CN106362449A - Clarifier system - Google Patents

Clarifier system Download PDF

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Publication number
CN106362449A
CN106362449A CN201610746248.1A CN201610746248A CN106362449A CN 106362449 A CN106362449 A CN 106362449A CN 201610746248 A CN201610746248 A CN 201610746248A CN 106362449 A CN106362449 A CN 106362449A
Authority
CN
China
Prior art keywords
pipe
defecator
cone bucket
water inlet
air dissolved
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.)
Pending
Application number
CN201610746248.1A
Other languages
Chinese (zh)
Inventor
凌清成
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.)
YIXING LINGTAI ENVIRONMENTAL PROTECTION Co Ltd
Original Assignee
YIXING LINGTAI ENVIRONMENTAL PROTECTION 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 YIXING LINGTAI ENVIRONMENTAL PROTECTION Co Ltd filed Critical YIXING LINGTAI ENVIRONMENTAL PROTECTION Co Ltd
Priority to CN201610746248.1A priority Critical patent/CN106362449A/en
Publication of CN106362449A publication Critical patent/CN106362449A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/02Settling tanks with single outlets for the separated liquid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D21/00Separation of suspended solid particles from liquids by sedimentation
    • B01D21/01Separation of suspended solid particles from liquids by sedimentation using flocculating agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities

Abstract

The invention provides a clarifier system. The clarifier system comprises an agent adding device, a clarifier and a dissolved gas pump. The clarifier comprises a barrel, a conical hopper is arranged at the bottom end of the barrel, a flange at the top end of the barrel is connected with a conical head, the top end of the conical head is connected with a gas producing escape pipe, and the side wall of the gas producing empty pipe is connected with a sludge discharge pipe. The bottom end of the conical hopper is provided with an evacuation pipe, a dissolved gas pump diffuser is arranged at the near-bottom end in the conical hopper in a vertically upward mode, and the dissolved gas pump diffuser is connected with the dissolved gas pump through a dissolved gas pipeline. A water inflow pipe is arranged at the near-top end of the conical hopper, a water outflow pipe is arranged at the near-bottom end of the conical hopper, and the agent adding device is connected with the water inflow pipe through an agent adding pipeline. The clarifier system is simple in structure, low in energy consumption and high in solid-liquid separation efficiency.

