CN106315797A - Small fine dosing, coagulating and precipitating integrated device - Google Patents
Small fine dosing, coagulating and precipitating integrated device Download PDFInfo
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- CN106315797A CN106315797A CN201610693807.7A CN201610693807A CN106315797A CN 106315797 A CN106315797 A CN 106315797A CN 201610693807 A CN201610693807 A CN 201610693807A CN 106315797 A CN106315797 A CN 106315797A
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- coagulating
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
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- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention provides a small fine dosing, coagulating and precipitating integrated device which comprises a coagulating purifier and a coagulating and dosing control system communicated with the coagulating purifier. A coagulating reaction area, a floc separation area and a precipitation area are arranged in the coagulating purifier, and an agent mixer is arranged in the middle of the coagulating reaction area; the coagulating and dosing control system comprises a water incoming pipe communicated with the agent mixer, a coagulating agent adding pipe, water outgoing pipes arranged on two sides of the outside of the floc separation area, a water incoming electromagnetic flow meter arranged on the water incoming pipe, a water incoming turbidity online monitoring sensor, a dosing tank arranged on the coagulating agent adding pipe, a coagulating agent metering pump, a water outgoing turbidity online monitoring sensor and an industrial personal computer. By using the device, equipment of a coagulating and precipitating system and process simplifying are realized, extensiveness and blindness in agent adding of conventional coagulating and precipitating systems are avoided, and economic efficiency and suitability of coagulating and precipitating technology in small dispersive water supply and drain treatment are improved.
Description
Technical field
The present invention relates to fwaater resources protection and water environment treatment field, a kind of small-sized fine dosing coagulating sedimentation one
Body gasifying device.
Background technology
Coagulating sedimentation be most basic during drinking water and various stain disease process also be of paramount importance process technique, by
Dosing coagulant and flocculation aid such as aluminium polychlorid (PAC) and polyacrylamide (PAM) etc. in water, make water is difficult to precipitate
Grain is aggregated with one another and forms colloid, and then the impurity in water body is combined and forms bigger coagulation body, by clean after solid-liquid separation
Change water body.Widely, it both can reduce the sense of the water quality such as the turbidity of former water, colourity in coagulating sedimentation application in water processes
See index, multiple hazardous contaminant can be removed again.
Ending for the end of the year 2015, it is 56.1% that China's urban population accounts for total population proportion, still has more than 600,000,000 rural area permanent resident populations
The small-sized supply and discharge engineering of water treatment having a large capacity and a wide range is relied on water.In order to remove oil removal, impurity or pollutant, coagulating sedimentation is usually
It is applied to tap water station in rural areas, Sewage Disposal and emergence watering system, but the most directly applies mechanically big-and-middle-sized concentration and supply
Water waterworks and the coagulative precipitation tank of stain disease treatment plant, with reference to " sewage coagulation and coagulating treatment engineering legislation " HJ
The coagulating sedimentation system of 2006-2010 design, generally by multiple structures such as solution pool, dissolving tank, sedimentation tank, blender, aerators
Building the composition such as thing and appliance arrangement, technological process is relatively complicated, and space availability ratio is the highest；Adding of coagulant or flocculation aid is main
Empirically, for ensureing effluent quality, excess dispensing is relatively conventional, which not only improves water treatment agent cost, also creates
Certain water pollution.
Inventor finds during realizing the present invention, and coagulation-settlement process is in small rural water supply and sewage processes practice
Have the disadvantage that the coagulating sedimentation facility that the centralized scale in (1) cities and towns processes processes at small-sized distributing rural area water supply and sewage
In the suitability poor, civil engineering and engineering construction cost are high, are badly in need of the miniaturization of coagulating sedimentation system, equipment；(2) vast agriculture
Village's regional economy condition falls behind, and technical staff lacks, and is difficult to the techniques such as the relatively complicated dispensing of management process, coagulation, precipitation, existing
The simplification of row coagulating sedimentation system and intellectuality are not enough；(3) in precipitation process of coagulation, coagulant and flocculation aid add blindly, throw
Specific aim and the science of medicine have much room for improvement.
