CN2931458Y - Highly effective physicochemical water treatment sedimentation basin - Google Patents

Highly effective physicochemical water treatment sedimentation basin Download PDF

Info

Publication number
CN2931458Y
CN2931458Y CN 200620026574 CN200620026574U CN2931458Y CN 2931458 Y CN2931458 Y CN 2931458Y CN 200620026574 CN200620026574 CN 200620026574 CN 200620026574 U CN200620026574 U CN 200620026574U CN 2931458 Y CN2931458 Y CN 2931458Y
Authority
CN
China
Prior art keywords
water
tank
mud
flocculation
settling
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
CN 200620026574
Other languages
Chinese (zh)
Inventor
吴作成
Original Assignee
吴作成
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 吴作成 filed Critical 吴作成
Priority to CN 200620026574 priority Critical patent/CN2931458Y/en
Application granted granted Critical
Publication of CN2931458Y publication Critical patent/CN2931458Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

An efficient physicochemical water treatment sedimentation tank relates to a sewage treatment and recycling facility. The traditional facility has the defects of long technological process, large field occupation, large water consumption, and high cost, therefore the efficient physicochemical water treatment sedimentation tank gathering the functions of amalgamate, flocculation, and deposition is designed which is mainly comprising a micro eddy currents waterpower agitator, a flow guiding baffle, a flocculation reaction tank, an inclined tube settling zone, and a sludge thickening zone. This utility model is characterized in that the micro eddy currents waterpower agitator is provided after the water inlet, the flocculation reaction tank is provided at the water inlet side of the precipitating tank, an agitator and a dosing tube are provided in the flocculation reaction tank, a flow guiding baffle is provided in the in the flocculation reaction tank, the sludge thickening zone is provided on the lower portion of the precipitating tank, an exhaust sludge pipe and a sludge reflux pipe are provided at the bottom of the sludge thickening zone, a deposition disengaging gear and a water collecting sump are provide on the upper portion of the precipitating tank, and the water collecting sump is communicated with the water out let channel. This utility model overcomes the shortcomings of traditional art work, increases the sewage precipitation efficiency by 2-4 times and is suitable for the water quality decontamination of dealing with municipal water supply, sewage treatment, and intermediate water advanced treatment and recycling use. One tank has the functions of a plurality of tanks.

