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Cracking assistant for improving low-carbon olefin concentration

A catalytic cracking aid and concentration technology, used in cracking, catalytic cracking, molecular sieve catalysts, etc., can solve the problem of weakening the conversion capacity of heavy oil, and achieve improved conversion capacity of heavy oil, high conversion activity of heavy oil, good coke and dry gas selectivity Effect

Active Publication Date: 2014-12-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0021] At present, for the vast majority of catalytic cracking units, under the premise of the same liquefied gas yield, increasing the propylene concentration in the liquefied gas is an important way to improve the economic benefits of the catalytic cracking unit. The propylene additive of transition metal modified MFI molecular sieve is used in catalytic cracking process, the concentration of propylene in liquefied gas is low, the yield of dry gas and coke is high, and when the addition amount is large, the conversion capacity of heavy oil will be weakened

Method used

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  • Cracking assistant for improving low-carbon olefin concentration
  • Cracking assistant for improving low-carbon olefin concentration
  • Cracking assistant for improving low-carbon olefin concentration

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preparation example Construction

[0032] In the preparation method of the catalytic cracking aid provided by the present invention, the first clay-containing phospho-aluminum inorganic binder, based on its dry basis weight, contains Al 2 O 3 15-40% by weight of aluminum component, as P 2 O 5 45-80% by weight of the phosphorus component and 1-40% by weight of the first clay on a dry basis, with a P / Al weight ratio of 1.0-6.0, a pH of 1.0-3.5, and a binder solid content of 15 ~60% by weight. The preparation method of the first clay-containing phosphorus aluminum compound inorganic binder includes:

[0033] (1) The alumina source, the first clay and water are beaten and dispersed into a slurry with a solid content of 8 to 45% by weight; the alumina source is aluminum hydroxide and / or aluminum oxide that can be peptized by acid. The first clay on dry basis and Al 2 O 3 The calculated weight ratio of the alumina source is 1-40:15-40;

[0034] (2) Under stirring, add concentrated phosphoric acid to the slurry obtained i...

specific Embodiment approach

[0045] A specific embodiment of the preparation method provided by the present invention includes:

[0046] (1) According to molecular sieve: ammonium salt: H 2 The weight ratio of O=1:(0.1~1):(5~10), the sodium type molecular sieve with MFI structure is exchanged at room temperature to 100℃ for 0.3~1 hour, then filtered and dried;

[0047] (2) The ammonium-exchanged molecular sieve is impregnated and modified with a phosphorus-containing compound solution and a solution containing a transition metal compound, and then dried and calcined; the calcining temperature is 400-800°C; The metal compound solution impregnating the molecular sieve after the ammonium exchange may be impregnated with a solution containing both a phosphorus compound and a transition metal compound, or may be impregnated with a solution containing a phosphorus compound and a solution containing a transition metal compound respectively; It can be carried out one or more times, preferably, impregnation is carried ...

Embodiment 1

[0061] Put 5kg NH 4 Cl is dissolved in 100kg water, and 10kg (dry basis) crystallized product ZSM-5 molecular sieve (produced by Qilu Branch of Sinopec Catalysts, synthesized by amine method, SiO 2 / Al 2 O 3 =50), after exchange at 90℃ for 0.5h, filter cake to be obtained; remove 0.9kg H 3 PO 4 (Concentration 85% by weight) and 0.81kgFe(NO 3 ) 3 ·9H 2 O was dissolved in 9kg of water, the impregnating solution was mixed with the filter cake, soaked, dried, and roasted at 550°C for 2 hours; 1kg of the above roasted molecular sieve was taken and mixed with 0.536kg of ethyl orthosilicate (Beijing Chemical Reagent Company, Analytical purity, SiO 2 The content is 28% by weight), 0.333kg of tetrapropylammonium bromide (produced by Guangzhou Dayou Fine Chemical Factory, analytically pure, 99%) and 1.2L of water are mixed, and placed in a crystallization kettle with polytetrafluoroethylene lining. After being statically crystallized at 150°C for 20 hours and then cooled to room temperatur...

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Abstract

The invention discloses a cracking assistant for improving a low-carbon olefin concentration. The cracking assistant comprises a modified MFI molecular sieve, a first clay-containing phosphor-aluminum inorganic binder and other inorganic binders, and second clay or no second clay. The first clay-containing phosphor-aluminum inorganic binder comprises an aluminum component, a phosphor component and first clay. The modified MFI molecular sieve contains phosphor and one or more of transition metals such as Fe, Co, Ni, Cu, Mn, Zn, Sn and Bi. There is not an absorption peak at the wavelength of 1633cm<-1> in a modified MFI molecular sieve infrared spectra obtained by trimethylpyridine as a probe molecule. Phosphorus distribution D is in a range of 0-0.8 and is a TEM-EDX-characterized ratio of phosphorus content of a part of a molecular sieve crystal grain to phosphorus content of the center of the molecular sieve crystal grain, wherein a distance between the part of the molecular sieve crystal grain and the edge of the molecular sieve crystal grain is 1 / 5 of a distance between the edge of the molecular sieve crystal grain and the center of the molecular sieve crystal grain. The cracking assistant is used for catalytic cracking, can improve a catalytic cracking liquefied gas yield, can improve yields of low-carbon olefins such as ethane, propylene and isobutene, can improve a low-carbon olefin concentration of catalytic cracking liquefied gas, can improve a heavy oil conversion capacity of a catalyst composition, and can improve the selectivity of dry gas and coke.

Description

Technical field [0001] The invention relates to a cracking aid used for catalytic cracking to produce low-carbon olefins. Background technique [0002] Low-carbon olefins are important organic chemical raw materials, and their demand is increasing year by year. Fluidized catalytic cracking is an important method for producing low-carbon olefins. In order to increase the yield of low-carbon olefins, it is an effective technical approach to use catalysts or additives containing zeolite with MFI structure in the catalytic cracking process. [0003] USP 3,758,403 earlier disclosed that the method of adding ZSM-5 zeolite to the catalytic cracking catalyst can increase the octane number of gasoline and increase C 3 ~C 4 The yield of olefins. For example, after adding 1.5, 2.5, 5 to 10% of ZSM-5 zeolite to a conventional catalyst containing 10% REY, the gasoline octane number will increase and the yield of low-carbon olefins will increase; the use of ZSM-5 zeolite will help It also has ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/46B01J29/48B01J29/40C10G11/05
Inventor 朱玉霞沈宁元陈蓓艳罗一斌欧阳颖邓景辉田辉平蒋文斌黄志青宋海涛
Owner CHINA PETROLEUM & CHEM CORP
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