Introduction

The injection–production mechanism of a watered-out oil rim underground gas storage is relatively complex and is related to three-phase (oil–gas–water) percolation and material exchange: the fluid phase distribution was complex and irregular before the storage was built, because the reservoir was influenced by retrograde condensation, the degassing of crude oil, water injection, and the presence of edge-bottom water (Li and Zhang 2000; Ding and Xie 2006; Wang et al. 2014). There is not much specialised research on impact mechanism of oil rim on underground gas storage operation, it is difficult to form an effective reference. However, the process of gas injection into the oil rim can be equivalent to natural gas flooding process. Domestic and foreign scholars have done a lot of laboratory tests and field studies in this aspect, have also made some achievements and describe the change of fluid seepage in the flooding reservoir after gas injection.

From the late 1950s, the US researchers designed a gas–water alternative flooding programme and carried out numerical simulation, initial figured out the phase change and seepage law of the oil gas and water three-phase after the gas injection into the reservoir (Caudle and Dyes 1958). Since then, a lot of scientists have conducted rock physical modelling experiment and numerical simulation studies (Haln and Monger 1990; Wozinak et al. 1997), these basically figure out: when the gas was injected rapidly into the storage, it would cause a series of reactions, such as the instigation of the Jamin effect, flow-around, water-locking, gas-locking, and emptying (Kurihara et al. 2000). These factors exert significant effects on production efficiency in underground gas storage facilities (Udegbunan et al. 1994).

The G393 fault-block was a condensate gas reservoir with an oil rim, which had experienced more than 5 years’ water-injection development before being converted to an underground gas storage. The reservoir was in the middle of the development and had a complex fluid distribution, in which oil, gas, and water coexisted (Fig. 1).

Fig. 1
figure 1

Location map of the G393 fault-block gas-condensate reservoirs

To improve the running efficiency of this type of underground gas storage, the factors influencing, and the extent of, the oil rim should be studied before any alterations are undertaken. Firstly, a three-dimensional (3-d) dynamic model should be established to simulate the gas reservoir development history and to establish a fluid distribution model before any alterations take place; then using numerical simulation method to study the impact mechanism of oil rim, design different schemes to study the barrier effect of the fluid and the influence degree of the oil rim on gas production capacity, clear the oil, gas and water three-phase seepage rule in the process of underground gas storage rebuilt. Finally, based on the results of numerical simulation, the underground gas storage injection and production scheme can be designed to preferably reasonable performance indicators, provide guidance for the smooth and efficient operation of 393 underground gas storage.

Numerical simulation of gas reservoir development history

The establishment of a 3-d, three-phase model for G393

The G393 fault-block underground gas storage has been altered by the abandoned condensate gas reservoir within its oil rim. Three-phase flow, including oil, gas, and water, in the reservoir was involved in the development thereof. A numerical simulation of 3-d, three-phase behaviour was, therefore, needed to analyse its development and history. Using Darcy’s law and the law of conservation of mass, and considering rock and fluid compressibility, we established a model for flow in a three-dimensional, three-phase, anisotropic, oil reservoir.

The 3-d seepage model governing three-phase continuous seepage is given by:

$$\left\{ \begin{aligned} & \nabla \cdot \left[ {M_{o} N_{o} \left( {\nabla P_{o} - \rho_{o} G\nabla D} \right)} \right] + q_{o} = \frac{\partial }{\partial t}\left( {S_{o} A_{o} } \right)\quad{\text{Oil}} \\ & \nabla \cdot \left[ {R_{s} M_{o} N_{o} \left( {\nabla P_{o} - \rho_{o} G\nabla D} \right) + M_{g} N_{g} \left( {\nabla P_{g} - \rho_{g} G\nabla D} \right)} \right] + q_{g} = \frac{\partial }{\partial t}\left( {R_{s} S_{o} A_{o} + S_{g} A_{g} } \right)\quad {\text{Gas}} \\ & \nabla \cdot \left[ {M_{w} N_{w} \left( {\nabla P_{w} - \rho_{w} G\nabla D} \right)} \right] + q_{w} = \frac{\partial }{\partial t}\left( {S_{w} A_{w} } \right)\quad {\text{Water}} \\ \end{aligned} \right.$$

where \(M\) is relative permeability/viscosity; \(A\) is porosity/volume coefficient; \(N\) is permeability/volume coefficient; \(P\) is pressure; \(\rho\) is fluid density; \(q\) is fluid flow rate; \(S\) is fluid saturation ratio; (the subscripts o, g, and w represent the water phase of the oil and gas, respectively). \(G\) is acceleration due to gravity; \(D\) is depth of the reservoir; \(R_{s}\) is dissolved gas oil ratio; \(C\) is model boundary. The initial conditions for three-phase equilibrium are as follows:

$$\left\{ \begin{aligned} & S_{g} + S_{o} + S_{w} = 1 \\ & P\left( {x,y,z} \right) = P_{0} \left( {x,y,z} \right) \\ \end{aligned} \right.$$

