CN201722171U - Air flotation sewage treatment unit - Google Patents

Air flotation sewage treatment unit Download PDF

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Publication number
CN201722171U
CN201722171U CN2010201457204U CN201020145720U CN201722171U CN 201722171 U CN201722171 U CN 201722171U CN 2010201457204 U CN2010201457204 U CN 2010201457204U CN 201020145720 U CN201020145720 U CN 201020145720U CN 201722171 U CN201722171 U CN 201722171U
Authority
CN
China
Prior art keywords
chamber
air
water outlet
air flotation
pump
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2010201457204U
Other languages
Chinese (zh)
Inventor
姚永秀
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
CHENGDU QUYUAN TECHNOLOGY Co Ltd
Original Assignee
CHENGDU QUYUAN TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by CHENGDU QUYUAN TECHNOLOGY Co Ltd filed Critical CHENGDU QUYUAN TECHNOLOGY Co Ltd
Priority to CN2010201457204U priority Critical patent/CN201722171U/en
Application granted granted Critical
Publication of CN201722171U publication Critical patent/CN201722171U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses an air flotation sewage treatment unit, which comprises an air flotation contact chamber and a separating chamber communicated with the upper part of the air flotation contact chamber, wherein the lower part of the separating chamber is communicated with a clear water outlet and a backflow water outlet, the backflow water outlet is positioned under the clear water outlet, the upper parts of the air flotation contact chamber and the separating chamber are provided with a slag scraping device, the upper part of the separating chamber is communicated with a slag discharge port, the bottom of the air flotation contact chamber is communicated with a flocculation chamber, the upper part of the flocculation chamber is provided with a sewage inlet, a stirring device is arranged in the flocculation chamber, the middle part of the air flotation contact chamber is provided with a dissolved gas water release pipe which is connected with a gas-liquid separating tank, the gas-liquid separating tank is connected with a dissolved gas pump, and the dissolved gas pump is connected with the backflow water outlet via a pipeline. The utility model has the advantages of simple technology, low energy consumption and less investment, and is convenient for promotion.

Description

Air floating sewage treatment plant
Technical field
The utility model relates to a kind of waste disposal plant, is specifically related to a kind of air floating sewage treatment plant.
Background technology
Sewage disposal, according to the proportion size of its pollutent that contains, can selective precipitation or pneumatically supported mode remove pollutent.
The ultimate principle of air flotation technology is a bubbling air in water, makes a large amount of micro bubble of generation in the water, by with the magazine particle adhesion to bubble, can form the buoyancy aid of proportion less than water, last floatation surface, thereby obtain a kind of process for purifying water of separating impurity.The water inlet of air-float technology generally will be added flocculation agent and form flocs unit, in water, form the network-like structures of an inner filling water, its sedimentation speed is slower, and adhered to the flocs unit of a certain amount of microbubble, its proportion will be less than the proportion of water, the ascent rate of flocs unit is more faster than the sinking velocity of former flocs unit, and this just makes the air supporting method shorten dramatically than the solid-liquid separation time of the precipitator method.
The utility model content
The utility model provides a kind of air floating sewage treatment plant.
The utility model is achieved in that
Air floating sewage treatment plant, comprise contact chamber, separate chamber with contact chamber top UNICOM, bottom, separate chamber and clear water output and recirculation water outlet UNICOM, the recirculation water outlet is positioned at the clear water output below, on contact chamber and top, separate chamber, be provided with a slag scraper, top, separate chamber and slag-drip opening UNICOM, it is characterized in that: described contact chamber bottom and flocculating chamber UNICOM, top, flocculating chamber is provided with a sewage import, inside, flocculating chamber is provided with a whipping appts, is provided with a dissolved air water releasing tube in the middle of the contact chamber, and the dissolved air water releasing tube is connected with knockout drum, knockout drum is connected with air dissolved pump, and air dissolved pump is connected with the recirculation water outlet by pipeline.
Further scheme is: the filter that also is provided with a level between described separate chamber and the slag-drip opening.
Further scheme is: described air dissolved pump is turbulence pump or gas-liquid multiphase pump.
In the utility model, air dissolved pump adopts turbulence pump or gas-liquid multiphase pump, its principle be at the ingress of pump air in water enters pump case, the impeller of high speed rotating repeatedly cuts into small bubbles with inhaled air, be dissolved in the water rapidly under the hyperbaric environment of small bubbles in pump, the formation dissolved air water enters air flotation pool then and finishes the air supporting process.During the utility model work, at first extract the water of recirculation water outlet as recirculation water by air dissolved pump, produce dissolved air water, dissolved air water discharges into by the dissolved air water releasing tube in the water of exposure chamber, and small bubbles slowly rise and adhere on the impurity particle, forms the buoyancy aid of proportion less than water, last floatation surface, form scum silica frost, and move forward with sluggish flow and to enter the separate chamber, by slag scraper scum silica frost is removed then.Clear water is regulated discharging through overflow, thereby finishes pneumatically supported working process.Sewage adds from the top of flocculating chamber, stirs the small bubbles that produce in the dissolved air water that flco and bottom by the flocculating chamber enter the exposure chamber by flocculation and contacts, and float.The utility model technology is simple, and energy consumption is low, and less investment is convenient to promote.
Description of drawings
Fig. 1 is the utility model structural representation.
Embodiment
As shown in Figure 1, air floating sewage treatment plant, comprise contact chamber 12, separate chamber 4 with contact chamber top UNICOM, bottom, separate chamber and clear water output 7 and recirculation water export 8 UNICOMs, the recirculation water outlet is positioned at the clear water output below, on contact chamber and top, separate chamber, be provided with a slag scraper 4, top, separate chamber and slag-drip opening 6 UNICOMs, described contact chamber bottom and flocculating chamber 2 UNICOMs, top, flocculating chamber is provided with a sewage import 1, and inside, flocculating chamber is provided with a whipping appts 13, be provided with a dissolved air water releasing tube 11 in the middle of the contact chamber, the dissolved air water releasing tube is connected with knockout drum 10, and knockout drum is connected with air dissolved pump 9, and air dissolved pump is connected with the recirculation water outlet by pipeline.Wherein also be provided with the filter 5 of a level between separate chamber and the slag-drip opening, air dissolved pump is turbulence pump or gas-liquid multiphase pump.

