CN105330105B - The flocculation integrated device of inorganic-organic microbial - Google Patents
The flocculation integrated device of inorganic-organic microbial Download PDFInfo
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- CN105330105B CN105330105B CN201510733861.5A CN201510733861A CN105330105B CN 105330105 B CN105330105 B CN 105330105B CN 201510733861 A CN201510733861 A CN 201510733861A CN 105330105 B CN105330105 B CN 105330105B
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Abstract
The invention discloses a kind of flocculation integrated device of inorganic-organic microbial, including processing pond, processing pond is separated into first module, second unit and third unit by first partition and second partition；Inlet channel delivery port is located at processing pond top, and pipe-line mixer is provided with inlet channel, and the first drug feeding pipeline is connected with pipe-line mixer；First module is separated into the first settling zone and the first reaction zone by first baffle, and stirring motor is set in the first reaction zone；Second drug feeding pipeline is passed through in the first reaction zone；Second unit is separated into the second settling zone and second reaction zone by the second plate washer；3rd drug feeding pipeline, gas pipeline are passed through in second reaction zone；Drainage pipe is set on the top of second partition, drainage pipe is connected with central tube；Effluent weir is provided with the upper inside wall of third unit；Discharge pipeline is provided with the bottom of processing pond.Sewage is handled using apparatus of the present invention, flocculant synthesis usage amount is reduced, and flocculation efficiency is high, and integrated management is convenient.
Description
Technical field
The present invention relates to a kind of flocculation plant, and in particular to a kind of inorganic-organic-microbial flocculation integrated apparatus, it is dirty
Water is purified by flocculation of the flocculation plant sequentially through inorganic flocculating agent, organic flocculant, microbial flocculant.
Background technology
At present, sewage needs to carry out a series of pre-treatments to carry out biochemical treatment again, and wherein flocculation sediment is common pre-treatment
One of method, used flocculant can be divided into inorganic flocculating agent, organic flocculant and microbial flocculant, inorganic flocculating agent
With organic flocculant individually or compounding use be relatively common method, be used alone inorganic flocculating agent when precipitating sludge amount compared with
Greatly, cost is higher when organic flocculant is used alone, and organic flocculant is macromolecular organic compound, can have one to environment
Fixed pollution, microbial flocculant be one kind as caused by microorganism, can coagulate solid suspended particle not degradable in liquid
Poly-, precipitation special macromolecule metabolite, has efficient, cheap, nontoxic, non-secondary pollution water treatment agent, is typical
Environmentally friendly functional material, either inorganic flocculating agent, organic flocculant or microbial flocculant, usage amount minimizing
It need further to excavate, with cost-effective, in actual applications, shortage considers inorganic flocculating agent, organic flocculant, micro-
The integrated flocculation plant of the respective advantage of biological flocculant.
The content of the invention
Present invention aim to address the deficiencies in the prior art, there is provided a kind of inorganic-organic-microbial flocculation one
Body makeup is put.
