An Efficient and Robust Method to Predict Multifractured ......CNOOC Research Institute Co., Ltd., Beijing 100028, China Correspondence should be addressed to Ling Chen; [email protected]
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Research ArticleAn Efficient and Robust Method to Predict MultifracturedHorizontal Well Production in Shale Oil and Gas Reservoirs
Ling Chen , Yuhu Bai, Bingxiang Xu, Yanzun Li, Zhiqiang Dong, and Suran Wang
CNOOC Research Institute Co., Ltd., Beijing 100028, China
Shale oil and gas reservoirs are developed by MFHWs. After large-scale hydraulic fracturing, it is hard to forecast the productionrate using the theoretical method. In the engineering application field, the empirical method of DCA is often used to forecast theproduction rate of shale oil and gas produced by MFHWs. However, there are some problems in using DCA, like how to find outthe proper decline model and switch point of two contiguous flowing periods and how to deal with the unsteady operationcondition which causes a lot of uncertainty in production forecast. In order to solve these problems, firstly, a straight line model,representing the linear flow period in the life cycle of shale oil and gas produced by MFHWs, in the ðQ, lg qÞ coordinate systemis proven to be theoretically proper. Secondly, the duration of the linear flow period is verified to be over 10~15 years by usingan analytical model to do the calculation with the method of Monte Carlo random sampling taking a large amount of parametercombinations of Eagle Ford shale oil and gas reservoirs into calculation. And a field data analysis of Barnett and Eagle Ford alsoshows that the duration of linear flow period can be more than 10~15 years. Thus, a method of production forecast takingadvantage of the straight line feature in the ðQ, lg qÞ coordinate system is raised. After practical use, it is found that the methodis robust and can increase the forecast efficiency and decrease the manual error. Moreover, it can increase the accuracy ofproduction forecast and deal with some unsteady operation conditions. Therefore, this new method has good promotional valuein the engineering field.
1. Introduction
Shale oil and gas reservoirs are developed by MFHWs (shortfor multifractured horizontal wells). After large-scalehydraulic fracturing, a complex fracture network forms inthe reservoir, which makes it difficult to describe the forma-tion of network and study fluid flow law in the reservoir.Therefore, it is hard to forecast the production rate ofMFHWs in shale oil and gas reservoirs using the theoreticalmethod. In the field of engineering application, in most cases,an empirical method of DCA (short for decline curve analy-sis) is used to forecast the production rate of shale oil and gas,because of its advantages in overall forecasting efficiency andaccuracy.
However, there are still some problems in using DCAwhen forecasting the production rate of MFHWs. As in theprocess of shale oil and gas produced by MFHWs, there are
several flowing periods and each flowing period has differentflowing characteristics, which cause it to be difficult to con-duct DCA using a single model with the purpose of achievinghigh accuracy. So the common solution is to use a multistagecombined decline model to increase the adaption of the mul-tiple flowing periods. The first problem is choosing a properdecline model for each flowing period in which strong sub-jectivity often exists. The second problem is deciding theswitch point of two contiguous flowing periods which evenhas no theoretical basis. Obviously, these two problems willbring big uncertainty in the forecast results and constrainthe increasing of forecasting accuracy. The third one is thatusually a DCA is conducted under the condition of steadyflowing pressure. When the operation condition changes,there is no way to deal with it. In order to solve these prob-lems, it is necessary to carry out theoretical research and findthe theoretical base of how to find out the proper decline
HindawiGeofluidsVolume 2021, Article ID 3730322, 11 pageshttps://doi.org/10.1155/2021/3730322
model, how to deal with the uncertain switch point, and howto handle the unsteady operation condition which is oftenmet.
In this paper, a straight line forecast method with a theo-retical basis which can be broadly used in shale oil and gasreservoirs produced byMFHWs is newly raised. By using thismethod, the efficiency and accuracy of production forecastcan be increased and at the same time the applicability ofunsteady operation condition can be increased.
