CN106277233B - A kind of superconduction sewage-treatment plant and method - Google Patents
A kind of superconduction sewage-treatment plant and method Download PDFInfo
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- CN106277233B CN106277233B CN201610874227.8A CN201610874227A CN106277233B CN 106277233 B CN106277233 B CN 106277233B CN 201610874227 A CN201610874227 A CN 201610874227A CN 106277233 B CN106277233 B CN 106277233B
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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
- C02F1/484—Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets
- C02F1/485—Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets located on the outer wall of the treatment device, i.e. not in contact with the liquid to be treated, e.g. detachable
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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
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
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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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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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
- C02F2001/007—Processes including a sedimentation step
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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
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The present invention relates to a kind of sewage-treatment plant and methods, belong to environmental technology field, are specifically related to a kind of superconduction sewage-treatment plant and method.The device and method is using quantum carbon element magnetic medium as magnetic adsorptive material, it being capable of each metal ion species in quick adsorption liquid, and be adsorbed under the action of the high-intensity magnetic field generated in superconduction in three-dimensional paramagnetic metal link network, quantum carbon element magnetic medium is taken out of and recycled by the machine driving of metal link network.
Description
Technical field
The present invention relates to a kind of sewage-treatment plant and methods, belong to environmental technology field, are specifically related to a kind of sewage
Processing unit and method.
Background technique
Heavy metal contained in waste water is big to environmental and human health impacts harm, the duration is long.It is a large amount of untreated useless
Gurry is shifted to soil system, and is collected under the action of natural cause, remained in soil environment.Soil pollution is mainly with weight
Based on metallic pollution, wherein cadmium, mercury, lead, arsenic pollution are the most prominent, chromium (Cr), arsenic (As), the cadmium (Cd), zinc contained in waste water
(Zn), the heavy metal ion such as nickel (Ni) have the characteristics that difficult to degrade, irreversible, toxicity is big and is easily bioaccumulation, micro
Poisonous effect is generated, it is very harmful.
The traditional treatment method of contaminant water has: chemical precipitation, ion exchange, absorption, UF membrane, redox, electrolysis and
Extraction etc., but these methods are often affected by factors such as water temperature, pH value, water quality, it is low to certain soluble substance removal rates,
And there are secondary pollutions.Soil organic matter and heavy metal are administered to repair and have more technology, including there are commonly objects
Physicochemical method, phytoremediation, microbial remediation method, soil wash the technology of leaching backfill method etc..Currently, the recovery project of soil
In, the method for comparing popularization and application is to be recovered to the pollutant in soil by washing leaching to wash in water drenching, and treated, and soil returns
It fills out, the contaminant water after washing leaching carries out water process again.
Magnetic separation technique is applied to be had in wastewater treatment, especially superconducting high-gradient magnetic separation technique processing heavy metal wastewater thereby
Its unique advantage.For weak magnetic in waste water and nonmagnetic pollutant, the sorption of the magnetic medium of various characteristics can be passed through
Method, rapidly Magneto separate is handled.The advantages that due to Magneto separate processing system low cost, small space, high efficiency and high speed processing,
As direction of scientific rersearch emerging in recent years.Realize that heavy metal containing sewage Magneto separate includes two aspect work, first is that superconducting magnet, second is that
Magnetic kind.Superconducting magnet equipment has been highly developed technology, is obtained from commercial product with can be convenient.Magneto separate critical issue
It is the concrete technology for the magnetic kind and Magneto separate for how preparing high-quality.
Photocatalytic oxidation is to study a more high-level oxidation technology at present, is at a kind of environmentally friendly Green Water
Reason technology, it can exhaustive oxidation degradation sewage in organic pollutant.In conjunction with a certain amount of light radiation, photosensitive medium material exists
The irradiation lower surface excited target of light and generate electronics (e-) and hole (h+).These electrons and holes have very strong reduction and oxygen
Change ability can be reacted with water or the oxygen stored, generate hydroxyl free radical (OH) and super negative oxonium ion (O).These oxygen
All chemical bonds for constituting organic molecule can almost be cut off and be decomposed, reach harmless treatment by the extremely strong free radical of the property changed.But
The catalyst utilization of photocatalysis oxidation method and the rate of recovery are low at present, need by improving catalyst efficiency, using photoproduction electricity
Son and hole-recombination, and other processing techniques improve reaction efficiency etc. problem jointly.
Superconducting high-gradient magnetic separation technique is with unique separation principle and plurality of advantages, it has also become most promising is novel
One of sewage disposal technology.As technical know-how and equipment continue to develop, application field increasingly increases, in industrial wastewater, life
Living sewage, polluted river water and lake water and in processing sludge and waste water weak magnetic and nonmagnetic pollutant in terms of have it is unique
Advantage has obtained numerous research and small-scale application using the adsorbent material of magnetic function.Same photocatalysis oxidation method
Also have the characteristics that extremely outstanding.But this two technologies are still without obtaining the case of due universal and large-scale engineer application
Example, reason are to lack the problems such as efficient, economically and reasonably technology is equipped with, especially equipment magnetism separate method and functionality
Magnetic adsorptive material whether can be well matched with, can the feature that be related to magnetic separation technique fully be brought into play.Light
Can catalysis oxidation be that light reaction medium could generate catalytic action under the irradiation of specific wavelength light source, develop light reaction Jie
Catalysis reaction, and important one of the project in the current field occur under the spectrum effect of more wide area for matter.
For these problems, the present inventor is proposed on the basis of long-term system exploitation and basic material research using super
The effect for the high-gradient intense magnetic field led is placed in the height of superconduction generation with the chain net structure that paramagnetic wire is made into specific standard
In gradient magnetic specific position, magnetisable material can be quickly captured into three-dimensional mesh, and pass through the blowing of air-pressure equipment, vacuum
Magnetic adsorptive material is returned and is reused by sucking, whirlwind solid gas separation system.
Summary of the invention
Present invention is primarily intended to solve the low technology of sewage metallic pollution treatment efficiency existing in the prior art to ask
Topic provides a kind of superconduction sewage-treatment plant and method.The device and method is using quantum carbon element magnetic medium as magnetism
Adsorbent material, can each metal ion species in quick adsorption liquid, and inhaled under the action of the high-intensity magnetic field generated in superconduction
It is attached in three-dimensional paramagnetic metal link network, quantum carbon element magnetic medium is taken out of and recycled by the machine driving of metal link network.
Above-mentioned technical problem of the invention is mainly to be addressed by following technical proposals:
A kind of superconduction sewage-treatment plant, comprising: Magneto separate tank body, superconducting magnet；Wherein:
The Magneto separate tank body is located in the field region of superconducting magnet, is internally provided with hinge joint in the metal on driving wheel
Link network, the metal link network extend at least partially into two skies being oppositely arranged in magnetic medium extraction mechanism and blow the trumpet between mouth；
One of sky blows the trumpet mouth as positive pressure, another sky blows the trumpet mouth as negative pressure；
The superconducting magnet includes: superconducting bodies, and superconducting bodies are internally provided with vaccum exhaust outlet and current terminal, refrigerant
Import, refrigerant exit.
Optimization, a kind of above-mentioned superconduction sewage-treatment plant, the superconducting magnet is cryogenic magnet, and refrigerant is liquid
Helium, it is 114A that current terminal, which conveys electric current into superconducting bodies, and temperature monitor and control is 4K, is vacuum-evacuated as 10-6hPa, magnetic field
Center is 2T.
