Method and equipment for cooling catalyst for gas-solid reaction
A catalyst, gas-solid phase technology, applied in the field of catalyst cooling for gas-solid phase reaction, to achieve the effects of reducing the use cost, low cost input, easy maintenance and replacement
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Embodiment 1
[0044] Embodiment 1, a certain annual output of 100 × 10 4 t / a catalytic device, reaction materials: heavy oil at atmospheric pressure, preheated at 220°C; conventional catalytic cracking catalyst is used; the reactor is in the form of a riser, the outlet temperature of the riser is 500°C, and the reaction time is 2.5s; the regeneration temperature is 685°C . The regeneration inclined pipe between the reaction-regeneration device is set as figure 2 In the desuperheater with the structure shown, the cooling baffle and catalyst flow control baffle are barrel-type, the heat exchange tube is in the form of a sleeve, and low-temperature water is used as the heat exchange medium; 60Kg / h of catalyst at 685°C enters the desuperheater, and there are 40 % of the catalyst passed through the delivery zone with a fluidizing air flow rate of 60 liters per kilogram of catalyst per hour. After heat exchange, the catalyst with a temperature of 640°C enters the reactor through the regenerati...
Embodiment 2
[0045] Embodiment 2, cooling device structure such as Figure 4 , the cooling partition and the catalyst flow control partition are divided baffles, the heat exchange tube is in the form of a sleeve, and low-temperature water is used as the heat exchange medium; 60Kg / h of catalyst at 685°C enters the cooler, and 60% of the catalyst passes through In the transfer area, the flow rate of fluidizing air in the transfer area is 70 liters per kilogram of catalyst per hour. After heat exchange, the catalyst with a temperature of 655°C enters the reactor through the regeneration slide valve. All the other parts are the same as in Example 1.
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