The research result of MFHW production performancein shale oil and gas reservoirs shows that there are mainlythree flowing periods: early-stage transient flow period, linearflow period, and boundary-dominated flow period [1–4].The linear flow period can be subdivided into transient linearflow period and compound linear flow period, and it is themost important flowing period of shale oil and gas produc-tion cycle produced by MFHW [5–9]. After formula manip-ulation of the linear flow model [10–14], it shows that thecumulative production Q has a linear relation to the loga-rithm of production rate q. This characterization on theone hand tells that, in the linear flow period, the productiondecline law matches Arps’ decline law with decline index n= 1; on the other hand, it can take the advantages of thestraight line in ðQ, lg qÞ coordinate system to increase theefficiency and accuracy of the production forecast. An analyt-ical model is used to calculate the time duration of the linearflow period. In this process, the reservoir parameters andfluid PVT parameters are gained from Eagle Ford shale oiland gas reservoirs, and the Monte Carlo random samplingmethod is used to determine a large amount of parametercombinations. Calculation results showed that the time dura-tion of the linear flow period is often over 10~15 years. A fielddata analysis is also used to study the time duration of the lin-ear flow period. After analyzing the production date of Bar-nett shale gas reservoir and Eagle Ford shale oil and gasreservoir, it is found that the duration of linear flow periodusually can be more than 10~15 years. During the productionof shale oil and gas, the initial production rate is very highand the production also decreases very rapidly. Usually, inthe first 3 years, the cumulative production can reach 50%of economic recovery, and in the first 10 years, the cumula-tive production can reach 80% of economic recovery. Whentaking economy into consideration, the production time ofshale oil and gas wells is less than 20 years, which meansthe linear flow period occupies the majority of the productioncycle. So it is reasonable to conduct the production forecastbased on the characterization of linear flow. Field test showsthat the newly raised method has better production forecastaccuracy than the widely used modified hyperbolic Arps’method [15–17], and the average forecast accuracy canachieve about 90%. In addition, the new method also hasthe ability to deal with some unsteady operation conditionswhen flowing pressure rose up or the well resumed produc-ing after a temporary shutting down.
Above all, using the straight line feature in ðQ, lg qÞ coor-dinate system to do the production forecast of shale oil andgas developed by multifractured horizontal well is provedto be a robust method and can increase the forecast efficiencya lot. It has good promotional value in the engineering field.
2. Flowing Period of Shale Oil and GasReservoirs Produced by MultifracturedHorizontal Well
Shale oil and gas reservoirs are developed by multifracturedhorizontal wells. During the production process, firstly, thereservoir fluid will flow into the stimulated region via thetight shale matrix, and then flow into the major fractures,and lastly flow into the wellbore through fracture. Becauseof the big differences in pore structure and permeability ofthese flow media, many researchers consider that there areseveral flowing periods in the shale oil and gas reservoirsdeveloped by MFHWs. The main three flowing periods areearly-stage transient flow period, linear flow period, andboundary-dominated flow period [1–4]. The early-stagetransient flow period is affected by wellbore storage effect,major fracture distribution, and inflow fluid characteristicswhen fracturing, and its duration is very short, which causesit to be hard to analyze. Midterm linear flow period is mainlyaffected by the characteristics of reserve and fluid and theparameters of fracturing transformation, and its duration isrelatively long. The production data of this period is used todo a lot of studies to analyze the fracture parameters ofMFHWs and the permeability of stimulated volume. The lastboundary domain flow period is determined by the well spac-ing of well pattern, the area of well controlled, and matrixpermeability, and the production data of which period ismainly used to analyze the decline law in the end of the pro-duction life cycle.
