C5 petroleum resin product and preparation method thereof with controllable molecular weight
A petroleum resin and molecular weight technology, which is applied to the preparation field of C5 petroleum resin products and their molecular weight controllable, can solve the problems of narrow molecular weight adjustment range and difficulty in meeting usage requirements, and achieve the effects of simple method, good quality and cost saving.
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Embodiment 1
[0028] A method for preparing C5 petroleum resin with controllable molecular weight of the present invention comprises the following steps: by adjusting the content range of the active monoolefin component in the production formula to 50%; the content of the active diolefin component is 10%, and controlling the addition of the catalyst 0.35%, reaction polymerization stirring speed control 150rpm, polymerization reaction temperature is 80 ℃, polymerization reaction residence time is 150min, after finishing, in the resin polymerization liquid that the reaction gained, add the polyoxyethylene polyoxypropylene alcohol ether that concentration is 500ppm as Demulsifier, the catalyst is removed at a stirring speed of 180rpm, and then the polymer solution obtained after the catalyst removal is added to the flashing and stripping device to extract solvent oil and oligomers, and finally the Z-average molecular weight of C5 petroleum resin can be obtained It is a C5 petroleum resin produc...
Embodiment 2
[0030]A method for preparing C5 petroleum resin with controllable molecular weight of the present invention comprises the following steps: by adjusting the content range of the active monoolefin component in the production formula to 10%; the content of the active diolefin component to 50%, controlling the amount of catalyst added At 0.35%, the reaction polymerization stirring speed is controlled at 250rpm, the polymerization temperature is 80°C, and the polymerization residence time is 150min. Demulsifier, the catalyst is removed at a stirring speed of 300rpm, and then the polymer solution obtained after the catalyst removal is added to the flashing and stripping device to extract solvent oil and oligomers, and finally the Z-average molecular weight of C5 petroleum resin can be obtained It is a C5 petroleum resin product with a softening point of 101°C and a temperature of 10,000.
Embodiment 3
[0032] A kind of C5 petroleum resin molecular weight controllable preparation method of the present invention comprises the following steps: by adjusting 2-methyl-1-butene, 2-methyl-2-butene and The total content of cyclopentene is 10%; the total content of trans-1,3-pentadiene, cis-1,3-pentadiene, cyclopentadiene and dicyclopentadiene in the active diene component is 50% %, the control catalyst addition is at 0.35%, the reaction polymerization stirring speed is controlled at 150rpm, the polymerization reaction temperature is 50°C, and the polymerization reaction residence time is 200min. The catalyst is removed at a stirring speed of 50rpm, and then the polymer solution obtained after the catalyst removal is added to a flash evaporation and stripping device to extract solvent oil and oligomers, and finally a C5 petroleum resin with a Z-average molecular weight of 15000 can be obtained. A C5 petroleum resin product with a softening point of 105°C.
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