KnE Materials Science | Sino-Russian ASRTU Conference Alternative Energy: Materials, Technologies, and Devices | pages: 190-200

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1. Introduction

Gas hydrates are ice-like crystalline compounds composed of hydrogen-bonded water molecules encapsulating gas molecules [1]. Natural gas hydrates have recently received considerable attention as a promising future energy source because of the large amounts of massive hydrate reservoirs [2]. A series of methods for gas hydrate production have been proposed based on the special characteristics of the hydrate, such as depressurization, thermal stimulation, and inhibitor injection [3], which are all based on decomposition of clathrate crystals through external stimulation. However, when the solid hydrate dissolves, it may lead to destabilization of sediments and subsequent seafloor subsidence [4]. Therefore, the CO 2 replacement method has recently emerged as a promising method of recovering hydrocarbons (HC) without hydrate dissociation and sequestering CO 2 into natural gas hydrate reservoirs, simultaneously [5].

Since the idea of swapping CO 2 for CH 4 in gas hydrates was first advanced by Ohgaki et al. [6], extensive research of the replacement behaviors of SI hydrates has been conducted [5] owing to their abundance in nature. Beside SI natural gas hydrates predominantly consisting of CH 4 molecules, natural occurrence of SII hydrates has been discovered in some deposits, such as the Gulf of Mexico outside the Caspian Sea [7], Lake Baikal [8], the Qilian Mountain permafrost of China [9], and the Pearl River Mouth Basin of the South China Sea [10]. To date, only few data are available for the swapping process of HC in structure II mixed hydrates [11–15]. The previous reports indicate that structural transformation and isostructural conversion may occur in the replacement of SII hydrates [15]. Compared with CH 4 hydrates, multiple guests engaged into small and large cages of SII natural gas hydrates may cause the unique pattern of the replacement occurring in SII hydrates. Larger HC entrapped in large cages, such as C 2 H 6 , C 3 H 8 , and C 4 H 10 , play an important role in the stability of the hydrate structure. Therefore, the release of larger HC from SII hydrates can cause the structural transformation. However, studies on the replacement kinetics of SII hydrates with CO 2 / N 2 are still insufficient.

In this work, the replacement of CH 4 + C 2 H 6 + C 3 H 8 mixed hydrates using CO 2 /N 2 is experimentally studied. The guest-exchange behavior of different HC with CO 2 and N 2 occurring in SII natural gas hydrates was examined through the composition analysis of the fluid phase during replacement. The heterogeneous composition of the final replaced hydrates caused by solid state diffusion was indirectly obtained by coupling gas production measurements with compositional analysis. Furthermore, the replacement efficiencies of different HC were calculated based on the final compositions of the replaced hydrates and the composition of the vapor phases measured by a gas chromatography.

2. Experimental Section

CO 2 (99.99%) and gas mixtures of CH 4 (81.10%) + C 2 H 6 (9.53%) + C 3 H 8 (9.37%), CO 2 (21.10%) + N 2 (78.9%), and CO 2 (53.87%) + N 2 (46.13%) were supplied by Beifang Special Gas Industry Corporation.

Figure 1 shows a schematic diagram of the apparatus and its components. The high-pressure cell has an effective volume of 240 ml, which was immersed in the circulating and cooling glycol bath to keep stable temperature during the experiments. The temperature and pressure of the system are recorded on a PC using a Monitor and Control Generated System through a data acquisition device at regular time intervals.

Figure 1

Schematic of the experimental apparatus.

fig-1.jpg

The experimental procedure for the initial CH 4 + C 2 H 6 + C 3 H 8 hydrate formation was similar to that in our previous work [16]. The cell was initially charged with a known amount of water-saturated porous quartz sands and submerged in the glycol bath to control the temperature. The gas mixture of CH 4 + C 2 H 6 + C 3 H 8 was injected into the pressure cell to the desired value after vacuuming the whole apparatus, and then the temperature of the cell was gradually lowered to 277.2 K to form mixed hydrates.

After completion of mixed hydrate formation, the pre-cooled replacement gas was rapidly injected into the reactor to purge the remaining gas mixture of HC. When the HC composition of the discharged gas appeared to be less than 0.5 mol %, the outlet valve was closed and the replacement gas was continuously injected into the pressure cell. The replacement process started once the desired pressure was reached and was monitored by taking a series of gas samples at specified time intervals; the gas samples were analyzed using a gas chromatograph. In this study, the experimental parameters of 3 runs for replacement are listed in Table 1.

Table 1

Experimental conditions for CH 4 –C 2 H 6 –C 3 H 8 hydrates replacement by CO 2 /N 2 .