As linear flow is the most important flowing period, thereare a lot of research achievements of its flowing theory andmodeling. And as the research further develops, the linearflow period can be subdivided into transient linear flowperiod [5, 6] and compound linear flow period [7, 8]. Thetransient linear flow period indicates the flow that occurs inthe stimulated volume, in which the reservoir fluid flows per-pendicularly to the fracture. The compound linear flow addsthe flowing period that the reservoir fluid in the weak stimu-lated volume flows perpendicularly to the strong stimulatedvolume. These phenomena match the traditional theory oftrilinear flow of MFHWs [9], and correspondingly, theenhanced frac region (EFR) model and multifrac composite(MFC) model are built to characterize the compound linearflow [10, 11]. No matter the transient linear flow or the com-pound linear flow, they are both linear flows and share thesame flowing model. The research of linear flow shows thatin the condition of constant flowing pressure which has thesame condition of DCA the reciprocal of production has alinear ordered relation with square root time [12–14] as
1q=m
ffiffit
p+ b: ð1Þ
The production q integration in Equation (1) gains thecumulative production Q as
Q =ðt0qdt =
ðt0
1m
ffiffit
p+ b
dt: ð2Þ
2 Geofluids
Set x =ffiffit
p, and the limit of integration changes to ð0, ffiffi
tp Þ
, so Equation (3) is obtained.
Q =ð ffiffi
tp
0
2xmx + b
dx: ð3Þ
Finally, the definite integration result of Equation (3) is
Q = 2m
ffiffit
p−
bm
ln mffiffit
p+ b
� �+ bm
ln b� �
: ð4Þ
Bring Equation (1) into Equation (4); Equation (5) isobtained.
Q = 2m2
1q− b ln q − b + b ln b
� �: ð5Þ
Usually, in the linear flow period, q≫ 1, so 1/q ≈ 0; then,the simplified form of Equation (5) is obtained.
Q = 2bm2 −ln q − 1 + ln bð Þ: ð6Þ
Equation (6) shows a linear order relation of cumulativeproduction Q and logarithm of production rate q.
3. Decline Law of Shale Oil and Gas in LinearFlow Period
Although the flowing law is complex for MFHWs whendeveloping shale oil and gas reservoirs, by statistical law,the production decline feature matches several decline curvemodels. The first one is the hyperbolic decline model or mod-ified hyperbolic decline model based on Arps’ decline theory[18, 19]; the second one is the Duong model which takes thelong-term linear flow into consideration [20], and the thirdone is the stretched exponential decline model establishedby the principle of statistics and focus boundary dominantflow [21]; and the others are mostly the transformation ofcombination of the former three models. These three basicmodels, on the basis of the modeling hypothesis, have differ-ent range of application individually (Table 1). However, inregard to the problems of how to choose a suitable multiseg-ment model and how to decide the segment point, there are alot of empirical methods raised by many researchers [22, 23].However, no method has a strong theoretical basis, and thedifference between the production forecast results calculatedby different methods may be large or small.
As a matter of experience in field application, the modi-fied hyperbolic decline model based on Arps’ decline theoryis the most widely used. The basic formation of Arps’ declinemodel is
q = q01 + nD0tð Þ1/n : ð7Þ
Set b = 1, and the production q integration in Equation(7) gains the cumulative production Q as
Q =ðt0
q01 +D0t
dt = q0D0
ln 1 +D0tð Þ: ð8Þ
Bring Equation (7) into Equation (8) to eliminate thetime t; Equation (9) showing the relation of cumulative pro-duction Q and production rate q is obtained.
Q = q0D0
ln q0 −q0D0
ln q: ð9Þ
When comparing Equation (9) with Equation (6), thesame format is found, which is the linear order relation ofcumulative production Q and the logarithm of productionrate q. It is recognized that, in the process of shale oil andgas reservoirs developed by MFHWs, the decline law of thelinear flow period matches Arps’ decline law with declineindex n = 1.
4. Validation of the Duration Time ofLinear Flow
4.1. Analytical Model Validation. The time of duration of thelinear flow period can be calculated by the investigation dis-tance equation [12], which is Equation (10). And the dura-tion time equation is the transformation of Equation (10),which is Equation (11).
y = 0:113ffiffiffiffiffiffiffiffiffiffiffiffiffiffikt
ϕμctð Þi
s, ð10Þ
t = y2 ϕμctð Þi0:1132k : ð11Þ
For the compound linear flow, as it shows in Figure 1,there are two different flow regions with different permeabil-ity. The total duration time needs to be calculated separatelyand then added together.
