Gas-lifting multi-stage loop reactor for strain cultivation

A loop reactor, airlift technology, which is applied in chemical methods, chemical instruments and methods, chemical/physical processes, etc. to make liquids react with gaseous media. The distribution is not ideal and other problems, to achieve the effect of increasing the overall gas holdup, increasing the circulating liquid velocity, and improving the gas-liquid distribution

Inactive Publication Date: 2018-05-11
邵环宇
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, for some gas-liquid mixed systems with high viscosity fluids, the gas-liquid mixing intensity and gas distribution of the multi-stage loop reactor are still not ideal.

Method used

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  • Gas-lifting multi-stage loop reactor for strain cultivation

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Embodiment Construction

[0008] Such as figure 1 As shown, an air-lift multi-stage loop reactor for strain planting includes a guide tube 1 and a guide tube 2, the inside of the guide tube 1 is provided with a guide tube 2, and the upper part of the guide tube 2 is provided with a distribution 3, the lower part is provided with a nozzle 4, the nozzle is connected with the gas-liquid mixing tank 5, and the gas-liquid mixing tank 5 is provided with three branches, the second one is connected with the metering pump 6, the third one is connected with the air compressor 7, and the air compression The machine 7 is also connected with the sprayer 8, the sprayer 8 is placed at the bottom of the guide tube 1, the upper part of one side of the guide tube 1 is provided with a drain port 10, and the middle part is provided with an optical fiber probe 9.

[0009] The diameter of the guide tube 1 is 213mm.

[0010] The principle is as follows:

[0011] The guide tube 1 is divided into three sections, and the heig...

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Abstract

The invention discloses a gas-lifting multi-stage loop reactor for strain cultivation. The loop reactor comprises a flow guide tube and a flow guide pipe; the flow guide pipe is arranged in the flow guide tube; a distributor is arranged at the upper part of the flow guide pipe; nozzles are arranged at the lower part of the flow guide pipe; the nozzles are connected with a gas-liquid mixing tank; the gas-liquid mixing tank is provided with three branches; the second branch is connected with a metering pump; the third branch is connected with an air compressor; the air compressor is also connected with a sprayer; the sprayer is positioned at the bottom of the flow guide tube; a water outlet is arranged at the upper part of one side of the flow guide tube; and the middle part of the flow guide tube is provided with optical fiber probes. The loop reactor provided by the invention has the advantages that the structure is simple, the chord length of rising air bubbles can be reduced by jet flows, the overall gas content rate is increased, the distribution of the gas liquid in a descent section is improved, the liquid circulation velocity is increased, and finally, the gas-liquid volume mass transfer coefficient is obviously improved.

Description

technical field [0001] The invention relates to the technical field of mechanical equipment, in particular to an airlift multi-stage loop reactor for strain cultivation. Background technique [0002] Airlift loop reactors are widely used in gas-liquid, gas-liquid-solid reaction or separation processes in biochemical, petrochemical, sewage treatment and other fields. In the traditional air-lift loop reactor, the bubbles continue to coalesce and become larger during the rising process, which brings two adverse effects: 1. The buoyancy force of the large bubbles is large and the drag force is small, so they cannot be brought to the descending section by the circulation, making the descending section, Especially the gas holdup at the bottom is very small; 2. The gas-liquid interface area is reduced, which is not good for mass transfer. In order to solve this problem, a multi-stage loop reactor was developed. By dividing the guide tube into multiple sections to form a circulatio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J10/00
CPCB01J10/00
Inventor 邵环宇
Owner 邵环宇
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