Jiaming Zhang*ab,
Xiaodong Wua,
Zhangxin Chenb,
Guoqing Hana,
Jingyao Wangc,
Zongxiao Rena and
Kai Zhangb
aMOE Key Laboratory of Petroleum Engineering, China University of Petroleum, Beijing 102249, China. E-mail: jiaming.zhang@ucalgary.ca; Tel: +86-10-89734338
bDepartment of Chemical & Petroleum Engineering, University of Calgary, Calgary T2N 1N4, Canada
cPetroChina Exploration and Development Research Institute, Beijing 100083, China
First published on 27th August 2015
Formation damage is a serious problem in oil and gas industries. Based on common reservoir damage, the conditions and factors resulting in damage were summarized into four categories in this paper. The worldwide advanced technologies applied in reservoir damage treatment are reviewed. For the first time, we propose the concept of injecting nitrogen foam into a formation to treat the damage caused by sand blocking. An application of Cyclic Foam Stimulation is introduced, which enhances productivity significantly. Experimental apparatus for the Cyclic Foam Stimulation was designed, which included a wellbore vessel that could stimulate the effect of sand setting. A reservoir vessel was also designed to supply the foam. Additionally, in order to simulate the formation damage caused by the size and distribution of fine sand, six artificial cores, which were porosity contrastive and sand producing, were prepared based on the technologies of pressure control and PVA membrane wrapping. The experimental results show that the foam has a good discharging effect on sand blockages. Moreover, the effects of the size and distribution of the fine sand on the porosity was studied. It was found that the smaller the size of the grains and the more uniform the grain distribution, the worse the formation porosity. A porosity recovery factor has been defined and the recovery rate of the porosity was also studied. A scientific guide for the application of Cyclic Foam Stimulation can be generated from the studies in this paper.
A lot of effort has been devoted to finding effective ways of treating formation damage. Traditional formation damage repairing methods include matrix stimulation and hydraulic fracturing, which have shown some success in field applications. However, they also come with many limitations. The fluids (usually acid) used in matrix stimulation can cause equipment/tubing corrosion, resulting in secondary reservoir damage, as well as the pollution of the environment. Hydraulic fracturing construction costs huge amounts of time and capital. In addition, these two methods have specific usage requirements, which limit their applications. Furthermore, they are not easily applied to horizontal wells, especially matrix stimulation.5
Foam is used to enhance oil recovery in oil and gas fields.6 The foam used must pass a stability test before the qualified foam can be used as a method to enhance oil recovery.7–10 By reducing the mobility of gas and steam, nitrogen foam flooding and thermal foam flooding respectively, are used in traditional oil reservoirs and heavy oil reservoirs.11,12 Foam can reduce bottom water coning in thin reservoirs by the use of negative pressure near the wellbore, which is called foam inhibited anti-water coning technology.13 Nitrogen foam mud drilling can be used to reduce fluid column pressure in a wellbore, improve the drilling speed and reduce the pollution of a reservoir.14 Foam flooding is one of the effective ways to improve oil recovery after water flooding, test results and practical applications have proved the method to be very effective.15,16 In this paper, a foam method is used to treat the reservoir damage caused by sand plugging.
Nitrogen foam is a complicated system and a structured fluid. Bubbles with different sizes, which are separated by lamellae, form a foam fluid with a special structure. Under the shearing action, a foam can deform, collapse, coalesce and regenerate, which can eventually lead to the complications of foam transport and blocking in porous media.17 Therefore, an experimental study on the effects of Cyclic Foam Stimulation is required.
Experimental apparatus for Cyclic Foam Stimulation was designed, which includes a wellbore vessel that can simulate the effect of sand setting. A reservoir vessel was also designed to supply the foam. Six artificial cores, which were porosity contrastive and sand producing, were prepared based on the technologies of pressure control and PVA membrane wrapping, in order to simulate formation damage caused by the size and distribution of fine sand. The results from the Cyclic Foam Stimulation experiments show that foam has a good remedying effect on sand blocking. In addition, the effects of the size and distribution of fine sand on the formation porosity were studied. A scientific guide for the application of Cyclic Foam Stimulation can be generated from the studies in this paper.
The conditions and factors affecting formation damage can be divided into four categories:1
(1) The type, shape and location of the original mineral, such as: the reservoir fluid and the characteristics of the matrix.
(2) The composition of the original and external fluids: the invasion of external fluid, such as water chemicals used to improve oil recovery, drilled mud invasion and workover fluid.
(3) The temperature, pressure and characteristics of the original reservoir, such as: the production system, well production, wellbore pressure and temperature changes.
(4) The development practices of the well and reservoir, such as: the processes of drilling and completion, and all kinds of processes for EOR and fracturing.
