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Hydrocarbon oil catalytic cracking catalyst rich in naphthenic cyclic hydrocarbon,preparation method and application method thereof

A technology for catalytic cracking and naphthenic hydrocarbons, applied in catalytic cracking, physical/chemical process catalysts, molecular sieve catalysts, etc. rate drop etc.

Active Publication Date: 2020-10-27
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the catalyst is used in the conversion of naphthenes to ethylene and the yield is not high
[0006] CN104607255B discloses a method for preparing a low-L acid high-B acid catalytic cracking catalyst impregnated with boric acid. The method improves the coke selectivity of the catalyst by introducing boron into the catalyst and improves the yield of gasoline and diesel, but the low Carbon yield drops
The composition is used to crack hydrocarbon feeds, especially when processing high-nickel and high-vanadium residue feedstocks, to reduce hydrogen and coke yields, but not to improve low-carbon olefins yields

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  • Hydrocarbon oil catalytic cracking catalyst rich in naphthenic cyclic hydrocarbon,preparation method and application method thereof

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preparation example Construction

[0058] Catalytic cracking catalyst provided by the present invention, a kind of preparation method comprises the following steps: beating natural mineral matter and water, then adding inorganic oxide binder thereinto, stirring to obtain slurry A; Y-type molecular sieve and shape-selective molecular sieve and Water beating to obtain molecular sieve slurry, mixing slurry A and molecular sieve slurry, finally adding boron-aluminum-silicon composite oxide, beating and stirring, to obtain catalyst slurry, and spray-drying catalyst slurry to obtain catalyst microspheres, and the obtained catalyst microspheres were heated at 450 Calcining at -550°C for 0.5-4 hours, preferably 1-3 hours, for example, 2 hours at 500°C, to obtain a catalytic cracking catalyst.

[0059] According to the method for preparing a catalytic cracking catalyst provided by the present invention, one embodiment, the method for preparing a boron-aluminum-silicon composite oxide includes the following steps:

[0060]...

Embodiment 1

[0088] (1) Preparation of boron-aluminum-silicon composite oxide: Add 602g of deionized water to the beaker, then add 94g of SB powder, disperse in the homogenizer for 30min, then add 100mL of slurry dispersed with 53g of boric acid, in the homogenizer Disperse for 20 minutes, and finally add 20 g of hydrochloric acid to acidify to obtain mixture 3, whose pH value is 1.0; add 90 g of silica sol to mixture 3, stir for 30 minutes, dry at 120 ° C for 12 h, and roast at 650 ° C for 4 h to obtain boron-aluminum-silicon composite oxide object, denoted as BAS1. The composition of the boron-aluminum-silicon composite oxide: B 2 o 3 The content is 23.5% by weight, and the silicon oxide content is 21.2% by weight; the content of aluminum oxide is 55.3% by weight, has a rod-like structure, the shortest side of the crystal grain is 10nm, the pore volume is 0.28ml / g, and the pore distribution (in terms of pore diameter 2-100nm Pores as the benchmark): 2-2 / g.

[0089] (2) Catalyst prepa...

Embodiment 2

[0092] (1) Preparation of boron-aluminum-silicon composite oxide: add 302g of deionized water to a beaker, then add 94g of pseudoboehmite dry powder, disperse in a homogenizer for 30min; add 300g of deionized water to another beaker, Then 53g of boric acid was added, heated at 80°C for 30min to dissolve it; then the two slurries were mixed, dispersed in a homogenizer for 20min, and 20g of hydrochloric acid was added for acidification to obtain mixture 3, whose pH value was 2.41. Add 90g of water glass (SiO 2 Concentration 251.3g / L, modulus 3.6), stirring for 30min, drying at 100°C for 24h, and calcination at 800°C for 2h to obtain boron-aluminum-silicon composite oxide, denoted as BAS2. The composition of the boron-aluminum-silicon composite oxide: B 2 o 3 The content is 23.5% by weight, the content of silicon oxide is 21.2% by weight; the content of aluminum oxide is 55.3% by weight, it has a rod-like structure, the shortest side of the crystal grain is 11nm, the pore volum...

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Abstract

The invention relates to a hydrocarbon oil catalytic cracking catalyst rich in naphthenic cyclic hydrocarbon, a preparation method and an application method thereof. The catalytic cracking catalyst comprises natural minerals, a boron-aluminum-silicon composite oxide, an inorganic oxide binder, a Y-type molecular sieve and a shape-selective molecular sieve. The preparation method comprises the following steps: preparing a boron-aluminum-silicon composite oxide, forming a slurry containing boron-aluminum-silicon composite oxide, a molecular sieve, natural mineral substance, an inorganic oxide binder and water, and carrying out spray drying, wherein the preparation method of the boron-aluminum-silicon composite oxide comprises the steps of mixing an aluminum oxide precursor, a boron precursorand water, adding an acid, acidifying to obtain a mixture, mixing the mixture with a silicon precursor, drying, and roasting. The catalytic cracking catalyst provided by the invention has relativelyhigh naphthenic cyclic hydrocarbon-containing conversion activity, is used for conversion of hydrocarbon oil rich in naphthenic cyclic hydrocarbon, and has relatively high ethylene yield and propyleneyield.

Description

technical field [0001] The invention relates to a catalytic cracking catalyst for producing light olefins from hydrocarbon oil rich in naphthenic naphthenes, and a preparation method and application method thereof. Background technique [0002] Low-carbon olefins such as ethylene, propylene, and butene are essential chemical raw materials and can be used to synthesize resins, fibers, and rubber. Among them, propylene is an important raw material used to manufacture petrochemical products after ethylene, and is mainly used to produce chemical products such as polypropylene, acrylonitrile, and propylene oxide. At present, propylene at home and abroad mainly comes from the by-products of thermal cracking to produce ethylene. The second largest source of propylene is the FCC unit, which provides about 30% of the demand. In the United States, the FCC unit provides the demand for propylene from petrochemical products. half of. Therefore, it is an effective and efficient way to i...

Claims

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Application Information

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IPC IPC(8): B01J29/08B01J35/10C10G11/04
CPCB01J29/084C10G11/05B01J35/615B01J35/647Y02P20/52
Inventor 王鹏孙敏陈惠严加松田辉平王丽霞宋海涛林伟张久顺
Owner CHINA PETROLEUM & CHEM CORP