CN108751512A - A kind of oil-water separation system - Google Patents
A kind of oil-water separation system Download PDFInfo
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- CN108751512A CN108751512A CN201810799123.4A CN201810799123A CN108751512A CN 108751512 A CN108751512 A CN 108751512A CN 201810799123 A CN201810799123 A CN 201810799123A CN 108751512 A CN108751512 A CN 108751512A
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- oil
- water
- bulky grain
- sewage
- sundries
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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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/101—Sulfur compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/12—Halogens or halogen-containing compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The present invention discloses a kind of oil-water separation system, including oil water separator, sundries processing unit (plant) and sewage-treatment plant, not only realize the separation between solid sundries and oil water mixture and between oil and water, it is furthermore achieved that the processing of solid sundries, convenient for the recycling of later stage solid, also sewage is further processed simultaneously, drinking water is become, waste resource is made rationally to be utilized.
Description
Technical field
The invention belongs to kitchen garbages to handle manufacturing technology field, and in particular to a kind of oil-water separation system.
Background technology
Food residues after kitchen garbage refers to the food residue abandoned in food processing process, diet and
In washing foodstuff, scrub tableware etc. during the raw sewerage that generates.Its ingredient is mainly broken including smashed peel bone, food
The non-solubility organic matter of grain, insoluble protein, cellulosic and starchiness state, ingredient are extremely multiple according to the difference of food
It is miscellaneous.Due to containing abundant nutriment in kitchen garbage, if being directly discharged to nature without processing, suitable
It is i.e. putrid and deteriorated in a short time under the action of temperature and bacterium, not only ambient enviroment is polluted, grows mosquitos and flies, is occupied a large amount of
Soil, and also result in a large amount of wastes of resource.Based on this, the research and development of food waste treatment equipment carry out kitchen garbage
Effectively degradation and integrated treatment, realize that the minimizing of kitchen garbage and recycling will have a very important significance.
In the prior art, oil-water separation system can only realize water-oil separating, and cannot by after separation solid sundries and
Sewage is further processed, i.e., resource is not by rational utilization, and then leads to the wasting of resources.
Invention content
The technical problem to be solved by the invention is to provide a kind of oil-water separation system, solves grease in the prior art
The bad technical problem of separating effect between solid sundries and oil water mixture, between oil and water in piece-rate system.
In order to solve the above technical problems, the technical solution adopted by the present invention：A kind of oil-water separation system, it is characterised in that：
The oil-water separation system includes oil water separator, receives the solid sundries of oil water separator separation and processed to solid sundries
Sundries processing unit (plant) and the sewage-treatment plant for receiving the sewage of oil water separator separation and sewage being handled；Wherein,
Sundries processing includes at least solid sundries crushing and solid sundries compacting, and sewage disposal includes at least solid impurity processing, has
The processing of machine object, anionic treatments and reverse-osmosis treated.
Preferably, the oil water separator includes water-oil separating babinet and the control for controlling oil water separator operation
Case processed, the water-oil separating babinet are internally provided with several partition boards, and the water-oil separating babinet is separated to form by partition board successively
Bulky grain decanting zone, microparticle decanting zone, first fluid channel, water-oil separating area, second fluid channel and sewage discharge
Area；
Feed inlet is provided at the top of the bulky grain decanting zone, the top of bulky grain decanting zone is provided with bulky grain sedimentation
Slot, bulky grain subsider are settled for receiving bulky grain solid sundries with bulky grain described in bulky grain sedimentation groove location corresponding position
Area is provided with solid sundries floss hole, and the bottom of bulky grain decanting zone is provided with particle macerator pump, the particle macerator pump connection
Enter microparticle decanting zone after thering is discharge nozzle, discharge nozzle one end to pass through partition board；
Microparticle decanting zone bottom is provided with microparticle subsider, and microparticle subsider receives in microparticle decanting zone
Particle, oil water mixture enters water-oil separating area by first fluid channel；
The top in the water-oil separating area is provided with oil wiper, is located at solid in the water-oil separating babinet at oil wiper position
There are oil trap, the bottom of oil trap to be provided with oil outlet, oil wiper is discharged after scraping oil to oil trap by oil outlet, grease surely
The lower part of Disengagement zone is provided with filtering material, and filtering material is fixed on by the via in bulkhead bracket in water-oil separating area, water
The second circulation passage is flowed into after filtering material, and sewage discharge area is flowed by second fluid channel；
It is fixed with floating ball lever meter at the top of the sewage discharge area, third fluid channel is provided in sewage discharge area,
Sewage is discharged from third fluid channel.