Some new repairing measures are:
(i) Heating remedies: using heat to remove the reservoir damage caused by clay swelling and water blocking.19
(ii) Hydraulic vibration remedies: using low frequency hydraulic vibration generators to load water, which makes the water form low frequency and high pressure water jet shock waves.20
(iii) Artificial earthquake remedies: sending electricity to the ground through a cable (usually the voltage is about 10–70 kV and the electricity is 10–25 kA) after the switching of capacitor discharge, which discharges a pulse in the well fluid, forming a pressure pulse in the reservoir.21
(iv) Ultrasonic remedies: putting an ultrasonic transducer into a reservoir with a cable, the generated ultrasonic waves have direct effects on the solid and liquid underground after the power is turned on, which forms an intense vibration wave near the wellbore.22
(i) Discharging phase: the first phase injects foam to discharge fluid into the wellbore.
(ii) Foam injection phase: the second phase injects foam into the formation through the wellbore, a specific foam quality and injection rate are used to avoid sand plugging in the deeper strata. The amount of required foam depends on the degree of formation damage. By injecting high-pressure foam into the formation, foam can extend to the pore throats and remove sand plugging.
(iii) Soaking phase: the third phase is a soaking phase. Its objective is to let the foam spread throughout the formation.
(iv) Foam production phase: the fourth phase produces foam, which can treat formation damage by carrying sand into the wellbore. The production phase is maintained until there is no more foam.
(v) Sand production phase: the final phase cycles foam to take sand out of the wellbore.
Well-X was the oilfield under study herein and it is a heavy oil production well, which was chosen for the application of Cyclic Foam Stimulation. The phase properties of Cyclic Foam Stimulation are demonstrated in Fig. 1. Fig. 2 indicates that the oil production rate before the Cyclic Foam Stimulation pilot project in Well X was 15–20 m3 d−1. The well was shut for 11 months due to sand plugging. The oil rate in the first production period after soaking was 18 m3 d−1 and reached its peak production of 80 m3 d−1 on the 67th production day. This showed that permeability and porosity were enhanced significantly.
The foam injection part included: a nitrogen bottle (for supplying air), a high pressure vessel (for depositing the foaming agent solution), a foam generator (for mixing nitrogen and the foaming agent solution; revolving speed, 0–1000 rpm; volume, 5000 mL; pressure, 20 MPa) and a high-pressure pump (for injecting the foam).
The reservoir part included: a core holder (pressure, 30 MPa; temperature, 150 °C; a screen was connected to one end of the reservoir vessel to prevent sand from entering the reservoir vessel), a core, a reservoir vessel (storing more foam; 38 × 300 mm; pressure, 20 MPa), and a back pressure pump (providing the surrounding pressure; pressure, 30 MPa).
The wellbore part included: a wellbore vessel (a screen was loaded at the entry point for collecting sand which was carried into the wellbore vessel; pressure, 20 MPa) and two digital pressure gauges (on both ends of the wellbore vessel; precision, 0.25%; pressure, 40 MPa).
The sand producing cores needed to be put into a PVA dissolved solution for eight hours before use, in order to degrade the PVA membrane and release the fine sand. After being saturated by the formation water, they were dried at a constant temperature of 80 °C for 24 hours in a dryer. The physical properties of the cores are shown in Table 1.
Core number | Height (cm) | Volume (cm3) | Grain diameter (μm) | Ratio | Quantity (g) | Porosity (%) |
---|---|---|---|---|---|---|
B1 | 8.16 | 91.38 | 99 | 1 | 40 | 23.45 |
B2 | 8.23 | 93.63 | 124 | 1 | 40 | 24.17 |
B3 | 8.25 | 92.39 | 148 | 1 | 40 | 24.89 |
Y1 | 8.17 | 92.23 | 99![]() ![]() ![]() ![]() |
1![]() ![]() ![]() ![]() |
40 | 25.08 |
Y2 | 8.29 | 93.86 | 99![]() ![]() ![]() ![]() |
1![]() ![]() ![]() ![]() |
40 | 23.26 |
Y3 | 8.31 | 94.24 | 99![]() ![]() ![]() ![]() |
2![]() ![]() ![]() ![]() |
40 | 24.18 |
(i) The initial porosity of a core was tested and then it was put into the core holder.
(ii) Nitrogen gas was injected at a certain pressure (P1) into the foam generator using six valves.
(iii) The foaming agent was put into the high pressure vessel using a high pressure pump and then the foaming agent was injected at a certain pressure (P2) into the foam generator.
(iv) The magnetic stirring device in the foam generator was operated for five minutes to make sure that the nitrogen gas and foaming agent mixed uniformly in the foam generator.
(v) The high pressure pump was used to inject the foam in the foam generator slowly into the wellbore vessel–core holder–reservoir vessel and the pressures at the ends of the wellbore were recorded at the same time.
(vi) The injection valve was closed to keep the foam fully reacting in the core for a period of time.