Therefore, how coagulating sedimentation system is carried out equipment, miniaturization, simplification, intellectuality, by dispensing, coagulation, sink
The process integrated designs such as shallow lake, and carry out Automated condtrol, processing for rural area water supply and sewage provides complete suitable device, to building U.S.
Beautiful rural area, improves Rural Human Settlements, ensures rural area water safety, has great economy, society, environmental benefit and answers
Use prospect.
Summary of the invention
The present invention provides a kind of small-sized fine dosing coagulating sedimentation integrated apparatus, is mainly used in small-sized distributing rural area
Water supply and sewage processes, and need not build individually dispensing, coagulation, deposition facility, rely on coagulation and settling system integrated design, it is achieved
The equipment of coagulating sedimentation system and handling process are simplified, and decrease the occupation of land of coagulation-settlement process；Turbid by Inlet and outlet water
Degree on-line monitoring, the dosage of Precise control coagulated agent, it is to avoid traditional coagulating sedimentation system medicament throw in extensive with
Blindness, improves coagulating sedimentation technology economy in small-sized distributing water supply and sewage processes and the suitability.
For achieving the above object, the technical solution used in the present invention is:
A kind of small-sized fine dosing coagulating sedimentation integrated apparatus, including coagulation depurator, coagulation depurator is top circle
Cylinder, the cone cylinder shape of lower cone body, be provided with in coagulation depurator and be positioned at the coagulating district of cylindrical region, flco Disengagement zone
And it is positioned at the flco settling zone of cone area, and flco Disengagement zone is positioned at coagulating district both sides external, it is characterised in that: also wrap
Include the coagulation dosing control system connected with coagulation depurator, in the middle part of coagulating district, be provided with agent mixer, coagulating district
Bottom be provided with the aerator being connected with air compressor, the both sides, top in coagulating district are provided with profile of tooth overflow launder, coagulation
Control system for adding drugs includes the water inlet pipe connected with agent mixer, coagulant dosage pipe, is located at flco Disengagement zone both sides external
Outlet pipe, the water inlet electromagnetic flowmeter being located on water inlet pipe, influent turbidity on-line monitoring sensor, be located at coagulant dosage pipe
On grug feeding jar, coagulant dosing pump, the delivery turbidity on-line monitoring sensor being located on outlet pipe and with water inlet electromagnetic current
The industrial computer that gauge, influent turbidity on-line monitoring sensor, coagulant dosing pump are connected.
Further, coagulating district is internally installed multiple water body water conservancy diversion flap being vertically crisscross arranged, multiple water bodys
Form flow-guiding channel between water conservancy diversion flap, guide water inlet to be pressed in coagulating district by bottom or the top of water body water conservancy diversion flap
Sequence flows.
Further, industrial computer is for the flow of inlet water recorded according to water inlet electromagnetic flowmeter, influent turbidity on-line monitoring
The delivery turbidity that influent turbidity that sensor records, delivery turbidity on-line monitoring sensor record, measures by controlling coagulant
Pump adjusts the coagulant charging quantity in agent mixer.
Further, agent mixer includes medicament vortex mixer and the coagulant dosage shower nozzle being located in medicament vortex mixer,
Inside agent mixer, former water in water inlet pipe or the stain disease coagulant solution pre-configured with coagulant dosage pipe
Being sufficiently mixed, coagulant dosage shower nozzle bottom is funnel-form, is used for storing coagulant solution, and top is spherical perforated tube, uses
In dispersion coagulant solution, coagulant solution escapes from top aperture through funnel from bottom to top, uniformly mixes with former water or stain disease
Close, carry out coagulation subsequently into coagulating district.
Further, described aerator includes the aeration tube being located at the bottom in coagulating district and connects with aeration tube
Being located at the aeration head in the centre position of adjacent two blocks of water body water conservancy diversion flaps, air compressor is connected with aeration tube, is used for blasting sky
The high-efficient contact of water body, enhanced coagulation agent and pollutant is moved in gas mixing.
Further, the flco solid-liquid separation swash plate for reinforced deposition and flco solid-liquid separation it are provided with in flco Disengagement zone
Assembly, granule flco carries out solid-liquid separation through flco solid-liquid separation swash plate under gravity, on flco solid-liquid separation swash plate
Side is clear liquid, and lower section is solid precipitation.
