# Analysis of Wellhead Uplift in Offshore Thermal Recovery by Using Finite Element Numerical Simulation

Authors: Shexia Dong; Dongsheng Zhuang; Gongming Ji; Chunming Zhu; Ting Sun
Journal: Journal of Engineering
 (2018)

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## Abstract

Pilot test of complex thermal fluid recovery technology was conducted in NB35-2 heavy oil field. Wellhead uplift was detected among some oil wells, and development of offshore thermal recovery technology could be restricted by the serious safety problems behind. This paper is based on the specific operating conditions of one oil well in the trial block, and the simulation calculation of casing elongation and wellhead uplift are conducted by using finite element analysis. The total casing elongation calculated is 4.2 cm, which is consistent with the field test results. According to the research, we concluded that the wellhead uplift is caused by upper casing elongation. 88% of the total elongation happens in the air and seawater sections. Elongation is lesser in strata and the casing string below 360 m can be considered as anchored.


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## Body

## 1. Introduction

Pilot test of complex thermal fluid recovery technology was conducted in Bohai heavy oil filed since 2009 with significant producing progress achieved in NB block and LD block [1–3]. However, wellhead uplift was detected during the pilot test among many thermal injection wells. Based on field measuring, the average wellhead uplift is 4~5 cm with the highest reaching 24.5 cm. As the last firewall for oil well safety, Christmas tree should be paid special attention and protected with all kinds of safety precautions. Possible consequences caused by wellhead uplift are as follows:(1)
Jet of complex thermal fluid wounding people when the weld bead of wellhead pipeline cracks due to over uplifting(2)
Oil and gas leakage caused by casing displacement and cement failure(3)
Casing hanger wrecks inside Christmas tree.This paper presents simulation calculation of wellhead uplift-related casing elongation in the air section, seawater section, and strata section by using finite element analysis. Issues are studied including whether the downhole string elongation is uniform, whether the cement between casings is under destruction, and what is the safety limit for uplift.


## 2. Current Advances

Numerical simulation calculation is a widely applied research method both domestic and overseas in analyzing casing stress and deformation process during thermal injection and production [2–5]. According to the investigation, the numerical study on the stress state and deformation process of casing is less abroad. The finite element method is used to analyze the wellbore, casing, and formation as a whole and to establish the wellbore and formation temperature field calculation model at home. Under ideal conditions, the bearing characteristics are analyzed under the action of uniform internal pressure, uniform ground stress, and temperature load. The method does not consider the casing state of different sections, and the error is larger. Now, domestic application of finite element analysis is operated in steps. First, take wellbore, casings, and strata as an entity and build a temperature calculation model. Then, build a stress field calculation model and analyze the stress status of steam injection string and the casing string in the well. Obtain stress and strain of casing string by deriving stress calculation formats of steam injection string and casing string while operating. Furthermore, based on the ideal conditions of uniform internal pressure, uniform stress, and uniform temperature load, analyze the bearing behavior of the selected study object of casing-cement sheath-strata with plane strain element PLANE183 [4, 5].Although there is a lot of analysis on casing stress, wreck, and precautions for thermal recovery both domestic and overseas, still no integrated solution for wellhead uplift is brought up. Exploratory research on wellbore uplift in offshore thermal recovery is also under its way, most of which bases on the ideal cylinder model without casing coupling. Besides, the uplift calculation is mainly based on free elongation, which cannot accurately simulate the real structure and uplift process of thermal recovery wellbores. Limitations of existing calculation methods are as follows [6–10].(1) Temperature field plays a decisive role in casing elongation and Christmas tree uplift. However, in present calculations for temperature field, seawater’s impact on heat transfer is neglected [11]. In fact, considering the differences between land recovery and offshore recovery, seawater has a major influence on temperature distribution to the three layers of casings.(2) In present domestic research, downhole string is always taken as an entity under uniform load and applied plane strain element [12–15], while, in this paper, 3D finite element model is built for simulation, which is unlike the present model without decoupling and sliding between casings, cement sheath, and strata. By simulating the casing stress and elongation separately in the air section, seawater section, and strata section, the new model makes sure the simulation conditions are more congruous with real work conditions and leads to more accurate results.


