Propane dehydrogenation reaction product cascade refrigeration separation system and method
A cascading refrigeration and reaction product technology, applied in cold treatment separation, refrigeration and liquefaction, sustainable manufacturing/processing, etc., can solve problems such as high equipment speed, increased PSA separation load, economic loss, etc., to save system energy consumption , avoid economic loss, improve the effect of hydrogen purity
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Embodiment 1
[0067] like figure 1 A cascade refrigeration and separation system for propane dehydrogenation reaction products shown, the system includes a multi-stage cooling flash separation unit 1, a liquid product pressurization conveying unit 2 and a cascade refrigeration cycle unit 3, wherein the multi-stage cooling flash evaporation The separation unit 1 is respectively connected with the liquid product pressurized conveying unit 2 and the cascade refrigeration cycle unit 3 .
[0068] The multi-stage cooling flash separation unit 1 includes heat exchangers 101 / 102 / 103 / 104 / 105 for step-by-step cooling, and regulating valves 106 / 107 / for step-by-step distribution of fresh propane (feed 2). 108 / 109 / 110, regulating valve 111 for adjusting the proportion of hydrogen in the combined reaction feed (outlet 2), separator 112 / 113 / 114 / 115 / for the step-by-step flash separation of the cooled reaction product gas 116. Regulating valves 117 / 118 / 119 / 120 / 121 for regulating the flow of liquid produc...
Embodiment 2
[0081] Different from embodiment 1, the method for cascade refrigeration separation of propane dehydrogenation reaction product comprises the following steps:
[0082] (a) The reaction product (Feed 1, The temperature was 60 °C, the pressure was 1.4 MPaG) and fresh propane (Feed 2) containing components such as hydrogen (1 mole.%), ethane (2 mole.%), propylene (2 mole. , the temperature is 45°C, the pressure is 2.0MPaG) as a hot fluid into the primary heat exchanger 101, and part of the cooled fresh propane (feed 2, temperature is -21°C) passes through the first regulating valve 106 and comes from the secondary exchange The combined feed (outlet 2, temperature of -24°C) of the heat exchanger 102 enters the primary heat exchanger 101 as a cold fluid after mixing, and the remaining part enters the secondary heat exchanger 102; the dry gas product (outlet 3, temperature -24°C), flash steam (outlet 4, temperature -24°C) and liquid product (outlet 1, temperature -24°C) in primary ...
Embodiment 3
[0091] Adopt the same kind of propane dehydrogenation reaction product cascade refrigeration separation system and method as in Example 1, the implementation method and steps are the same as in Example 1, the reaction product (feed 1, containing hydrogen (35 mole.%), methane ( 2 mole.%), ethane (2 mole.%), propylene (18 mole.%), propane (43 mole.%) and other components.
[0092] Finally, the present embodiment obtains a liquid product that meets the requirements of the separation process (discharge 1, the temperature is 30 ° C, the pressure is 3MPaG, wherein the hydrogen content is not more than 0.1 mole.%); combined feed (discharge 2, the temperature is 30 ℃, pressure is 0.3MPaG), dry gas product (discharge 3, temperature is 30℃, pressure is 0.4MPaG, wherein the content of propylene and propane is not more than 0.03 mole.%, the purity of hydrogen is not less than 96 mole.%), flash Steam (outlet 4, temperature is 30°C, pressure is 0.1MPaG), the recovery rate of C3 in the liqui...
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