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Method for recovering reforming catalyst, catalyst and adsorbent

a technology of reforming catalyst and catalyst, applied in the field of recovering reforming catalyst, can solve the problems of reducing the operational life of the catalyst, reducing the total surface area of the used catalyst, and reducing the phase form of aluminum oxide, so as to achieve the effect of easy recovery and reus

Inactive Publication Date: 2010-07-29
CPC CORPORATION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The present invention provides a method for easily classifying used catalysts based on their degree of aging. This allows for the collection and reuse of less aged catalysts, saving costs. The method involves immersing the catalysts in a light solution to lower their pseudo-skeletal density, and then immersing them in a heavy solution to increase their pseudo-skeletal density. The settled catalysts are then layered due to different settling velocities. Overall, this method allows for easy classification and recovery of used catalysts."

Problems solved by technology

However, total surface area of the used catalysts will be gradually decreased as the catalysts are used multiple times, so an operational life of the catalysts will be reduced.
Furthermore, phase form of aluminum oxide (Al2O3) support also affects the total surface area.
However, when a total output value of catalytic reformers decreases because properties of the catalysts are less preferential, a lost output value is more expensive than cost of the fresh catalysts.
But units have troubles sometimes, some catalysts may be more severely aging due to unusual operation conditions such as hot spot in certain area of catalyst cycle system.
Economic benefits of the catalytic reformers will be affected if the catalysts are not substituted correctly.
However, the particle sizes or the densities between reforming catalysts with different degrees aged do not present significant differences, so the reforming catalysts cannot be easily and effectively classified.
However, because reforming catalyst has large pores and most liquid solution is easily filled in the pores of the reforming catalyst and a solution with a density greater than the density of γ-form Al2O3 (3.97 g / cm3) is not easy obtained, especially without negative effect after separation.
Therefore, this method cannot be used for separating reforming catalysts.

Method used

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  • Method for recovering reforming catalyst, catalyst and adsorbent
  • Method for recovering reforming catalyst, catalyst and adsorbent
  • Method for recovering reforming catalyst, catalyst and adsorbent

Examples

Experimental program
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example 1

[0042]12 g of reforming catalysts from F catalytic reformer, which had been burned to remove coke deposits and were charged in a container to obtain immersed catalysts. The reforming catalysts were immersed in 9 g of n-hexadecane. A mixture of tetrachloroethane and tetrabromoethane (2.56 g / cm3) were filled in a funnel-shaped container. The immersed catalysts were poured into the funnel-shaped container and immersed in the mixture. Then, most severely aged reforming catalysts firstly settled to the bottom of the funnel-shaped container and other immersed catalysts sequentially settled according to degrees of aging. After all immersed catalysts settled in the funnel-shaped container to obtain settled catalysts, all solution including the heavy solution and the light solution were drained out of the funnel-shaped container. The settled catalysts were washed by n-hexane, classified into six sections and taken out from the funnel-shaped container. The six sections of the settled catalyst...

example 2

[0044]The method of Example 1 was repeated with 12 g of reforming catalysts from F catalytic reformer which had not been burned so comprised coke deposits absorbed on the surface of the reforming catalysts. The six sections of the settled catalyst were calcined and were analyzed as shown in Table 3.

TABLE 3Characteristics of the settled catalysts after calcination in Example 2Characteristics of catalyst1st2nd3rd4th5th6thpercentage of weight (%)7.209.2010.4013.4016.843.10average particle size (mm)1.47911.58801.59421.61251.65861.6983largest particle size (mm)1.681.721.771.781.831.87smallest particle size (mm)1.211.461.411.401.431.51specific surface area (m2 / g)100.2125.0129.5128.8127.5145.3pore volume (m3 / g)0.600.740.750.760.730.80

[0045]There are 43.1 wt % of the settled catalysts in the sixth section and specific surface area of the settled catalysts is 145.3 m2 / g. According to the curve in FIG. 1, the settled catalysts in the sixth section were recovered from about 500 cycle numbers t...

example 3

[0047]The method of Example 1 was further applied to 12 g of reforming catalysts obtained from S catalytic reformer. The six sections of the settled catalyst were calcined and analyzed as shown in Table 4.

TABLE 4Characteristics of the settled catalysts after calcination in Example 3characteristics of catalyst1st2nd3rd4th5th6thpercentage of weight (%)8.4810.5712.569.8514.9143.63average particle size (mm)1.60251.63481.63901.64181.66271.6910largest particle size (mm)1.781.771.771.801.831.93smallest particle size (mm)1.351.451.521.441.491.55specific surface area (m2 / g)132.7132.3135.3133.9134.6139.4pore volume (m3 / g)0.720.750.770.770.770.79

[0048]The specific surface area (139.4 m2 / g) of the settled catalysts in the sixth section (totally about 43.63 wt %) is larger than that (133.7 m2 / g) of the reforming catalysts in S catalytic reformer. Therefore, the settled catalysts in the S catalytic reformer were recovered using the present invention, but recovering efficiency in S catalytic refor...

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Abstract

A method for recovering reforming catalyst comprises obtaining spent reforming catalysts; immersing the spent reforming catalysts with different degrees of aging into a light solution to obtain immersed catalysts and allowing the light solution to enter pores in the spent reforming catalysts to lower a pseudo-skeletal density of each spent reforming catalyst to obtain immersed catalysts; immersing the immersed catalysts into a heavy solution that has a density greater than pseudo-skeletal density of the immersed catalysts and replacing the light solution in the pores in the immersed catalysts by the heavy solution to increase density of the immersed catalysts; and awaiting the immersed catalysts to settle in the heavy solution to obtain settled catalysts, wherein different settling velocities due to aging creates layers of settled catalysts. Therefore, the reforming catalysts with different degrees of aging are easily classified into different layers, which can be reused for cost saving.

Description

BACKGROUND OF THE INVENTION[0001]1. Field of Invention[0002]The present invention relates to a method for recovering reforming catalyst and more particularly to a method for classifying used catalysts with different degrees of aging, so reforming catalysts with a low degree of aging are collected easily to be recovered and reused.[0003]2. Description of the Related Art[0004]Catalytic reforming procedure is a main procedure in secondary processing of feed oil and is used to produce ingredients for gasoline, aromatic hydrocarbons and hydrogen cheaply in petroleum refineries. Catalytic reforming procedure categories include three kinds of reforming processes depending on processes for reforming catalysts, including a semi-regeneration reforming process, a continuous catalytic reforming process and a cyclic catalytic reforming process. In related industry, above processes are used in a proportion of 6:3:1. Now most new units adopt continuous catalytic reforming process.[0005]The continu...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B01J38/56B01J38/48
CPCB01J20/08B01J20/103B01J20/12B01J20/18B01J20/20B01J20/3408B01J20/3475B01J38/12B01J38/54B01J38/56B03D3/00B01J20/3433B01J20/3416
Inventor KANG, WEN-CHENGCHIU, HUNG-TZUWANG, SHU-LISHIH, CHENG-CHIEHHONG, CHENG-TSUNG
Owner CPC CORPORATION