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

Active Publication Date: 2009-07-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its main disadvantage is that the amount of catalyst that needs to be presulfurized outside the device is large, the pretreatment process outside the device takes a long time, and the processing cost increases. , which may affect the on-time start-up of the hydrocracking unit
In addition, the hydrocracking catalyst contains acidic cracking active components (such as molecular sieves, etc.), and the external presulfurization usually needs to be carried out in the presence of organic solvents. Cracking reaction occurs, and then accidents such as over-temperature occur

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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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PUM

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Abstract

The invention discloses a hydrocracking process operation method. Hydrocracking pre-refining catalyst is treated by precuring outside a reactor while hydrocracking catalyst is not treated or is partially treated by precuring outside the reactor. Curing ingredient introduced by the hydrocracking pre-refining catalyst and the hydrocracking catalyst precured outside the reactor accounts for 90-120% of the theoretical sulfur demand for all the catalyst. The hydro cracking pre-refining catalyst and the hydro cracking catalyst are layered in the reactor and then activated by heating, so that all the catalyst is sulfurated effectively. The method of the invention can precure the hydrocracking pre-refining catalyst outside the reactor or precure the hydrocracking pre-refining catalyst and partial hydrocracking catalyst outside the reactor, thus reducing the catalyst requiring precuring outside the reactor, reducing the production period and production cost of the precuring catalyst and improving the economic benefit and production security.

Description

technical field [0001] The invention relates to a start-up method of a hydrocracking process, in particular to a start-up method of a hydrocracking process using an external presulfided catalyst. technical background [0002] In the past ten years, due to the slow growth of crude oil production and the increasingly heavy quality, while the market demand for light oil products has continued to increase, coupled with increasingly stringent environmental protection regulations, therefore, the world has paid special attention to oil upgrading technology . Hydrocracking technology is the best means for deep processing of heavy oil to produce high-quality clean fuel, and its application is becoming more and more extensive. The active metal components of hydrocracking catalysts will have high catalytic activity only when they are transformed into sulfurized state, so catalyst presulfidation is very important to fully exert the catalyst performance. The presulfurization method of ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G47/12
Inventor 陈光高玉兰杜艳泽黄新露曹凤兰李崇慧徐黎明
Owner CHINA PETROLEUM & CHEM CORP
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