CN106927600A - The integrated sewage treating apparatus of fluoride waste - Google Patents
The integrated sewage treating apparatus of fluoride waste Download PDFInfo
- Publication number
- CN106927600A CN106927600A CN201710255568.1A CN201710255568A CN106927600A CN 106927600 A CN106927600 A CN 106927600A CN 201710255568 A CN201710255568 A CN 201710255568A CN 106927600 A CN106927600 A CN 106927600A
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- Prior art keywords
- pond
- treating apparatus
- control module
- central control
- integrated sewage
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- 239000010865 sewage Substances 0.000 title claims abstract description 47
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 title claims abstract description 29
- 239000002699 waste material Substances 0.000 title claims abstract description 29
- 238000006243 chemical reaction Methods 0.000 claims abstract description 31
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 31
- 230000007246 mechanism Effects 0.000 claims abstract description 30
- 239000003814 drug Substances 0.000 claims abstract description 28
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims description 35
- 229910052731 fluorine Inorganic materials 0.000 claims description 35
- 239000011737 fluorine Substances 0.000 claims description 35
- 239000007788 liquid Substances 0.000 claims description 22
- 239000010802 sludge Substances 0.000 claims description 15
- 230000005611 electricity Effects 0.000 claims description 3
- 229940079593 drug Drugs 0.000 claims description 2
- 230000003472 neutralizing effect Effects 0.000 claims description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 12
- 239000002893 slag Substances 0.000 abstract description 7
- 239000000377 silicon dioxide Substances 0.000 abstract description 6
- 239000006228 supernatant Substances 0.000 abstract description 5
- 239000000523 sample Substances 0.000 abstract description 4
- 238000004062 sedimentation Methods 0.000 abstract description 4
- 238000012544 monitoring process Methods 0.000 abstract description 3
- 238000005189 flocculation Methods 0.000 abstract description 2
- 230000016615 flocculation Effects 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 238000009297 electrocoagulation Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/12—Halogens or halogen-containing compounds
- C02F2101/14—Fluorine or fluorine-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
Landscapes
- Life Sciences & Earth Sciences (AREA)
- 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 present invention discloses a kind of integrated sewage treating apparatus of fluoride waste, and it includes the oil interceptor, dosing reaction tank, neutralization pond, second pond and the central control module that are sequentially connected, and sewage pump is electrically connected with central control module；Skimming plate of the minimum point less than the pool wall peak of oil interceptor is provided with above oil interceptor, during the oil slick and scum silica frost in sewage skimmed into the collection slag bath of side；Dosing reaction tank includes the reaction medicating mechanism that a delivery valve is electrically connected with by central control module with elevator pump, medicament is added fully to be reacted in dosing reaction tank by reacting medicating mechanism, and flocculation separation goes out supernatant, neutralization pond includes the neutralization medicating mechanism that a delivery valve is electrically connected with pH on-line detectors, the pH on-line checkings probe of pH on-line detectors is arranged in neutralization pond, controls to neutralize the switch of medicating mechanism delivery valve by its monitoring result；Detachable inclined tube is finally provided with second pond, carrying out that High-rate sedimentation reaches to sewage can discharge standard.
Description
Technical field
The present invention relates to a kind of sewage-treatment plant, and in particular to a kind of integrated sewage treating apparatus of fluoride waste.
Background technology
With the development of technological innovation, the application field of fluorine-containing electronic chemical product constantly expands, and has penetrated into national economy
With the every field of national defense construction.Fluorine-containing electronic chemical product as fluorine-containing electronic chemical product upstart's ability ground zero, development potentiality
It is huge, there is no high-quality fluorine-containing electronic chemical product to be impossible to produce high performance electronic component, and fluorine-containing electronization
One of problem that the high speed exhibition of product brings is exactly the increasing fluorine-containing electronic chemical product manufacture waste water for urgently processing.
