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Optimized diesel hydrocracking catalyst and preparation method thereof

A hydrocracking and catalyst technology, applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems that the catalyst is difficult to exert the best performance, the product quality of middle distillate oil is average, and the catalytic activity of the catalyst is not high. , to achieve the effects of fast transfer, guaranteed diesel yield and large pore volume

Active Publication Date: 2020-02-14
WUHAN KAIDI ENG TECH RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
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AI Technical Summary

Problems solved by technology

[0004] However, in the hydrocracking catalyst prepared by the existing method, the components are simply mechanically mixed, and the components in the catalyst are easily agglomerated into secondary particles, which makes the dispersion of the active component poor, and the prepared catalyst is difficult to Play the best performance, but also have the problem of complicated preparation process and high cost
For example: CN98114489.6 discloses a hydrocracking catalyst, amorphous silica-alumina and Y-type molecular sieve are used as cracking components, and metal oxides of Group VIB and Group VIII are hydrogenation components, and a series of hydrocracking is adopted Production of middle distillate oil, the catalyst has good nitrogen resistance, but its preparation method is relatively complicated and the preparation cost is relatively high
CN139352IA discloses a medium-oil type hydrocracking catalyst and its preparation method. The carrier used in the catalyst is amorphous silica-alumina, alumina and composite molecular sieves of Y and β, wherein the composite molecular sieve is obtained by burning the former powder of β molecular sieve to remove the template agent. After mixing with modified Y molecular sieve, it is obtained by ammonium exchange treatment. The catalytic activity of this catalyst is not high, and the product quality of middle distillates of jet fuel and diesel oil is average, which needs to be further improved.

Method used

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  • Optimized diesel hydrocracking catalyst and preparation method thereof
  • Optimized diesel hydrocracking catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Take by weighing 201.3g tetraethylammonium bromide (technical grade), 27.39g sodium hydroxide, 7.2g pseudo-boehmite (70wt%, technical grade), 870g water mix and stir to clear solution, then under constant stirring Add 180g of white carbon black (industrial grade) to the solution, and continue to stir to obtain a uniform silica-alumina gel; the silica-alumina gel was dynamically crystallized at 145°C for 7 days, and after solid-liquid separation, washing and drying, it was placed in the air Roast at 550°C in stream for 8 hours to obtain β molecular sieve. After the template is removed, ammonium exchange is carried out twice at 80°C with a concentration of 0.5mol / L ammonium chloride solution. The liquid-solid ratio is 10:1. After washing and drying, Carry out hydrothermal treatment again, under water vapor pressure 0.15MPa, treatment temperature is 600 ℃, treatment time is 2.5 hours, carry out aluminum salt treatment afterwards, put the molecular sieve after hydrothermal t...

Embodiment 2

[0039] Modified molecular sieve is the same as the β modified molecular sieve in embodiment 1; Molecular sieve and γ-Al 2 o 3 Composite material is the same as embodiment 1; Composite material 195.5g (dry basis 93%), amorphous silicon aluminum 204.5g (dry basis 88%), MoO 3 108.5g (99.1wt%), Ni(NO 3 ) 2 ·6H 2 O (NiO, 26.6wt%) was mixed with 163.4g and 360g of binder (25% on a dry basis), and rolled in a wheel mill for 40 minutes to form an extrudable paste, extruded into strips, and shaped as Columnar shape with a length of 3-8nm, dried at 120°C for 20 hours, and calcined at 500°C for 5-6 hours to obtain a hydrocracking catalyst, numbered C-2, and its properties are shown in Table 2.

Embodiment 3

[0041] The modified molecular sieve is the same as the β modified molecular sieve in Example 1; 140g ammonium oxalate is weighed and mixed with 3000ml aluminum chloride solution (concentration is 1.5mol / L) in a 5000ml beaker, and 52.6g (dry basis 98%) is modified Molecular sieves were added to the mixture, kept at a constant temperature of 70°C, continuously added 2mol / L ammonia water until the pH value was 4, evaporated at 85°C, dried at 100°C for 3 hours, and roasted at 500°C for 4 hours to obtain molecular sieves γ-Al 2 o 3 Composite material 272.8g (dry basis 93%), conversion rate 72.3%. Molecular sieve and γ-Al 2 o 3 Composite material 173.2g (dry basis 93%), amorphous silicon aluminum 238.6g (dry basis 88%), MoO 3 108.5g (99.1wt%), Ni(NO 3 ) 2 ·6H 2 O (NiO, 26.6wt%) was mixed with 116.7g and 360g of binder (25% on a dry basis), and rolled in a wheel mill for 40 minutes to form an extrudable paste, extruded into strips, and shaped as Columnar shape with a length o...

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Abstract

An optimized diesel hydrocracking catalyst and a method for preparing same. Raw materials comprise the following components in percentage by weight: 1-25% of modified molecular sieve, 10-65% of γ-Al2O3, 15-70% of amorphous silica-alumina, 9-40% of binder, and 10-35% of active metal oxide. The specific surface area of the catalyst is 200-450 m2 / g, and the total pore volume is 0.30-0.65 cm3 / g. To obtain a carrier, a modified molecular sieve is added to an inorganic aluminum salt solution used for preparing γ-Al2O3, and precipitation, drying, and roasting are performed to obtain a composite of molecular sieve and γ-Al2O3; then the remaining materials are mixed with the composite according to the material proportion of the catalyst, and rolling, forming, drying, and activation are performed to obtain the catalyst. The molecular sieve in the catalyst carrier has a high silica / alumina ratio and high specific surface area, and is highly dispersed in the carrier; thus, the carrier has more uniform acid sites, and alumina is in closer contact with the molecular sieve; and therefore, the catalyst can remarkably reduce the pour point of a diesel fraction and improve the cetane number of diesel while guaranteeing a high diesel yield.

Description

technical field [0001] The invention relates to a catalyst, in particular to an optimized diesel hydrocracking catalyst and a preparation method thereof. Background technique [0002] Hydrocracking is a very important technology for the efficient conversion of heavy oil and the production of clean oil products in the oil refining industry. It can process heavy crude oil with high sulfur and high metals. It has a wide source of raw materials, high production flexibility, good product quality and middle distillate Features such as high oil yield. Hydrocracking technology can directly produce low-aromatic, low-sulfur and low-nitrogen high-quality middle distillate products from vacuum diesel oil (VGO), which can meet increasingly stringent environmental protection requirements, and the catalyst plays a central role in the hydrocracking reaction. The key to hydrocracking technology lies in the development and improvement of catalysts. [0003] The conventional preparation meth...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/14B01J29/16B01J29/46B01J29/48B01J29/72B01J29/76B01J29/78C10G47/20
CPCB01J29/146B01J29/166B01J29/46B01J29/48B01J29/7284B01J29/7615B01J29/7684B01J29/7692B01J29/7815B01J29/7884B01J29/7892B01J35/1019B01J35/1033C10G47/20C10G2300/1037C10G2300/70
Inventor 明卫星石友良许莉杨伟光赖波王春锋
Owner WUHAN KAIDI ENG TECH RES INST CO LTD
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