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High Regenerator Temperature

The modern reforming process operates with continuous regeneration of the catalyst, at low pressure (2 to 5 bar) and high temperature (510-530°C). [Pg.371]

The catalytic cracking processes, as well as most other refinery catalytic processes, produce coke which collects on the catalyst surface and diminishes its catalytic properties. The catalyst, therefore, needs to be regenerated continuously or periodically essentially by burning the coke off the catalyst at high temperatures. [Pg.88]

A good catalyst is also stable. It must not deactivate at the high temperature levels (1300 to 1400°F) experienced in regenerators. It must also be resistant to contamination. While all catalysts are subject to contamination by certain metals, such as nickel, vanadium, and iron in extremely minute amounts, some are affected much more than others. While metal contaminants deactivate the catalyst slightly, this is not serious. The really important effect of the metals is that they destroy a catalyst s selectivity. The hydrogen and coke yields go up very rapidly, and the gasoline yield goes down. While Zeolite catalysts are not as sensitive to metals as 3A catalysts, they are more sensitive to the carbon level on the catalyst than 3A. Since all commercial catalysts are contaminated to some extent, it has been necessary to set up a measure that will reflect just how badly they are contaminated. [Pg.16]

Technology exists to recover heat from processes operating at all temperatures, from regenerators on high-temperature plant to heat pumps using low-temperature effluent as a heat source. The problem in many cases is to find a use for the heat recovered. The best solution is to recycle the heat within the same plant, as the supply will always be matched to the demand. An alternative is to use the heat recovered in associated plant (for example, the heat recovered from a melting furnace can be used to dry feedstock for the furnace). [Pg.265]

Recuperators are limited in their performance, partly by problems with materials operating for long periods at elevated temperatures and by the efficiency of simple gas-to-gas heat exchangers. For high-temperature applications, a regenerator has advantages. [Pg.266]

FCC regeneration can be further subdivided into low, intermediate, and high temperature regeneration. In low temperature regeneration (about I,190°F or 640°C), complete combustion is impossible. One of the characteristics of low temperature regeneration is that at 1,190°F, all three components (Oj, CO, and COj) are present in the flue gas at... [Pg.18]

Vanadium and sodium neutralize catalyst acid sites and can cause collapse of the zeolite structure. Figure 10-5 shows the deactivation of the catalyst activity as a function of vanadium concentration. Destruction of the zeolite by vanadium takes place in the regenerator where the combination of oxygen, steam, and high temperature forms vanadic acid according to the following equations ... [Pg.325]


See other pages where High Regenerator Temperature is mentioned: [Pg.312]    [Pg.392]    [Pg.324]    [Pg.312]    [Pg.392]    [Pg.324]    [Pg.2702]    [Pg.254]    [Pg.475]    [Pg.424]    [Pg.427]    [Pg.449]    [Pg.206]    [Pg.49]    [Pg.215]    [Pg.408]    [Pg.532]    [Pg.179]    [Pg.223]    [Pg.226]    [Pg.371]    [Pg.286]    [Pg.415]    [Pg.2102]    [Pg.2403]    [Pg.174]    [Pg.154]    [Pg.72]    [Pg.253]    [Pg.205]    [Pg.219]    [Pg.315]    [Pg.26]    [Pg.105]    [Pg.323]    [Pg.2]    [Pg.231]    [Pg.232]    [Pg.39]    [Pg.466]    [Pg.266]    [Pg.4]    [Pg.20]    [Pg.90]    [Pg.229]   
See also in sourсe #XX -- [ Pg.20 , Pg.256 ]




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