Further, flco solid-liquid separation swash plate material is plastics or fiberglass, is fixed on the wall of coagulation depurator, inclines
Tiltedly arranging, inclination angle is generally 45-60 °, spacing 8-10cm of adjacent two pieces of flco solid-liquid separation swash plates.
Further, flco settling zone is provided with sludge bucket, and the bottom of sludge bucket is provided with mud valve, can periodically pass through gravity
Discharge body refuse, top, flco settling zone, in cylinder and the cone junction of coagulation reactor, it is provided with flush pipe along inwall
Road, pipeline has the Flushing nozzle towards cone cylinder inwall, utilizes water inlet to rinse flco settling zone, discharges and is difficult to what nature was removed
Body refuse.
Further, water inlet pipe is additionally provided with intake pump, water intaking valve.
Further, it is provided with four coagulation depurator supports bottom coagulation depurator, coagulation depurator support is provided with
Coagulation depurator castor, it is simple to mobile and carrying.
Owing to have employed such scheme, technological innovation and marked improvement that the present invention highlights be:
(1) integrating the processes such as coagulation, flco separation and precipitation, form compact conformation, flow process continuous print integrated purifying fills
Putting, same device possesses multi-functional, small and exquisite flexibly, device space availability ratio is high.
(2) water body water conservancy diversion flap is set, it is achieved that water body, at the olderly flowage in coagulating district, improves pollutant with mixed
The contact performance of solidifying agent；Often organize the centre position of water body water conservancy diversion flap, be provided with boring aeration pipe, utilize air agitation water body,
The dirt destroyed and rinse flap surface attachment, meanwhile, it is to avoid pollutant are deposited in bottom coagulating district and deposit.
(3) in coagulating district, agent mixer is set, by coagulant shower and medicament vortex mixer, it is ensured that medicament
The efficient uniform real with water inlet mixes, and improves service efficiency and the coagulation effect of coagulated agent.
(4) use flco solid-liquid separation swash plate and assembly thereof, utilize shallow pond sedimentation theory to lay multilayer incline-plate, add wadding
The surface that body separates processes load, is effectively increased the solid-liquid separation performance of granule flco, reduces the bulk of device.
(5) utilize turbidity on-line monitoring and Real-time Feedback, automatically adjusted the dosage of coagulant by industrial computer, guaranteeing
On the basis of coagulating sedimentation effect, improve the science of coagulant dosage and the level that becomes more meticulous, reduce dosing and throwing
Expenses for medicine is used.
Accompanying drawing explanation
Fig. 1 is the horizontal section structure of coagulation depurator in the small-sized fine dosing coagulating sedimentation integrated apparatus of the present invention
Figure；
Fig. 2 is the longitudinal profile structure of coagulation depurator in the small-sized fine dosing coagulating sedimentation integrated apparatus of the present invention
Figure；
Fig. 3 is the structural representation of coagulation dosing control system in the small-sized fine dosing coagulating sedimentation integrated apparatus of the present invention
Figure.
In figure: 1 water inlet pipe, 2 intake pumps, 3 water intaking valves, 4 water inlet electromagnetic flowmeters, 5 air compressors,
6 influent turbidity on-line monitoring sensors, 7 grug feeding jars, 8 enter medicine valve, 9 coagulant dosing pumps, 10 coagulant dosages
Pipe, 11 industrial computers, 12 outlet filter screens, 13 delivery turbidity on-line monitoring sensors, 14 outlet valves, 15 water outlets
Pipe, 16 agent mixers, 17 coagulating districts, 18 water body water conservancy diversion flaps, 19 flco solid-liquid separation swash plates, 20 waddings
Body Disengagement zone, 21 well word supports, 22 settling of floccus districts, 23 flush pipes, 24 sludge buckets, 25 coagulation depurators prop up
Frame, 26 coagulation depurator castors, 27 medicament vortex mixers, 28 coagulant dosage shower nozzles, 29 flco solid-liquid separation assemblies；
30 coagulation depurator shells, 31 aeration heads, 32 aeration tubes, 33 Flushing nozzles, 34 mud valves, 35 profile of tooth overflows
Groove.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the present invention, the technical scheme in the present invention is clearly and completely described.