Optimization, a kind of above-mentioned superconduction sewage-treatment plant, further includes: blending tank, wherein be arranged on the blending tank
There is medium dispensing port, the outlet of the blending tank is connected with the inlet of the Magneto separate tank body.
Optimization, a kind of above-mentioned superconduction sewage-treatment plant, the sky of negative pressure mouth of blowing the trumpet connects the separation of several solid gases
Device.
Optimization, above-mentioned a kind of superconduction sewage-treatment plant, the solid outlet and medium of the solid-gas separator is launched
Mouth is connected.
Optimize, a kind of above-mentioned superconduction sewage-treatment plant, is provided with inlet, overflow on the Magneto separate tank body
Mouthful, the inlet and overflow port are located at the two sides of the metal link network, wherein the overflow port respectively with sample detection
Mouth is connected with blending tank.
A kind of superconduction sewage water treatment method, comprising: the liquid to be treated for being mixed with quantum carbon element magnetic medium is passed through and is set
In in the Magneto separate tank body of field region, metal will have been adsorbed using the rotatable metal link network being arranged in Magneto separate tank body
Quantum carbon element magnetic medium takes Magneto separate tank body out of, is blown quantum carbon element magnetic medium on the net from metallic bond using sky mouth of blowing the trumpet
Out, quantum carbon element magnetic medium is separated from air-flow using solid-gas separator.
Therefore, the present invention has the advantage that
1. quantum carbon element magnetic medium provided by the invention can be special and efficiently separates and adsorb the heavy metal in water
Ion improves the treatment effeciency of metal ion；
2. superconducting magnet used in the present invention can be dismantled, be changed to cryogenic magnet or high-temperature superconducting magnet, superconduction
Magnet is provided with metal paramagnetic link network extraction mechanism to predetermined high-gradient magnetic field is provided inside superconduction separator in magnetic field,
Paramagnetic link network is magnetized in high-gradient magnetic field, adsorbs the magnetisable material in water, and the magnetisable material inhaled passes through metal paramagnetic chain
Net is promoted and is separated to air operated mechanism, to achieve the effect that Magneto separate, significantly improves Magneto separate effect, and reduce magnetic
Isolated cost.
Detailed description of the invention
Fig. 1 is waste water processes schematic diagram；
Fig. 2-1 is the heavy metal processing partial schematic diagram of sewage-treatment plant system；
Fig. 2-2 is the organic matter processing partial schematic diagram of sewage-treatment plant system；
Fig. 3 is magnetic separation system structural schematic diagram；
Fig. 4-1 is superconducting magnet shape main view；
Fig. 4-2 is superconducting magnet shape top view；
Fig. 5 is magnetic kind recycling and reusing system；
Fig. 6-1 is three-dimensional paramagnetic metal link network main view；
Fig. 6-2 is three-dimensional paramagnetic metal link network side view；
Fig. 7 is that the sky of magnetic medium extraction mechanism is blown the trumpet a mouthful schematic diagram；
Fig. 8-1 is that magnetic medium extraction mechanism sky mouth of blowing the trumpet is schemed in detail；
Fig. 8-2 is the bottom view of Fig. 8-1；
Fig. 8-3 is the left view of Fig. 8-1；
Fig. 9 is dissolved oxygen microvesicle generators structural schematic diagram；
Figure 10-1 is the structural schematic diagram of the sheet metal A1 of dissolved oxygen microvesicle generators；
Figure 10-2 is the schematic side view of Figure 10-1；
Figure 10-3 is the structural schematic diagram of the sheet metal B1 of dissolved oxygen microvesicle generators；
Figure 10-4 is the schematic side view of Figure 10-3；
Figure 10-5 is the structural schematic diagram of the sheet metal A2 of dissolved oxygen microvesicle generators；
Figure 10-6 is the schematic side view of Figure 10-5；
Figure 10-7 is the structural schematic diagram of the sheet metal B2 of dissolved oxygen microvesicle generators；
Figure 10-8 is the schematic side view of Figure 10-7；
Figure 10-9 is the structural schematic diagram of the sheet metal C of dissolved oxygen microvesicle generators；
Figure 10-10 is the schematic side view of Figure 10-9；
Figure 10-11 is the structural schematic diagram of the sheet metal D of dissolved oxygen microvesicle generators；
Figure 10-12 is the schematic side view of Figure 10-11；
Figure 10-13 is the structural schematic diagram of sheet metal A1 and the B1 superposition of dissolved oxygen microvesicle generators；
Figure 10-14 is the structural schematic diagram of sheet metal A2 and the B2 superposition of dissolved oxygen microvesicle generators；
Figure 10-15 is the structural schematic diagram of sheet metal A and the B superposition of dissolved oxygen microvesicle generators；
Figure 11 is the structural schematic diagram after each sheet metal combination of dissolved oxygen microvesicle generators；
Figure 12 is bubble size and density schematic diagram；
Figure 13 is microvesicle ionic forms；
Figure 14 is Photoreactor structural schematic diagram；
Figure 15 is metallic fiber sintered felt filter structure schematic representation；
Figure 16 is plating organic oil ink factory's water treatment effect and medium circulation statistical data；
Figure 17-1 is certain printed circuit board plant chimney stalk treatment effect schematic diagram 1.
Figure 17-2 is certain printed circuit board plant chimney stalk treatment effect schematic diagram 2.
Specific embodiment
Below with reference to the embodiments and with reference to the accompanying drawing the technical solutions of the present invention will be further described.
In figure, sewage collecting tank 1, refrigeration machine control cabinet 2, blending tank 3, stirring system 4, system control cabinet 5, superconductor 6,
Refrigerator 6-1, field region 6-2, magnetic field center 6-3, superconducting bodies 6-4, current terminal 6-5, refrigerant inlet 6-6, refrigerant go out
Mouth 6-7, vaccum exhaust outlet 6-8, temperature monitoring 6-9, Magneto separate tank body 7, overflow port 7-1, magnetic medium extraction mechanism 8, driving wheel
8-1, driven wheel 8-2, tensioning wheel 8-3, air entry 8-4, inflatable mouth 8-5, three-dimensional paramagnetic metal link network 8-6, air flue 8-7, fixation
Plate 8-8, horn mouth 8-9, magnetic medium collection system 9, the first whirlwind solid-gas separator 9-1, the second whirlwind solid-gas separator 9-
2, air hose 9-3, quantum carbon element light reaction medium blending tank 10, quantum carbon element light reaction medium dispensing port 10-1, dissolved oxygen microvesicle hair
Raw device 11, positioning bolt 11-1, dissolved oxygen microvesicle generators shell 11-2, Photoreactor 12, light source end cap 12-1, outlet 12-2,
Metal outer cylinder 12-3, reflective layer 12-4, light source 12-5, entrance 12-6, first stage precipitation tank 13, second-level settling pond 14, water purification filter
Device 15, water purification outlet 15-1, purifier shell 15-2, filtering body 15-3, intake pump P1, sewage pump P2, air pressure pump P3, light are anti-
Answer pressure pump P4, recovery pump P5, draining pump P6, level-one return valve F1, level-one sampling valve F2, inlet valve F3, recovery valve F4, light anti-
Inlet valve F5, light reaction outlet valve F6, quantum carbon element light reaction dielectric film filter valve F7, quantum carbon element light reaction medium second level is answered to return
It receives valve F8, recoil purge valve F9, recoil shut-off valve F10, second level and returns to valve F11, drain valve F12, second level sampling valve F13, pressure
Recoil Table V 1, vacuum table V2,
One, sewage treatment process and system structure
Fig. 1 is the sewage treatment process of the present embodiment, and sewage purification system used in the technique includes successively connection
Sewage collecting tank, blending tank, superconduction magnetic separation system, photocatalytic reactor, wherein further include Superconducting magnetic dielectric film filter again
The magnetic medium circulator and quantum carbon element light reaction media recycler utilized.
