Start working method for hydrocracking process
A hydrocracking and process technology, applied in hydrocarbon oil cracking, petroleum industry and other directions, can solve the problems affecting the on-time start-up of hydrocracking units, increased processing costs, and large amount of catalyst, and achieves reduction of human body damage and pre-vulcanization process. Uniform, high cure rate effect
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Embodiment 1
[0045] FF-26 is 90g, soaked in 30g of organic solvent (the organic solvent is coking kerosene fraction), the proportion of carbon number 9-12 in the organic solvent is not less than 50%, and the soaking time is 1 hour. Elemental sulfur 10g and 5g (NH 4 ) 2 S mixed. The impregnated catalyst was mixed with a vulcanizing agent, treated at 180°C for 3 hours, and cooled naturally. The obtained presulfided catalyst, presulfurized FF-26 catalyst and oxidized state FC-12 catalyst are layered into small reactors (the order of contacting FC-12 after the reaction material first contacts FF-26 is loaded, other embodiments and The comparative example is the same), the airtightness is qualified, and the temperature is started to rise at 20°C / h, and rises to 220°C, and the temperature is kept constant for 8 hours. End the constant temperature and continue to raise the temperature to 360°C at 20°C / h, and switch the raw material oil according to the operation. The vulcanization time is abo...
Embodiment 2
[0047] 90g of FF-26 is soaked in 20g of organic solvent (organic solvent is coking kerosene fraction), the ratio of carbon number 9 to 12 in the organic solvent is not less than 50%, and the soaking time is 1 hour. Elemental sulfur 12g and 6g (NH 4 ) 2 S mixed. The impregnated catalyst was mixed with a vulcanizing agent, treated at 180°C for 3 hours, and cooled naturally. The obtained pre-sulfurized catalyst, the pre-sulfurized FF-26 catalyst and the oxidized FC-12 catalyst were layered into a small reactor, and the airtightness was qualified, and the temperature was raised at 20°C / h at the beginning, and the temperature was raised to 220°C, and the temperature was constant for 8 Hour. End the constant temperature and continue to raise the temperature to 360°C at 20°C / h, and switch the raw material oil according to the operation. The vulcanization time is about 27 hours. After switching the raw materials, run for 48 hours according to the process evaluation conditions in ...
Embodiment 3
[0049] 90g of FF-26 and 30g of FC-12 are respectively immersed in 25g and 15g of organic solvent (organic solvent is coking kerosene fraction), the ratio of carbon number 9 to 12 in the organic solvent is not less than 50%, and the immersion time is 1 hour. The vulcanizing agent used in the FF-26 catalyst is elemental sulfur 6g and 3g (NH 4 ) 2 The mixture of S, the vulcanizing agent used by the FC-12 catalyst is elemental sulfur 4g and 2g (NH 4 ) 2 Mixture of S. The impregnated FF-26 and FC-12 were mixed with corresponding vulcanizing agents respectively, and treated at 180°C for 3 hours, and cooled naturally. The obtained presulfurized catalyst, presulfurized FC-12 and oxidized FC-12 are mixed, presulfurized FF-26 and mixed FC-12 are layered into a small reactor, and the airtightness is qualified. h, the temperature was raised to 220° C., and the temperature was kept constant for 6 hours. End the constant temperature and continue to raise the temperature to 360°C at 20°...
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