The boundary conditions for the closed boundary are:

$$\frac{\partial P}{\partial n}\left| {_{C} = 0} \right.$$

Model meshing

While establishing the 3-d geological model, the grid line of the plan must reflect the heterogeneity of the reservoir, the degree of heterogeneity, and subtle changes in the extent of the whole: the simulation results must fully reflect the various geological and developmental factors encountered, reflect the movement of the underground water, gas, and oil when the injection–production well pattern is adjusted, and reflect the injection–production well pattern adjustment and its effects on the distribution and influence of water, oil, and gas, at the same time, considering the power and capacity of the computer available (Zhang and Xie 2011). The grid type of G393 model is structured corner point grids, uses two (m + 1) × (n + 1) rules topology control surfaces to generate unit structure. In the middle, each unit’s top and bottom boundary is defined by sliding line, adjacent to the interface between the grid by irregular connection. Conductivity between the grid blocks is calculated using fluid properties, rock properties, fluid rock interaction between two grid blocks and connected to the grid geometry direction, the formula is as follows:

$$T_{a} = {\left( {\frac{AK}{h}} \right)_{av}} \times {\left( {\frac{{K_{ra} }}{{\mu_{a} B_{a} }}} \right)_{av}} = {\text{TRAN}}{\left( {\frac{{K_{ra} }}{{\mu_{a} B_{a} }}} \right)_{av}}$$

where a is one phase of oil, gas and water; T a is unidirectional conductivity of phase a; K is the absolute permeability; A is contact area of the adjacent grid; h is distance of adjacent mesh centre in the direction; \(\mu_{a}\) is viscosity of phase a; \(K_{ra}\) is relative permeability of phase a; B a is volume factor of phase a

In this 3-d geological model, 10 m × 10 m corner point grids were used in the plane lying longitudinally to the individual development of small strata units: this was divided into nine separate flow units. The even-numbered layers allowed no seepage and represented a stable shale layer between the sand strata (Fig. 2).

Fig. 2
figure 2

3-d geological model used for meshing

History matching of the development of the gas reservoir

To test the reliability of the three-phase, 3-d numerical simulation model, a 5-year production history of the G393 gas reservoirs was modelled. The main indicators were: gas reservoir pressure, gas reservoir gas production, and the gas reservoir oil and water production rates. G393 gas reservoir numerical simulation process is shown in Fig. 3.

Fig. 3
figure 3

G393 gas reservoir numerical simulation process

Gas reservoir numerical simulation result is shown in Fig. 4. Analysis the simulation results can be obtained that the difference between the results of computer simulation (continuous line) and gas reservoirs’ actual production index (point) is small. There is a little difference in the development period between December 2006 and December 2007, that may be due to the well pattern adjusted more frequently in this time period; continuous production measure changes lead to instabilities fitting, affecting the fitting precision. On the whole, the trend remained the same between the two values, the established three-phase, 3-d model did match actual gas reservoir behaviour, so it could be used to simulate and predict changes therein (Fig. 4).

Fig. 4
figure 4

Gas reservoir production history matching

The effect of the oil rim on gas storage injection and production

The development history of the G393 fault-block condensate gas reservoir showed that they developed the fault-block oil rim and ring contact parts at the same time, but since there was insufficient control at the oil–gas interface, gas channelling occurred, as well as a significant decline in the production capacity of the oil and gas wells. During its development, to add to the underlying energy output, water-injection development policy was used in the oil rim zone. The relationship between the oil and water distributions is complex: if the gas storage were to be rebuilt, it must impact the injection volume and gas recovery therefrom and was not conducive to the smooth and efficient operation of the underground gas storage. Therefore, to enact those control measures needed to reduce the effect of these disadvantages, an understanding of the behaviour of the oil rim, as it affects gas storage, was sought.

The presence or absence of oil rim impact mechanism of gas storage

The original state of G393 gas reservoir is a condensate gas reservoir with oil ring, the original gas–oil contact depth is −3257 m, and the water–oil contact depth is −3327 m. It can be obtained through the 3D modelling calculation: the oil rim pore volume is about 58.42 × 104 m3, the gas cap pore volume is about 129.09 × 104 m3, the pore volume of the active water body is about 182.65 × 104 m3. The gas, oil, water pore volume ratio is about 2:1:3, therefore, it is a weak edge water condensate gas reservoir. The basic fluid properties of gas, oil and water are shown in Table 1.

Table 1 The basic fluid properties table of gas, oil and water

Compared with the same type of condensate gas reservoir, the extent to which the oil rim affected gas storage injection and production was unknown. To reveal this, we used the previously established 3-d, three-phase model as the basis for gas storage injection–production capacity predictions which assumed the existence of oil rim. In this simulation: the gas was only present at the gas–oil interface, there were no three-phase coexistence reservoirs when the field was in its original condition (Kilincer and Gumarch 2000). Figure 5 shows the two gas reservoir models used.

Fig. 5
figure 5

The two numerical simulation models used

Table 2 summarises the analysis simulation parameters used along with a series of simulation parameters used in the numerical simulation of the process: consistent injection and production parameters were used in each of the two models to compare the differences in their results.

Table 2 Analysis simulation parameters

In the two prediction schemes, gas was injected into the formation until the formation pressure was restored to its original value: the cumulative injection curve and stress change curve are plotted in Fig. 6. From the graph and its horizontal ordinate A, B, C, and D are points at which the oil rim lies at the bottom of the condensate gas reservoir, the injection rate and injection volume had decreased to a certain extent, but the pressure rose faster than in a pure gas reservoir. Under the same injection conditions and at the same formation pressure, the condensate gas reservoir, with an oil rim, needed about 68 days to develop, and the peak pressure of pure condensate gas reservoirs was reached in approximately 92 days: the accumulation of the final injection volumes were 1.33 × 108 and 1.76 × 108 m3, respectively.

Fig. 6
figure 6

The injection parameters for block G393 with an oil rim and a pure condensate gas reservoir

Figure 7 shows the mechanism underpinning the behaviour of this underground gas storage injection–production. In the pure condensate gas reservoir, the gas promoted a uniform transverse distribution during injection. The gas was pushed into the water (a vertical distance of 36 m, and a 260 m plane distance) and did not form a serious fingering pattern when gas was injected into the formation until the formation pressure reached its original value. The gas velocity decreased, and the flow path occupied a shorter distance (a vertical distance of 13 m, and an 8 m plane distance) with the oil rim of this condensate gas reservoir during the injection process due to the blocking effect of the oil rim, especially after the gas entered the oil rim and dissipated therein which induced significant lateral deviation errors: a single direction dash phenomenon would have been more serious, but the fluid had not yet spread to cover the entire oil rim area at that stage.

Fig. 7
figure 7

The injection–production behaviour: oil rim effects on underground gas storage

Oil rim recovery degree impact on underground gas storage

The aforementioned research showed that the presence of the oil rim affected the injection of gas in this underground storage, and that was not conductive to the spread of the gas therein. The first issue facing the operators of this type of gas reservoir was that it produced as much of the remaining oil in the underground reservoir as possible, and vacated sufficient rock pore volume to provide more gas storage. The gas pressure increased as injection progressed; the degassed oil will reach a second saturation during development of the gas reservoir, as it absorbs some of the dissolved gas. An allied viscosity reduction, enhancing the flow properties, meant that this oil could be easily recovered.

Therefore, the main task for this injection–production well near the oil rim was to extract oil early in the gas storage injection–production cycle.

To simulate the impact of the recovery from the oil rim to the extent of injection–production process gas storage, this research used the design of different schemes to numerically simulate underground conditions. Different degrees of recovery from the oil rim oil wells in the vicinity of the oil rim were simulated. Injection–production wells, using the original development wells, and injection–production parameters derived from the use of the injection–production parameters of each well in the study scheme were predicted from the beginning for each corresponding degree of recovery (Fu et al. 2007). Wells G393-2 and G393-3 were predicted to be best stopped when their production gas–oil ratio exceeded 100,000: thereafter, number of cycles to be run was compared. Table 3 shows the parameters used in this numerical simulation.

Table 3 Numerical simulation parameters

The numerical simulation results shown in Fig. 8 show that with increasing recovery from the oil rim, the production period of the well near the gas storage zone within the oil rim was gradually shortened, and the oil rim recovery showed a power–function relationship therewith; the magnitude of this change decreased and gradually stabilised once the extent of the oil rim recovery reached 25 %. Therefore, when the oil rim recovery was between 25 and 30 %, the conditions for renovation of underground gas storage were optimal.

Fig. 8
figure 8

The relationship between the oil production cycle and oil rim recovery

Effects of the oil rim on G393 underground gas storage operation analysis

Until the reconstruction of this gas storage, 61.03 % of the condensate gas in the geological reserve was recovered, and 20.81 % of the condensate oil and crude oil were recovered. According to the principles guiding underground gas storage reconstruction, the degree of recovery of condensate gas was suitable for the rebuilding of this underground gas storage (the best recovery rate was 60 %). The extent of the oil recovery was not very high. If calculated according to the forecast results, at least 10 injection–production cycles could be produced in the reservoir in which crude oil was present: for the operation of the gas storage, this was without doubt a very unfavourable factor. Hence, the need for this study is on the basis of the existing oil rim recovery, as designed for the rapid recovery of gas storage injection–production well patterns, so that the quickest underground gas storage operation could be brought about. There are three main principles guiding the design of such schemes (Chen and Tan 2001):

  1. 1.

    Increase the degree of control of the well pattern in the oil rim region, especially near the oil–gas interface where corresponding control wells should be used.

  2. 2.

    The volume of injected gas should be controlled during injection into the injection–production well in the oil rim region, in this way, there is sufficient time to mix the injected gas and crude oil, thus increasing the crude oil quadratic saturation.

  3. 3.

    To prevent the formation of a pressure drop funnel (a result affecting the crude oil use area), the differential pressure must be controlled during production recovery.

By adhering to these principles, we designed an injection–production well pattern for the G393 underground gas storage: there were nine wells in all (four in the area of the gas cap, two in the oil–gas interface, and three within the oil rim). Table 4 shows the injection parameters used therein.

Table 4 The forecast injector–producer parameter table for the underground gas storage operation plan

Figure 9 shows well positions used in these numerical simulations.

Fig. 9
figure 9

Designed well positions for the numerical simulation of the G393 underground gas storage

Figure 10 shows the numerical simulation forecast of the cumulative recovery of crude and gas oil in the form of a ratio curve for the operation of the G393 underground gas storage: it can be seen that, over the operating cycles, the oil in the oil rim was produced continuously, oil recovery gradually decreased until about the tenth cycle, and the production gas–oil rate reached 100,000, at a recovery efficiency reaching 75 %, the crude oil was largely emptied from the reservoir space, the operational efficiency of gas storage improved, and the capacity and working period were also gradually stabilised.

Fig. 10
figure 10

Numerical prediction of the cumulative recovery of crude and gas oil as a ratio curve for the G393 underground gas storage

Figure 11 shows the change in oil saturation in the oil rim during the operation of the G393 underground gas storage: as the underground gas storage increased over several operational cycles, the oil saturation within the oil rim decreased quickly, crude oil around the operation wells showed a high degree of recovery, the pore ratio was high, the local area around the edge, or the local area near the fault was changed due to reservoir or gas injection, there was little crude oil in the pore body, but this had less effect on gas storage capacity and the operations as a whole (Zhao 2000; Tan and Lin 2008). On the whole, about eight cycles later, the influence exerted by the oil rim had diminished, and the gas storage was operating smoothly.

Fig. 11
figure 11

Changes in oil saturation in the oil rim during the operation of the G393 underground gas storage

Conclusions

According to the extent of the effect of the oil rim on production, and the influencing mechanism of the presence, or absence, of the oil rim on oil injection and production from this gas storage, the following main conclusions were drawn:

  1. 1.

    In the presence of the oil rim, the injected gas spread and promoted a significant lateral deviation error; a single direction of penetration would have been more deleterious and would have reduced the gas injection rate and amount of gas injected to nearby wells, and it would have affected the diffusion velocity of gas in the water. In the G393 underground gas storage, the gas was used to drive the water forward over a reduced distance of 180 m (plane) and 23 m (longitudinal).

  2. 2.

    The oil rim, with regard to the crude oil recovery ratio, can directly affect the operating efficiency of such an underground gas storage. When the recovery factor was reduced, the production period gradually increased. According to the numerical prediction, an oil rim recovery of 25–30 % was optimal for the renovation of this underground gas storage.

  3. 3.

    Under low oil recovery conditions, during reconstruction of this underground gas storage, we can increase the injection–production well flow rate within the oil rim for a more rapid resource recovery: this can vacate underground reservoir pores and improved the efficiency of gas storage. In addition, the edge of the well can be used as an inspection well and a drainage well during the later stages of operation, thus saving money.