## 3. Simulation Methods

### 3.1. Simulation Ideas

(1) Based on completion string structure and offshore casing program of thermal recovery, build a finite element analysis model.(2) Analyze radial and axial temperature distribution to casings under impacts of seawater.(3) Based on string temperature field, simulate casing stress.(4) By calculating elongation of all casings, obtain total wellbore uplift.(5) Conclude regular rules of casing displacement and find the most dangerous surface by confirming the sliding critical point between different casings.


### 3.2. Simulation and Elongation Calculation Methods

String stress is mainly formed by interreaction between thermal field and stress field, so coupling of heat and structure in ANSYS is often applied in concrete analysis. Basic coupling method of heat and structure begins with thermal analysis and continues by loading the analysis results into structure stress analysis directly.(1)
Fill in string structure parameter list, build finite element solid model, and choose thermal analysis unit.(2)
Define property of different materials and apply to each solid.(3)
Conduct mesh generation by using map mesh or sweep mesh.(4)
Conduct Glue operation on contact surfaces.(5)
Define temperature boundary conditions and analyze temperature distribution.(6)
Carry on unit transformation of heat-structure.(7)
Define restrict conditions, import temperature analysis results, and load fluid and strata stress.(8)
Conduct coupling analysis of thermal and structure and analyze the calculation results.


## 3.1. Simulation Ideas

(1) Based on completion string structure and offshore casing program of thermal recovery, build a finite element analysis model.(2) Analyze radial and axial temperature distribution to casings under impacts of seawater.(3) Based on string temperature field, simulate casing stress.(4) By calculating elongation of all casings, obtain total wellbore uplift.(5) Conclude regular rules of casing displacement and find the most dangerous surface by confirming the sliding critical point between different casings.


## 3.2. Simulation and Elongation Calculation Methods

String stress is mainly formed by interreaction between thermal field and stress field, so coupling of heat and structure in ANSYS is often applied in concrete analysis. Basic coupling method of heat and structure begins with thermal analysis and continues by loading the analysis results into structure stress analysis directly.(1)
Fill in string structure parameter list, build finite element solid model, and choose thermal analysis unit.(2)
Define property of different materials and apply to each solid.(3)
Conduct mesh generation by using map mesh or sweep mesh.(4)
Conduct Glue operation on contact surfaces.(5)
Define temperature boundary conditions and analyze temperature distribution.(6)
Carry on unit transformation of heat-structure.(7)
Define restrict conditions, import temperature analysis results, and load fluid and strata stress.(8)
Conduct coupling analysis of thermal and structure and analyze the calculation results.


