Method of producing gasoline blending component with high octane value by light aromatic hydrocarbon and/or alcohol/ether compound
A technology for high-octane gasoline and light aromatics, applied in the preparation of liquid hydrocarbon mixtures, petroleum industry, biological raw materials, etc., can solve the problems of reduced conversion rate of raw materials, poor catalyst stability, low conversion rate of toluene, etc., to promote high efficiency Transformation, simple process, high conversion rate of raw materials
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Embodiment 1
[0014] Using the method provided by the invention, using benzene and methanol as raw materials, the reaction conditions are as follows: the inlet temperature of each section of the reaction bed is 360 ° C, the pressure is 0.5 MPa, the molar ratio of benzene to alcohol is 0.5, and the feed space velocity is 2.0 h -1 .
[0015] The raw material benzene enters the reactor from the top of the reactor, and the methanol raw material is equally divided into 4 paths and enters the inlets of each bed of the alkylation reactor, and reacts with benzene on the DL0812 special catalyst. The methanol conversion rate is 100%, and the liquid product yield is >99.8% (based on the hydrocarbon group in the raw material). The product is separated, benzene is recycled back to the alkylation reactor, and the hydrocarbonated liquid is fractionated to obtain high-octane gasoline (>98%) and 91%, the content of normal paraffins with low octane number is less than 1%, and the rest are isoparaffins, norma...
Embodiment 2
[0017] Using the method provided by the invention, coking hydrogenated benzene (purity>99.9%) and dimethyl ether are used as raw materials, and the reaction conditions are as follows: the inlet temperature of each stage of the reaction bed is 320 ° C, the pressure is 0.5 MPa, and the molar ratio of benzene to alcohol is 1. Material space velocity 2.0h -1 .
[0018] The raw material coking and hydrogenation benzene enters the reactor from the top of the reactor, and the dimethyl ether raw material is divided into 5 paths and enters each bed entrance of the alkylation reactor, and reacts with the raw material benzene on the DL0802G special catalyst. The conversion rate of dimethyl ether is 100%, and the liquid product yield is >99.6% (based on the hydrocarbon group in the raw material). The product is separated, benzene is recycled back to the alkylation reactor, and the hydrocarbonated liquid is fractionated to obtain high-octane gasoline (>98%) and 93%, the content of normal ...
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