Do not manufacture the ripe scheme of wastewater treatment for fluorine-containing electronic chemical product also in the market, it is existing fluorine-containing useless
Method for treating water mainly has absorption method, electrocoagulation, hyperfiltration, ion-exchange, chemical precipitation method and coagulation sedimentation etc..
In these methods, ion-exchange is costly, and strict to waste water quality requirement；Wherein electrocoagulation and hyperfiltration device are answered
Miscellaneous, power consumption is big, investment and operating cost are high, thus all few use.
The content of the invention
The present invention is directed to the quality of all kinds of methods in the prior art, and the characteristics of combination fluorine-containing electronic chemical product manufacture waste water
It is analyzed, proposes a kind of integrated sewage treating apparatus of fluoride waste.
To reach above-mentioned technical purpose, technical scheme provides a kind of integrated sewage disposal dress of fluoride waste
Put, it includes being sequentially connected the oil interceptor of setting, dosing reaction tank, neutralization pond, second pond and central control module, it is described every
Oil sump, dosing reaction tank, neutralization pond, the delivery port of second pond be arranged at pool wall top, sewage by elevator pump pump to every
In oil sump, the elevator pump is electrically connected with central control module；
A detachable skimming plate, the pool wall of the minimum point less than oil interceptor of the skimming plate are provided with above the oil interceptor
Peak；
The dosing reaction tank includes a reaction medicating mechanism, and the delivery valve of the reaction medicating mechanism is controlled by center
Module is electrically connected with elevator pump；
The neutralization pond includes that one neutralizes medicating mechanism, and the delivery valve of the neutralization medicating mechanism passes through central control module
It is electrically connected with a pH on-line detectors, the pH on-line checkings probe of the pH on-line detectors is arranged in neutralization pond；
Detachable inclined tube is provided with the second pond.
Preferably, the oil interceptor delivery port is set less than pool wall peak.
Preferably, the skimming plate is movably arranged on a guide rail by a sliding block, and the motor of the guide rail is with
Centre control module is electrically connected with.
Preferably, liquid level gauge is provided with the oil interceptor, the liquid level gauge is electrical with elevator pump by central control module
Connection.
Preferably, the dosing reaction tank includes fluorine removal medicament mixing subpool and PAM mixing subpools, is flowed out from oil interceptor
Sewage sequentially pass through fluorine removal medicament mixing subpool, PAM mixing subpools and enter back into dosing reaction tank.
Preferably, the fluorine removal medicament mixing subpool, PAM mixing subpool include that fluorine removal medicament medicating mechanism, PAM add respectively
Medicine mechanism.
Preferably, the fluorine removal medicament medicating mechanism, the delivery valve of PAM medicating mechanisms pass through central control module and carry
Pump is risen to be electrically connected with.
Preferably, be mounted on agitator in the fluorine removal medicament mixing subpool and PAM mixing subpools, the agitator with
Central control module is electrically connected with.
Preferably, the bottom of pond of the dosing reaction tank, neutralization pond and second pond is equipped with sludge hopper, a spoil disposal pipeline
Suction end is respectively protruding into sludge hopper, and the outlet side of the spoil disposal pipeline is stretched out outside pond body, and the height of outlet side is less than pond body
Interior liquid level.
Preferably, the integrated sewage treating apparatus of the fluoride waste also include a storage basin, the spoil disposal pipeline
Outlet side connects storage basin, and the delivery outlet of the storage basin is arranged on bottom of pond, and is connected with sludge suction pump by blow-off line,
The sludge suction pump is electrically connected with central control module.
The integrated sewage treating apparatus of fluoride waste of the present invention, it is provided with removably by oil interceptor
Skimming tool, it is in the oil slick and scum silica frost in sewage skimmed into the collection slag bath of side and anti-in dosing by reacting medicating mechanism
Ying Chizhong adds fluorine removal medicament, PAM fully to be reacted, and flocculation separation goes out supernatant, is finally neutralized in neutralization pond
After adjustment, according to shallow pool principle, the sewage to flowing into second pond carries out High-rate sedimentation so that water outlet reach can discharge standard.
