Continuous isosynthesis method and continuous isosynthesis device of ethylidene norbornene
A technology for ethylidene norbornene and isomerization synthesis, which is applied in the chemical industry and can solve the problems such as the inability to solve the continuous removal of waste catalysts, the inability to solve the deactivation of catalysts in contact with water, and the inability to efficiently utilize catalysts.
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[0032] In a first aspect of the present invention, a continuous isomerization synthesis method of ENB is provided, the method comprises the following steps:
[0033] (a) The reactors at all levels are connected in series, and the circulating materials of the reactors are pumped from the bottom of the reactors through the circulating pump after exchanging heat through the heat exchanger;
[0034] (b) The interstage cyclone separator realizes the continuous separation of interstage materials, the materials flow continuously from the first stage reactor to the last stage reactor, and the catalyst continuously flows from the last stage reactor to the first stage reactor Flow, so that the material and the catalyst are in reverse contact;
[0035] (c) The heat exchanger controls the temperature rise in the reactor through the heat exchange effect on the circulating material, so as to maintain the optimum operating temperature of the reactor temperature at 10-20°C;
[0036] (d) The ...
Embodiment 1
[0065] In a 15,000-ton / year ENB isomerization synthesis device, according to the catalyst efficient utilization method and device in the ENB isomerization synthesis of the present invention, to maximize the efficient utilization of the catalyst, while playing a role in the output of all levels and the final product Purification and removal of spent catalyst while the unit is in continuous operation. Its specific operation process and effects are described as follows:
[0066] 1. Operating conditions
[0067] The device adopts 4-stage series ebullating bed reactors, and the reaction volume of a single unit is 7.6m 3 , The filling coefficient is 79%. The reactor operates continuously, the residence time of a single reactor of materials is more than 1 hour, and the overall residence time is more than 4 hours. The first-stage reactor feeds 2.1t / h, the last-stage reactor discharges 1.875t / h, and the catalyst feeds 0.062t / h. The cyclone separator between each stage is composed o...
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