Single-stage hydrocracking process

A hydrocracking, single-stage technology, which is applied in the fields of hydrocarbon oil cracking and petroleum industry, etc., can solve the problems of shortening the service life of the catalyst, increasing the severity of the operation, reducing the processing capacity, etc., so as to reduce the construction investment and operation cost and increase the aromatics Saturation capacity, effect of enhancing hydrogenation performance

Active Publication Date: 2007-12-19
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
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  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the disadvantage of single-stage hydrocracking is that the reaction temperature is high, which is unfavorable to the hydrogenation reaction of aromatics. The impact on the properties of jet fuel products is the low smoke point, and the impact on the properties of the product diesel is the increase in cetane number. limited
Due to the high metal content of the catalyst prepared by this method, there is often a lack of sufficient interaction between the metal and alumina, resulting in poor catalyst strength
The active component part is composed of a large number of metals, and some internal metal components cannot be fully utilized during the formation of Ni-Mo or Ni-Mo-W powder, resulting in loss of ac

Method used

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  • Single-stage hydrocracking process

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Effect test

Embodiment 1

[0037] Add 1000mL of water into the reaction tank, then add 40g of nickel chloride to dissolve, then add 52g of ammonium metatungstate to dissolve, then add 5g of zirconium oxychloride to dissolve, then add 10% ammonia water to form a gel until the pH value is 8, and then gel The temperature is 50°C, aging for 1 hour after forming the gel, and then filtering, adding 600ml of clean water, 16g of molybdenum trioxide and 32g of aluminum hydroxide to the filter cake, beating and stirring evenly, filtering, drying the filter cake at 80°C for 5 hours, and then extruding Molded, washed 3 times with clean water, dried at 120°C for 5 hours, and calcined at 500°C for 4 hours to obtain the final catalyst A. The composition and main properties are shown in Table 1.

Embodiment 2

[0039] According to the method of Example 1, according to the component content ratio of catalyst B in Table 1, add aluminum chloride, nickel chloride, sodium tungstate in the reaction tank, then add 16% ammonia water to form a gel, until the pH value is 9 , the gelling temperature is 80°C, aging for 3 hours after gelling, then filtering, washing the filter cake twice with 500mL clean water, adding clean water and molybdenum trioxide, beating and stirring evenly, filtering, and drying the filter cake at 70°C for 7 hours , and then extruded, washed twice with clean water, dried at 100°C for 8 hours, and calcined at 550°C for 3 hours to obtain the final catalyst B. The composition and main properties are shown in Table 1.

Embodiment 3

[0041]According to the method of Example 1, according to the component content ratio of catalyst C in Table 1, nickel nitrate, ammonium metatungstate, aluminum hydroxide, silica sol are added to the reaction tank, and then 12% ammonia water is added to form a gel until the pH The value is 10, the gelling temperature is 60°C, aging for 2 hours after gelling, then filtering, adding molybdenum trioxide to the filter cake, beating and stirring evenly, filtering, drying the filter cake at 120°C for 1 hour, and then extruding into strips, wet strips It was dried at 130°C for 3 hours and calcined at 600°C for 3 hours to obtain the final catalyst C, whose composition and main properties are shown in Table 1.

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Abstract

The single-stage hydrocracking process has the VGO and/or other heavy fraction oil as the material oil hydrocracked under certain condition to obtain various kinds of products. The catalyst in the upper region includes at least one kind of bulk phase catalyst comprising complex oxide NixWyOz and oxide MoO3 in the weight ratio 0.1-10 and accounting for 40-100 wt% of total catalyst. The present invention has the advantages of simple technological process, high volume space velocity, low apparatus cost, high material oil adaptability, flexible production scheme and high product quality.

Description

technical field [0001] The invention relates to a single-stage hydrocracking method, in particular to a single-stage two-agent (multi-agent) hydrocracking method for producing clean light oil products from vacuum distillate oil by using a high-activity hydrogenation catalyst. Background technique [0002] With the increasing emphasis on environmental protection, the requirements of environmental regulations are becoming more and more stringent. Motor exhaust has become an important source of air pollution, especially for large and medium-sized cities. As a result, higher quality restrictions are imposed on motor fuels and stricter requirements are placed on motor fuels for urban use. The vast majority of motor fuels are obtained from petroleum, and petroleum products are obtained through various processing methods. Among these processing methods, the hydrocracking process is the most direct and effective method to produce products that meet high-quality requirements from in...

Claims

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Application Information

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IPC IPC(8): C10G47/02
Inventor 刘涛曾榕辉孙洪江李宝忠宋若霞黄新露潘德满王平
Owner CHINA PETROLEUM & CHEM CORP
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