Preferably, the bulky grain subsider include be set to bottom strainer and with the fixed baffle of strainer, strainer
" V " type groove body is formed with baffle, one end of strainer and water-oil separating babinet are hinged, and one end of baffle and the piston rod of cylinder connect
It connects, cylinder is fixed on water-oil separating babinet, and the piston rod in cylinder pulls bulky grain subsider to be arranged to solid sundries floss hole
Put sundries.
Preferably, the oil wiper include shaft, the arc-shaped base that is connected with the rotating shaft oil scraping plate, is abutted with oil scraping plate,
And the driving motor of drive shaft rotation, the shaft are rotatablely connected with water-oil separating babinet, the arc-shaped base is fixed on
The inside of water-oil separating babinet, the driving motor are fixed on the outside of water-oil separating babinet.
Preferably, the bottom of the bulky grain decanting zone is provided with weight sensor, close to bulky grain decanting zone bottom position
The place of the setting bulky grain decanting zone is provided with sewage draining exit, and bulky grain sedimentation blowoff electromagnetic valve, the weight are provided at sewage draining exit
Sensor and bulky grain sedimentation blowoff electromagnetic valve are connect with control cabinet.
Preferably, the oil trap is internally provided with liquid level sensor, and the oil outlet of oil trap is connected with flowline,
It is provided with oil trap in the flowline and opens and closes solenoid valve and flow sensor, the liquid level sensor, oil trap open and close electricity
Magnet valve and flow sensor are connect with control cabinet.
Preferably, the sundries processing unit (plant) includes pulverizer and solid filter press, and the pulverizer receives grease point
From the bulky grain solid sundries in device, the bottom of pulverizer is equipped with disintegrating mechanism；The solid filter press receives pulverizer powder
Solid sundries after broken are provided with the first ultraviolet lamp, the discharge outlet of solid filter press and water-oil separating at the top of solid filter press
Device connects.
Preferably, the sewage-treatment plant includes sequentially connected sterilization groove body, granule foreign treating column, at organic matter
Manage tower, sulfate radical treating column, halogen ion treating column and RO reverse osmosis membrane processing devices；The sterilization groove body is received from oil
Sewage in separator, sterilization groove body top are equipped with the second ultraviolet lamp.
Preferably, the sterilization groove body is additionally provided with security filter with the connecting line of granule foreign treating column.
Beneficial effects of the present invention：The present invention discloses a kind of oil-water separation system, including oil water separator, sundries processing dress
It sets and sewage-treatment plant, not only realizes the separation between solid sundries and oil water mixture and between oil and water, also
The processing of solid sundries is furthermore achieved, is convenient for the recycling of later stage solid, while also sewage is further processed, makes it
As drinking water, waste resource is made rationally to be utilized.
