Method for preparing 2-propenyl ethanoate by using propylene gas phase oxidation method
A gas-phase oxidation and allyl acetate technology, which is applied in the preparation of carboxylic acid esters, preparation of organic compounds, chemical instruments and methods, etc., can solve the problems of low space-time yield and selectivity, low single-pass conversion rate of propylene and acetic acid, etc. , to achieve the effect of improving space-time yield and selectivity, and improving single-pass conversion rate
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Embodiment 1
[0018] use as figure 1 The shown propylene gas-phase oxidation method prepares the fixed-bed vertical pipe reactor of allyl acetate, the diameter of the reactor is 32mm, the height is 800mm, the catalyst loading capacity is 6L, the catalyst particle diameter is 3-6 millimeters, and the palladium content in the catalyst is 3.36 g / L, the copper content is 0.48g / L, and the potassium acetate content is 48g / L. The feed ratio of raw materials is: propylene / acetic acid / oxygen / water=72.0 / 6.0 / 6.0 / 16.0 (molar ratio), and the space velocity is 2000hr -1 . During the reaction process, the catalyst reaction temperature was controlled to be 160° C., and the reactor inlet pressure was 0.7 MPa. Propylene, acetic acid, oxygen and water are fed after being mixed in the preheater. According to the oxygen content analysis result of the online analysis port, supplement the oxygen content to 4% through the oxygen supplement port. The composition of the reaction product was analyzed by gas chrom...
Embodiment 2
[0020] The palladium content in the catalyst is 9.12g / L, the copper content is 1.92g / L, and the potassium acetate content is 72g / L. The feed ratio of raw materials is: propylene / acetic acid / oxygen / water=69.0 / 8.0 / 5.0 / 18.0 (molar ratio), and the space velocity is 2500hr -1 . During the reaction process, the catalyst reaction temperature was controlled to be 170° C., and the reactor inlet pressure was 0.8 MPa. Propylene, acetic acid, oxygen and water are fed after being mixed in the preheater. According to the oxygen content analysis result of the online analysis port, supplement the oxygen content to 3% through the oxygen supplement port. Other conditions are with embodiment 1.
Embodiment 3
[0022] According to the oxygen content analysis result of the online analysis port, supplement the oxygen content to 6% through the oxygen supplement port. Reactor, reaction conditions and catalyzer are with embodiment 1. Due to the large amount of oxygen supplementation, the side reactions increase and the selectivity decreases significantly, so the supplementation of oxygen should not be too much.
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