A catalytic cracking method for producing light olefins and light aromatics

A technology of catalytic cracking and low-carbon olefins, applied in chemical instruments and methods, only multi-stage series refining and cracking process treatment, hydrocarbon cracking and hydrocarbon production, etc., can solve problems such as limited and increased yield of light aromatics, and achieve rich Mesoporous structure, high conversion rate, high yield effect

Active Publication Date: 2020-09-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] In summary, the existing technologies all take low-carbon olefins as the main target yield and co-produce light aromatics, so the increase in the yield of light aromatics is limited. It is necessary to develop a catalytic cracking method with higher yields of low-carbon olefins and light aromatics on the basis of current technology and catalytic materials

Method used

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  • A catalytic cracking method for producing light olefins and light aromatics

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Effect test

preparation example Construction

[0063] The preparation method of the catalytic cracking catalyst of the present invention comprises preparing the microsphere composition that comprises Y-type molecular sieve, BEA structure molecular sieve, natural mineral matter, oxide binding agent, and the present invention is called the first composition microsphere, described the first A composition microsphere modification treatment; the first composition microsphere modification treatment comprises the following steps:

[0064] a. Put the microspheres of the first composition into an alkaline solution for treatment, filter and wash to obtain the microspheres of the first composition of alkali treatment;

[0065] b. Treat the alkali-treated first composition microspheres obtained in step a in a compound acid solution composed of fluosilicic acid, organic acid and inorganic acid, filter and wash, optionally exchange ammonium for sodium treatment, and optionally filter and optionally washed, optionally dried, to obtain me...

Embodiment approach

[0086] According to one embodiment of the present invention, when the method of the present invention is carried out in riser reactor, generally carry out as follows:

[0087] The regenerated catalyst (catalyst for catalytic cracking) enters the pre-lift section of the riser reactor and flows upward under the action of the pre-lift medium. The preheated raw oil and atomized steam are injected into the lower part of the riser reactor to contact the regenerated catalyst. The catalytic cracking reaction flows upward at the same time; the reacted oil and gas and the catalyst to be produced enter the fluidized bed reactor through the outlet of the riser reactor, and the reacted oil and gas react again, and the reacted stream enters the cyclone separator through the outlet of the riser reactor, and the separated reaction The oil and gas extraction device is further separated to obtain fractions such as methane, ethylene, propylene, C4 hydrocarbons, and pyrolysis gasoline rich in ligh...

Embodiment 1

[0107] according to figure 1 The flow process of the test is carried out, the raw oil is a vacuum distillate, and the catalyst A of the present invention is used to test on a medium-sized device, operated at normal pressure, and the preheated raw oil enters the bottom of the riser, at a reaction temperature of 545 ° C and a reaction time of 2.0 seconds , the weight ratio of catalytic cracking catalyst and raw oil is 10, and the cracking reaction is carried out under the condition that the weight ratio of water vapor and raw oil is 0.25, and the reaction oil gas and steam and the catalyst to be born enter the fluidized bed reactor from the reactor outlet, and Reaction temperature 530°C, weight hourly space velocity 3.4h -1 The reaction continues under the condition of seconds, and the post-reaction stream enters the closed cyclone, and the reaction oil gas and the unborn catalyst are quickly separated, and the reaction oil gas is cut according to the distillation range in the s...

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Abstract

The invention relates to a catalytic cracking method for producing low-carbon olefins and light aromatic hydrocarbons. According to the catalytic cracking method, pre-heated heavy hydrocarbon oil enters a reactor, and reacts with a catalytic cracking catalyst; the reaction oil-gas and the spent catalysts enter a cyclone separator, and are subjected to gas-solid separation; the reaction oil-gas isfurther separated to obtain a product containing light-carbon olefins and light aromatic hydrocarbons; and the spent catalysts are subjected to steam stripping, the steam stripped catalysts enter a catalyst regenerator, charring regeneration is performed, and the regenerated catalyst returns to the reactor so as to be recycled, wherein the catalytic cracking catalyst comprises, by weight, 5-65% ofnatural minerals, 10-60% of an oxide, 24-75% of a Y-type molecular sieve and a BEA structure molecular sieve, 0.1-15% of a phosphorus additive and 0.1-10% of a metal additive. With the method of thepresent invention, the yield of low-carbon olefins is high, and the yield of light aromatic hydrocarbons is high.

Description

technical field [0001] The present invention relates to a method for catalytic conversion of hydrocarbon oil in the absence of hydrogen, and more particularly to a catalytic cracking method for producing light olefins and light aromatics. Background technique [0002] Low-carbon olefins represented by ethylene and propylene are the most basic raw materials in the chemical industry. Natural gas or light petroleum fractions are mostly used as raw materials at home and abroad, and low-carbon olefins are produced by steam cracking technology in ethylene complexes. In addition to the production of ethylene, about 70% of propylene, 90% of butadiene, and 30% of aromatics come from steam cracking by-products. Although the steam cracking technology has been developed for decades and the technology has been continuously improved, it still has high energy consumption, high production cost, and CO 2 Due to technical limitations such as large emissions and difficult adjustment of produc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G55/06C10G3/00C07C4/06C07C4/18C07C11/04C07C11/06C07C15/02B01J29/80
CPCB01J29/106B01J29/7215B01J29/80C07C4/06C07C4/18C10G3/49C10G55/06C10G2300/70C10G2400/02C10G2400/04C10G2400/30C07C11/04C07C11/06C07C15/02Y02P20/52Y02P20/584
Inventor 魏晓丽谢朝钢张久顺张执刚罗一斌田辉平陈学峰刘银亮李福超
Owner CHINA PETROLEUM & CHEM CORP
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