Description of the drawings
Fig. 1 is the structural schematic diagram of oil-water separation system；
Fig. 2 is the structural schematic diagram of oil water separator in Fig. 1；
Fig. 3 is the physical structure diagram of oil water separator；
Fig. 4 is the structural schematic diagram of oil scraping plate；
Fig. 5 is the structural schematic diagram of sundries processing unit (plant) in Fig. 1；
Fig. 6 is the structural schematic diagram of sewage-treatment plant in Fig. 1；
Fig. 7 case control system schematic diagrames in order to control；
Reference numeral in figure, I-oil water separator；II-sundries processing unit (plant)；III-sewage-treatment plant；1- water-oil separatings
Babinet, 1.1- first partitions, 1.2- second partitions, 1.3- third partition boards, the 4th partition boards of 1.4-, the 5th partition boards of 1.5-, 1.6-
Six partition boards, 1.7- feed inlets, 1.8- solid sundries floss holes, the second sewage draining exits of 1.9-, 1.10- third sewage draining exits, 1.11- the 4th
Sewage draining exit；1.12- the first sewage draining exit；2- control cabinets, 2.1- controllers；3- bulky grain subsiders, 3.1- strainers, 3.2- baffles；
4- cylinders；5- particle macerator pumps, 6- discharge nozzles；7- weight sensors；9- microparticle subsiders, 9.1- windows；12- frizings
Device, 12.1- shafts, 12.2- oil scraping plates, 12.2.1- rigid portions, the soft modeling portions 12.2.2-, 12.3- arc-shaped bases；13- oil traps,
13.1- oil outlets；14- liquid level sensors；16- filtering materials；17- bulkhead brackets, 17.1- vias；18- first fluids channel；
19- second fluids channel；21- floating ball lever meters；22- third fluid channels, 22.1- liquid feeding ends, 22.1.1- liquid feeding ends into
Mouthful, 22.2- outlet ends, the outlet of 22.2.1- outlet ends；23- dredge pumps；The first solenoid valves of 24-；25- second solenoid valves；26-
Third solenoid valve；A- bulky grains decanting zone；B- microparticles decanting zone；C- water-oil separatings area；D- sewage discharges area；27- pulverizers,
The feed inlet of 27.1- pulverizers, 27.2- crush motor, 27.3- crushing knifes, the discharge port of 27.4- pulverizers；28- solid press filtrations
Machine, the feed inlet of 28.1- solid filter presses, the slag-drip opening of 28.2- solid filter presses, the discharge outlet of 28.3- solid filter presses；
The first ultraviolet lamps of 30-；31- sterilizes groove body, and 31.1- sterilizes the feed inlet of groove body, and 31.2- sterilizes the discharge port of groove body；32- particles
Impurity treatment tower, the first tower bodies of 32.1-, the first tower bodies of 32.1.1- bottom, the first tower bodies of 32.1.2- top, the filter of 31.2-PP cottons
Core；33- organic matter treating columns, the second tower bodies of 33.1-, the second tower bodies of 33.1.1- bottom, the second tower bodies of 33.1.2- top,
33.2- active carbon fillers；34- sulfate radical treating columns, 34.1- third tower bodies, 34.1.1- third tower bodies bottom, 34.1.2- thirds
At the top of tower body, 34.2- sulfate ion exchanger resin fillers；35- halogen ion treating columns, the 4th tower bodies of 35.1-, 35.2- halogen from
Sub-exchange resin filler；36-RO reverse osmosis membrane processing devices；The second ultraviolet lamps of 37-；38- security filters.
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
Embodiment 1：
As shown in Figure 1, oil-water separation system includes oil water separator I, receives the solid sundries of oil water separator separation simultaneously
It sundries processing unit (plant) II to solid sundries processing and receives the sewage of oil water separator separation and sewage is handled
Sewage-treatment plant III.Wherein, sundries processing includes at least solid sundries crushing and solid sundries compacting, and sewage disposal is at least
Including solid impurity processing, organic matter processing, anionic treatments and reverse-osmosis treated.