With reference to Fig. 1, Fig. 2 and Fig. 3, the small-sized fine dosing coagulating sedimentation integrated apparatus of the present invention include coagulation depurator and
The coagulation dosing control system being connected with coagulation depurator.
Described coagulation depurator be top be cylinder, bottom be the cone cylindrical container of cone, this container can use anti-
Rotten crashproof stainless steel is made, and bottom is provided with four coagulation depurator supports 25, and coagulation depurator support 25 is provided with
Coagulation depurator castor 26, it is simple to mobile and carrying.Be provided with in coagulation depurator be positioned at cylindrical region coagulating district 17,
Flco Disengagement zone 20 and be positioned at the settling of floccus district 22 of cone area.Be provided with aeration tube 32 in coagulating district 17, water body is led
Stream flap 18, agent mixer 16 and profile of tooth overflow launder 35, coagulation dosing control system is located at top, coagulating district 17, coagulation
Control system for adding drugs includes water inlet pipe 1, intake pump 2, water intaking valve 3, water inlet electromagnetic flowmeter 4, influent turbidity on-line monitoring sensing
Device 6, grug feeding jar 7, enter medicine valve 8, coagulant dosing pump 9, coagulant dosage pipe 10 and industrial computer 11.
When not possessing natural gravity stream condition, utilize intake pump 2 by the former water outside coagulation depurator or stain disease through water inlet
Agent mixer 16 in the continuous suction coagulating district 17 of pipe 1.Coagulating district 17 is propped up by the rustless steel well word bottom it
Frame 21 is fixed in the cylindrical region on coagulation depurator top.Coagulating district 17 is made up of high density polyvinyl-chloride material,
Do waterproof sealing to process, it is ensured that former water or stain disease before and after coagulation the most mutually blend.The flow of intake pump 2 passes through coagulation dosing
The water intaking valve 3 of control system regulates and controls with water inlet electromagnetic flowmeter 4.
Agent mixer 16 is positioned at the middle part in coagulating district 17, including medicament vortex mixer 27 and be located at medicament vortex mixer 27
In coagulant dosage shower nozzle 28, inside agent mixer 16, former water in water inlet pipe 1 or stain disease and coagulant dosage pipe
Coagulant solution pre-configured in 10 is sufficiently mixed.Coagulant dosage shower nozzle 28 bottom is funnel-form, is used for storing coagulation
Agent solution, top is spherical perforated tube, is used for disperseing coagulant solution.Coagulant solution is little from top through funnel from bottom to top
Hole escapes, and uniformly mixes with former water or stain disease.
Coagulating district 17 is internally installed multiple water body water conservancy diversion flap 18 vertically set up, multiple water body water conservancy diversion flaps 18
Between formed flow-guiding channel.Considering for the purpose of ensuring that coagulation efficiency, the spacing of adjacent two blocks of water body water conservancy diversion flaps 18 is not more than 15cm,
Former water or the stain disease time of staying in coagulating district 17 were less than 5 minutes.For guiding former water or stain disease anti-at coagulation
Sequentially flowing in answering district 17, the top and bottom of every block of water body water conservancy diversion flap 18 is all fixed on coagulating district in the way of slot
On the wall of 17.
The bottom in coagulating district 17, the centre position of adjacent two blocks of water body water conservancy diversion flaps 18 two-way perforate is installed with exposure
The aeration head 31 of trachea 32 connection, aeration head 31 have be evenly distributed, aperture that aperture is parallel with water inlet direction.Aeration process
In, gas-water ratio is 5:1～10:1.Aeration tube 32 is connected, by drum with the air compressor 5 being arranged on top, coagulating district 17
Enter air agitation water body, enhanced coagulation agent and the high-efficient contact of pollutant in former water or stain disease；Meanwhile, aeration disturbance is also
The dirt being attached to water body water conservancy diversion flap 18 surface can be destroyed, reduce flco and be deposited in the alluvial bottom coagulating district 17.