The sewage purification system of the present embodiment is handled by heavy metal and what two parts of organic matter processing formed is
System is by the heavy metal and the method that is respectively processed of organic pollutant in sewage.The method of especially two kinds Combined Treatments
In, magnetic absorption medium provided by the invention and quantum carbon element light reaction medium cooperate sewage purification system, special and effectively
Separation and heavy metal, organic pollutant in decomposition water.
Sewage purification system of the present invention, superconduction magnetic separation mechanism used includes superconducting magnet, and superconducting magnet can
To dismantle, be changed to cryogenic magnet or high-temperature superconducting magnet, superconducting magnet is predetermined high to offer inside superconduction separator
Gradient magnetic.Metal paramagnetic link network extraction mechanism is provided in magnetic field, paramagnetic link network is magnetized in high-gradient magnetic field, absorption
Magnetisable material in water.The magnetisable material inhaled is promoted to air operated mechanism by metal paramagnetic link network and is separated, to reach
The effect of Magneto separate.The magnetisable material is quantum carbon element magnetic medium provided by the present invention.
Sewage purification system of the present invention, light reaction processing mechanism used include 1 group or multiple groups Photoreactor, amount
Sub- carbon light reaction medium participates in the reaction of Photoreactor with certain size and specific gravity.Solid-liquid is carried out by natural sedimentation method
Separation, quantum carbon element light reaction medium are recycled by the circulatory system.The quantum carbon element light reaction medium is by of the invention
The quantum carbon element light reaction medium of preparation.Water is after Magneto separate and light reaction processing, then passes through high-precision metallic fiber sintered
The filtering of felt filtering body obtains clean water up to standard.
Fig. 2-1 and Fig. 2-2 is an optional specific implementation system structure diagram of the present embodiment sewage disposal system.
Wherein, the A2 mouth in the A1 mouth connection figure 2-2 in Fig. 2-1.
Wherein, heavy metal processing part specifically includes: sewage collecting tank 1, the bottom of sewage collecting tank 1 as shown in Fig. 2-1
It is connected by sewage pump P2 with blending tank 3；Blending tank 3 is provided with the agitating device 4 for stirring scarce tank interior, blending tank 3
Bottom be connected with Magneto separate tank body 7 by intake pump P1；Magnetic medium extraction mechanism 8 is provided on Magneto separate tank body 7, which is situated between
Matter extraction mechanism 8 is connected with magnetic medium collection system 9；The recovery port of magnetic medium collection system 9 is communicated with blending tank 3；Magnetic
Property medium collection system 9 include that two two skies being oppositely arranged being connected with air pressure pump P3 are blown the trumpet mouth, two gas nozzles are opposite
The two sides of three-dimensional paramagnetic metal link network 8-6 are set to, for one of gas nozzle for generating positive pressure, another generates negative pressure；To
Magnetic medium is withdrawn from three-dimensional paramagnetic metal link network 8-6.Magneto separate tank body 7 is located in the magnetic field range of superconductor 6, this is super
Conductor 6 connects refrigeration machine 2 and is connected with system control cabinet 5.
Fig. 2-2 is organic matter processing part, is specifically included: the quantum carbon element being connected with 7 top overflow port of Magneto separate tank body
The bottom of light reaction medium blending tank 10, quantum carbon element light reaction medium blending tank 10 is micro- by light reaction pressure pump P4 and dissolved oxygen
Generator 11 is steeped to be connected；Dissolved oxygen microvesicle generators 11 successively with Photoreactor 12, first stage precipitation tank 13, second-level settling pond 14, net
Water filter 15 is connected.
Wherein, first stage precipitation tank 13, second-level settling pond 14 bottom pass through recovery pump P5 and recovery valve F4 and quantum carbon element
Light reaction medium blending tank 10 is connected.
The present embodiment is provided with sample detection mouth on the pipeline being connected with overflow port above Magneto separate tank body 7.The pipeline
Valve F1 is returned by level-one to be connected with sewage collecting tank 1, is connected by level-one sampling valve F2 with sample detection mouth, is passed through inlet valve
F3 is connected with quantum carbon element light reaction medium blending tank 10,
The waste water processes of the present embodiment are specifically described below.In the present embodiment, for heavy metal processing and organic matter
Corresponding ion processing step and organic matter decomposition step has been respectively adopted in processing, is introduced separately below.
Wherein, ion processing step specifically includes following sub-step:
After step 1, sewage enter sewage collecting tank 1, blending tank 3, the top of blending tank 3 are quantitatively entered by sewage pump P2
Equipped with magnetic medium dispensing port, quantitative offer amount is required according to concentration by dispensing port below the first whirlwind solid-gas separator 9-1
Sub- carbon magnetic medium, and be sufficiently mixed under the stirring of stirring system 4.
Uniformly mixed liquid is delivered directly to Magneto separate tank body 7 by pipeline by intake pump P1 by step 2.
Step 3, Magneto separate tank body 7 connect superconducting magnet 6, and superconducting magnet 6 is to providing 0.5T-5T inside Magneto separate tank body 7
The magnetic field of intensity.Magneto separate tank body 7 according to entrance come mixed liquor fluid properties and the water conservancy diversion panel designed of magnetic field properties,
The deflector can be 45 ° of plates being arranged below entry to mixed solution, the metallic bond net lower semisection in magnetic medium extraction mechanism 8
It is placed in Magneto separate tank body 7 in liquid, mixed liquor first passes around in magnetic medium extraction mechanism 8 through the trend that water conservancy diversion panel flows to
Metal link network, the magnetisable material of mixed liquor are all drawn onto three-dimensional paramagnetic metal chain as in Figure 6-1 under the absorption of high-intensity magnetic field
On the net, and it is transported to Recovery of magnetic medium reutilization system cycling and reutilization.Non magnetic large particulate matter precipitating in mixed liquor
To 7 Magneto separate tank body lower parts, and regularly sediment exclusion (spoil disposal), the cleaning objects after mixed liquor Magneto separate pass through Magneto separate
Overflow port continuous overflow discharge above tank body.Superconductor is connected with refrigeration control cabinet 2.Keep the control of high-intensity magnetic field.System
Control cabinet 5 controls system.
In this implementation, organic matter decomposition step specifically includes following sub-step:
Step 1, the water after Magneto separate passes through flows out by the overflow port of Magneto separate tank body 7, through valve F2 in sample detection mouth 1
Locate sample detection heavy metal indices, below standard water body will return to sewage collecting tank 1 by valve F1 and reprocess.It takes
Valve F1, F2 are closed after sample detection is up to standard, are opened F3 and are entered photoreaction system.
Step 2, water body is entered into quantum carbon element light reaction medium blending tank 10, quantum carbon element light reaction medium by valve F3
There is quantum carbon element light reaction medium dispensing port above blending tank 10, it is fixed that quantum carbon element light reaction medium dispensing port is required according to concentration
The dispensing quantum carbon element light reaction medium of amount, after being sufficiently mixed in blending tank, mixed liquor gives certain kinetic pressure through pumping P4
By force, it by dissolved oxygen microvesicle generators 11, carries out entering Photoreactor 12, light by valve F5 after sufficient dissolved oxygen reacts
Reactor 12 is made of at least one set of or multiple groups, and the mixed liquor after Photoreactor reaction enters first stage precipitation tank 13 through valve F6.