Oil water separator I, as shown in Figures 2 and 3, including water-oil separating babinet 1 and for control oil water separator operation
Control cabinet 2.The inside of water-oil separating babinet 1 is longitudinally positioned 6 pieces of partition boards, respectively first partition 1.1, second partition
1.2, third partition board 1.3, the 4th partition board 1.4, the 5th partition board 1.5 and the 6th partition board 1.6.First partition 1.1 is fixed on grease
Detach babinet 1 top and bottom, and first partition 1.1 by water-oil separating babinet 1 be separated to form bulky grain decanting zone A and
Microparticle decanting zone B；Second partition 1.2 is fixed on the bottom of water-oil separating babinet 1, and the top of second partition 1.2 and grease
The top of separation babinet 1 retains certain spacing, and third partition board 1.3 is fixed on the top of water-oil separating babinet 1, the 4th partition board
1.4 are fixed on the bottom of water-oil separating babinet 1, and between the bottom of third partition board 1.3 and the bottom of water-oil separating babinet 1 and
Retain certain spacing, second partition 1.2, third partition board between the top and the top of water-oil separating babinet 1 of 4th partition board 1.4
1.3 and the 4th partition board 1.4 water-oil separating babinet 1 is separated to form microparticle decanting zone B, first fluid channel 18 and oil
Water Disengagement zone C；5th partition board 1.5 is fixed on the top of water-oil separating babinet 1, and the 6th partition board 1.6 is fixed on water-oil separating babinet 1
Bottom, and between the bottom and the bottom of water-oil separating babinet 1 of the 5th partition board 1.5 and top of the 6th partition board 1.6 with oil
Retain a determining deviation, the 5th partition board 1.5 and the 6th partition board 1.6 between the top of water separating tank body 1 by water-oil separating babinet point
Every formation water-oil separating area C, second fluid channel 19 and sewage discharge area D.
Feed inlet 1.7 is provided at the top of the A of bulky grain decanting zone, the top of bulky grain decanting zone A is provided with bulky grain and sinks
Slot 3 drops, and bulky grain subsider 3 is for receiving bulky grain solid sundries.It is settled with bulky grain sedimentation groove location corresponding position bulky grain
The side in area is provided with solid sundries floss hole 1.8.In the present embodiment, in order to realize the automatic-discharging of solid sundries, bulky grain
Subsider 3 includes being set to the strainer 3.1 of bottom and forming " V " with the fixed baffle 3.2 of strainer, strainer 3.1 and baffle 3.2
One end of type groove body, strainer 3.1 is hinged with water-oil separating babinet 1, and one end of baffle 3.2 is connect with the piston rod of cylinder 4, cylinder
4 are fixed on the top of water-oil separating babinet 1, and the piston rod in cylinder 1 pulls bulky grain subsider 3 to solid sundries floss hole
1.8 discharge sundries.It should be noted that feed liquid enters from feed inlet in bulky grain subsider, bulky grain solid sundries is retained in
Inside bulky grain subsider, oil water mixture and fine particle fall to the lower zone of bulky grain decanting zone from strainer.
The bottom of bulky grain decanting zone A is provided with particle macerator pump 5, and the exit of particle macerator pump 5 is connected with discharge nozzle 6, discharge nozzle 6
One end enters microparticle decanting zone B after passing through first partition 1.1.Liquid in order to avoid entering microparticle decanting zone upsets micro-
The sedimentation of particle in grain decanting zone, preferably 6 nozzle of discharge nozzle of microparticle decanting zone B is upward in the present embodiment.Liquid flowing side
To as shown by arrows in figure.Particle macerator pump will fall off to the particle of bulky grain decanting zone lower zone and further smash, and be formed
Fine particle, fine particle and oil water mixture enter microparticle decanting zone by particle macerator pump and discharge nozzle.In order to
Avoid fine particle long time sedimentation in the bottom of bulky grain subsider, the present embodiment, the bottom of bulky grain decanting zone A is provided with
Weight sensor 7 is provided with the first sewage draining exit 1.12, the first sewage draining exit close to the side of bottom position bulky grain decanting zone A
Bulky grain sedimentation blowoff electromagnetic valve (not illustrating in figure) is provided at 1.12.Weight sensor 7 settles blowdown electromagnetism with bulky grain
Valve is connect with control cabinet 2.
