A kind of method of efficient rectification production tetraethyl orthocarbonate
A technology of tetraethyl orthocarbonate and rectification, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problems of waste of resources, unsafe handling, aggravated product hydrolysis, etc., and achieve high-efficiency rectification, The effect of raising pH
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0024] (1) drop into 320kg of sodium ethylate, 1280kg of dehydrated alcohol to the reactor of clean, dry 2000L;
[0025] (2) Control the temperature between 65° C. and 70° C., add 97 kg of trichloropicrin dropwise, continue the heat preservation reaction for 3 hours after the addition, and recover 900 kg of absolute ethanol by atmospheric distillation;
[0026] (3) add water 1600kg, all residues are dissolved, add n-heptane 1280kg to extract;
[0027] (4) The organic phase enters the rectifying tower, adds sodium ethylate 0.05kg, and the normal pressure control reflux ratio is 1~2, and first normal pressure steams out normal heptane 1024kg;
[0028] (5) control the reflux ratio again to be 3~5, rectify product tetraethyl orthocarbonate under the pressure of-0.098MPa, obtain product altogether: 104kg, purity 99.7%, single impurity<0.1%, yield 91%.
Embodiment 2
[0030] (1) drop sodium ethylate 320kg, dehydrated alcohol 1600kg into clean, dry 2000L reactor;
[0031] (2) Control the temperature between 65° C. and 68° C., add 91.4 kg of trichloropicrin dropwise, continue the insulation reaction for 3 hours after the addition, and recover 1120 kg of absolute ethanol by atmospheric distillation;
[0032] (3) add 1920kg of water, all residues are dissolved, add n-heptane 1280kg to extract;
[0033] (4) The organic phase enters the rectifying tower, adds sodium ethylate 0.5kg, and the normal pressure control reflux ratio is 1~2, first normal pressure steams 896kg of n-heptane;
[0034] (5) control the reflux ratio again to be 4~6, rectify product tetraethyl orthocarbonate under the pressure of-0.095MPa, obtain product altogether: 102kg, purity 99.7%, single impurity<0.1%, yield 90%.
Embodiment 3
[0036] (1) drop into 320kg of sodium ethylate, 1280kg of dehydrated alcohol to the reactor of clean, dry 2000L;
[0037] (2) Control the temperature between 60°C and 65°C, add 97kg of trichloropicrin dropwise, continue the heat preservation reaction for 3 hours after the addition, and recover 900kg of absolute ethanol by atmospheric distillation;
[0038] (3) Add 1600kg of water, dissolve all the residue, add 1280kg of n-hexane to extract;
[0039] (4) The organic phase enters the rectifying tower, adds sodium ethylate, sodium tert-butoxide 0.05kg, and the normal pressure control reflux ratio is 1~2, first normal pressure steams 1024kg of n-heptane;
[0040] (5) control the reflux ratio again to be 3~5, rectify product tetraethyl orthocarbonate under the pressure of-0.098MPa, obtain product altogether: 103kg, purity 99.7%, single impurity<0.1%, yield 91%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More