CN103787476A - Sewage flocculation and blow-down system - Google Patents

Sewage flocculation and blow-down system Download PDF

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Publication number
CN103787476A
CN103787476A CN201410028222.4A CN201410028222A CN103787476A CN 103787476 A CN103787476 A CN 103787476A CN 201410028222 A CN201410028222 A CN 201410028222A CN 103787476 A CN103787476 A CN 103787476A
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sewage
flocculation
dirt
cover body
tank body
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CN201410028222.4A
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CN103787476B (en
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马勇杰
王淑芳
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Beijing Union University
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Beijing Union University
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Abstract

The invention provides a sewage flocculation and blow-down system and belongs to the technical field of sewage treatment. The sewage flocculation and blow-down system comprises a sewage and flocculating agent leading-in pipeline (1), a tank body (2), a bracket (3), a double-grade agitator (4), a water collection groove (5), an overflowing groove (6), a spiral umbrella-type cover body I (7), a spiral umbrella-type cover body II (8), a precipitator (9), a water quality monitoring device, a dirt collection barrel (12), a centrifuging drying machine (13) and an equipment adjusting central processor. The sewage flocculation and blow-down system can be used for realizing fixed-period automatic control blow-down so that the flocculation and blow-down system can be prevented from being frequently started and stopped and a liquid supernatant can be continuously overflowed and stored.