The purpose of the present invention is achieved through the following technical solutions：
A kind of inorganic-organic-microbial flocculation integrated apparatus, including processing pond 16, inlet channel 1, for adding nothing
First drug feeding pipeline 3 of machine flocculant, first baffle 4, the second drug feeding pipeline 5 for adding organic flocculant, mixer 6,
First partition 7, the second plate washer 8, the 3rd drug feeding pipeline 9 for adding microbial flocculant, gas pipeline 10, second partition
11st, drainage pipe 12, central tube 13, effluent weir 14, discharge pipeline；The processing pond 16 is divided by first partition 7 and second partition 11
First module 161, second unit 162 and third unit 163 are divided into, the upper end of first partition 7 makes less than edge in processing pond 16
Sewage flow to second unit 162 from upper end of the first module 161 through first partition 7；The delivery port of the inlet channel 1 is arranged on
The top of processing pond 16 makes sewage enter first module 161, and pipe-line mixer 2 is provided with inlet channel 1, and described first adds
Pencil road 5 is connected with the dosing mouth of pipe-line mixer 2, inorganic flocculating agent is mixed into pipe-line mixer 2 in sewage；
First baffle 4 is installed in one unit 161 first module is separated into the first settling zone and the first reaction zone, first baffle 4
Hypomere, which is obliquely installed, to be made the first settling zone bottom narrow to be easy to form sludge collecting region；Mixer 6 is set in the first reaction zone；
Second drug feeding pipeline 5 is passed through in the first reaction zone, and organic flocculant is sufficiently mixed under the agitation of mixer 6 with sewage；
Second plate washer 8 is installed in second unit 162 second unit 162 is separated into the second settling zone and second reaction zone, second
The hypomere of plate washer 8, which is obliquely installed, to be made the second settling zone bottom narrow to be easy to form sludge collecting region；3rd drug feeding pipeline 9,
Gas pipeline 10 is passed through in second reaction zone, and the air in gas pipeline 10 is discharged from the outlet of gas pipeline 10, and generation is stirred
The effect of mixing, complete the mixed process of microbial flocculant and sewage；On the top of the second partition 11, drainage pipe 12 is set,
Drainage pipe 12 is connected with central tube 13, and the sewage of second reaction zone is drained into third unit 163；In the third unit
163 upper inside wall is provided with effluent weir 14；Discharge pipeline is provided with the bottom of the processing pond 16.
Preferably, the height of the first partition 7 is less than the height 20-40cm of processing pond 16, makes sewage in mixer 6
After being sufficiently mixed under agitaion with organic flocculant, second unit is crossed into from the upper end of first partition 7；Described
The height of two dividing plates 11 is identical with the height of processing pond 16.
The first baffle 4, the second plate washer 8 are fixed on the pool wall of processing pond 16, equivalent to the partition wall in processing pond 16.
Preferably, the hypomere of the first baffle 4 is obliquely installed, and from the horizontal by 50 ° of -60 ° of angles, makes the first settling zone
Bottom, which narrows, to be easy to form sludge collecting region.The lower end of first baffle 4 is preferably apart from the bottom plate 60-80cm of processing pond 16
70cm, it is ensured that sewage flow to the first reaction zone from the first settling zone.
Preferably, the hypomere of the second baffle 8 is obliquely installed, and from the horizontal by 50 ° of -60 ° of angles, makes the second settling zone
Bottom, which narrows, to be easy to form sludge collecting region.Preferably, the lower end of second baffle 8 is excellent apart from the bottom plate 60-80cm of processing pond 16
Elect 70cm as, it is ensured that sewage flow to second reaction zone from the second settling zone.
Preferably, the depth that second drug feeding pipeline 5 is passed through processing pond 16 is the half of the height of processing pond 16；Institute
State the 3rd dosing 9 be passed through processing pond 16 depth be the height of processing pond 16 half；The gas outlet of the gas pipeline 10
Air in the bottom plate 80-100cm of processing pond 16, gas pipeline 10 is discharged from the outlet of gas pipeline 10, produces stirring
Effect, while completion microbial flocculant mixes with sewage, additionally it is possible to so that the dissolved oxygen (DO) in sewage is kept
0.5mg/L or so, improve the flocculating effect of microbial flocculant.
Preferably, the height of the drainage pipe 12 is less than the upper end 10cm of first partition 7.
Preferably, cross beam type support is set to be used to stirring motor 6, the cross beam type branch are installed in first reaction zone
Frame is arranged on the upper edge hole of processing pond 16.
Preferably, the discharge pipeline includes the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152, the 3rd spoil disposal branch pipe 153
With spoil disposal house steward 15, it is single that the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152 and the 3rd spoil disposal branch pipe 153 are separately positioned on first
The bottom of member 161, second unit 162 and third unit 163, the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152 and the 3rd row
The mud mouth of mud branch pipe 153 connects with spoil disposal house steward 15.
