New technique for concentrating methane in oxygen-containing coal bed gas
A coal seam gas and new process technology, applied in the field of gas separation, to achieve the effect of simple equipment, reduced investment and operating costs, and reduced purification processes
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Embodiment 1
[0022] Example 1 , the process is as figure 1 As shown, the methane content of coal mine gas is 12%, the adsorption pressure is 0.02MPa.G, the adsorption temperature is 40°C, and the adsorption tower is equipped with adsorption CH 4 The adsorbent, the pressure swing adsorption device is carried out using safety facilities associated with the present invention, the vacant space of the adsorption tower is filled with explosion-suppressing materials, and the pipeline is filled with explosion-suppressing materials accounting for 1% of the pipeline volume. Pressure swing adsorption process such as figure 1 As shown, a VPSA process with single-column adsorption and two pressure equalizations is adopted. The gas compressed by the compressor enters the pressure swing adsorption system consisting of five adsorption towers from 181 to 185. Taking the adsorption tower 181 as an example for CH 4 Process integration of recycling systems figure 1 To illustrate.
[0023] 1. Adsorption...
Embodiment 2
[0045] Example 2, Process such as figure 2 As shown, the methane content of coal mine gas is 40%, the adsorption pressure is 0.7 MPa.G, the adsorption temperature is 30°C, and the adsorption tower is equipped with 2 Adsorbent. The pressure swing adsorption device is carried out with the safety facilities associated with the present invention. Explosion-suppressing materials are filled in the empty space of the adsorption tower, and explosion-suppressing materials accounting for 1% of the pipeline volume are installed in the pipeline. Pressure swing adsorption process such as figure 1 As shown, a VPSA process with single-column adsorption and two pressure equalizations is adopted. The gas compressed by the compressor enters the pressure swing adsorption system consisting of five adsorption towers from 181 to 185. Taking the adsorption tower 181 as an example to remove O from gas 2 , N 2 Process integration of recycling systems figure 2 To illustrate.
[0046] 1. ...
example 3
[0066] Example 3 , the process is as figure 1 As shown, the methane content of coalbed methane is 75%, the adsorption pressure is 1.0 MPa.G, and the adsorption temperature is 40°C. A single tower is used for adsorption, and the adsorption tower is equipped with adsorption CH 4 the adsorbent. This PSA device also adopts the safety facility associated with the present invention to carry out, and the empty place of adsorption tower is filled with explosion-suppressing material, and pipeline is filled with the explosion-suppressing material accounting for 1% of pipeline volume. The implementation of PSA technological process is as example 1.
[0067] This example can get CH 4 Content 95%, O 2 For products with a content of <0.5%, the yield of methane is 99.5%.
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