CN207418477U - A kind of emulsifying liquid waste water processing movement equipment and system - Google Patents
A kind of emulsifying liquid waste water processing movement equipment and system Download PDFInfo
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- CN207418477U CN207418477U CN201721296140.3U CN201721296140U CN207418477U CN 207418477 U CN207418477 U CN 207418477U CN 201721296140 U CN201721296140 U CN 201721296140U CN 207418477 U CN207418477 U CN 207418477U
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Abstract
The utility model discloses a kind of mobile equipment of emulsifying liquid waste water processing and system, the mobile equipment of emulsifying liquid waste water processing includes：The drive system in compartment and the movement of carrying compartment equipped with accommodating space；The De-emulsification flocculent subsystem fluidly coupled successively, air supporting subsystem, the first membrane filtration subsystem, photoelectrocatalysis subsystem, filter subsystem are equipped in accommodating space so that pending waste water is followed by De-emulsification flocculent subsystem, air supporting subsystem, the first membrane filtration subsystem, photoelectrocatalysis subsystem, filter subsystem.The utility model creatively provides a kind of portable emulsifying liquid waste water processing unit, there is good treatment effect to emulsifying liquid waste water, and the mobile equipment of the utility model uses for different manufacturers, so as to reduce the free time of this movement equipment, the utilization rate of this movement equipment is improved, making house calls for mobility also improves the service experience of blowdown enterprise.
Description
Technical field
The utility model is related to sewage disposal system, espespecially a kind of emulsifying liquid waste water processing movement equipment and system.
Background technology
Emulsion is widely used in mechanical processing industry as cooling lubricant, plays cooling, lubrication, antirust, clearly
The effects that washing, while equipment attrition is reduced, improve equipment and cutting-tool's used life.Emulsion category is more, sometimes referred to as
Coolant, lubricating fluid, cutting fluid etc., after a series of recyclings, hydraulic performance decline becomes waste emulsified mixture, in addition in equipment and
Also the cleaning waste water containing substantial amounts of sump oil and emulsion can be generated in the cleaning process of place.It is main in these oil-containing emulsifying waters
Contain：Machinery oil or mineral oil, soaps, emulsifier, antifoaming agent, lubrication preservative, dissolved organic matter, metal cutting and solid
Suspended matter, certain density surfactant, stabilizer and oil emulsion, with oil content is high, COD concentration is high, stability is high, no
The characteristics of destructible, intractability is big.
Oil-containing emulsifying water, which is such as discharged into environment, can cause great environmental pollution, for large-scale enterprise, generate
Wastewater flow rate it is more, can build alone the waste water processing system handled after discharge or carried out after being mixed with other waste water
Processing；But for some medium-sized and small enterprises, since its waste water yield is few, if building the processing system of the waste water alone,
Since the intractability of emulsion is high, water is few, but system cost is expensive；Cause most medium-sized and small enterprises are powerless to undertake at sewage
The construction of reason system and its maintenance cost；Therefore the waste emulsified mixture processing of these enterprises is mainly voluntarily collected by Chan Fei enterprises
Storage, wait have it is a certain amount of after recommit it is qualified disposal unit handled.Following bad phenomenon is caused as a result,：One, when long
Between storage, the waste water is caused to generate stench, influences the working environment of on-site；Two, to save cost of sewage disposal and guarantor
The works fine environment of on-site is demonstrate,proved, untreated sewage is stealthily discharged in the risk of these enterprises, but this is clearly to violate China
Laws and regulations, and run in the opposite direction with the state basic policy in China.
Therefore, the application is directed to providing a kind of mobile equipment of emulsifying liquid waste water processing and system.
The content of the invention
The purpose of this utility model is to provide a kind of mobile equipment of emulsifying liquid waste water processing and system, creatively provides
A kind of movable type emulsifying liquid waste water processing unit, has emulsifying liquid waste water good treatment effect, and the movement of the present invention is set
It is standby to be used for different manufacturers, so as to reduce the free time of this movement equipment, the utilization rate of this movement equipment is improved, is flowed
Dynamic making house calls for property also improves the service experience of blowdown enterprise.
The technical scheme that the utility model is provided is as follows：
A kind of mobile equipment of emulsifying liquid waste water processing, including：
The drive system of compartment and carrying the compartment movement equipped with accommodating space；
The De-emulsification flocculent subsystem fluidly coupled successively, air supporting subsystem, the first membrane filtration are equipped in the accommodating space
Subsystem, photoelectrocatalysis subsystem, filter subsystem so that pending waste water is followed by the De-emulsification flocculent subsystem, institute
State air supporting subsystem, the first membrane filtration subsystem, the photoelectrocatalysis subsystem, the filter subsystem.
In the technical program, first emulsifying liquid waste water is carried out by De-emulsification flocculent subsystem to be effectively demulsified and flocculate；
Then the oil reservoir (and/or floating material) that waste water is effectively realized by air supporting subsystem is separated with waste water, so as to realize greasy dirt
While layering with waste water, the part COD in waste water is also reduced；Then waste water again by photoelectrocatalysis subsystem, (urge by photoelectricity
It is by applying electric field to change (PEC) water technology, makes electrode and electric charge transfer (such as calcium, magnesium, organic on electrolyte interface
Object) and accelerate a kind of catalytic action of reaction, including depositing, polymerizeing, redox and decomposition reaction.Pass through capacity substrate surface
Catalysis material apply electric field or illumination, anode catalysis material is formed on its surface after absorbing electric energy or luminous energy with electron hole
It is right, highly reactive form of oxygen, hydroxyl etc. are formed after oxygen reaction in vivo with water, the in vivo oxidation operation of water can be polymerize or be decomposed
Into inorganic matter (water+carbon dioxide), the decomposition such as chlorine root, sulfate ion are oxidized to hypochlorous acid, chlorine, sulfur dioxide etc..In electricity
Under field action, cathode surface can then deposit the solids such as calcium, magnesium, sulphur, nickel, copper, chromium, zinc.It, can be effective using photoelectricity collective effect
Remove the heavy metal ion such as calcium, magnesium, nickel, copper, chromium, zinc in water removal, and oxygenolysis organic matter and chlorion etc., reduce water COD,
Colourity, turbidity, ammonia nitrogen, phosphorus, cyanide etc.) further carry out COD, colourity, turbidity, ammonia nitrogen, phosphorus in reduction waste water etc.；Finally
Waste water is filtered processing so that waste water reach general factory and enterprise discharge index (national discharge index, industry discharge refers to
Mark etc.) or according to the demand of owner by wastewater treatment to the requirement of recycling.