Description

Efficient materialization sedimentation pond for water treatment
Technical field
The utility model relates to a kind of water treatment, waste water treating and reutilizing purification of water quality treatment facility, particularly a kind of efficient materialization sedimentation pond for water treatment given.
Background technology
Poor day by day in water resources, water pollutes serious day by day, advocates energetically under the condition of waste water treating and reutilizing, and water treatment coagulating, the purification techniques of economical and efficient will be widely used.Traditional water treatment clarification--the precipitation water processing establishment is made up of mixing pit, reaction tank, settling tank, sludge thickener etc. respectively, has shortcomings such as technical process is long, floor space is big, water consumption is big, construction cost height.
Summary of the invention
The purpose of this utility model is to overcome long, the shortcomings such as floor space is big, water consumption is big, construction cost height of technical process that above-mentioned traditional water treatment facility exists, and designs a kind of efficient materialization sedimentation pond for water treatment.
The efficient materialization sedimentation pond for water treatment of the utility model design is according to following principle:
1. oligodynamics coagulation-settlement process theory: according to little ydrodynamics principle, provide different distributions density, the vortex of frequency and peak strength takes place, increase the particle collision number of times, improve the effective collision rate; Subtract along the journey sorrow according to RANGE IN HOMOGENEOUS ISOTROPIC TURBULENCE simultaneously, form high-frequency vortex, make several materials obtain thorough mixing.
2. the shallow layer precipitating theory that proposes of theoretical promptly 1904 of shallow layer precipitating Ha Zhen (Hazen), in settling tank, sedimentary clearance mainly is the function of surface-area and irrelevant with the degree of depth, time.
3. crowded sedimentation theory is promptly after concentration of suspension in the water is brought up to a certain degree, particulate disturbed around each particulate precipitation all will be subjected to it, sedimentation speed decreases, and forms tangible interface between clear water and mixed water, and precipitation process essence is exactly the decline process at this interface.And employing flocculation back mud technique of backflow, promptly mud circulation composition in flocculation back is than high many of influent concentration, the fluctuation of water inlet suspended substance is absorbed by flocculation back mud round-robin mud, promptly use the mud after flocculating to improve flocculation and sedimentation effect as a kind of catalyzer, also be that sewage is able to the prerequisite of rapid precipitation and guarantees the basic assurance that the anti-influent load of settling tank fluctuates, a kind ofly mixed by micro swirl and design, flocculation reaction, mud concentrate, tube settling separates the efficient materialization sedimentation pond for water treatment of a new generation that forms.
The efficient materialization sedimentation pond for water treatment of the utility model design is mainly realized by following structure.
It mainly is made up of micro swirl hydraulic mixer (3), diaphragm (5), flocculation reaction stirrer (6), flocculation tank (8), tube settling district (10), water leg (11), mud enrichment region (13) and mud thickner (14).At water inlet pipe (1) afterwards, flocculation tank water inlet pipe (4) is provided with micro swirl hydraulic mixer (3) and coagulating agent chemical feed pipe (2) before; Influent side at settling tank is provided with flocculation tank (8), and be provided with a guide shell (9) in the flocculation tank (8), the guide shell center is provided with mixing and blending machine (6), stirrer (6) bottom is provided with dosing endless tube (7), pond bottom is provided with water inlet pipe (4) and from the mud return line (16) of settling tank, is respectively equipped with diaphragm (5) at the flocculation tank wall; Be provided with mud enrichment region (13) and mud thickner (14) in the settling tank bottom, thickner (14) bottom center lowermost end is provided with shore pipe (15) and mud return line (16), be provided with tube settling tripping device (10) on settling tank top, be provided with water leg (11) on inclined tube device (10) top, this water leg is communicated with the water channel (12) that goes out in the settling tank outside.
Description of drawings
Accompanying drawing is a structural representation of the present utility model.
In the drawings: (1) water inlet pipe, (2) coagulating agent chemical feed pipe, (3) micro swirl hydraulic mixer, (4) flocculation basin water inlet pipe, (5) diaphragm, (6) coagulating stirrer, (7) the polymer coagulant aids adds pipe, (8) flocculation tank, (9) guide shell, (10) tube settling district, (11) water leg, (12) go out water channel, (13) mud enrichment region, (14) mud thickner, (15) mud discharging pipe, (16) mud return line.
As shown in the figure at water inlet pipe (1) afterwards, flocculation tank water inlet pipe (4) is provided with before Micro swirl hydraulic mixer (3) and coagulant chemical feed pipe (2). Influent side at sedimentation basin is established Flocculation tank (8) is arranged, and be provided with a guide shell (9) in the flocculation tank (8), lead Stream tube center is provided with mixing and blending machine (6), and mixer (6) bottom is provided with dosing endless tube (7), Pond bottom is provided with water inlet pipe (4) and from the mud return line (16) of sedimentation basin, and is anti-in flocculation Answer the pond wall to be respectively equipped with diaphragm (5); Be provided with mud enrichment region (13) in the sedimentation basin bottom And sludge concentrator (14), thickener (14) bottom center lowermost end is provided with discharge pipeline (15) And mud return line (16), be provided with tube settling separator (10) on sedimentation basin top, Inclined tube device (10) top is provided with water leg (11), going out outside this water leg and the sedimentation basin Water channel (12) is communicated with.
Both water leg of the present utility model was communicated with sedimentation basin outside outlet canal, and this pond from top to bottom Be clear water zone, sloping plate deposition district, mud enrichment region successively, this body another side, pond and coagulation are anti-Answer the chamber to be communicated with, and guide shell of the common layout of coagulation reaction tank, the guide shell center is provided with stirring Machine, coagulating chamber wall is provided with diaphragm simultaneously. The bottom is provided with water inlet pipe and sludge reflux Advance the mud pipe. Before the coagulation reaction tank water inlet, be provided with the micro swirl hydraulic mixer, make into water and coagulation Agent fully mixes.
Use the water treatment technology of the efficient physicochemical water treatment sedimentation basin of the utility model:
The sewage that mixes through dosing at first enters efficient physicochemical water treatment sedimentation basin coagulation by pipeline Reative cell, high polymer coagulant and the returned sludge indoor with hybrid reaction stir mixed through mixer After the solidifying reaction, in guiding region flows into the sedimentation pond for water treatment of side, coagulating chamber. In the water Mud is downward, sinks to then the mud enrichment region, is scraped into discharge pipeline by sludge concentrator and discharges section Divide mud to return in the coagulating chamber through reflux sludge tube again; Enter the water of sedimentation basin to the upper reaches, The collector pipe of water above the body of pond after the tube settling clarification collected, and flows out sedimentation basin, again warp Total outlet pipe flows out. This efficient physicochemical water treatment sedimentation basin can in water treatment, use separately or In combining water treatment technique, use.
The beneficial effects of the utility model are: collection dosing mixing, flocculation reaction, settlement of sewage Clarification, mud concentrating function are in one, and the effect of many ponds effect is played in a pond. Solved tradition That coagulating sedimentation clarification water-purifying process accounts for is big at area, water treatment process is long, energy consumption is high, dosage Greatly, the mud concentrated effect is poor, hydraulic loss is big etc. problem, its deposition efficiency height, floor space The concentrated aqueous rate of little, mud is low, water consumption is little, technological process is short, has reduced energy consumption and worker The journey investment. Can be widely used in municipal water supply processing, sewage disposal or middle water Treatment for Reuse, dirt In the mud concentration technology, it is the desirable efficient thing that substitutes traditional coagulating sedimentation water technology Change sedimentation pond for water treatment.
Embodiment
As shown in the figure, the structure of the efficient materialization sedimentation pond for water treatment of the utility model, this pond body is water leg (11) from top to bottom successively, this water leg goes out water channel (12) with the external side in pond and is communicated with, inclined tube (10), mud enrichment region (13) is provided with mud thickner (14) in the mud enrichment region of body bottom, pond, mud thickner bottom center is communicated with shore pipe (15) and mud return line (16).
This body left side, pond is communicated with flocculation tank (8), be provided with a guide shell (9) of vertically arranging in the flocculation tank, the guide shell center is provided with coagulating stirrer (6), the bottom is provided with flocculation basin water inlet pipe (4), the flocculation tank wall is provided with diaphragm (5), is communicated with polymer coagulant aids chemical feed pipe (7) above the flocculation tank.
It is preceding to enter into flocculation tank (8) at sewage, and a micro swirl hydraulic mixer (3) is arranged, and which is provided with coagulating agent chemical feed pipe (2), sewage inlet pipe (1).
The efficient materialization sedimentation pond for water treatment of the utility model is when carrying out sewage disposal and use, and sewage flows into micro swirl hydraulic mixer (3) by water inlet pipe (1), and micro swirl hydraulic mixer (3) is provided with coagulating agent chemical feed pipe (2) and carries out dosing coagulant.Process dosing blended sewage and the mud that refluxes by mud return line (16) enter into flocculation tank (8) by flocculation basin water inlet pipe (4), add the polymer coagulant aids by being provided with polymer coagulant aids chemical feed pipe (7) in the flocculation tank (8) to sewage, through the sewage that adding the polymer coagulant aids in flocculation tank (8) through coagulating stirrer (6) fully after the flocculation reaction from flow into tube settling district (10) carry out sludge water content from, isolated clear water flows into out water channel (12) and discharges after water leg (11) is collected, isolated mud is discharged by mud thickner (15) and mud discharging pipe (15) after mud enrichment region (3) concentrates.

