Recovering and recycling method of excessive methyl catechol in vanillin production process
A guaiacol and production process technology, which is applied in the field of recovery and recycling of excess guaiacol in the vanillin production process, can solve the problems of high energy consumption and complicated operation in rectification operation, and save steam , the effect of improving the purity and reducing the cost of recycling
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Embodiment 1
[0027] A method for the recovery and recycling of excess guaiacol in the vanillin production process, specifically comprising the steps:
[0028] (1), at 12M 3 In the condensation reaction kettle of , add 8.0 M under cooling conditions 3 Water, adding 752 Kg of guaiacol (6.06Kmol) with a purity of 99.5%, and then adjusting the pH value of the solution with an aqueous sodium hydroxide solution with a concentration of 30% by weight to be 12.1 is the criterion to obtain a solution with a concentration of 9.1% by weight. guaiacol sodium salt solution;
[0029] Add 665 Kg of glyoxylic acid (4.49Kmol) with a concentration of 50% (weight percent) to the guaiacol sodium salt solution with a concentration of 9.1% by weight obtained above, and then use a hydrogen concentration of 30% by weight. The pH value of the sodium oxide aqueous solution was adjusted to 11.9, and the temperature was controlled to be 20 to 22° C. After the condensation reaction was carried out for 20 hours, it wa...
Embodiment 2
[0039] A method for the recovery and recycling of excess guaiacol in the vanillin production process, specifically comprising the steps:
[0040] (1), in the 2000ml condensation reaction kettle, add 1000ml water under cooling conditions, add 125.5 Kg of guaiacol (1.0mol) with a purity of 99.6%, and then adjust the solution with an aqueous sodium hydroxide solution with a weight percent concentration of 31% The pH value is 11.6, that is, the guaiacol sodium salt solution with a weight percent concentration of 12.6% is obtained;
[0041] In the above-obtained guaiacol sodium salt solution with a concentration of 12.6% by weight, add glyoxylic acid (0.7 mol) with a content of 103 grams and a concentration of 50% (by weight), and then use a hydrogen concentration of 31% by weight. The pH value of the sodium oxide aqueous solution was adjusted to 11.1, and the temperature was controlled to be 30 to 32° C. After the condensation reaction was carried out for 15 hours, it was detected...
Embodiment 3
[0052] A method for the recovery and recycling of excess ethyl guaiacol in the production process of ethyl vanillin, specifically comprising the steps:
[0053] (1), at 50 M 3 Add 28 M to the ethyl guaiacol preparation kettle 3 Water, the purity of 98.5% ethyl guaiacol (the main impurity is o-diphenyl ether, the content is 1.3%) 3465Kg (25.2kmol), the pH value is adjusted with the sodium hydroxide aqueous solution that the weight percent concentration is 30% under cooling Be as the criterion to 11.6, to obtain the ethyl guaiacol sodium salt solution with a weight percent concentration of 11.6%;
[0054] Add 2980kg 50% concentration (weight percent) glyoxylic acid (20.1 kmol) to the 11.6% weight percent concentration of ethyl guaiacol sodium salt solution obtained above, and then use 30 percent weight percent concentration of hydrogen The pH value of the sodium oxide aqueous solution is adjusted to 11.2, and the condensation reaction is carried out at a temperature of 12 to 1...
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