## 4. Instance Study

### 4.1. Basic Conditions

Well structure instance is shown in Figure1, wellbore structure parameter is shown in Table 1, environment parameter is shown in Table 2, and thermal injection parameter is shown in Table 3.Table 1
Wellbore structure parameter.
String
ID/mm
OD/mm
Depth/m
Ø88.9 mm (3 1/2′′) Insulated tubing
75.997
114.3
—
ø244.475 mm (9 5/8′′) Technical casing
232.49
244.48
1768
Ø339.73 mm (13 3/8′′) Surface casing
327.54
339.73
360
Ø508 mm (20′′) Riser pipe
495.3
508
96.2Table 2
Environmental parameter.
String length in the air/m
39
String length in seawater
12.2
Thermal coefficient of insulated tubing/[W·(m−1·K−1)]
0.02
Thermal coefficient of cement/[W·(m−1·K−1)]
0.35
Thermal coefficient of strata/[W·(m−1·K−1)]
1.743
Temperature coefficient of strata/(m2·s−1)
10~6
Geothermal gratitude/(°C·m−1)
0.03
Air temperature/°C
20
Seawater temperature/°C
15
Wind speed/(m·s−1)
3
Seawater flow speed/(m·s−1)
0.5
—
—Table 3
Thermal injection parameter.
Expense of the air/(kg·h−1)
3000
Injection temperature/°C
270
Expense of diesel oil/(kg·h−1)
200
Injection pressure/MPa
18
Injection rate of hot water/(kg·h−1)
8000
Injection pressure of nitrogen/MPa
18
Injection rate of all thermal fluid/(kg·h−1)
11200
Injection rate of nitrogen/(Nm3·h−1)
500Figure 1
Well structure.Based on present details, the riser pipe is 96.2 m long with 39 m in the air, 12 m in seawater, and 45 m in strata. The surface casing is 360 m long. Since the thermal coefficients of the air, seawater, and strata are much dissimilar which exerts relative big effects on temperature distribution to casings, elongation simulation is separately conducted in the air, seawater, and strata for more accurate results of wellhead uplift.


### 4.2. Calculation of Temperature Distribution

#### 4.2.1. Heat Transfer of Wellbore under Seawater’s Impact

Consider thermal resistance of insulated tubing, annular convection of nitrogen injection, heat transfer resistance of radiation, cement and strata heat resistance in radial direction, and consider impacts of the air, seawater, and strata in axial direction. Obtain total temperature coefficient along wellbore which is shown in Figure2 and heat loss distribution along wellbore which is shown in Figure 3. As seen from the figures, comparatively large heat loss takes place in seawater, is lesser in the air, and is the least in strata.Figure 2
Total thermal coefficient along wellbore.Figure 3
Thermal loss along wellbore.


#### 4.2.2. Temperature Distribution Calculation in Seawater

The complex thermal fluid injected in this well is 270°C and the temperature gratitude is 3°C/100 m. Temperature coefficient of the insulated tubings without insulated couplings is 0.12 W/(m·K). Based on heat transfer calculation, temperature distribution is shown in Table4 including the ø244.475 mm (9 5/8′′) casings, the 1st cement sheath, the ø399.725 mm (13 3/8′′) casings, the 2rd cement sheath, and the ø508 mm (20′′) casings.Table 4
Radial temperature distribution to the completion string.
Depth/m
Fluid temperature/°C
ø244.475 mm (9 5/8′′) casing temperature/°C
Cement boundary temperature/°C
ø399.725 mm (13 3/8′′) casing temperature/°C
Cement sheath boundary temperature/°C
ø508 mm (20′′) pipe temperature/°C
0
270
119.56
82.43
82.43
34.57
34.57
10
269.84
119.5
82.39
82.39
34.56
34.56
20
269.68
119.43
82.35
82.35
34.55
34.55
30
269.51
119.36
82.3
82.3
34.54
34.54
40
269.34
106.13
66.39
66.39
15.18
15.18
50
269.17
106.06
66.36
66.36
15.18
15.18
60
269.02
141.45
109.32
109.32
67.91
67.91
70
268.87
141.53
109.46
109.46
68.12
68.12
80
268.72
141.62
109.6
109.6
68.33
68.33
90
268.58
141.7
109.74
109.74
68.54
68.54
100
268.43
141.79
109.88
109.88
190
267.12
142.54
111.14
111.14
280
265.82
143.29
112.39
112.39
360
264.66
143.96
113.51
113.51


