Method using fluidized bed to synthesize methyl phosphonic dichloride
A technology for synthesizing methyl phosphine dichloride and methyl phosphine dichloride, which can be used in chemical instruments and methods, compounds of Group 5/15 elements of the periodic table, organic chemistry, etc., and can solve the problem of high solvent consumption and dangerous operation It can solve the problems of high stability and unstable complex intermediates, and achieve the effect of continuous production, improved product purity and low cost of raw materials.
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Embodiment 1
[0023] Firstly, nitrogen gas with a pressure of 0.2MPa is passed into the reaction system, phosphorus trichloride and additives are mixed with methane in the presence of nitrogen gas, mixed through a heat exchanger and a mixing preheater, and preheated to 250°C, and passed through at a certain flow rate. A fluidized bed reactor loaded with catalyst, wherein the molar ratio of methane to phosphorus trichloride is 8:1, the reactor temperature is controlled at 350°C, the reactor pressure is controlled at 0.03MPa, and the residence time is 0.6s. After the first-stage condensation, the liquid containing 14% MDP is collected, and the non-condensable gas after passing through the first and second-stage condensers is absorbed by the water washing alkali washing tower, then enters the drying tower for drying, and re-enters the reaction system after removing impurities by pressure swing adsorption. The collected methylphosphine dichloride liquid is sent to a rectification tower with a th...
Embodiment 2
[0025] Firstly, argon gas with a pressure of 0.3 MPa is introduced into the reaction system, and phosphorus trichloride and additives are mixed with methane in the presence of argon gas through a heat exchanger and a mixing preheater and preheated to 250°C. The flow rate passes through a fluidized bed reactor loaded with catalyst, wherein the molar ratio of methane to phosphorus trichloride is 4:1, the temperature of the reactor is controlled at 450°C, the pressure of the reactor is controlled at 0.02MPa, and the residence time is 0.5s. 1. After the secondary condensation, the liquid containing 13% MDP is collected. After passing through the primary and secondary condensers, the non-condensable gas is absorbed by the water washing and alkali washing tower, then enters the drying tower for drying, and re-enters the reaction system after removing impurities by pressure swing adsorption. , the post-treatment of methylphosphine dichloride is the same as above, and the obtained cont...
Embodiment 3
[0027] Firstly, nitrogen gas with a pressure of 0.3MPa is passed into the reaction system, phosphorus trichloride and additives are mixed with methane in the presence of nitrogen gas, mixed through a heat exchanger and a mixing preheater and preheated to 300°C, and passed through at a certain flow rate. A fluidized bed reactor loaded with catalyst, in which the molar ratio of methane to phosphorus trichloride is 6:1, the temperature of the reactor is controlled at 450°C, the pressure is controlled at 0.1MPa, and the residence time is 0.8s. After primary and secondary condensation Finally, the liquid containing 15% MDP is collected, and the non-condensable gas after passing through the primary and secondary condensers is absorbed by the washing and alkali washing tower, then enters the drying tower for drying, and re-enters the reaction system after removing impurities by pressure swing adsorption. The post-treatment of phosphine chloride is the same as above to obtain phosphoru...
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