|
84
|
Fe3O4
|
CH4
|
20 |
0.2–1.6 g L−1
|
SDS-coated |
275.15 |
6 |
|
Compared with only SDS, the induction time was shorter and the gas consumption was higher |
|
34
|
Fe3O4
|
CO2
|
50 |
0.01–0.15 wt% |
Magnetic field |
274.15–276.15 |
3.01–4.06 |
CTAB |
Under the optimum conditions, the gas consumption increased by 443.9% and the induction time decreased by 96.6% |
|
85
|
Fe3O4
|
CH4
|
|
0.1 wt% |
SDS & SO-coated, magnetic field |
276.15 |
6 |
|
Shortening induction time and increasing gas storage capacity |
|
35
|
Fe3O4
|
CO2
|
50 |
0.05–0.25 wt% |
|
274.15, 276.15 |
2.5 |
SDS or CTAB |
0.15 wt% Fe3O4 nanoparticle and 400 ppm SDS in the based fluid is the best aqueous solution for CO2 hydrate formation, with a 70.6% decrement in induction time and a 160% increment in gas consumption |
|
35
|
CuO |
CH4
|
|
0.01–1 wt% |
|
275.65 |
5.5 |
SDS |
The induction time decreased by 92.7% and the gas storage capacity increased by 34% |
|
35
|
CuO |
CH4
|
40 |
0.05–1 wt% |
|
274.65, 276.65 |
5, 6 |
SDS |
There is no significant effect on the final gas storage capacity |
|
86
|
Cu |
CH4
|
25, 75 |
0.0157 M, 0.157 M |
|
275.15–275.76 |
5.24–5.55 |
CTAB |
Cu nanoparticles and CTAB can shorten the induction time, increase the reaction rate and increase gas consumption |
|
9
|
Cu |
HFC134a |
20 |
0.1 wt%, 1 wt% |
|
274.15 |
5.7 |
SDBS |
The rate of gas hydrate formation is increased and the dissociation pressure is changed |
|
87
|
ZnO |
CH4
|
10–30 |
0.05 wt%, 0.1 wt% |
|
274.65 |
4.9–6 |
SDS |
Positive effect on induction time, reaction rate, solubility of methane and gas consumption. But no significant effect on gas capacity |
|
88
|
ZnO |
CO2
|
11.5 |
0.1 wt% |
|
274 |
2.2, 2.6, 3.2 |
|
Increase the gas consumption by up to 16% |
|
89
|
Ag |
CH4
|
50–75 |
|
|
275.15 |
4.7, 5.7 |
|
The induction time was shortened by 85% and 73.9%, and the gas consumption was increased by 33.7% and 7.4%, respectively |
|
90
|
Ag |
CH4
|
6–30 |
4.5, 9, 18, 27, 36 μM |
Triangular silver nanoparticles |
275.15, 276.15 |
4.5,4.8,5,5.3,5.5 |
|
Induction time reduced by 97% |
|
91
|
Ag |
C2H6
|
6–30 |
4.5, 9, 18, 27, 36 μM |
|
276.15, 277.65 |
1.5,1.9,2.2 |
|
Induction time reduced by 97.5% |
|
36
|
Ag |
CO2
|
|
45, 90 μM |
|
273.65, 275.65 |
2, 3 |
SDS |
Ag nanoparticles + SDS can increase gas consumption and apparent rate constant |
|
92
|
Al2O3
|
CO2
|
|
0.1–0.6 wt% |
|
273.15 |
0.1 |
THF, SDS |
Under the optimum ratio of THF, SDS and Al2O3, the formation rate can be increased by 3.74 times |
|
93
|
Al2O3
|
CO2
|
30 |
0.005–0.5 wt% |
Non-modified, hydrophilic and hydrophobic |
275.15 |
4.5 |
|
Three kinds of particles have little effect on the phase equilibrium. The non-modified particles can shorten the induction time, but reduce the gas consumption. 0.01 wt% hydrophilic modification has better promoting effect, shortening induction time and increasing gas consumption |
|
21, 22
|
C |
CH4
|
10–15 |
0.003 wt%, 0.004 wt% |
Carbon nanotubes |
274.15 |
|
|
Carbon nanotubes can increase gas consumption by 300% and reaction rate, and oxidized carbon nanotubes are more effective at increasing rate. Both have a slightly positive effect on thermodynamic equilibrium |
|
37
|
C |
CO2
|
50 |
0.4 wt% |
Graphite nanoparticles |
277.15 |
3.5 |
|
Induction time was shortened by 80.8%, and the maximum air consumption was increased by 12.8% |
|
23
|
C |
CO2
|
50 |
0.4 wt%, 0.8 wt%, 1.2 wt% |
Graphite nanoparticles |
275.7–280.9 |
1.6–3.3 |
|
Graphite nanoparticles have an adverse effect on the phase equilibrium of CO2 hydrate formation, but it is independent of particle concentration |
|
94
|
C |
CH4
|
31.4 |
0.1–10 ppm |
Hydrophilic, hydrophobic carbon nanotubes |
275.15 |
4.6 |
|
The formation rate of hydrophobic carbon nanotubes was increased by 6% at high concentration and by 16.34% at low concentration |
|
38
|
GO |
CO2
|
|
20–300 ppm |
|
279 |
3–5 |
|
The induction time was shortened by 53–74.3%, the gas consumption increased by 5.1–15.9%, and the optimal concentration was 50 ppm |
|
95
|
SiO2
|
CH4
|
20–30 |
0.1–0.4 wt% |
Porous medium |
274.15 |
6 |
|
The concentration of 0.1–0.3 wt% has positive effect on the rate of hydrate formation, while the concentration of 0.4 wt% significantly inhibits hydrate formation |
|
96
|
Al2O3, SiO2, Cu, Ag |
75% CH4 + 25% CO2
|
<50, 10–20, 40–60, <150 |
0.1–0.3 wt% |
|
274.15 |
4 |
|
SiO2 can increase the gas consumption by the most, up to 45%, Cu and Al2O3 by 1–15%, and Ag has no significant effect |
|
97
|
Al2O3 + GO |
CH4
|
Al2O3: 10–20 |
0.2–0.6 wt% + 100–400 ppm |
|
281.15 |
3 |
THF |
The induction time was shortened and the reaction rate was increased, but the final gas consumption and gas reserves were not affected |