# The Characteristics of Gas-Water Two-Phase Radial Flow in Clay-Silt Sediment and Effects on Hydrate Production

Authors: Cheng Lu; Xuwen Qin; Lu Yu; Lantao Geng; Wenjing Mao; Hang Bian; Fanle Meng
Journal: Geofluids
 (2021)

---

## Abstract

Many hydrate-bearing sediments in the Shenhu area of the South China Sea are featured with unconsolidated clayed silt, small particle size, and high content of clay, which can pose a great challenge for gas production. In order to investigate the gas-water relative permeability in clay-silt sediments, through a radial flow experiment, samples from the target sediment in the Shenhu area were selected and studied. The results show that the irreducible water saturation is high and the influence of the gas-water interaction is obvious. The relative permeability analysis shows that the two-phase flow zone is narrow and maximum gas relative permeability is below 0.1. The flow pattern in clay-silt sediment is more complicated, and the existing empirical models are inadequate for flow characterization. The depressurization method to extract a hydrate reservoir with clay-silt sediments faces the problem of insufficient production capacity. Compared with the ordinary hydrate reservoir with sandstone sediment, the hydrate reservoir with clay-silt sediment has a low permeability and poor gas flow capacity. The gas-water ratio abnormally decreases during the production. It is urgent to enhance production with cost-effective measures.


---

## Body

## 1. Introduction

Gas hydrates are solid crystalline compounds and usually formed at low temperature and high pressure. Natural gas hydrate deposits vastly exist in the permafrost and subsea or deep ocean sediments [1]. In recent years, natural gas hydrate deposits with abundant reserves have been discovered in the northern part of the South China Sea and the eastern part of the Pearl River Mouth Basin [2]. More significantly, in 2020, a gas production pilot testing had been successfully conducted in the Shenhu region of the South China Sea operated by the China Geological Survey [3], in which over 86.14×104m3 natural gas had been extracted during 30 days. This testing has strongly demonstrated the feasibility of a controllable gas extraction from hydrate-bearing sediments and provided a precious experience for future research and development.Research shows that valuable natural gas hydrate reserves are considered mainly in coarse-grained sediments [4], and high abundance of hydrates, coinciding with sediments with large grain sizes, is usually accumulated in the turbidity current deposits and coarse sandstone formations [5]. These hydrate-bearing layers are featured with favorable porosity and permeability [6–8]. The average hydrate saturation in the Shenhu region of the South China Sea is over 20%, with a maximum of 47.3%. However, the core analysis demonstrated that hydrate reservoirs in the Shenhu region are typical clay-silt sediments with silt content up to 80-90% [9], which have poor bonding, high clay content, and low median diameter [10].In the exploitation of the clay-silt hydrate reservoir, the generated gas and water from solid hydrate must flow through clay-silt porous medium and then into the production well. It is generally known that multiphase relative permeability is an important feature of porous medium flow characteristic, especially in hydrate reservoirs where gas and water coexist. With the decomposition edge extending, the gas-water flow characteristic of clay-silt sediments near the production well will determine the production capacity. Therefore, an accurate characterization of relative permeability behavior in a clay-silt hydrate reservoir has great significance for a sustainable gas production rate. Today, the research activities are actively targeting relative permeability of a common hydrate reservoir with sandstone. There are two different methods for the relevant study: theoretical method and experimental method.Theoretical methods for modeling and simulating relative permeability in the hydrate-bearing formation have been developed for a long time. Singh et al. [11] derived analytical models to investigate relative permeability in hydrate-gas-water systems with an evenly distributed pore radius. Recently, Liu et al. [12] used fractal theory to describe pore structure of hydrate-bearing sediments and derived fractal-based models to study permeability and relative permeability. However, these models did not consider unconsolidated argillaceous siltstones, which have been shown to influence the properties of the hydrate reservoir in the South China Sea significantly.Johnson et al. [13] conducted the experimental investigation of gas-water relative permeability for gas-hydrate-bearing sediments from the Mount Elbert Gas Hydrate Stratigraphic Test Well, Alaska North Slope. During two runs, nitrogen was used to displace water and the effective permeability of gas at irreducible water saturation was determined as a function of hydrate saturation. Moreover, unsteady-state relative permeability experiments produce piston-like displacement results suggesting that steady-state experiments might be preferable. Jarrar et al. [14] conducted a gas-water flow experiment with quartz sands containing kaolin, simulating the gas-water flow during hydrate extraction, and observed fine migration and fracture by means of a computed tomography scan. Experimental determination of relative permeability requires the sample undisturbed, which is a challenging task. It needs a precise control of pressure to ensure the maintenance of stable hydrodynamics and mechanical conditions, which is usually expensive and hard. Most scholars only studied the single-phase flow in the hydrate-bearing formations [15, 16]. Konno et al. [17] analyzed the effective permeability of different hydrate-bearing sediments and found that effective stress change during exploitation can compact the unconsolidated sediment. Meanwhile, water produced by hydrate dissociation can change the salinity of stratum water, which may cause clay mineral expansion and permeability reduction.However, there are few experiments on the flow characteristics of the clay-silt hydrate reservoir in the South China Sea. The hydrate-bearing sediments in the Shenhu region of the South China Sea are featured with unconsolidated argillaceous siltstones, which have high clay content and small sediment particle size. Accurate prediction and analysis of this type of sediments are an important foundation in effective and efficient exploitation of hydrate reservoirs. The gas-water flow experiment can truly reflect the transport situation of two-phase coexistence in the clay-silt sediments, and the relative permeability, irreducible water saturation, and residual gas saturation are closer to the field situation. So to that extent, a comprehensive research on flow characteristic of hydrate-bearing sediments with clay-silt formation is urgent.In the early experiment of water flow in the clay-silt sediment core from the South China Sea, it is found that the permeability decreased gradually with the increase in differential pressure and this process is irreversible [18]. CT scanning was used to observe the phenomenon of pore volume creep in the sample during the flow process, and there was a clear power law relationship between the effective permeability and porosity of sediments under different pressure differences. It was worth noting that when the pressure gradient was less than 3 MPa/m, the sediment pore deformation was not obvious. When the pressure gradient exceeded 3 MPa/m, it had a great impact on the pore structure and the permeability decreases rapidly. In this paper, an experiment which discussed the two-phase flow pattern of gas and water in the clay-silt sediments was conducted. Moreover, the experimental results of two-phase flow in clay-silt sediments are combined to realize the simulation and production capacity evaluation of the hydrate reservoir with clay-silt sediments.


