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BULK SOLID TEMPERATURE OR REGULATING PROCESS BY MEANS OF A FLUIDIZED OR MOBILE BED MULTICOMPARTMENTED HEAT EXCHANGER
BULK SOLID TEMPERATURE OR REGULATING PROCESS BY MEANS OF A FLUIDIZED OR MOBILE BED MULTICOMPARTMENTED HEAT EXCHANGER
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机译:通过流化床或移动床多室换热器的整体温度或调节过程
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摘要
A method and a device for thermal regulation of fluidized or moving catalyst beds are described, the device comprising a heat exchanger with a fluidized or moving bed. According to the invention, a pulverulent solid is circulated essentially at the base of an enclosure in a heat exchanger comprising an internal partition separating which defines two elongated and adjacent compartments communicating by their lower part. In the compartment where the pulverulent solid flows down, the fluidization speed is between 0.1 cm / s and 2 m / s while in the compartment where the pulverulent solid rises in the heat exchanger. heat, the fluidization speed is between 0.1 and 6 m / s. Application in particular to refining reactions (catalytic reforming for example) or to the regeneration of a catalytic cracking catalyst in a fluidized bed of an petroleum charge, or to the combustion of coal.
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机译:描述了一种用于热调节流化床或移动床的方法和设备,该设备包括具有流化床或移动床的热交换器。根据本发明,粉状固体基本上在热交换器的外壳的底部循环,该热交换器包括内部分隔件,该分隔件限定了两个细长且相邻的隔间,这些隔间通过其下部连通。在粉状固体向下流动的舱室中,流化速度在0.1 cm / s和2 m / s之间,而在粉状固体在热交换器中上升的舱室中。加热时,流化速度在0.1至6 m / s之间。特别地应用于精炼反应(例如催化重整)或在石油装料的流化床中催化裂化催化剂的再生或煤的燃烧中。
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