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Light-oil-type hydrocracking catalyst carrier, preparation method thereof and applications thereof

A catalyst carrier, hydrocracking technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problem that the octane number of light naphtha is not very high, and achieve high catalytic cracking performance, acid The number of centers is small and the effect of improving the reaction rate

Active Publication Date: 2013-11-27
CHINA NAT OFFSHORE OIL CORP +3
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Light naphtha octane is not very high

Method used

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  • Light-oil-type hydrocracking catalyst carrier, preparation method thereof and applications thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026]Take 500 grams of NaY molecular sieve with 5 L of 1.5N ammonium nitrate solution, exchange at 90 ° C for 1 hour, suction filtration, repeat 2 times, and finally wash with deionized water, suction filtration; The filter cake is placed in hydrothermal treatment to heat up with electricity, During the heating process, nitrogen (1.5 liters / min) was introduced, and when the temperature rose to 580°C, the nitrogen was changed to water vapor (105°C, 1.5 liters / min), and the temperature of the hydrothermal treatment was controlled to be 580°C, and the pressure of the hydrothermal treatment was 0.12 MPa, hydrothermal treatment for 2.5 hours; molecular sieve samples after hydrothermal treatment were treated with 5L of 1.0N ammonium nitrate and 45.4g / 100ml of HNO 3 100 g of the mixed solution was treated at 92°C for 1 hour, the slurry was suction filtered, and the treatment was repeated for 2 times. Its physicochemical properties are: the relative crystallinity is 97%, the unit cel...

Embodiment 2

[0028] Take 1000 grams of NaY molecular sieve with 8 L of 1.8N ammonium nitrate solution, exchange at 90 ° C for 1.5 hours, suction filtration, repeat 2 times, and finally wash with deionized water, suction filtration; The filter cake is placed in a hydrothermal treatment to heat up with electricity, During the heating process, nitrogen (2.0 liters / min) was introduced, and when the temperature rose to 620°C, the nitrogen was changed to water vapor (105°C, 2.0 liters / min), and the hydrothermal treatment temperature was controlled to be 620°C, and the hydrothermal treatment pressure was 0.15 MPa, hydrothermally treated for 1.5 hours; the molecular sieve samples after hydrothermal treatment were treated with 8L of 1.5N ammonium nitrate and 45.4g / 100ml of HNO 3 200 g of the mixed solution was treated at 95°C for 1 hour, the slurry was suction filtered, and the treatment was repeated for 2 times. Its physicochemical properties are: the relative crystallinity is 103%, the unit cell ...

Embodiment 3

[0030] Take commercially available SiO 2 / Al 2 O 3 300 g of HZSM-23 molecular sieve with a molar ratio of 65 was placed in a hydrothermal treatment furnace, the temperature of the control system was 500 °C, the water vapor pressure was 0.05 MPa, and the modified ZSM-23 molecular sieve C was obtained by hydrothermal treatment for 1.0 hours, and its physical and chemical properties were: SiO 2 / Al 2 O 3 The molar ratio is 65, and the specific surface area is 352m 2 / g, the pore volume is 0.230ml / g, and the total infrared acid is 0.14 / g.

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Abstract

The invention discloses a light-oil-type hydrocracking catalyst carrier comprising a modified Y molecular sieve, a modified ZSM-23 molecular sieve and foraminate aluminium oxide. The light-oil-type hydrocracking catalyst carrier comprises the modified Y molecular sieve with high cracking activity, and the modified ZSM-23 molecular sieve with excellent isomerization performance, and therefore the carrier has more comprehensive catalytic performances. A Y molecular sieve is modified to remove aluminium and improve the Si / Al skeleton, thus generating unit cell contraction, reducing the concentration of surface acid sites, and enhancing intensity of the acid sites and producing rich secondary mesopores, thereby facilitating improvement of adsorption and desorption performances of the molecular sieve, reducing diffusion resistance of reactant and resultant and improving the reaction speed, and therefore a catalyst can obtain a high catalytic cracking performance and more light distillates can be produced. The modified ZSM-23 molecular sieve has unobstructed pore channels, a little amount of the acid sites and an outstanding isomerization performance, thereby facilitating isomerization of the light distillates to improve the octane value.

Description

technical field [0001] The present invention relates to a hydrocracking catalyst carrier and its preparation method and application, in particular to a light oil type hydrocracking catalyst carrier suitable for producing light distillate oil, and its preparation method and application. Background technique [0002] With the development of society, people's demand for light fuel oil is increasing day by day, and with the progress of society, the environment's requirements for fuel oil are becoming more and more demanding. The quantity and quality of primary processing of petroleum cannot meet people's needs. Converting heavy distillate oil into high-quality light fuel through secondary processing of petroleum not only fully utilizes limited petroleum resources, but also alleviates the problem of light distillate oil. Market demand. Hydrocracking technology has strong adaptability to raw materials, flexible production plan, and high product quality. It is one of the main mean...

Claims

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Application Information

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IPC IPC(8): B01J29/80C10G47/16
Inventor 齐邦峰甘为民孟繁梅
Owner CHINA NAT OFFSHORE OIL CORP
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