CN205472856U - Integration tube settler - Google Patents

Integration tube settler Download PDF

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Publication number
CN205472856U
CN205472856U CN201620279361.9U CN201620279361U CN205472856U CN 205472856 U CN205472856 U CN 205472856U CN 201620279361 U CN201620279361 U CN 201620279361U CN 205472856 U CN205472856 U CN 205472856U
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China
Prior art keywords
tube
basin
dosing tank
bucket
tube settler
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CN201620279361.9U
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Chinese (zh)
Inventor
焦明月
张环芝
蔡先胜
许青锋
蒋松钰
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Henan Hongsheng Environmental Protection Equipment Manufacturing Co Ltd
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Henan Hongsheng Environmental Protection Equipment Manufacturing Co Ltd
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Priority to CN201620279361.9U priority Critical patent/CN205472856U/en
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Abstract

The utility model discloses an integration tube settler, including the box, be equipped with equipment room, coagulating basin, flocculation basin and tube settler in the box, be equipped with PAC dosing tank and PAM dosing tank in the equipment room, the PAC dosing tank is connected with the coagulating basin, and the PAM dosing tank is connected with the flocculation basin, all is equipped with the agitator in coagulating basin and the flocculation basin, the tube settler middle part is equipped with the pipe chute, and the tube settler lower part is equipped with the bagger. The utility model discloses utilizing the shallow layer to precipitate the principle, making precipitation efficiency obtain great improvement, area is little, convenient operation, and the running cost is low, and it is integrated to be convenient for, can realize the management of full automatic operation.