Claims (1)

1, a kind of efficient materialization sedimentation pond for water treatment, it mainly is made up of micro swirl hydraulic mixer (3), diaphragm (5), flocculation reaction stirrer (6), flocculation tank (8), tube settling district (10), water leg (11), mud enrichment region (13) and mud thickner (14); It is characterized in that afterwards flocculation tank water inlet pipe (4) is provided with micro swirl hydraulic mixer (3) and coagulating agent chemical feed pipe (2) before at water inlet pipe (1); Influent side at settling tank is provided with flocculation tank (8), and be provided with a guide shell (9) in the flocculation tank (8), the guide shell center is provided with mixing and blending machine (6), stirrer (6) bottom is provided with dosing endless tube (7), pond bottom is provided with water inlet pipe (4) and from the mud return line (16) of settling tank, is respectively equipped with diaphragm (5) at the flocculation tank wall; Be provided with mud enrichment region (13) and mud thickner (14) in the settling tank bottom, thickner (14) bottom center lowermost end is provided with shore pipe (15) and mud return line (16), be provided with tube settling tripping device (10) on settling tank top, be provided with water leg (11) on inclined tube device (10) top, this water leg is communicated with the water channel (12) that goes out in the settling tank outside.
CN 200620026574 2006-06-28 2006-06-28 Highly effective physicochemical water treatment sedimentation basin Expired - Fee Related CN2931458Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200620026574 CN2931458Y (en) 2006-06-28 2006-06-28 Highly effective physicochemical water treatment sedimentation basin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200620026574 CN2931458Y (en) 2006-06-28 2006-06-28 Highly effective physicochemical water treatment sedimentation basin