The integrated sewage treating apparatus of fluoride waste of the present invention, simple structure is easy to operate, is suitable to extensive use.
Brief description of the drawings
Fig. 1 is the top view of the integrated sewage treating apparatus of fluoride waste of the present invention；
Fig. 2 is the front view of the integrated sewage treating apparatus of fluoride waste of the present invention；
Fig. 3 is the circuit module control block diagram of the integrated sewage treating apparatus of fluoride waste of the present invention.
Specific embodiment
In order to make the purpose , technical scheme and advantage of the present invention be clearer, it is right below in conjunction with drawings and Examples
The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and
It is not used in the restriction present invention.
The embodiment provides a kind of integrated sewage treating apparatus of fluoride waste, as shown in Figure 1 to Figure 3,
It includes being sequentially connected the oil interceptor 10 of setting, dosing reaction tank 20, neutralization pond 30, second pond 40 and central control module
50, the oil interceptor 10, dosing reaction tank 20, neutralization pond 30, the delivery port of second pond 40 are arranged at pool wall top, and sewage leads to
Cross during elevator pump 60 pumps to oil interceptor 10, the elevator pump 60 is electrically connected with central control module 50.
Liquid level gauge 11 is provided with the oil interceptor 10, the liquid level gauge 11 is by central control module 50 and the electricity of elevator pump 60
Property connection, the liquid level gauge 11 is provided with minimum liquid level and highest liquid level, and the highest liquid level is arranged at the pool wall of oil interceptor 10 most
High point, therefore, when the liquid level in oil interceptor 10 is less than minimum liquid level, the control work of elevator pump 60 of the central control module 50
Make, to sewage is passed through in oil interceptor 10, when the liquid level in oil interceptor 10 reaches minimum liquid level, the central control module 50 is controlled
Elevator pump processed 60 is stopped.
The top of the oil interceptor 10 is provided with a detachable skimming plate 12, and the minimum point of the skimming plate 12 is less than oil interceptor
10 pool wall peak, for skimming the oil slick in sewage level in oil interceptor 10 and scum silica frost；The skimming plate 12 passes through one
Sliding block is movably arranged on a guide rail 13, and motor 14 and the central control module 50 of the guide rail 13 are electrically connected with.It is described
Stroke end of the skimming plate 12 on guide rail 13 is provided with a collection slag bath 70；The collection slag bath 70 is arranged on oil interceptor 10 and is not provided with
The side of delivery port, the delivery port of the oil interceptor 10 is set less than pool wall peak, it is to avoid oil slick scum silica frost is entered by delivery port
In dosing reaction tank 20.
When the liquid level in oil interceptor 10 reaches minimum liquid level, the driving electricity of the control guide rail 13 of the central control module 50
Machine 14 works, and skimming plate 12 carries out skimming under the drive of motor to liquid level, and can be in liquid level in skimming stroke motion
Take up the very low ripples of rising and falling, when skimming plate 12 moves to stroke end, oil slick and scum silica frost crossed under the drive of ripples every
Pool wall between oil sump 10 and collection slag bath 70 is flowed into collection slag bath 70.
The dosing reaction tank 20 includes fluorine removal medicament mixing subpool 21 and PAM mixing subpool 22, is flowed from oil interceptor 10
The sewage for going out sequentially passes through fluorine removal medicament mixing subpool 21, PAM mixing subpool 22 and enters back into dosing reaction tank 20, the fluorine removal medicine
Agent mixing subpool 21, PAM mixing subpool 22 include fluorine removal medicament medicating mechanism 211, PAM medicating mechanisms 221, the fluorine removal respectively
Medicament medicating mechanism 211, PAM medicating mechanisms 221 include medicine-adding bin, dosing pump and chemical feed pipe, the fluorine removal medicament dosing
Mechanism 211, the input port of the chemical feed pipe of PAM medicating mechanisms 221 each lead into fluorine removal medicament mixing subpool 21, PAM mixing subpools
In 22, the switch valve 201 for being arranged at the dosing mouth of pipe is electrically connected with by central control module 50 with elevator pump 60.
