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Improved diesel hydrocracking catalyst carrier and preparation method thereof

A catalyst carrier and hydrocracking technology, which is applied in the direction of catalyst carrier, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problems of average quality of middle distillate oil products, difficulty in exerting the best performance of catalysts, and low catalytic activity of catalysts, etc. Achieve good cracking effect, facilitate rapid transfer, and not easy to damage

Active Publication Date: 2020-02-07
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

CN1393521A discloses a medium-oil type hydrocracking catalyst and its preparation method. The carrier used in the catalyst is amorphous silica-alumina, composite molecular sieve of alumina, Y and β molecular sieve, wherein the composite molecular sieve is to burn off the former powder of β molecular sieve to remove template 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.
However, the above-mentioned hydrocracking catalyst carrier components are simply mechanically mixed, and the components in the catalyst are easily agglomerated into secondary particles, which makes the dispersion of the active components poor, and the prepared catalyst is difficult to exert the best performance.

Method used

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  • Improved diesel hydrocracking catalyst carrier and preparation method thereof
  • Improved diesel hydrocracking catalyst carrier and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0034] Take by weighing 201.3g tetraethylammonium bromide (98wt%, technical grade), 27.39g sodium hydroxide, 7.2g pseudo-boehmite (70wt%, technical grade), 870g water mix and stir to clear solution, then in Add 180g of white carbon black (98wt%, technical grade) to the solution under constant stirring, and continue to stir to obtain a uniform silica-alumina gel, and the silica-alumina gel was dynamically crystallized at 145° C. for 7 days, and the solid-liquid separation and After washing and drying, the β molecular sieve was obtained, coded as B1. The main properties of the β molecular sieve are shown in Table 1.

[0035] Add 3000ml of aluminum chloride solution (concentration: 1.5mol / L) into a 5000ml beaker, add 19g of B1 molecular sieve (99% on a dry basis) into the mixture, keep the temperature at 70°C, and continuously add 2mol / L of ammonia water until the pH value is 4 , evaporated at 80°C (evaporation temperature can be 50-90°C), dried the sucked white solid at 100°C fo...

Embodiment 2

[0038] Take by weighing 201.3g tetraethylammonium bromide (98wt%, technical grade), 27.39g sodium hydroxide, 7.2g pseudo-boehmite (70wt%, technical grade), 870g water mix and stir to clear solution, then in Add 180g of white carbon black (98wt%, technical grade) to the solution under constant stirring, and continue to stir to obtain a uniform silica-alumina gel, and the silica-alumina gel was dynamically crystallized at 145° C. for 7 days, and the solid-liquid separation and After washing and drying, the β molecular sieve was obtained, coded as B1. The main properties of the β molecular sieve are shown in Table 1.

[0039] Add 3000ml of aluminum chloride solution (concentration: 1.5mol / L) into a 5000ml beaker, add 28g of B1 molecular sieve (99% on a dry basis) into the mixture, keep the temperature at 70°C, and continuously add 2mol / L of ammonia water until the pH value is 4.3 , evaporated at 85°C, dried the sucked white solid at 100°C for 3 hours, and roasted at 500°C for 4 h...

Embodiment 3

[0042] Take by weighing 185.3g tetraethylammonium bromide (98wt%, technical grade), 22.65g sodium hydroxide, 10.3g pseudo-boehmite (70wt%, technical grade), 870g water mix and stir to clear solution, then in Add 180g of white carbon black (industrial grade) to the solution under constant stirring, and continue to stir to obtain a uniform silica-alumina gel, and dynamically crystallize the silica-alumina gel at 145°C for 7 days, after solid-liquid separation, washing and drying The β molecular sieve was obtained, coded as B2, and the main properties of the β molecular sieve are shown in Table 1.

[0043] Add 3000ml of aluminum chloride solution (concentration: 1.5mol / L) into a 5000ml beaker, add 60.5g of B2 molecular sieve (99% on a dry basis) into the mixture, keep the temperature at 70°C, and continuously add 2mol / L of ammonia water until the pH is 4. Evaporate at 85°C, dry the sucked white solid at 100°C for 3 hours, and roast at 500°C for 4 hours to obtain 296.4g (dry basis...

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Abstract

The invention discloses an improved diesel hydrocracking catalyst carrier and a preparation method thereof. The carrier raw materials include the following components and weight percentages: 3-35% molecular sieve, 5-75% γ-Al 2 O 3 , 15-75% amorphous silicon aluminum and 7-40% binder; the specific surface area of ​​the carrier is 200-450m 2 / g, the total pore volume is 0.35~0.75cm 3 / g. In the present invention, in the process of preparing the molecular sieve and alumina composite material, a molecular sieve that does not release the template is added. In the mixed liquid, the NH4 generated by the reaction of the aluminum salt and ammonia water is + In exchange with the alkali Na+ that balances the negative charge of the molecular sieve skeleton, during the roasting process, the organic template agent and NH in the molecular sieve are 4 + removal, thereby completing the ammonium exchange and template release of the zeolite molecular sieve during the preparation of composite materials. There is no need to separately perform the template release agent and ammonium exchange on the molecular sieve. The template agent has a supporting and protective effect on the molecular sieve channel structure. It is prepared with this carrier The hydrocracking catalyst can significantly reduce the freezing point of the diesel fraction and increase the cetane number of the diesel while ensuring a high yield of diesel.

Description

technical field [0001] The invention relates to a catalyst carrier, in particular to an improved diesel hydrocracking catalyst carrier and a preparation method thereof. Background technique [0002] With the rapid development of the economy, the demand for petroleum products has grown rapidly, and my country's hydrocracking processing capacity has also achieved rapid development. However, as the quality of raw oil processed in my country gradually becomes heavier and worse, the processing volume of high-sulfur crude oil is increasing year by year, and environmental protection has increasingly strict requirements on the refining process itself and the quality of petroleum products, which put forward higher requirements on the level of hydrocracking technology , while the catalyst plays a central role in the hydrocracking reaction, the key to the hydrocracking technology lies in the development and improvement of the catalyst. [0003] The conventional preparation methods of h...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J32/00B01J29/70B01J35/10C10G47/20
CPCC10G47/20B01J29/7007C10G2300/70B01J35/615B01J35/635B01J35/633
Inventor 明卫星赖波杨伟光徐田
Owner WUHAN KAIDI ENG TECH RES INST CO LTD
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