Publications (1)

Publication Number Publication Date
CN2931458Y true CN2931458Y (en) 2007-08-08

Family

ID=38347959

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200620026574 Expired - Fee Related CN2931458Y (en) 2006-06-28 2006-06-28 Highly effective physicochemical water treatment sedimentation basin

Country Status (1)

Country Link
CN (1) CN2931458Y (en)

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101343100B (en) * 2008-08-28 2011-05-04 重庆交通科研设计院 Dual treating device for wastewater of construction
CN101580292B (en) * 2009-06-03 2011-06-15 中国科学院兰州化学物理研究所 Water-distribution anti-disturbance floc precipitation reverse separation device
CN102139972A (en) * 2011-02-15 2011-08-03 北京新源国能科技有限公司 Sewage treatment method and device
CN102179073A (en) * 2011-03-31 2011-09-14 重庆大学 Pump suction type sludge residue external reflux high-efficiency clarification tank
CN102309872A (en) * 2011-09-06 2012-01-11 江苏海洲水务工程有限公司 Clarifying tank
CN102515383A (en) * 2011-11-24 2012-06-27 西安热工研究院有限公司 Water-saving clarification and purification system and process thereof
CN102688615A (en) * 2011-08-29 2012-09-26 甘肃金桥给水排水设计与工程(集团)有限公司 Adjustable micro-flocculation clarification tank and clarification technology
CN102795729A (en) * 2012-09-10 2012-11-28 浙江汉蓝环境科技有限公司 Device and method for treating COD through compound precipitation
CN103145300A (en) * 2013-03-27 2013-06-12 四川省水处理及资源化工程技术研究中心 Sewage treatment system
CN103214141A (en) * 2012-12-07 2013-07-24 北京翰祺环境技术有限公司 Sewage advanced treatment and recycling method capable of substantially raising economy
CN104709986A (en) * 2015-02-13 2015-06-17 河海大学 Combined type water treatment device for improving efficiency of coagulating sedimentation process
WO2016095232A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and vortex sedimentation device therefor
CN108545814A (en) * 2018-03-22 2018-09-18 苏州思纳环保科技有限公司 A kind of precipitation reactor and its application method of heavy-metal ion removal
CN111170559A (en) * 2020-01-07 2020-05-19 无锡市远洲环保科技有限公司 Integrated sewage treatment equipment
CN111592128A (en) * 2020-04-29 2020-08-28 福建省环境保护设计院有限公司 Near water source (ecological) protection area tunnel construction waste water treatment complete equipment
WO2021017615A1 (en) * 2019-08-01 2021-02-04 科盛环保科技股份有限公司 Emergency treatment system for water quality of pump station forebay
CN113072153A (en) * 2021-06-07 2021-07-06 北京水利发展有限公司 Medical waste water is from mixing purification unit