Use the method for inorganic-organic of the present invention-microbial flocculation integrated apparatus processing sewage：Raw sewage and inorganic wadding
It is transported to after being mixed in solidifying pipe-line mixer 2 of the agent on inlet channel 1 in the first module 161 of processing pond 16, sewage
The flocculation sediment in the first settling zone of first module 161, obtained precipitation are accumulated in the first settling zone bottom；Sewage enters the
One reaction zone, toward the first reaction zone in be passed through organic flocculant, under the agitation of mixer 6, sewage mixes with organic flocculant,
Upper end of the mixed sewage through first partition 7 enters second unit 162, in the second settling zone flocculation sediment, obtained precipitation
It is accumulated in the second settling zone bottom；Sewage enters second reaction zone, toward second reaction zone in be passed through microbial flocculant and air,
Sewage mixes with microbial flocculant in air stirring effect；Sewage mixed with microbial flocculant after through drainage pipe 12 and in
Heart pipe 13 enters third unit 163 and carries out flocculation sediment, and the supernatant after precipitation is discharged through effluent weir 14, and precipitation is accumulated in the 3rd
The bottom of unit 163；Processing is accumulated in by inorganic flocculating agent, organic flocculant and the microbial flocculant precipitation to be formed of flocculating
Sludge is formed on the bottom of pond 16, is discharged through spoil disposal pipeline.
Beneficial effects of the present invention：
It using inorganic-organic of the present invention-microbial flocculation integrated apparatus processing sewage, can use flocculant synthesis
Amount is reduced, and flocculation efficiency is high, and integrated management is convenient, reduces duct length, reduces hydraulic loss, reduces energy consumption；Respectively
Only rely on dividing plate separation between unit, it is co-walled and build, when separate unit is connected compared with, saved about 27.6% and built pond material
Material, shortens flow, and effectively reduces the loss of flood peak caused by the pipeline of connection separate unit, avoids addition wadding
Sewage after solidifying agent precipitates the possibility of caused line clogging in conveyance conduit, and is stirred in third unit using air
Mix, not only acted as immixture, and dissolved oxygen in sewage is improved microbial flocculant in 0.5mg/L or so
Activity and its flocculating effect.
Inorganic-organic of the present invention-microbial flocculation integrated apparatus is formed higher than drainage pipe due to first partition upper end
Depth displacement the reason for, the water surface can be caused gradually to reduce from left to right, form natural-drop phenomenon, it is single that sewage sequentially flows through first
Member, second unit and third unit, so, sewage are made by the flocculation of inorganic flocculating agent, organic flocculant, microbial flocculant
With the material such as suspended particulate substance SS, COD in sewage obtains most of removal, special for the flocculating effect of livestock breeding wastewater
It is unobvious.
Brief description of the drawings
Fig. 1 is the structural representation of inorganic-organic of the present invention-microbial flocculation integrated apparatus.
In Fig. 1,1- inlet channels, 2- pipe-line mixers, the drug feeding pipelines of 3- first, 4- first baffles, the chemical feed pipes of 5- second
Road, 6- mixers, 7- first partitions, the plate washers of 8- second, the drug feeding pipelines of 9- the 3rd, 10- gas pipelines, 11- second partitions, 12-
Drainage pipe, 13- central tubes, 14- effluent weirs, 15- spoil disposal house stewards, 151- the first spoil disposal branch pipes, 152- the second spoil disposal branch pipes,
The spoil disposal branch pipes of 153- the 3rd, 16- processing ponds, 161- first modules, 162- second units, 163- third units.
Embodiment
Technical scheme is described further with reference to the accompanying drawings and detailed description.
