Cracking gasification catalytic composition, preparation method thereof, and cracking gasification method of petroleum hydrocarbons

A composition and compound technology, applied in chemical instruments and methods, physical/chemical process catalysts, cracking, etc., can solve the problems of potassium loss, low cracking activity, high gasification temperature, etc., and achieve improved gasoline yield and high catalytic The effects of cracking activity and low gasification temperature

Active Publication Date: 2016-12-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The purpose of the present invention is to provide a cracking gasification catalytic composition, its preparation method and the cracking gasification method of petroleum hydrocarbons, to overcome the high gasification temperature, low cracking activity, potassium serious loss problem

Method used

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  • Cracking gasification catalytic composition, preparation method thereof, and cracking gasification method of petroleum hydrocarbons
  • Cracking gasification catalytic composition, preparation method thereof, and cracking gasification method of petroleum hydrocarbons
  • Cracking gasification catalytic composition, preparation method thereof, and cracking gasification method of petroleum hydrocarbons

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Experimental program
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preparation example Construction

[0047] In the preparation method of the above-mentioned mesoporous active material, the room temperature is usually 5-40°C, for example, 5°C, 10°C, 15°C, 20°C, 25°C, 30°C or 35°C.

[0048]In addition, optionally, the preparation method of the above-mentioned active mesoporous material may also include the step of roasting the dried product, and the conditions of the roasting generally include that the roasting temperature may be 500-700° C., and the roasting time may be 1-4 hours. .

[0049] In the preparation method of the above-mentioned mesoporous active material, the type of phosphorus source described in step (4) can be a conventional choice in the art, for example, can be selected from ammonium phosphate, diammonium hydrogen phosphate, ammonium dihydrogen phosphate and phosphoric acid one or more of .

[0050] In the preparation method of the above-mentioned mesoporous active material, the compound of the metal M in step (4) may be any water-soluble compound.

[0051] ...

Embodiment approach

[0096] According to the preparation method of the above-mentioned catalytic composition provided by the present invention, after mixing the active mesoporous material, gasification active component, clay, and heat-resistant inorganic oxide matrix, perform beating, spray drying and roasting according to conventional methods in the art That's it. In a preferred embodiment of the present invention, the preparation method of the above-mentioned catalytic composition comprises the following steps:

[0097] (1) Neutralize the aluminum source and alkali solution at room temperature to 85°C to form a gel, and control the pH value of the gel to be 7-11 to obtain a gelled slurry; according to SiO 2 :Al 2 o 3 =1: (1.0-7.5) weight ratio, adding a silicon source to the gelling slurry, aging at room temperature to 90° C. for 1-5 hours, to obtain the first solid precipitate; the first solid precipitate Contact treatment with ammonium salt or acid solution, filter to obtain a second solid ...

Embodiment 1

[0126] (1) With a concentration of 90gAl 2 o 3 / L Al 2 (SO 4 ) 3 solution and concentration of 102gAl 2 o 3 / L, NaAlO with a caustic ratio of 2.5 2 The solution is the raw material for the reaction. It adopts the method of co-flow gelation, and mixes it under vigorous stirring to form a gel. The temperature of the system is controlled at 50°C, the pH value of the system is 9.0, and it is collected and measured to form a gelatinous liquid;

[0127] (2) According to SiO under stirring 2 :Al 2 o 3 = 1: 1.94 weight ratio, add SiO with a concentration of 60g to the gelling slurry 2 / L of water glass, warming up to 60 ℃ for aging for 3 hours, to obtain the first solid precipitate; (3) the first solid precipitate according to its precipitate dry basis: ammonium salt: H 2 Add NH at a weight ratio of O=1:0.5:12 4 Cl and deionized water, carry out ion exchange to remove sodium ion to precipitate at 60 ℃, exchange repeats once, each 0.5 hour, to sodium oxide content is lower t...

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Abstract

The invention discloses a cracking gasification catalytic composition, a preparation method thereof and a petroleum hydrocarbon cracking gasification method. In weight percentage, the catalytic composition comprises: 1% to 50% of mesoporous active materials, wherein, The anhydrous chemical expression of the active mesoporous material in terms of oxide weight is (0-0.2) Na 2 O·(40-85)Al 2 o 3 ·(10-55)SiO2 2 ·(0.5-10)P 2 o 5 ·(0.5-10)M x o y , wherein the metal M is selected from Mg, one or more of the periodic table IIB, IIIB, IVB, VIIB group elements, and lanthanide rare earth elements, y is the highest valence state when the metal M forms an oxide, and x and The value of y is such that the valences of M and O are balanced. It has better cracking activity and gasification conversion performance when applied in heavy oil catalytic cracking-gasification combined process, and can obtain higher yield of liquefied gas.

Description

technical field [0001] The invention relates to a cracking gasification catalytic composition and a preparation method thereof, and a petroleum hydrocarbon cracking gasification method using the cracking gasification catalytic composition. Background technique [0002] At present, when catalytic cracking processes heavy and low-quality feedstock oil, it poses challenges to the catalytic cracking process itself and the catalyst. Non-catalytic processing of low-quality heavy oil, including delayed coking, fluidized coking, and flexible coking, has attracted increasing attention. However, the coking process has the problems of high coke yield and low-quality coke that is difficult to utilize. The delayed coking process will produce a large amount of low-value-added petroleum coke, so petroleum resources have not been efficiently utilized. [0003] Part of the coke produced by the fluidized coking and flexible coking processes developed by Exxon in the United States is burned to...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80C10G11/05
Inventor 杨昕杨雪刘倩倩朱玉霞任飞郑金玉罗一斌张书红
Owner CHINA PETROLEUM & CHEM CORP
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