Step 3, first stage precipitation tank 13 carries out precipitating type separation of solid and liquid, and quantum carbon element light reaction medium is deposited to level-one precipitating
The bottom in pond 13, isolated water overflow to second-level settling pond 14, and the quantum carbon element light reaction medium of precipitating becomes slurry in bottom
State, quantum carbon element light reaction dielectric paste back within quantum carbon element light reaction medium through valve F7 and pump P5 and valve F4 and mix
Close the mixed cycling and reutilization of tank 10.
Step 4, the residual quantum carbon element light reaction medium in water is continued precipitation and separation, the quantum of bottom by second level blending tank
Carbon light reaction dielectric paste through valve F8 and pump P5 and valve F4 back within quantum carbon element light reaction medium blending tank 10 into
The mixed cycling and reutilization of row.Second level blending tank supernatant is obtained via water-purifying filter 15, valve F10, pressure gauge V1 and pump P6
To clean water, water is by valve F13 in 2 sample detection of sample detection mouth, the water up to standard water in line, below standard by valve F13
It returns to quantum carbon element light reaction medium blending tank 10 by valve F11 and pump P5, valve F4 and handles again.
Two, Magneto separate and magnetic medium recycling
As shown in figure 3, magnetic separation system is by superconducting magnet 6, Magneto separate tank body 7, magnetic medium extraction mechanism 8, adsorption machine
Structure composition, superconducting magnet 6 can be high-temperature superconducting magnet, be also possible to cryogenic magnet.
Magneto separate tank body 7 includes Magneto separate tank body, is provided with inlet, overflow port, mud discharging mouth on Magneto separate tank body,
In, overflow port is preferably disposed on Magneto separate top of the tank position.
Inlet and overflow port 7-1 are located at the two sides of the metal link network, also, set on the Magneto separate tank body 7
The side for setting inlet is provided with the structure that classification is inwardly indented, and every grade of outer wall is parallel to each other, and inclination is provided between every grade
45 degree of reducer.
Liquid to be treated is handled after entering Magneto separate tank interior from inlet, and the liquid bottom handled is from overflow port
It is discharged, the precipitating magazine in liquid is discharged from the mud discharging mouth of bottom.Magneto separate tank interior is provided with metal link network, the metal
The driven wheel of one end of link network and Magneto separate tank interior links, the other end extend with magnetic medium extraction mechanism and with 8 inside
Roller hinge joint, Magneto separate tank body middle part are provided with several nervous wheels to connect with metal link network.
In the field region that Magneto separate tank body is located at the offer of superconducting magnet 6, superconducting magnet is outer shaped like Fig. 4-1, Fig. 4-2 institute
Show.Specifically include: superconducting bodies, superconducting bodies are internally provided with vaccum exhaust outlet and current terminal, refrigerant inlet, and refrigerant goes out
Mouthful.The outer dimension of superconducting magnet is the needs according to magnetic separation system and designs that superconducting magnet can be high-temperature superconducting magnet,
It is also possible to cryogenic magnet.Central magnetic field intensity is 2T-5T, and refrigerator refrigerant is liquid helium or liquid nitrogen.As an example, it selects
Cryogenic magnet, refrigerant are liquid helium, and current terminal conveys electric current 114A into superconducting bodies, and temperature monitor and control is 4K, very
Idle discharge gas is 10-6hPa, and magnetic field center 2T provides high-gradient magnetic field for magnetic separation system.
Magnetic medium extraction mechanism 8 and magnetic medium circulator are as shown in Figure 5.The magnetic medium extraction mechanism 8 is internally provided with
Driving wheel, one end of metal link network are articulated on the driving wheel.There are two the skies being oppositely arranged to blow loudspeaker in magnetic medium extraction mechanism 8
Mouth, metal link network are located at two skies and blow the trumpet between mouth, and one of sky mouth of blowing the trumpet is connected with the positive pressure side of air pump P3,
The other end is sequentially connected several solid-gas separators and communicates with the load pressure of air pump P3.In the present embodiment, two are preferably connected
A whirlwind solid-gas separator.
After adopting the above structure, sky blows the trumpet mouth with by air pump P3 offer circulation pneumatics power, and positive pressure air passes through wind
Pipe is sent to sky and blows the trumpet mouth, carries out empty stripping from while air pump P3 to the magnetisable material that three-dimensional paramagnetic metal chain adsorbs on the net
Other end pipeline generate negative pressure, the magnetisable material online to three-dimensional paramagnetic metal chain carries out negative pressure absorbing.
Whirlwind solid-gas separator carries out solid gas separation twice to achieve the purpose that recycle magnetisable material.Wherein, whirlwind solid gas
The quantum carbon element magnetic medium that separator collection arrives quantitatively can provide magnetic medium to blending tank 3 according to system requirements.Make
For citing, it is 8.0m that preferably air pump P, which selects air quantity,3The air pump that/min, static pressure 16KPa, power are 88KW, but be not limited to
This example, generating static pressure as air hose can be in the range of 10KPa-30KPa.
Metal link network in the present embodiment is as shown in Fig. 6-1, Fig. 6-2.The metal link network is the tool prepared by paramagnetic metal
There are the metal mesh of three-dimensional space, i.e. " three-dimensional paramagnetic metal link network ".Comprising: multiple horizontal axis, the end of adjacent horizontal axis passes through chain
Ring connects, and is provided with chain wire side on horizontal axis, which is entwined in three dimensions by chain silk is wavy.In use,
The metal mesh of the three-dimensional space is magnetized in high-gradient magnetic field, and the magnetisable material in mixed liquor is adsorbed onto the three of metal link network
In dimension space, the movement of link network carries magnetisable material and transports magnetic medium extraction mechanism 8 together.In principle, all paramagnetic metals
It may be by, the three-dimensional geometry space of metal link network can also be in the form of various structures.As an example, preferably paramagnetic material is
SUS316, three-dimensional space net areSUS316 steel wire winding helix tube, screwed pipe diameter 15mm, screw pitch 6mm, Guan Yuguan it
Between bySteel wire linking.
The sky of the present embodiment mouth of blowing the trumpet is as shown in Figure 7.Its loudspeaker inflatable mouth identical and opposite by a pair of of geometric dimension
It being formed with air entry, there is the three-dimensional paramagnetic metal link network of respective width among inflatable mouth, the static pressure of inflatable mouth and air entry is equal,
But inflatable mouth is positive pressure, and air entry is negative pressure, forms the absorption to the three-dimensional online magnetisable material of paramagnetic metal chain and detachment function.
Any adjustment that inflatable mouth, three-dimensional paramagnetic metal link network, the geometric dimension between air entry and orientation can be suitable for.As act
Example, the distance between inflatable mouth and air entry are 30mm, and three-dimensional paramagnetic metal link network is placed in middle.
Fig. 8-1 to Fig. 8-3 is that the present embodiment horn mouth is schemed in detail.Specifically include that tracheae, horn mouth, fixed plate.Blow and
The bell-mouthed geometric dimension of air-breathing is identical and the adjustment that can be suitable for.As an example, present invention discover that optimal selection is air
Static pressure is in 16KPa, the bell-mouthed the geometric dimension most preferably 7mm × 600mm, material SUS304 that blow with air-breathing.
