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.

Active Publication Date: 2012-07-04
SICHUAN LESHAN FUHUA TONGDA AGRO-CHEM TECH CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] At present, the industrial production of dimethyl phosphite has been using the batch method of single-pot reaction and single-pot rectification. The reaction materials are fed through the high-level tank, and the measurement control is difficult, and the reaction needs to be controlled below 55°C. , frequent operations, high labor intensity, long production cycle and low equipment capacity
At the same time, the heat of reaction needs to be removed by freezing during the reaction process, and the material needs to be heated during deacidification, so the energy utilization rate in the production process is low

Method used

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  • Production method of dimethyl phosphite
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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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Abstract

The invention relates to a production method of dimethyl phosphate, which takes phosphorus trichloride and methyl alcohol as raw materials for reaction. The method comprises the steps of: in a reaction chamber space having cross injection angle and the injection structures of the raw materials, respectively and continuously injecting and sending the phosphorus trichloride and the methyl alcohol which are based on the molar ratio of 1: (3.0-3.1) into the reaction chamber space through respective injection structures by corresponding pumping mechanisms for mixing together and reaction; then, introducing reaction material into a centrifugal cyclone separator with the pressure lower than that of the reaction chamber space along the tangential direction, and leading noncondensable gas and condensing liquid product to have centrifugal cyclone separation; and collecting the liquid dimethyl phosphate product descending along the inner wall of the centrifugal cyclone separator. The method canrapidly complete the reaction and the separation for products, effectively reduces the contact between HCl and the dimethyl phosphate, inhibits the occurrence of side reaction, improves the yield andthe quality of the product, and greatly reduces the energy consumption.

Description

technical field [0001] What the present invention relates to is a kind of production method of improved dimethyl phosphite. Background technique [0002] Dimethyl phosphite is an important product in fine chemical industry. It is not only an intermediate for the production of glyphosate, trichlorfon, rice blast, omethoate and other pesticides, but also a raw material for organophosphorus corrosion inhibitors, dye additives, plastic additives and flame retardants, and can be used for synthetic water treatment It can also be used as a methylating agent to synthesize quaternary ammonium salt fungicides, antistatic agents, softeners and other products. [0003] Dimethyl phosphite is generally produced by reacting phosphorus trichloride and methanol in industry: [0004] PCl 3 +3CH 3 OH→(CH 3 O) 2 POH+2HCl↑+CH 3 Cl↑ [0005] The reaction process and mechanism are: [0006] PCl 3 +CH 3 OH→CH 3 OPCl 2 +HCl↑ (1) [0007] CH 3 OPCl 2 +CH 3 OH→(CH 3 O) 2 PCl+HCl↑ (2...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07F9/142B01J19/26
Inventor 蒋文伟晏加一吴世见姜永红李晶晶杨国华杨琴姜林罗芩
Owner SICHUAN LESHAN FUHUA TONGDA AGRO-CHEM TECH CO LTD
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