Method for purifying natural gas
A purification method and natural gas technology, applied in separation methods, chemical instruments and methods, gas fuels, etc., can solve the problems of high energy consumption, large methane gas loss, environmental pollution, etc., achieve high separation efficiency, and increase the gas-liquid contact area , The effect of simple process
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Embodiment 1
[0031] Take a gas sample, where CH 4 , CO 2 and H2 The molar ratios of S are 90.5%, 8.1% and 1.4%, respectively. After pressurization to 10MPa, it is passed into the ionic liquid absorption chamber. The ionic liquid is 1-ethyl-3-methylimidazolium hexafluorophosphate ([EMIm]PF 6 ), the temperature of the ionic liquid absorption chamber was controlled at 300K. After entering the hydrate reaction kettle, keep the pressure in the kettle at 2.5MPa and the temperature at 273K. After 24 hours of reaction, the analysis of gas chromatography shows that CH in the gas 4 The content is 96.5%, CO 2 The content is 2.9%, H 2 The S content is 0.6%.
Embodiment 2
[0033] Adopt the same gas sample as in Example 1 to pressurize to 4MPa and then pass into the ionic liquid absorption chamber, and the ionic liquid adopts 1-hexyl-3-methylimidazolium hexafluorophosphate ([HMIm]PF 6 ), the temperature of the ionic liquid absorption chamber was controlled at 275K. After passing through the ionic liquid absorption chamber, the gas enters the hydrate reaction kettle through the gas booster pump, and the pressure inside the kettle is kept at 3.0MPa, and the temperature is 273K. After 24 hours of reaction, the gas chromatography analysis results show that CH in the gas 4 The content is 97.1%, CO 2 The content is 2.4%, H 2 The S content is 0.5%.
Embodiment 3
[0035] Change the ratio of the initial gas components, using CH 4 , CO 2 and H 2 Natural gas with S molar ratios of 85.5%, 10.1% and 4.4%, respectively, is pressurized to 3MPa and then passed into the ionic liquid absorption chamber. The ionic liquid is 1-ethyl-3-methylimidazolium tetrafluoroborate ([EMIm] BF4), the temperature of the ionic liquid absorption chamber was controlled at 280K. After passing through the ionic liquid absorption chamber, the gas enters the hydrate reactor through the gas booster pump, and the pressure of the hydrate reactor is kept at 3.5MPa and the temperature is 275K. After 24 hours of reaction, gas chromatography analysis results showed that CH in the gas 4 The content is 92.4%, CO 2 The content is 5.0%, H 2 The S content is 2.6%.
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