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Fluidized bed alcohol dehydration reaction device

2026-11-14 16:09
2026-11-14 20:06

A fluid bed reactor used for preparing ethene from dehydrated alcohol is in the shape of a barrel with an upper cover, and is divided into an upper part and a lower part by a horizontal partition plate at the middle and lower part of the barrel. The upper part was covered with a multi-layer vertical separation sleeve, which was divided into a cylindrical reaction chamber, a ring-shaped heating chamber, and a ring-shaped heat-resistant greenhouse in turn. The cylindrical reaction chamber is a separated hollow cylinder that can be lifted up. The rock wool layer in the cylinder divided the cylinder into a catalyze dehydration layer and a glass bead zeolite layer. The cylinder is equipped with a movable upper cover and a lower bottom directly connected to the cylinder. A small hole is arranged at the center of the upper cover to extend a heating couple into the catalyst, and another small hole is installed with an air outlet pipe. The ring-shaped heating chamber is composed of an electric heating wire and an electric heating wire fixing sleeve, the sleeve is made of a fire-resistant insulation material, the inner diameter of the sleeve is greater than the outer diameter of a hollow cylinder which can be separated from the reaction chamber, and the outer wall of the electric heating wire fixing sleeve is provided with a spiral groove for fixing the electric heating wire; the ring-shaped heat-insulation chamber is composed of a sleeve made of an asbestom and a fire-resistant insulation material, the ring-shaped sleeve is positioned between the outer wall of the reactor and the ring-shaped heating chamber, and the space between the outer wall of the reactor and the ring-shaped sleeve is filled with the asbestom. The lower part is an alcohol vaporizing chamber, which is provided with an electric heating plate, an electric heating plate fixing frame and an alcohol conveying pipe. The generated ethene enters the collector through the air outlet pipe. During the preparation, the temperature of the ring-shaped heating chamber was controlled at 220 ° C, and the temperature of the vaporizing chamber was controlled at 80 - 95 ° C. The alcohol was pumped by a constant flow pump at a flow rate of 1500 - 2000ml/min·m2. The conversion rate of alcohol in the reactor reached more than 96%, and the ethene was more than 95.0%. Read more exciting novels for free

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