Because lifting flow of the elevator pump 60 within the unit interval is fixed, and the dosing mouth of pipe switch valve 201 in list
The dose of output is fixed in the time of position, therefore the central control module 50 determines dirt by monitoring the working time of elevator pump 60
The increased volume of water, so that the accordingly switch time of the switch valve 201 of the control dosing mouth of pipe.Meanwhile, the fluorine removal medicament mixing
The agitator 202 being electrically connected with central control module 50 is mounted in subpool 21 and PAM mixing subpool 22, makes fluorine removal medicament
Sewage in mixing subpool 21 and PAM mixing subpool 22 is sufficiently mixed with medicament.
The sewage enters dosing reaction tank after being sufficiently mixed in fluorine removal medicament mixing subpool 21, PAM mixing subpool 22
In 20, chemical reaction is carried out in dosing reaction tank 20 and separates out supernatant and sludge, the sludge sinks under gravity
Bottom of pond, the supernatant is entered in neutralization pond 30 by top delivery port.
The neutralization pond 30 includes that one neutralizes medicating mechanism 31, during the delivery valve 301 for neutralizing medicating mechanism 31 passes through
Centre control module 50 is electrically connected with a pH on-line detectors 32, and the pH on-line checkings probe of the pH on-line detectors 32 is set
In in neutralization pond 30；The pH value that the pH on-line detectors 32 are popped one's head in real-time monitoring neutralization pond 30 by pH on-line checkings, when
When pH value in neutralization pond 30 is higher than 9, the delivery valve 301 that the control of the central control module 50 neutralizes medicating mechanism 31 is opened,
Until the pH value in pH on-line checking probe monitors neutralization pond 30 is not more than 9, also it is provided with the neutralization pond 30 and is controlled with center
The agitator 202 that molding block 50 is electrically connected with, mixes soda acid more uniform；PH value range in the neutralization pond 30 is preferably
6~9.
Detachable inclined tube 41 is provided with the second pond 40, according to shallow pool principle, the sewage flowed into second pond 40 leads to
Crossing the inclined tube 41 carries out High-rate sedimentation so that the water outlet of second pond 40 reach can discharge standard.
The bottom of pond of the dosing reaction tank 20, neutralization pond 30 and second pond 40 is equipped with sludge hopper 81, described fluorine-containing useless
The integrated sewage treating apparatus of water also include a storage basin 80, and the storage basin 80 is by spoil disposal pipeline 82 and dosing reaction tank
20th, neutralization pond 30 and second pond 40 are connected, and the suction end of the spoil disposal pipeline 82 is respectively protruding into sludge hopper 81, and outlet side is stretched
Go out in storage basin 80, and outlet side is provided with mud valve 83, wherein, the height of the outlet side of the spoil disposal pipeline 82 is anti-less than dosing
The liquid level in pond 20, neutralization pond 30 and second pond 40 is answered, therefore in spoil disposal, the mud valve 83 of discharge pipeline is opened i.e.
Pool bottom sludge can be entered by static pressure and temporarily be stored in storage basin 80；The delivery outlet of the storage basin 80 is arranged on bottom of pond,
And be connected with sludge suction pump 85 by blow-off line 84, the sludge suction pump 85 is electrically connected with central control module 50.
The integrated sewage treating apparatus of fluoride waste of the present invention, it is provided with detachably by oil interceptor 10
Skimming tool, in the oil slick and scum silica frost in sewage skimmed into the collection slag bath 70 of side, and in fluorine removal medicament mixing subpool 21
Fully reacted with dosing in PAM mixing subpool 22, entered in dosing reaction tank 20 by flow by gravity and flocculated, isolate supernatant
Liquid, according to shallow pool principle after finally carrying out neutralization adjustment in neutralization pond 30, the sewage to flowing into second pond 40 is efficiently sunk
Form sediment so that water outlet reach can discharge standard.