Description

A kind of defecator system
Technical field
The present invention relates to sewage treatment area, due to being related to the clarifying equipment of sewage after electro-catalysis or electric flocculation reaction.
Background technology
Defecator is a kind of quick mixing by medicaments such as water and flocculating agents, coagulation, the device of three kinds of processes unifications of precipitation, General scrapes in mud defecator and can arrange inclined tube, and on the one hand its effect is equivalent to guiding device, can mitigate turbulent flow phenomenon, another Aspect can make contamination precipitation in honeycomb inclined-tube surface, reduce precipitation distance, shorten the sedimentation time.
Traditional defecator complex structure with inclined tube, needs to arrange mud-scraping apparatus, energy consumption is higher, has much room for improvement.
Content of the invention
The present invention is directed to the deficiencies in the prior art, there is provided a kind of structure is simple, and energy consumption is relatively low, and solid-liquid separation efficiency is high Defecator system.
For realizing the object of the invention, provide technical scheme below: a kind of defecator system is it is characterised in that include dosing dress Put, defecator, air dissolved pump, defecator includes cylinder, and cylinder bottom is set to cone bucket, and cylinder top flange is connected with taper envelope Head, conical head top is connected with aerogenesis blow-down pipe, and aerogenesis emptying tube side wall is connected with mud discharging pipe, and cone bucket bottom is provided with Evacuated tube, in cone bucket, nearly bottom is provided with air dissolved pump bubbler straight up, and it is molten that air dissolved pump bubbler passes through the connection of Gas dissolving pipe road Air pump, the nearly top of cone bucket is provided with water inlet pipe, and the nearly bottom of cone bucket is provided with outlet pipe, chemicals dosing plant by drug feeding pipeline connect into Water pipe.
Preferably, water inlet pipe stretches in cone bucket, end seal, water inlet pipe offers some on the tube wall in cone bucket Individual water distributing pore.
Preferably, outlet pipe stretches in cone bucket, end seal, outlet pipe offers some on the tube wall in cone bucket Individual gully-hole.
Preferably, electromagnetism liquidometer is provided with cylinder lateral wall.
Preferably, air dissolved pump bubbler is horn mouth.
The invention has the advantages that: the conical design of defecator top and bottom of the present invention is it is ensured that the effect of mud-water separation And its high efficiency;The setting of air dissolved pump, makes mud-water separation effect more efficient, and does not need to produce using during electrochemical reaction Bubble also can achieve separating effect, reduces the energy consumption of electrochemical reaction of registering;Ensure that consolidating at taper layering in defecator Determine liquid level, make equipment in normal operation, need not supervise, also can persistently carry out water outlet and mud extraction;The design of chemicals dosing plant, So that flocculating effect in sewage is accelerated, make sewage accelerate to separate;This equipment can be carried out and electrochemical reaction separately as corollary equipment Connect use, also can directly assembly on electrochemical reaction equipment;This equipment makes the mud producing during electrochemical reaction and bubble system One process, reach the effect of solid-liquid separation, and do not need the time of staying, can continuous effluent and water inlet, W-response is close Carry out under closed loop border, other harmful substances and abnormal smells from the patient will not be produced, make electrochemical reaction more efficient simultaneously, and decrease rear road Flocculating sedimentation technique, decreases civil engineering and puts into and equipment investment, save land resource and cost of investment.
Brief description
Fig. 1 is the structural representation of the present invention.
Fig. 2 is a-a sectional view.
Fig. 3 is b-b sectional view.
Specific embodiment
Embodiment 1: a kind of defecator system, including chemicals dosing plant 1, defecator 2, air dissolved pump 3, defecator 1 includes cylinder 2.1, cylinder 2.1 bottom is set to cone bucket 2.2, and cylinder 2.1 top flange is connected with conical head 2.3, conical head 2.3 top It is connected with aerogenesis blow-down pipe 2.4, aerogenesis blow-down pipe 2.4 side wall is connected with mud discharging pipe 2.5, and cone bucket 2.2 bottom is provided with row Blank pipe 2.6, in cone bucket 2.2, nearly bottom is provided with air dissolved pump bubbler 2.7 straight up, and air dissolved pump bubbler 2.7 passes through molten gas Pipeline 4 connects air dissolved pump 3, and the nearly top of cone bucket 2.2 is provided with water inlet pipe 2.8, and the nearly bottom of cone bucket 2.2 is provided with outlet pipe 2.9, plus Medicine device 1 connects water inlet pipe 2.8 by drug feeding pipeline 5.Water inlet pipe 2.8 stretches in cone bucket 2.2, end seal, water inlet pipe 2.8 Several water distributing pores 2.8.1 is offered on the tube wall in cone bucket 2.2.Outlet pipe 2.9 stretches in cone bucket 2.2, and end seal goes out Water pipe 2.9 is located at and offers several gully-holes 2.9.1 on the tube wall in cone bucket 2.2.It is provided with electromagnetic liquid on cylinder 2.1 side wall Position meter 6.Air dissolved pump bubbler 2.7 is horn mouth.Outlet pipe 2.9 connects the water outlet of annular outlet pipe 7, and annular outlet pipe 7 is vertical U-shaped pipe up, u-shaped pipe is designed as adjustment height structure, primarily serves the number according to mud amount, is observed by external liquid level meter Sludge-water interface height, adjusts annular outlet pipe 7 height, to ensure the effect of water outlet simultaneously.
Its operation logic is: electro-catalysis or the reacted sewage of electric flocculation under closed environment, through cloth after water inlet pipe Water hole enters defecator system, and meanwhile, chemicals dosing plant and air dissolved pump are started working, and (air dissolved pump water inlet can access defecator water outlet Pond, air dissolved pump and diffuser apparatus primarily serve nano grade air bubbles quantity in increase defecator, to guarantee Mud up-floating effect), After sewage entrance defecator after a small amount of dosing, start to be layered, at the taper layering entering defecator upper end, muddy water formally divides From completing, mud is from mud discharging mouth mud extraction, and clear liquid passes through to export distributor pipe and enters circular outlets water outlet, and overall operation is just In the case of often, mud persistently floats, and clear liquid is maintained at defecator lower end, and by annular outlet pipe water outlet, mud enters mud Mummifying pool, clear water enters defecator discharge bay.And excessive gas during electrochemical reaction air dissolved pump work are put by aerogenesis Eat dishes without rice or wine to be vented.The design of evacuation port primarily serves the effect of periodic cleaning defecator.

