Aromatic hydrocarbon modified C5 petroleum resin and synthesis method thereof
A technology of petroleum resin and synthesis method, which is applied in the synthesis of petroleum resin and the field of synthetic petroleum resin modified by aromatic compounds, which can solve the problems of low bonding strength, poor compatibility between petroleum resin and hot melt adhesive substrate, etc., and achieve raw material The effect of high utilization
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Embodiment 1
[0025] Mixing components with C10, C15, and C20 as main components (mass percentage composition of mixing components: C10 content 85%, C15 content 9%, C20 content 5%, other components 1%.) and 3% modified Mix the cut fractions of agent C9 (modifier addition is mass percentage) and add to the reactor, add anhydrous aluminum trichloride of 2.5% by weight of the mixed component under stirring, and polymerize at a temperature of 125 ° C and a pressure of 1 MPa for 6 hours Afterwards, the reaction temperature was raised to 150° C., and the pressure was controlled at 1.2 MPa for 8 hours of polymerization reaction. After the reaction, the crude resin was diluted with mineral oil, washed with water, settled, and vacuum distilled to obtain petroleum resin. It is determined that the softening point of the petroleum resin product is 98°C; the chromaticity is 4.3; the number average molecular weight is 575; and the molecular weight distribution is 1.61.
Embodiment 2
[0027] Mixing components with C10, C15, and C20 as main components (mass percentage composition of mixing components: C10 content 87%, C15 content 8%, C20 content 4%, other components 1%.) and 5% modified Agent (styrene and C9 are mixed in a mass ratio of 95:5) mixed (modifier addition is mass percentage) is added to the reactor, and anhydrous aluminum trichloride of 2.5% by weight of the mixed component is added under stirring, at a temperature of 120 Polymerize for 9 hours at ℃ and pressure of 1MPa; then raise the reaction temperature to 145℃, control the pressure at 1.1MPa and polymerize for 10 hours. After the reaction, add mineral oil to the crude resin to dilute, wash with water, settle, and distill under reduced pressure Get petroleum resin. It was determined that the petroleum resin product had a softening point of 104° C.; a chroma of 4.1; a number average molecular weight of 573; and a molecular weight distribution of 1.43.
Embodiment 3
[0029] Mixing components with C10, C15, and C20 as main components (mass percentage composition of mixing components: C10 content 90%, C15 content 5%, C20 content 4%, other components 1%.) and 7% modified Mixing agent styrene (addition amount of modifier is mass percent) was added to the reactor, and anhydrous aluminum trichloride of 1.0% by weight of the mixed component was added under stirring, and the temperature was 135° C. and the pressure was 1.1 MPa for polymerization reaction for 8 hours. Afterwards, the reaction temperature was raised to 155° C., and the pressure was controlled at 1.3 MPa for 7 hours of polymerization reaction. After the reaction, the crude resin was diluted with mineral oil, washed with water, settled, and distilled under reduced pressure to obtain petroleum resin. After measurement, the softening point of the petroleum resin product is 106° C.; the chromaticity is 5.0; the number average molecular weight is 563; the molecular weight distribution is 1...
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