Runs T/K CO 2 /N 2 Replacement Pressure /MPa <Gas Compositions (Mole Fraction, CH 4 /C 2 H 6 /C 3 H 8 ) Hydrate Saturation /% Water Saturation /% Replacement Time/Hour
Feed gas Hydrate
1 277.2 100/0 2.90 81.10/9.53/9.37 70.44/14.61/14.95 17.85 1.95 210
2 277.2 53.87/46.13 5.37 81.10/9.53/9.37 70.44/14.07/15.48 19.23 0.89 286
3 277.2 21.10/78.90 14.84 81.10/9.53/9.37 69.49/14.94/15.57 18.06 1.82 286

The replaced hydrates dissociation experiment was performed at the end of the replacement stage. The cell was depressurized rapidly to the atmospheric pressure. At the same time, the gas released from hydrates dissociation was collected in gas sample bags one by one through the ball valve group. The compositions of the gas phase in the sample bags were measured by a gas chromatograph.

3. Results and Discussion

Composition analysis of fluid phase

In order to examine the exchange behaviors of multiguests CH 4 , C 2 H 6 , and C 3 H 8 in hydrate cavities with CO 2 and N 2 , the compositions of the fluid phase under different experimental conditions were measured during replacement. As seen in Figure 2, the fluid composition became gradually decease in CO 2 /N 2 and rich in HC as the HC in hydrates were continuously released to the fluid phase during replacement. This indicated that CO 2 and N 2 molecules could substitute CH 4 , C 2 H 6 , and C 3 H 8 molecules entrapped in the cages of mixed hydrates in initial stage of swapping, which was also confirmed in the previous reports.

Figure 2

Composition changes in the vapor phase/ liquid phase during replacement at (a) run 1, (b) run 2, (c) run 3.

fig-2.jpg

In particular, the C 3 H 8 concentration was found to remain nearly constant after a rapid increase, implying that a small amount of C 3 H 8 in the mixed hydrates was displaced especially in the initial stage of swapping. This phenomenon is in accordance with the C 3 H 8 –CO 2 exchange behavior during the CH 4 +C 3 H 8 –CO 2 replacement in earlier investigation [15]. Earlier studies reported that the driving force of replacement was the gradient of the chemical potential between the hydrate phase and the surrounding phase [12]. The phenomenon in exchange features of C 3 H 8 is likely attributed to the difference in chemical potential of the C 3 H 8 molecules between the hydrate phase and the surrounding fluid after the rapid initial reaction.

To further investigate the roles of N 2 and CO 2 in the replacement reaction of SII hydrates, the time evolutions of N 2 and CO 2 consumed for the replacement are shown in Figure 3. As shown in Figure 3(a), when the mixed hydrates reacted with 53.87 mol % CO 2 and balanced N 2 gas mixture, the consumption of CO 2 for replacement was large in the early stage of replacement, while the consumption rate of N 2 nearly kept the constant. This indicated that CO 2 had a great replacement driving force at the initial stage of replacement, which could have a great contribution to the production of HC gases. As the replacement proceeded, the replacement driving force of CO 2 became smaller, and it was more difficult to participate in replacement reaction in the later period. As shown in Figure 3(b), when the mixed hydrates reacted with 21.10 mol % CO 2 and balanced N 2 gas mixture, unlike run 2, the consumption of CO 2 and N 2 for replacement was large in the early stage of replacement. This indicated that both CO 2 and N 2 had a great replacement driving force at the initial stage of replacement, and the thermodynamic effect of CO 2 and N 2 played an important role in the whole process of replacement, because N 2 had a higher partial pressure during run 3 than that during run 2.

Figure 3

Amount of CO 2 and N 2 consumed for hydrate replacement at 277.2 K: (a) run 2 and (b) run 3.

fig-3.jpg

Heterogeneous composition of the replaced hydrates

During the replacement, the parent- and ambient-gas molecules are diffusively transported across the mixed gas hydrate structure [17–21], resulting in the heterogeneous composition of the replaced gas hydrate particles with the continuous concentration changes of guest species along the radius of the replaced gas hydrate particles. As reported, hydrate decomposition occurs at the solid surface and follows a shrinking-core type pattern [22–24]. Therefore, in this study, the method of coupling gas production measurements with compositional analysis was put forward to investigate the heterogeneous composition of the replaced hydrates.

Figure 4 shows the evolution of the composition of different layers within the replaced gas hydrate particles. It can be observed that the fractions of HC components increased gradually along the radius of the replaced hydrate particles, accompanying a decrease of the CO 2 and N 2 fraction. This indicated that more HC molecules were substituted by CO 2 and N 2 molecules at the surface of replaced hydrates and the replacement efficiency of each hydrate layer decreased gradually from the surface to the core, which was attributed to the outer mixed-hydrate layers hindering the inbound and outbound transport of guest species. The different roles of the CO 2 /N 2 gas molecules in the replacement reaction could be more clearly observed in the composition changes across the replaced gas hydrate particle. As shown in Figure 4, the CO 2 concentration of each hydrate layer decreased faster from the surface to the core, while N 2 concentrations of different hydrate layers changed little. This meant that the surface mixed hydrates might hinder the diffusion of CO 2 molecules across the mixed gas hydrate structure and had almost no effects on N 2 molecules. The initial mole ratio of N 2 to CO 2 in gas phase of run 3 was about 4, but after replacement reaction it decreased to about 1 in different hydrates layers. A similar fractionation effect occurred also in run 3. This gives us an important information about the replacement reaction, implying that there is preferential occupancy of CO 2 in the hydrate cavities.

