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Hydrocracking catalyst for diesel and jet fuel production and preparation method thereof

A technology for jet fuel and hydrocracking, which is applied in catalyst activation/preparation, physical/chemical process catalysts, molecular sieve catalysts, etc. It can solve the problems of low crystallization retention of small-grain Y-type molecular sieves, difficulty in realization, and high preparation costs. Achieve the effects of excellent product selectivity, improved acidity and acid distribution, and high activity

Active Publication Date: 2020-11-06
WUHAN KAIDI ENG TECH RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN1382632A introduces a small-grain Y-type zeolite and its preparation method. The unit cell constant of the molecular sieve is 2.425-2.45nm, the crystallization retention is greater than 75%, and silicon tetrachloride gaseous state is used to contact the prepared molecular sieve. , modified small-grain Y-type molecular sieve, the small-grain Y-type molecular sieve prepared by the raw material has low crystallization retention, and the modification method adopted has high preparation cost and is difficult to realize in industry

Method used

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  • Hydrocracking catalyst for diesel and jet fuel production and preparation method thereof

Examples

Experimental program
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Effect test

preparation example Construction

[0028] Preparation of NaY molecular sieve directing agent: 6.00g sodium hydroxide (96wt% NaOH, technical grade), 1.24g sodium metaaluminate (41.0wt% Al) 2 O 3 , industrial grade), 18.75g distilled water, 15.00g silica sol (30wt% SiO 2 , industrial grade), mix evenly, ultrasonically shake for 1 h, and stir at 30 °C for 20 h to obtain a guiding agent, which is ready for use.

[0029] Preparation of modified Y-type molecular sieve (MNY-1): 1) 1.12g sodium hydroxide (96wt% NaOH, technical grade), 2.49g sodium metaaluminate (41.0wt% Al) 2 O 3 , industrial grade), 25.67g distilled water, 16.80g silica sol (30wt% SiO 2 , industrial grade) at 30 ° C and mix evenly, then slowly drop 1.84g of the directing agent into it, mix well, stir for 4h, and then add 0.74g of tetradecyldimethylbenzyl ammonium chloride (50wt% TDBAC, Industrial grade) was added dropwise and stirred for 1 hour to obtain a viscous aluminosilicate gel; the gel was put into the reaction kettle and crystallized at 80...

Embodiment 1

[0036] Weigh 2g MNY-1, 40g amorphous silica-alumina, 35g macroporous alumina, 23g small pore alumina, and 1g succulent powder additive in a kneader for dry mixing for 10min, and then add a certain amount of 3% nitric acid solution, Continue kneading for 30min; transfer the kneaded material to the extruder for extrusion molding; dry the extruded carrier for 20h, then calcinate at 500°C for 4h in an air atmosphere and cool to room temperature to obtain carrier a-1.

[0037] Weigh 20 g of carrier a-1 and immerse it in 40 mL of Ni-W immersion solution at room temperature for supersaturated immersion for 6 hours, filter and stand for 2 hours, then dry for 2 hours, and finally calcinate at 450 °C for 4 hours in an air atmosphere and then cool to room temperature to obtain a hydrogenation catalyst. A-1.

Embodiment 2

[0039] Weigh 5g MNY-1, 40g amorphous silica-alumina, 30g macroporous alumina, 25g small pore alumina, and 1g succulent powder in a kneader for dry mixing for 10min, then add a certain amount of 3% nitric acid solution, and continue to knead 30min; transfer the uniformly kneaded material to the extruder for extrusion molding; dry the extruded carrier for 20h, then calcinate at 500°C for 4h in an air atmosphere and cool to room temperature to obtain carrier a-2.

[0040] Weigh 20g of carrier a-2 and immerse it in 40mL Ni-W immersion solution at room temperature for supersaturated immersion for 6h, filter and stand for 2h, then dry for 2h, and finally calcinate at 450°C for 4h in an air atmosphere and then cool to room temperature to obtain a hydrogenation catalyst A-2.

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Abstract

The invention discloses a hydrocracking catalyst for diesel and jet fuel production and a preparation method thereof, which includes a carrier and a metal active component. The metal active component is loaded on the carrier. The carrier is composed of a weight percentage of 1 to 8 wt%. It is composed of modified Y-type molecular sieve, 20-60wt% amorphous silica alumina, 10-50wt% macroporous alumina and 10-40wt% small-pore alumina; the metal active component accounts for 10% of the weight of the catalyst. ~40wt%. The mesoporous NaY type molecular sieve prepared by the invention is a special Y molecular sieve composed of nanocrystals aggregated into a mesoporous structure. It has a high specific surface and a developed mesoporous structure, which can not only improve the hydrogenation activity, but also facilitate the diffusion and diffusion of reaction products. The selectivity of the target product and the carbon holding capacity are also greatly enhanced, which reduces the probability of over-cracking and secondary cracking and improves the activity of the catalyst and product selectivity.

Description

technical field [0001] The present invention relates to a catalyst, in particular to a hydrocracking catalyst for diesel and jet fuel production and a preparation method thereof. Background technique [0002] The main features of hydrocracking technology are strong adaptability of raw materials, flexible product schemes, high selectivity of target products, good product quality and high added value, and can directly produce a variety of high-quality petroleum products (gasoline, jet fuel, diesel, lubricating oil and base oil, etc.) and high-quality chemical raw materials (benzene, toluene, xylene, ethylene, etc.). The core of hydrocracking technology is hydrocracking catalyst. People have been working on modifying acidic components or substrates to adjust the physicochemical properties of the carrier to make the hydrocracking catalyst meet the needs of the hydrocracking process. [0003] For hydrocracking catalysts, while paying attention to the activity of the catalyst, th...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/16C10G49/08
CPCC10G49/08B01J29/166B01J37/0207C10G2400/04C10G2300/1077B01J35/617B01J35/633
Inventor 冯春峰许莉王杰华张然明卫星施苗
Owner WUHAN KAIDI ENG TECH RES INST CO LTD