### 4.3. Stress Distribution to All Casings

#### 4.3.1. Meshing

Take Glue operation to simulate the surface bond state of cement and casings. Build a model of riser pipe-surface casing-production casing. The diameter is ø244.475 mm (9 5/8′′) for the production casing, ø399.725 mm (13 3/8′′) for the surface casing, and ø508 mm (20′′) for the riser pipe. Glue the contact surfaces. Choose elementbrick 8 node 70 which is a hexahedron element with 8 nodes. It transfers heat in three dimensions with each node having only one temperature DOF. It is used for 3D heat analysis in both static and momentary state and is able to realize uniform heat current. A solid structure of element brick 8 node 45 can be transferred from this element for relevant structure analysis. Conduct sweep mesh generation, respectively, for each part of the wellbore. Meshing results are shown in Figure 4. Obtain temperature distribution results based on analysis of complex thermal fluid and define temperature boundary conditions for all casings.Figure 4
Sweep meshing of wellbore.


#### 4.3.2. Casing Elongation Simulation

Based on the previous temperature distribution analysis, conduct heat-structure coupled analysis. In order to facilitate the calculation, divide the downhole string into the air and seawater section (0~51.2 m), strata section 1 (51.2~96.2 m), strata section 2 (96.2~360 m), and strata section 3 (360~1710 m). The elongation analysis results of all 4 sections are shown in Figures5~6.Figure 5
Axial casing elongation in the air and seawater section (0~51.2 m).Figure 6
Axial casing elongation in different strata section.
(a)
Axial casing elongation in strata section 1 (51.2~96.2 m)
(b)
Axial casing elongation in strata section 2 (96.2~360 m)
(c)
Axial casing elongation in strata section 3 (360~1710 m)As shown in Figure5, the largest integral axial casing elongation in the air and seawater section (0~51.2 m) is 37.89 mm.As shown in Figure6(a), the largest integral axial casing elongation in strata section 1 (51.2~96.2 m) is 3.55 mm.As shown in Figure6(b), the largest integral axial casing elongation in strata section 2 (96.2~360 m) is 0.368 mm.As shown in Figure6(c), the largest integral axial casing elongation in strata section 3 (360~1710 m) is 0.003 mm, which is almost neglected. The thermal expansion can be considered expansion at an end, so this section is considered to be anchored.From the above simulation, the total string (0~1710 m) elongation is 4.281 cm, which is highly congruous with the field measuring result of wellhead uplift of 4~5 cm during heat injection process.In summary, the elongation of the air water column is about 95% of the total elongation. The elongation of the casing in the stratum is small, and the casing string below 360 m can be regarded as anchor. The analysis shows that the formation has a greater binding force on the casing string, which limits the elongation of the casing string.


## 4.1. Basic Conditions

Well structure instance is shown in Figure1, wellbore structure parameter is shown in Table 1, environment parameter is shown in Table 2, and thermal injection parameter is shown in Table 3.Table 1
Wellbore structure parameter.
String
ID/mm
OD/mm
Depth/m
Ø88.9 mm (3 1/2′′) Insulated tubing
75.997
114.3
—
ø244.475 mm (9 5/8′′) Technical casing
232.49
244.48
1768
Ø339.73 mm (13 3/8′′) Surface casing
327.54
339.73
360
Ø508 mm (20′′) Riser pipe
495.3
508
96.2Table 2
Environmental parameter.
String length in the air/m
39
String length in seawater
12.2
Thermal coefficient of insulated tubing/[W·(m−1·K−1)]
0.02
Thermal coefficient of cement/[W·(m−1·K−1)]
0.35
Thermal coefficient of strata/[W·(m−1·K−1)]
1.743
Temperature coefficient of strata/(m2·s−1)
10~6
Geothermal gratitude/(°C·m−1)
0.03
Air temperature/°C
20
Seawater temperature/°C
15
Wind speed/(m·s−1)
3
Seawater flow speed/(m·s−1)
0.5
—
—Table 3
Thermal injection parameter.
Expense of the air/(kg·h−1)
3000
Injection temperature/°C
270
Expense of diesel oil/(kg·h−1)
200
Injection pressure/MPa
18
Injection rate of hot water/(kg·h−1)
8000
Injection pressure of nitrogen/MPa
18
Injection rate of all thermal fluid/(kg·h−1)
11200
Injection rate of nitrogen/(Nm3·h−1)
500Figure 1
Well structure.Based on present details, the riser pipe is 96.2 m long with 39 m in the air, 12 m in seawater, and 45 m in strata. The surface casing is 360 m long. Since the thermal coefficients of the air, seawater, and strata are much dissimilar which exerts relative big effects on temperature distribution to casings, elongation simulation is separately conducted in the air, seawater, and strata for more accurate results of wellhead uplift.