Three, organic matter decomposition and quantum carbon element light reaction dielectric film filter
It mainly includes quantum carbon element light reaction medium blending tank, dissolved oxygen microvesicle generators, light reaction that organic matter, which decomposes part,
The parts such as device.Wherein, quantum carbon element light reaction medium blending tank is mainly used for the mixing of sewage and quantum carbon element light reaction medium.
Main component is introduced below.
1, dissolved oxygen microvesicle generators
It is mixed that liquid after Magneto separate enters quantum carbon element light reaction medium after the outflow of the overflow port of Magneto separate tank body 7
Tank 10 is closed, then enters dissolved oxygen microvesicle generators 11 through light reaction pressure pump P4.
Dissolved oxygen microvesicle generators 11 are microvesicle chamber and multipath chamber respectively as shown in figure 9, be divided into two parts.
Wherein, microvesicle is intracavitary is provided with multiple dissolved oxygen reaction members, and each dissolved oxygen reaction member includes muti-piece via metal
Piece.
The shape of sheet metal is as shown in Figure 10-1 to Figure 10-15.In figure, A1 piece and B1 piece are evenly distributed logical of hexagon
Mesoporous metal piece, hexagon clear size of opening is identical, different in the arrangement of A1 piece and B1 on piece, when A1 piece and the coincidence of B1 piece, A1 piece
On each hexagon through-hole the center of circle be three adjacent hexagons through-holes of B1 on piece nearest outer crosspoint, in figure, A1-B1
For schematic diagram after coincidence.
A2 piece and B2 piece are round evenly distributed via metal pieces, and circular through hole size is identical, in A2 piece and B2 on piece
Arrangement it is different, when A2 piece and B2 piece are overlapped, the center of circle of each circular through hole of A2 on piece is that three of B2 on piece are adjacent
The nearest outer crosspoint of circular through hole, the i.e. distance of center circle in the center of circle and three adjacent circular holes of B2 on piece of each round hole on A2
From identical, A2-B2 is schematic diagram after being overlapped.
C piece is that excircle part is provided with the metal plate of multiple arcs through-hole, opens that there are five caging bolt holes among it.
D piece is the metal plate that centre is provided with through-hole.When A1 piece and D piece are overlapped, the hexagon through-hole of A1 on piece is just formed
One minisize reaction kettle space.Same A2 piece, B1 piece, B2 piece have identical effect.Figure 11 dissolved oxygen microvesicle generators principle
Be the structure combined by A piece, B piece, C piece, D piece in figure, form a minisize reaction kettle after combination, each minisize reaction kettle with
Adjacent reaction kettle communicates, and constitutes liquid medium and continuously flows simultaneously under the states such as different spaces, pressure, temperature, jet stream
Participate in the multiple minisize reaction kettle of reaction.
It in Fig. 9 dissolved oxygen microvesicle generators, is made of a unit or multiple units, liquid medium is laggard by microvesicle chamber
Enter multipath chamber.The intracavitary setting A chamber of multipath, B chamber, C chamber, D chamber, E chamber.The diameter of each cavity is different and mutates, liquid medium
Reaction is participated under the flow velocity difference environment different with positive/negative-pressure, the dissolved oxygen in liquid medium is in fierce stretching and compressive state
It is lower to generate a large amount of ionizing particulate.
For example, preferably 3-5 group unitary reactor forms for the unit process device of dissolved oxygen microvesicle generators front end.Afterwards
Hold A chamber, B chamber, C chamber, D chamber, E chamber caliber the suitable any selection of proportional sizes, wherein D chamber is conical cavity, taper 1:
1, caliber is bore, and E chamber is open cavity, and the import diameter of E chamber is equal to the bore out of D chamber, caliber >=D chamber pipe of E chamber
Diameter.The caliber of each chamber is preferably in a proportion of 3:1.5:4:1:1.Dissolved oxygen microvesicle generators arrival end provides 3-5kg/cm2 by pump P4.
After adopting the above structure, the liquid of quantum carbon element light reaction medium and processing water passes through Fig. 9 dissolved oxygen microvesicle generators
When, multiple micro- reaction kettle of generator front end generates the dissolved oxygen microvesicle in a large amount of liquid, and experiment detection obtains Figure 12 microvesicle ruler
The very little frequency figure with density, the order of magnitude of the longitudinal axis is 10 in figure6, show this example the result is that frequency maximum number diameter is 100nm,
Frequency peak diameter is about 20nm (50% population), and there are about 1,200,000,000 population/cm3, frequency minimum value diameter about 25nm.Largely
Dissolved oxygen microvesicle after the reaction of generator rear end, the dielectric surface and dissolved oxygen microbubble surface of liquid produce microvesicle ion
Form, Figure 13 microvesicle ionic forms show the schematic diagram of ion electric field status with model is established.
2. Photoreactor principle and structure
Figure 14 is Photoreactor structure chart of the invention.By metal outer cylinder, reflective layer, fluorescent tube, light source end cap, entrance, go out
Mouth composition.Wherein, fluorescent tube is set to inside metal outer cylinder, and reflective layer is provided between fluorescent tube and outer cylinder, and metal outer cylinder lower end is set
Set liquid-inlet, upper end setting outlet.
By the liquid of dissolved oxygen microvesicle generators, carries a large amount of dissolved oxygen ion and be attached to quantum carbon element light reaction medium
Enter Photoreactor through Photoreactor entrance on surface layer to be reacted, this phenomenon forms ultraviolet light, quantum carbon element light reaction
The conspiracy relation of medium, dissolved oxygen microvesicle and water is advantageous to improve light-catalyzed reaction efficiency, be situated between for quantum carbon element light reaction
Matter decomposes the rate for generating the strong oxidizers such as hydroxyl radical free radical and the oxidation removal rate of organic matter is promoted to greatly improve.Quantum carbon
There are many light reaction substances for plain light reaction medium, mainly there is TiO2, ZnO, CdS, WO3, SnO2 etc..In 200nm-400nm wavelength
Light source irradiation under, light reaction substance generates a large amount of strongly active oxidation material, such as OH-, O2, H strong oxidizer, almost to institute
Some organic matters or some inorganic matters are compared thoroughly oxygenolysis, produce non-hazardous substance H2O, CO2 etc..This hair
Bright citing, Photoreactor is in a system of the invention, at least one set of, and preferably 4 groups.Medium is granular quantum carbon prepared by the present invention
Light reaction medium, partial size 10um-100um, preferably 30um-60um, handling injected volume in water is 0.1%-1.2% (quality
Than), preferably 0.5%-1% (mass ratio).The dominant wavelength of the preferred 6-8w of light source be 315nm-400nm ultraviolet radiator, light it is strong
Degree is 1mW/cm2.The preferred SUS316 of tank body, tank body inside are equipped with reflective layer, and reflective layer can select the material with reflection function
The light-reflecting product of material, preferably acrylic plating mercury technique, is attached on the inside of tank body.Mixed liquor is defeated from exporting with the flow of 30L/min
Out.
3. water-purifying filter principle and structure
Liquid after light reaction enters first stage precipitation tank 13, second-level settling pond 14.It is provided in second-level settling pond 14
Water-purifying filter 15.15 structure of water-purifying filter is as shown in figure 15.Include: shell, filter hole is provided on shell, is set in filter hole
It is equipped with filtering body, enclosure interior is provided with water purification outlet.By the clear water that precipitates twice using water-purifying filter purified treatment.
