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Hydrocracking catalyst and preparation method thereof

A hydrocracking and catalyst technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as low catalyst activity, adverse effects on product quality, and insignificant increase in oil selectivity in catalysts, etc., to achieve Effects of reduced coke yield, good cracking activity and product selectivity, and high proportion of mesopores

Active Publication Date: 2019-11-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Due to the relatively low acidity of the molecular sieve, the activity of the catalyst is too low, which requires an increase in the hydrocracking reaction temperature. The thermal cracking tendency of the molecular sieve is enhanced, but the hydrogenation reaction is inhibited, so that the catalyst's medium oil selectivity is not significantly improved. quality also suffers badly

Method used

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  • Hydrocracking catalyst and preparation method thereof
  • Hydrocracking catalyst and preparation method thereof
  • Hydrocracking catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Take 278g of NaY raw powder and put it into 800mL of clean water, raise the temperature to 95°C, and start to add dropwise (NH 4 ) 2 SiF 6 Aqueous solution, 307mL solution concentration is 72g / L (NH 4 ) 2 SiF 6 solution, stirring at constant temperature for 2 hours after the dropwise addition, filtering and drying after the completion of the constant temperature, the dry basis of the dried molecular sieve is 65.3wt%; the above-mentioned dried molecular sieve is added to the hydrothermal treatment device, under gauge pressure 0.25MPa, temperature Under the conditions of 610°C and treatment time of 1.0 hour, carry out hydrothermal treatment on molecular sieve; take 130g of molecular sieve after hydrothermal treatment and put it into 520mL aqueous solution of tetraethylammonium hydroxide with a mass concentration of 5.3%, and stir at constant temperature at 80°C for 4 hours , and then transfer the mixed material to a crystallization tank for hydrothermal crystallizatio...

Embodiment 2

[0048] Take 278g of NaY raw powder and put it into 800mL of clean water, raise the temperature to 100°C, and start to add dropwise (NH 4 ) 2 SiF 6 Aqueous solution, 182mL solution concentration is 55g / L (NH 4 ) 2 SiF 6 solution, stirring at constant temperature for 2 hours after the dropwise addition, filtering and drying after the completion of the constant temperature, the dry basis of the dried molecular sieve is 68.0wt%; the above-mentioned dried molecular sieve is added to the hydrothermal treatment device, under gauge pressure 0.30MPa, temperature Under the conditions of 670°C and treatment time of 2.0 hours, the molecular sieve was hydrothermally treated; 130g of the hydrothermally treated molecular sieve was put into 910mL of tetrapropylammonium hydroxide aqueous solution with a mass concentration of 7.5%, and stirred at 90°C for 4 hours , and then transfer the mixed material to a crystallization kettle for hydrothermal crystallization, the crystallization temperat...

Embodiment 3

[0050] Take 278g of NaY raw powder and put it into 1000mL of clean water, raise the temperature to 100°C, and start to add dropwise (NH 4 ) 2 SiF 6 Aqueous solution, 417mL solution concentration is 85g / L (NH 4 ) 2 SiF 6 solution, stirring at constant temperature for 3 hours after the dropwise addition, filtering and drying after the completion of the constant temperature, the dry basis of the dried molecular sieve is 67.2wt%; the above-mentioned dried molecular sieve is added to the hydrothermal treatment device, under gauge pressure 0.35MPa, temperature Under the conditions of 700°C and treatment time of 3.0 hours, the molecular sieve was hydrothermally treated; 130g of the hydrothermally treated molecular sieve was put into 1040mL of tetraethylammonium hydroxide aqueous solution with a mass concentration of 3.5%, and stirred at a constant temperature of 85°C for 3 hours , and then transfer the mixed material to a crystallization tank for hydrothermal crystallization, the...

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Abstract

The invention discloses a hydrocracking catalyst and a preparation method thereof. The hydrocracking catalyst comprises hydrogenation active metal components and a carrier, wherein the carrier comprises a modified Y-type molecular sieve and amorphous silica-alumina; the properties of the modified Y-type molecular sieve are as follows: the relative crystallinity is 110-150%, the molar ratio of SiO2 / Al2O3 is 55-100, the cell parameter is 2.425-2.435nm, the total pore volume is 0.55-1.0mL / g, and the volume of mesopores accounts for 70% or above of the total pore volume. The catalyst is suitable for being used as a middle distillate hydrocracking catalyst and has relatively high activity and selectivity of middle distillate; meanwhile, the quality of the produced middle distillate is high.

Description

technical field [0001] The invention relates to a hydrocracking catalyst and a preparation method thereof, in particular to a hydrocracking catalyst for producing high-quality middle distillate oil by hydrocracking and a preparation method thereof. Background technique [0002] With the recovery and development of the world economy, the demand for high-quality middle distillate oil products (that is, the power fuel of the aviation industry: jet fuel, and the main power fuel of the sea and land transportation industry: diesel oil) in the world's oil market has been increasing. At the same time, the reserves of oil and gas resources in the world are decreasing year by year, and the quality is deteriorating year by year, and the requirements for the quality of refined oil are getting higher and higher. Therefore, hydrocracking technology has become the best refining technology to produce high-quality middle distillates with its unique technical advantages. [0003] The hydrocr...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16C10G47/20
CPCB01J29/166B01J2229/24B01J2229/32C10G47/20C10G2300/70
Inventor 刘昶王凤来关明华杜艳泽黄薇赵红郝文月曹均丰
Owner CHINA PETROLEUM & CHEM CORP