## 4.2. Calculation of Temperature Distribution

### 4.2.1. Heat Transfer of Wellbore under Seawater’s Impact

Consider thermal resistance of insulated tubing, annular convection of nitrogen injection, heat transfer resistance of radiation, cement and strata heat resistance in radial direction, and consider impacts of the air, seawater, and strata in axial direction. Obtain total temperature coefficient along wellbore which is shown in Figure2 and heat loss distribution along wellbore which is shown in Figure 3. As seen from the figures, comparatively large heat loss takes place in seawater, is lesser in the air, and is the least in strata.Figure 2
Total thermal coefficient along wellbore.Figure 3
Thermal loss along wellbore.


### 4.2.2. Temperature Distribution Calculation in Seawater

The complex thermal fluid injected in this well is 270°C and the temperature gratitude is 3°C/100 m. Temperature coefficient of the insulated tubings without insulated couplings is 0.12 W/(m·K). Based on heat transfer calculation, temperature distribution is shown in Table4 including the ø244.475 mm (9 5/8′′) casings, the 1st cement sheath, the ø399.725 mm (13 3/8′′) casings, the 2rd cement sheath, and the ø508 mm (20′′) casings.Table 4
Radial temperature distribution to the completion string.
Depth/m
Fluid temperature/°C
ø244.475 mm (9 5/8′′) casing temperature/°C
Cement boundary temperature/°C
ø399.725 mm (13 3/8′′) casing temperature/°C
Cement sheath boundary temperature/°C
ø508 mm (20′′) pipe temperature/°C
0
270
119.56
82.43
82.43
34.57
34.57
10
269.84
119.5
82.39
82.39
34.56
34.56
20
269.68
119.43
82.35
82.35
34.55
34.55
30
269.51
119.36
82.3
82.3
34.54
34.54
40
269.34
106.13
66.39
66.39
15.18
15.18
50
269.17
106.06
66.36
66.36
15.18
15.18
60
269.02
141.45
109.32
109.32
67.91
67.91
70
268.87
141.53
109.46
109.46
68.12
68.12
80
268.72
141.62
109.6
109.6
68.33
68.33
90
268.58
141.7
109.74
109.74
68.54
68.54
100
268.43
141.79
109.88
109.88
190
267.12
142.54
111.14
111.14
280
265.82
143.29
112.39
112.39
360
264.66
143.96
113.51
113.51


## 4.2.1. Heat Transfer of Wellbore under Seawater’s Impact

Consider thermal resistance of insulated tubing, annular convection of nitrogen injection, heat transfer resistance of radiation, cement and strata heat resistance in radial direction, and consider impacts of the air, seawater, and strata in axial direction. Obtain total temperature coefficient along wellbore which is shown in Figure2 and heat loss distribution along wellbore which is shown in Figure 3. As seen from the figures, comparatively large heat loss takes place in seawater, is lesser in the air, and is the least in strata.Figure 2
Total thermal coefficient along wellbore.Figure 3
Thermal loss along wellbore.