More preferably, the technical program creatively provides a kind of portable emulsifying liquid waste water processing unit, is suitble to special
It is the less medium-sized and small enterprises of blowdown flow rate, emulsifying liquid waste water need to be only discharged into certain storage device by these enterprises, work as waste water
When reaching a certain amount of, it can be handled by there is this movement equipment and qualified waste water dis posal unit of tool.So
Discharge of wastewater enterprise need not build sewage disposal device, and so as to substantially reduce its waste water dis posal cost, and this movement equipment can be with
It cries with to waste water dis posal unit also according to customer demand or can improve waste water treatment efficiency, and one time wastewater treatment can configure simultaneously
More playscripts with stage directions move equipment, and for large enterprise, mixed processing is carried out without to emulsifying liquid waste water and other waste water, so as to
Add the processing cost or process flow of other waste water；The breast that large enterprise individually can also generate it by this movement equipment
Change liquid and carry out storage post processing, and then reduce the totle drilling cost of its wastewater treatment and the occupied place space of wastewater treatment.It is more excellent
Ground, this movement equipment use for different manufacturers, so as to reduce the free time of this movement equipment, improve this movement equipment
Utilization rate, making house calls for mobility also improve the service experience of blowdown enterprise.
It is further preferred that further including control subsystem, communicate and connect with the De-emulsification flocculent subsystem.
In the technical program, the working condition of De-emulsification flocculent subsystem is controlled by control subsystem, such as the throwing of demulsifier
The dispensing with flocculant is put, reduces the input of cost of labor, so as to improve the intelligence of this movement equipment and automation.
It is further preferred that the water inlet for further including to detect pending waste water detects subsystem, with control
System communication connects；And/or detect subsystem for detecting the water outlet through the filter subsystem treated pending waste water
System is communicated with the control subsystem and connected.
In the technical program, water inlet detection subsystem is obtained by control subsystem and/or water outlet detects subsystem and detects
The data arrived, and the dispensing of the demulsifier, flocculant according to these data control De-emulsification flocculent subsystem, so as to ensure this movement
The water treatment effect of equipment, to meet the requirement of client.
It is further preferred that the De-emulsification flocculent subsystem includes mixer, demulsifier dispenser and flocculant dispenser,
Along the flow direction of pending waste water, the demulsifier dispenser and the flocculant dispenser are sequentially arranged in the mixer
Place；And/or the first reflux subsystem is equipped between the filter subsystem and the air supporting subsystem；And/or the air supporting
Subsystem is molten gas-gas float system, including air-floating apparatus and feeder, between the air-floating apparatus and the feeder
Equipped with the second reflux subsystem.
In the technical program, after first dispensing demulsifier carries out demulsification processing to waste water, then flocculant is launched in waste water
Pollutant effectively gather, flocculates, convenient for the layering of oil reservoir and waste water in subsequent air-flotation process and part COD
Removal.
In the technical program, (emission request is recycled and wanted waste water not up to requirement after filtered subsystem processes
Ask when) when, can will be reprocessed in the return of waste water after filtered subsystem processes to air supporting subsystem, to ensure this movement
Treated that waste water can reach requirement for equipment, ensures the treatment efficiency of this movement equipment.
In the technical program, air supporting subsystem is preferably that molten gas-gas is floated, and is pressure air-dissolving-air supporting, and then will be through air supporting
Device treated a part of Sewage treatment pressurizes and is supplied in air-floating apparatus to after mixing with the gases in feeder,
So as to ensure treatment effect that molten gas-gas is floated.
It is further preferred that further including exhaust-gas treatment subsystem, urged respectively with the air supporting subsystem and the photoelectricity
Sub-systems fluidly couple；And/or first promoted subsystem, be used for by pending emulsion be promoted to it is described demulsification wadding
Solidifying subsystem；And/or oily collection subsystem, it is connected with the air supporting subsystem；And/or deposit collection subsystem,
Connect respectively with the air supporting subsystem, the first membrane filtration subsystem, the photoelectrocatalysis subsystem, the filter subsystem
It connects；And/or buffering subsystem, fluidly couple with the filter subsystem, handled for storing through the filter subsystem
Water outlet afterwards；And/or the second membrane filtration subsystem, after being arranged on the filter subsystem along the flow direction of pending waste water
Side.
In the technical program, in order to avoid the pollution exhaust gas generated in sewage disposal process is stored in each equipment,
And then influence the work efficiency in each equipment or even cause undesirable safety consequences (such as equipment explosion), but if directly
The exhaust gas generated in each equipment is directly discharged in environment, then is polluted the environment, ecological environment is destroyed, influences human body
Health, therefore, this movement equipment are provided with exhaust-gas treatment subsystem, and processing heel row is carried out to the exhaust gas generated in each equipment
It puts, environmental protection, respective country policy.
In the technical program, in order to ensure that this movement equipment is applicable in the storage device of the waste water of different enterprises, this movement is set
It is standby also to have provided lifting system for oneself, when the hydraulics deficiency between storage device and De-emulsification flocculent subsystem, promotion can be passed through
System will be handled in waste water lifting to De-emulsification flocculent subsystem.
In the technical program, collect being separated in air supporting subsystem by oil recycling subsystem and be located above waste water
Oil reservoir and floating material, convenient for the processing subsequently to waste water.
In the technical program, air supporting subsystem, the first membrane filtration subsystem, light are collected by deposit collection subsystem respectively
The sediment that electro-catalysis subsystem, filter subsystem generate, so as to ensure the wastewater treatment efficiency of entirely mobile equipment, and in time
The sediment in above-mentioned subsystem is discharged, avoids influencing air flotation effect, membrane filtration effect, photoelectrocatalysis effect due to sediment is excessive
Fruit, filter effect.
In the technical program, the direct discharge of the waste water after being filtered in order to avoid filtered device, this mobile device is also set
Buffering subsystem is put, for storing the water outlet after filtered subsystem processes, with stabilizing water outlet quality.
In the technical program, in order to meet the different requirements of client (recycling requirement, discharging standards, industry discharge mark
It is accurate), this movement equipment is also provided with the second membrane filtration subsystem, to continue with the waste water from filter subsystem processing, makes waste water
Reach requirement.
The utility model additionally provides a kind of emulsifying liquid waste water processing system, including：
It is equipped with successively along the flow direction of pending waste water：
Mixer is equipped with demulsifier dispenser and flocculant at the mixer successively along the flow direction of pending waste water
Dispenser；
Air-floating apparatus；
First membrane-filtering unit；
Photoelectrocatalysidevice device；And
Filter device.
