the formation pressure p into a pseudo pressure psi form required by the dynamic calculation of the gas well pressure.
3. A method for dynamically simulating pressure in a gas well with variable control reserve as claimed in claim 2 wherein step S103 further comprises step S2 of updating the initial virtual formation pressure in a first stage, injecting the previous cumulative gas production into the new reserve system, and calculating the pseudo pressure of the initial virtual pressure as:
Figure FDA0003224973860000031
wherein psii,2Pseudo pressure, G, representing the virtual initial pressure of the new reserve system, phase 2p1Cumulative gas production, # indicating the end of the early, i.e. phase 11Pseudo pressure representing formation pressure at the previous end point, ctRepresenting the overall compression factor of the system.
4. The method for dynamically simulating gas well pressure with variable control reserves according to claim 3, wherein the step S3 specifically comprises:
and calculating the bottom hole flow pressure simulation pressure under the variable flow effect of the 2 nd stage by using the simulation pressure of the virtual initial formation pressure through a superposition principle:
Figure FDA0003224973860000032
wherein t represents time, hour; q represents a flow rate, m3/d;qj=q(tj),q0=0,q(tj) Represents the flow sequence, j ═ 1,2, …, N;PDthe method is a dimensionless pressure solution of any oil reservoir model containing the skin and the well reservoir, and B represents a gas volume coefficient under the original pressure; μ represents the gas viscosity at the original pressure, mpa.s; k denotes reservoir permeability, um2(ii) a h represents reservoir thickness, m;
pseudo pressure psi calculated from bottom hole flowing pressure pseudo pressure formulawf(t) reconversion to bottom hole flow pressure Pwf(t) dynamic fitting of measured pressure; when the control storage amount changes more than 2 sections, the processing mode is similar to the 2-stage condition.
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