Natural gas purification system and method
A purification system and natural gas technology, applied in the field of natural gas, can solve problems such as lack of theory, and achieve the effects of real-time adjustment of parameters, increase of production rate, and optimization of parameters
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Embodiment 1
[0035] refer to figure 1 , is a structural schematic diagram of Embodiment 1 of the present invention, a natural gas purification system, comprising
[0036] Intake pipeline 1, one end of the intake pipeline 1 communicates with natural gas raw material gas;
[0037] The gas-liquid separator 2, the air inlet of the gas-liquid separator 2 communicates with the other end of the intake pipeline 1, and the sewage outlet of the gas-liquid separator 2 communicates with the sewage system through the sewage pipeline 17;
[0038] Absorption tower 3, the air inlet of absorption tower 3 is communicated with the outlet of gas-liquid separator 2 by pipeline, and the outlet of absorption tower 3 is communicated with downstream pipeline by absorption tower outlet pipeline 13;
[0039] A regeneration unit, the inlet of the regeneration unit is communicated with the drain of the absorption tower 3 through a pipeline, the gas outlet of the regeneration unit is communicated with the recovery sys...
Embodiment 2
[0045] Compared with Embodiment 1, the difference of this embodiment is that a regulator 9 is connected between the pipeline connected to the inlet of the absorption tower 3 and the pipeline connected to the outlet of the solution pump 8 .
[0046] In actual use: adjust the pressure at the inlet of the absorption tower 3 and the outlet of the solution pump 8 through the regulator 9 to ensure the stability of the inlet pressure of the absorption tower 3 .
Embodiment 3
[0048] Compared with Embodiment 1, the difference of this embodiment is that a circulator 12 is also connected to the pipeline connecting the outlet of the solution pump 8 with the absorption tower 3 .
[0049] In actual use: through the cooperation of the circulator 12 and the solution pump 8, the liquid-phase circulating solution generated by the regeneration unit is pumped into the absorption tower 3 for absorbing H 2 S and CO 2 .
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