## 2. Sample and Experimental Method

### 2.1. Geological Background and Sample

The Shenhu region is located in the northern slope area of the South China Sea [19]. The experimental sample was obtained from the Shenhu region of the South China Sea. The particles were relatively fine, with a medium particle size of 12 μm. The main mineral components were quartz 53%, carbonate 16%, and clay minerals 26-30%. The main components of clay minerals were montmorillonite and illite [20].


### 2.2. Experimental Equipment and Procedure

The experimental system of gas-water two-phase radial flow in clay-silt sediment is shown in Figure1. The device is mainly composed of gas-water injection, overburden pressure, gas and water measurement, backpressure, and radial flow vessel. The radial flow vessel is the core of the device, which simulates a production well in the formation center. In the experiment, distilled water and nitrogen with a purity of 99.9% were used as an injection phase. The remaining experimental parameters are shown in Table 1.Figure 1
Experimental system.Table 1
Experimental parameters.
ParameterValueParameterValueμw—viscosity of the water at 20°C (mPa·s)1μg—viscosity of the nitrogen at 20°C (mPa·s)0.0178re—sample radius (cm)14.5rw—well radius (cm)1.3h—well height (cm)7Pe—inlet pressure (10-1 MPa)Experimental valuePw—outlet pressure (10-1 MPa)Experimental valueQw—flow rate of water (cm3/s)Experimental valueQg—flow rate of nitrogen (cm3/s)Experimental valueThe details of the experimental procedures are described as follows:(1)
Dry and triturate the sediment sample from the Shenhu region and fill it into the vessel with sand-proof measures(2)
Samples were watered and compacted (Figure2). The equipment was sealed up, and the overburden pressure was increased to simulate the formation pressure and ensure the similar degree of sample compaction. In the experiment, the overburden is usually set at 15 MPa. After that, the sample was saturated with water. The sample pore volume and porosity are calculated according to(1)Vp=Vt−m0ρ0,(2)Vt=πre2hm−πrw2h,(3)ϕ=VpVt×100%,where Vp is the pore volume (cm3); Vt is the sample volume (cm3); hm and h are the sample height and well length (cm), respectively; m0 is the dry sample weight (g); ρ0 is the dry sample density (g/cm3). The measured value is 2.6 g/cm3.(3)
The gas and water were injected into the sample at a constant rate according to a certain flow ratio. The inlet and outlet pressure was measured. The gas and water flow rate was measured. Then, calculate the effective permeability of gas and water and the water saturation of the sample. Sample water saturation measurement methods included the weighing method, material balance method, and resistivity method. In this experiment, the material balance method was used because of the large sample size. It was expressed as(4)Sj=Stj+Vcfj−VcjVp,where Sj and Stj are the saturation of the j-phase at the present test point and the previous test point, respectively; Vc is the total injection volume (cm3/s); fj is the proportion of the j-phase in the total injection volume; Vcj is the total volume of the j-phase in the outlet (cm3); Vp is the pore volume (cm3).Figure 2
Compacted sample.Therefore, as long as the water flow rates of the inlet and outlet are accurately recorded, the fluid saturation in the sample at the corresponding test point can be calculated.(4)
In the experiment, decrease the water injection rate and increase the gas injection rate gradually. Repeat the above procedure, and gas-water relative permeability with different water saturation can be obtained. In the experiment, the pressure gradient of the sample must be kept less than 3 MPa/m.


