A kind of technique for preparing p-toluic acid by continuous catalytic oxidation
A technology of p-toluic acid and sodium toluate, applied in the field of chemical technology, can solve the problems of high energy consumption, low output, low yield of catalytic oxidation reaction process, etc., and achieve the effect of low energy consumption
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0027] A process for preparing p-toluic acid by continuous catalytic oxidation, the specific steps comprising:
[0028] (1) Stir and mix p-xylene 20Kg, 32% caustic soda aqueous solution 23Kg and catalyst cobalt naphthenate 1.0Kg in a mixing tank to obtain a feed liquid, and adopt a multiphase pump to feed the feed liquid at 1m 3 / h into the gas-liquid high-efficiency mixer to mix evenly with oxygen to carry out continuous catalytic oxidation reaction, use the pump to circulate through the steam heater on the circulation pipeline to heat the material liquid to 100-110°C, and then enter the continuous tubular reactor to continue Reaction, the reaction temperature is 110°C, and the reaction pressure is 0.3MPa;
[0029] (2) when the massfraction that sodium p-toluate accounts for reaction solution in the reaction solution that enters two-phase continuous separator is 20%, when the massfraction that sodium p-toluate accounts for caustic soda aqueous solution in reaction solution is...
Embodiment 2
[0033] A process for preparing p-toluic acid by continuous catalytic oxidation, the specific steps comprising:
[0034] (1) Stir and mix p-xylene 40.0Kg, 32% caustic soda aqueous solution 46.0Kg and catalyst cobalt naphthenate 2.0Kg in a mixing tank to obtain a feed liquid, and adopt a multiphase pump to feed the feed liquid at 5m 3 / h into the gas-liquid high-efficiency mixer to mix evenly with oxygen to carry out continuous catalytic oxidation reaction, use the pump to circulate through the steam heater on the circulation pipeline to heat the material liquid to 100-110°C, and then enter the continuous tubular reactor to continue Reaction, the reaction temperature is 140°C, and the reaction pressure is 0.6MPa;
[0035] (2) when the massfraction that sodium p-toluate accounts for reaction solution in the reaction solution that enters two-phase continuous separator is 20%, when the massfraction that sodium p-toluate accounts for caustic soda aqueous solution in reaction solutio...
Embodiment 3
[0039] A process for preparing p-toluic acid by continuous catalytic oxidation, the specific steps comprising:
[0040] (1) Stir and mix p-xylene 70Kg, caustic soda aqueous solution 80.5Kg and catalyst cobalt naphthenate 3.0Kg in a mixing tank to obtain a feed liquid, and adopt a multiphase pump to feed the feed liquid at 3m 3 / h into the gas-liquid high-efficiency mixer to mix evenly with oxygen to carry out continuous catalytic oxidation reaction, use the pump to circulate through the steam heater on the circulation pipeline to heat the material liquid to 100-110°C, and then enter the continuous tubular reactor to continue Reaction, the reaction temperature is 130°C, and the reaction pressure is 0.4MPa;
[0041] (2) when the massfraction that sodium p-toluate accounts for reaction solution in the reaction solution that enters two-phase continuous separator is 20%, when the massfraction that sodium p-toluate accounts for caustic soda aqueous solution in reaction solution is 40%...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

