Pressure swing absorption decarbonization process and apparatus
A technology of pressure swing adsorption and decarbonization, which is applied to the separation of dispersed particles, hydrogen separation, and hydrogen separation using solid contact, which can solve problems such as pollution, increased energy consumption, and increased difficulty in vacuuming and desorption of the system, so as to reduce energy consumption, The effect of improving utilization rate and reducing difficulty
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Embodiment 1
[0055] See Figure 4, this process is 6000Nm 3 / h pressure swing adsorption decarburization process
[0056] This process flow is to produce liquid alcohol, and the CO of the product gas decarbonized by pressure swing adsorption 2 The content is 0.2%. The system consists of six adsorption towers. During the operation of the device, there are two adsorption towers for adsorption at the same time. The two adsorption towers are evacuated at the same time, and the pressure is equalized twice, which is referred to as the 6-2-2-2 / V process. Each adsorption tower has to go through in one cycle: adsorption (A), first pressure equalization drop (E1L), second pressure equalization drop (E2L), recovery (RP), vacuum pumping (CU), first pressure equalization There are nine steps including pressure rise (E1R), pressure second equalization rise (E2R), reverse charge (RRL), and final charge (RL).
[0057] Taking the working condition of tower A going through nine steps in one cycle as an ex...
Embodiment 2
[0079] This embodiment is: referring to Fig. 5, this technological process is 15000Nm 3 / h pressure swing adsorption decarburization process
[0080] This process is the production of co-alcohol, pressure swing adsorption decarburization product gas CO 2The content is 0.5% to 1%. The system consists of eight adsorption towers. During the operation of the device, there are three adsorption towers for adsorption at the same time, two adsorption towers are evacuated at the same time, and the pressure is equalized three times, referred to as 8-3-2-3 / V process. Each adsorption tower has to go through in one cycle: adsorption (A), pressure first equilibrium drop (E1L), pressure second equilibrium drop (E2L), pressure third equilibrium drop (E3L), recovery (RP), pumping Vacuum (CU), pressure first equalization rise (E1R), pressure second equalization rise (E2R), pressure third equalization rise (E3R), reverse charge (RRL), final charge (RL) and other eleven steps sequence.
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