Description

Sewage flocculation drainage
Technical field
The present invention relates to a kind of Sewage treatment systems, relate in particular to a kind of sewage flocculation drainage.
Background technology
In technical field of sewage treatment equipment; mostly the flocculation blowdown treatment system that wastewater treatment in China adopts is at present according to traditional flocculation water purification feature design; flocculation tank external and internal compositions has many shortcomings; tend to cause flocculation and blowdown process to disconnect; and operation adjustment process need be shut down rear manual realization, and technological method falls behind.Existing flocculation blowdown technology can cause flocculation supernatant liquor quality unstable conventionally, and emissions is the shortcoming such as automatic control supply not in time and continuously, particular embodiment below what time:
(1) in traditional wastewater flocculation drainage, because equipment mechanism is mostly subject to disposable performance constraint, cannot be according to character such as the water quality in sewage flocculation process, colourity and turbidity, must enter sewage in good time, flocculation agent adds and the operation such as blowdown is adjusted, and has very big blindness like this with regard to the process operation that causes the blowdown of flocculating;
(2) owing to can producing a large amount of flocculation dirts in sewage flocculation process, dirt-collecting is merely able to complete by simple guide shell, these structures of whipping appts at present, but the dirt sinking to the bottom can be easy to be taken up, and then cause dirt can not be collected by fast and stable in whipping process, special in the flocculation drainage of wishing continuous operation, this deficiency can be brought larger problem;
(3) in sewage treatment process, need sufficient supernatant liquor to supply with, existing flocculation drainage, can utilize water pump to take out the method that deposits follow-up storage tank in outward, also has system in the middle part perforate of flocculation tank wall, to carry out liquid and to take out outward simultaneously.These supernatant liquor extracting method can not be guaranteed water quality characteristic, and the economy that frequent start-stop can be supplied with supernatant liquor continuous high-efficient is brought very big infringement.
Summary of the invention
The object of the invention is for a kind of sewage flocculation drainage is provided, implement blindly to solve in existing flocculation method for discharging pollution operation, can not the comprehensive automatic control adjusting of system, method for discharging pollution falls behind and the problem such as supernatant liquor water quality is bad.
For achieving the above object, the present invention is by the following technical solutions:
A kind of sewage flocculation drainage; comprise that sewage and flocculation agent import pipeline 1, tank body 2, support 3, twin-stage stirrer 4, water leg 5, overflow groove 6, spiral umbrella cover body I7, spiral umbrella cover body II8, settling vessel 9, water quality monitoring (WQM) components and parts, dirt-collecting cylinder 12, centrigugal swing dryer 13 and equipment and regulate center processor; it is characterized in that: described tank body 2 is for processing sewage; sewage and flocculation agent import pipeline 1 and are connected with tank body 2, for sewage being imported in tank body 2; The turning axle of twin-stage agitator 4 is positioned at tank body 2, and described spiral umbrella cover body I7 embedding is connected on the turning axle of twin-stage stirrer 4, and in tank body 2 bottom fixed installation spiral umbrella cover body II 8, described settling vessel 9 is installed under described spiral umbrella cover body II 8.The outlet of settling vessel 9 is connected to dirt-collecting cylinder 12, and dirt-collecting cylinder 12 is connected with centrigugal swing dryer 13, between dirt-collecting cylinder 12 and centrigugal swing dryer 13, magnetic valve is installed.In described water leg 5 and overflow groove 6, be welded in tank body 2 upper ends, described water leg 5 is for collecting sewage sample, and described overflow groove 6 receives the excessive liquid of water leg 5, between water leg 5 and overflow groove 6, magnetic valve is installed, it is the middle input channel with Y-shaped magnetic valve body that described sewage and flocculation agent import pipeline 1, described water quality monitoring (WQM) components and parts are arranged on respectively sewage and flocculation agent imports in pipeline 1 and water leg 5, the input terminus of described equipment center treater is connected with the water quality monitoring (WQM) components and parts that sewage and flocculation agent import in pipeline 1 and water leg 5, the control end of described