As shown in figure 1, a kind of inorganic-organic-microbial flocculation integrated apparatus, including processing pond 16, inlet channel 1,
For adding the first drug feeding pipeline 3, first baffle 4, the second drug feeding pipeline for adding organic flocculant of inorganic flocculating agent
5th, mixer 6, first partition 7, the second plate washer 8, the 3rd drug feeding pipeline 9 for adding biological flocculant, gas pipeline 10,
Two dividing plates 11, drainage pipe 12, central tube 13, effluent weir 14, discharge pipeline；The processing pond 16 by first partition 7 and second every
Plate 11 is separated into first module 161, second unit 162 and third unit 163；The delivery port of the inlet channel 1 is arranged on place
The top in reason pond 16 makes sewage enter first module 161, and pipe-line mixer 2, first dosing are provided with inlet channel 1
Pipeline 5 is connected with the dosing mouth of pipe-line mixer 2, inorganic flocculating agent is mixed into pipe-line mixer 2 in sewage；First
First baffle 4 is installed in unit 161 first module is separated into the first settling zone and the first reaction zone, under first baffle 4
Section is obliquely installed, and from the horizontal by 50 ° of -60 ° of angles, the first settling zone bottom is narrowed and is easy to form sludge collecting region；
Mixer 6 is set in one reaction zone；Second drug feeding pipeline 5 is passed through in the first reaction zone, and organic flocculant is in mixer 6
Agitation is lower to be sufficiently mixed with sewage；Second plate washer 8 is installed in second unit 162 second unit 162 is separated into second and sunk
Shallow lake area and second reaction zone, the hypomere of the second plate washer 8 are obliquely installed, and from the horizontal by 50 ° of -60 ° of angles, are made under the second settling zone
Portion, which narrows, to be easy to form sludge collecting region；3rd drug feeding pipeline 9, gas pipeline 10 are passed through in second reaction zone, appendix
Air in road 10 is discharged from the outlet of gas pipeline 10, produces stirring action, completes the mixed of microbial flocculant and sewage
Conjunction process；Drainage pipe 12 is set on the top of the second partition 11, drainage pipe 12 is connected with central tube 13, anti-by second
The sewage in area is answered to be drained to third unit 163；The upper inside wall of the third unit 163 is provided with effluent weir 14；Described
The bottom of processing pond 16 is provided with discharge pipeline.
Cross beam type support is set to be used to stirring motor 6, the cross beam type support installation are installed in first reaction zone
On the upper edge hole of processing pond 16.
It is total that the discharge pipeline includes the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152, the 3rd spoil disposal branch pipe 153 and spoil disposal
Pipe 15, the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152 and the 3rd spoil disposal branch pipe 153 are separately positioned on first module 161,
The bottom of two units 162 and third unit 163, the first spoil disposal branch pipe 151, the second spoil disposal branch pipe 152 and the 3rd spoil disposal branch pipe 153
Mud mouth connected with spoil disposal house steward 15.
The height of the first partition 7 is less than the height 20-40cm of processing pond 16；The height of described second partition 11 and
The height of processing pond 16 is identical.
The first baffle 4, the second plate washer 8 are fixed on the pool wall of processing pond 16, equivalent to the partition wall in processing pond 16.
The depth that second drug feeding pipeline 5 is passed through processing pond 16 is the half of the height of processing pond 16；Described 3rd
The depth that dosing 9 is passed through processing pond 16 is the half of the height of processing pond 16；At the gas outlet distance of the gas pipeline 10
The bottom plate 80-100cm of pond 16 is managed, the air in gas pipeline 10 is discharged from the outlet of gas pipeline 10, produces stirring action,
While completion microbial flocculant mixes with sewage, additionally it is possible to so that the dissolved oxygen (DO) in sewage keeps 0.5mg/L or so,
Improve the flocculating effect of microbial flocculant.
The height of the drainage pipe 12 is less than the upper end 10cm of first partition 7.
In the present embodiment, the long 4.5m of processing pond 16, wide 1.5m, high 2m, first partition 7 and second partition 11 are in length side
To according to 2：2：Processing pond is separated into three units by 1.