## 2.1. Geological Background and Sample

The Shenhu region is located in the northern slope area of the South China Sea [19]. The experimental sample was obtained from the Shenhu region of the South China Sea. The particles were relatively fine, with a medium particle size of 12 μm. The main mineral components were quartz 53%, carbonate 16%, and clay minerals 26-30%. The main components of clay minerals were montmorillonite and illite [20].


## 2.2. Experimental Equipment and Procedure

The experimental system of gas-water two-phase radial flow in clay-silt sediment is shown in Figure1. The device is mainly composed of gas-water injection, overburden pressure, gas and water measurement, backpressure, and radial flow vessel. The radial flow vessel is the core of the device, which simulates a production well in the formation center. In the experiment, distilled water and nitrogen with a purity of 99.9% were used as an injection phase. The remaining experimental parameters are shown in Table 1.Figure 1
Experimental system.Table 1
Experimental parameters.
ParameterValueParameterValueμw—viscosity of the water at 20°C (mPa·s)1μg—viscosity of the nitrogen at 20°C (mPa·s)0.0178re—sample radius (cm)14.5rw—well radius (cm)1.3h—well height (cm)7Pe—inlet pressure (10-1 MPa)Experimental valuePw—outlet pressure (10-1 MPa)Experimental valueQw—flow rate of water (cm3/s)Experimental valueQg—flow rate of nitrogen (cm3/s)Experimental valueThe details of the experimental procedures are described as follows:(1)
Dry and triturate the sediment sample from the Shenhu region and fill it into the vessel with sand-proof measures(2)
Samples were watered and compacted (Figure2). The equipment was sealed up, and the overburden pressure was increased to simulate the formation pressure and ensure the similar degree of sample compaction. In the experiment, the overburden is usually set at 15 MPa. After that, the sample was saturated with water. The sample pore volume and porosity are calculated according to(1)Vp=Vt−m0ρ0,(2)Vt=πre2hm−πrw2h,(3)ϕ=VpVt×100%,where Vp is the pore volume (cm3); Vt is the sample volume (cm3); hm and h are the sample height and well length (cm), respectively; m0 is the dry sample weight (g); ρ0 is the dry sample density (g/cm3). The measured value is 2.6 g/cm3.(3)
The gas and water were injected into the sample at a constant rate according to a certain flow ratio. The inlet and outlet pressure was measured. The gas and water flow rate was measured. Then, calculate the effective permeability of gas and water and the water saturation of the sample. Sample water saturation measurement methods included the weighing method, material balance method, and resistivity method. In this experiment, the material balance method was used because of the large sample size. It was expressed as(4)Sj=Stj+Vcfj−VcjVp,where Sj and Stj are the saturation of the j-phase at the present test point and the previous test point, respectively; Vc is the total injection volume (cm3/s); fj is the proportion of the j-phase in the total injection volume; Vcj is the total volume of the j-phase in the outlet (cm3); Vp is the pore volume (cm3).Figure 2
Compacted sample.Therefore, as long as the water flow rates of the inlet and outlet are accurately recorded, the fluid saturation in the sample at the corresponding test point can be calculated.(4)
In the experiment, decrease the water injection rate and increase the gas injection rate gradually. Repeat the above procedure, and gas-water relative permeability with different water saturation can be obtained. In the experiment, the pressure gradient of the sample must be kept less than 3 MPa/m.