equipment center treater imports the magnetic valve phase downlink connection on pipeline 1 with flocculation agent, control the switching that flocculation agent adds Y-shaped magnetic valve, the control end of described equipment center treater be connected with twin-stage stirrer 4 turning axle control motors, the magnetic valve of the control end of described equipment center treater respectively and between water leg 5 and overflow groove 6, the magnetic valve of controlling between dirt-collecting cylinder 12 and centrigugal swing dryer 13 is connected, end equipment regulates center processor by two-stage water quality monitoring (WQM) feedback signal, first step monitoring is installed on sewage by detection and flocculation agent imports the water quality monitoring (WQM) components and parts in pipeline 1, the rotating speed of regulating and controlling flocculant addition and twin-stage stirrer 4, second stage monitoring is by the water quality monitoring (WQM) components and parts in water leg 5, control magnetic valve between water leg 5 and overflow groove 6 and open and close, and the open and close controlling of controlling the magnetic valve between dirt-collecting cylinder 12 and centrigugal swing dryer 13 realizes the dirt cycle and drains into centrigugal swing dryer 13 outward, described sewage and flocculation agent import pipeline 1 and are connected in tank body 2.Described tank body 2 is positioned on support 3.
Preferably, described Y-shaped magnetic valve flows out a side water quality monitoring (WQM) components and parts is installed, water quality monitoring (WQM) components and parts are colourity and turbidity detector I 10, the sidewall access of Y-valve outlet pipe route tank body 2, and entrance is between spiral umbrella cover body I7, spiral umbrella cover body II 8.
Preferably, it is identical with the blade rotation direction of twin-stage stirrer 4 that embedding is connected on twin-stage stirrer 4 turning axles spiral umbrella cover body I7, and contrary with the blade rotation direction of described twin-stage stirrer 4 at the blade of the tank body 2 hard-wired described spiral umbrella cover body II 8 in bottom, the upper blade of described settling vessel 9 is with contrary in the blade rotation direction of the tank body 2 hard-wired described spiral umbrella cover body II 8 in bottom.
Preferably, the water quality monitoring (WQM) components and parts in water leg 5 are suspended substance detector, CODcr detector, turbidity and chromaticity detector II 11.
Preferably, the dirt that described settling vessel 9 is collected regulates center processor control magnetic valve to be regularly disposed to dirt-collecting cylinder 12 by equipment, is more regularly disposed to centrigugal swing dryer 13 through dirt-collecting cylinder 12 bottom electrical magnet valves.
Sewage flocculation drainage of the present invention can demonstrate very large superiority as in a whole set of Sewage treatment systems.During flocculation working order, embedding is connected in the spiral umbrella cover body on stirrer turning axle, by the rotation direction structure design of multistage umbrella shape cover body blade, can guarantee that throw out accelerates in whipping process, and supernatant liquor floats and enter in the water leg of tank body top, high-quality supernatant liquor flows into overflow groove from water leg; And be fixed on the spiral umbrella cover body of tank base, and can be used for stoping throw out and prevent from being stirred and take up, and then using settling vessel to collect throw out, during blowdown thing working order, can realize as far as possible dirt to arrange outward so outside, flow out and reduce liquid; Dirt-collecting cylinder design can realize flocculation and blowdown process non-interference.Regularly automatic control blowdown, can avoid so the frequent start-stop of drainage of flocculating, the flocculation process of guaranteeing sewage can be successive, make the supernatant liquor can continuous overflow external memory, and dirt can be according to the Transition Design of dirt-collecting cylinder storage volume, realize dirt and drain into centrigugal swing dryer and process according to Production requirement is outer at any time.
Accompanying drawing explanation
Fig. 1 is the connection block diagram of sewage flocculation drainage in prior art;
Fig. 2 is the connection block diagram of sewage flocculation drainage of the present invention;
Fig. 3 is the concrete structure schematic diagram of flocculation drainage of the present invention.
In figure: 1, sewage and flocculation agent import pipeline, 2, tank body, 3, support, 4, twin-stage stirrer, 5, water leg, 6, overflow groove, 7, spiral umbrella cover body I, 8, spiral umbrella cover body II, 9, settling vessel, 10, turbidity and chromaticity detector I, 11, suspended substance detector, CODcr detector, turbidity and chromaticity detector II, 12, dirt-collecting cylinder, 13, centrigugal swing dryer.
