Optimized diesel hydrocracking catalyst and preparation method thereof

A hydrocracking and catalyst technology, which is applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of general product quality of middle distillates, difficulty in exerting optimal performance of catalysts, and low catalytic activity of catalysts, etc. , to achieve the effects of ensuring diesel oil yield, facilitating rapid transfer, and large pore volume

A hydrocracking and catalyst technology, which is applied in the direction of physical/chemical process catalysts, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of general product quality of middle distillates, difficulty in exerting optimal performance of catalysts, and low catalytic activity of catalysts, etc. , to achieve the effects of ensuring diesel oil yield, facilitating rapid transfer, and large pore volume

CN107051575AActive Publication Date: 2017-08-18WUHAN KAIDI ENG TECH RES INST CO LTD

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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

The invention discloses an optimized diesel hydrocracking catalyst and a preparation method thereof. The optimized diesel hydrocracking catalyst is prepared from the following raw materials in percentage by weight: 1 to 25 percent of a modified molecular sieve, 10 to 65 percent of gamma-Al2O3, 15 to 70 percent of amorphous silica-alumina, 9 to 40 percent of an adhesive and 10 to 35 percent of active metal oxide. The catalyst has a specific surface area of 200 to 400m<2> / g and a total pore volume of 0.30 to 0.65cm<3> / g. The catalyst is obtained by adding the modified molecular sieve into an inorganic aluminum salt solution for preparing the gamma-Al2O3, performing precipitation, drying and calcination to obtain a composite material of the molecular sieve and the gamma-Al2O3, and performing mixing, rolling, forming, drying and activating on the other materials and the composite material according to the material proportion of the catalyst. The molecular sieve in a catalyst carrier of the catalyst is high in silica-alumina ratio, high in dispersity in the carrier and large in specific surface area, so that the carrier has more uniform acidic sites; alumina makes contact with the molecular sieve more closely, so that the condensation point of a diesel distillate can be obviously reduced and the cetane number of diesel can be increased on the premise of ensuring high yield of the diesel.

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

Patent Timeline
18 Aug 2017
Publication
CN107051575A
IPC
B01J29/14; B01J29/16; B01J29/46; B01J29/48; B01J29/72; B01J29/76; B01J29/78; C10G47/20
CPC
C10G47/20; B01J29/146; B01J29/166; B01J29/46; B01J29/48; B01J29/7284; B01J29/7615; B01J29/7684
Inventors
明卫星; 石友良