When the fluid flows through the region with the perme-ability of k1, the corresponding duration time t1 is calculatedby
t1 =y21 ϕμctð Þi0:1132k1
: ð12Þ
From Equation (10), the speed of pressure propagationcan be obtained as it shows in
v tð Þ = dy tð Þdt
= 0:113ffiffiffiffiffiffiffiffiffiffiffiffiffiffi
kϕμctð Þi
s1
2ffiffit
p : ð13Þ
When the fluid flows through the region with the perme-ability of k2, the corresponding relation of flowing distanceand duration time is calculated by
As different shale oil and gas reservoirs have differentparameters of reserve, fluid, and fracture, it is hard to makea certain decision of the duration time of compound linearflow. Therefore, the theory of probability is brought intouse. The basic parameter values and their regularity of distri-bution are gained from a typical shale oil and gas field, takingEagle Ford as an example [24–27]. And the Monte Carlo ran-dom sampling method is used to determine a large number ofparameter combinations, with which the distribution ofduration time of compound linear flow can be calculatedand an analysis can be done. The typical shale oil and gasreservoirs’ parameters for calculating the duration time ofcompound linear flow is shown in Table 2.
After 100,000 times of calculation, the outputs are stable.The result show that no matter the reservoir fluid is oil or gas,the time duration of linear flow is very long, and usually, aduration over 10~15 years can be achieved (Figure 2).
4.2. Production Data Validation. Two sets of production datacan also achieve the similar conclusion. Figure 3 shows sev-eral production data from Eagle Ford shale with differentfluid types. What is shown in Figures 3(a) and 3(b) are typicalgas wells that have been in production from 2012 and keptproducing for about 8 years. And what is showed inFigures 3(c) and 3(d) are typical oil wells that have been inproduction from 2013 and kept producing for about 7 years.In the ðQ, lg qÞ coordinate system, they all show a feature ofmatching with a straight line and keep no change.
Table 1: The comparison of the primary decline model.
Name Equation States range of application
Hyperbolic declinemodel
q tð Þ = qi/ 1 + nDitð Þ1/n Decline index n > 1; it is suitable for the production forecast of transientflow period.
Modified hyperbolicdecline model
q tð Þ = qi/ 1 + nDitð Þ1/n, t < t∗
q t∗ð Þe−Dlim t−t∗ð Þ, t > t∗
(The front part is suitable for the transient flow, and the latter half is suitable for
the boundary-dominated flow. The risk is to determine the segment point.
Duong model q tð Þ = q1t−me a/ 1−mð Þð Þ t1−m−1ð Þ It is suitable for the production forecast of linear flow period, and it will
overestimate in the boundary-dominated flow period.
Stretched exponentialmodel
q tð Þ = q0 exp − t/τð Þn½ � It is suitable for the production forecast of boundary-dominated flow period,and it will underestimate the production.
Fracture
y1 y2
k1 k2
k1
k2
k1 k2
Figure 1: Schematic diagram of the compound linear flow model.
Table 2: Parameters for calculation of Eagle Ford.
Fracture distance (ft) 150~300Oil viscosity in reservoir condition 0.5~2Oil reservoir total compressibility 8 × 10−6 ~ 1 × 10−5
Gas viscosity in reservoir condition 0.02~0.05Gas reservoir total compressibility 8 × 10−5 ~ 1 × 10−4
4 Geofluids
Figure 4 shows several production data from Barnettshale with different production times. In Figures 4(a) and4(b), they are two typical wells that have kept producing forabout 12 years. In the ðQ, lg qÞ coordinate system, the featureof straight line appears and keeps no change. In Figures 4(c)and 4(d), they are two typical wells that have kept producingfor about 21 years. In the ðQ, lg qÞ coordinate system, thefeature of straight line appears. One well, like Figure 4(c),keeps straight with no change, but another one, likeFigure 4(d), appears to show a curve in the end.
