Production method of dimethyl phosphite
A technology of dimethyl phosphite and production method, which is applied in chemical instruments and methods, compounds of elements of Group 5/15 of the periodic table, chemical/physical/physical-chemical nozzle reactors, etc. It is difficult to control, labor-intensive and other problems, so as to shorten the reaction time, improve the effective conversion rate, and avoid the side reaction of acid hydrolysis.
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Embodiment 1
[0029] exist figure 1 In the shown device, methanol 810kg / h and phosphorus trichloride 1160kg / h are respectively metered by their respective metering pumps 1 and then continuously sprayed into the reaction tank with a high-pressure nozzle 2 at an angle of 70°. Reaction chamber space 3 of extension tube and cooling jacket structure. Under the action of the injection of the high-pressure nozzle 2, the pressure of the raw material entering the chamber space 3 of the reaction section is controlled at a gauge pressure of -0.085 to -0.090 MPa. Collide and mix with each other in a spray mode, and make the reaction materials enter the centrifugal cyclone (wind) separator 4 with a pressure of -0.090~0.092 (gauge pressure) along the reaction extension pipe at a speed of 8.5m / s along the tangential direction. Separation of liquid phase product dimethyl phosphite crude product and non-condensable gases such as HCl and methyl chloride at ~70°C. In the dimethyl phosphite crude product obt...
Embodiment 2
[0031] by two such as figure 1The same device of the structure shown constitutes a two-stage reaction scheme. The raw materials are 890kg / h of methanol and 1257kg / h of phosphorus trichloride, and after being metered by respective metering pumps 1, the full amount of phosphorus trichloride and 594kg of methanol are sprayed into the reaction chamber space 3 of the first-stage device. The included angle of the jet stream is 120°. The pressure of the primary reaction device is controlled at gauge pressure -0.075~-0.080MPa, the reaction temperature is controlled at 48~50°C, the speed of entering the cyclone (wind) separator is 5.5m / s, and the inner temperature of the cyclone separator is controlled at 75±1°C. The gauge pressure of the second-stage reaction device is -0.085~-0.090MPa, the included angle of the jet flow is 90°, the reaction temperature is 50~53°C, the velocity entering the cyclone (wind) separator is 7.5m / s, and the inner temperature of the cyclone separator Contro...
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