Preparation of diethyl phosphoric acid
A technology of triethyl phosphate and ethanol, which is applied to organic phosphorus compounds, compounds of group 5/15 elements of the periodic table, chemical instruments and methods, and can solve problems such as loss of products, ethanol and extractants
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Embodiment 1
[0040] Reactions were carried out in a stirred tube reaction set consisting of three stirred tanks each with a liquid capacity of 1 liter. The three stirring tanks are connected to each other and to the storage tank via a submerged connection so that the reaction product can easily overflow to the storage tank. All three stirred tanks were fitted with reflux condensers, which were connected to each other and to a cooling circuit at -20°C.
[0041]The first stirred tank was kept at internal temperature (reaction temperature) 3-6°C, the second stirred tank was at 13-15°C, and the third stirred tank was at 18-20°C by external cooling (thermostat). 517.5 g / h of ethanol (11.25 mol / h) and 383.8 g / h of phosphorus oxychloride (2.5 mol / h) were metered continuously into the first stirred tank.
[0042] The stirring tank set and the storage tank are connected via a valve and connected to a vacuum pump via a scrubber, which is used to maintain the pressure of the stirring tank set at 50 ...
Embodiment 2
[0048] Example 2 was carried out in a similar manner to Example 1, except that 598 g / h ethanol (13 mol / h) and 307 g / h phosphorous oxychloride (2 mol / h) were metered in continuously into the first stirred tank.
[0049] Upon reaching the equilibrium of the reaction tank set, the reaction product obtained in the storage tank consisted of 57.4 wt % triethyl phosphate, 35.5 wt % ethanol and 7.1 wt % hydrogen chloride. Separation in the degassing column gave 367 g / h of crude product containing 96.8% by weight of triethyl phosphate. The resulting product was extracted by distillation and contained more than 99% by weight of triethyl phosphate in 96.3% yield based on phosphorous oxychloride used.
[0050] 1034g / h of fresh water is added to the washing tower from above, and about 1575g / h of liquid from the washing circuit is sent to the connected distillation tower for azeotropic distillation. At the top of the distillation column, 358 g / h of a mixture of 90% by weight of ethanol and...
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