(vii) The production valve was opened and the foam was rapidly discharged.
(viii) After a period of time, the production valve was closed. The sand in the wellbore vessel was taken out and dried; then the quantity of sand was measured. The core was dried and its porosity after Cyclic Foam Stimulation was tested; finally, the core was put into the core holder and steps (vii) and (viii) were repeated.
V1 = Vh × P1/P2 | (1) |
In this equation, Vh equals the volume of the foam generator. The volume of the foaming agent solution is:
VL = Vh × (1 − P1/P2) | (2) |
Thus the gas–liquid ratio is:
![]() | (3) |
During the experiments, by controlling the nitrogen gas injection pressure P1 in the foam generator and the foaming agent solution injection pressure P2, we tried to keep the same quality of foam in each experiment to eliminate the effect of foam quality on the experiments.
βΦ = (Φ1 − Φ0)/Φ0 | (4) |
ε = m1/m0 | (5) |
The sizes of the drifting sand filling the cores of B1–3 were 99 μm, 124 μm and 148 μm, respectively. The total quantity of fine sand was 40 g. B1–3 were used to simulate formation damage from different sizes of particles. As shown in Fig. 5, the initial porosity order of the B cores was B3, B2 and B1 from large to small. As the compaction pressures of the B cores were all the same, the differences between B1–3 were due to the size of the fine sand. It can be seen that the smaller the blocking particle size, the more obviously the porosity declines. When the produced sand ratio was between 2.5% and 5.8%, the porosity order of the B cores from large to small changed to: B3, B1 and B2. In combination with Fig. 6, we can see that the B1 core recovery degree was far higher than those of B3 and B2. After Cyclic Foam Stimulation, the order of porosity from large to small was: B1, B2 and B3. In addition, we can see that the smaller sized particles make more of a contribution to formation damage remediation than the bigger sized particles do.
As shown in Fig. 6, more blocked pores have become unblocked as the produced sand ratio becomes bigger. Moreover, the porosity recovery rate becomes slower when the produced sand ratio is larger.
Similarly, the quantity of fine sand filled in the Y1–3 cores was 40 g, but their fine sand ratios were different. The quantities of fine sand in the Y1 core, with grain diameters of 99 μm, 124 μm and 148 μm, were 10 g, 10 g and 20 g, respectively. The Y2 core contained 20 g of drifting sand of 124 μm diameter and 10 g of both 99 μm and 148 μm diameter grains. The Y3 core contained 20 g of drifting sand of 99 μm diameter and 10 g of both 124 μm and 148 μm diameter grains. They were used to simulate the porosity damage degree according to different particle size distributions.
As shown in Fig. 7, the porosity order before producing the sand from large to small was: Y1, Y3 and Y2. As the free sand particle size in the Y2 core was 124 μm, the fine sand distribution in Y2 was more uniform than that in Y3 and Y1. According to the original porosity order, we can conclude that the more uniform the blocking particle size, the more serious the porosity damage. Since blocking particles of different sizes can mix better and combine more tightly, it is more difficult for Y2 to have fluid inflow and outflow. When the produced sand ratio was more than 6%, the porosity order of Y from large to small was: Y2, Y3 and Y1. Therefore, the blocking caused by sand with a uniform particle size distribution generates the most serious problem in terms of formation porosity. The final porosity of the Y3 core was higher than that of the Y1 core. As the size of most of the free sand particles within the Y3 core was 99 μm and the size of most of the free sand particles within the Y1 core was 148 μm, we can see that the smaller the size of the blocking particles, the more damage there is to the formation porosity.
Similarly, as shown in Fig. 8, more blocked pores become unblocked as the produced sand ratio becomes bigger. In addition, the porosity recovery rate becomes slower when the produced sand ratio is larger.
In this paper, the damage conditions and factors affecting common reservoirs were summarized into four categories. According to sand plugging, sand particles tend to stay in three areas of the pores. Advanced technologies applied as reservoir damage remedies have already been introduced. After this review, we developed the concept of injecting nitrogen foam into a formation to treat its damage from sand plugging for the first time. The results of a Cyclic Foam Stimulation application show that it enhances the well productivity significantly. Experimental apparatus for Cyclic Foam Stimulation has been designed. Additionally, in order to simulate the formation damage caused by the size distribution of fine sand, six artificial cores, which were sand producing, were prepared based on the technologies of pressure control and PVA membrane wrapping.
The experimental results show that foam has a good discharging effect on sand blockages. A scientific guide for the application of Cyclic Foam Stimulation can be generated from the method developed. As the effects of Cyclic Foam Stimulation are due to the quality of foam, it is necessary to do more systematic research on it.
The experimental results show that foam has a good discharging effect on sand blockages and reveals some relationships between the size and distribution of free sand vs. the formation porosity. Moreover, a porosity recovery factor has been defined. Some guidelines on porosity recovery have been given.
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