Interface convection inducing bioreactor and applications thereof

A bioreactor and induced interface technology, applied in biological water/sewage treatment, waste fuel, chemical instruments and methods, etc., can solve the problem of high equipment investment and maintenance costs, limited processing capacity, and no real operation of continuous fermentation devices, etc. problems, to achieve the effect of improving the efficiency of sewage treatment and renewable energy, reducing the use and investment and operation costs, and speeding up the start-up and operation speed

Active Publication Date: 2015-05-06
深圳市山水乐环保科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Most of such devices currently in operation need to add a secondary sedimentation tank process downstream, and recover the granular sludge brought out with the liquid through the external circulation reflux method. This method generally has a long process route, complicated operation control, and equipment investment and cost. high maintenance costs
There are also devices that use the so-called internal circulation method. The essence is still to connect the secondary settling tank in series outside the main device, but the split equipment is integrated. The main body of the reactor and the settling tank are still separated by a clear wall, and improper design and handling can easily cause Return mixed flow of water body before and after treatment, reducing treatment efficiency
The processing capacity of the batch fermentation devices currently in operation is limited, and the continuous fermentation devices are either inoperative or unstable, and the conversion of sewage and the output of energy and gas need to be improved

Method used

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  • Interface convection inducing bioreactor and applications thereof
  • Interface convection inducing bioreactor and applications thereof
  • Interface convection inducing bioreactor and applications thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Such as figure 1 As shown, the main body of the reactor is mainly composed of eight parts, which are in order from bottom to top: inlet pipe 1, water distribution device 2, diversion belt 4, pulse tube 5, purified water outlet 6, gas collection bag 7 and gas discharge Pipe 8, the water distribution device 2 is composed of distributors and structured packing, the guide zone 4 and the pulse tube 5 are the main components of the induced fermentation zone 3, the guide zone 4 is a helical coiled metal component, and the pulse The tube 5 is introduced along the tangential direction of the inner wall of the induced fermentation zone, and is distributed in four positions, and the angle between any two pulse tubes is 90° or 180°. The diameter D5 of the diversion zone 4 is equivalent to the inner diameter D1 of the induction zone, the bandwidth D6 is 15% of the diameter D5 of the diversion zone, and the height difference H4 between layers of rotation is 1 / 4 of the height H1 of th...

Embodiment 2

[0041] An induced interface convection bioreactor, the reactor is in order from bottom to top: inlet pipe, water distribution device, induced fermentation area, purified water outlet, gas collection bag and gas discharge pipe, the water distribution device consists of distributor and Structured packing, the induced fermentation zone is equipped with diversion belts and pulse tubes, the guide zone is a helical coiled metal member, and the pulse tubes are introduced along the tangential direction of the inner wall of the induced fermentation zone, distributed in four positions, any The angle between the two pulse tubes is 90° or 180°. The height (H3) of the water distribution device generally does not exceed 1 / 5 of the inner diameter (D1) of the induction zone. The diameter D5 of the diversion zone is equivalent to the inner diameter D1 of the induction zone, and the bandwidth D6 is 10% of D5. The interlayer height difference H4 of the helical rotation of the diversion zone is ...

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Abstract

The present invention discloses an interface convection inducing bioreactor and applications thereof. The interface convection inducing bioreactor comprises an inlet pipe, a water distribution device, a fermentation induction zone, a purified water outlet, a gas collection bag and a gas discharge pipe, wherein the water distribution device comprises a distributor and a structured filler, the fermentation induction zone is provided with a diversion belt and pulse pipes, the diversion belt is a helical and coiled metal member, the pulse pipe is introduced along the tangential direction of the inner wall of the fermentation induction zone, the included angle between any two pulse pipes is 90 DEG or 180 DEG, the diameter D5 of the diversion belt is equivalent to the inner diameter D1 of the induction zone, the belt width D6 is 10-20% of the D5, the height difference H4 between the layers formed through helical rotation of the diversion belt is 1/10-1/4 of the height H1 of the induction zone. According to the present invention, the regulation on the granular sludge interface morphology and the self-coagulation effect are utilized to reduce the biomass loss along with the liquid removing so as to reduce the use of the subsequent sedimentation tank, the aeration tank and the related equipment and the investment operating cost.

Description

technical field [0001] The invention specifically relates to an induced interface convection bioreactor and a sewage treatment process related thereto, belonging to the technical field of environmental protection equipment. Background technique [0002] In the process of sewage treatment, under the condition of high-load operation of the bioreactor, due to the strong turbulence of multiple convective flows, the high flocculation and high shear force generated by it destroy the structure of the activated granular sludge, causing the sludge to gradually Crack and disperse into small particles. The spallation of small particles increases the effective interface mass transfer area, but if effective control measures cannot be taken, the disordered splitting of particles will lead to being carried out with the water flow, resulting in the loss of biomass and the instability of bed operation . The efficiency of converting sewage into clean energy mainly depends on the effective b...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/34C02F9/14
CPCC02F3/2806C02F3/286Y02E50/30
Inventor 朱明
Owner 深圳市山水乐环保科技有限公司
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