Claims (5)

1. it is characterised in that including chemicals dosing plant, defecator, air dissolved pump, defecator includes cylinder, cylinder to a kind of defecator system Bottom is set to cone bucket, and cylinder top flange is connected with conical head, and conical head top is connected with aerogenesis blow-down pipe, and aerogenesis is put Blank pipe side wall is connected with mud discharging pipe, and cone bucket bottom is provided with evacuated tube, and in cone bucket, nearly bottom is provided with molten gas straight up Pump bubbler, air dissolved pump bubbler connects air dissolved pump by Gas dissolving pipe road, and the nearly top of cone bucket is provided with water inlet pipe, the nearly bottom of cone bucket It is provided with outlet pipe, chemicals dosing plant connects water inlet pipe by drug feeding pipeline.
2. a kind of defecator system according to claim 1 is it is characterised in that water inlet pipe stretches in cone bucket, end seal, Water inlet pipe is located at and offers several water distributing pores on the tube wall in cone bucket.
3. a kind of defecator system according to claim 1 is it is characterised in that outlet pipe stretches in cone bucket, end seal, Outlet pipe is located at and offers several gully-holes on the tube wall in cone bucket.
4. a kind of defecator system according to claim 1 is it is characterised in that be provided with electromagnetism liquidometer on cylinder lateral wall.
5. a kind of defecator system according to claim 1 is it is characterised in that air dissolved pump bubbler is horn mouth.
CN201610746248.1A 2016-08-29 2016-08-29 Clarifier system Pending CN106362449A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610746248.1A CN106362449A (en) 2016-08-29 2016-08-29 Clarifier system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610746248.1A CN106362449A (en) 2016-08-29 2016-08-29 Clarifier system

Publications (1)

Publication Number Publication Date
CN106362449A true CN106362449A (en) 2017-02-01

Family

ID=57902912

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610746248.1A Pending CN106362449A (en) 2016-08-29 2016-08-29 Clarifier system

Country Status (1)

Country Link
CN (1) CN106362449A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107082508A (en) * 2017-05-09 2017-08-22 江苏凌泰环境技术有限公司 The efficient pollution treatment water cleaning systems of modularization
CN110156124A (en) * 2019-06-21 2019-08-23 马一帅 A kind of closed micro swirl clarifier and its defecation method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2401273Y (en) * 1999-12-03 2000-10-18 西安建筑科技大学 High-efficient gas flotation apparatus
KR100919367B1 (en) * 2008-04-15 2009-09-29 이순화 Flotation device using high efficiency tank for dissolving a gases into liquids
CN102100979A (en) * 2011-01-11 2011-06-22 东北电力大学 Adjustable air-floating and precipitating switching solid-liquid separating device
CN203922786U (en) * 2014-04-28 2014-11-05 深圳科力迩科技有限公司 A kind of air-flotation separation equipment
CN206103425U (en) * 2016-08-29 2017-04-19 宜兴市凌泰环保设备有限公司 Clarifier system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2401273Y (en) * 1999-12-03 2000-10-18 西安建筑科技大学 High-efficient gas flotation apparatus
KR100919367B1 (en) * 2008-04-15 2009-09-29 이순화 Flotation device using high efficiency tank for dissolving a gases into liquids
CN102100979A (en) * 2011-01-11 2011-06-22 东北电力大学 Adjustable air-floating and precipitating switching solid-liquid separating device
CN203922786U (en) * 2014-04-28 2014-11-05 深圳科力迩科技有限公司 A kind of air-flotation separation equipment
CN206103425U (en) * 2016-08-29 2017-04-19 宜兴市凌泰环保设备有限公司 Clarifier system

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李杰训等编著: "《聚合物驱油地面工程技术》", 31 October 2008 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107082508A (en) * 2017-05-09 2017-08-22 江苏凌泰环境技术有限公司 The efficient pollution treatment water cleaning systems of modularization
CN110156124A (en) * 2019-06-21 2019-08-23 马一帅 A kind of closed micro swirl clarifier and its defecation method

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Application publication date: 20170201

RJ01 Rejection of invention patent application after publication