The microparticle decanting zone bottoms B are provided with microparticle subsider 9, into microparticle decanting zone fine particle at micro-
It is settled in grain subsider.For the ease of the discharge of solid particle in microparticle subsider, microparticle subsider 9 is close to bottom position
It is provided with the second sewage draining exit 1.9, microparticle sedimentation blowdown valve (not illustrating in figure) is provided at the second sewage draining exit 1.9.In order to just
Height is deposited in microparticle subsider 9 in observation particle, and window 9.1 is provided on microparticle subsider 9.Oil water mixture
Enter water-oil separating area C by first fluid channel 18.The bottom in first fluid channel 18 is provided with third sewage draining exit 1.10, the
The first circulation passage blowdown valve (not illustrating in figure) is provided at three sewage draining exits 1.10.
The top of water-oil separating area C is provided with oil wiper 12.In the present embodiment, oil wiper 12 includes shaft 12.1 and turns
The driving motor of the oil scraping plate 12.2 of axis connection, the arc-shaped base 12.3 abutted with oil scraping plate and drive shaft rotation is (in figure
For signal).The both ends of shaft 12.1 are rotatablely connected with water-oil separating babinet 1, and one end is divided after oil-water separation tank 1 with grease
From the driving motor axis connection outside case.The both ends of arc-shaped base 12.3 are fixed on the inside of oil-water separation tank 1.As shown in figure 4,
Oil scraping plate 12.2 is arc plate structure, and arc panel includes rigid portion 12.2.1 and soft modeling portion 12.2.2.Wherein, arc panel rigidity
Portion 12.2.1 is prepared using 304 stainless steels, and rigid portion 12.2.1 is connect with shaft 12.1, and the soft modeling portion 12.2.2 of arc panel is used
Prepared by the soft modelings of PVC, the outside of soft modeling portion 12.2.2 is abutted with arc-shaped base 12.3.Oil scraping plate had been prepared using two kinds of unlike materials both
It can ensure the rigidity of oil scraping plate, while also ensure the scraping effect of oil scraping plate.Due to the soft modeling portion of oil scraping plate and arc-shaped base
Fitting it is close, therefore scraping effect is more preferably.It is fixed with oil trap 13 between arc-shaped base 12.3 and the 5th partition board 1.5, is scraped
Oiled-plate method hangs oil enters oil trap from after oil water mixture along arc-shaped base.Oil trap 13 is internally provided with liquid level sensor
14, the bottom of oil trap 13 is provided with oil outlet 13.1, and the flowline that oriented oil drum is drained the oil, flowline are connected at oil outlet 13.1
In be provided with oil trap and open and close solenoid valve and flow sensor (being signal in figure), oil trap opens and closes solenoid valve and flow
Sensor is connect with control cabinet 2.The lower part of water-oil separating area C is provided with filtering material 16, and filtering material 16 passes through bulkhead bracket
Via 17.1 in 17 is fixed in water-oil separating area C.In the present embodiment, filtering material 16 is PP filter cottons.Water is through filter material
Second fluid channel 19 is flowed into after material, and sewage discharge area D is flowed by second fluid channel 19.The bottom in water-oil separating area is set
It is equipped with the 4th sewage draining exit 1.11, water-oil separating blowdown valve (not illustrating in figure) is provided at the 4th sewage draining exit 1.11.
It is fixed with floating ball lever meter 21 at the top of sewage discharge area D, third fluid channel 22 is provided in sewage discharge area,
Third circulation passage 22 is inverse u shape channel, and the liquid feeding end 22.1 in inverse u shape channel is located at the inside of oil water separator 1,
The outlet end 22.2 in U-typed channel is located at the outside of oil water separator 1, the import 22.1.1 of liquid feeding end and the outlet of outlet end
22.2.1 be connected with dredge pump 23, and the import 22.1.1 of liquid feeding end, the outlet 22.2.1 of outlet end and liquid feeding end import and
The junction of outlet end outlet is respectively arranged with the first solenoid valve 24, second solenoid valve 25 and third solenoid valve 26, the first electricity
Magnet valve 24, second solenoid valve 25 and third solenoid valve 26 are connect with control cabinet.