In the technical program, first emulsifying liquid waste water is carried out by De-emulsification flocculent subsystem to be effectively demulsified and flocculate；
Then the oil reservoir (and/or floating material) that waste water is effectively realized by air supporting subsystem is separated with waste water, so as to realize greasy dirt
While layering with waste water, the part COD in waste water is also reduced；Then waste water again by photoelectrocatalysis subsystem, (urge by photoelectricity
It is by applying electric field to change (PEC) water technology, makes electrode and electric charge transfer (such as calcium, magnesium, organic on electrolyte interface
Object) and accelerate a kind of catalytic action of reaction, including depositing, polymerizeing, redox and decomposition reaction.Pass through capacity substrate surface
Catalysis material apply electric field or illumination, anode catalysis material is formed on its surface after absorbing electric energy or luminous energy with electron hole
It is right, highly reactive form of oxygen, hydroxyl etc. are formed after oxygen reaction in vivo with water, the in vivo oxidation operation of water can be polymerize or be decomposed
Into inorganic matter (water+carbon dioxide), the decomposition such as chlorine root, sulfate ion are oxidized to hypochlorous acid, chlorine, sulfur dioxide etc..In electricity
Under field action, cathode surface can then deposit the solids such as calcium, magnesium, sulphur, nickel, copper, chromium, zinc.It, can be effective using photoelectricity collective effect
Remove the heavy metal ion such as calcium, magnesium, nickel, copper, chromium, zinc in water removal, and oxygenolysis organic matter and chlorion etc., reduce water COD,
Colourity, turbidity, ammonia nitrogen, phosphorus, cyanide etc..) further carry out COD, colourity, turbidity, ammonia nitrogen, phosphorus in reduction waste water etc.；Most
Waste water is filtered processing afterwards so that waste water reaches the discharge index of general factory and enterprise or incited somebody to action according to the demand of owner
Wastewater treatment to recycle requirement.
It is further preferred that further including control subsystem, thrown respectively with the demulsifier dispenser and the flocculant
Put device communication connection.
In the technical program, the working condition of De-emulsification flocculent subsystem is controlled by control subsystem, such as the throwing of demulsifier
The dispensing with flocculant is put, reduces the input of cost of labor, so as to improve the intelligence of this movement equipment and automation.
It is further preferred that further include into water detection device, communicate and connect with the control subsystem, for detect into
The flooding parameter of pending waste water before entering the mixer.
In the technical program, the data that detection subsystem detects of intaking are obtained by control subsystem, and according to these
The dispensing of the demulsifier, flocculant of data control De-emulsification flocculent subsystem, so as to ensure the water treatment effect of this movement equipment,
To meet the requirement of client.
It is further preferred that further include the first reflux subsystem, respectively with the filter device and the air-floating apparatus
Fluidly couple；Water outlet detection device is used to detecting the filter device treated the water outlet parameter of pending waste water；
The control subsystem connects respectively with the described first reflux subsystem and water outlet detection device communication.
In the technical program, the system is obtained treated the data of waste water by control subsystem, and according to these numbers
It is judged that treated, whether waste water needs to be back in air-floating apparatus to be reprocessed, and then ensures the processing effect of the system
Can, to meet the different requirement of client.
It is further preferred that further including the second membrane-filtering unit, the filtering is arranged on along the flow direction of pending waste water
The rear of device；And/or buffer storage, along the flow direction of pending waste water arranged on the rear of the filter device；With/
Or, oil collector sump tank, it is arranged at the air-floating apparatus；And/or emission-control equipment, respectively with the air-floating apparatus, described
Photoelectrocatalysidevice device connects；And/or deposit collection device, respectively with the air-floating apparatus, first membrane-filtering unit,
The filter device connection.
In the technical program, in order to meet the different requirements of client (recycling requirement, discharging standards, industry discharge mark
It is accurate), this movement equipment is also provided with the second membrane-filtering unit, to continue with the waste water from filter subsystem processing, reaches waste water
To requirement.
In the technical program, the direct discharge of the waste water after being filtered in order to avoid filtered device, this mobile device is also set
Buffering subsystem is put, for storing the water outlet after filtered subsystem processes, with stabilizing water outlet quality.
In the technical program, oil reservoir being separated in air-floating apparatus and above waste water is collected by oil collector sump tank
And floating material, convenient for the processing subsequently to waste water.
In the technical program, in order to avoid the pollution exhaust gas generated in sewage disposal process is stored in each equipment,
And then influence the work efficiency in each equipment or even cause undesirable safety consequences (such as equipment explosion), but if directly
The exhaust gas generated in each equipment is directly discharged in environment, then is polluted the environment, ecological environment is destroyed, influences human body
Health, therefore, this movement equipment are provided with exhaust-gas treatment subsystem, and processing heel row is carried out to the exhaust gas generated in each equipment
It puts, environmental protection, respective country policy.
In the technical program, air supporting subsystem, the first membrane filtration subsystem, light are collected by deposit collection subsystem respectively
The sediment that electro-catalysis subsystem, filter subsystem generate, so as to ensure the wastewater treatment efficiency of entirely mobile equipment, and in time
The sediment in above-mentioned subsystem is discharged, avoids influencing air flotation effect, membrane filtration effect, photoelectrocatalysis effect due to sediment is excessive
Fruit, filter effect.
A kind of emulsifying liquid waste water processing movement equipment and system provided by the utility model, can bring following at least one
Advantageous effect：
1st, during this practicality is new, first emulsifying liquid waste water is carried out by De-emulsification flocculent subsystem to be effectively demulsified and flocculate；
Then the oil reservoir (and/or floating material) that waste water is effectively realized by air supporting subsystem is separated with waste water, so as to realize greasy dirt
While layering with waste water, the part COD in waste water is also reduced；Then waste water again by photoelectrocatalysis subsystem, (urge by photoelectricity
It is by applying electric field to change (PEC) water technology, makes electrode and electric charge transfer (such as calcium, magnesium, organic on electrolyte interface
Object) and accelerate a kind of catalytic action of reaction, including depositing, polymerizeing, redox and decomposition reaction.Pass through capacity substrate surface
Catalysis material apply electric field or illumination, anode catalysis material is formed on its surface after absorbing electric energy or luminous energy with electron hole
It is right, highly reactive form of oxygen, hydroxyl etc. are formed after oxygen reaction in vivo with water, the in vivo oxidation operation of water can be polymerize or be decomposed
Into inorganic matter (water+carbon dioxide), the decomposition such as chlorine root, sulfate ion are oxidized to hypochlorous acid, chlorine, sulfur dioxide etc..In electricity
Under field action, cathode surface can then deposit the solids such as calcium, magnesium, sulphur, nickel, copper, chromium, zinc.It, can be effective using photoelectricity collective effect
Remove the heavy metal ion such as calcium, magnesium, nickel, copper, chromium, zinc in water removal, and oxygenolysis organic matter and chlorion etc., reduce water COD,
Colourity, turbidity, ammonia nitrogen, phosphorus, cyanide etc..) further carry out COD, colourity, turbidity, ammonia nitrogen, phosphorus in reduction waste water etc.；Most
Waste water is filtered processing afterwards so that waste water reaches discharge index (national discharge index, the industry discharge of general factory and enterprise
Index etc.) or according to the demand of owner by wastewater treatment to the requirement recycled.
