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Catalytic cracking catalyst and preparation method thereof

A catalytic cracking and catalyst technology, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problems of unstable molecular sieve framework and lower crystal retention, so as to improve hydrothermal stability, reduce reaction dosage, Effect of lowering exhaust gas temperature

Active Publication Date: 2018-10-26
QINGDAO RUNQIAN HI TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In this way, it is difficult to avoid the pollution of the waste filtrate to the environment caused by the repeated exchange and roasting of molecular sieves. Moreover, different degrees of aluminum extraction and silicon supplementation will lead to instability of the molecular sieve skeleton to a certain extent, greatly reducing its Crystal retention
At present, most patents and documents mainly use SiCl 4 The improvement and improvement of the catalyst performance can be achieved by modifying the molecular sieve, and directly through SiCl 4 There are few reports on the reaction with catalytic cracking catalysts to improve catalytic performance and stabilize the skeleton structure

Method used

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  • Catalytic cracking catalyst and preparation method thereof
  • Catalytic cracking catalyst and preparation method thereof
  • Catalytic cracking catalyst and preparation method thereof

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preparation example Construction

[0033] The preparation method of the phosphorus-silicate-aluminum glue is: phosphoric acid and pseudo-boehmite are prepared under acidic conditions, and the phosphorus-aluminum glue is prepared, P 2 o 5 / Al 2 o 3 Mass ratio=2.8-5.0, the reaction temperature is controlled between 55-85°C, the solid content of the slurry is 40% according to phosphorus pentoxide and aluminum oxide during preparation, slowly add silica sol and stir in the phosphorus-aluminum glue, so that The pH of the system is controlled between 2.5-4.0.

[0034] Described silica sol is alkaline silica sol, and it contains SiO 2 20-40wt%, Na 2 O≤0.2wt%, pH 9-10, SiO 2 Colloidal particle diameter 7-13nm.

[0035] A preparation method for catalytic cracking catalyst, comprising the following steps:

[0036] (1) Clay and deionized water are mixed and beaten until fully uniform, and active components and binders are respectively added to the slurry, mixed and stirred, spray-dried and granulated after acidifi...

Embodiment 1

[0059] (1) Mix 1658g of kaolin and deionized water for beating, and add 1000g of USY cross-baked molecular sieve and 2027g (calculated as phosphorus pentoxide, aluminum oxide and silicon oxide) of phosphorus-silicon-alumina gel to the slurry and mix and stir 3h, beating evenly and then spray drying to obtain the primary product.

[0060] (2) 1000 g of the obtained primary product was roasted in a muffle furnace at 380° C. for 1.5 h to obtain a roasted product, and after the reaction, the roasted product was taken out and cooled to 300° C.

[0061] (3) Introduce gaseous SiCl with a temperature of 85°C into the reactor containing the roasted product 4 120g.

[0062] (4) The reacted product was beaten with 4500 g of deionized water, washed with 5000 g of deionized water, filtered, and dried to obtain catalyst sample 1.

Embodiment 2

[0064] (1) Mix 1658g of kaolin and deionized water for beating, and add 1000g of REY cross-baked molecular sieve and 2027g (calculated as phosphorus pentoxide, aluminum oxide and silicon oxide) of phosphorus-silicon-aluminum glue to the slurry and mix and stir 3h, beating evenly and then spray drying to obtain the primary product.

[0065] (2) 1000 g of the obtained primary product was roasted in a muffle furnace at 380° C. for 1.5 h to obtain a roasted product, and after the reaction, the roasted product was taken out and cooled to 300° C.

[0066] (3) Introduce gaseous SiCl with a temperature of 85°C into the reactor containing the roasted product 4 120g.

[0067] (4) The reacted product was beaten with 4500g of deionized water, washed with 5000g of deionized water, finally filtered, and dried to obtain catalyst sample 2.

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Abstract

The invention discloses a catalytic cracking catalyst. The catalytic cracking catalyst is prepared from, by weight, 20-45 parts of active components, 35-45 parts of clay and 10-45 parts of adhesive. The adhesive is calculated based on oxide, and the adhesive is phosphorus silica-alumina gel. The invention further discloses a preparation method of the catalytic cracking catalyst. The preparation method includes the steps that the clay and deionized water are mixed and pulped to be fully uniform, the active components and the adhesive are added into pulp, mixing and stirring are conducted, spray drying and pelleting are conducted after acidification, and a head product is obtained; the head product is calcined at the set temperature, a calcined product is obtained, and the cauterant decrease of the calcined product is controlled; the calcined product and silicon tetrachloride are subjected to a contact reaction at a set ratio, the reaction temperature is controlled at the set temperature, the product is washed, filtered and dried after the reaction is completed, and the catalytic cracking catalyst is obtained. According to the catalyst, multiple times of exchange and calcination of the active components are not needed, and the process is simple and environmentally friendly. The adopted phosphorus silica-alumina gel is good in adhesion, no acid gas is generated in the calcination process, equipment is prevented from being corroded, and the energy consumption and the production cost of the catalyst are reduced.

Description

technical field [0001] The invention relates to the technical field of catalyst preparation, in particular to a catalytic cracking catalyst and a preparation method thereof. Background technique [0002] Catalytic cracking (FCC) is an important secondary processing process of crude oil and occupies a pivotal position in the oil refining industry. With the increasingly heavy and inferior raw material oil and increasingly stringent environmental protection regulations, the production of catalysts that can improve the cracking performance of catalysts and meet environmental protection requirements has become one of the current hot research. [0003] In 1949, Breck of UCC successfully synthesized Y molecular sieve with industrial application value for the first time. It has a regular pore structure and is based on β cages and hexagonal column cages to form an octahedral zeolite with a supercage structure. Y molecular sieve shows high stability and catalytic activity in the crac...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/08C10G11/05
CPCB01J29/08B01J2229/16B01J2229/24C10G11/05
Inventor 盖新清解宏伟
Owner QINGDAO RUNQIAN HI TECH CO LTD
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