Preparation method of catalytic cracking catalyst for blending and refining dense oil

一种催化裂化、催化剂的技术,应用在催化裂化、物理/化学过程催化剂、分子筛催化剂等方向,能够解决难以适应催化裂化等问题,达到高催化裂化活性、高转化率、高汽油收率的效果

Active Publication Date: 2018-07-31
SHANDONG DUOYOU TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] Due to the small pores of traditional microporous molecular sieves, it shows an obvious effect of restricting the diffusion of larger raw material molecules, especially when some pores are blocked by heavy metals, making it difficult for pure microporous molecular sieves to be suitable for blending with high iron content. Catalytic cracking of tight oil requires the use of molecular sieve materials with large pore size and no diffusion limitation for reactant molecules

Method used

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  • Preparation method of catalytic cracking catalyst for blending and refining dense oil
  • Preparation method of catalytic cracking catalyst for blending and refining dense oil
  • Preparation method of catalytic cracking catalyst for blending and refining dense oil

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0052] Based on the dry basis weight of the catalytic cracking catalyst, the mass percent of each component in the catalyst is: 15% of the first molecular sieve component, 15% of the second molecular sieve component, and 15% of the modified pseudo-boehmite , pseudo-boehmite 5%, clay 40% and binder 10%.

[0053] One, prepare the second molecular sieve component, the preparation method is as follows:

[0054] In the first step, 2.55 kg of sodium silicate is mixed with 2.60 kg of water to obtain solution one,

[0055] Mix 0.035 kg of sodium hydroxide, 0.164 kg of sodium aluminate and 1.60 kg of water to obtain solution 2, add solution 1 to solution 2 at a constant speed, control the feeding time of solution 1 at 1.0 hour, stir for 3 hours after adding, and then heat up Continue stirring at 100°C for 8 hours to obtain a Y zeolite nano precursor;

[0056] In the second step, 6.949 kilograms of 1-hexadecyl-3-methyl imidazole bromide and 24 kilograms of water are mixed to obtain so...

Embodiment 2

[0072] Based on the dry basis weight of the catalytic cracking catalyst, the mass percent of each component in the catalyst is: 35% of the first molecular sieve component, 25% of the second molecular sieve component, and 10% of the modified pseudo-boehmite , pseudo-boehmite 9%, clay 11% and binder 10%.

[0073] One, prepare the second molecular sieve component, the preparation method is as follows:

[0074] In the first step, 2.55 kg of sodium silicate is mixed with 2.60 kg of water to obtain solution one,

[0075] Mix 0.035 kg of sodium hydroxide, 0.164 kg of sodium aluminate and 1.60 kg of water to obtain solution 2, add solution 1 to solution 2 at a constant speed, control the feeding time of solution 1 at 0.5 hours, stir for 3 hours after adding, and then heat up Continue stirring at 100°C for 8 hours to obtain a Y zeolite nano precursor;

[0076] In the second step, 6.949 kilograms of 1-hexadecyl-3-methyl imidazole bromide and 24 kilograms of water are mixed to obtain s...

Embodiment 3-5

[0091] Catalytic cracking catalysts were prepared according to the method of Example 1. The difference was that the feed amounts were shown in Table 2 below, and spray drying was carried out after mixing and beating evenly. The feed amounts of each component were in parts by weight, thereby respectively preparing Catalytic cracking catalysts C-3 to C-5. Catalyst components are shown in Table 2 in the embodiment 1-5.

[0092] Components in catalytic cracking catalysts in Table 2 Examples 1-5 (on a dry basis)

[0093]

[0094] It has been proved by experiments that the clay can be one or a mixture of kaolin, halloysite, montmorillonite, diatomaceous earth, halloysite, saponite, retortite, sepiolite, attapulgite and bentonite; The binder can be one or more of alumina sol, silica sol or silica-alumina gel. The first molecular sieve component is one or more mixtures of rare earth Y-type molecular sieve REY, rare earth ultra-stable Y-type molecular sieve REUSY, and ultra-stable...

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Abstract

The invention discloses a preparation method of a catalytic cracking catalyst for blending and refining dense oil. The method comprises the following concrete steps: under a stirring condition, addinga first molecular sieve ingredient, a second molecular sieve ingredient, modified pseudo-boehmite and pseudo-boehmite into water, mixing to obtain seriflux, adding hydrochloric acid into the obtainedseriflux to carry out peptizing, stirring for 30min, then adding clay and a binding agent successively, mixing, then beating, afterwards, performing spray drying to obtain a catalyst microsphere, roasting the microsphere for 30min at 550 DEG C, washing the microsphere by using an ammonium salt solution at 20-80 DEG C until the sodium oxide content is less than 0.20wt%, finally rinsing the catalyst microsphere by using deionized water, filtering, and then drying the catalyst microsphere to obtain the catalytic cracking catalyst for the blending and refining dense oil. The preparation method has the following beneficial effects: the catalytic cracking catalyst has a relatively great matrix specific surface area, shows relatively high catalytic cracking activity in the process of performingcatalytic cracking reaction on raw oil of the blending and refining dense oil, has a relatively high conversion rate in the process of performing catalytic cracking treatment on the dense oil with relatively high blending and refining alkaline nitrogen compound content (i.e., the alkaline nitrogen content of mixed oil is about 1,200-2,000mu g / g), can be used for obtaining relatively high gasolineand diesel oil yield, and particularly has relatively high yield for light oil such as gasoline.

Description

[0001] This case is a divisional application. The invention name of the original application is: a catalytic cracking catalyst for blending tight oil and its preparation method. The filing date of the original application is: 2016-01-29, and the application number of the original application is: 201610063454.2. technical field [0002] The invention relates to the technical field of catalysts, in particular to a method for preparing a catalytic cracking catalyst blended with tight oil. Background technique [0003] Fluid catalytic cracking, as an important means of secondary processing of crude oil, occupies a pivotal position in the oil refining industry, and every small progress of it will bring huge economic benefits to the enterprise. Fluid catalytic cracking catalyst is one of the technical cores of the catalytic cracking process, and its technological progress is also an important means for the fluid catalytic cracking process to obtain the maximum benefit. [0004] In...

Claims

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Application Information

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Patent Type & AuthorityApplications(China)
IPC IPC(8): B01J29/08B01J29/03B01J35/10C10G11/18C10G11/05
CPCC10G11/05C10G11/18B01J29/005B01J29/03B01J29/084C10G2400/04C10G2400/02C10G2300/70B01J35/615B01J35/633
Inventor于心玉郭万里
OwnerSHANDONG DUOYOU TECH