Device and method for recovering C2 from catalytic dry gas
A technology for recovering carbon and dry gas, applied in chemical instruments and methods, processing of gas mixtures, organic chemistry, etc., can solve the problems of high energy consumption, large investment, and affecting the purity of product gas and ethylene, and reduce equipment investment and energy consumption. consumption effect
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Embodiment 1
[0068] The second section of catalytic dry gas is compressed to 4MPaG and cooled to 15°C, and then mixed with carbon four (the flow rate is 41t / h (by the carbon four recycled in the step (4) and the newly added carbon four (the flow rate is 1.2t / h) h) maintain the constant flow rate)) contact, the conditions for C4 to contact with catalytic dry gas include: the number of theoretical plates is 40, the pressure is 3.6MPaG, the temperature at the top of the tower is 19°C, and the temperature at the bottom of the tower is 115°C; Conditions include: number of theoretical plates is 40, pressure is 2.1MPaG, tower top temperature is 63 ℃, and tower bottom temperature is 124 ℃; The aromatics (flow rate is 0.04t / h) maintains flow rate constant))) and the condition that coarse carbon dioxide contacts comprises: theoretical plate number is 35, and pressure is 2MPaG, and tower top temperature is 37 ℃, and tower bottom temperature is 80 ℃; Step ( 3) The remaining gasoline-containing compone...
Embodiment 2
[0070] The second section of catalytic dry gas is compressed to 3MPaG and cooled to 10°C, and then mixed with carbon four (the flow rate is 47t / h (by the carbon four recycled in the step (4) and the newly added carbon four (the flow rate is 1.2t / h) h) to maintain a constant flow rate)) contact, the conditions for C4 to contact with catalytic dry gas include: the number of theoretical plates is 25, the pressure is 3MPaG, the temperature at the top of the tower is 19°C, and the temperature at the bottom of the tower is 101°C; the conditions for the first rectification Including: the number of theoretical plates is 50, the pressure is 2.7MPaG, the temperature at the top of the tower is 59°C, and the temperature at the bottom of the tower is 136°C; Aromatics (flow rate is 1t / h) maintains flow rate constant)) and the condition of crude carbon dioxide contact comprises: theoretical plate number is 25, and pressure is 1.5MPaG, and tower top temperature is 34 ℃, and tower bottom temper...
Embodiment 3
[0072] The catalytic dry gas is compressed to 5MPaG in the second section and cooled to 15°C, and then mixed with carbon four (flow rate is 37t / h (by carbon four recycled in step (4) and newly added carbon four (flow rate is 1.2t / h) h) keep the flow rate constant)) contact, the conditions for C4 to contact with catalytic dry gas include: the number of theoretical plates is 50, the pressure is 4.2MPaG, the temperature at the top of the tower is 19°C, and the temperature at the bottom of the tower is 124°C; Conditions include: number of theoretical plates is 30, pressure is 2.7MPaG, tower top temperature is 59 DEG C, tower bottom temperature is 136 DEG C; The aromatics (flow rate is 1t / h) maintains flow rate constant))) and the condition of coarse carbon dioxide contact comprises: theoretical plate number is 43, and pressure is 2.5MPaG, and tower top temperature is 42 ℃, and tower bottom temperature is 101 ℃; Step ( 3) The remaining gasoline-containing components in the step (1)...
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