2nd, during this practicality is new, a kind of portable emulsifying liquid waste water processing unit is creatively provided, is suitble to particularly arrange
Less medium-sized and small enterprises are measured in dirt, and emulsifying liquid waste water need to be only discharged into certain storage device by these enterprises, when waste water reaches
When a certain amount of, it can be handled by there is this movement equipment and qualified waste water dis posal unit of tool.Such waste water
Discharge enterprise need not build sewage disposal device, so as to substantially reduce its waste water dis posal cost, and this movement equipment can with cry with
It arrives, waste water dis posal unit also according to customer demand or can improve waste water treatment efficiency, and one time wastewater treatment can configure more simultaneously
This movement equipment for large enterprise, carries out mixed processing, so as to increase without to emulsifying liquid waste water and other waste water
The processing cost or process flow of other waste water；The emulsion that large enterprise individually can also generate it by this movement equipment
Storage post processing is carried out, and then reduces the totle drilling cost of its wastewater treatment and the occupied place space of wastewater treatment.More preferably, originally
Mobile equipment uses for different manufacturers, so as to reduce the free time of this movement equipment, improves the profit of this movement equipment
With rate, making house calls for mobility also improves the service experience of blowdown enterprise.
3rd, during this practicality is new, the flooding parameter that is detected online according to water inlet detection subsystem by control system, to broken
The dispensing of emulsion and flocculant is controlled, so as to while the treatment efficiency of this product is ensured, can also be achieved the essence of medicament
It really launches, so as to save medicament, while the intelligence and automation of medicament delivery is realized, saves cost for wastewater treatment.
More preferably, control system can also detect the water outlet parameter that subsystem detects according to water outlet, further control demulsifier and flocculation
The dispensing of agent, the reprocessing that can also be discharged and flowed back to water outlet according to water outlet parameter carry out intelligent, automation control.
4th, during this practicality is new, discharges, make again after also the exhaust gas that can generate the equipment for polluting exhaust gas is collected and is handled
Obtain the environmental protection policy of the product active response country of the utility model.
5th, during this practicality is new, the sludge of the equipment also to that can generate deposit is collected and handled, so as to effectively keep away
Exempt to influence air flotation effect, membrane filtration effect, photoelectrocatalysis effect, filter effect due to sediment is excessive, and then ensure that this practicality
The treatment efficiency of new product.
Description of the drawings
Below by a manner of clearly understandable, preferred embodiment is described with reference to the drawings, emulsifying liquid waste water processing is moved
Above-mentioned characteristic, technical characteristic, advantage and its realization method of equipment and system are further described.
Fig. 1 is a kind of example structure schematic diagram of the mobile equipment of emulsifying liquid waste water processing of the utility model；
Fig. 2 is the first example structure schematic diagram of the utility model emulsion waste water treatment process；
Fig. 3 is the emulsion breaking principle schematic diagram of the organic high molecular compound based on natural materials of the utility model.
Drawing reference numeral explanation：
1. collecting pit, 2. demulsifier dispensers, 3. mixers, 4. air-floating apparatus, 5. first membrane-filtering units, 6. filtering ponds,
7. feeder, 8. photoelectrocatalysidevice devices, 9. filter devices, 10. oil collector sump tanks, 11. deposit collection devices, 12. flocculants
Dispenser, 13. clear water reserviors, 14. power control cabinets, 15. compartments, 151. accommodating spaces.
Specific embodiment
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, attached drawing will be compareed below
Illustrate specific embodiment of the present utility model.It should be evident that the accompanying drawings in the following description is only the one of the utility model
A little embodiments, for those of ordinary skill in the art, without creative efforts, can also be according to these
Attached drawing obtains other attached drawings, and obtains other embodiments.
To make simplified form, in each figure only schematically show with the relevant part of the utility model, they are simultaneously
Its practical structures as product is not represented.In addition, so that simplified form readily appreciates, have in some figures identical structure or
The component of function only symbolically depicts one of those or has only marked one of those.Herein, "one" is not
It only represents " only this ", can also represent the situation of " more than one ".
In embodiment one, as depicted in figs. 1 and 2, a kind of mobile equipment of emulsifying liquid waste water processing, including：Equipped with accommodating
The drive system that the compartment 15 and carrying compartment 15 in space 151 move；It is equipped in accommodating space 151 and fluidly couples successively
De-emulsification flocculent subsystem (not indicated in figure), air supporting subsystem (not indicated in figure), the first membrane filtration subsystem (do not mark in figure
Show), photoelectrocatalysis subsystem (not indicated in figure), filter subsystem (not indicated in figure) so that pending waste water followed by
De-emulsification flocculent subsystem, air supporting subsystem, the first membrane filtration subsystem, photoelectrocatalysis subsystem, filter subsystem.
The technique collection that will there is good treatment effect to pollutants such as colourity, ammonia nitrogen, total phosphorus, COD of the invention
It is especially suitable but be not only applicable in emulsifying liquid waste water into, being applicable in the waste water containing COD higher together, other contents containing COD compared with
High sanitary sewage, dyeing and printing sewage or even industrial wastewater is also suitable, but should be all belonged to the scope of protection of the present invention.
First emulsifying liquid waste water is carried out by De-emulsification flocculent subsystem to be effectively demulsified and flocculate；Then air supporting is passed through
The oil reservoir (and/or floating material) that system effectively realizes waste water separates and the preliminary removal of COD etc. with waste water, so as in reality
While existing greasy dirt is layered with waste water, part COD in waste water etc. is also reduced；Then waste water passes through photoelectrocatalysis subsystem again
(photoelectrocatalysis (PEC) water technology be by applying electric field, make electrode on electrolyte interface electric charge transfer (such as calcium,
Magnesium, organic matter) and accelerate a kind of catalytic action of reaction, including depositing, polymerizeing, redox and decomposition reaction.Pass through capacitance
The catalysis material of substrate surface applies electric field or illumination, and being formed on its surface after anode catalysis material absorption electric energy or luminous energy has
Electron hole pair forms highly reactive form of oxygen, hydroxyl etc. after oxygen reaction in vivo with water, can gather the in vivo oxidation operation of water
Inorganic matter (water+carbon dioxide) is closed or resolves into, the decomposition such as chlorine root, sulfate ion are oxidized to hypochlorous acid, chlorine, sulfur dioxide
Deng.Under electric field action, cathode surface can then deposit the solids such as calcium, magnesium, sulphur, nickel, copper, chromium, zinc.Made jointly using photoelectricity
With, the heavy metal ion such as calcium in water, magnesium, nickel, copper, chromium, zinc, and oxygenolysis organic matter and chlorion etc. can be effectively removed, drop
COD, colourity, turbidity, ammonia nitrogen, phosphorus, cyanide of low water etc.) further carry out COD, colourity, turbidity, ammonia in reduction waste water
Nitrogen, phosphorus etc.；Waste water is finally filtered processing so that waste water reach general factory and enterprise discharge index (country discharge refers to
Mark, industry discharge index etc.) or according to the demand of owner by wastewater treatment to the requirement recycled.