Description

A kind of integrated inclined-tube settling tank
Technical field
This utility model relates to the technical field of sewage disposal, it is specifically related to a kind of integrated inclined-tube settling tank, can be widely applied to industrial wastewater, sanitary sewage, the process of non-ferrous metals processing waste water, power plant, the process of boiler room hydraulic dust-removing waste water, the process of gas station washings, the process of biochemical water and the pretreatment etc. of water supply purification.
Background technology
Along with socioeconomic development, the swift and violent increase of population, cause sharply increasing of sanitary sewage and industrial wastewater, cause serious water resource pollution.The problem of short water supply and sewage discharge is more and more prominent, and the nowadays process of sewage has become as one of urgent problem in society, and sewage disposal has the biggest necessity.Sedimentation tank is that application precipitation removes a kind of structures of float in water, and sedimentation tank is the most widely used, and the most conventional has auxiliary flow settling pond, vertical sedimentation basin and tube settler.Auxiliary flow settling pond uses mechanical dredge, runs preferably, and equipment is relatively simple, the existing approved product of soil discharging facility, and precipitability is effective, and day output is big, little to water body agitation, the beneficially removal of float;Its shortcoming is that water water velocity is unstable, is affected relatively big by water inlet, and mud, soil discharging facility complexity are scraped in bottom, and the requirement to unit in charge of construction is high, and floor space is big compared with other sedimentation tanks, applies in general to large and medium-sized sewage treatment plant.Vertical sedimentation basin spoil disposal is convenient, and management is simple, and floor space is little;Its shortcoming has the pond degree of depth big, constructional difficulties, and the adaptation ability of impact load and variations in temperature is poor, and cost is higher, and Chi Jing is difficult to excessive, easily causes water distribution uneven.Tube settler is a kind of new and effective settling apparatus, theoretical according to discrete particles shallow layer precipitating, drawing advanced foreign technology and development on the basis of rectangular sedimentation tank to update, improve, its advantage has: increase desilting area, shortens settling height thus improves the clearance of granule.The swash plate inclination angle of tube settler is 60 degree, the multiple that its efficiency improves is equivalent to the multiple that the swash plate former pool area of total projection area ratio increases, re-uniting of swash plate inclined tube, promote the further increasing of wadding grain, thus improve sedimentation velocity, create laminar flow condition, thus improve settling efficiency, water project situation is good, and treatment effeciency is high;Disposal ability is more much bigger than general sedimentation tank, promotes the use of prospect the most wide.
Utility model content
In order to solve above-mentioned technical problem, this utility model provides a kind of integrated inclined-tube settling tank, and treatment effeciency is high, and effluent quality is good, and operating cost is low, and floor space is little, it is simple to integrated, easy to operate, it is possible to achieve fully automatic operation manages.
In order to achieve the above object, the technical solution of the utility model is: a kind of integrated inclined-tube settling tank, including casing, equipment room, coagulating basin, flocculation basin and tube settler it is provided with in casing, PAC dosing tank and PAM dosing tank it is provided with in described equipment room, PAC dosing tank is connected with coagulating basin, and PAM dosing tank is connected with flocculation basin, is equipped with agitator in coagulating basin and flocculation basin;Being provided with inclined tube in the middle part of described tube settler, tube settler bottom is provided with bucket.
Described equipment room is arranged on above coagulating basin and flocculation basin, the most adjacent connection of coagulating basin, flocculation basin and tube settler.
Described PAC dosing tank is positioned at above coagulating basin, and PAM dosing tank is positioned at the top of flocculation basin.
It is provided with water hole between described coagulating basin and flocculation basin, between flocculation basin and tube settler, is provided with water hole.
Described bucket includes that the first bucket and the second bucket, the first bucket and the second bucket are connected in parallel, and the first bucket and the second bucket bottom are equipped with mudhole.
The inclination angle of described inclined tube is 60 degree, and inclined tube is paved with the middle part of tube settler.
Described tube settler top is provided with discharge outlet, and discharge outlet is connected with drain pipe.
Described PAC dosing tank is all connected with electric control system with PAM dosing tank.
Of the present utility model being unique in that tube settler utilizes shallow layer precipitating principle, make deposition efficiency be greatly improved, floor space is little simultaneously, easy to operate, and operating cost is low, it is simple to integrated, it is possible to achieve fully automatic operation manages.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, the accompanying drawing used required in embodiment or description of the prior art will be briefly described below, apparently, accompanying drawing in describing below is only embodiments more of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, it is also possible to obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model.
Fig. 2 be in this utility model Fig. 1 A-A to profile.
In figure, 1 is casing, and 2 is equipment room, and 3 is coagulating basin, and 4 is flocculation basin, and 5 is PAC dosing tank, and 6 is PAM dosing tank, and 7 is the first agitator, and 8 is the second agitator, and 9 is association control sedimentation tank, and 10 is inclined tube, and 11 is the first bucket, and 12 is the second bucket.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is clearly and completely described, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole embodiments.Based on the embodiment in this utility model, the every other embodiment that those of ordinary skill in the art are obtained under not paying creative work premise, broadly fall into the scope of this utility model protection.
As depicted in figs. 1 and 2, a kind of integrated inclined-tube settling tank, including casing 1, casing 1 is made up of carbon steel (or rustless steel) material.Being provided with equipment room 2, coagulating basin 3, flocculation basin 4 and tube settler 9 in casing 1, casing 1 is by whole device becoming one equipment.Equipment room 2 and coagulating basin 3, flocculation basin 4, tube settler 9 are the most adjacent, and flocculation basin 4 is between coagulating basin 3 and tube settler 9, and equipment room 2 is positioned at coagulating basin 3 and flocculation basin 4 homonymy.Being provided with PAC dosing tank 5 and PAM dosing tank 6 in equipment room 2, PAC dosing tank 5 is connected with coagulating basin 3, and PAC dosing tank 5 adds PAC coagulant in coagulating basin 3, and PAM dosing tank 6 is connected with flocculation basin 4, and PAM dosing tank 6 adds PAM flocculant in flocculation basin 4.It is provided with water hole between coagulating basin 3 and flocculation basin 4, between flocculation basin 4 and tube settler 9, is provided with water hole.
Being equipped with agitator in coagulating basin 3 and flocculation basin 4, the first agitator 7 is positioned at the middle part of coagulating basin 3, and the second agitator 8 is positioned at the middle part of flocculation basin 4.First agitator 7 and the second agitator 8 bottom are provided with stirring vane, for increasing the contact area with agitated liquid.In coagulating basin 3 under the effect of PAC coagulant, utilize coagulant sedimentation to make the colloid in waste water and fine suspension be condensed into floccule body, be then separated off.Coagulant sedimentation application in water processes is the most widely, and it both can reduce the sense index of the water quality such as the turbidity of former water, colourity, can remove again multiple hazardous contaminant.The first agitator 7 it is provided with in coagulating basin 3, floccule body in coagulating basin 3 is mix homogeneously under the effect of the first agitator 7, flocculation basin 4 is entered by water hole, under the effect of PAM flocculant, it is bigger floccule body by tiny floccule body cohesion, mix homogeneously under the stirring of the second agitator 8, enters tube settler 9 by water hole.Being provided with inclined tube 10 in the middle part of tube settler 9, tube settler 9 bottom is provided with bucket.
Preferably, equipment room 2 is arranged on above coagulating basin 3 and flocculation basin 4, coagulating basin 3, flocculation basin 4 and the most adjacent connection of tube settler 9.PAC dosing tank 5 is positioned at the top of coagulating basin 3, and PAM dosing tank 6 is positioned at the top of flocculation basin 4, conveniently adds PAC coagulant in coagulating basin 3 and adds PAM flocculant in flocculation basin 4.
Preferably, tube settler 9 is internal is divided into three layers, and top is clear water layer, and middle part is inclined tube layer, and bottom is cushion.Inclined tube 10 inclination angle of inclined tube layer is 60 degree, and is paved with whole aspect.Tube settler 9 top is provided with discharge outlet, and discharge outlet is connected with drain pipe.The cushion of bottom is arranged below bucket, the muddy water after discharging precipitation.Bucket includes that the first bucket 11 and the second bucket 12, the first bucket 11 and the second bucket 12 are connected in parallel, and the first bucket 11 and the second bucket 12 bottom are equipped with mudhole.
Preferably, after the bigger floccule body of mix homogeneously enters tube settler 9, according to shallow pond sedimentation theory, the inclined tube 10 of a lot of area is set at settling zone, the suspended impurity made in mixed liquor in bigger floccule body and water precipitates in inclined tube, the body refuse separated under gravity along swash plate in the bucket being snapped down at the bottom of pond, then concentrate discharge, tube settler 9 top connects drain pipe, arranges outside supernatant.
Preferably, PAC dosing tank 5 is all connected with electric control system with PAM dosing tank 6, can control, by electrical apparatus control system, amount and the time that PAC dosing tank 5 and PAM dosing tank 6 adds PAC and PAM respectively in coagulating basin 3 and flocculation basin 4.
The above; it is only this utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; any those familiar with the art is in the technical scope that this utility model discloses; the change that can readily occur in or replacement, all should contain within protection domain of the present utility model.

