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HDD Regenerator 2011 V.15.0.0.573 Crack !!!!

catalytic cracking units can be operated in a variety of modes. the most common mode is called delayed coking. in delayed coking, a temperature of 450 to 550 degrees fahrenheit is maintained in the riser. a vacuum is applied to the riser to keep the pressure below one atmosphere. hydrogen is injected into the riser to keep the pressure below one atmosphere, while oxygen is fed into the riser to keep the pressure under one atmosphere. the heated riser and catalyst circulate in a closed loop that permits the cracked products to flow directly to the fractionator. with delayed coking, two-thirds of the gasoline boiling range is produced as distillate and one-third is produced as light cycle oil.

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the catalyst flow then enters the catalyst standpipe which is typically located in a shallow well near the bottom of the reactor. the catalyst flow is drawn into the regenerator standpipe by a blower. the regenerated catalyst flows from the regenerator standpipe into the top of the reactor. the flow of catalyst then follows the same route as the flow of hydrocarbon feed in the u-pipe back to the regenerator standpipe. the catalyst flow in the standpipe is drawn by a blower into the regenerator. the regenerator is a vessel having a small diameter. the diameter of the regenerator is small because most of the air needed for the combustion process is introduced into the regenerator through one or more nozzles in the upper portion of the regenerator. the air/catalyst flow is usually delivered through the nozzle(s) by a blower. as the catalyst flows through the regenerator, it is heated to a temperature in the order of 2000-2500&deg f. the combustion process converts the carbonaceous material in the catalyst to carbon dioxide, carbon monoxide, water and heat. the heat is removed from the catalyst in the regenerator by a circulating fluid, typically steam.
the combustion process is supported by the pressurized steam supplied by the boiler. the steam heat is used to drive the combustion of the carbonaceous material. in the high-temperature regenerator, the heat of combustion is transferred to the catalyst. the hot catalyst is continuously circulated by a blower from the regenerator back to the reactor and then to the regenerator. the carbonaceous material is removed from the catalyst by a circulating fluid, typically steam. this is a highly efficient process as the circulating steam is also used to drive the blower and the combustion process.
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