## 3. Experimental Results and Discussion

This experiment tested three sets of clay-silt sediment samples. The permeability of sample 1 is 0.274 mD. The permeability of sample 2 is 0.481 mD. The permeability of sample 3 is 0.213 mD. The relative permeability curve of gas and water with different permeability samples are shown in Figure3.Figure 3
Relative permeability curve of different samples.Figure4 shows the relative permeability curves of three other gas reservoirs [21–23]. As shown from the relative permeability curve of the conventional sandstone gas reservoir, irreducible water saturation is low. It also reveals that, with the water saturation increasing, the gas relative permeability decreases slowly and the water relative permeability increases relatively slowly. Overall, the fluid flow capacity of the conventional sandstone gas reservoir is good. In the exploitation of this type of gas reservoir, water content rises slowly and the stable production cycle is long. In the coalbed gas reservoir, the irreducible water saturation is greater. With the increase in water saturation, the water relative permeability increases rapidly. For the tight sandstone gas reservoir, the irreducible water saturation is very high. The gas relative permeability under the irreducible water saturation is low. With the water saturation rising, the gas relative permeability rapidly decreases in a straight line form. The water relative permeability initially rises slowly and rises rapidly after a turning point. The isotonic point is deviation to the right. The flow capacity of the tight sandstone gas reservoir is weak.Figure 4
Relative permeability curve of other gas reservoirs.By comparison, it can be found that, in the gas-water relative permeability curve of the clay-silt sediment, the irreducible water saturation is much higher than that of other reservoirs, which is determined by the high clay content of the clay-silt sediment [24]. It also directly determines that the mobile gas porosity in the clay-silt sediment is very low. The two-phase flow area is unusually narrow, and the maximum gas relative permeability, less than 0.1, is very low. These characteristics are closely related to the permeability, mobile fluid porosity, pore-throat structure, and clay content of the clay-silt sediment [25]. To some extent, the maximum gas relative permeability also reflects the difficulty in extracting this type of hydrate reservoir.For the porous system composed of water, gas, and clay-silt sediment, water is a strong wetting phase [6]. Gas is a nonwetting phase. The three sets of the relative permeability curve are generally the same, but the values of the feature points are different, which are determined by the pore structure characteristics of the samples. From the curve, it can be seen that the lower the absolute permeability of the sample, the greater the irreducible water saturation is. It is because the pore-throat structure of the sample with low permeability is smaller and more complex. The capillary pressure is greater, and water is difficult to drive.Although the different samples have different permeability, the flow characteristics are similar. Initially, there is more water than gas, due to the hydrophilic sediment, there exists water film/water ring/water bridge on the pore wall, and the distribution is very uneven. There also exists the irreducible water in the small pore. Because of the great capillary resistance, the gas has difficulty entering the small pore. The gas can only flow along the center of the wide throat in limited quantities. At this time, the flow pattern of gas and water is mainly like “water-packed gas” and the relative permeability of the gas is very low [26]. It can be seen from Figure 3, with the increase in gas saturation, the interference between gas and water is more serious and the water relative permeability decreases rapidly. This is because the main flow channel—large throat channel—is gradually occupied by gas and free water content decreased. However, the gas permeability does not rise significantly. The remaining water in the sample is distributed in a ring-like form on the surface of the particles or at the corner of the particles, which seriously affects the flow capacity of the gas phase. At last, the gas saturation increases and the number of gas clusters (uneven distribution of gases, cluster distribution) in the sample rises. The “Jamin effect” on gas flow is increased. Therefore, under the irreducible water saturation, the relative permeability of the gas phase is not high.In the previous study that was aimed at numerical simulation of hydrate development, the relative permeability model usually adopted the empirical formula. Corey’s model is listed as follows, which is widely used in the tough+hydrate simulator [27].(5)krl=S4,krg=1−S21−S2,where S=Sl−Slr/1−Slr−SgrTo demonstrate the applicability of the common empirical model to clay-silt formations, the comparison between experimental results and Corey’s empirical formula has been illustrated in Figure5. As clearly shown in Figure 5, the fitting result is poor. In the empirical model, with the water saturation decreasing, the water relative permeability drops more rapidly. Meanwhile, the gas relative permeability rockets upwards. It is notable that the gas relative permeability at the irreducible water saturation is greatly high, which is similar to the flow characteristics in the conventional sandstone gas reservoir.Figure 5
The comparison between experimental results and Corey’s empirical formula.It is concluded that the flow pattern in clay-silt sediment is more complicated and the existing empirical models are inadequate for flow characterization. However, the way to obtain an empirical equation of the relative permeability curve in clay-silt formation through the experimental method still faces some difficulties, such as standardization of sample preparation and instrument precision. More standardized experiments should be conducted. Seeing the lack of empirical equation, one of the relative permeability curves from the experimental results will be used in the following numerical simulation.


