A method for desulfurization and light hydrocarbon removal from natural gas by using ionic liquid
An ionic liquid and natural gas technology, applied in the field of desulfurization and desulfurization of light hydrocarbons, can solve the problem of no separation effect of light hydrocarbon components, and achieve the effects of low saturated vapor pressure, simplified process route and high separation efficiency.
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Embodiment 1
[0038] Absorbent composition: [P 4444 ][C 5 h 11 COO] Tetrabutylphosphonium n-hexanoate pure ionic liquid absorbent. Raw natural gas composition (molar ratio): methane 79.8%, ethane 1.9%, propane 7.6%, butane 5.6%, hydrogen sulfide 1.1%, sulfide 305mg / m 3 , Mercaptan 421mg / m 3 and other components.
[0039] The raw natural gas is pressurized to 1.0MPa through the compressor, and the temperature is lowered to 15°C by cooling, and it is passed into the bottom of the absorption tower, and the absorbent is added to the top of the absorption tower to ensure that most of the C 2 ~C 4 Hydrocarbons and organic sulfides are absorbed, and the C-rich 2 ~C 4 Absorption liquid of hydrocarbons and organic sulfides, methane-rich gas and a small amount of almost insoluble H in the absorbent are obtained at the top of the tower 2 , CO, N 2 Wait for gas.
[0040] The absorption liquid at the bottom of the tower enters the light hydrocarbon desorption tower, adopts the method of temper...
Embodiment 2
[0042] Absorbent composition: [N 4444 ][C 7 h 15 COO] tetrabutylammonium octanoate pure ionic liquid absorbent. Raw natural gas composition (molar ratio): 81.5% methane, 8.5% ethane, 8.5% propane, 5.1% butane, 1.0% hydrogen sulfide and other components.
[0043] As in Example 1, the raw natural gas and the absorbent are contacted and absorbed in countercurrent at 5°C and 2.5 MPa, and the light hydrocarbon components are desorbed by the absorption liquid at a temperature of 50°C. Hydrogen sulfide is desorbed at 0.1MPa, and the absorbent is recovered and recycled at the bottom of the tower. Hydrogen sulfide removal rate: 97.6%, ethane removal rate: 91.4%, propane removal rate: 95.2%, butane removal rate: 97.7%.
Embodiment 3
[0045] Absorbent composition: [bmpyrr][Bu 2 PO 4 ] N, N-butyl methylpyrrolidone phosphate dibutyl ionic liquid, N-methylpyrrolidone mixed absorbent, the ionic liquid accounts for 95% (volume fraction). Raw natural gas composition (molar ratio): methane 88.2%, ethane 5.9%, propane 2.0%, butane 0.9%, hydrogen sulfide 1.2% and other components.
[0046] As in Example 1, the raw natural gas and the absorbent are contacted and absorbed in countercurrent at 10°C and 1.8 MPa, and the light hydrocarbon components are desorbed by raising the temperature of the absorbing liquid at 55°C, and the absorbing liquid is then desorbed through a sulfide desorption tower at 85°C and 85°C. Hydrogen sulfide is desorbed at 0.05MPa, and the absorbent is recovered and recycled at the bottom of the tower. Hydrogen sulfide removal rate: 97.5%, ethane removal rate: 92.1%, propane removal rate: 96.7%, butane removal rate: 97.1%.
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