It is worth noting that in practical applications, since subsystems are integrated in the accommodating space 151 in compartment 15
It is interior, it therefore,, only need to be by this movement equipment without being pre-processed (such as PH adjustings) to pending waste water when handling waste water
Leave for enterprise for storing at the collecting pit 1 of waste water, and piping directly banishes the waste water in collecting pit 1 to De-emulsification flocculent
In system, the processing of waste water can be realized, staff is assembled, use is non-without transportation processing equipment without scene
Normal facility, and the time is saved, processing time is substantially reduced, improves the treatment effeciency of waste water；Easy to operate, easy realization；
It is also operable without professional knowledge, general staff and more for wastewater flow rate in collecting pit 1, and enterprise needs quickly
What processing was completed, it can be handled simultaneously by this movement equipment of more (two or more).More preferably, this movement equipment for
Different manufacturers use, and so as to reduce the free time of this movement equipment, improve the utilization rate of this movement equipment, mobility
And on call make house calls also improves the service experience of blowdown enterprise.
In embodiment two, as depicted in figs. 1 and 2, on the basis of embodiment one, De-emulsification flocculent subsystem includes mixing
Device 3, demulsifier dispenser 2 and flocculant dispenser 12, along the flow direction of pending waste water, demulsifier dispenser 2 and flocculation
Agent dispenser 12 is sequentially arranged at mixer 3.In order to reduce occupied space of the mixer 3 in compartment 15, mixer 3 is preferably
Pipe-like mixer 3, and the duct-like mixer 3 be made of a bend pipe containing multiple turnings or by more straight tubes according to
Secondary series connection is folded to be set to be formed.
Preferably, control subsystem (not indicated in figure) is further included, control subsystem connects with the communication of De-emulsification flocculent subsystem
It connects；Control subsystem includes a power control cabinet 15, and power control cabinet 15 is equipped with human-computer interaction interface, and staff can pass through human-computer interaction
Dispensing of the interface to the demulsifier dispenser 2 and flocculant dispenser 12 that are arranged in the De-emulsification flocculent subsystem in compartment 15
Amount is monitored and operates, i.e., staff can set demulsifier and flocculation according to the influent quality situation of pending waste water
The injected volume of agent.And the current injected volume of demulsifier and flocculant, remaining total amount can be also shown on human-computer interaction interface, may be used also
Show the parameters such as the present flow rate of pending waste water, and staff can also be controlled according to the effluent quality situation of pending waste water
Flow parameter of pending waste water etc. is made, to ensure the treatment effect of this movement equipment.Preferably, control subsystem also with air supporting
One or more of subsystem, photoelectrocatalysis subsystem, filter subsystem communication connection so that staff can be by man-machine
The keying of interactive interface control subsystems and the setting of other parameters (pressure in such as air supporting subsystem).
In embodiment three, as depicted in figs. 1 and 2, on the basis of embodiment one or two, further include to detect and wait to locate
The water inlet detection subsystem (not indicated in figure) of waste water is managed, preferably communicates and connects with control subsystem；It is filtered for detecting
The water outlet detection subsystem of pending waste water after subsystem processes, communicates with control subsystem and connects.This movement equipment is led to
It crosses control subsystem and obtains the data that water inlet detection subsystem and/or water outlet detection subsystem detect, and according to these data
Demulsifier, the injected volume of flocculant of De-emulsification flocculent subsystem are controlled, it is achieved thereby that this movement equipment is intelligent and automatic
Change adjustment and control, it is ensured that the water treatment effect of this movement equipment, to meet the requirement of client.Such as when water inlet detects subsystem
The flooding parameter that system detects, at this point, control subsystem automatically configures the dispensing of demulsifier, flocculant according to these flooding parameters
Amount.In practical applications, staff first passes through the detection into water detection subsystem before handling pending waste water
Probe is detected it, and then control subsystem can configure the injected volume of corresponding demulsifier, flocculant.In wastewater treatment
In the process, staff not can take out detection probe.It is worth noting that in practical applications, staff
Also can flooding parameter be obtained by manual operation, and the setting of the injected volume of medicament is set according to flooding parameter, by artificial
Medicament delivery amount on demulsifier dispenser 2 and flocculant dispenser 12 is directly set or is set by human-computer interaction interface
, but should all belong to the scope of protection of the present invention interior.
Preferably, the alarm of the remaining total amount of demulsifier and flocculant is also provided on human-computer interaction interface, when broken
When emulsion, the content of flocculant are inadequate, control subsystem sends alarm, and staff is in demulsifier dispenser 2, flocculant for warning
Dispenser 12 adds demulsifier, flocculant.Since each processing subsystem is respectively positioned on inside compartment 15, for the ease of work
Make the operation of personnel, the wall surface in compartment 15 should be provided with action pane in position, as human-computer interaction interface is arranged on compartment
On 15, but its exterior space towards compartment 15 is configured, and certainly, in order to protect control subsystem, human-computer interaction interface is excellent
It elects as and is embedded in compartment 15, and the outside of human-computer interaction interface is preferably provided with protection structure (such as covering, baffle), avoids it
It is subject to external environmental interference or destroys (such as maloperation of rainy weather, staff), and for the ease of observing human-computer interaction
Interface, protection structure is preferably that transparent material is made.Certainly, human-computer interaction interface can be also set directly in driver's cabin.