Claims (3)

1. air floating sewage treatment plant, comprise contact chamber (12), separate chamber (4) with contact chamber top UNICOM, bottom, separate chamber and clear water output (7) and recirculation water outlet (8) UNICOM, the recirculation water outlet is positioned at the clear water output below, on contact chamber and top, separate chamber, be provided with a slag scraper (4), top, separate chamber and slag-drip opening (6) UNICOM, it is characterized in that: described contact chamber bottom and flocculating chamber (2) UNICOM, top, flocculating chamber is provided with a sewage import (1), inside, flocculating chamber is provided with a whipping appts (13), is provided with a dissolved air water releasing tube (11) in the middle of the contact chamber, and the dissolved air water releasing tube is connected with knockout drum (10), knockout drum is connected with air dissolved pump (9), and air dissolved pump is connected with the recirculation water outlet by pipeline.
2. air floating sewage treatment plant according to claim 1 is characterized in that: the filter (5) that is provided with a level between described separate chamber and the slag-drip opening.
3. air floating sewage treatment plant according to claim 1 is characterized in that: described air dissolved pump is turbulence pump or gas-liquid multiphase pump.
CN2010201457204U 2010-03-31 2010-03-31 Air flotation sewage treatment unit Expired - Fee Related CN201722171U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010201457204U CN201722171U (en) 2010-03-31 2010-03-31 Air flotation sewage treatment unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010201457204U CN201722171U (en) 2010-03-31 2010-03-31 Air flotation sewage treatment unit

Publications (1)

Publication Number Publication Date
CN201722171U true CN201722171U (en) 2011-01-26

Family

ID=43490481

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010201457204U Expired - Fee Related CN201722171U (en) 2010-03-31 2010-03-31 Air flotation sewage treatment unit

Country Status (1)

Country Link
CN (1) CN201722171U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102557178A (en) * 2012-02-20 2012-07-11 无锡工源机械有限公司 Air floating concentration treatment device
CN102951714A (en) * 2012-12-03 2013-03-06 杭州太一化工科技有限公司 Gas dissolving floatation machine
CN103848466A (en) * 2014-03-21 2014-06-11 山东建筑大学 Novel water treatment air floating tank
CN106927558A (en) * 2017-05-09 2017-07-07 山东省城市供排水水质监测中心 The multiphase flow air-floating apparatus and processing method of a kind of ozone Multi-class propagation
CN108529830A (en) * 2018-05-25 2018-09-14 李凯捷 Sewage-treatment plant

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102557178A (en) * 2012-02-20 2012-07-11 无锡工源机械有限公司 Air floating concentration treatment device
CN102557178B (en) * 2012-02-20 2015-03-25 无锡工源机械有限公司 Air floating concentration treatment device
CN102951714A (en) * 2012-12-03 2013-03-06 杭州太一化工科技有限公司 Gas dissolving floatation machine
CN103848466A (en) * 2014-03-21 2014-06-11 山东建筑大学 Novel water treatment air floating tank
CN106927558A (en) * 2017-05-09 2017-07-07 山东省城市供排水水质监测中心 The multiphase flow air-floating apparatus and processing method of a kind of ozone Multi-class propagation
CN108529830A (en) * 2018-05-25 2018-09-14 李凯捷 Sewage-treatment plant

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
DD01 Delivery of document by public notice

Addressee: Chengdu Quyuan Technology Co., Ltd.

Document name: Notification to Pay the Fees

DD01 Delivery of document by public notice

Addressee: Yao Yongxiu

Document name: Notification of Termination of Patent Right

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20110126

Termination date: 20110331