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A kind of production method of diethyl ethyl phosphonate

A technology of diethyl ethyl phosphonate and a production method, which is applied in the production field of diethyl ethyl phosphonate, can solve problems such as long process reaction time, pollute the environment, and low conversion rate, and achieve high product yield, The effect of high conversion rate and short production cycle

Active Publication Date: 2015-09-23
南京晨化新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The disadvantages of the prior art are: the reaction time of the process is long, and there are still unreacted low boilers generated, so that the conversion rate of the product is relatively low, and the treatment of low boilers not only increases the cost, but also pollutes the environment

Method used

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  • A kind of production method of diethyl ethyl phosphonate
  • A kind of production method of diethyl ethyl phosphonate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] The production method of this diethyl ethyl phosphonate is to take triethyl phosphite as main raw material, with iodine as catalyzer, and its production steps are as follows:

[0030] The first step: start the vacuum pump, open the vacuum valve on the reaction kettle, and use negative pressure to pump 2000kg of triethyl phosphite into the reaction kettle; close the vacuum valve, open the vent valve, and then add 6kg of iodine catalyst from the catalyst feeding port;

[0031] Step 2: Close the vent valve, turn on the agitator, and open the return pipe valve;

[0032] The third step: pass steam to the jacket of the reaction kettle to raise the temperature, and heat the material to 135°C±5°C to promote the positive reaction; at the same time, open the reflux condenser to condense the steamed gas;

[0033] Step 4: After the evaporated gas is condensed, it flows back into the reaction kettle from the reflux pipe. After the reflux flow is stable, stop heating, and the tempera...

Embodiment 2

[0040]The production method of this diethyl ethyl phosphonate is to take triethyl phosphite as main raw material, with iodine as catalyzer, and its production method comprises the steps:

[0041] The first step: Start the vacuum pump, open the vacuum valve on the reactor, and use negative pressure to pump 2000kg of triethyl phosphite into the reactor; close the vacuum valve of the reactor, open the vent valve, and then add 2kg of iodine from the catalyst feeding port catalyst;

[0042] Step 2: Turn on stirring and open the return pipe valve; the return pipe valve is installed on the return pipe set on the top of the reactor, and the upper end of the return pipe is respectively connected to the gas inlet and condensate outlet of the reflux condenser; the condensate can be refluxed through the return pipe into the reactor;

[0043] The third step: pass steam to the jacket of the reaction kettle to raise the temperature, and heat the material to 135°C±5°C to promote the positive...

Embodiment 3

[0050] A kind of production method of diethyl ethyl phosphonate is characterized in that comprising the following steps successively:

[0051] 1) Add 1000kg of triethyl phosphite and 2kg of catalyst iodine into the closed reaction kettle;

[0052] 2) Stir the materials in the reactor and open the return pipe valve. The return pipe valve is installed on the return pipe provided on the top of the reaction kettle, and the upper end of the return pipe is respectively connected to the gas inlet and the condensate outlet of the reflux condenser;

[0053] 3) Heat the material in the reactor to 135°C±5°C; promote the forward reaction; at the same time, turn on the reflux condenser to condense the evaporated gas;

[0054] 4) After the evaporated gas is condensed, it returns from the return pipe to the reactor. After the reflux flow is stable, the heating is stopped, and the temperature of the reaction material will gradually increase through its own exothermic reaction; the reactor is ...

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Abstract

The invention discloses a production method for diethyl ethanephosphonate, belonging to the technical field of chemical industry production. The production method comprises the following steps of: respectively adopting triethyl phosphate and iodine as a raw material and a catalyst, wherein the adding amount of the iodine is equal to 0.1-0.3% of the total mass of the triethyl phosphate; warming to 135+ / -5 DEG C; starting reaction, and simultaneously starting a reflux condenser to condense streamed gas; controlling the temperature in a reaction kettle at 130-170 DEG C within 40-80 min, and controlling the temperature in the reaction kettle at 160-175 DEG C until the reaction kettle cannot release heat and no reflux exists in a reflux line; and carrying out aging for 3-4 hours; and carrying out reduced pressure distillation, and enabling the condensed diethyl ethanephosphonate to enter a finished product tank. The method has the advantages that the reaction is simple, the device investment is little, the product yield is high, no sewage is discharged and the production period is short.

Description

technical field [0001] The invention relates to a production method of chemical products, in particular to a production method of diethyl ethyl phosphonate. Background technique [0002] Diethyl ethyl phosphonate (DEEP for short) is an important raw material in the pharmaceutical industry and flame retardant industry. Widely used in epoxy resin, phenolic resin, polyester, polycarbonate, polyurethane, polyvinyl chloride, polyethylene, polypropylene, ABS, etc. It is a flame retardant for polyurethane flexible foam products, unsaturated polyester resin, epoxy resin and other polymer material products. The product is a colorless transparent liquid, molecular formula: C 6 h 15 o 3 P, boiling point: 198°C, melting point: -83°C, flash point: >200°C, decomposition temperature: >180°C, easily soluble in alcohol, ether, benzene and other organic solvents. [0003] A preparation method of diethyl ethyl phosphonate is disclosed in the Chinese patent database, its application ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07F9/40
Inventor 董晓红房连顺杨健
Owner 南京晨化新材料科技有限公司