Method for producing pale disproportionated rosin with high content dehydroabietic acid and P-camphogen simultinuously
A technology for dehydroabietic acid and p-cymene, which is applied in the field of deep processing of rosin, can solve the problems of low concentration of dehydroabietic acid, large investment, long process, etc., achieves inhibition of browning and oxidation, and reduces equipment investment and energy consumption, the effect of shortening the production process
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Embodiment 1
[0029] The purchased fresh turpentine is crushed and sent to the turpentine tank, and then rinsed and maintained by adding sterilized and low dissolved oxygen water. The water quality should be 20-30cm higher than the resin surface, and the tap water should be changed every 5-30 days. After three consecutive changes The rosin that has been rinsed is sent to the dissolving tank and added with turpentine to adjust to contain 60-80% by weight of rosin, and the purified rosin liquid is obtained after heating, dissolving, filtering and clarifying processes, and then added to the disproportionation reactor after metering from the head tank. And add the Pd / C catalyst by 0.10~0.20% of the weight of the feed, after vacuumizing and replacing the air in the autoclave with nitrogen, adjust the protective gas nitrogen pressure in the autoclave to be 0.01~0.5MPa, start the agitator and the agitator of the disproportionation reactor Heating the system, raising the temperature to 260-280°C, ma...
Embodiment 2
[0031] Send the rinsed turpentine to the dissolving tank and add turpentine to adjust to 50-60% by weight of rosin. The reaction time is 0.8-1.8 hours, and the rest are the same as in Example 1.
Embodiment 3
[0033] Send the rinsed turpentine to the dissolving kettle and add turpentine to adjust to 20-50% by weight of rosin. The reaction time is 0.5-1.5 hours, and the rest are the same as in Example 1.
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