According to the above analysis, it is proved that in thelinear flow period of shale oil and gas produced by MFHWs,the production decline law matches Arps’ decline law withdecline index n = 1 and the duration time of linear flow canusually last over 10~15 years.
5. Application
During the production of shale oil and gas, the initial produc-tion rate is very high and the production also decreases veryrapidly. Usually, in the first 3 years, the cumulative produc-tion can reach 50% of economic recovery, and in the first10 years, the cumulative production can reach 80% of eco-nomic recovery. When taking economy into consideration,the production time of shale oil and gas wells is less than 20years, which means the linear flow period occupies themajority of the production cycle. Therefore, the productionforecast in 15 years is critically important. According to theresearch conclusion, it is suggested that when doing the pro-duction forecast it is better to use the newly raised ðQ, lg qÞcoordinate system other than the traditional ðt, qÞ coordinate
0
10
20
30
40
50
60
70
80
90
100
0 10 20 30 40 50 60 70 80 90 100
Reve
rse c
umul
ativ
e fre
quen
cy (%
)
Duration time (years)
Duration>15 years10 years<Duration<15 yearsDuration<10 years
(a) Gas EFR model
Duration>15 years10 years<Duration<15 yearsDuration<10 years
Figure 2: Time duration of linear flow of different fluid phases and model.
5Geofluids
system, because if we take the advantages of the straight line,on the one hand, it can increase the efficiency of productionforecast, and on the other hand, it can decrease the manualerror to increase the accuracy of production forecast. In addi-tion, the traditional DCA needs the flowing pressure to besteady, but the new method has the ability to deal with someunsteady flowing pressure cases. The detailed workflowbuilds upon three steps that are described below.
Step 1. Data regulation: get production rate q and cumulativeproduction Q from shale oil/gas production data. Plot therelationship of q and Q in the ðQ, lg qÞ coordinate system.
Step 2.Data fitting: fit the straight line feature in the ðQ, lg qÞcoordinate system and build the linear regression modelwhich should be the form as
lg q = AQ + B: ð16Þ
But if there is no straight line feature, we should go backto use the modified hyperbolic decline model to conduct theproduction forecast.
Step 3.Model transformation: transform Equation (16) to therelationship of q and t, which is usually accepted as the pre-dictive result, shown as
q = 110−B − tc ⋅ A ln 10 : ð17Þ
In Equation (17), tc represents the computing productiontime and it has a transform relationship with the actual pro-duction time t, which is shown in
t = tc − tci + ti: ð18Þ
5.1. Increasing the Accuracy of Production Forecast. There areactual production data of Barnett shale gas, Eagle Ford shalegas, and Eagle Ford shale oil used to make a comparison of
10
100
1000
10000
0 200 400 600 800 1000 1200
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
(a) Typical gas well no. 1
10
100
1000
10000
0 200 400 600 800 1000
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
(b) Typical gas well no. 2
1
10
100
1000
0 20 40 60 80 100
Loga
rithm
oil
rate
(lg
stb/d
)
Cumulative oil (mstb)
oil ratematching straight line
(c) Typical oil well no. 1
10
100
1000
0 50 100 150 200 250
Loga
rithm
oil
rate
(lg
stb/d
)
Cumulative oil (mstb)
oil ratematching straight line
(d) Typical oil well no. 2
Figure 3: Typical production date of Eagle Ford shale.
