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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Embodiment 1
[0041] Install a thermometer, a stirrer and a constant pressure dropping funnel on the three-necked flask respectively, and place the flask in a low-temperature constant temperature reaction bath; add 100 mL of toluene into the three-necked flask, and turn on the refrigerator until the temperature in the flask reaches -6°C; Quickly weigh 8.2 g of anhydrous AlCl 3 , and ground it into a slurry with 30 mL of toluene in a mortar, and transferred it into a reaction bottle, at this time, the temperature in the bottle was -5°C; 144.9 g of turpentine (which contained 75 %wt of Pinene 15 %wt) and 16.1 g of eucalyptus pinene (which contains α-pinene 96 %wt) were added to the constant pressure dropping funnel, the cock was opened, and the raw materials were added dropwise at a rate of about 100 d / min, the temperature in the bottle rises rapidly, reaching a maximum of 9°C; when the reaction temperature in the bottle begins to drop, add catalysts in the same way, including AlCl 3 5.0 ...
Embodiment 2
[0043] The raw material is 160.5 g turpentine (which contains 75% α-pinene and 15% β-pinene), the initial reaction temperature is 5°C, and the amount of co-catalyst is 5.2 g. The rest of the process is the same as in Example 1. Finally, 140 g of toluene and turpentine mixture were recovered, and 86 g of terpene resin product was obtained, with a yield of 59.7%, a softening point of 91°C, a chlorine content of 53.8 mg / kg, and a residual toluene content of 17.5 mg / kg.
Embodiment 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 processes are 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%. The softening point of the product was 84°C, the chlorine content in the product was 82.0 mg / kg, and the residual toluene content was 19.9 mg / kg.
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