Novel method for producing dihydromyrcenol
A technology of dihydromyrcenol and dihydromyrcene, which is applied in the field of continuous production of dihydromyrcenol, can solve the problems of solid catalyst pulverization, reaction rate drop, conversion rate limitation, etc., to improve selectivity and reduce equipment Corrosion and equipment cost reduction effects
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Embodiment 1
[0029] The reaction tower 11 is filled with Amberlyst 35 cation exchange resin, and the rectification towers 8 and 16 are filled with high-efficiency packing of BX corrugated wire mesh. Send deionized water and dioxane solvent into the evaporation kettle 9 according to the volume ratio of 1:2 through the pump 6 and the pump 7. The total addition is 0.8 of the volume of the evaporation kettle. After the feeding, stop the pump 6 and the pump 7 and start the evaporation. Stirring and heating of the kettle; the reflux rate of the control rectification tower 8 is 1 / 8 of the total evaporation capacity, after the rectification tower 8 and the reaction tower 11 are all refluxed normally, start the pump 5 and add dihydromyrcene continuously to the reaction unit, The purity of dihydromyrcene is 85% (wt%). The temperature of the reaction tower is controlled at 85°C. After 3 hours of feeding, the valve 12 is opened, and part of the oil-water mixture is extracted to the stratifier 14. The e...
Embodiment 2
[0031]Similar to the operation method of Example 1, the difference is that the solvent is isopropanol, the volume ratio of the solvent to deionized water is 1:1, and the HZSM-5 zeolite catalyst bundled in the reaction tower is used to solve the problem of powder The problem of packing zeolite in a fixed bed. Dihydromyrcene in the evaporator: water: solvent = 1:1:1. Other operating steps are the same as in Example 1, and the single pass conversion rate of this process is 57 ~ 58%, and the selectivity is 95%.
Embodiment 3
[0033] Similar to the operation method of Example 1, the difference is that butanone is used as the solvent, the volume ratio of the solvent to deionized water is 1:1, and the dihydromyrcene in the evaporation kettle: water: solvent = 1:1:1. Other operating steps are the same as in Example 1, and the single pass conversion rate of this process is 55 ~ 56%, and the selectivity is 92%.
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