CN108128970A - A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater - Google Patents
A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater Download PDFInfo
- Publication number
- CN108128970A CN108128970A CN201711404474.2A CN201711404474A CN108128970A CN 108128970 A CN108128970 A CN 108128970A CN 201711404474 A CN201711404474 A CN 201711404474A CN 108128970 A CN108128970 A CN 108128970A
- Authority
- CN
- China
- Prior art keywords
- pond
- tank
- mediben
- neutralization pond
- containing wastewater
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 54
- IWEDIXLBFLAXBO-UHFFFAOYSA-N dicamba Chemical compound COC1=C(Cl)C=CC(Cl)=C1C(O)=O IWEDIXLBFLAXBO-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 238000011221 initial treatment Methods 0.000 title claims abstract description 15
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 39
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 238000001556 precipitation Methods 0.000 claims abstract description 21
- 230000001105 regulatory effect Effects 0.000 claims abstract description 20
- 230000001112 coagulating effect Effects 0.000 claims abstract description 19
- 238000007872 degassing Methods 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000004065 wastewater treatment Methods 0.000 claims abstract description 5
- 239000002253 acid Substances 0.000 claims description 15
- 239000010802 sludge Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 5
- 238000002425 crystallisation Methods 0.000 abstract description 5
- 230000008025 crystallization Effects 0.000 abstract description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 12
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- 239000000395 magnesium oxide Substances 0.000 description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 4
- 229910052791 calcium Inorganic materials 0.000 description 4
- 239000011575 calcium Substances 0.000 description 4
- 239000003814 drug Substances 0.000 description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 3
- 229910052906 cristobalite Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 230000007935 neutral effect Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- 229910052682 stishovite Inorganic materials 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- 229910052905 tridymite Inorganic materials 0.000 description 3
- 230000003139 buffering effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- PALNZFJYSCMLBK-UHFFFAOYSA-K magnesium;potassium;trichloride;hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[Cl-].[Cl-].[Cl-].[K+] PALNZFJYSCMLBK-UHFFFAOYSA-K 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002699 waste material Substances 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
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
-
- 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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- 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
- C02F1/5263—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using natural chemical 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2866—Particular arrangements for anaerobic reactors
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)
- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
Abstract
The present invention relates to field of waste water treatment, more particularly to a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, including the collecting-tank set gradually along wastewater treatment process, regulating reservoir, reaction tank, neutralization pond, deaerate pond and coagulative precipitation tank, the regulating reservoir is connected by the first connecting tube with reaction tank, agitating device is equipped in the reaction tank and its top is equipped with first charging aperture and second charging aperture, the reaction tank is connected by the second connecting tube with neutralization pond, the side of the neutralization pond is equipped with PH automatons, the neutralization pond, degassing pond is connected with coagulative precipitation tank by third connecting tube with the 4th connecting tube respectively.The present invention is handled one by one by regulating reservoir, reaction tank, neutralization pond, degassing pond and coagulative precipitation tank, completes the pretreatment process of waste water, and cost of investment is low, can strengthen the pretreatment process to high slat-containing wastewater, consequently facilitating the evaporative crystallization work of postorder waste water.
Description
Technical field
The present invention relates to field of waste water treatment, more particularly to a kind of reinforcing for the processing of Mediben high slat-containing wastewater is located in advance
Manage device.
Background technology
High-salt wastewater refers to the waste water of salt content mass fraction at least 1%, this kind of waste water mostly containing high concentration inorganic salts,
Hardly degraded organic substance, heavy metal and SS etc., it is difficult to carry out biological treatment.Bio-refractory organic pollution refers to by micro- life
Speed is very slow when object decomposes, decomposes halfway organic matter again, also includes the metabolite of certain organic matters, this pollutant
Stability is good, and the existing time is long in the environment, can be enriched with by food chain, endanger human health.
High slat-containing wastewater mostlys come from Treatment of Industrial Water counter-infiltration system and generates the life of the enterprises such as concentrate and chemical industry, pharmacy
The high-salt wastewater generated, such as production Mediben can generate a large amount of high-salt wastewater；In addition, the quick hair with China's industry
Exhibition, environmental pollution caused by high salinity waste water difficult to degrade and harm problem are also increasingly severe, directly result in water-mineralizing degree
It significantly improves, accelerates salinization of soil, desertification process, serious negative effect is brought to ecological environment.
With the shortage of water resource, the processing recycling of waste water (high saliferous) is increasingly valued by people, and is given up
The processing recovery utilization rate of water is closely coupled with its pretreatment, if the pretreatment system of waste water is improper, cause waste water hardness,
Silicon, turbidity removal are not thorough, follow-up membranous system, evaporation and crystallization system dirt is caused to block up, fouling it is serious；Film concentration systems cycles of concentration
It is relatively low, increase investment and the operating cost of subsequent evaporation crystal system；The mixing carnallite of evaporation and crystallization system output is without exploitation value
Value, content of organics is higher, can only carry out processing disposition as dangerous waste, expense is high.
Invention content
In view of the above-mentioned deficiencies in the prior art, it is an object of the present invention to provide it is a kind of for Mediben high slat-containing wastewater processing
Strenuous primary treatment device.
To solve the above problems, the present invention provides following technical scheme：
A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, including what is set gradually along wastewater treatment process
Collecting-tank, regulating reservoir, reaction tank, neutralization pond, degassing pond and coagulative precipitation tank, the collecting-tank will by suction pump with regulating reservoir
Waste water in collecting-tank is flow in regulating reservoir, and the regulating reservoir is connected by the first connecting tube with reaction tank, the reaction tank
Interior to be equipped with first charging aperture and second charging aperture equipped with agitating device and its top, the reaction tank is by the second connecting tube in
Be connected with pond, the side of the neutralization pond is equipped with coupled logical PH automatons, the neutralization pond, degassing pond and
Coagulative precipitation tank is connected respectively by third connecting tube with the 4th connecting tube.
Further, the agitating device is included in the first blender and the second blender that are vertically arranged, and described the
One blender and the second blender are symmetrical arranged along the center line of reaction tank, the stirring rod of first blender and the second blender
On be equipped with the paddle of multigroup equidistantly distributed.
Further, the first charging aperture and second charging aperture are set upward in funnel-form and large port.
Further, the PH automatons include the acid feeding machanism that is connected with neutralization pond and with neutralization
The alkaline feeding machanism that pond is connected, the outer wall of the neutralization pond are equipped with controller, acid feeding machanism and alkaline feeding machine
Structure is electrically connected with controller.
Further, the acid feeding machanism includes the first solenoid valve and be connected with first solenoid valve one end first
Metering pump, the outer wall of neutralization pond are equipped with the first feeding pipe being connected with the other end of the first solenoid valve.
Further, the alkaline feeding machanism includes second solenoid valve and be connected with second solenoid valve one end second
Metering pump is additionally provided with the second feeding pipe being connected with the other end of second solenoid valve on the outer wall of neutralization pond.
Further, the side in the degassing pond is equipped with coupled logical air blower.
Further, the side of the coagulative precipitation tank is equipped with coupled logical sludge pump, and coagulative precipitation tank is outer
Wall is equipped with drainpipe.
Advantageous effect：A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater of the present invention, passes through pumping
Waste water in collecting-tank is passed through to regulating reservoir by water pump, and regulating reservoir, into row buffering, ensures anaerobism to the water and water quality of waste water
Stable reaction is run；By being passed through calcium carbonate and magnesia to first charging aperture and second charging aperture respectively, the first blender and
Second stirrer-driven makes waste water come into full contact with calcium carbonate and magnesia to react, effectively remove most of calcium in waste water, magnesium,
SiO2, total alkalinity, suspended matter and partial organic substances；Control acid feeding machanism and alkaline feeding machanism work respectively by controller
Make, waste water is made to keep neutral in neutralization pond, and the first metering pump and the second metering pump can be controlled strictly to neutralization pond and lead to people
Soda acid medicament dosage, prevent the pH value imbalance of waste water from being had an impact to subsequent handling；Exhaust gas is made by air blower work
A small amount of bubble is removed in degassing pond, is fully reacted finally by flocculant PAM is put into coagulative precipitation tank, flco precipitation,
Supernatant is up to standard to discharge from drainpipe, and sludge is handled by sludge pumping to raw sewage processing system, the configuration of the present invention is simple,
Cost of investment is low, can strengthen the pretreatment process to high slat-containing wastewater, consequently facilitating the evaporative crystallization work of postorder waste water.
Description of the drawings
Fig. 1 is the dimensional structure diagram one of the present invention；
Fig. 2 is the dimensional structure diagram two of the present invention；
Fig. 3 is the enlarged drawing at A in Fig. 2；
Fig. 4 is the broken section dimensional structure diagram of the reaction tank of the present invention；
Reference sign：Collecting-tank 1, regulating reservoir 2, reaction tank 3, neutralization pond 4, deaerate pond 5, coagulative precipitation tank 6, suction pump
6a, the first connecting tube 7, agitating device 8, the first blender 8a, the second blender 8b, paddle 8c, first charging aperture 9, second
Feed inlet 10, the second connecting tube 11, third connecting tube 12, the 4th connecting tube 13, acid feeding machanism 14, the first solenoid valve 14a,
First metering pump 14b, alkaline feeding machanism 15, second solenoid valve 15a, the second metering pump 15b, controller 16, air blower 17 are dirty
Dredge pump 18, drainpipe 19.
Specific embodiment
With reference to the accompanying drawings of the specification and embodiment, specific embodiments of the present invention are described in further detail：
Referring to figs. 1 to a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater shown in Fig. 4, including along waste water
Collecting-tank 1, regulating reservoir 2, reaction tank 3, neutralization pond 4, degassing pond 5 and the coagulative precipitation tank 6 that treatment process is set gradually, the collection
Waste water in collecting-tank 1 is flow in regulating reservoir 2 by pond 1 with regulating reservoir 2 by suction pump 6a, and the regulating reservoir 2 passes through first
Connecting tube 7 is connected with reaction tank 3, is equipped with agitating device 8 in the reaction tank 3 and its top is equipped with first charging aperture 9 and the
Two feed inlets 10, the reaction tank 3 are connected by the second connecting tube 11 with neutralization pond 4, the side of the neutralization pond 4 be equipped with
Its PH automaton being connected, the neutralization pond 4, degassing pond 5 and coagulative precipitation tank 6 pass through third connecting tube 12 respectively
It is connected with the 4th connecting tube 13.
Operation principle：Waste water in collecting-tank 1 is passed through to regulating reservoir 2 by the present invention by suction pump 6a, and regulating reservoir 2 is right
The water and water quality of waste water ensure anaerobic reaction stable operation into row buffering；By being fed respectively to first charging aperture 9 and second
Mouth 10 is passed through calcium carbonate and magnesia, and the first blender 8a and the second blender 8b drivings make waste water be filled with calcium carbonate and magnesia
Divide haptoreaction, effectively remove most of calcium, magnesium, SiO2, total alkalinity, suspended matter and partial organic substances in waste water；Pass through control
Device 16 processed controls acid feeding machanism 14 and alkaline feeding machanism 15 to work respectively, and waste water is made to keep neutral in neutralization pond 4, and
First metering pump 14b and the second metering pump 15b can strictly control the dosage for leading to the soda acid medicament of people to neutralization pond 4, prevent from giving up
The pH value imbalance of water has an impact subsequent handling；Exhaust gas is made to remove a small amount of gas in degassing pond 5 by the work of air blower 17
Bubble is fully reacted finally by flocculant PAM is put into coagulative precipitation tank 6, flco precipitation, and supernatant is up to standard from drainpipe 19
Discharge, sludge are sent to raw sewage processing system by sludge pump 18 and are handled, and the configuration of the present invention is simple, cost of investment is low, can
Strengthen the pretreatment process to high slat-containing wastewater, consequently facilitating the evaporative crystallization work of postorder waste water.
The agitating device 8 is included in the first blender 8a and the second blender 8b being vertically arranged, and described first stirs
It mixes device 8a and the second blender 8b is symmetrical arranged along the center line of reaction tank 3, the first blender 8a and the second blender 8b's
The paddle 8c of multigroup equidistantly distributed is equipped on stirring rod, is stirred using the first blender 8a and the second the multigroup of blender 8b
Mix leaf 8c waste water can be made to be come into full contact with calcium carbonate and magnesia and react, effectively remove most of calcium in waste water, magnesium,
SiO2, total alkalinity, suspended matter and partial organic substances, so as to improve working efficiency.
The first charging aperture 9 and second charging aperture 10 are set upward in funnel-form and large port, can control carbonic acid
The pan feeding speed of calcium and magnesia.
The PH automatons include the acid feeding machanism 14 that is connected with neutralization pond 4 and with 4 phase of neutralization pond
The alkaline feeding machanism 15 of connection, the outer wall of the neutralization pond 4 are equipped with controller 16, and acid feeding machanism 14 and alkalinity are fed
Mechanism 15 is electrically connected with controller 16, controls acid feeding machanism 14 and alkaline feeding machanism 15 respectively by controller 16
Work makes waste water keep neutral in neutralization pond 4, and the first metering pump 14b and the second metering pump 15b can be controlled strictly in
Lead to the dosage of the soda acid medicament of people with pond 4, prevent the pH value imbalance of waste water from being had an impact to subsequent handling.
The acidity feeding machanism 14 includes the first solenoid valve 14a and be connected with first solenoid valve 14a one end first
Metering pump 14b, the outer wall of neutralization pond 4 are equipped with the first feeding pipe being connected with the other end of the first solenoid valve 14a, the first meter
Amount pump 14b can strictly control the dosage for leading to the acid medicine of people to neutralization pond 4, prevent the pH value imbalance of waste water to follow-up work
Sequence has an impact.
The alkalinity feeding machanism 15 includes second solenoid valve 15a and be connected with second solenoid valve 15a one end second
Metering pump 15b, is additionally provided with the second feeding pipe being connected with the other end of second solenoid valve 15a on the outer wall of neutralization pond 4, and first
Metering pump 14b can strictly control the dosage for leading to the basic agent of people to neutralization pond 4, prevent the pH value imbalance of waste water to follow-up
Process has an impact.
The side in the degassing pond 5 is equipped with coupled logical air blower 17, makes exhaust gas de- by the work of air blower 17
Gas pond 5 removes a small amount of bubble.
The side of the coagulative precipitation tank 6 is equipped with coupled logical sludge pump 18, and is set on the outer wall of coagulative precipitation tank 6
There is drainpipe 19, fully reacted by putting into flocculant PAM into coagulative precipitation tank 6, flco precipitates, and supernatant is up to standard from draining
Pipe 19 is discharged, and sludge is sent to raw sewage processing system by sludge pump 18 and handled.
The above described is only a preferred embodiment of the present invention, any limit not is made to the technical scope of the present invention
System, therefore any subtle modifications, equivalent variations and modifications that every technical spirit according to the present invention makees above example,
In the range of still falling within technical scheme of the present invention.
Claims (8)
1. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, it is characterised in that：Including along wastewater treatment
The collecting-tank that process is set gradually（1）, regulating reservoir（2）, reaction tank（3）, neutralization pond（4）, degassing pond（5）And coagulative precipitation tank
（6）, the collecting-tank（1）With regulating reservoir（2）Pass through suction pump（6a）By collecting-tank（1）Interior waste water flow to regulating reservoir（2）It is interior,
The regulating reservoir（2）Pass through the first connecting tube（7）With reaction tank（3）It is connected, the reaction tank（3）It is interior to be equipped with agitating device
（8）And its top is equipped with first charging aperture（9）And second charging aperture（10）, the reaction tank（3）Pass through the second connecting tube（11）
With neutralization pond（4）It is connected, the neutralization pond（4）Side be equipped with coupled logical PH automatons, the neutralization
Pond（4）, degassing pond（5）And coagulative precipitation tank（6）Pass through third connecting tube respectively（12）With the 4th connecting tube（13）It is connected.
2. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 1
In：The agitating device（8）Including being in the first blender being vertically arranged（8a）With the second blender（8b）, described first stirs
Mix device（8a）With the second blender（8b）Along reaction tank（3）Center line be symmetrical arranged, first blender（8a）It is stirred with second
Mix device（8b）Stirring rod on be equipped with the paddle of multigroup equidistantly distributed（8c）.
3. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 1
In：The first charging aperture（9）And second charging aperture（10）Set upward in funnel-form and large port.
4. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 1
In：The PH automatons include and neutralization pond（4）The acid feeding machanism being connected（14）With with neutralization pond（4）Phase
The alkaline feeding machanism of connection（15）, the neutralization pond（4）Outer wall be equipped with controller（16）, acid feeding machanism（14）With
Alkaline feeding machanism（15）And controller（16）It is electrically connected.
5. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 4
In：The acidity feeding machanism（14）Including the first solenoid valve（14a）With with the first solenoid valve（14a）One end be connected first
Metering pump（14b）, neutralization pond（4）Outer wall be equipped with and the first solenoid valve（14a）The first feeding pipe for being connected of the other end.
6. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 5
In：The alkalinity feeding machanism（15）Including second solenoid valve（15a）With with second solenoid valve（15a）One end be connected second
Metering pump（15b）, neutralization pond（4）Outer wall on be additionally provided with and second solenoid valve（15a）The second pan feeding for being connected of the other end
Pipe.
7. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 1
In：The degassing pond（5）Side be equipped with coupled logical air blower（17）.
8. a kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater, feature exist according to claim 1
In：The coagulative precipitation tank（6）Side be equipped with coupled logical sludge pump（18）, and coagulative precipitation tank（6）Outer wall on
Equipped with drainpipe（19）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711404474.2A CN108128970A (en) | 2017-12-22 | 2017-12-22 | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711404474.2A CN108128970A (en) | 2017-12-22 | 2017-12-22 | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108128970A true CN108128970A (en) | 2018-06-08 |
Family
ID=62392103
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711404474.2A Pending CN108128970A (en) | 2017-12-22 | 2017-12-22 | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108128970A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101519251A (en) * | 2009-04-09 | 2009-09-02 | 广西大学 | Process for treating bio-refractory waste water by up-flow multi-phase oxidation column |
| CN104841324A (en) * | 2015-04-16 | 2015-08-19 | 泰州润达环保科技有限公司 | Novel double-shaft stirrer |
| CN105523666A (en) * | 2016-01-30 | 2016-04-27 | 内蒙古久科康瑞环保科技有限公司 | Strengthened pretreatment system for high-salt-content industrial wastewater and production process of strengthened pretreatment system |
| CN106186459A (en) * | 2016-08-05 | 2016-12-07 | 苏州他山石环保科技有限公司 | A kind of laboratory waste water integrated equipment for wastewater treatment |
| CN206435129U (en) * | 2016-12-26 | 2017-08-25 | 武平县象洞乡绿色仙草专业合作社 | A kind of sweet High-efficient Stirrer of celestial grass |
| CN206730890U (en) * | 2017-04-21 | 2017-12-12 | 广州邦诚洗涤用品有限公司 | A kind of cleaning solution homogeneous emulsifying machine |
| CN207775025U (en) * | 2017-12-22 | 2018-08-28 | 南京工大环境科技南通有限公司 | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater |
-
2017
- 2017-12-22 CN CN201711404474.2A patent/CN108128970A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101519251A (en) * | 2009-04-09 | 2009-09-02 | 广西大学 | Process for treating bio-refractory waste water by up-flow multi-phase oxidation column |
| CN104841324A (en) * | 2015-04-16 | 2015-08-19 | 泰州润达环保科技有限公司 | Novel double-shaft stirrer |
| CN105523666A (en) * | 2016-01-30 | 2016-04-27 | 内蒙古久科康瑞环保科技有限公司 | Strengthened pretreatment system for high-salt-content industrial wastewater and production process of strengthened pretreatment system |
| CN106186459A (en) * | 2016-08-05 | 2016-12-07 | 苏州他山石环保科技有限公司 | A kind of laboratory waste water integrated equipment for wastewater treatment |
| CN206435129U (en) * | 2016-12-26 | 2017-08-25 | 武平县象洞乡绿色仙草专业合作社 | A kind of sweet High-efficient Stirrer of celestial grass |
| CN206730890U (en) * | 2017-04-21 | 2017-12-12 | 广州邦诚洗涤用品有限公司 | A kind of cleaning solution homogeneous emulsifying machine |
| CN207775025U (en) * | 2017-12-22 | 2018-08-28 | 南京工大环境科技南通有限公司 | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105366839B (en) | The processing unit and processing method of the SS of desulfurization wastewater middle and high concentration, fluoride, sulfate, arsenate and COD are removed simultaneously | |
| CN109851139B (en) | High-salt wastewater softening and concentrating device and method | |
| CN207775025U (en) | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater | |
| CN107285489A (en) | A kind of device and method of desulfurization wastewater pretreatment | |
| CN101684029B (en) | Structure for dyeing and finishing waste water from woolen mill and treatment process | |
| CN106938866A (en) | A kind of desulfurization wastewater resource utilization system and method | |
| CN206279009U (en) | A kind of tiny flocculation combined with hyperfiltration processing unit | |
| CN107265696A (en) | A kind of desulfurization wastewater sofening treatment device and method | |
| CN106315809A (en) | Novel treatment device of wastewater containing sulfate radicals | |
| CN108455773A (en) | A kind of system and method for the industrially desulfurized waste water of processing | |
| CN100408488C (en) | Agent for softening hard water | |
| CN108128970A (en) | A kind of strenuous primary treatment device for the processing of Mediben high slat-containing wastewater | |
| CN207121501U (en) | A kind of hardness removing device suitable for the hard waste water of high magnesium | |
| CN212151731U (en) | Novel upflow coagulation and flocculation device | |
| CN1412128A (en) | Oil field visous crude sewage silicone-removing and cleaning process | |
| CN104692557A (en) | Chemical pretreatment method and device thereof for treating high-salinity wastewater | |
| CN107473340A (en) | A kind of quick Magneto separate sewage disposal system | |
| CN210313691U (en) | Magnetic activated sludge system | |
| CN209065586U (en) | A kind of waste water circulation treating device producing soda ash based on BDO | |
| CN208829517U (en) | A kind of meat processing waste water processing dedicated unit | |
| CN207845426U (en) | Flax poaching wastewater processing system | |
| CN205710180U (en) | A kind of coking wastewater containing phenol and cyanide advanced treatment system | |
| CN206735967U (en) | A kind of desulfurization wastewater resource utilization system | |
| CN206395898U (en) | A kind of coagulation reaction tank dosing multiple spot water distribution system | |
| CN212025013U (en) | Device for reducing sewage hardness |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180608 |