The preferred metal shell of case of the invention is SUS316, and various specific high-accuracy filter screens can be used in filter screen, preferably golden
Belong to fiber sintering felt serving filtering body, filtering accuracy 3-10um can reach standard requirements by the water quality of water-purifying filter.
Four, magnetic medium preparation and activation method
When carrying out Magneto separate to the present embodiment at this preparation method of used quantum carbon element magnetic medium liquor and
Activation method is introduced.
1, magnetic medium preparation method
In the present embodiment, the preparation method of quantum carbon element magnetic medium is as shown in following two embodiment.
Embodiment 1:
It (1) is (2.8-3.2): 1 H by mass ratio12Cl3FeO6And FeC12·4H2O is dissolved in ionized water, wherein every
The solute weight that 100ml ionized water is added are as follows: 6.5-7.5g；
(2) solution of step (1) is then used into heating water bath, and is stirred continuously and heats up, be passed through in temperature-rise period
Nitrogen protection, it is 9 or so that concentrated ammonia liquor to pH value of solution is added dropwise after being warming up to 40~60 DEG C, and temperature is kept to stablize, the reaction time 1 hour
More than；
(3) liquid in flask is transferred in beaker after having reacted, is staticly settled；
(4) supernatant for staticly settling rear mixture is removed, it is three times 7 left to cleaning solution pH that deionized water washing, which is added,
The right side obtains nano ferriferrous oxide；
(5) it is adsorbed with magnet in beaker bottom, adds deionized water and quantum carbon element liquid after water is filtered dry, wherein go
Ionized water, nano ferriferrous oxide, quantum carbon element liquid ratio are as follows: 100ml:(3-3.6mg): (60-70ml)；
(6) step (5) mixture is added in active fruit shell carbon, stirred simultaneously, 400~600r/min of revolving speed, mixing time
20~60 minutes；Wherein, 1.9-2.1g active fruit shell carbon is added in every 100ml mixture solution；
(7) it is adsorbed with magnet in beaker bottom, water is filtered dry to be placed in Electric heat oven and is dried；
(8) medium of drying is placed in Muffle furnace oxygen-free atmosphere after calcination activation cooling；
(9) product after cooling is ground to the product between 80um-120um up to quantum carbon element magnetic medium.
Wherein, H12Cl3FeO6For ferric chloride (FeCl36H2O).
Embodiment 2:
(1) by the H of 25.3g12Cl3FeO6With the FeC of 8.6g12·4H2O is dissolved in 500ml deionized water beaker, completely
It is transferred in three-neck flask after dissolution；
(2) three-neck flask is heated in water bath, is stirred continuously, nitrogen protection is passed through in temperature-rise period；
(3) 60 DEG C of dropwise addition concentrated ammonia liquors, control PH9 or so are warming up to；
(4) temperature is kept to stablize, the reaction time 1 hour；
(5) liquid in bottle is transferred in beaker, is staticly settled；
(6) supernatant water is removed, deionized water washing is added three times, control PH7 or so obtains 9.8 grams of nanometers four and aoxidizes
Three-iron；
(7) it is adsorbed with 3000Gs permanent magnet in beaker bottom, 300ml deionized water is added after water is filtered dry；
(8) 200ml quantum carbon element liquid is added and is reacted, stirred simultaneously, revolving speed 500r/min, mixing time 30 minutes；
(9) 9.8g active fruit shell carbon is added and is reacted, stirred simultaneously, revolving speed 500r/min, mixing time 30 minutes；
(10) it is adsorbed with 3000Gs permanent magnet in beaker bottom, water is filtered dry and is placed on 100 DEG C of drying in Electric heat oven；
(11) medium of drying is placed in 550 DEG C of Muffle furnace oxygen-free atmosphere calcination activation 4 hours, natural cooling.
(12) grinding product after cooling to the product between 80um-120um is exactly quantum carbon element magnetic of the invention
Property medium.
Wherein, active fruit shell carbon is the plant carbon of the walnut shell quality of partial size 50um-100um, and iodine number is >=1200mg/g；
Intensity >=95%.
In the present embodiment, quantum carbon element liquid is the aqueous solution containing quantum carbon element, and the ORP of the quantum carbon element liquid is
280mv-380mv, conductivityσ 1-5ms/cm, electromotive force are 280mv~380mv, pH value 1.5-3.2, solute concentration are
0.1%-0.45%.The quantum carbon element liquid solute is the carbon of the single-layer graphene being oxidized and multi-layer graphene (≤10 layers)
Particle (referred to as: quantum carbon element particle) composition, the single-layer graphene and multi-layer graphene mass fraction ratio are 2-4:8-6.Institute
Stating graphene is the periodic cellular shape two dimension carbonaceous material formed by the carbon atom of sp2 hydridization with hexagonal array, single layer stone
Black alkene is with a thickness of 0.335nm.The quantum carbon element particle surface being oxidized has a variety of oxygen-containing groups, such as hydroxyl, carbonyl and carboxyl
Isoreactivity group, quantum carbon element particle on the whole oxygen content mass fraction be 40%-60%.
Under normal conditions for the metal ion in sewage treatment especially water, heavy metal ion is difficult to effectively pass through life
Object method and chemical method remove, and therefore, absorption method is one of the method for current relatively most effective heavy-metal ion removal, due to amount
Sub- carbon particle surface high activity oxygen-containing functional group rich in, so that quantum carbon element particle has good aqueous solubility and mutability
The chemical activity of change can have an effect with metal ion.
The hydroxyl and epoxy group of carboxyl and carbonyl and random distribution, a large amount of hydroxyl in surface is distributed in quantum carbon element particle surface
Base and carboxyl increase the negative electricity density on quantum carbon element surface, strengthen and strong complexing and electrostatic work occurs with metal ion
With promoting the absorption of metal ion.The quantum carbon element particle that exists for of a large amount of functional groups provides adsorption site abundant, ties
Structure characteristic makes quantum carbon element liquid become a kind of high-performance adsorbent material.
The preparation of quantum carbon element magnetic medium through this embodiment makes quantum carbon element magnetic medium have the spy of superparamagnetic
Property, in sewage, each metal ion species in quantum carbon element magnetic medium quick adsorption liquid, and quilt under the action of high-intensity magnetic field
It is adsorbed onto three-dimensional paramagnetic metal link network (Fig. 6-1), by the machine driving of metal link network, by quantum carbon element magnetic medium and takes
It send with the pollutant including metal ion being adsorbed to sky and blows, at suction horn mouth.
2, magnetic medium activation method
Quantum carbon element magnetic medium, can adsorption capacity decline due to absorption tends to saturation in reuse.In the present invention
The detection at sample detection mouth 1 in device systems handles any index of water close to before line up to standard, and quantum carbon element is magnetic
Medium will be recycled all, the medium more renewed.The quantum carbon element magnetic medium of recycling carries out activation.It is activated step
It is rapid as follows:
(1) the quantum carbon element magnetic medium of recycling and deionized water are placed in ultrasonic container in the ratio of 1:3, while stirring
It mixes side and carries out processing 1 hour with the ultrasonic wave of 25KHz frequency；
(2) filter out water adds the deionized water of new same amount to continue stirring ultrasonic treatment 1 hour again；Repeat the side of (1) and (2)
Method is filtered dry afterwards three times, 100 DEG C of oven dryings；
(3) dry medium is placed in 550 DEG C of Muffle furnace oxygen-free atmosphere calcination activation 4 hours, natural cooling.