## 4.2.2. Temperature Distribution Calculation in Seawater

The complex thermal fluid injected in this well is 270°C and the temperature gratitude is 3°C/100 m. Temperature coefficient of the insulated tubings without insulated couplings is 0.12 W/(m·K). Based on heat transfer calculation, temperature distribution is shown in Table4 including the ø244.475 mm (9 5/8′′) casings, the 1st cement sheath, the ø399.725 mm (13 3/8′′) casings, the 2rd cement sheath, and the ø508 mm (20′′) casings.Table 4
Radial temperature distribution to the completion string.
Depth/m
Fluid temperature/°C
ø244.475 mm (9 5/8′′) casing temperature/°C
Cement boundary temperature/°C
ø399.725 mm (13 3/8′′) casing temperature/°C
Cement sheath boundary temperature/°C
ø508 mm (20′′) pipe temperature/°C
0
270
119.56
82.43
82.43
34.57
34.57
10
269.84
119.5
82.39
82.39
34.56
34.56
20
269.68
119.43
82.35
82.35
34.55
34.55
30
269.51
119.36
82.3
82.3
34.54
34.54
40
269.34
106.13
66.39
66.39
15.18
15.18
50
269.17
106.06
66.36
66.36
15.18
15.18
60
269.02
141.45
109.32
109.32
67.91
67.91
70
268.87
141.53
109.46
109.46
68.12
68.12
80
268.72
141.62
109.6
109.6
68.33
68.33
90
268.58
141.7
109.74
109.74
68.54
68.54
100
268.43
141.79
109.88
109.88
190
267.12
142.54
111.14
111.14
280
265.82
143.29
112.39
112.39
360
264.66
143.96
113.51
113.51


## 4.3. Stress Distribution to All Casings

### 4.3.1. Meshing

Take Glue operation to simulate the surface bond state of cement and casings. Build a model of riser pipe-surface casing-production casing. The diameter is ø244.475 mm (9 5/8′′) for the production casing, ø399.725 mm (13 3/8′′) for the surface casing, and ø508 mm (20′′) for the riser pipe. Glue the contact surfaces. Choose elementbrick 8 node 70 which is a hexahedron element with 8 nodes. It transfers heat in three dimensions with each node having only one temperature DOF. It is used for 3D heat analysis in both static and momentary state and is able to realize uniform heat current. A solid structure of element brick 8 node 45 can be transferred from this element for relevant structure analysis. Conduct sweep mesh generation, respectively, for each part of the wellbore. Meshing results are shown in Figure 4. Obtain temperature distribution results based on analysis of complex thermal fluid and define temperature boundary conditions for all casings.Figure 4
Sweep meshing of wellbore.


### 4.3.2. Casing Elongation Simulation

Based on the previous temperature distribution analysis, conduct heat-structure coupled analysis. In order to facilitate the calculation, divide the downhole string into the air and seawater section (0~51.2 m), strata section 1 (51.2~96.2 m), strata section 2 (96.2~360 m), and strata section 3 (360~1710 m). The elongation analysis results of all 4 sections are shown in Figures5~6.Figure 5
Axial casing elongation in the air and seawater section (0~51.2 m).Figure 6
Axial casing elongation in different strata section.
(a)
Axial casing elongation in strata section 1 (51.2~96.2 m)
(b)
Axial casing elongation in strata section 2 (96.2~360 m)
(c)
Axial casing elongation in strata section 3 (360~1710 m)As shown in Figure5, the largest integral axial casing elongation in the air and seawater section (0~51.2 m) is 37.89 mm.As shown in Figure6(a), the largest integral axial casing elongation in strata section 1 (51.2~96.2 m) is 3.55 mm.As shown in Figure6(b), the largest integral axial casing elongation in strata section 2 (96.2~360 m) is 0.368 mm.As shown in Figure6(c), the largest integral axial casing elongation in strata section 3 (360~1710 m) is 0.003 mm, which is almost neglected. The thermal expansion can be considered expansion at an end, so this section is considered to be anchored.From the above simulation, the total string (0~1710 m) elongation is 4.281 cm, which is highly congruous with the field measuring result of wellhead uplift of 4~5 cm during heat injection process.In summary, the elongation of the air water column is about 95% of the total elongation. The elongation of the casing in the stratum is small, and the casing string below 360 m can be regarded as anchor. The analysis shows that the formation has a greater binding force on the casing string, which limits the elongation of the casing string.