The hypomere of the first baffle 4 is obliquely installed, from the horizontal by 55 ° of angles；At the lower end distance of first baffle 4
Manage the bottom plate 70cm of pond 16；The hypomere of second plate washer 8 is obliquely installed, from the horizontal by 55 ° of angles；Under the second baffle 8
End is apart from the bottom plate 70cm of processing pond 16；The height of the first partition 7 is less than the height 20cm of processing pond 16；The gas pipeline
10 gas outlet is apart from the bottom plate 80cm of processing pond 16.
Use the method for the present embodiment inorganic-organic-microbial flocculation integrated apparatus processing sewage：Raw sewage and inorganic
Flocculant is transported in the first module 161 of processing pond 16 after being mixed in the pipe-line mixer 2 on inlet channel 1, dirty
Water flocculation sediment in the first settling zone of first module 161, obtained precipitation are accumulated in the first settling zone bottom；Sewage enters
First reaction zone, toward the first reaction zone in be passed through organic flocculant, under the agitation of mixer 6, sewage mixes with organic flocculant
Close, mixed sewage enters second unit 162 through the upper end of first partition 7, in the second settling zone flocculation sediment, obtained precipitation
It is accumulated in the second settling zone bottom；Sewage enters second reaction zone, toward second reaction zone in be passed through microbial flocculant and air,
Sewage mixes with microbial flocculant in air stirring effect；Sewage mixed with microbial flocculant after through drainage pipe 12 and in
Heart pipe 13 enters third unit 163 and carries out flocculation sediment, and the supernatant after precipitation is discharged through effluent weir 14, and precipitation is accumulated in the 3rd
The bottom of unit 163；Processing is accumulated in by inorganic flocculating agent, organic flocculant and the microbial flocculant precipitation to be formed of flocculating
Sludge is formed on the bottom of pond 16, is discharged through spoil disposal pipeline.
The physical dimension for three units being separated according to the present embodiment integrated apparatus dividing plate, make three flocculations
Sedimentation basin (is followed successively by inorganic flocculation sedimentation tank, organic-flocculation sedimentation basin, microbial flocculation sedimentation basin), and with pipeline coordinator
Body formula device.The integrated apparatus provided using the present embodiment, certain pig breeding farm is handled after big debris is fallen in grid interception
Sewage, handle sewage quantity 1t/h, add inorganic flocculating agent PAC20g, organic flocculant PAM2.5g and micro- life in sewage per ton
Thing flocculant 20L is (using the SKHZYE-RBW1000 microorganisms wadding of Borrow Di Muhan (Weifang) bio tech ltd production
Solidifying microbial inoculum, similarly hereinafter), the content of main component in water before and after the processing is investigated, as shown in table 1.And use the nothing in two part arrangement
Machine flocculation sedimentation tank individually handles same amount of sewage, it is necessary to which feeding machine flocculant PAC360g can just make water outlet reach similar
Effect；Same amount of sewage is individually handled, it is necessary to add organic flocculant using the organic-flocculation sedimentation basin in two part arrangement
PAM15g just can make water outlet reach similar effect；There is microbial flocculation sedimentation basin individually to handle phase using in two part arrangement
The sewage of same amount just can make water outlet reach similar effect, it is necessary to add microbial flocculant 100L.