(4) product grinding after cooling is sized to the product between 80um-120um.
Quantum carbon element magnetic medium after being activated using the above method can still keep 95% or more adsorption activity energy
Power.
Five, the preparation of quantum carbon element light reaction medium and activation method
The preparation side of quantum carbon element light reaction medium used in organic matter decomposable process is carried out to the present embodiment at this
Method and activation method are described below.
1, the preparation method of quantum carbon element light reaction medium
Embodiment 1
The quantum carbon element light reaction medium of the present embodiment the preparation method is as follows:
(1) by quantum carbon element liquid, TiO2, high purity water and appropriate N (CH3)4OH·5H2O is stirred and heats and is prepared as
Slurries, wherein quantum carbon element liquid and TiO2Ratio are as follows: 100ml:200g；Slurries are placed in oven and dried solidification and obtain Rh-
C/TiO2Product；
(2) by Rh-C/TiO2Product, dry zeolite powder and the H containing Pt weight metal 1%3PtCl6·5.3H2O is mixed
Slurries are prepared in conjunction；
(3) it calcines the slurries dry solidification in step (2) to obtain Rh-Pt-C-M/TiO2Composite photocatalytic oxidation body,
Be ground to after cooling 200 mesh to the product between 300 mesh be light reaction medium.
Embodiment 2
The quantum carbon element light reaction medium of the present embodiment the preparation method is as follows:
(1) by 50gTiO2Be distributed in the beaker equipped with 200ml high purity water respectively with 50g zeolite (M), at room temperature into
Several minutes of row stirring (stirring rotator with nonmetallic), water is removed.Repeatedly for three times；
(2) it is dried for standby in 80 DEG C of vacuum ovens.The quantum carbon element liquid of 25ml, the TiO of 50g are weighed respectively2Dry
Powder and Rh (NO containing Rh weight metal 5%3)3；
(3) by quantum carbon element liquid, TiO2, 350ml high purity water and N (CH3)4OH·5H2O, which is added in three-neck flask, to be added
It is (a small amount of every time in whipping process that Rh (NO is slowly added into flask to prepare the slurries that temperature is 60 DEG C for hot mixing3)3, protect
60 DEG C are held, is stirred 1 hour)；
(4) slurries are put into 100 DEG C of baking ovens dry solidification 12 hours, obtain Rh-C/TiO2Product；
(5) Rh-C/TiO will be obtained respectively2Product, 50g dry zeolite powder and contain Pt weight metal 1%
H3PtCl6·5.3H2O be added in three-neck flask be mixed with out slurries (in whipping process every time it is a small amount of into flask slowly
H is added3PtCl6·5.3H2O is stirred 1 hour, stands 6 hours)；
(6) slurries are put into 100 DEG C of baking ovens dry solidification 12 hours, are then placed in the electric dry oven of 380 DEG C of oxygen-free atmospheres
In, it calcines 6 hours, obtains Rh-Pt-C-M/TiO2Composite photocatalytic oxidation body, in agate cone or glass neck after cooling
In be ground to 200 mesh to the product between 300 mesh be exactly quantum carbon element light reaction medium of the invention.
TiO of the present invention2For fumed nano titanium dioxide TiO2P25 (marketing), average grain diameter are 25nm's
The titanium dioxide of anatase and brilliant red stone mixed phase.Zeolite (M) of the present invention is the modenite for being crushed to 300 mesh.
Wherein, N (CH3)4OH·5H2O is tetramethylammonium hydroxide pentahydrate, H3PtCl6·5.3H2O is chloroplatinic acid water
Close object.
2, the agent activating method of quantum carbon element light reaction
Quantum carbon element light reaction medium prepared by the present invention can keep catalysis oxidation energy in reuse for a long time
Power and activity degree, decaying are slow.But the detection at the sample detection mouth 2 in present device system, handles any of water
Index is close to before line up to standard, and quantum carbon element light reaction medium will be recycled all, the medium more renewed.The quantum carbon of recycling
Plain light reaction medium carries out activation.Activation process step is as follows:
(1) the quantum carbon element light reaction medium of recycling and deionized water are placed in ultrasonic container in the ratio of 1:3, side
Stirring side carries out processing 1 hour with the ultrasonic wave of 25KHz frequency；
(2) filter out water adds the deionized water of new same amount to continue stirring ultrasonic treatment 1 hour again；
(3) method for repeating (1) and (2) is filtered dry afterwards three times, 100 DEG C of oven dryings；
(4) dry medium is placed in the Muffle furnace of 380 DEG C of oxygen-free atmospheres, is calcined 4 hours；
(5) grinding is sized to 200 mesh to the product between 300 mesh after cooling
Quantum carbon element light reaction medium after being activated using the above method can still keep 95% or more catalysis oxidation
Activity.
Six, implementation result
For the solution of the present invention, analysis verifying is carried out to above-mentioned implementation result with two case histories herein.It is specific to be situated between
It continues as follows.
Embodiment 1
Certain plating organic oil ink factory, the factory production waste water are 300 ton/days, the Waste Water Centralized that production line each unit generates
It collects, is uniformly processed.Influent quality indices and treatment effect, as shown in the table:
Organic oil ink factory's water treatment effect and medium circulation statistical data is electroplated in table 1
As shown in figure 16, specific embodiment is as follows for index comparison:
The waste water of factory enters in contaminant water purification equipment system of the invention, and quantum carbon element magnetic medium injected volume is dirt
1.2% (weight ratio) of water, quantum carbon element light reaction medium injected volume are 1.5% (weight ratio) of sewage；Superconducting magnet uses
Cryogenic magnet (such as Fig. 4-1, Fig. 4-2 superconducting magnet outline drawing), refrigerant is liquid helium, and current terminal is conveyed into superconducting bodies
Electric current 114A, temperature monitor and control are 4K, are vacuum-evacuated as 10-6hPa, magnetic field center 2T, provide high ladder for magnetic separation system
Spend magnetic field.The processing that the other various pieces of device systems preferred parameter according to the invention carries out.Processing result is completely up to standard,
Especially for 96% or more the processing removal rate of heavy metal, some is close to 100%.From treatment effect and medium circulation statistical number
According to middle display, after being repeated 20 times wastewater treatment, chemistry is needed for quantum carbon element magnetic medium and quantum carbon element light reaction medium
The removal rate of oxygen amount CODcr remains between 96%-97%；The removal rate of ammonia nitrogen is maintained between 97%-98%；Total copper
Removal rate is maintained between 98%-99%；The removal rate of total lead is maintained between 97%-99%；The removal rate of total phosphorus is maintained at
Between 97%-99%；PH stable illustrates that quantum carbon element magnetic medium and quantum carbon element light reaction medium are being assisted between 6-9
With in use, still also maintaining very high synergistic activity ability after 20 times are reused.
