Hydrocracking technology for increase production of low solidifying point diesel oil and ethylene producing raw material
A technology for hydrocracking and ethylene production, which can be used in hydrotreating process, hydrocarbon oil cracking, petroleum industry, etc., and can solve problems such as reducing catalyst utilization efficiency.
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[0019] This process plan deals with a heavy vacuum gas oil VGO, the main properties of this petroleum hydrocarbon material are: specific gravity 0.9002cm 3 / g, distillation range 362°C-524°C, carbon residue 0.20wt%, sulfur 1.44wt%, nitrogen 720μg / g.
[0020]This scheme has two reactors, including hydrofinishing reactor R1 and hydrocracking reactor R2, and the two reactors are used in series and share a set of circulating hydrogen system, which belongs to a serial process flow. Hydrofining reactor R1 is loaded with 3996 heavy oil hydrofining catalyst produced by Fushun Petrochemical Company Catalyst Factory. The operating conditions of hydrofining are: pressure 15MPa, average bed temperature 368°C, volumetric space velocity of feed liquid 0.8hr -1 , The volume ratio of hydrogen to oil is 800. The nitrogen content of refined oil is less than 10μg / g.
[0021] Preparation of hydrocracking catalysts containing Y zeolite: A1, A2, A3.
[0022] A1:
[0023] Take by weighing amorp...
example 1~4
[0035] Examples 1-4: Operating conditions of each cracking section: reaction pressure 15MPa, hydrogen-to-oil ratio 1200, one-pass operation mode, and control of <350°C single-pass conversion of fractions to 70wt%. Mid-oil selectivity is calculated as middle distillate (jet fuel and / or diesel fraction) yield divided by converted liquids yield (100 minus tails).
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