Embodiment
With reference to accompanying drawing, will describe specific embodiment of the invention scheme in detail.
As shown in Figure 1; in the sewage flocculation drainage of prior art; sewage and flocculation agent are input in tank body according to a certain constant proportioning; and stirrer carries out mixed flocculation with a fixing rotating speed to it; can rule of thumb determine subsequently stop time; use water pump that supernatant liquor is extracted to external memory, and the flocculation dirt of tank base adopt the mode of hands off carry out outer row and close.
As shown in Figure 2, sewage flocculation drainage of the present invention specific embodiment.Itself and prior art, the difference of sewage flocculation drainage is as shown in Figure 1, the present invention has used two-stage water quality monitoring (WQM), be that center processor is respectively to adding the mixed sewage quality monitoring of flocculation agent and stirring the supernatant liquor water quality monitoring (WQM) after flocculation, realize flocculation agent addition and the control of flocculation stirring speed adjustment, also used center processor to carry out cycle emission control to flocculation dirt.Be with another distinguishing characteristics of existing system, the present invention has used double-deck umbrella shape cover body as shown in Figure 3 and the throw out collection structure of settling vessel combination, can realize throw out and separate smoothly with supernatant liquor, improve supernatant liquor quality, and accelerate the stable collection of throw out.
In Fig. 3, sewage and flocculation agent importing pipeline 1 connect by Y-shaped magnetic valve, turbidity and chromaticity detector I 10 are installed in Y-valve body exit, center processor, by the unlatching size of water quality monitoring (WQM) signal feedback adjustable Y-shaped valve body flocculation agent ingress electromagnetism butterfly valve, is realized the control of flocculation agent addition.Water leg 5 and overflow groove 6 junctions are provided with magnetic valve, suspended substance detector, CODcr detector, chromaticity detector and turbidity detector II 11 have been installed in water leg, when water quality detection is not up to standard, center processor determines closed electromagnetic valve between two grooves by the feedback of water quality monitoring (WQM) signal, and reopens magnetic valve after regulating stirrer rotating speed qualified in the hope of water quality.As being used twin-stage stirrer 4 to accelerate sewage flocculation, system in Fig. 3 mixes, 7 embeddings of spiral umbrella cover body I are connected on stirrer turning axle, be positioned at blade of stirrer top, this cover body blade section can be tetragon or circular section, umbrella shape cover body rotates with stirrer, and this cover body blade is identical with blade of stirrer rotation direction, and supernatant liquor floats from cover body blade gaps, throw out is sunk by cover body leaf baffle, and downward beveled structure design can realize dirt and accelerate to decline; Spiral umbrella cover body II 8 is fixedly installed in tank body lower part, cover body blade section can be tetragon or circular section, be positioned under blade of stirrer, this cover body blade rotation direction is contrary with spiral umbrella cover body I 7 blade rotation directions, spiral umbrella cover body II 8 is mainly used in collecting the flocculation dirt of sinking, prevents that dirt is again taken up in pot liquid whipping process; Settling vessel 9 be installed in spiral umbrella cover body II 8 under, in settling vessel 9 structures, top is the blade of spiral tetragon or circular cross-section, this blade is contrary with spiral umbrella cover body II 8 blade rotation directions, settling vessel sidepiece is closed guard structure, this also can guarantee that dirt is by stable collection again, and settling vessel bottom is circular open, with rows of openings size match outside tank body 2 bottoms.In Fig. 3, tank body 2 bottoms are provided with the dirt-collecting cylinder 12 of two ends with magnetic valve, by the center processor control in Fig. 2, the flocculation dirt of being collected by settling vessel can drain in surge drum outside regularly, this surge drum volume is the several times that settling vessel structure contains dirt volume, and the volume of dirt-collecting cylinder can mate with the dirt storage volume of the centrigugal swing dryer of below 13, utilize the dirt of dirt-collecting cylinder to deposit fade function in, the present invention has just realized separating of flocculation and blowdown these two main process in sewage treatment process, utilize the automatic control function of the center processor quality adjustment of conveniently flocculating, and the emissions time regularly control.