Embodiment 2
The reuse of certain printed circuit board plant chimney stalk is tested, which is 30 ton/days, each list of production line
The Waste Water Centralized that member generates is collected, and is uniformly processed.Influent quality indices and treatment effect, statistical data is as shown in the table,
Certain printed circuit board plant chimney stalk treatment effect and medium circulation statistical data are as shown in the table:
Certain the printed circuit board plant chimney stalk treatment effect of table 2 and medium circulation statistical data
Its Contrast on effect such as Figure 17-1, shown in Figure 17-2.Specific embodiment is as follows:
The waste water of factory enters in contaminant water purification equipment system of the invention, and quantum carbon element magnetic medium injected volume is dirt
1.0% (weight ratio) of water, quantum carbon element light reaction medium injected volume are 1.2% (weight ratio) of sewage；Device systems are other
The processing that various pieces preferred parameter according to the invention carries out.Processing result is completely up to standard, especially for improve COD and
The indexs such as ammonia nitrogen have remarkable result.It is shown from treatment effect and medium circulation statistical data, quantum carbon element magnetic medium and amount
For sub- carbon light reaction medium after being repeated 10 times wastewater treatment, the removal rate of COD CODcr is maintained at 91%-
Between 93%；The removal rate of ammonia nitrogen is maintained between 94%-97%；Turbidity is maintained between 3.2-4.4；PH stable is in 6-9
Between, illustrate quantum carbon element magnetic medium and quantum carbon element light reaction medium collaboration in use, by 10 times reuse after,
Still very high synergistic activity ability is also maintained.
Sewage of the present invention includes but is not limited to various plant emissions sewage, such as electroplate factory, printing house, chemicals
The sewage effluents such as factory, electronics industry factory, paper mill, food factory.It also include municipal sewage and daily life sewage effluent.Also
Including river water, surface water, underground water etc..The waste water can carry out concentration purified treatment by waste water treatment plant.
Pollutant in sewage of the present invention includes many kinds of substance, as chromium (Cr), arsenic (As), cadmium (Cd), zinc (Zn),
The heavy metal ion such as nickel (Ni), mercury (Hg), lead (Pb).Further include organic substance, lead to COD (COD), BOD (biology
Oxygen demand) and the raised substance of TOC (total organic carbon) index.These substances only as an example, but are not limited only to this, further include ratio
Such as special chemical structure of bacterium, virus.
Specific embodiment described herein is only an example for the spirit of the invention.The neck of technology belonging to the present invention
The technical staff in domain can make various modifications or additions to the described embodiments or replace by a similar method
In generation, however, it does not deviate from the spirit of the invention or beyond the scope of the appended claims.
Claims (7)
1. a kind of superconduction sewage-treatment plant characterized by comprising Magneto separate tank body (7), superconducting magnet (6)；Wherein:
The Magneto separate tank body (7) is located in the field region of superconducting magnet (6), is internally provided with hinge joint in the gold on driving wheel
Belong to link network, the metal link network extends at least partially into two skies being oppositely arranged on magnetic medium extraction mechanism (8) and blows the trumpet mouth
Between；One of sky blows the trumpet mouth as positive pressure, another sky blows the trumpet mouth as negative pressure；
The superconducting magnet (6) includes: superconducting bodies (6-4), and superconducting bodies (6-4) are internally provided with vaccum exhaust outlet (6-8)
With current terminal (6-5), refrigerant inlet (6-6), refrigerant exit (6-7)；
The metal link network includes multiple horizontal axis, and the end of adjacent horizontal axis is connected by chain link, is provided with chain wire side on horizontal axis, should
Chain wire side is entwined in three dimensions by chain silk is wavy.
2. a kind of superconduction sewage-treatment plant according to claim 1, which is characterized in that the superconducting magnet (6) is low
Temperature superconductive magnet, refrigerant are liquid helium, and current terminal (6-5) conveying electric current into superconducting bodies (6-4) is 114A, temperature monitoring control
System is 4K, is vacuum-evacuated as 10-6hPa, magnetic field center 2T.
3. a kind of superconduction sewage-treatment plant according to claim 1, which is characterized in that further include: blending tank (3),
In, be provided with medium dispensing port on the blending tank (3), the outlet of the blending tank (3) and the Magneto separate tank body (7) into
Liquid mouth is connected.
4. a kind of superconduction sewage-treatment plant according to claim 1, which is characterized in that the sky of negative pressure blow the trumpet mouth connection
Several solid-gas separators.
5. a kind of superconduction sewage-treatment plant according to claim 1, which is characterized in that further include: organic decomposition device,
Wherein:
The organic decomposition device includes: the light reaction medium blending tank for mixing quantum carbon element light reaction medium, and described
The connected inside of light reaction medium blending tank is disposed with the dissolved oxygen of metal chip arrays and the different cavity of several diameters
Microvesicle generators, the Photoreactor with ultraviolet source being connected with the dissolved oxygen microvesicle generators；Wherein, the sheet metal battle array
Column include the sheet metal that several have through-hole, the through-hole Heterogeneous Permutation of each sheet metal.
6. a kind of superconduction sewage-treatment plant according to claim 1, which is characterized in that on the Magneto separate tank body (7)
It is provided with inlet, overflow port (7-1), the inlet and overflow port (7-1) are located at the two sides of the metal link network,
In, the overflow port (7-1) is connected with sample detection mouth and blending tank (3) respectively.
7. a kind of superconduction sewage water treatment method characterized by comprising the liquid to be processed of quantum carbon element magnetic medium will be mixed with
Body is passed through in the Magneto separate tank body (7) for being placed in cryogenic magnetic field region, utilizes the rotatable metal being arranged in Magneto separate tank body (7)
Link network takes the quantum carbon element magnetic medium for having adsorbed metal out of Magneto separate tank body (7), blows the trumpet mouth for quantum carbon element using sky
Magnetic medium is blown out on the net from metallic bond, is separated quantum carbon element magnetic medium from air-flow using solid-gas separator；
Also, further includes organic decomposition step, quantum carbon element light reaction medium is added specially into sewage and mixes, then to mixed
It closes liquid and carries out dissolved oxygen reaction and light reaction；Wherein, the quantum carbon element light reaction medium is light reaction Jie for including quantum carbon element
Matter mixture；In the dissolved oxygen reaction, mixed liquor is passed through into the sheet metal being arranged successively with through-hole and several diameters not
Same cavity；Wherein, the through-hole Heterogeneous Permutation of each sheet metal.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
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| CN201610874227.8A CN106277233B (en) | 2016-10-07 | 2016-10-07 | A kind of superconduction sewage-treatment plant and method |
| KR1020197002388A KR20190022739A (en) | 2016-10-07 | 2016-10-10 | Wastewater treatment method and system |
| EP16918177.3A EP3524578A4 (en) | 2016-10-07 | 2016-10-10 | Sewage treatment method and system |
| US16/339,949 US20190284072A1 (en) | 2016-10-07 | 2016-10-10 | Sewage processing method and system |
| PCT/CN2016/101620 WO2018064844A1 (en) | 2016-10-07 | 2016-10-10 | Sewage treatment method and system |
| JP2019513291A JP2019526444A (en) | 2016-10-07 | 2016-10-10 | Wastewater treatment method and system |
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| CN201610874227.8A CN106277233B (en) | 2016-10-07 | 2016-10-07 | A kind of superconduction sewage-treatment plant and method |
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| CN106904811A (en) * | 2017-03-23 | 2017-06-30 | 湖北保灵华环保科技有限公司 | One kind precipitation dewatering system and method |
| CN106881341A (en) * | 2017-03-23 | 2017-06-23 | 湖北保灵华环保科技有限公司 | A kind of heavy-metal contaminated soil leaching repairing method |
| CN106986429A (en) * | 2017-03-23 | 2017-07-28 | 湖北保灵华环保科技有限公司 | A kind of heavy-metal contaminated soil leachates processing equipment and sewage water treatment method |
| CN106881342A (en) * | 2017-03-23 | 2017-06-23 | 湖北保灵华环保科技有限公司 | A kind of heavy-metal contaminated soil drip washing repair system and method |
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