Crude benzene hydrorefining process
A hydrorefining and process technology, applied in hydrocarbons, organic chemistry, distillation purification/separation, etc., can solve problems such as the use of organic raw materials, environmental pollution, and low added value
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[0012] The raw material is coking crude benzene, and its components and mass fractions are as follows:
[0013] Benzene: 75%, toluene: 13.9%, xylene: 2.24%, light component: 0.86%, heavy component: 8%, total sulfur content 6546.57ppm, total nitrogen content 899.3ppm.
[0014] In this example, the reaction temperature of the liquid-phase catalytic prehydrogenation reaction is 140°C, the catalyst is Co-Mo, the volume ratio of hydrogen to oil is 500:1, the volume space velocity is 3h-1, and the pressure is 2.8MPa;
[0015] The reaction temperature of the gas-phase catalytic prehydrogenation reaction is 190°C, the catalyst is Ni-Mo catalyst, the volume ratio of hydrogen to oil is 400:1, the volume space velocity is 0.5h-1, and the pressure is 2.0MPa;
[0016] The reaction temperature of the main catalytic hydrogenation reaction is 270°C, the catalyst is Cr-Mo catalyst, the volume ratio of hydrogen to oil is 400:1, the volume space velocity is 0.5h-1, and the pressure is 2.0MPa.
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