Litsea cubeba nucleolus deep-processing and comprehensive utilization process
A technology for deep processing of litsea cubeba seeds, which is applied in the field of deep processing and comprehensive utilization of litsea cubeba kernel kernels, can solve the problems of high catalyst cost, long reaction time, and high equipment requirements, and achieve short reaction time, high reaction conversion rate, The effect of comprehensive utilization of resources
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Embodiment 1
[0031] Get 410 grams of acid value 42mg / KOH as Litsea cubeba kernel, directly crush to 50-500 mesh, use 500 milliliters of 120# solvent gasoline (produced by Guangdong Maoming Petrochemical Refinery) as solvent to extract Litsea cubeba kernel by Soxhlet method 100 grams of oil; then 100 grams of Litsea cubeba kernel oil, 30 grams of methanol, 3 grams of anhydrous sodium sulfate and 1 gram of concentrated sulfuric acid are mixed and added to a stirring reactor for lipid-lowering reaction, and the reaction temperature is controlled at 70 ° C. The time is controlled at 1 hour; after the reaction stops, add 1.5 grams of anhydrous sodium carbonate to the mixed solution and continue to heat to 70 ° C, and stir for 1 hour to make the system neutral; and use vacuum distillation to recover methanol, and then raise the temperature to 130 ℃ decompression distillation to remove the water in the system, cooling, centrifugation and recovery of solid salt, the acid value was 1.7mg / KOH; then t...
Embodiment 2
[0033]Take 410 grams of acid value 42mg / KOH as Litsea cubeba kernel, directly crush to 50-500 mesh, use 500 milliliters of petroleum ether (boiling range 60-90°C) as solvent to extract Litsea cubeba kernel oil 100 by Soxhlet method gram; Then 100 grams of Litsea cubeba kernel oil, 50 grams of methanol, 5 grams of anhydrous sodium sulfate and 1 gram of concentrated sulfuric acid are mixed and added to the stirring reactor to carry out lipid-lowering reaction, the reaction temperature is controlled at 85 ° C, and the reaction time is controlled After 1.5 hours; after the reaction stopped, add 1.5 grams of anhydrous sodium carbonate to the mixture and continue heating to 70°C, and stir for 1 hour to make the system neutral; and recover methanol by vacuum distillation, and raise the temperature to 130°C after recovering methanol Remove the water in the system by distillation under reduced pressure, cool, and centrifuge to reclaim the solid salt, and the acid value is 1.6mg / KOH; the...
Embodiment 3
[0035] Get 410 grams of acid value 42mg / KOH as Litsea cubeba kernel, directly crush to 50-500 mesh, use 500 milliliters of 120# solvent gasoline as solvent to extract 100 grams of Litsea cubeba kernel oil by Soxhlet method; then 100 grams Litsea cubeba kernel oil, 30 grams of methanol, 3 grams of anhydrous sodium sulfate and 1 gram of concentrated sulfuric acid are mixed and added to the stirring reactor for lipid-lowering reaction. The reaction temperature is controlled at 80 ° C, and the reaction time is controlled at 2 hours; the reaction is stopped Add 1.5 grams of anhydrous sodium carbonate to the mixed solution and continue heating to 70°C, stir for 1 hour to make the system neutral; and recover methanol by vacuum distillation, raise the temperature to 130°C to remove the water in the system by vacuum distillation , cooling, centrifugation reclaims solid salt, records acid value and is 1.63mg / KOH; Then filtrate, methyl alcohol, phase transfer catalyst triethylbenzyl ammon...
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