Preparation method of C5/C9 hydrocarbon resin
A technology for hydrogenating petroleum resins and petroleum resins, applied in chemical instruments and methods, chemical/physical processes, physical/chemical process catalysts, etc. The effect of improving compatibility and reducing energy consumption in production
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Embodiment 1~6
[0081] The following table 8 is the embodiment of preparing C5 / C9 petroleum resin, the raw material is Pd / Al 2 o 3 The processes of catalyst selective hydrogenation, Friedel-Crafts catalyst pretreatment and subsequent catalyst removal, raw material rectification to remove oligomers, solvent dilution, and resin polymerization liquid catalyst removal are as follows:
[0082] (1) Prepare C5 / C9 petroleum resin polymerization raw material D from three raw materials A, B, and C;
[0083] (2) After dehydrating the above-mentioned polymerization raw material D through a 4A molecular sieve packed tower, use Pd / Al 2 o 3 The catalyst is selectively hydrogenated to remove alkynes, then add Friedel-Crafts catalyst and pre-polymerize at room temperature for 0.5-1.5 hours, then remove the catalyst with a mixture of calcium hydroxide and methanol, and obtain polymerization raw materials with a boiling point of 25-180°C after distillation Fraction E;
[0084] (3) Thermally prepolymerizing ...
Embodiment 7~10
[0090] Table 9 is an example of the hydrogenation process in the method of the present invention. The C5 / C9 petroleum resin liquid used in Examples 7 to 10 is prepared by the polymerization process in Example 2, and is removed by vacuum distillation in the post-hydrogenation treatment. The solvent and oligomer process technology is:
[0091] (1) The above resin solution is dehydrated by electro-desalting, and then passed through active Al 2 o 3 solid bed;
[0092](2) The C5 / C9 petroleum resin liquid after the above pretreatment is dissolved in a diluting solvent, and hydrogenation reaction is carried out in the presence of a modified Pd catalyst to obtain a hydrogenated diluted resin liquid;
[0093] (3) Remove the solvent and oligomers from the above-mentioned hydrogenated diluted resin liquid through a vacuum rectification tower with an operating pressure of -0.075 ~ -0.090 MPa and a temperature of 220 ° C to obtain C5 / C9 hydrogenated petroleum resin .
[0094] The hydro...
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