Terpene resin and preparation method thereof
A technology of terpene resin and terpenes, applied in the field of preparation of terpene resin, can solve the problems of equipment corrosion, catalyst poisoning, high chlorine content, and achieve the effects of improving product yield, reducing material loss and reducing residual amount
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[0040] Example 1
[0041] Install the thermometer, stirrer and constant pressure dropping funnel on the three-necked flask respectively, and place the flask in the low-temperature thermostatic reaction bath; add 100 mL of toluene into the three-necked flask, open and cool until the temperature in the bottle reaches -6℃; Quickly weigh out 8.2 g of anhydrous AlCl 3 , And grind into a slurry together with 30 mL of toluene in a mortar, and transfer them into the reaction flask together. At this time, the temperature in the flask is -5°C; 144.9 g turpentine oil (containing 75% wt of α-pinene, β- A mixture of pinene 15%wt) and 16.1 g of cineole pinene (containing 96%wt of α-pinene) was added to the constant pressure dropping funnel, the stopcock was opened, and the raw materials were started to be dropped. The dropping speed was controlled to about 100 d / min, the temperature in the bottle rises rapidly, reaching a maximum of 9°C; when the reaction temperature in the bottle starts to...
Example Embodiment
[0042] Example 2
[0043] The raw material is 160.5 g of turpentine (containing 75% of α-pinene and 15% of β-pinene), the initial reaction temperature is 5°C, the amount of co-catalyst is 5.2 g, and the remaining processes are the same as in Example 1. In the end, 140 g of the mixture of toluene and turpentine was recovered, and 86 g of terpene resin product was obtained. The yield was 59.7%, the softening point was 91°C, the chlorine content in the product was 53.8 mg / kg, and the residual toluene content was 17.5 mg / kg.
Example Embodiment
[0044] Example 3
[0045] The raw material is a mixture of 80 g turpentine oil and 82.5 g eucalyptus pinene, the initial reaction temperature is 0°C, and the rest of the process is the same as in Example 1. Finally, 131.2 g of toluene and unreacted turpentine were recovered, and 86.5 g of terpene resin product was obtained, with a yield of 53.2%, a product softening point of 84°C, a chlorine content of 82.0 mg / kg in the product, and a residual toluene content of 19.9 mg / kg.
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