Method and device for improving pressure-swing-adsorption gas separation yield and purity
A pressure swing adsorption and gas separation technology, applied in separation methods, dispersed particle separation, chemical instruments and methods, etc. Small investment and small footprint, wide application effect
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Embodiment 1
[0022] This example is an example of using pressure swing adsorption to separate shift gas in methanol production.
[0023] Such as Figure 4 As shown, the conventional pressure swing adsorption system of the device in this embodiment is composed of 8 parallel-connected adsorption towers A1-A8 and two pressure equalization towers J1, J2, and the recovery system is composed of a compression mechanism 12. In the recovery system, the inlet of the compression mechanism 12 is directly connected to the recovery pipeline 10 at the top of each adsorption tower in the conventional pressure swing adsorption system, and the gas outlet of the compression mechanism 12 is directly connected to the product gas of the difficult-to-adsorb component of the conventional pressure swing adsorption system. 1 output pipeline 9 is connected.
[0024] A1
adsorption
A2
an average drop
Second to fourth average pressure drop
five average drop
Recycle
A3
Re...
Embodiment 2
[0037] This embodiment is an example of separating semi-water gas by pressure swing adsorption.
[0038] Such as Figure 5 As shown, the pressure swing adsorption system of the device in this embodiment is composed of five parallel-connected adsorption towers A1-A5, a vacuum buffer tank C, and four pressure equalizing towers J1, J2, J3, and J4, and the recovery system is composed of recovery The regulating valve V and the compression mechanism 12 are composed. In the recovery system, the inlet of the compression mechanism 12 is connected to the recovery pipeline 10 at the top of each adsorption tower in the conventional pressure swing adsorption system through the recovery regulating valve V, and the gas outlet of the compression mechanism 12 is directly connected to the pipeline 9 of the product gas 1 .
[0039] The raw material semi-water gas pressure of the present embodiment is gauge pressure 1.6MPa, and the pressure swing adsorption flow process that adopts is 5-1112-41...
Embodiment 3
[0052] This embodiment is an example of separating water gas by pressure swing adsorption.
[0053] Such as Figure 6 As shown, the pressure swing adsorption system of the device in this embodiment is composed of five parallel-connected adsorption towers A1-A5, a vacuum buffer tank C, and four pressure equalizing towers J1, J2, J3, and J4, and the recovery system is composed of recovery Regulating valve V is composed of sequentially connected compression mechanism 12 and air storage tank 13 . In the recovery system, the air inlet of the compression mechanism 12 is connected to the recovery pipeline 10 at the top of each adsorption tower in the conventional pressure swing adsorption system through the recovery regulating valve V, and the gas outlet of the compression mechanism 12 is connected to the air inlet of the gas storage tank 13. The gas outlet of the gas storage tank 13 is directly connected with the forward pressure pipeline 11 at the bottom of each adsorption tower i...
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