The content of main component before and after certain the pig breeding farm waste water flocculating of table 1
Using foregoing two part arrangement and integrated apparatus, locate respectively according to the method for handling certain pig breeding farm waste water
Manage the sewage after certain dairy cow farm intercepts big debris through grid.The integrated apparatus provided using the present embodiment, processing
Sewage quantity 1t/h, inorganic flocculating agent PAC20g, organic flocculant PAM2.5g and microbial flocculant 20L are added in sewage per ton,
The content of main component in water before and after the processing is investigated, as shown in table 2.And use the inorganic flocculation sedimentation tank list in two part arrangement
The same amount of sewage of reason of staying alone is, it is necessary to which feeding machine flocculant PAC360g just can make water outlet reach similar effect；Using split type
Organic-flocculation sedimentation basin in device individually handles same amount of sewage, it is necessary to which water outlet can just be made by adding organic flocculant PAM15g
Reach similar effect；Using in two part arrangement there is microbial flocculation sedimentation basin individually to handle same amount of sewage, it is necessary to
Adding microbial flocculant 100L just can make water outlet reach similar effect.
The content of main component before and after certain the dairy cow farm waste water flocculating of table 2
From Tables 1 and 2, the present embodiment integration flocculation plant and two part arrangement are directed to the wadding of livestock breeding wastewater
Solidifying effect is all obvious, almost without significant difference.Required comprehensive throwing when simultaneously using inorganic, organic, biological flocculant
Dosage will be considerably less than only the amount added during using a certain flocculant.In above-mentioned two application examples, run one week and found that
There is sediment in connecting pipe between split type each pond, be exactly after being mixed with flocculant in sewage, flow velocity in the duct is not
It is sufficiently large, cause the suspended particulate substance that sewage flocculation gets off to be deposited on caused by bottom of pond.And in practical engineering application, if using
Two part arrangement, built due to not co-walled, pond material increase by 27.6% is built compared with integrated apparatus；Between three units
Connecting pipe is up to tens of rice, and the 3rd pond is then flowed into order to ensure that sewage sequentially can flow to the second pond from the first pond, each pond it
Between must assure that certain depth displacement, typically at least more than 20cm, cause the loss of flood peak increase more than 40cm；It is in addition, split type
Device prevents that in order to which sludge deposits in connecting pipe the flow velocity general control of sewage is in more than 5m/s, sewage in pipeline
Inevitable consumed energy is flowed in the duct, increases operation energy consumption.
Part that the present invention does not relate to is same as the prior art or can be realized using prior art.
Above is technical solution of the present invention is described in further detail in conjunction with specific embodiments, but it is not of the invention
Limitation.Essence that every foundation is originally put and any simple modification is made to above example, still fall within the solution of the present invention
Scope.
Claims (8)
1. a kind of inorganic-organic-microbial flocculation integrated apparatus, it is characterised in that including processing pond (16), inlet channel
(1), for add the first drug feeding pipeline (3) of inorganic flocculating agent, first baffle (4), for add organic flocculant second
Drug feeding pipeline (5), mixer (6), first partition (7), the second plate washer (8), the 3rd chemical feed pipe for adding biological flocculant
Road (9), gas pipeline (10), second partition (11), drainage pipe (12), central tube (13), effluent weir (14), discharge pipeline；Institute
State processing pond (16) and first module (161), second unit (162) and are separated into by first partition (7) and second partition (11)
Unit three (163), first partition (7) upper end make sewage from first module (161) through first less than edge in processing pond (16)
The upper end of dividing plate (7) flow to second unit (162), the height of described second partition (11) and the height phase of processing pond (16)
Together；The top that the delivery port of the inlet channel (1) is arranged on processing pond (16) makes sewage enter first module (161), is entering
Pipe-line mixer (2) is installed, first drug feeding pipeline (3) and the dosing mouth of pipe-line mixer (2) connect on waterpipe (1)
Connect, inorganic flocculating agent is mixed into pipe-line mixer (2) in sewage；First baffle is installed in first module (161)
(4) first module is separated into the first settling zone and the first reaction zone, the hypomere of first baffle (4), which is obliquely installed, makes the first precipitation
Area bottom, which narrows, to be easy to form sludge collecting region；Mixer (6) is set in the first reaction zone；Second drug feeding pipeline (5)
It is passed through in the first reaction zone, organic flocculant is sufficiently mixed under the agitation of mixer (6) with sewage；In second unit (162)
Second plate washer (8) is inside installed second unit (162) is separated into the second settling zone and second reaction zone, the second plate washer (8)
Hypomere, which is obliquely installed, to be made the second settling zone bottom narrow to be easy to form sludge collecting region；3rd drug feeding pipeline (9), appendix
Road (10) is passed through in second reaction zone, and the air in gas pipeline (10) is discharged from the outlet of gas pipeline (10)；Described
The top of second partition (11) sets drainage pipe (12), and drainage pipe (12) is connected with central tube (13), the drainage pipe
(12) height is less than first partition (7) upper end 10cm, and the sewage of second reaction zone is drained into third unit (163)；Institute
The upper inside wall for stating third unit (163) is provided with effluent weir (14)；Discharge pipeline is provided with the bottom of the processing pond (16).
2. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that described first every
The height of plate (7) is less than the height 20-40cm of processing pond (16).
3. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that the first gear
The hypomere of plate (4) is obliquely installed, from the horizontal by 50 ° of -60 ° of angles；First baffle (4) lower end is apart from processing pond (16) bottom
Plate 60-80cm；
The hypomere of the second baffle (8) is obliquely installed, from the horizontal by 50 ° of -60 ° of angles；Second baffle (8) lower end away from
From processing pond (16) bottom 60-80cm.
4. inorganic-organic according to claim 3-microbial flocculation integrated apparatus, it is characterised in that the first gear
Plate (4) lower end is apart from processing pond (16) bottom plate 70cm；
Second baffle (8) lower end is apart from processing pond (16) bottom plate 70cm.
5. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that described second adds
The depth that pencil road (5) is passed through processing pond (16) is the half of processing pond (16) height；3rd drug feeding pipeline (9)
The depth for being passed through processing pond (16) is the half of processing pond (16) height.
6. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that the appendix
The gas outlet in road (10) is apart from processing pond (16) bottom plate 80-100cm.
7. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that described first
Cross beam type support is set to be used to mixer (6) be installed in reaction zone, the cross beam type support is arranged on the upper edge of processing pond (16)
On mouth.
8. inorganic-organic according to claim 1-microbial flocculation integrated apparatus, it is characterised in that the discharge pipeline
Including the first spoil disposal branch pipe (151), the second spoil disposal branch pipe (152), the 3rd spoil disposal branch pipe (153) and spoil disposal house steward (15), first
Spoil disposal branch pipe (151), the second spoil disposal branch pipe (152) and the 3rd spoil disposal branch pipe (153) are separately positioned on first module (161),
The bottom of Unit two (162) and third unit (163), the first spoil disposal branch pipe (151), the second spoil disposal branch pipe (152) and the 3rd row
The mud mouth of mud branch pipe (153) connects with spoil disposal house steward (15).
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| CN1412133A (en) * | 2001-10-15 | 2003-04-23 | 中国市政工程华北设计研究院 | Air-stirring sludge-refluxing chemical flocculation precipitation sewage treatment method |
| JP2005177602A (en) * | 2003-12-19 | 2005-07-07 | Ebara Corp | Method of mixing flocculant, mixing vessel and method and apparatus for treating rain-water-including sewage using the mixing method and vessel |
| CN101012079A (en) * | 2007-01-25 | 2007-08-08 | 天津长芦海晶集团有限公司 | Natural organism coagulant aid and preparing method theroef |
| CN101973653A (en) * | 2010-09-30 | 2011-02-16 | 南京大学 | Method for treating high-concentration PAM (Polyacrylamide) production wastewater by using composite coagulation method |
| CN102329021A (en) * | 2011-08-10 | 2012-01-25 | 戴群 | High-eutrophication water advanced purification treatment method and device |
| CN103755006A (en) * | 2014-01-17 | 2014-04-30 | 上海交通大学 | Integrated heterogeneous baffled Fenton continuous reactor |
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