6 Geofluids
production forecast accuracy between the newly raisedmethod and the widely used modified hyperbolic declinemethod. The absolute forecast percentage error (AFPE) isused as the evaluation method of production forecast accu-racy, whose computing method is shown in
AFPE = 1 −ΔQf
ΔQa − ΔQf
" #× 100%: ð19Þ
Figure 5(a) is the application comparison of the newlyraise method and the widely used modified hyperbolicmethod in Barnett shale gas. The curve fitting of productionhistory is about 2 years, and the extrapolating forecast time isabout 10 years. The results of production forecast are that theaverage accuracy of the newly raised method is 93.9% and theaverage accuracy of the modified hyperbolic method is69.8%. Figure 5(b) is the application comparison of the twomethods in Eagle Ford shale gas. The curve fitting of produc-
tion history is about 2 years, and the extrapolating forecasttime is about 7 years. The results of production forecast arethat the average accuracy of the newly raised method is93.5% and the average accuracy of the modified hyperbolicmethod is 81.0%. Figure 5(c) is the application comparisonof the two methods in Eagle Ford shale oil. The curve fittingof production history is about 2 years, and the extrapolatingforecast time is about 5~7 years. The results of productionforecast are that the average accuracy of the newly raisedmethod is 89.2% and the average accuracy of the modifiedhyperbolicmethod is 79.8%. Overall, the average forecast accu-racy of the newly raised method is about 90%, but the averageforecast accuracy of the widely used modified hyperbolicmethod is about 70%~80%. The reasons are that when thenewly raised method is used, the decline law is certain andthe straight-lined advantage can decrease the manual error.
5.2. Dealing with the Unsteady Operating Condition. In tradi-tional DCA, the operation condition of production wells is
100
1000
10000
100000
0 5000 10000 15000 20000
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
(a) Typical gas well no. 1
100
1000
10000
0 500 1000 1500 2000 2500 3000
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
(b) Typical gas well no. 2
10
100
1000
10000
0 200 400 600 800 1000 1200
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
(c) Typical gas well no. 3
100
1000
10000
100000
0 2000 4000 6000 8000 10000 12000 14000
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
matching curve
gas ratematching straight line
(d) Typical gas well no. 4
Figure 4: Typical production data of Barnett shale.
7Geofluids
0102030405060708090
100
BG 1 BG 2 BG 3 BG 4 BG 5 BG 6
Acc
urac
y of
pro
duct
ion
fore
cast
(%)
Well nameNewly-raised methodModified hyperbolic method
(a) Shale gas of Barnett
Acc
urac
y of
pro
duct
ion
fore
cast
(%)
0102030405060708090
100
EG 1 EG 2 EG 3 EG 4 EG 5 EG 6Well name
Newly-raised methodModified hyperbolic method
(b) Shale gas of Eagle Ford
Acc
urac
y of
pro
duct
ion
fore
cast
(%)
0102030405060708090
100
EO 1 EO 2 EO 3 EO 4 EO 5 EO 6Well name
Newly-raised methodModified hyperbolic method
(c) Shale oil of Eagle Ford
Figure 5: Forecast accuracy comparison of two methods.
10
100
1000
0 100 200 300 400 500 600 700
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
Pressure raise up
gas ratematching straight line
(a) Numerical simulation data
10
100
1000
0 100 200 300 400 500 600 700
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
Pressure raise up
gas ratematching straight line
(b) Actual production data
Figure 6: Production feature of flowing pressure raising up.
8 Geofluids
needed to be stable, which means the flowing pressure usu-ally needs to be steady. However, the reality is stably produc-ing wells are minorities. The unstably producing wells can beclassified into two categories: bottom hole pressure droppingdown and resuming producing after temporarily shuttingdown. Based on this research, we suggest that no matter whatunsteady operating condition is encountered, keep the pro-duction forecast using the last seen straight line feature inthe ðQ, lg qÞ coordinate system, because the changed opera-tion condition cannot change the flowing period. After thechanged operation condition comes into being stable again,the flowing feature of the correspondingly flowing periodappears again, and the last seen feature is the one we shoulduse in production forecast. What are shown below are thespecific methods dealing with each operation condition.
Figure 6(a) shows the numerical simulation of the opera-tion condition that the flowing pressure goes down duringthe production. The straight line in the ðQ, lg qÞ coordinatesystem moves upward parallel. Thus, it is suggested thatwhen doing producing forecast using the newly raisedmethod, the slope of the straight line can be determined byany straight line feature, and the location of the forecaststraight line needs to fit for the last seen straight line, asshown in Figure 6(b).
