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Catalytic cracking method

A catalytic cracking and nano-catalyst technology, applied in the field of catalytic cracking, can solve the problems of low utilization rate, frequent regeneration, and containment, and achieve the effects of improving utilization rate, simple method and reducing cost.

Active Publication Date: 2006-07-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The following problems generally exist in the use of heterogeneous catalysts: 1. The amount of catalyst is large, the utilization rate is low, and the service life is short; 2. It is easy to form carbon and requires frequent regeneration; 3. There are still many active components in the deactivated catalyst that do not play a role Wait
[0007] Since the fixed-bed reaction process uses a heterogeneous catalyst, the main disadvantage is that the catalyst is easy to coke, the service life is short, and frequent regeneration is required; the main disadvantage of the fluidized-bed reaction process is that not only the investment is large, but also the product contains nitrogen and oxygen, resulting in a reaction with hydrogen. , methane, ethylene and other light components are difficult to separate

Method used

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  • Catalytic cracking method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Taking Yanhua naphtha as raw material, its composition is as follows (w%):

[0042] C4-1.85, C5 6.96, C6 21.29, C7 19.29, C8 23.66, C9 16.04, C10 7.40, C11 2.61, C12 0.64. Among them, 26.18 normal alkanes, 33.66 isoparaffins, 27.35 naphthenes, 0.20 olefins, 12.35 aromatics, and 0.26 unknowns.

[0043] Naphtha with a water-to-oil ratio of 1 enters the preheater 2 at a flow rate of 0.3g / min, and the water liquid containing 700ppm nano-sized alumina is fed into the preheater through the peristaltic pump 4 at a flow rate of 0.3g / min under stirring 2 and the pipeline between reactor 6. The catalytic cracking reaction was carried out at 785°C, and gas samples were taken every 0.5hr to analyze its composition. After about 1 hour of reaction, the cumulative amounts of gaseous and liquid phase products were metered. The reaction results and yields of main products in the gas phase are shown in Table 1.

Embodiment 2

[0048] Except that the catalytic cracking reaction was carried out at 790° C., other reaction conditions were the same as in Example 1. Table 2 shows the reaction results and yields of main products in the gas phase.

Embodiment 3

[0053] Taking Yanhua naphtha as raw material, its composition is as follows (% by weight):

[0054] C4-1.85, C5 6.96, C6 21.29, C7 19.29, C8 23.66, C9 16.04, C10 7.40, C11 2.61, C12 0.64. Among them, 26.18 normal alkanes, 33.66 isoparaffins, 27.35 naphthenes, 0.20 olefins, 12.35 aromatics, and 0.26 unknowns.

[0055] Naphtha with a water-to-oil ratio of 1 enters the preheater 2 at a flow rate of 0.3 g / min, and the aqueous solution containing 700 ppm alkaline earth metal-modified ZSM-5 molecular sieve (particle size <160 mesh) is stirred at a rate of 0.- The flow rate of 1g / min is added into the pipeline between the preheater 2 and the reactor 6 through the peristaltic pump 4 . Catalytic cracking reactions were carried out at 750°C, and gas samples were taken every 0.5hr to analyze its composition. After about 1 hour of reaction, the cumulative amounts of gaseous and liquid phase products were metered. The reaction results and yields of main products in the gas phase are sho...

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Abstract

This invention describes a process for catalytic pyrolysis, comprising the steps of: (1) introducing the reactants into a pre-heater, wherein the reactants are vaporized into gases; (2) introducing the mixed solutions containing ultrafine or nanoscale catalyst into the pipeline between the pre-heater and the reactor, or directly into the reactor, wherein the said ultrafine or nanoscale catalyst is uniformly mixed with the process (1) wherein said gaseous reactants; (3) pyrolysis of the said uniform mixture in the reactor. The average diameter of the said ultrafine or nanoscale catalyst is in the range of 1nm-100ª–m. This invention resolves such problems existing in the present fixed-bed reaction process as easy carbonization of the catalyst, a short service periodic and frequent need for recovery. The process of this invention is easy to operate, and suitable for a wide variety of catalytic pyrolysis reactions. Compared with the present pyrolytic process, the process of this invention can increase the weight yield rate of ethylene+propylene+butadiene by at least 5%, while the equipment remains the same with only a feeding pipeline added.

Description

technical field [0001] The present invention relates to a method for catalytic cracking, more specifically, relates to a method for preparing low carbon number olefins by catalytic cracking of petroleum hydrocarbons. Background technique [0002] There are two main types of catalysts used in petrochemical production: heterogeneous catalysts and homogeneous catalysts. Because homogeneous catalysts are difficult to separate from the product, people have explored the method of loading homogeneous catalysts on the carrier, that is, homogeneous catalytic heterogeneity. After years of research and exploration, industrialization has not been realized so far, mainly because the problem of active component loss is difficult to solve. . It is because of the above-mentioned disadvantages of homogeneous catalysts that most industrial catalysts are heterogeneous catalysts. The following problems generally exist in the use of heterogeneous catalysts: 1. The amount of catalyst is large, ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G11/00
Inventor 吉媛媛杨元一戴伟茅文星陈硕张兆斌张永刚郭敬杭巴海鹏
Owner CHINA PETROLEUM & CHEM CORP
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