In example IV, as depicted in figs. 1 and 2, on the basis of embodiment one, two or three, exhaust-gas treatment is further included
Subsystem (does not indicate) in figure, and exhaust-gas treatment subsystem fluidly couples respectively with air supporting subsystem and photoelectrocatalysis subsystem,
The air supporting subsystem of this movement equipment is preferably molten gas-gas float system, including air-floating apparatus 4 and feeder 7.Preferably,
Between air-floating apparatus 4 and feeder 7 be equipped with second reflux subsystem (i.e. this dissolved-gas-air supporting subsystem be preferably pressure air-dissolving-
Air supporting subsystem).Since during air supporting, oxidation reaction can occur for the pollutant (organic pollution, ammonia nitrogen etc.) in waste water,
Since the degradation of pollutant can generate the toxic gas, corrosive gas, flammable explosive gas of part during this, in order to avoid
These pernicious gases can be discharged into environment and pollute environment, and the subsystem for generating pernicious gas preferably carries out in the enclosed space,
And the pernicious gas that these subsystems generate is delivered to after exhaust-gas treatment subsystem handled by this movement equipment by pipeline
It discharges again.Wherein exhaust-gas treatment subsystem is preferably activated carbon adsorption system, and certain exhaust-gas treatment subsystem can be according to its processing
The water quality parameter of waste water select different processing system, if the reducibility gas in pernicious gas is more, at exhaust gas
It is preferably oxidizing treatment system to manage subsystem, is discharged again after pernicious gas is aoxidized；If the oxidisability gas in pernicious gas
When body is more, then exhaust-gas treatment subsystem is preferably reproducibility processing system, is discharged again after pernicious gas is reduced；It is if harmful
When gas contains reducibility gas and oxidizing gas simultaneously, then reprocess after being mixed, finally discharge again.
Preferably, the first membrane filtration subsystem is preferably ceramic membrane (micron order or nanoscale), and the ceramic membrane is preferably plate
Shape structure or tubular structure.During air supporting, waste water can be because of the continuous release high pressure gas in the air feeding tube road for being arranged on bottom
Body and constantly turn over and gush, and with the rising of gas, the larger suspended matter of oleaginous material or specific surface area in waste water can be because of gas
Rising and float to the top of air supporting subsystem, and then realize oil reservoir separation, in order to avoid because influencing the steady of oil reservoir during air supporting
It is qualitative, cause the not easily collecting of oil reservoir, for the present invention preferably by ceramic micron air-floating apparatus, which is in net
Shape or array arrangement are in the bottom of air flotation zone.Preferably, control subsystem is also led to the reflux subsystem of feeder 7 and second
News connection, in this way, staff can set the reflux of air supporting pressure and the second reflux subsystem by human-computer interaction interface
Than controlling and adjusting oil reservoir separating effect, the water surface situation of air supporting subsystem is run through for the ease of staff, compartment 15
The optimum position of wall surface is equipped with transparent windows.
It is further preferred that in order to recycle the oil reservoir generated in air supporting subsystem in time, and then reduce subsequent wastewater treatment
Load, the side of air supporting subsystem is preferably also provided with oily collection subsystem, and oily collection system is included arranged on air supporting subsystem
The scraping plate of automatic device of top and the Fuel Tanking Unit for storing oil reservoir, wherein scraping plate of automatic device are preferably with controlling subsystem
System communication connection, staff can set scraping plate of automatic device to scrape the interval time of oil reservoir by human-computer interaction interface.Into one
Preferably, Fuel Tanking Unit is additionally provided with branch to step, which is used for the preliminary collection of the oil reservoir in collecting pit 1.
In embodiment five, as depicted in figs. 1 and 2, on the basis of embodiment one, two, three or four, deposit is further included
Collection subsystem (does not indicate) in figure, respectively with air supporting subsystem, photoelectrocatalysis subsystem, the first membrane filtration subsystem, filtering
Subsystem connects, since air supporting subsystem, photoelectrocatalysis subsystem, the first membrane filtration subsystem, filter subsystem are in filtered wastewater
When can generate sludge (i.e. deposit), and the presence of sludge can influence it where subsystem operational effect, therefore, at waste water
During reason, regularly recycling the sludge generated in subsystems is necessary.
In embodiment six, as depicted in figs. 1 and 2, on the basis of embodiment one, two, three, four or five, is further included
Two membrane filtration subsystems (not indicated in figure) are arranged on the rear of filter subsystem along the flow direction of pending waste water.Certainly,
Two membrane filtration subsystems may also be arranged on the front of filter subsystem, and positioned at the rear of photoelectrocatalysis subsystem.By adding
Two membrane filtration subsystems, to carrying out photoelectrocatalysis, treated that waste water is reprocessed, and so as to improve the effluent quality of waste water, makes it
Meet more stringent standard of drainage (such as professional standard or recycling standard), it is preferable that originally second membrane filtration subsystem is preferably
Dish tubular type membrane technology (DT), further preferably disc tube reverse osmosis (dt-ro) membrane technology (DTRO).
In embodiment seven, as depicted in figs. 1 and 2, on the basis of embodiment one, two, three, four, five or six, further include
First promotion subsystem (does not indicate, such as pump) in figure, is used to pending waste water being promoted to De-emulsification flocculent subsystem from collecting pit 1
System；Preferably, realized and connected by overflow manner between air supporting subsystem and photoelectrocatalysis subsystem.Certainly, when air supporting subsystem
When system and the difference in height of photoelectrocatalysis subsystem between the two can not meet overflow condition, in order to meet water conservancy item between the two
Part can set the second promotion subsystem (not indicated in figure, such as pump) between air supporting subsystem and photoelectrocatalysis subsystem.
In embodiment eight, as depicted in figs. 1 and 2, on the basis of embodiment one, two, three, four, five or six, further include
Subsystem (i.e. clear water reserviors 13) is buffered, is fluidly coupled with filter subsystem (or second membrane filtration subsystem), is passed through for storing
Filter subsystem (or second membrane filtration subsystem) water outlet that treated, and water outlet is after buffering subsystem stabilizing water quality, it can root
It is discharged or is recycled according to the requirement of client.Preferably, the detection structure of water outlet detection subsystem is arranged on buffering subsystem
At system, i.e. water outlet detection subsystem by detecting the water outlet in buffering subsystem obtains water outlet parameter.Certainly, if do not had
Buffer subsystem, then water outlet detection subsystem by (or the second membrane filtration subsystem) water outlet that treated of filtered subsystem come
Obtain water outlet parameter.
What deserves to be explained is in above-described embodiment, filter subsystem is preferably film filtering system, and preferably MBR membrane filtrations system
System, further preferably MBR microfiltration membrane systems, after the waste water after photoelectrocatalysis subsystem processes first flows through filtering ponds 6,
It is filtered by MBR microfiltration membrane systems.Further the waste water from photoelectrocatalysis subsystem out is filtered, further except useless
Colourity, ammonia nitrogen, total phosphorus, COD in water etc..
