Customization: | Available |
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After-sales Service: | Guide Installation and Operation Training |
Warranty: | 12 Months |
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The raw biogas is first pressurized to the design pressure by a biogas compressor and then enters the decarbonization unit for pre-treatment, including dehydration, oil removal, and particulate separation. When the various indicators of the incoming gas meet the design standards of the membrane separation unit, it enters the membrane separation system. The membrane separation unit can be divided into a two-stage system and a three-stage system according to the CH4 recovery rate requirements of the product gas.
In the two-stage membrane separation process: the retentate from the first-stage membrane enters the second-stage membrane for further filtration to increase methane purity. The retentate from the second-stage membrane is output as product gas, while the permeate from the first-stage membrane is discharged as tail gas. The permeate from the second-stage membrane is recycled back into the process to improve methane recovery.
In the three-stage membrane process: the retentate from the first-stage membrane enters the second-stage membrane for further filtration to increase methane purity. The retentate from the second-stage membrane is output as product gas, while the permeate from the first-stage membrane enters the third-stage membrane system. The permeate from the third-stage membrane is discharged as tail gas. The permeate from the second-stage membrane and the retentate from the third-stage membrane are recycled back into the process to improve methane recovery.
Item | Parameters | ||
Standard Code |
GB 17820 Level 1 |
GB 17820 Level 2 |
GB 18047 |
Higher Calorific Value /(MJ/m3) |
≥31.4 | ≥31.4 | ≥31.4 |
()Total Sulfur /(mg/m3) |
≤20 | ≤100 | ≤100 |
H2S/(mg/m3) | ≤6 | ≤20 | ≤20 |
CO2 mol:mol /(%) | ≤3.0 | ≤4.0 | ≤4.0 |
O2 mol:mol /(%) | / | / | ≤0.5 |
Remark: The standard reference conditions for gas volume are 101.325kPa and 20ºC. |