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101343100B (en) * 2008-08-28 2011-05-04 重庆交通科研设计院 Dual treating device for wastewater of construction
CN101580292B (en) * 2009-06-03 2011-06-15 中国科学院兰州化学物理研究所 Water-distribution anti-disturbance floc precipitation reverse separation device
CN102139972A (en) * 2011-02-15 2011-08-03 北京新源国能科技有限公司 Sewage treatment method and device
CN102179073A (en) * 2011-03-31 2011-09-14 重庆大学 Pump suction type sludge residue external reflux high-efficiency clarification tank
CN102688615B (en) * 2011-08-29 2015-06-17 甘肃金桥水科技(集团)股份有限公司 Adjustable micro-flocculation clarification tank and clarification technology
CN102688615A (en) * 2011-08-29 2012-09-26 甘肃金桥给水排水设计与工程(集团)有限公司 Adjustable micro-flocculation clarification tank and clarification technology
CN102309872A (en) * 2011-09-06 2012-01-11 江苏海洲水务工程有限公司 Clarifying tank
CN102515383B (en) * 2011-11-24 2013-08-28 西安西热水务环保有限公司 Water-saving clarification and purification system and process thereof
CN102515383A (en) * 2011-11-24 2012-06-27 西安热工研究院有限公司 Water-saving clarification and purification system and process thereof
CN102795729A (en) * 2012-09-10 2012-11-28 浙江汉蓝环境科技有限公司 Device and method for treating COD through compound precipitation
CN103214141A (en) * 2012-12-07 2013-07-24 北京翰祺环境技术有限公司 Sewage advanced treatment and recycling method capable of substantially raising economy
CN103145300A (en) * 2013-03-27 2013-06-12 四川省水处理及资源化工程技术研究中心 Sewage treatment system
WO2016095232A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and vortex sedimentation device therefor
CN104709986A (en) * 2015-02-13 2015-06-17 河海大学 Combined type water treatment device for improving efficiency of coagulating sedimentation process
CN108545814A (en) * 2018-03-22 2018-09-18 苏州思纳环保科技有限公司 A kind of precipitation reactor and its application method of heavy-metal ion removal
WO2021017615A1 (en) * 2019-08-01 2021-02-04 科盛环保科技股份有限公司 Emergency treatment system for water quality of pump station forebay
CN111170559A (en) * 2020-01-07 2020-05-19 无锡市远洲环保科技有限公司 Integrated sewage treatment equipment
CN111170559B (en) * 2020-01-07 2022-02-18 无锡市远洲环保科技有限公司 Integrated sewage treatment equipment
CN111592128A (en) * 2020-04-29 2020-08-28 福建省环境保护设计院有限公司 Near water source (ecological) protection area tunnel construction waste water treatment complete equipment
CN113072153A (en) * 2021-06-07 2021-07-06 北京水利发展有限公司 Medical waste water is from mixing purification unit

Similar Documents

Publication Publication Date Title
CN2931458Y (en) Highly effective physicochemical water treatment sedimentation basin
CN102659227B (en) Middle-set type high density sediment water purification tank and purification technology thereof
CN202223979U (en) Integrated inclined-tube settling tank
CN201908018U (en) Sewage treatment device
CN204702591U (en) Sewage treatment systems
CN203866080U (en) Circular efficient precipitating device
CN201890794U (en) Novel high-efficiency physicochemical water treatment settling tank device
CN102976526B (en) Forced external circulating type efficient precipitation method and equipment based on addition of lime
CN201971670U (en) High-efficiency coagulative precipitation tank
CN101564609B (en) Vortex grid clarifying pool and clarifying method for enhancing clarifying effect of coagulation reaction in water treatment
CN213803071U (en) Flocculation reactor and sewage treatment equipment
CN204752298U (en) High density depositing reservoir
CN206645932U (en) Integrated high load capacity precipitates separation equipment
CN209468260U (en) A kind of waste water coupling processing device based on magnetic-coagulation and sodium peroxydisulfate catalysis oxidation
CN208814853U (en) Quick black smelly water treatment system of the biochemistry pool in conjunction with efficient sedimentation tank
CN101596374B (en) Swirling flow reaction inclined tube sedimentation tank
CN202844656U (en) Vortex flocculation-clearing equipment
CN109824186A (en) Minerals sand, which is promoted, by negative pressure recycles high speed pellets pool process
CN101428943A (en) Full-flow process for upgrading and reconstructing urban sewage factory
CN203295250U (en) Novel high-speed high-efficiency sedimentation tank for sand addition
CN108328786A (en) A kind of water treatment facilities and method for treating water
CN202080969U (en) Efficient combined water purifier
CN104817234B (en) High concentration wire drawing lubricant Waste Water Treatment
CN210394034U (en) Mineral sand circulation high-speed sedimentation tank lifted by negative pressure
CN101314087A (en) High-efficiency steel-smelting wet-process dedusting sewage water and refining sewage processor

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee