CN108911414A - A kind of processing system of industry copper-containing wastewater - Google Patents
A kind of processing system of industry copper-containing wastewater Download PDFInfo
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- CN108911414A CN108911414A CN201810889806.9A CN201810889806A CN108911414A CN 108911414 A CN108911414 A CN 108911414A CN 201810889806 A CN201810889806 A CN 201810889806A CN 108911414 A CN108911414 A CN 108911414A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/14—NH3-N
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
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- 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)
- Water Treatment By Sorption (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses a kind of processing systems of industrial copper-containing wastewater, which includes setting pot, conditioning tank, multiple copper-stripping reaction pond, filtering ponds, MBR system, residue pool, tank.The multiple copper-stripping reaction pond of this system is original creation design, physical technology is used completely, diatomite is nontoxic, with unique pore structure, weight is light and soft, and porosity is big, absorption property is strong, the most of organic substance and copper ion that are right can be absorbed, unique baffle design allows the contact area of diatomite and water to increase again, increases treatment effeciency.
Description
Technical field
A kind of processing system of industrial copper-containing wastewater of the present invention, belongs to the field of waste water treatment in environmental protection.
Background technique
Diatomite is the accumulational stage after being referred to as the one-celled plants death of diatom by 1 to 20,000 year or so, is formed
A kind of fossil diatom cumulose soil mineral deposit.Diatom is one of the protist occurred on earth earliest, is survived in seawater
Or in lake water.This diatomite is formed by the remains deposition of unicellular water plant diatom, the uniqueness of this diatom
The free silica in water can be absorb and form its anatomy, deposit after its end of life, formed under certain geological conditions
Diatomite Deposit.It has some unique performances, such as：Porosity, lower density, biggish specific surface area, it is opposite not
Compressibility and chemical stability change by manufacturing procedures such as crushing, sorting, calcining, air current classifying, impurity eliminations to original soil
After the distribution and surface nature of its granularity, it is applicable to a variety of industrial requirements such as paint of coating additive.
Using diatomite：PH value is neutral, nontoxic, and suspendability is good, and absorption property is strong, and bulk density is light, oil absorbency 115%, fineness
In 325 mesh --- 500 mesh, mixing uniformity is good, and when use will not block agricultural machinery pipeline, can play moisturizing, loose in the soil
Soil property extends drug effect fertilizer efficiency time, encourages crop growth effect.Compound fertilizer industry：The various farmings such as fruit tree, vegetables, flowers and plants
The compound fertilizer of object.Using diatomite advantage：Absorption property is strong, bulk density is light, and fineness is uniform, and pH value neutrality is nontoxic, mixing uniformity
It is good.Diatomite can become concentrated fertilizer, promote crop growth, improvement soil etc. effect.Rubber industry：Vehicle tyre,
Filler in the various rubber products such as rubber tube, V belt, rubber rolling, conveyer belt, automatic foot-mat.It is excellent using diatomite
Point：The rigidity and intensity of product can be remarkably reinforced, settling volume up to 95%, and can be improved product it is heat-resisting, wear-resisting, heat preservation, it is anti-ageing
The performance of the chemical actions such as change.Building heat preservation industry：Thermal-insulating roof, insulating brick, calcium-silicate thermal insulation material, porosity honey comb briquet stove,
The heat preservation such as sound-insulating fireproof decoration plate, heat-insulated, soundproof construction composition, wall sound isolation decoration board, floor tile, ceramic etc..
Summary of the invention
To solve the deficiencies in the prior art, the present invention provides a kind of processing systems of industrial copper-containing wastewater, should
System includes setting pot, conditioning tank, multiple copper-stripping reaction pond, filtering ponds, MBR system, residue pool, tank etc.；Wherein, it comes from
Copper-containing wastewater in industrial processes is discharged into the water inlet of setting pot by pipeline connection, and the water outlet of setting pot passes through pipeline
The water inlet of conditioning tank is connected, the water outlet of conditioning tank connects the water inlet in multiple copper-stripping reaction pond, multiple copper removal by pipeline
The water outlet of reaction tank connects the water inlet of filtering ponds by pipeline, and the water outlet of filtering ponds connects MBR system by pipeline
Water inlet, the water outlet of MBR system connect the water inlet of tank by pipeline, and the water outlet of tank connects discharge tube,
The backwash water outlet in multiple copper-stripping reaction pond connects the backwashing water entrance of setting pot by pipeline, and the slag notch of setting pot is logical
The first of piping connection residue pool enters cinder notch, and the slag notch in multiple copper-stripping reaction pond enters by the second of pipeline connection residue pool
The slag notch of cinder notch, filtering ponds enters cinder notch by the third that pipeline connects residue pool, and the reuse mouth of tank is connected by pipeline
The backwash water inlet in multiple copper-stripping reaction pond；Wherein, multiple copper-stripping reaction pond includes absorption region, recovery zone, magnetized area
Domain, purification region, buffer area, back washing area；Absorption region interior walls two sides are covered with baffle, are spaced between baffle
5cm, baffle have 5 kinds of angles, and the baffle for being located at absorption region bottom to 1/5th height is parallel to the horizontal plane, five/
The baffle and horizontal sextant angle of 2/1 to five height are 30 °, the baffle and level of 3/2nds to five/5ths height
Angle is 45 °, and the baffle and horizontal sextant angle of 4/3rds to five/5ths height are 60 °, and 4/5ths to region top inhale
Plate and horizontal vertical are received, diatomite is housed on baffle；One group of tilted slot, the inclined-plane and ground of tilted slot are installed in recovery zone
Angle is 60 °, and mud retaining plate is uniformly provided on tilted slot, is spaced 10cm, mud retaining plate height 5cm, perpendicular to the ground, every group of mud retaining plate
Under be designed with leakage cinder notch, leak cinder notch diameter 0.3cm, tilted slot bottom is equipped with slag receiving trough, and slag receiving trough passes through Residue extraction pipeline connection
Slag notch, slag notch are located in pool bottom；Magnetized area middle position is equipped with electromagnetic system, in magnetized area and purification region
Junction be equipped with connection door；It purifies filling magnetic fillers, filler in region and enters with region contour at water, filler is Polymer Magnetic
Property rubber ball body, partial size is respectively 0.5cm, 0.25cm, 0.1cm, and 0.5cm partial size filler accounts for Domain Volume in sections bottom
50%, 0.25cm partial size filler portion in the zone, account for 35%, the 0.1cm partial size filler of Domain Volume in the top in region, occupied area domain
The 15% of volume, region top are equipped with backwash water outlet, are equipped between purification region and buffer area and connect door；Buffer area
It is interior to be equipped with strong magnets group；The bottom of equipment is arranged in back washing area, and there are backwash water inlets in left side.
Wherein, the baffle in multiple copper-stripping reaction pond is bamboo material, and with a thickness of 2cm, the positive and negative two sides of baffle, which are provided with, is deposited
Put slot, groove depth 0.5cm is uniformly laid with diatomite in slot, is highly 0.4cm, diatomite is fixed on gauze and metal screen
In slot.
Wherein, the leakage cinder notch of the mud retaining plate in multiple copper-stripping reaction pond is designed with switching device, can open and close simultaneously, leakage
There is hose to be connected to slag receiving trough under cinder notch.
Wherein, connection Men Junke is turned on or off by remotely control everywhere.
Wherein, a length of 30min when setting pot is stood；Bottom is equipped with automatic Slag Scraping Device in setting pot；PH is controlled in conditioning tank
For 6.5-7.5, adjusting solvent is sodium hydroxide and dilute sulfuric acid.
The advantage of the invention is that：
（1）This system is completely adapted to the processing of various types of industrial copper-containing wastewaters, can reach the discharge of wastewater mark of country
Standard meets environmental requirement.
（2）The concentration treatment effeciency of copper and every pollutant in waste water is high, and the treatment effeciency of copper reaches in water
99.9%, COD treatment effeciency is up to 99.3% or more, and the treatment effeciency of ammonia nitrogen is up to 99.3% or more, the place of suspended matter
Efficiency is managed up to 99.6% or more, effluent quality is without obvious coloration, the visible specification table 1 of specific data, table 2.
（3）The multiple copper-stripping reaction pond of this system is original creation design, uses physical technology completely, and diatomite is nontoxic, is had only
Special pore structure, weight is light and soft, and porosity is big, and absorption property is strong, can by the most of organic substance being right and copper from
Son absorbs, and unique baffle design allows the contact area of diatomite and water to increase again, increases treatment effeciency.
（4）Total system the Automation Design, key processing, without waiting, uses material natural environmental-protective, low energy, physics
Processing, reduces the addition of chemical substance, avoids secondary pollution.
Detailed description of the invention
Fig. 1 is equipment schematic diagram of the invention.
In figure：The multiple copper-stripping reaction pond 1- setting pot, 2- conditioning tank, 3-, 4- filtering ponds, 5-MBR system, 6- residue pool,
7- tank
Fig. 2 is the schematic diagram in multiple copper-stripping reaction pond.
In figure：The absorption region 31-, the recovery zone 32-, 33- magnetized area, 34- purify region, the buffer area 35-, 36-
Back washing area, 37- baffle, 38- tilted slot, 39- mud retaining plate, 310- leakage cinder notch, 311- slag receiving trough, 312- connection door,
313- magnetic fillers, 314- strong magnets, 315- water outlet, 316- water inlet, 317- backwash water inlet, 318- recoil wash out
The mouth of a river, 319- electromagnetic system, 320- slag notch.
Specific embodiment
A kind of processing system of industrial copper-containing wastewater as shown in Figure 1, which includes setting pot 1, conditioning tank 2, multiple
Copper-stripping reaction pond 3, filtering ponds 4, MBR system 5, residue pool 6, tank 7；Wherein：Cupric in industrial processes is useless
Water is discharged into the water inlet of setting pot 1 by pipeline connection, and waste water is in setting pot 1 by impurity such as the soil generated in production process
It is discharged in water here, sand setting, 1 a length of 30min when standing；Bottom is equipped with automatic Slag Scraping Device in detritus tank.The water outlet of setting pot 1
Mouth connects the water inlet of conditioning tank 2 by pipeline, and the pH of control waste water is 6.5-7.5 in conditioning tank 2, and adjusting solvent is hydroxide
Sodium and dilute sulfuric acid.The water outlet of conditioning tank 2 connects the water inlet in multiple copper-stripping reaction pond 3, multiple copper-stripping reaction pond 3 by pipeline
Water outlet by pipeline connect filtering ponds 4 water inlet, filtering ponds time of repose be 1h, it is here, anti-by multiple copper removal
The magnetic fillers carried in the waste water in pond 3 and diatomite are answered completely to be filtered.The water outlet of filtering ponds 4 is connected by pipeline
The water inlet of MBR system 5, by MBR advanced treating, the content of organics in water is greatly reduced, and coloration reduces.MBR system 5
Water outlet the water inlet of tank 7 is connected by pipeline, water waits for reuse or outlet here.The water outlet of tank 7
Mouth connection discharge tube.The backwash water outlet 318 in multiple copper-stripping reaction pond 3 is entered by the backwashing water that pipeline connects setting pot
Mouthful, the slag notch of setting pot 1 enters cinder notch by the first of pipeline connection residue pool 6, and the slag notch in multiple copper-stripping reaction pond 3 passes through
The second of pipeline connection residue pool 6 enters cinder notch, and the slag notch of filtering ponds 4 enters cinder notch by the third that pipeline connects residue pool 6, stores up
The reuse mouth in pond 7 connects the backwash water inlet 317 in multiple copper-stripping reaction pond 3 by pipeline.Wherein, 31 interior wall of absorption region
Wall two sides are covered with baffle 37, and 5cm is spaced between baffle 37, and baffle 37 has 5 kinds of angles, are located at 31 bottom of absorption region extremely
The baffle 37 of 1/5th height is parallel to the horizontal plane, the baffle 37 and horizontal sextant angle of 2/1sts to five/5th height
It is 30 °, the baffle 37 and horizontal sextant angle of 3/2nds to five/5ths height are 45 °, 4/3rds to five/5ths height
Baffle 37 and horizontal sextant angle be 60 °, 4/5ths to region top baffle 37 and horizontal vertical, be equipped on baffle 37
Diatomite；The baffle 37 in multiple copper-stripping reaction pond 3 is bamboo material, and with a thickness of 2cm, the positive and negative two sides of baffle 37 are provided with storage
Slot, groove depth 0.5cm are uniformly laid with diatomite in slot, are highly 0.4cm, diatomite is fixed on slot with gauze and metal screen
Interior, waste water is entered in this region by water inlet 316, due to waste water at this time under the drainage of baffle 37 from level to level around absorbing
Plate 37 rises, and on its surface, organic matter, copper ion and polluter in water are by metal mesh and gauze by the diatom in board slot
Soil absorption, while extremely least a portion of diatomite can be gone out outside slot by the impact force of water flow, due to the resistant presence of baffle 37,
More arrive top, the angle folding of baffle 37 is bigger, reduces the resistance to water with this, water energy is allowed enough to rise the next area of inflow
Domain.One group of tilted slot 38 is installed, the inclined-plane and ground angle of tilted slot 38 are 60 °, on tilted slot 38 uniformly in recovery zone 32
Equipped with mud retaining plate 39, it is spaced 10cm, mud retaining plate 39 height 5cm is perpendicular to the ground, is designed with leakage cinder notch under every group of mud retaining plate 39
310,310 diameter 0.3cm of cinder notch is leaked, 38 bottom of tilted slot is equipped with slag receiving trough 311；Waste water enters in this region, carries in water
The diatomite of part is intercepted when flowing through tilted slot 38 by mud retaining plate 39 out, is leaked cinder notch 310 at this time and is belonged to closed state, when useless
When water is integrally flowed out out of region, all leakage cinder notch 310 are opened, diatomite is directly over hose connection by gravity and enters
In slag receiving trough 312, slag receiving trough 312 connects slag notch 320 by Residue extraction pipeline, and slag notch 320 is located in pool bottom.Magnetized area
33 middle position of domain is equipped with electromagnetic system 319, system and company contour at the water outlet of region, in 33 domain of magnetized area and purification region 31
It meets place and is equipped with connection door 312, connect door 312 at this time and be in close state, electromagnetic system is opened, and there is remaining major part in water supply
Machine substance and copper ion carry out electrostatic treatment, allow organic matter surface with positive charge, and copper ion then shows under in charge
It is more active, waste water stops 20min in this area.It purifies and fills magnetic fillers 313 in region 34, filler and region enter water
Locate it is contour, filler be High Polymer Magnetic rubber, sphere, partial size 0.5cm, 0.25cm, 0.1cm, small particle size filler is at region bottom
Portion, the 50% of occupied area domain, middle partial size filler portion, the 35% of occupied area domain in the zone, large particle size filler is in the top in region, occupied area domain
15%, purification region 34 and buffer area 35 between be equipped with connection door 312, at this time open connection door 312, magnetic fillers 313 pass through
After crossing processing, surface carries negative electrical charge, is attracted by the organic matter and copper ion with positive charge in waste water and waste water, is reached
The purpose of removal.Away from strong magnets group 314 is equipped at the 30cm of bottom in buffer area 35, magnet is opened at this time, by filling out for outflow
Material generates electrostatic efficiency, is all adsorbed onto surface, in order to avoid outflow reaction tank.The bottom of equipment is arranged in back washing area 36, left
There are backwash water inlets 317 for side, and when in water discharge reaction tank, opening backwash water inlet 317, water is flowed from tank 7
Enter, the sundries in filler is gone out in region, is discharged by the backwash water outlet at the top of region.
1 process efficiency list position mg/L of table, except coloration
| Copper | COD | Ammonia nitrogen | Suspended matter | Coloration（Times） | |
| Before processing | 100 | 714 | 143 | 500 | 128 |
| After processing | 0.1 | 5.0 | 1.0 | 2.0 | 2 |
| Treatment effeciency（%） | 99.9 | 99.3 | 99.3 | 99.6 | — |
2 conventional physical aeration system treatment effeciency list position mg/L of table, except coloration
| Oil | COD | Ammonia nitrogen | Suspended matter | Coloration（Times） | |
| Before processing | 100 | 300 | 60 | 500 | 128 |
| After processing | 5 | 60 | 12 | 16 | 32 |
| Treatment effeciency（%） | 95.0 | 80.0 | 80.0 | 96.8 | — |
Claims (5)
1. a kind of processing system of industry copper-containing wastewater, which is characterized in that the system includes setting pot, conditioning tank, multiple copper removal
Reaction tank, filtering ponds, MBR system, residue pool, tank etc.；Wherein, the copper-containing wastewater in industrial processes passes through pipe
Road connects the water inlet for being discharged into setting pot, and the water outlet of setting pot connects the water inlet of conditioning tank by pipeline, and conditioning tank goes out
The mouth of a river connects the water inlet in multiple copper-stripping reaction pond by pipeline, and the water outlet in multiple copper-stripping reaction pond is connected by pipeline to be filtered
The water inlet in pond, the water outlet of filtering ponds connect the water inlet of MBR system by pipeline, and the water outlet of MBR system passes through pipeline
The water inlet of tank is connected, the water outlet of tank connects discharge tube, and the backwash water outlet in multiple copper-stripping reaction pond is logical
Piping connects the backwashing water entrance of setting pot, and the slag notch of setting pot enters cinder notch by the first of pipeline connection residue pool,
The slag notch in multiple copper-stripping reaction pond connects the second of residue pool by pipeline and enters cinder notch, and the slag notch of filtering ponds is connected by pipeline
The third for connecing residue pool enters cinder notch, and the reuse mouth of tank connects the backwash water inlet in multiple copper-stripping reaction pond by pipeline；
Wherein, multiple copper-stripping reaction pond includes absorption region, recovery zone, magnetized area, purification region, buffer area, backwash area
Domain；Absorption region interior walls two sides are covered with baffle, and 5cm is spaced between baffle, and baffle has 5 kinds of angles, are located at uptake zone
The baffle of domain bottom to 1/5th height is parallel to the horizontal plane, the baffle and level of 2/1sts to five/5th height
Angle is 30 °, and the baffle and horizontal sextant angle of 3/2nds to five/5ths height are 45 °, and 4/3rds to five/5ths is high
The baffle of degree and horizontal sextant angle are 60 °, 4/5ths to region top baffle and horizontal vertical, diatom is housed on baffle
Soil；One group of tilted slot is installed, the inclined-plane and ground angle of tilted slot are 60 °, and resistance mud is uniformly provided on tilted slot in recovery zone
Plate is spaced 10cm, mud retaining plate height 5cm, perpendicular to the ground, and leakage cinder notch is designed under every group of mud retaining plate, leaks cinder notch diameter
0.3cm, tilted slot bottom are equipped with slag receiving trough, and slag receiving trough connects slag notch by Residue extraction pipeline, and slag notch is located at pond body bottom
Portion；Magnetized area middle position is equipped with electromagnetic system, is equipped with connection door in the junction in magnetized area and purification region；Purifying area
Fill magnetic fillers in domain, filler enters contour at water with region, and filler is High Polymer Magnetic rubber ball body, and partial size is respectively
0.5cm, 0.25cm, 0.1cm, 0.5cm partial size filler account for 50%, the 0.25cm partial size filler of Domain Volume in area in sections bottom
In the middle part of domain, 35%, the 0.1cm partial size filler of Domain Volume is accounted on the top in region, the 15% of Domain Volume is accounted for, is equipped at the top of region
Water outlet is backwashed, connection door is equipped between purification region and buffer area；Strong magnets group is equipped in buffer area；Backwash
The bottom of equipment is arranged in region, and there are backwash water inlets in left side.
2. the processing system of industry copper-containing wastewater according to claim 1, which is characterized in that the suction in multiple copper-stripping reaction pond
Receipts plate is bamboo material, and with a thickness of 2cm, the positive and negative two sides of baffle are provided with storage groove, groove depth 0.5cm, is uniformly laid with diatom in slot
Soil is highly 0.4cm, and diatomite is fixed in slot with gauze and metal screen.
3. the processing system of industry copper-containing wastewater according to claim 1, which is characterized in that the resistance in multiple copper-stripping reaction pond
The leakage cinder notch of mud plate is designed with switching device, can open and close simultaneously, and leaking under cinder notch has hose to be connected to slag receiving trough.
4. the processing system of industry copper-containing wastewater according to claim 1, which is characterized in that connect Men Junke everywhere and pass through
Long-range control is turned on or off.
5. the processing system of industry copper-containing wastewater according to claim 1, which is characterized in that setting pot is a length of when standing
30min；Bottom is equipped with automatic Slag Scraping Device in setting pot；Control pH is 6.5-7.5 in conditioning tank, adjust solvent be sodium hydroxide or
Dilute sulfuric acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810889806.9A CN108911414A (en) | 2018-08-07 | 2018-08-07 | A kind of processing system of industry copper-containing wastewater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810889806.9A CN108911414A (en) | 2018-08-07 | 2018-08-07 | A kind of processing system of industry copper-containing wastewater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108911414A true CN108911414A (en) | 2018-11-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810889806.9A Withdrawn CN108911414A (en) | 2018-08-07 | 2018-08-07 | A kind of processing system of industry copper-containing wastewater |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013012395A1 (en) * | 2011-07-19 | 2013-01-24 | National University Of Singapore | Wastewater treatment using natural solid additives in activated sludge process |
| CN204237680U (en) * | 2014-10-31 | 2015-04-01 | 苏州工业园区清源华衍水务有限公司 | A kind of industrial sewage advanced treatment system |
| CN106116055A (en) * | 2016-08-19 | 2016-11-16 | 湖南富森泰智能科技有限公司 | A kind of intelligence decomposes Industrial sewage treatment system |
-
2018
- 2018-08-07 CN CN201810889806.9A patent/CN108911414A/en not_active Withdrawn
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2013012395A1 (en) * | 2011-07-19 | 2013-01-24 | National University Of Singapore | Wastewater treatment using natural solid additives in activated sludge process |
| CN204237680U (en) * | 2014-10-31 | 2015-04-01 | 苏州工业园区清源华衍水务有限公司 | A kind of industrial sewage advanced treatment system |
| CN106116055A (en) * | 2016-08-19 | 2016-11-16 | 湖南富森泰智能科技有限公司 | A kind of intelligence decomposes Industrial sewage treatment system |
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Application publication date: 20181130 |