Energy recovery system and recovery method used in feeding section of acrylonitrile production process
A production process and energy recovery device technology, applied in the chemical industry, sustainable manufacturing/processing, hydrocarbon ammonia oxidation preparation, etc., can solve the problems of cold energy and pressure waste, achieve small energy loss and improve energy recovery and utilization rate Effect
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Embodiment 1
[0054] In this embodiment, the liquid raw material working medium is liquid propylene, the circulating working medium is propane, and the circulating working medium is dry fluid. The reaction raw material liquid propylene is sent from the spherical tank 1 through the first working medium pump 2 to the condensing evaporator 3 for constant pressure vaporization and superheating. In this embodiment, the vaporization pressure in the condensing evaporator 3 is 1.3 MPa; the saturated gaseous state Propylene enters the raw material working fluid expander 4 to expand and recover pressure energy, and the two-phase fluid with a pressure of about 0.35 MPa from the raw material working fluid expander 4 enters the superheater 5, and the superheated propylene enters the reactor 6 to participate in the reaction. The liquid propane coming out of the condensing evaporator 3 enters the second working medium pump 7, and the liquid propane coming out of the second working medium pump 7 is divided ...
Embodiment 2
[0056] In this embodiment, the liquid raw material working medium is liquid ammonia, the circulating working medium is ammonia, and the circulating working medium is wet fluid. The reaction raw material liquid ammonia is sent from the spherical tank 1 through the first working medium pump 2 to the condensing evaporator 3 for constant pressure vaporization. In this embodiment, the vaporization pressure of the liquefied ammonia in the condensing evaporator 3 is 1.2 MPa; after vaporization The saturated ammonia gas enters the raw material working fluid expander 4 to expand and recover pressure energy, and the two-phase fluid with a pressure of about 0.3 MPa from the raw material working fluid expander 4 enters the superheater 5, and the superheated ammonia gas enters the reactor 6 to participate in the reaction. The liquid ammonia coming out of the condensing evaporator 3 enters the second working medium pump 7, and the liquid ammonia coming out of the second working medium pump 7...
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