## 4. Numerical Simulation

In order to study the effect of flow characteristics of clay-silt sediment on the production capacity of hydrate reservoir with clay-silt sediments, numerical simulation software (CMG STARS) has been used. The hydrate reaction kinetics is set by partial equilibrium reaction. The experimental results of two-phase flow of clay-silt sediments are combined to realize the simulation and production capacity evaluation of the hydrate reservoir with clay-silt sediments.


### 4.1. Model Parameters for a Real Case Study

A numerical simulation model based on the multiphase flow characteristics described above and the geological parameters of hydrate-bearing sediments in the Shenhu region in the South China Sea was built. It can be seen from Figure6 that a two-dimensional radial homogeneous model is established to simulate a depressurized well in the center of the hydrate reservoir with clay-silt sediments.Figure 6
Schematic model of the methane hydrate production scenario.Suppose that a shallow methane hydrate reservoir with clay-silt sediments is located 200 m below the mud line. The sea is 1000 m deep. The reservoir pressure is 12.13 MPa, and the temperature is 15.15°C. The whole model grid is200m×20m. The main properties of the simulated hydrate-bearing sediment are listed in Table 2. For seawater and porous media used in this investigation, Figure 7 can determine the equilibrium state of hydrate. The above experimental result of sample 1 has been used for the relative permeability model.Table 2
Parameters of hydrate-bearing formations.
ParameterValueParameterValueHydrate saturation0.3Initial water saturation0.7Porosity0.35Permeability (mD)Experimental valueRelative molecular mass of hydrate (g/mol)119.54Density of hydrate (kg/m3)919.7Specific heat of hydrate (J/(m3·K))1.47×106Heat conduction coefficient of hydrate (J/(m·d·K))4.58×104Specific heat of formation (J/(m3·K))8×105Heat conduction coefficient of formation (J/(m·d·K))1.5×105Figure 7
Phase equilibrium curve of methane hydrate.Radial mesh and local grid refinement (Figure8) are used in order to explore the mobility of two phases near the straight well and consider the convergence and running speed of the model. The production well is operated at a constant pressure of 4 MPa at the bottom of the wellbore. The production period is 1 year.Figure 8
Mesh generation and local grid refinement.


