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Stirring device of hydrocarbon derivatives hydrogenation reaction reactor

A technology of hydrogenation reaction and stirring device, which is applied in mixers with rotary stirring devices, chemical/physical/physical-chemical stationary reactors, chemical instruments and methods, etc., can solve problems such as affecting the stability of the device

Active Publication Date: 2015-10-07
JIANGSU LIANHE CHEM TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But its disadvantages are: since the self-priming agitator has high requirements on the speed, it needs to run at a high speed, generally above 400 rpm, which affects the stability of the device

Method used

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  • Stirring device of hydrocarbon derivatives hydrogenation reaction reactor
  • Stirring device of hydrocarbon derivatives hydrogenation reaction reactor
  • Stirring device of hydrocarbon derivatives hydrogenation reaction reactor

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Embodiment Construction

[0010] The invention relates to a stirring device for a hydrogenation reactor of hydrocarbon derivatives, such as figure 1 — image 3 As shown, it includes a reaction kettle body 1, a jacket 2 is arranged outside the kettle body, a reducer 3 is arranged on the kettle body, a motor 4 is arranged on the reducer, a stirring shaft 5 is arranged in the kettle body, and the stirring shaft is connected with the output shaft of the reducer. It is characterized in that: the upper, middle and lower layers of stirring paddles 6 are arranged on the stirring shaft 5, wherein the horizontal angles of the upper and lower layers of stirring paddles and the middle layer of the stirring paddles are staggered by 90°, and the stirring paddles 6 Including the connection sleeve 7, the two sides of the connection sleeve are formed with sheet-like oblique blades 8, and the end of the oblique blades is formed with multi-layer connection blades. Blade 10 and following blade 11, upper blade is shaped o...

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Abstract

A stirring device of a hydrocarbon derivatives hydrogenation reaction reactor comprises a reactor body, wherein a jacket is arranged outside the reactor body, a speed reducer is arranged on the reactor body, a motor is arranged on the speed reducer, a stirring shaft is arranged in the reactor body, and the stirring shaft is connected with an output shaft of the speed reducer. The stirring device is characterized in that an upper-layer stirring paddle, a middle-layer stirring paddle and a lower-layer stirring paddle are arranged on the stirring shaft, wherein the angle, in the horizontal direction, of each of the upper-layer stirring paddle and the lower-layer stirring paddle is staggered with and forms an included angle being 90 degrees with the angle, in the horizontal direction, of the middle-layer stirring paddle, and each of the stirring paddles comprises a connecting sleeve, the two sides of each connecting sleeve are provided with sheet oblique oar blades, the end part of each oblique oar blade is provided with multi-layer of connecting oar blades, each layer of connecting oar blades comprises a bottom plate, an upper oar blade and a lower oar blade are arranged on each bottom plate, an upper left blade and an upper right blade are arranged on each upper oar blade, and a lower left blade and a lower right blade are arranged on each lower oar blade.

Description

technical field [0001] The invention relates to a stirring device for a reaction kettle, in particular to a stirring device for a hydrogenation reaction reaction kettle of hydrocarbon derivatives. Background technique [0002] Hydrogenation reaction is a common chemical unit operation, widely used in pesticides, medicines, dyes and petrochemicals, such as benzene ring hydrogenation, olefin hydrogenation, etc. For the combined agitator used in the reactor in the previous hydrogenation reaction, the lower layer is axial flow agitation, and the upper layer is radial flow agitation. The combined paddle is easily affected by the ventilation position and ventilation volume, and the large ventilation volume may deteriorate the performance of the catalyst. Suspension effect, resulting in uneven distribution of catalyst; moreover, due to the incompatibility of gas and liquid, and the density difference is very large, hydrogen only gets dispersed and reacted by the combined paddle dur...

Claims

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Application Information

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IPC IPC(8): B01J19/18B01J8/10B01F7/18
Inventor 王荣杰蔡新宇王朝斐李鹏鹏张毅陈磊彭寅生
Owner JIANGSU LIANHE CHEM TECH