Hydrocracking method for processing low-sulfur raw material
A technology for hydrocracking and raw materials, applied in hydrotreating process, petroleum industry, processing of hydrocarbon oil, etc., can solve the problems of gas blockage of raw oil pump, difficulty in long-term operation, consumption of vulcanizing agent, etc., so as to improve product quality and save equipment. The effect of low investment and operating costs
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[0024] Such as figure 1 Shown, a kind of implementation mode of combined hydrogenation process flow of the present invention is as follows:
[0025] The high-sulfur raw material 1 is mixed with hydrogen gas 30 and then enters the hydrotreating unit 2, the reaction effluent 3 enters the hot high-pressure separator 4, the liquid 6 obtained by the hot high-resolution is sent to the fractionation tower, the obtained gas 7 is injected into the washing water 8, and is cooled by high-pressure air After the reactor 9, it enters the cold high-pressure separator 10, and the waste liquid 11 containing sulfide amine and hydrosulfide amine is separated, and the hydrogen-rich gas 12 enters the circulating hydrogen desulfurization tower 13 and contacts with the lean amine liquid 15, and the obtained rich amine liquid 14 is discharged for desulfurization The tower enters the regeneration system, and at the same time obtains hydrogen-rich gas 16 with a certain concentration of hydrogen sulfide...
Embodiment 1
[0030] use figure 1 In the process flow shown, the hydrotreating unit for processing high-sulfur raw material 2 and the circulating hydrogen path of hydrocracking unit for processing low-sulfur raw material 1 are organically combined. The properties of the catalysts used in the examples are listed in Table 1. The catalyst is a commercial catalyst developed and produced by Fushun Petrochemical Research Institute.
[0031] The properties of raw oil are shown in Table 2, the operating conditions of the hydrogenation process are shown in Table 3, and the concentration of hydrogen sulfide in circulating hydrogen, DMDS consumption, injection cycle of lean amine solution and unit operation cycle are shown in Table 4.
[0032] Table 1 Main physicochemical properties of the catalyst
[0033] project
FF-36
FC-14
FF-14
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1.5~1.7
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