Using the integrated sewage treating apparatus of fluoride waste of the present invention, GB is reached after wastewater treatment can be made
18918-2002《Urban wastewater treatment firm pollutant emission standard》One-level A is marked, and fluoride can reach GB8978- in waste discharge
1996《Integrated wastewater discharge standard》Primary standard in table 4.And the integrated sewage treating apparatus of fluoride waste of the present invention
Treatment effect it is excellent, it is stable, can be widely applied to fluorine-containing electronic chemical product manufacture waste water and other fluoride wastes
Treatment.
The specific embodiment of present invention described above, is not intended to limit the scope of the present invention..Any basis
Various other corresponding change and deformation that technology design of the invention is made, should be included in the guarantor of the claims in the present invention
In the range of shield.
Claims (10)
1. a kind of integrated sewage treating apparatus of fluoride waste, it is characterised in that the oil interceptor including being sequentially connected setting
(10), dosing reaction tank (20), neutralization pond (30), second pond (40) and central control module (50), the oil interceptor (10),
Dosing reaction tank (20), neutralization pond (30), the delivery port of second pond (40) are arranged at pool wall top, and sewage passes through elevator pump
(60) pump in oil interceptor (10), the elevator pump (60) is electrically connected with central control module (50)；
A detachable skimming plate (12) is provided with above the oil interceptor (10), the minimum point of the skimming plate (12) is less than oil removal
The pool wall peak in pond (10)；
During the dosing reaction tank (20) includes that a dosing reaction mechanism, the switch valve (201) of the dosing reaction mechanism pass through
Centre control module (50) is electrically connected with elevator pump (60)；
The neutralization pond (30) neutralizes medicating mechanism (31) including one, and the delivery valve (301) for neutralizing medicating mechanism (31) leads to
Cross central control module (50) to be electrically connected with a pH on-line detectors (32), the pH of the pH on-line detectors (32) is examined online
Probing head is arranged in neutralization pond (30)；
Detachable inclined tube (41) is provided with the second pond (40).
2. integrated sewage treating apparatus of fluoride waste according to claim 1, it is characterised in that the oil interceptor (10)
Delivery port is set less than pool wall peak.
3. integrated sewage treating apparatus of fluoride waste according to claim 2, it is characterised in that the skimming plate (12)
It is movably arranged on a guide rail (13) by a sliding block, motor (14) and the central control module (50) of the guide rail (13)
It is electrically connected with.
4. integrated sewage treating apparatus of fluoride waste according to claim 1, it is characterised in that the oil interceptor (10)
Liquid level gauge (11) is inside provided with, the liquid level gauge (11) is electrically connected with by central control module (50) and elevator pump (60).
5. integrated sewage treating apparatus of fluoride waste according to claim 1, it is characterised in that the dosing reaction tank
(20) including fluorine removal medicament mixing subpool (21) and PAM mixing subpool (22), the sewage of outflow is passed through successively from oil interceptor (10)
Cross fluorine removal medicament mixing subpool (21), PAM mixing subpool (22) and enter back into dosing reaction tank (20).
6. integrated sewage treating apparatus of fluoride waste according to claim 5, it is characterised in that the fluorine removal medicament is mixed
Zygote pond (21), PAM mixing subpool (22) include fluorine removal medicament medicating mechanism (211), PAM medicating mechanisms (221) respectively.
7. integrated sewage treating apparatus of fluoride waste according to claim 6, it is characterised in that the fluorine removal medicament adds
Medicine mechanism (211), the switch valve (201) of PAM medicating mechanisms (221) are by central control module (50) and elevator pump (60) electricity
Property connection.
8. integrated sewage treating apparatus of fluoride waste according to claim 6, it is characterised in that the fluorine removal medicament is mixed
Agitator (202), the agitator (202) and center control mould are mounted in zygote pond (21) and PAM mixing subpool (22)
Block (50) is electrically connected with.