Figure 4

Composition changes of HC, CO 2 , and N 2 across the replaced gas hydrate particle: (a) run 1, (b) run 2, and (c) run 3.

fig-4.jpg

Replacement efficiencies of CH 4 -C 2 H 6 -C 3 H 8 hydrates

The guest-to-cavity size ratios of C 1 , CO 2 , C 2 , and C 3 in SI and SII hydrates indicating the preferential occupation of different cages by different guests [1] are listed in Table 2. C 3 H 8 molecules possess a sufficient enclathration power to be entrapped in SII-L, because the order of the guest-to-cavity size ratios for SII-L was C 3> C 2> CO 2> C 1> N 2 . Therefore, it is reasonably expected that during the replacement, the exchange of C 3 with CO 2 and N 2 in large cavities of SII hydrates could be accomplished more difficult than that of C 2 and C 1 in large cavities, when the SII hydrates go through SII-isostructural replacement.

Table 2

Ratios of molecular diameters to cavity diameters for some guest molecules [1].


Molecule Guest diameter/Å Structure I Structure II
5 12 5 12 6 2 5 12 5 12 6 4
N 2 4.1 0.804 0.700 0.817 0.616
CH 4 4.36 0.855 0.744 0.868 0.652
CO 2 5.12 1.00 0.834 1.02 0.769
C 2 H 6 5.5 1.08 0.939 1.10 0.826
C 3 H 8 6.28 1.23 1.07 1.25 0.943

In this study, we defined the replacement efficiency of each component as the ratio of the mole of each component in gas phase to the initial mole of each component in hydrate. The final replacement ratios of different HC in all experiments were measured by gas chromatograph (Figure 5). As shown in all experiments, the order of the replacement efficiencies of different HC was C 1> C 2> C 3 . The overall preferential exchange of C 2 H 6 than C 3 H 8 indicating SII-isostructural replacement played a major role, although the structural transformation into SI hydrate might occur during the replacement. In particular, all runs had the similar partial pressure of CO 2 , the replacement efficiency gradually decreased with the increase of N 2 concentration. Compared to previous reports on the replacement of CH 4 hydrate with external CO 2 /N 2 gas, the addition of N 2 in replacement gas could bring replacement efficiency down instead up, which might be attributable to differences in swapping patterns. The swapping pattern of the mixed hydrates by CO 2 /N 2 is shown in Figure 6. In run 1, the SII mixed hydrates at surface may transform into SI hydrates after the injection of CO 2 followed by a SII isostructural replacement occurred inside the particle. In runs 3 and 4, the SII mixed hydrates may mainly go through isostructural replacement. The hydrate structural transition from SII into SI that led to a markedly decrease of small cage fraction [11] would result in the release of HC to a large extent and enhance the extent of replacement. Since pure N 2 gas could react with water and form SII hydrates, the addition of N 2 in replacement gas might strengthen the stability of SII hydrate structure and lead to reduce the portion of SII hydrates transformed to SI hydrates.

Figure 5

Final replacement ratios for different conditions.

fig-5.jpg
Figure 6

Schematic illustration of the swapping pattern of CH 4 –C 2 H 6 –C 3 H 8 hydrates by CO 2 and CO 2 +N 2 .

fig-6.jpg

4. Conclusion

The replacement reaction occurred in mixed gas hydrates containing three guests CH 4 , C 2 H 6 , and C 3 H 8 in the presence of CO 2 /N 2 . The composition changes of gas phase indicated that CO 2 molecules preferably attacked CH 4 molecules compared to C 2 H 6 and C 3 H 8 molecules in hydrate phase, and only a small amount of C 3 H 8 in the mixed hydrates were displaced especially in the initial stage of swapping. Moreover, it can be concluded from the CO 2 and N 2 consumption for replacement and heterogeneous composition of the final replaced hydrates that CO 2 /N 2 played the different roles during the replacement reaction in different CO 2 concentrations. In particular, analysis of replacement efficiencies revealed that the addition of N 2 in replacement gas could cause the decrease in the replacement efficiency, which might be attributable to differences in swapping patterns.

Acknowledgements

The financial support for this research work was received from the National Natural Science Foundation of China (No. 51474112 and No.51506073).

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