Pollutant in former water or stain disease are after abundant coagulation, and the flco mixed liquor of formation passes through 17 liang of coagulating district
The profile of tooth overflow launder 35 of side, flows into flco Disengagement zone 20 and the settling of floccus district 22 of coagulating district 17 both sides external.For guaranteeing
Flco separates and effluent quality, and flco mixed liquor is not less than with the time of staying in flco settling zone 22 in flco Disengagement zone 20
15min。
In flco Disengagement zone 20, the both sides in coagulating district 17 are provided with the flco solid-liquid separation swash plate for reinforced deposition
19 and flco solid-liquid separation assembly 29, granule flco under gravity, carries out solid-liquid through flco solid-liquid separation swash plate 19 and divides
From, flco solid-liquid separation swash plate 19 is arranged above clear liquid, and lower section is solid precipitation.Flco solid-liquid separation swash plate 19 material be plastics or
Fiberglass, is fixed on the wall of coagulation depurator, is in tilted layout, and inclination angle is generally 45 °-60 °, adjacent two pieces of flco solid-liquid separation
Spacing 8-10cm of swash plate 19.
Flco settling zone 22 is provided with sludge bucket 24, and the bottom of sludge bucket 24 is provided with mud valve 34, can periodically pass through gravity
Discharge body refuse.Top, flco settling zone 22, in cylinder and the circular cone junction of coagulation reactor, is provided with flushing line along inwall
23, pipeline has the Flushing nozzle 33 towards cone cylinder inwall, utilizes water inlet to rinse flco settling zone 22, it is clear that discharge is difficult to nature
The body refuse removed.
The both sides external of flco Disengagement zone 20 is provided with outlet pipe 15, and the clear liquid after solid-liquid separation swash plate 19 processes passes through
Mouth of a river filter screen 12 filters further, after intercepting scum silica frost or granule flco, by the outer row of outlet pipe 15.
In During Coagulation Process, throwing in of coagulant is main by the coagulation dosing control system being connected with coagulation depurator
Carry out fine-grained management.As it is shown on figure 3, control system for adding drugs includes grug feeding jar 7, enters medicine valve 8, coagulant dosing pump 9, coagulant
Add pipe 10, industrial computer 11, influent turbidity on-line monitoring sensor 6, delivery turbidity on-line monitoring sensor 13, water inlet electromagnetic current
Gauge 4, water intaking valve 3 and outlet valve 14, coagulation dosing control system is connected with coagulation depurator by circuit.
Industrial computer 11 passes with water inlet electromagnetic flowmeter 4, influent turbidity on-line monitoring sensor 6, delivery turbidity on-line monitoring
Sensor 13 is connected with coagulant dosing pump 9, according to flow of inlet water, influent turbidity, delivery turbidity, by controlling coagulant dosing pump
9 adjust the coagulant charging quantity in agent mixer 16.
Grug feeding jar 7 and industrial computer 11 are positioned at top, coagulating district 17, and the coagulant being pre-configured with in grug feeding jar 7 is (inorganic
Class coagulant such as aluminium polychlorid, organic coagulant such as polyacrylamide etc.) solution by coagulant dosing pump 9, enter medicine valve 8
Enter coagulant blender 16 with coagulant dosage pipe 10, uniformly mix in medicament vortex mixer 27 with the pollutant in water inlet
Close.
Water inlet pipe 1 and outlet pipe 15 are separately installed with influent turbidity on-line monitoring sensor 6 and delivery turbidity on-line monitoring
Sensor 13, it is possible to turbidity change before and after industrial computer 11 feeds back coagulation in real time；It is also equipped with water intaking valve 3 on water inlet pipe 1 and enters
Water power magnetic flowmeter 4, is used for showing and controlling flow of inlet water.
Industrial computer 11 is according to processing flow, the change of Inlet and outlet water turbidity, with reference to " sewage coagulation and coagulating treatment engineering
Specification (HJ 2006-2010) " or the influent turbidity coagulation corresponding with former water or stain disease treating capacity set up according to pre research
Agent dosage scope, automatically adjusts coagulant dosing pump 9, dosage of PAC is increased or decreased, until delivery turbidity reaches predetermined
Process target.In general, the selection of coagulant kind and consumption thereof, should tie according to former water or stain disease coagulation and sedimentation experiment
Fruit or with reference to the operating experience etc. under similar condition of water quality, determine through Integrated comparative.
