A method and equipment for deamination and recovery of propylene oxide and propylene in a propylene oxide plant
A technology for propylene oxide and deamination, which is used in chemical instruments and methods, purification/separation of hydrocarbons, hydrocarbons, etc., and can solve the requirements of continuous circulation, waste of propylene oxide, and negative pressure devices on equipment and pipeline systems It can reduce the generation of waste water and increase the anti-blocking performance.
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Embodiment 1
[0047] Get propylene oxide mixed gas (i.e. propylene oxide releases air), the main components are as follows: propylene oxide 75wt%, propylene 22wt%, ammonia 3wt%, with a flow rate of 2m 3 / h into the deamination adsorption tower 1, from top to bottom through 3A molecular sieve (the diameter of the 3A molecular sieve packing layer is 200mm, the length is 1000mm) for adsorption deamination, adsorption temperature 40 ℃, adsorption pressure 0.12MPa, the gaseous material after deamination is discharged from the outlet at the bottom of the deamination adsorption tower, the ammonia concentration in the material is reduced to 308ppm, and the deamination rate is 98.9%.
Embodiment 2
[0049] Take propylene oxide mixed gas, the main components are as follows: propylene oxide 75%wt, propylene 22%wt, ammonia 3%wt, with a flow rate of 2m 3 / h into the deamination adsorption tower 1, from top to bottom through the MgO-3A molecular sieve modified by MgO (molecular sieve filling diameter 200mm, length 1000mm) for adsorption deamination, adsorption temperature 40 ℃, adsorption pressure 0.12MPa, after deamination The gaseous material is discharged from the discharge port at the bottom of the deammonization adsorption tower, the ammonia concentration in the material is reduced to 153ppm, and the deammonization rate is 99.49%.
[0050] Wherein, MgO content is 5wt% in the MgO-3A molecular sieve, and MgO-3A molecular sieve is made by the following method: get 3A molecular sieve 10g, the Mg(NO of 0.4mol / L 3 ) 2 ·6H 2 O solution 35mL, impregnated 3A molecular sieve in Mg(NO 3 ) 2 ·6H 2 In O solution, ultrasonically oscillate for 2h, filter, and dry the precipitate at...
Embodiment 3
[0052] Take propylene oxide mixed gas, the main components are as follows: propylene oxide 75wt%, propylene 22wt%, ammonia 3wt%, with a flow rate of 2m 3 / h into the deammonization adsorption tower 1, passing through SiO from top to bottom 2 -3A molecular sieve (molecular sieve filling diameter 200mm, length 1000mm) for adsorption deamination, adsorption temperature 40 ℃, adsorption pressure 0.12MPa, the gaseous material after deamination is discharged from the outlet at the bottom of the deamination adsorption tower, and the ammonia concentration in the material is reduced To 112ppm, the deamination rate is 99.63%.
[0053] Among them, SiO 2 SiO in -3A molecular sieve 2 Content is 5wt%, SiO 2 -3A molecular sieve is prepared by the following method: take 10g of 3A molecular sieve, add 55mL of cyclohexane at 35°C, and then add 5mL of Si(OCH 3 ) 4 Impregnated at 35°C, ultrasonically oscillated for 2h, filtered, dried at 120°C for 24h, heated to 550°C under nitrogen protecti...
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