In Figure 7(a), it shows the numerical simulation of theoperation condition that the well resumes production after atemporary shutting down. The straight line in the ðQ, lg qÞcoordinate system keeps extending from the former one aftera small disturbance. Thus, it is suggested that when doing pro-ducing forecast using the newly raised method, the slope andlocation of the forecast straight should be determined by thefirst straight line feature, as shown in Figure 7(b).
6. Conclusions
With the purpose of increasing the production forecast accu-racy of shale oil and gas reservoirs developed by MFHWs,this paper completed the theory of DCA and raised a more
efficient DCA method to provide a reference for the engi-neering field. The main conclusions of this work are asfollows:
(1) During the life cycle of shale oil and gas reservoirsdeveloped by multifractured horizontal wells, thedecline law of linear flow period matches Arps’decline law with decline index n = 1 and shows astraight line feature in ðQ, lg qÞ coordinate system
(2) During the life cycle of shale oil and gas production,the duration time of linear flow period lasts longand can usually achieve over 10~15 years, taking upthe majority of the life cycle
(3) A new method of production forecast using a ðQ, lgqÞ coordinate system and taking advantages of thefeature of straight line is raised. The newly raisedmethod can increase the accuracy of the productionforecast to about 90%
(4) The newly raised method can also deal with someunsteady operation conditions like flowing pressuredropping down, resuming production after a tempo-rary shutting down, and flowing pressure rising up.Thereby, it can increase the feasibility of DCA inthe engineering field
Nomenclature
q: Oil or gas production rate (mscfd for gas, bbl/d foroil)
m: Slope of linear flow analysis (mscfd-1·d3/2 for gas,bbl-1·d3/2 for oil)
t: Production time (d)b: Intercept of linear flow analysis (mscfd-1 for gas,
bbl-1 for oil)Q: Cumulative production of oil or gas (mscfd for gas,
bbl for oil)
10
100
1000
0 100 200 300 400 500 600
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
gas ratematching straight line
well shut down
(a) Numerical simulation data
gas ratematching straight line
10
100
1000
0 100 200 300 400 500 600
Loga
rithm
gas
rate
(lg
msc
fd)
Cumulative gas (mmscf)
well shut down
(b) Actual production data
Figure 7: Production feature of resuming production after a temporary shutting down.
9Geofluids
q0: Initial oil or gas production rate (mscfd for gas,bbl/d for oil)
D0: Initial decline rate (d-1)n: Decline indexy: Distance of investigation (ft)k: Permeability (md)ϕ: Porosityμ: Viscosity (cP)ct: Total compressibility (psi-1)ðϕμctÞi: The product of porosity, viscosity, and total com-
pressibility (cp·psi-1) in the initial conditionk1: Permeability of the inner space in compound linear
flow (md)k2: Permeability of the outer space in compound linear
flow (md)y1: Distance of inner space in compound linear flow (ft)y2: Distance of outer space in compound linear flow (ft)t1: Time duration of fluid flow through the inner space
in compound linear flow (d)t2: Time duration of the whole compound linear flow
period (d)v: Speed of pressure propagation (ft/d)A: Slope of straight feature in the ðQ, lg qÞ coordinate
systemB: Intercept of straight feature in the ðQ, lg qÞ coordi-
nate systemtc: Computing production time (d)tci: Computing production time at the beginning of
production forecast (d)ti: Actual production time at the beginning of pro-
duction forecast (d)ΔQa: Cumulative production of the predictive period for
the actual production data (mmscf for gas, stb foroil)
ΔQf : Cumulative production of the predictive period forthe forecast production data (mmscf for gas, stb foroil).
Data Availability
The data used to support the findings of this study some areshown within the article, and the others are from LENS data-base of Wood Mackenzie.
Conflicts of Interest
The authors declare that there are no conflicts of interestregarding the publication of this article.
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10 Geofluids
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