The invention discloses a method for separating a
mixed gas FTrPSA in a reaction for preparing propylene by dehydrogenizing
propane. The method comprises the following steps: (1) taking a reactant
mixed gas in a
reaction zone for preparing the propylene by dehydrogenizing the
propane as a raw gas, and performing pre-treatment to obtain a raw gas A; (2) enabling the raw gas A to enter a medium-hightemperature PSA concentrating
system with the
operating temperature of 30 to 160 DEG C and the operating pressure of 0.2 to 4.0 MPa to obtain a
hydrogen-rich gas component and a C<2+>-rich concentrated gas; (3) directly using part of the
hydrogen-rich gas component as circulating
hydrogen required by a PDH
reaction zone, and enabling the other part of the hydrogen-rich gas component to enter a PSA hydrogen extracting process to obtain a product, namely, the hydrogen, wherein desorbed gas of the hydrogen is directly output as fuel; and (4) after the C<2+>-rich concentrated gas is cooled, compressed and subjected to gas-liquid separation, recycling C<2+> and forming a liquid to enter a PDH product
fractionation zone to obtain a propylene product, and returning the unreacted
propane to propane raw gas to mix and enter the PDH
reaction zone for reacting. Through the combination of the processes of performing pre-treatment, medium-high temperature PSA concentrating and PSA hydrogen extracting, the comprehensive
energy consumption is low, and the equipment is low in
investment cost and is safe.