Industrial fluidized bed reactor

Abstract

The invention discloses an industrial fluidized bed reactor which comprises a reactor shell, a plurality of guide cylinders and a plurality of gas distributors arranged at the bottoms of the guide cylinders, the axes of the guide cylinders are parallel, and the guide cylinders are arranged in the reactor shell at intervals. And the guide cylinders as well as the guide cylinders and the reactor shell are connected by adopting support plates through welding or bolts. By reasonably designing the arrangement mode of the guide cylinders, the oxygen utilization rate is improved, the fluidization state in the reactor is improved under the condition that the overall height of the reactor is not changed, the optimal matching of oxygen and air inflow required by aerobic biochemistry of microorganisms is met, the air consumption is reduced, and the mass transfer efficiency of the reactor is improved.

Description

technical field [0001] The invention belongs to the field of biological fluidized bed design for waste water and sewage treatment, and specifically relates to an industrial fluidized bed reactor. Background technique [0002] The aerobic biological fluidized bed reactor is widely used in the field of wastewater treatment. The reactor has the advantages of simple structure, low energy consumption, small shear stress, and good mixing. It is currently the most widely used biological reaction equipment. In terms of engineering design, how to further optimize the design of the internal components of the aerobic biological fluidized bed, strengthen the mixing and mass transfer of the reactor, and make the COD removal faster, more efficient, and lower consumption is the current research on the sewage biological treatment technology of the aerobic biological fluidized bed the key of. In the design of aerobic biological fluidized bed reactor, the circulating liquid velocity and gas ...

AI Technical Summary

Problems solved by technology

At present, most of the domestic biological fluidized bed reactors are in the form of central airlift, and there is a large dead angle at the connection between the guide tube and the guide partition, the fluidization effect is not ideal, and with the increase of the processing capacity, The volume of the reactor is also getting larger and larger, and it is difficult to ensure the normal fluidization inside the reactor with this form of internal component arrangement, the fluidization effect is not ideal, and the gas-liquid mass transfer efficiency is reduced

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