## 4.3.1. Meshing

Take Glue operation to simulate the surface bond state of cement and casings. Build a model of riser pipe-surface casing-production casing. The diameter is ø244.475 mm (9 5/8′′) for the production casing, ø399.725 mm (13 3/8′′) for the surface casing, and ø508 mm (20′′) for the riser pipe. Glue the contact surfaces. Choose elementbrick 8 node 70 which is a hexahedron element with 8 nodes. It transfers heat in three dimensions with each node having only one temperature DOF. It is used for 3D heat analysis in both static and momentary state and is able to realize uniform heat current. A solid structure of element brick 8 node 45 can be transferred from this element for relevant structure analysis. Conduct sweep mesh generation, respectively, for each part of the wellbore. Meshing results are shown in Figure 4. Obtain temperature distribution results based on analysis of complex thermal fluid and define temperature boundary conditions for all casings.Figure 4
Sweep meshing of wellbore.


## 4.3.2. Casing Elongation Simulation

Based on the previous temperature distribution analysis, conduct heat-structure coupled analysis. In order to facilitate the calculation, divide the downhole string into the air and seawater section (0~51.2 m), strata section 1 (51.2~96.2 m), strata section 2 (96.2~360 m), and strata section 3 (360~1710 m). The elongation analysis results of all 4 sections are shown in Figures5~6.Figure 5
Axial casing elongation in the air and seawater section (0~51.2 m).Figure 6
Axial casing elongation in different strata section.
(a)
Axial casing elongation in strata section 1 (51.2~96.2 m)
(b)
Axial casing elongation in strata section 2 (96.2~360 m)
(c)
Axial casing elongation in strata section 3 (360~1710 m)As shown in Figure5, the largest integral axial casing elongation in the air and seawater section (0~51.2 m) is 37.89 mm.As shown in Figure6(a), the largest integral axial casing elongation in strata section 1 (51.2~96.2 m) is 3.55 mm.As shown in Figure6(b), the largest integral axial casing elongation in strata section 2 (96.2~360 m) is 0.368 mm.As shown in Figure6(c), the largest integral axial casing elongation in strata section 3 (360~1710 m) is 0.003 mm, which is almost neglected. The thermal expansion can be considered expansion at an end, so this section is considered to be anchored.From the above simulation, the total string (0~1710 m) elongation is 4.281 cm, which is highly congruous with the field measuring result of wellhead uplift of 4~5 cm during heat injection process.In summary, the elongation of the air water column is about 95% of the total elongation. The elongation of the casing in the stratum is small, and the casing string below 360 m can be regarded as anchor. The analysis shows that the formation has a greater binding force on the casing string, which limits the elongation of the casing string.


## 5. Innovation and Conclusions

(1) 3D finite element model is built for simulation, which is unlike the present model without decoupling and sliding between casings, cement sheath, and strata. By simulating the casing stress and elongation separately in the air section, seawater section, and strata section, the new model makes sure the simulation conditions are more congruous with real work conditions and leads to more accurate results.(2) The wellhead uplift is caused by upper casing elongation. 88% of the total elongation happens in the air and seawater sections. Elongation is lesser in strata and the casing string below 360 m can be considered as anchored. It is believed from this research that strata have relative larger binding force to the string which restricts elongation.(3) It is suggested that simulation calculation for more wells should be conducted, and on the same time, simulation tests should be run to further testify conformity between calculation and field measuring. Moreover, by constant modification, it is suggested that wellhead uplift prediction software should be developed to provide guidance for new well thermal injection and by continuously researching on precautions, wellhead uplift will be relieved or diminished and safe thermal recovery will be realized.



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*Source: 2581929-2018-01-02.xml*