The above, the only detailed description of the invention of the present invention, but protection scope of the present invention is not limited thereto, and any
Belong to those skilled in the art in the technical scope that the invention discloses, the change that can readily occur in or replacement, all answer
Contain within protection scope of the present invention.Therefore, protection scope of the present invention should be as the criterion with scope of the claims.
Claims (10)
1. a small-sized fine dosing coagulating sedimentation integrated apparatus, including coagulation depurator, coagulation depurator is Upper cylindrical
Body, the cone cylinder shape of lower cone body, be provided with in coagulation depurator and be positioned at the coagulating district (17) of cylindrical region, flco separation
District (20) and be positioned at the flco settling zone (22) of cone area, flco Disengagement zone (20) are positioned at coagulating district (17) outside two
Side, it is characterised in that: also include that the coagulation dosing control system connected with coagulation depurator, coagulating district (17) middle part are provided with
Agent mixer (16), the bottom of coagulating district (17) is provided with the aerator being connected with air compressor (5), coagulating
The both sides, top in district (7) are provided with profile of tooth overflow launder (25), and coagulation dosing control system includes connecting with agent mixer (16)
Water inlet pipe (1), coagulant dosage pipe (10), it is located at the outlet pipe (15) of flco Disengagement zone (20) both sides external, is located at water inlet pipe
(1) water inlet electromagnetic flowmeter (4), influent turbidity on-line monitoring sensor (6) on, it is located at adding on coagulant dosage pipe (10)
Medicinal cupping (7), coagulant dosing pump (9), delivery turbidity on-line monitoring sensor (13) being located on outlet pipe (15) and with enter
The industrial computer (11) that water power magnetic flowmeter (4), influent turbidity on-line monitoring sensor (6), coagulant dosing pump (9) are connected.
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: coagulating district
(17) internally installed have multiple water body water conservancy diversion flap (18) being vertically crisscross arranged, and forms water conservancy diversion between water body water conservancy diversion flap (18)
Passage, guides water inlet sequentially to be flowed in coagulating district (17) by bottom or the top of water body water conservancy diversion flap (18).
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: industrial computer (11) is used
The water inlet recorded in the flow of inlet water recorded according to water inlet electromagnetic flowmeter (4), influent turbidity on-line monitoring sensor (6) is turbid
The delivery turbidity that degree, delivery turbidity on-line monitoring sensor (13) record, mixes by controlling coagulant dosing pump (9) adjustment medicament
Coagulant charging quantity in clutch (16).
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: agent mixer
(16) medicament vortex mixer (27) and the coagulant dosage shower nozzle (28) being located in medicament vortex mixer (27) are included, at agent mixer
(16) internal, former water in water inlet pipe (1) or the stain disease coagulant solution pre-configured with coagulant dosage pipe (10)
Being sufficiently mixed, coagulant dosage shower nozzle (28) bottom is funnel-form, is used for storing coagulant solution, and top is spherical pipe with holes
Road, is used for disperseing coagulant solution, and coagulant solution escapes from top aperture through funnel from bottom to top, equal with former water or stain disease
Even mixing, carries out coagulation subsequently into coagulating district (17).
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: described aerator
Including be located at the aeration tube (32) of bottom in coagulating district (17) and connect with aeration tube (32) be located at adjacent two pieces of water bodys
The aeration head (31) in the centre position of water conservancy diversion flap (18), air compressor (5) is connected with aeration tube (32), is used for blasting air
Agitation water body, enhanced coagulation agent and the high-efficient contact of pollutant.
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: flco Disengagement zone
(20) being provided with flco solid-liquid separation swash plate (19) for reinforced deposition and flco solid-liquid separation assembly (29) in, granule flco exists
Carrying out solid-liquid separation through flco solid-liquid separation swash plate (19) under action of gravity, flco solid-liquid separation swash plate (9) is arranged above clear liquid,
Lower section is solid precipitation.