9. integrated sewage treating apparatus of fluoride waste according to claim 1, it is characterised in that the dosing reaction tank
(20), the bottom of pond of neutralization pond (30) and second pond (40) is equipped with sludge hopper (81), the suction end point of a spoil disposal pipeline (82)
Do not stretch into sludge hopper (81), the outlet side of the spoil disposal pipeline (82) is stretched out outside pond body, and the height of outlet side is less than pond body
Interior liquid level.
10. integrated sewage treating apparatus of fluoride waste according to claim 9, it is characterised in that the fluoride waste
Integrated sewage treating apparatus also include a storage basin (80), the spoil disposal pipeline (82) outlet side connection storage basin
(80), the delivery outlet of the storage basin (80) is arranged on bottom of pond, and is connected with sludge suction pump (85) by blow-off line (84),
The sludge suction pump (85) is electrically connected with central control module (50).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710255568.1A CN106927600A (en) | 2017-04-19 | 2017-04-19 | The integrated sewage treating apparatus of fluoride waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710255568.1A CN106927600A (en) | 2017-04-19 | 2017-04-19 | The integrated sewage treating apparatus of fluoride waste |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106927600A true CN106927600A (en) | 2017-07-07 |
Family
ID=59436906
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710255568.1A Pending CN106927600A (en) | 2017-04-19 | 2017-04-19 | The integrated sewage treating apparatus of fluoride waste |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106927600A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006055728A (en) * | 2004-08-19 | 2006-03-02 | Matsushita Electric Ind Co Ltd | Method and apparatus for treating fluorine-containing wastewater |
| JP2007209886A (en) * | 2006-02-09 | 2007-08-23 | Bokuto Kasei Kogyo Kk | Fluorine removing agent, and method and apparatus for treating drain containing fluorine using the agent |
| WO2008067723A1 (en) * | 2006-12-05 | 2008-06-12 | Fada Xie | Method and device for treating waste water congtaining fluorine by using limestone |
| CN201424419Y (en) * | 2009-05-18 | 2010-03-17 | 浙江科技学院 | High-concentration fluorine-containing wastewater treatment system |
| CN101875518A (en) * | 2010-07-01 | 2010-11-03 | 陈启松 | Treatment method of stainless steel pickling waste water |
| CN103102027A (en) * | 2013-02-26 | 2013-05-15 | 宏大中源太阳能股份有限公司 | Sewage treatment system and method for solar cell production |
| CN205346900U (en) * | 2016-01-12 | 2016-06-29 | 绍兴鑫杰环保科技有限公司 | Oil separator |
-
2017
- 2017-04-19 CN CN201710255568.1A patent/CN106927600A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006055728A (en) * | 2004-08-19 | 2006-03-02 | Matsushita Electric Ind Co Ltd | Method and apparatus for treating fluorine-containing wastewater |
| JP2007209886A (en) * | 2006-02-09 | 2007-08-23 | Bokuto Kasei Kogyo Kk | Fluorine removing agent, and method and apparatus for treating drain containing fluorine using the agent |
| WO2008067723A1 (en) * | 2006-12-05 | 2008-06-12 | Fada Xie | Method and device for treating waste water congtaining fluorine by using limestone |
| CN201424419Y (en) * | 2009-05-18 | 2010-03-17 | 浙江科技学院 | High-concentration fluorine-containing wastewater treatment system |
| CN101875518A (en) * | 2010-07-01 | 2010-11-03 | 陈启松 | Treatment method of stainless steel pickling waste water |
| CN103102027A (en) * | 2013-02-26 | 2013-05-15 | 宏大中源太阳能股份有限公司 | Sewage treatment system and method for solar cell production |
| CN205346900U (en) * | 2016-01-12 | 2016-06-29 | 绍兴鑫杰环保科技有限公司 | Oil separator |
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Application publication date: 20170707 |
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