Claims (8)

1. an integrated inclined-tube settling tank, including casing (1), equipment room (2), coagulating basin (3), flocculation basin (4) and tube settler (9) it is provided with in casing (1), it is characterized in that: in described equipment room (2), be provided with PAC dosing tank (5) and PAM dosing tank (6), PAC dosing tank (5) is connected with coagulating basin (3), PAM dosing tank (6) is connected with flocculation basin (4), is equipped with agitator in coagulating basin (3) and flocculation basin (4);Described tube settler (9) middle part is provided with inclined tube (10), and tube settler (9) bottom is provided with bucket.
Integrated inclined-tube settling tank the most according to claim 1, it is characterised in that: described equipment room (2) is arranged on coagulating basin (3) and flocculation basin (4) top, coagulating basin (3), flocculation basin (4) and tube settler (9) the most adjacent connection.
Integrated inclined-tube settling tank the most according to claim 2, it is characterised in that: described PAC dosing tank (5) is positioned at the top of coagulating basin (3), and PAM dosing tank (6) is positioned at the top of flocculation basin (4).
Integrated inclined-tube settling tank the most according to claim 2, it is characterised in that: it is provided with water hole between described coagulating basin (3) and flocculation basin (4), between flocculation basin (4) and tube settler (9), is provided with water hole.
Integrated inclined-tube settling tank the most according to claim 1, it is characterized in that: described bucket includes the first bucket (11) and the second bucket (12), first bucket (11) and the second bucket (12) are connected in parallel, and the first bucket (11) and the second bucket (12) bottom are equipped with mudhole.
Integrated inclined-tube settling tank the most according to claim 1, it is characterised in that: the inclination angle of described inclined tube (10) is 60 degree, and inclined tube (10) is paved with the middle part of tube settler (9).
Integrated inclined-tube settling tank the most according to claim 1, it is characterised in that: described tube settler (9) top is provided with discharge outlet, and discharge outlet is connected with drain pipe.
Integrated inclined-tube settling tank the most according to claim 1, it is characterised in that: described PAC dosing tank (5) is all connected with electric control system with PAM dosing tank (6).
CN201620279361.9U 2016-04-07 2016-04-07 Integration tube settler Active CN205472856U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620279361.9U CN205472856U (en) 2016-04-07 2016-04-07 Integration tube settler

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Application Number Priority Date Filing Date Title
CN201620279361.9U CN205472856U (en) 2016-04-07 2016-04-07 Integration tube settler

Publications (1)

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CN205472856U true CN205472856U (en) 2016-08-17

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109775894A (en) * 2019-03-15 2019-05-21 杭州航民达美染整有限公司 A kind of pre-processing system of dyeing and printing sewage
CN111268777A (en) * 2019-01-09 2020-06-12 晴邦(上海)环保科技有限公司 Novel self-cleaning inclined tube sedimentation tank
CN112174395A (en) * 2020-11-13 2021-01-05 中冶京诚工程技术有限公司 Multistage coagulating sedimentation device
CN112573690A (en) * 2020-05-20 2021-03-30 汕头市国富锆钛实业有限公司 Method for treating beneficiation wastewater of zirconium-titanium concentration plant

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111268777A (en) * 2019-01-09 2020-06-12 晴邦(上海)环保科技有限公司 Novel self-cleaning inclined tube sedimentation tank
CN109775894A (en) * 2019-03-15 2019-05-21 杭州航民达美染整有限公司 A kind of pre-processing system of dyeing and printing sewage
CN109775894B (en) * 2019-03-15 2022-04-01 杭州航民达美染整有限公司 Leading processing system of printing and dyeing sewage
CN112573690A (en) * 2020-05-20 2021-03-30 汕头市国富锆钛实业有限公司 Method for treating beneficiation wastewater of zirconium-titanium concentration plant
CN112174395A (en) * 2020-11-13 2021-01-05 中冶京诚工程技术有限公司 Multistage coagulating sedimentation device

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