### 4.2. Simulation Results

The performance of gas production up to 1 year is shown in Figure9. As shown, the gas rate reaches their peaks (2960 m3/d) in the early stage rapidly and then decreases to 2300 m3/d and eventually fluctuates at a stable state in a long term. The ultimate cumulative gas production after 1 year is8.36×105m3. Figure 10 shows the water production in 1 year. It is notable that the water production rate drops from 25 m3/d initially to around 21 m3/d at the 50th day and then slowly rises to 22.4 m3/d at the end of the simulation.Figure 9
Performance of gas production.Figure 10
Performance of water production.In the middle and late production stage of the conventional sandstone hydrate reservoir, with the extension of the decomposition edge, the gas production rate continues to rise and water production declines continuously, which also means that the instantaneous gas-water ratio will decline. However, the simulation results based on the two-phase flow characteristic of clay-silt sediments are different from that of conventional sandstone hydrate reservoirs. The gas production rate cannot rise rapidly, and the water production rate is high. The instantaneous gas-water ratio (Figure11) slides from the initial 118 to 102 at the end of the simulation. Some criteria will be used to evaluate the technical feasibility of gas production from an unconsolidated argillaceous siltstone hydrate reservoir, including sufficiently high gas production rate and relatively high gas-to-water ratio. Considering the complexity and high cost of deepwater operations, it is generally believed that the daily gas production of deepwater gas wells needs to exceed 2.5×105m3/d and the water production is controllable. From this point of view, production capacity of the hydrate reservoir with clay-silt sediments using a single depressurization method cannot achieve economic feasibility.Figure 11
Performance of the gas-water ratio.The distribution evolution of temperature and pressure in the reservoir can also react with the production conditions of the hydrate reservoir. The variations of the formation pressure after 30 days, half a year, and 1 year are plotted in Figure12. As can be seen from the figure, the pressure diffusion is slow and the average formation pressure decreases by only 13% (to 10.55 MPa) in 1 year. The rate of pressure drop decreases gradually. The reason is that the irreducible water saturation in the hydrate reservoir with clay-silt sediments is too great. The mobile water saturation is low, and the formation water cannot be driven effectively, resulting in the slow pressure diffusion. The variations of the formation temperature after 30 days, half a year, and 1 year are plotted in Figure 13. Hydrate dissociation is an endothermal reaction that absorbs enough heat from surrounding fluid and formation. As revealed, the reservoir temperature dropped rapidly to less than 7°C on the 30th day, due to the hydrate dissociation near the well. During the production, the low-temperature edge continued to extend, but the advance speed is low. In the end of the simulation, the low-temperature edge only advanced to 5 m from the well.Figure 12
The distributions of pressure and average formation pressure at different times.Figure 13
The distributions of temperature at different times.In the process of hydrate extraction, the reservoir is usually divided into three parts: the dissociated zone, the dissociating zone, and the stable zone. The variations of the hydrate saturation after 30 days, half a year, and 1 year are plotted in Figure14. It can be seen that the front edge of the dissociated zone advances very slowly. The edge is located 1.4 m from the well at 30 days and only 4.7 m at the end of the simulation. The front edge of the dissociating zone advances faster, but the dissociation rate of hydrate in this zone is slow and the saturation of hydrate decreases slowly.Figure 14
The distributions of hydrate saturation at different times.It is assumed that no creep deformation occurs in the sediment during extracting the pore structure and porosity does not change and the space is fully occupied by the water and methane gas from dissociated hydrate. The variations of the water and gas saturation are plotted in Figure15. As revealed, gas and water saturation with different distances from the well increases with the dissociation of hydrate, but the water saturation increased by a small margin. The water saturation in the dissociated zone increased from 0.7 to 0.76, while the gas saturation increased to 0.24 from the initial value, forming a high gas saturation zone near the well. Combined with the production curve, it can be found that the formation of a high gas saturation zone near the well does not lead to a significant increase in gas production. Figure 16 shows the variations of the water and gas relative permeability 1 m from the well. It can be found from the figure that the water saturation rises, with an increase of 8.6%, from 0.7 to 0.76 within 20 days. But the relative permeability of the water phase increased by 800%. Although the gas saturation increased from the initial value to 0.238, the relative permeability of the gas phase was still less than 0.01. The same situation can be seen from Figures 17 and 18, which are the changes of the water-gas relative permeability 5 m and 10 m from the well. The low relative permeability of gas means that the gas flow capacity is poor. The dissociated gas cannot flow smoothly into the well, and a lot of them stay in the formation.Figure 15
The distributions of water saturation and gas saturation at different times.Figure 16
The variations of the water and gas relative permeability 1 m from the well.Figure 17
The variations of the water and gas relative permeability 5 m from the well.Figure 18
The variations of the water and gas relative permeability 10 m from the well.Figure19 is a comparison between the gas volume from the dissociated hydrate and the output gas volume from the well. It can be clearly seen that the dissociated gas is much greater than the gas produced from the well. At the end of the simulation, the dissociated gas volume is nearly 1.6×106m3, but the produced gas volume is only half of the dissociated gas volume.Figure 19
The comparison between the gas volume from the dissociated hydrate and the output gas volume from the well.Compared with the ordinary hydrate reservoir with sandstone sediment, the hydrate reservoir with clay-silt sediment has a low permeability and poor flow capacity. In other simulation conditions, it can be seen from Figures20 and 21 that the production capacity of the sandstone formation is nearly 5 times that of the clay-silt sediment. The gas-to-water ratio of sandstone formation can increase to nearly 900. In summary, it can be found that the depressurization method to extract the hydrate reservoir with clay-silt sediments faces the problem of insufficient production capacity. It is urgent to enhance production measures, such as thermal stimulation and hydrofracturing.Figure 20
The comparison of cumulative gas production.Figure 21
The comparison of the gas-water ratio.


## 4.1. Model Parameters for a Real Case Study

A numerical simulation model based on the multiphase flow characteristics described above and the geological parameters of hydrate-bearing sediments in the Shenhu region in the South China Sea was built. It can be seen from Figure6 that a two-dimensional radial homogeneous model is established to simulate a depressurized well in the center of the hydrate reservoir with clay-silt sediments.Figure 6
Schematic model of the methane hydrate production scenario.Suppose that a shallow methane hydrate reservoir with clay-silt sediments is located 200 m below the mud line. The sea is 1000 m deep. The reservoir pressure is 12.13 MPa, and the temperature is 15.15°C. The whole model grid is200m×20m. The main properties of the simulated hydrate-bearing sediment are listed in Table 2. For seawater and porous media used in this investigation, Figure 7 can determine the equilibrium state of hydrate. The above experimental result of sample 1 has been used for the relative permeability model.Table 2
Parameters of hydrate-bearing formations.
ParameterValueParameterValueHydrate saturation0.3Initial water saturation0.7Porosity0.35Permeability (mD)Experimental valueRelative molecular mass of hydrate (g/mol)119.54Density of hydrate (kg/m3)919.7Specific heat of hydrate (J/(m3·K))1.47×106Heat conduction coefficient of hydrate (J/(m·d·K))4.58×104Specific heat of formation (J/(m3·K))8×105Heat conduction coefficient of formation (J/(m·d·K))1.5×105Figure 7
Phase equilibrium curve of methane hydrate.Radial mesh and local grid refinement (Figure8) are used in order to explore the mobility of two phases near the straight well and consider the convergence and running speed of the model. The production well is operated at a constant pressure of 4 MPa at the bottom of the wellbore. The production period is 1 year.Figure 8
Mesh generation and local grid refinement.


## 4.2. Simulation Results

The performance of gas production up to 1 year is shown in Figure9. As shown, the gas rate reaches their peaks (2960 m3/d) in the early stage rapidly and then decreases to 2300 m3/d and eventually fluctuates at a stable state in a long term. The ultimate cumulative gas production after 1 year is8.36×105m3. Figure 10 shows the water production in 1 year. It is notable that the water production rate drops from 25 m3/d initially to around 21 m3/d at the 50th day and then slowly rises to 22.4 m3/d at the end of the simulation.Figure 9
Performance of gas production.Figure 10
Performance of water production.In the middle and late production stage of the conventional sandstone hydrate reservoir, with the extension of the decomposition edge, the gas production rate continues to rise and water production declines continuously, which also means that the instantaneous gas-water ratio will decline. However, the simulation results based on the two-phase flow characteristic of clay-silt sediments are different from that of conventional sandstone hydrate reservoirs. The gas production rate cannot rise rapidly, and the water production rate is high. The instantaneous gas-water ratio (Figure11) slides from the initial 118 to 102 at the end of the simulation. Some criteria will be used to evaluate the technical feasibility of gas production from an unconsolidated argillaceous siltstone hydrate reservoir, including sufficiently high gas production rate and relatively high gas-to-water ratio. Considering the complexity and high cost of deepwater operations, it is generally believed that the daily gas production of deepwater gas wells needs to exceed 2.5×105m3/d and the water production is controllable. From this point of view, production capacity of the hydrate reservoir with clay-silt sediments using a single depressurization method cannot achieve economic feasibility.Figure 11
Performance of the gas-water ratio.The distribution evolution of temperature and pressure in the reservoir can also react with the production conditions of the hydrate reservoir. The variations of the formation pressure after 30 days, half a year, and 1 year are plotted in Figure12. As can be seen from the figure, the pressure diffusion is slow and the average formation pressure decreases by only 13% (to 10.55 MPa) in 1 year. The rate of pressure drop decreases gradually. The reason is that the irreducible water saturation in the hydrate reservoir with clay-silt sediments is too great. The mobile water saturation is low, and the formation water cannot be driven effectively, resulting in the slow pressure diffusion. The variations of the formation temperature after 30 days, half a year, and 1 year are plotted in Figure 13. Hydrate dissociation is an endothermal reaction that absorbs enough heat from surrounding fluid and formation. As revealed, the reservoir temperature dropped rapidly to less than 7°C on the 30th day, due to the hydrate dissociation near the well. During the production, the low-temperature edge continued to extend, but the advance speed is low. In the end of the simulation, the low-temperature edge only advanced to 5 m from the well.Figure 12
The distributions of pressure and average formation pressure at different times.Figure 13
The distributions of temperature at different times.In the process of hydrate extraction, the reservoir is usually divided into three parts: the dissociated zone, the dissociating zone, and the stable zone. The variations of the hydrate saturation after 30 days, half a year, and 1 year are plotted in Figure14. It can be seen that the front edge of the dissociated zone advances very slowly. The edge is located 1.4 m from the well at 30 days and only 4.7 m at the end of the simulation. The front edge of the dissociating zone advances faster, but the dissociation rate of hydrate in this zone is slow and the saturation of hydrate decreases slowly.Figure 14
The distributions of hydrate saturation at different times.It is assumed that no creep deformation occurs in the sediment during extracting the pore structure and porosity does not change and the space is fully occupied by the water and methane gas from dissociated hydrate. The variations of the water and gas saturation are plotted in Figure15. As revealed, gas and water saturation with different distances from the well increases with the dissociation of hydrate, but the water saturation increased by a small margin. The water saturation in the dissociated zone increased from 0.7 to 0.76, while the gas saturation increased to 0.24 from the initial value, forming a high gas saturation zone near the well. Combined with the production curve, it can be found that the formation of a high gas saturation zone near the well does not lead to a significant increase in gas production. Figure 16 shows the variations of the water and gas relative permeability 1 m from the well. It can be found from the figure that the water saturation rises, with an increase of 8.6%, from 0.7 to 0.76 within 20 days. But the relative permeability of the water phase increased by 800%. Although the gas saturation increased from the initial value to 0.238, the relative permeability of the gas phase was still less than 0.01. The same situation can be seen from Figures 17 and 18, which are the changes of the water-gas relative permeability 5 m and 10 m from the well. The low relative permeability of gas means that the gas flow capacity is poor. The dissociated gas cannot flow smoothly into the well, and a lot of them stay in the formation.Figure 15
The distributions of water saturation and gas saturation at different times.Figure 16
The variations of the water and gas relative permeability 1 m from the well.Figure 17
The variations of the water and gas relative permeability 5 m from the well.Figure 18
The variations of the water and gas relative permeability 10 m from the well.Figure19 is a comparison between the gas volume from the dissociated hydrate and the output gas volume from the well. It can be clearly seen that the dissociated gas is much greater than the gas produced from the well. At the end of the simulation, the dissociated gas volume is nearly 1.6×106m3, but the produced gas volume is only half of the dissociated gas volume.Figure 19
The comparison between the gas volume from the dissociated hydrate and the output gas volume from the well.Compared with the ordinary hydrate reservoir with sandstone sediment, the hydrate reservoir with clay-silt sediment has a low permeability and poor flow capacity. In other simulation conditions, it can be seen from Figures20 and 21 that the production capacity of the sandstone formation is nearly 5 times that of the clay-silt sediment. The gas-to-water ratio of sandstone formation can increase to nearly 900. In summary, it can be found that the depressurization method to extract the hydrate reservoir with clay-silt sediments faces the problem of insufficient production capacity. It is urgent to enhance production measures, such as thermal stimulation and hydrofracturing.Figure 20
The comparison of cumulative gas production.Figure 21
The comparison of the gas-water ratio.


## 5. Conclusion

(1)
The hydrate-bearing sediments in the Shenhu region of the South China Sea are featured with unconsolidated argillaceous siltstones, which have high clay content and small sediment particle size. Its irreducible water saturation is more than 0.65. The pore of mobile gas is small, and the interference between gas and water is strong(2)
Clay-silt sediment has a poor permeability. The two-phase flow area is unusually narrow, and the maximum gas relative permeability, less than 0.1, is very low. These characteristics are closely related to the permeability, mobile fluid porosity, pore-throat structure, and clay content of the clay-silt sediment. The flow pattern is complicated, and many mechanisms have been inferred in the paper. Of course, the gas-water flow mechanisms in clay-silt sediment will be more persuasive with the help of microscopic visual experiments(3)
The fitting result between experimental results and Corey’s empirical formula is poor. That means that the existing empirical models are inadequate for flow characterization in the hydrate reservoir with clay-silt sediments(4)
The depressurization method to extract the hydrate reservoir with clay-silt sediments faces the problem of insufficient production capacity. The front edge of the dissociated zone advances very slowly. Half of the dissociated gas cannot flow into the well, and the gas-water ratio decreases during the production because of the weak flow capacity of methane. It is urgent to enhance production with cost-effective measures



---

*Source: 6623802-2021-05-12.xml*