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 6, it is characterised in that: flco solid-liquid separation
Swash plate (19) material is plastics or fiberglass, is fixed on the wall of coagulation depurator, is in tilted layout, and inclination angle is generally 45 °-60 °,
Spacing 8-10cm of adjacent two pieces of flcos solid-liquid separation swash plate (19).
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: flco settling zone
(22) being provided with sludge bucket (24), the bottom of sludge bucket (24) is provided with mud valve (34), periodically can discharge body refuse, wadding by gravity
Body settling zone (22) top, in cylinder and the cone junction of coagulation reactor, is provided with flushing line (23) along inwall, pipe
Having the Flushing nozzle (33) towards cone cylinder inwall on road, utilize water inlet to rinse flco settling zone (22), it is clear that discharge is difficult to nature
The body refuse removed.
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: on water inlet pipe (1)
It is additionally provided with intake pump (2), water intaking valve (3).
Small-sized fine dosing coagulating sedimentation integrated apparatus the most as claimed in claim 1, it is characterised in that: coagulation depurator
Bottom is provided with four coagulations depurator support (25), and coagulation depurator support (25) is provided with coagulation depurator castor (26),
It is easy to mobile and carrying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610693807.7A CN106315797A (en) | 2016-08-18 | 2016-08-18 | Small fine dosing, coagulating and precipitating integrated device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610693807.7A CN106315797A (en) | 2016-08-18 | 2016-08-18 | Small fine dosing, coagulating and precipitating integrated device |
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| CN117985832A (en) * | 2024-04-02 | 2024-05-07 | 珠江水利委员会珠江水利科学研究院 | Algae water separating station |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3626484C2 (en) * | 1986-08-05 | 1989-11-16 | Passavant-Werke Ag, 6209 Aarbergen, De | |
| CN2502769Y (en) * | 2001-09-07 | 2002-07-31 | 安徽国祯环保节能科技股份有限公司 | Hydraulic automatic stirring coagulating reactor |
| CN101570371A (en) * | 2009-06-12 | 2009-11-04 | 东华大学 | Pretreatment process method and device for removing aniline in wastewater through potassium ferrate |
| CN204910896U (en) * | 2015-07-20 | 2015-12-30 | 郑安犁 | High -efficient incorgruous class of swash plate (pipe) sedimentation tank |
| CN105800755A (en) * | 2016-05-12 | 2016-07-27 | 上海应用技术学院 | Water quality online monitoring system and method of wastewater coagulation treatment unit |
-
2016
- 2016-08-18 CN CN201610693807.7A patent/CN106315797A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3626484C2 (en) * | 1986-08-05 | 1989-11-16 | Passavant-Werke Ag, 6209 Aarbergen, De | |
| CN2502769Y (en) * | 2001-09-07 | 2002-07-31 | 安徽国祯环保节能科技股份有限公司 | Hydraulic automatic stirring coagulating reactor |
| CN101570371A (en) * | 2009-06-12 | 2009-11-04 | 东华大学 | Pretreatment process method and device for removing aniline in wastewater through potassium ferrate |
| CN204910896U (en) * | 2015-07-20 | 2015-12-30 | 郑安犁 | High -efficient incorgruous class of swash plate (pipe) sedimentation tank |
| CN105800755A (en) * | 2016-05-12 | 2016-07-27 | 上海应用技术学院 | Water quality online monitoring system and method of wastewater coagulation treatment unit |
Non-Patent Citations (2)
| Title |
|---|
| 宁夏长城水务有限责任公司: "《上海庙、红墩子能源化工基地供水工程创新与实践》", 31 December 2014, 阳光出版社 * |
| 林少宁等: "《中小型及乡镇纺织印染厂污染防治》", 29 February 1992, 中国环境科学出版社 * |
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| CN115947431A (en) * | 2022-12-31 | 2023-04-11 | 恩格拜（武汉）生态科技有限公司 | Method for rapidly combining flocs by using micro-sand as crystallization nucleus |
| CN117049624A (en) * | 2023-10-12 | 2023-11-14 | 河北中瀚水务有限公司 | Medicine-adding simulation experiment device for water purification plant |
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