When filter subsystem (or second membrane filtration subsystem) water outlet that treated is unsatisfactory for discharging or recycles standard, then should
The water outlet for being unsatisfactory for requiring, which is preferably back in air supporting subsystem, is reprocessed；Preferably, the present invention can be by controlling subsystem
It unites to realize the intelligence and automatic management whether water outlet recycles, and staff can be according to demand (country's discharge of client
Standard, discharge standard, enterprise's recycling standard etc.) the different water outlet preset value (or water outlet preset range value) of input, such as COD
Value, turbidity value etc.).It is worth noting that can be interchangeable accordingly between above-mentioned specific film filtering system, it is not limited in
Its preferred embodiment or other film filtering systems that requirement can be reached, such as other type membrane filtration technologies：Reverse osmosis (RO), receive
(NF), ultrafiltration (UF) and micro-filtration (MF) are filtered, and membrane filtration is biological membrane filtration, chemical membrane filtration, filtered by biochemistry film, physics membrane filtration etc..
Demulsifier in above-described embodiment can be one or more combinations in organic emulsion breaker, inorganic demulsifier, such as only
Use organic emulsion breaker；Only with inorganic demulsifier；Mixing demulsifier configured in proportion with organic emulsion breaker and inorganic demulsifier etc.,
And since the species of organic emulsion breaker and inorganic demulsifier is various, demulsifier of the invention can also be a type or more
The combination of type organic emulsion breaker and inorganic demulsifier.Flocculant in above-described embodiment can be organic flocculant, inorganic wadding
One or more combinations in solidifying agent, such as only use organic flocculant；Only use inorganic flocculating agent；With organic flocculant and inorganic flocculation
Mixed flocculation agent that agent configures in proportion etc., and since the species of organic flocculant and inorganic flocculating agent is various, the present invention
Flocculant can also be the combination of a type or polytype organic flocculant and inorganic flocculating agent.
The demulsifier of the present invention is preferably based on the organic high molecular compound of natural materials, in the positive charge energy carried
With the negative electrical charge of elaioleucite outer layer being dispersed in water.It is interrupted the connection of oil and water, elaioleucite is no longer with charge, because with phase
Repulsive force with charge can disappear, and small elaioleucite is constantly met in water, form increasing elaioleucite, until the water surface is floated up to,
Oil phase can be eventually entered by ultimately forming the close oil reservoir product, the quality without influencing the water after separating.The water content of oil phase
Less than 20%, if it is desirable, can complete the water removal of oil by subsequent processing, purification can be directly used for burning and obtain energy.
It can also be combined in water layer containing a small amount of elaioleucite not reacted completely with subsequent process flow, pass through chemistry or raw
Object method removes.
Because the most COD of waste emulsified mixture is because oil generates, after grease has been efficiently separated, the range of decrease of COD exists
90% or so.Its separation process influences from pH value, does not fear the high concentration COD into water, enters that the COD of water is higher, and oil mass is higher,
Separating effect is more notable.It is compared compared with traditional chemical method demulsification, the sludge quantity of generation is very little, is greatly reduced at sludge
The expense of flow and the dangerous waste processing of reason.
Distribution and position relationship of the subsystems in compartment 15 in above-described embodiment, can be according to its size, body
Context between product and subsystem carries out rational design, and in order to adapt to the distribution of weight in compartment 15, avoids this shifting
Crank and the overturning danger triggered due to unbalance stress etc. occur in moving process for dynamic equipment, even if adjacent subsystems
Between the upper relation of no flow process may also set up together.And the component in subsystems and different system can phase
It mutually stacks together, so as to reduce the occupied space of subsystems, improves the space availability ratio in the compartment 15 of this movement equipment.
In embodiment nine, as depicted in figs. 1 and 2, a kind of emulsifying liquid waste water processing system, including：It gives up along pending
The flow direction of water is equipped with successively：Mixer 3 is equipped with demulsifier along the flow direction of pending waste water at mixer 3 and throws successively
Put device 2 and flocculant dispenser 12；Air-floating apparatus 4；First membrane-filtering unit 5；Photoelectrocatalysidevice device 8；And filter device 9.
In the present embodiment, present treatment system may be provided in the sewage disposal system of blowdown enterprise, and be preferred for handling
Emulsifying liquid waste water, certainly, it can also be used to handle other COD contents higher sanitary sewage or industrial wastewater.And present treatment system
Can its size be set according to the pollution discharge capability of enterprise, from above-described embodiment, present treatment system can be integrated in one and hold
It is placed in compartment 15, it is seen that the space of present treatment system is small, and convenient for building, and cost is relatively low, is suitble to big, medium-sized and small enterprises, right
For large enterprises, the emulsifying liquid waste water generated after being mixed with other types of waste water without reprocessing, so as to reduce this
The treatment process (or processing unit) that the other waste water of large enterprises are added due to the addition of emulsifying liquid waste water, and then realize the pin of waste water
Property is handled, reduces the whole processing cost of sewage disposal；For medium-sized and small enterprises, can certainly it be advanced by the system
Row processing, without having to worry about because emulsifying liquid waste water there are due to influence the working environment of enterprise, without risking the risk punished
Sewerage steathily.Enterprise can also set the water quality requirement of water outlet according to its needs, highly practical, applied widely.
In embodiment ten, as depicted in figs. 1 and 2, on the basis of embodiment nine, control subsystem is further included (in figure
Do not indicate), it is connected respectively with demulsifier dispenser 2 and the communication of flocculant dispenser 12；Preferably, further include to detect into water and fill
Put and (do not indicated in figure), communicate and connect with control subsystem, for detect into the pending waste water before mixer 3 into
Water parameter；The flooding parameter that control subsystem can be detected according to water inlet detection device, and set according to these flooding parameters
Demulsifier, flocculant injected volume it is default.
In embodiment 11, as depicted in figs. 1 and 2, on the basis of embodiment nine or ten, the first reflux is further included
System (does not indicate) in figure, fluidly couples with filter device 9 and air-floating apparatus 4 respectively；Water outlet detection device (is not marked in figure
Show), it is used to detecting filter device 9 treated the water outlet parameter of pending waste water；Control subsystem respectively with first time
Flow subsystem and the communication connection of water outlet detection device.Control subsystem can according to the water outlet parameter that water outlet detection device detects,
And control whether the water outlet should be refluxed reprocessing according to these flooding parameters, it is full so as to ensure the water quality requirement of water outlet
The different needs of sufficient client.
In embodiment 12, as depicted in figs. 1 and 2, embodiment nine, ten or 11 or on the basis of, further include collection
Oily device 10 is arranged at air-floating apparatus 4, for collecting the oil reservoir or floating material of 4 top of air-floating apparatus.Preferably further include
Two membrane-filtering units (do not indicate) in figure, and the rear of filter device 9 is arranged on along the flow direction of pending waste water.Preferably, also
Including buffer storage (i.e. clear water reserviors 13), the second membrane-filtering unit (or filter device is arranged on along the flow direction of pending waste water
9) rear.Preferably, emission-control equipment is further included, is connected respectively with air-floating apparatus 4, photoelectrocatalysidevice device 8.It is preferred that
Ground further includes deposit collection device 11, respectively with air-floating apparatus 4, the first membrane-filtering unit 5, filter device 9, the second membrane filtration
Device connects.
