Semi-opening type coal bed gas nitrogen dilated and liquefied process taking advantage of variable pressure for adsorbing residual pressure
A technology of pressure swing adsorption and coalbed methane, which is applied to the liquefaction process of coalbed methane and the field of semi-open coalbed gas nitrogen expansion liquefaction process, which can solve the problems that the energy saving effect of coalbed methane compression power consumption is not obvious, and achieve a significant energy saving effect and reduce The effect of liquefaction
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Embodiment approach 1
[0018] Implementation Option 1: If figure 1 As shown, the semi-open coalbed gas nitrogen expansion liquefaction process when the adsorption residual pressure is lower than 3MPa includes the following steps:
[0019] 1. The normal temperature CBM feed gas with pressure is deoxidized, desulfurized, decarbonized and dried in the pre-purification system 1;
[0020] 2. The pre-purified coalbed methane is enriched by pressure swing adsorption in the adsorber 2, and the concentrated coalbed methane with residual pressure nitrogen and normal pressure is separated;
[0021] 3. The concentrated coalbed methane is compressed to a medium pressure of 0.6-0.8 MPa by the primary compressor 3 and compressed by the secondary compressor 5 to be greater than or equal to 4.5 MPa, and is water-cooled in the first cooler 4 and the second cooler 6 respectively. room temperature;
[0022] 4. The high-pressure concentrated coal-bed methane is cooled into low-temperature concentrated coal-bed methane...
Embodiment approach 2
[0024] Implementation Option 2: If figure 2 As shown, the semi-open CBM nitrogen expansion liquefaction process when the adsorption residual pressure is higher than 3MPa includes the following steps:
[0025] Step 1, step 2 and step 3 are respectively the same as step 1 in embodiment 1, step 2 and step 3;
[0026] 4. The high-pressure concentrated coal-bed methane is cooled into low-temperature concentrated coal-bed methane in the heat exchanger 7. Part of the required cooling capacity is provided by the semi-open nitrogen expansion cycle, and the other part is provided by the cold gas separated from the gas-liquid separator. supply. The semi-open nitrogen expansion cycle is as follows: the nitrogen with excess pressure separated by adsorption is first expanded to 3MPa in the excess pressure nitrogen expander 16, and then compressed to 3MPa with the first-level nitrogen compressor 10 and the second-level nitrogen compressor 12 respectively. And the third cooler 11 and the f...
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