Method for preparing condensation polycyclic polynuclear aromatic hydrocarbon resin
A technology for nuclear aromatic hydrocarbon resin and polynuclear aromatic hydrocarbon is applied in the field of preparation of condensed polycyclic polynuclear aromatic hydrocarbon resin, which can solve problems such as cost reduction, and achieve the effects of improving utilization rate and reducing synthesis cost.
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Embodiment 1
[0019] FCC oil slurry was used as raw material, and furfural was used as solvent to carry out liquid-liquid extraction to enrich aromatics. The aromatic components in the FCC oil slurry account for 62.80wt%, and the saturated content is 37.20wt%. The content of aromatics in the components reaches 90.50wt%, and the saturated content is 9.50wt%. The content of aromatics in the aromatic-poor component is 37.20wt%, and the saturated content is 72.80wt%. The derivatives are prepared using aromatic-rich components as raw materials. Take the aromatic-rich component: Br 2 =8:1 (weight ratio), plus FeCl 3 As a catalyst, the added amount accounts for 5.00wt% of the total amount, the maximum reaction temperature is 120° C., and the reaction time is 2 hours to obtain aromatic hydrocarbon brominated derivatives with a yield of 31.00wt%. Add 3 times the weight of 50% NaOH solution to the aromatic brominated derivatives and react at a constant temperature of 70° C. for 1 hour to obtain p...
Embodiment 2
[0021] FCC oil slurry was enriched with aromatics by liquid-liquid extraction using pyrrolidone as solvent. The aromatic components in the FCC oil slurry accounted for 55.20wt%, and the saturated content was 45.80wt%. After extraction at a temperature of 50°C and a solvent-to-oil ratio of 1:1, aromatic-rich components and aromatic-poor components were obtained. Among them, the aromatic-rich components The content of aromatics in the fraction reached 76.80wt%, and the saturated fraction was 23.20wt%. The content of aromatics in the aromatic-poor component is 28.80wt%, and the saturated content is 71.20wt%. The derivatives are prepared using aromatic-rich components as raw materials. Get aromatic-rich component: HCl=5:1 (weight ratio), add Al 2 o 3 As a catalyst, the added amount accounts for 5.00wt% of the total amount, the maximum reaction temperature is 90°C, and the reaction time is 3 hours to obtain aromatic hydrocarbon chlorinated derivatives with a yield of 31.00wt%. ...
Embodiment 3
[0023] FCC oil slurry was used as raw material, and furfural was used as solvent to carry out liquid-liquid extraction to enrich aromatics. The aromatic components in the FCC oil slurry account for 62.80wt%, and the saturated content is 37.20wt%. The content of aromatics in the components reaches 90.50wt%, and the saturated content is 9.50wt%. The content of aromatics in the aromatic-poor component is 37.20wt%, and the saturated content is 72.80wt%. The derivatives are prepared using aromatic-rich components as raw materials. Take the aromatic-rich component: H 2 SO 4 =8:1 (weight ratio), plus FeCl 3 As a catalyst, the added amount accounts for 5.00wt% of the total amount, the reaction temperature is 60°C, and the reaction time is 1 hour, to obtain aromatic hydrocarbon sulfonated derivatives with a yield of 32.00wt%. Add 3 times the weight of 50% NaOH solution to the aromatic hydrocarbon sulfonated derivatives, and react at a constant temperature of 70° C. for 1 hour to o...
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