Illustratively, pending waste water quality is：Influent COD：89000ppm,
Through the utility model (not including membrane filtration subsystem (i.e. DTRO)), treated, and effluent quality is：After demulsification
COD is reduced to 21000ppm, then is reduced to 48000ppm by aeration/filtering COD, and 420ppm is down to by the processing COD of PEC
Reach cities and towns and receive pipe discharge standard (GT/B 31962-2015, COD<500ppm) within tolerance band.
Illustratively, pending waste water quality is：Influent COD：65000ppm,
Through the utility model (including membrane filtration subsystem (i.e. DTRO)), treated, and effluent quality is：The COD after demulsification
Be reduced to 12000ppm, then by aeration/filtering, COD is reduced to 6500ppm, by the processing COD of DTRO be down to 15ppm with
It is interior.
It should be noted that above-described embodiment can be freely combined as needed.The above is only the utility model
Preferred embodiment, it is noted that for those skilled in the art, do not departing from the utility model principle
On the premise of, several improvements and modifications can also be made, these improvements and modifications also should be regarded as the scope of protection of the utility model.
Claims (10)
1. a kind of mobile equipment of emulsifying liquid waste water processing, which is characterized in that including：
The drive system of compartment and carrying the compartment movement equipped with accommodating space；
De-emulsification flocculent subsystem, air supporting subsystem, the first membrane filtration subsystem fluidly coupled successively is equipped in the accommodating space
System, photoelectrocatalysis subsystem, filter subsystem so that pending waste water is followed by the De-emulsification flocculent subsystem, the gas
Float system, the first membrane filtration subsystem, the photoelectrocatalysis subsystem, the filter subsystem.
2. the mobile equipment of emulsifying liquid waste water processing according to claim 1, which is characterized in that further include：Control subsystem,
It communicates with the De-emulsification flocculent subsystem and connects.
3. the mobile equipment of emulsifying liquid waste water processing according to claim 2, which is characterized in that further include：It is treated for detecting
The water inlet detection subsystem of waste water is handled, communicates and connects with the control subsystem；
And/or
Subsystem is detected for detecting the water outlet through the filter subsystem treated pending waste water, with control
System communication connects.
4. the mobile equipment of emulsifying liquid waste water processing according to claim 1, it is characterised in that：
The De-emulsification flocculent subsystem includes mixer, demulsifier dispenser and flocculant dispenser, along the stream of pending waste water
Dynamic direction, the demulsifier dispenser and the flocculant dispenser are sequentially arranged at the mixer；
And/or
The first reflux subsystem is equipped between the filter subsystem and the air supporting subsystem；
And/or
The air supporting subsystem is molten gas-gas float system, including air-floating apparatus and feeder, the air-floating apparatus and described
The second reflux subsystem is equipped between feeder.
5. the mobile equipment of emulsifying liquid waste water processing according to claim 1-4 any one, which is characterized in that further include：
Exhaust-gas treatment subsystem fluidly couples respectively with the air supporting subsystem and the photoelectrocatalysis subsystem；
And/or
First promotes subsystem, is used to pending emulsion being promoted to the De-emulsification flocculent subsystem；
And/or
Oily collection subsystem is connected with the air supporting subsystem；
And/or
Deposit collection subsystem, it is sub with the air supporting subsystem, the first membrane filtration subsystem, the photoelectrocatalysis respectively
System, filter subsystem connection；
And/or
Subsystem is buffered, is fluidly coupled with the filter subsystem, treated through the filter subsystem for storing
Water outlet；
And/or
Second membrane filtration subsystem is arranged on the rear of the filter subsystem along the flow direction of pending waste water.
6. a kind of emulsifying liquid waste water processing system, which is characterized in that including：
It is equipped with successively along the flow direction of pending waste water：
Mixer is equipped with demulsifier dispenser along the flow direction of pending waste water at the mixer and flocculant is launched successively
Device；
Air-floating apparatus；
First membrane-filtering unit；
Photoelectrocatalysidevice device；And
Filter device.
7. emulsifying liquid waste water processing system according to claim 6, which is characterized in that further include：
Control subsystem connects respectively with the demulsifier dispenser and flocculant dispenser communication.
8. emulsifying liquid waste water processing system according to claim 7, which is characterized in that further include：
Water inlet detection device, communicates with the control subsystem and connects, and waits to locate into before the mixer for detecting
Manage the flooding parameter of waste water.
9. emulsifying liquid waste water processing system according to claim 6, which is characterized in that further include：
First reflux subsystem, fluidly couples respectively with the filter device and the air-floating apparatus；
Water outlet detection device is used to detecting the filter device treated the water outlet parameter of pending waste water；
Control subsystem connects respectively with the described first reflux subsystem and water outlet detection device communication.
10. according to the emulsifying liquid waste water processing system described in claim 6-9 any one, which is characterized in that further include：
Second membrane-filtering unit is arranged on the rear of the filter device along the flow direction of pending waste water；
And/or
Buffer storage is arranged on the rear of the filter device along the flow direction of pending waste water；
And/or
Oil collector sump tank is arranged at the air-floating apparatus；
And/or
Emission-control equipment is connected respectively with the air-floating apparatus, the photoelectrocatalysidevice device；
And/or
Deposit collection device is connected respectively with the air-floating apparatus, first membrane-filtering unit, the filter device.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109534581A (en) * | 2018-12-30 | 2019-03-29 | 南京霄祥工程技术有限公司 | A kind of Zero-discharge treating process of Cutting Liquid Wastewater |
| CN112960841A (en) * | 2021-02-07 | 2021-06-15 | 郑州航空工业管理学院 | Emergency water treatment method for sudden petroleum pollution of drinking water |
| CN113121030A (en) * | 2019-12-30 | 2021-07-16 | 山东东顺环保科技有限公司 | Oily wastewater treatment device |
-
2017
- 2017-10-10 CN CN201721296140.3U patent/CN207418477U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109534581A (en) * | 2018-12-30 | 2019-03-29 | 南京霄祥工程技术有限公司 | A kind of Zero-discharge treating process of Cutting Liquid Wastewater |
| CN109534581B (en) * | 2018-12-30 | 2022-07-12 | 大连博斯特科技有限公司 | Zero-discharge treatment process for cutting fluid wastewater |
| CN113121030A (en) * | 2019-12-30 | 2021-07-16 | 山东东顺环保科技有限公司 | Oily wastewater treatment device |
| CN112960841A (en) * | 2021-02-07 | 2021-06-15 | 郑州航空工业管理学院 | Emergency water treatment method for sudden petroleum pollution of drinking water |
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