Gas hydrate preparation method using phase-change heat transfer of oil wrapped water emulsion
A water-in-oil emulsion and gas hydrate technology, which is applied in the direction of gas fuel, lighting and heating equipment, liquefaction, etc., can solve the problems of unadjustable temperature, uneven temperature, agglomeration of ice and hydrate particles, etc., and achieve the improvement of hydrate Generation rate and relative gas storage capacity, increased hydration rate, effect of increased hydration rate
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Embodiment 1
[0028] Select the oil phase n-hexane and n-heptane, deionized water, surfactant span80 and tween80 to make a mixed solution containing 74.0wt% oil phase, 25wt% water, and 1.0wt% surfactant, wherein the mass ratio of n-hexane and n-heptane is 11:9, and the mass ratio of span80 and tween80 is 0.783:1. The mixture was then kept at 30°C for 30 minutes. Then use a high-speed shearing machine to break the water phase into water droplets of 0.5 μm to 20 μm and disperse them in the oil phase to form an emulsion with good stability. The cooling method is used to cool down the emulsion, and after the water in the emulsion is partially or completely solidified into ice, the temperature is kept constant. The ice-containing slurry thus formed is fully contacted with methane gas and hydrated at 6.0 MPa. The hydration temperature is close to the freezing point of the water phase and maintained at -3°C-0°C. The consumption rate of methane gas is 0.012g / min / mLH 2 O.
Embodiment 2
[0030]Select the oil phase n-heptane, deionized water, surfactant span80 and tween80 to make a mixed liquid containing 62.5wt% oil phase, 35wt% water, and 2.5wt% surfactant, wherein the mass ratio of span80 and tween80 is 0.783:1 . The mixture was then kept at 30°C for 30 minutes. Then use a high-speed shearing machine or similar dispersing equipment to break the water phase into 20-50 μm water droplets and disperse them in the oil phase to form a stable emulsion. The cooling method is used to cool down the emulsion, and after the water in the emulsion is partially or completely solidified into ice, the temperature is kept constant. The ice-containing slurry thus formed was fully contacted with ethane gas and hydrated at 2.0 MPa. The hydration temperature is close to the freezing point of the water phase and maintained at -3°C-0°C. The consumption rate of ethane gas is 0.019g / min / mLH 2 O.
Embodiment 3
[0032] Select the oil phase dispersant n-hexane, deionized water, surfactant span80 and tween80 to make a mixture of oil phase 49.6wt%, water 45wt%, surfactant 5.4wt%, the mass ratio of span80 and tween80 is 0.783:1 . The mixture was then kept at 30°C for 30 minutes. Then use a high-speed shearing machine or similar dispersing equipment to break the water phase into 50-100 μm water droplets and disperse them in the oil phase to form an emulsion with good stability. The cooling method is used to cool down the emulsion, and after the water in the emulsion is partially or completely solidified into ice, the temperature is kept constant. The ice-containing slurry thus formed was fully contacted with carbon dioxide gas and hydrated at 3.0 MPa. The hydration temperature is close to the freezing point of the water phase and maintained at -3°C-0°C. The consumption rate of carbon dioxide gas is 0.015g / min / mLH 2 O.
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