Fluidized bed reactor for preparing vinyl chloride by hydrogen chloride and acetylene reaction and method
A fluidized-bed reactor and fluidized-bed technology are applied in hydrogen halide addition preparation, chemical instruments and methods, chemical/physical processes, etc., which can solve problems such as poor temperature control and low production intensity, and achieve gas-solid contact. The effect is enhanced, the contact effect is good, and the wear rate is small.
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Embodiment 1
[0045] Fix the component (6) on the heat exchange tube (5), connect the gas inlet (2), gas distributor (3), catalyst outlet (4), heat exchange tube (5), catalyst inlet (7), cyclone The separator (8) and the gas outlet (9) are sequentially connected with the cylinder wall of the fluidized bed (1) to form a complete fluidized bed (1). Among them, a tubular gas distributor with a pressure drop of 20% of the pressure drop of the catalyst bed is used; a heat exchange tube with a height of 200% of the catalyst dense phase height and a cross-sectional area of 5% of the bed cross-sectional area is used; a void ratio of 90% is used The cross angle between the two layers is 90°, the height is 20% of the diameter of the fluidized bed; the distance between the same layers is 10% of the diameter of the fluidized bed. The particle size is 0.1mm and the specific surface area is 600m 2 / g, the bulk density is 1000kg / m 3 The catalyzer containing mercuric chloride and tin chloride, catalyze...
Embodiment 2
[0048] Fix the component (6) on the heat exchange tube (5), connect the gas inlet (2), gas distributor (3), catalyst outlet (4), heat exchange tube (5), catalyst inlet (7), cyclone The separator (8) and the gas outlet (9) are sequentially connected with the cylinder wall of the fluidized bed (1) to form a complete fluidized bed (1). Among them, a plate gas distributor whose pressure drop accounts for 35% of the pressure drop of the catalyst bed is used; a heat exchange tube whose height is 100% of the catalyst dense phase height and whose cross-sectional area is 30% of the bed cross-sectional area; Components, the intersection angle between two layers of components is 45°, the height is 20% of the diameter of the fluidized bed; the distance between components of the same layer is 1% of the diameter of the fluidized bed. The particle size is 0.05mm and the specific surface area is 1000m 2 / g, the bulk density is 300kg / m 3 catalysts containing mercuric chloride and zinc chlori...
Embodiment 3
[0051] Fix the component (6) on the heat exchange tube (5), connect the gas inlet (2), gas distributor (3), catalyst outlet (4), heat exchange tube (5), catalyst inlet (7), cyclone The separator (8) and the gas outlet (9) are sequentially connected with the cylinder wall of the fluidized bed (1) to form a complete fluidized bed (1). Among them, a float valve gas distributor with a pressure drop of 30% of the catalyst bed pressure drop is used; a heat exchange tube with a height of 150% of the catalyst dense phase height and a cross-sectional area of 15% of the bed cross-sectional area is used; a void ratio of 70% is used. % of components, the intersection angle between two layers is 90°, the height is 80% of the diameter of the fluidized bed; the distance between the same layers is 10% of the diameter of the fluidized bed. The particle size is 0.3mm and the specific surface area is 1200m 2 / g, the bulk density is 600kg / m 3 Catalysts containing mercuric chloride and mangane...
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