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
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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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