Claims (5)

1. a sewage flocculation drainage, it is characterized in that: it comprises that sewage and flocculation agent import pipeline (1, tank body (2, support (3), twin-stage stirrer (4), water leg (5), overflow groove (6), spiral umbrella cover body I(7), spiral umbrella cover body II(8), settling vessel (9), water quality monitoring (WQM) components and parts, dirt-collecting cylinder (12), centrigugal swing dryer (13) and equipment regulate center processor, it is characterized in that: described tank body (2) is for processing sewage, sewage and flocculation agent import pipeline (1) and are connected with tank body (2), for sewage is imported in tank body (2), the turning axle of twin-stage agitator (4) is positioned at tank body (2), described spiral umbrella cover body I(7) embedding is connected on the turning axle of twin-stage stirrer (4), in tank body (2) bottom fixed installation spiral umbrella cover body II (8), described settling vessel (9) is installed under described spiral umbrella cover body II (8).The outlet of settling vessel (9) is connected to dirt-collecting cylinder (12), and dirt-collecting cylinder (12) is connected with centrigugal swing dryer (13), between dirt-collecting cylinder (12) and centrigugal swing dryer (13), magnetic valve is installed, in described water leg (5) and overflow groove (6), be welded in tank body (2) upper end, described water leg (5) is for collecting sewage sample, described overflow groove (6) receives the excessive liquid of water leg (5), between water leg (5) and overflow groove (6), magnetic valve is installed, it is the middle input channel with Y-shaped magnetic valve body that described sewage and flocculation agent import pipeline (1), described water quality monitoring (WQM) components and parts are arranged on respectively sewage and flocculation agent imports in pipeline (1) and water leg (5), the input terminus of described equipment center treater is connected with the water quality monitoring (WQM) components and parts that sewage and flocculation agent import in pipeline (1) and water leg (5), the control end of described equipment center treater imports the magnetic valve phase downlink connection on pipeline (1) with flocculation agent, control the switching that flocculation agent adds Y-shaped magnetic valve, the control end of described equipment center treater be connected with twin-stage stirrer (4) turning axle control motor, the magnetic valve of the control end of described equipment center treater respectively and between water leg (5) and overflow groove (6), the magnetic valve of controlling between dirt-collecting cylinder (12) and centrigugal swing dryer (13) is connected, end equipment regulates center processor by two-stage water quality monitoring (WQM) feedback signal, first step monitoring is installed on sewage by detection and flocculation agent imports the water quality monitoring (WQM) components and parts in pipeline (1), the rotating speed of regulating and controlling flocculant addition and twin-stage stirrer (4), second stage monitoring is by the water quality monitoring (WQM) components and parts in water leg (5), control magnetic valve switching between water leg (5) and overflow groove (6), and the open and close controlling of controlling the magnetic valve between dirt-collecting cylinder (12) and centrigugal swing dryer (13) realizes the dirt cycle and drains into centrigugal swing dryer (13) outward, described sewage and flocculation agent import pipeline (1) and are connected in tank body (2), described tank body (2) is positioned on support (3).
2. a kind of sewage flocculation drainage according to claim 1, it is characterized in that: described Y-shaped magnetic valve flows out a side water quality monitoring (WQM) components and parts are installed, water quality monitoring (WQM) components and parts are colourity and turbidity detector I (10), the sidewall access of Y-valve outlet pipe route tank body (2), entrance is positioned at spiral umbrella cover body I(7), between spiral umbrella cover body II (8).
3. a kind of sewage flocculation drainage according to claim 1, it is characterized in that: embedding is connected in spiral umbrella cover body I(7 on twin-stage stirrer (4) turning axle) identical with the blade rotation direction of twin-stage stirrer (4), and contrary with the blade rotation direction of described twin-stage stirrer (4) at the blade of tank body (2) the hard-wired described spiral umbrella cover body II in bottom (8), the upper blade of described settling vessel (9) is with contrary in the blade rotation direction of tank body (2) the hard-wired described spiral umbrella cover body II in bottom (8).
4. a kind of sewage flocculation drainage according to claim 1, is characterized in that: the water quality monitoring (WQM) components and parts in water leg (5) are suspended substance detector, CODcr detector, turbidity and chromaticity detector II (11).
5. a kind of sewage flocculation drainage according to claim 1, it is characterized in that: the dirt that described settling vessel (9) is collected regulates center processor control magnetic valve to be regularly disposed to dirt-collecting cylinder (12) by equipment, is more regularly disposed to centrigugal swing dryer (13) through dirt-collecting cylinder (12) bottom electrical magnet valve.
CN201410028222.4A 2014-01-21 2014-01-21 Sewage flocculation drainage Expired - Fee Related CN103787476B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104609480A (en) * 2014-12-31 2015-05-13 孙卫香 Sewage treatment tank device driven by motor
CN104923147A (en) * 2015-07-10 2015-09-23 盐城琛丹低碳技术研究院有限公司 Multi-stage stirring reactor
CN109019766A (en) * 2018-07-14 2018-12-18 芜湖中淇节能科技有限公司 A kind of energy-saving sewage Centrifugal treatment device

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CN103011448A (en) * 2012-11-28 2013-04-03 秦皇岛莱特流体设备制造有限公司 Combined double-vortex efficient muddy water purification device
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CN103172150A (en) * 2013-03-06 2013-06-26 南京梅山冶金发展有限公司 Clarification tank with submersible reflux pump composite micro-vortex reaction process

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JP2011161397A (en) * 2010-02-12 2011-08-25 Suirei:Kk Solid-liquid separator
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CN202185192U (en) * 2011-07-03 2012-04-11 甘肃金桥给水排水设计与工程(集团)有限公司 High-load settling tank
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CN202729865U (en) * 2012-05-17 2013-02-13 苏州苏水环境工程有限公司 Sludge recirculation reactor for treating industrial organic wastewater
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104609480A (en) * 2014-12-31 2015-05-13 孙卫香 Sewage treatment tank device driven by motor
CN104923147A (en) * 2015-07-10 2015-09-23 盐城琛丹低碳技术研究院有限公司 Multi-stage stirring reactor
CN109019766A (en) * 2018-07-14 2018-12-18 芜湖中淇节能科技有限公司 A kind of energy-saving sewage Centrifugal treatment device

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