As shown in figure 5, sundries processing unit (plant) II includes pulverizer 27 and solid filter press 28, pulverizer 27 receives grease
Bulky grain solid sundries in separator.Specifically, the feed inlet 27.1 of pulverizer and the solid sundries of oil water separator are discharged
Mouth 1.8 connects, and the bottom of pulverizer 27 is equipped with disintegrating mechanism.Disintegrating mechanism includes crushing motor 27.2 and crushing knife
27.3, it crushes motor 27.2 and crushing knife 27.3 is driven to rotate, comminuted solids sundries.Solid filter press 28 uses in the prior art
Some solid filter presses.The feed inlet 28.1 of solid filter press connects the discharge port 27.4 of pulverizer, solid filter press
Residual cake valve (not illustrating in figure) is provided at slag-drip opening 28.2, the outside of solid filter press can be arranged at slag-drip opening position
Solid collecting tank, solid collecting tank are received through the pressed solid impurity of solid filter press；The discharge outlet 28.3 of solid filter press
It is connect with the feed inlet 1.7 of oil water separator, the liquid generated after solid filter press extrusion solid sundries is back to grease point
From being detached in device.In order to be sterilized to solid sundries, the first ultraviolet lamp 30 is installed, first is ultraviolet at the top of solid filter press
Lamp 30 sterilizes solid sundries after irradiating solid sundries.
As shown in fig. 6, sewage-treatment plant III includes sterilization groove body 31, granule foreign treating column 32, organic matter treating column
33, sulfate radical treating column 34, halogen ion treating column 35 and RO reverse osmosis membrane processings device 36.Wherein, the charging of groove body is sterilized
Mouth 31.1 receives the sewage in oil water separator, and the second ultraviolet lamp 37, the second ultraviolet lamp 37 are equipped at the top of sterilization groove body
Sewage inside sterilization tank body is sterilized.The discharge port 31.2 for sterilizing groove body connects granule foreign treating column 32.In order to right
Sewage further filters, and sterilization groove body 31 is additionally provided with security filter 38 with the connecting line of granule foreign treating column 32.
Granule foreign treating column 32 includes the first tower body 32.1 and the PP cotton filter element 32.2 being set to inside the first tower body, the faces PP filter core
32.2 pairs of sewage further filter, and to remove the partial impurities particle in sewage, sewage enters from the first tower body bottom 32.1.1
And be discharged from top 32.1.2, the sewage after exclusion enters organic matter treating column 33.Organic matter treating column 33 includes the second tower body
33.1 and internal setting active carbon filler 33.2, active carbon filler can remove the organic matter in sewage.Sewage is from second
Tower body bottom 33.1.1 enters and is discharged from top 33.1.2, and the sewage after exclusion enters sulfate radical treating column 34.At sulfate radical
Reason tower 34 includes third tower body 34.1 and the sulfate ion exchanger resin filler 34.2 that is set to inside tower body, sulfate radical from
Sub-exchange resin filler removes the sulfate ion in sewage.Sewage enters from the bottom 34.1.1 of third tower body and from top
34.1.2 it is discharged, the sewage after discharge enters halogen ion treating column 35.Halogen ion treating column 35 include the 4th tower body 35.1 and
The halogen ion exchanger resin filler 35.2 being set to inside tower body, halogen ion exchanger resin filler 35.2 is for removing in sewage
Chlorion in halogen ion, such as sewage.Sulfate ion exchanger resin filler and halogen ion exchanger resin filler be it is cloudy from
Sub-exchange resin filler can directly be purchased by market.It is reverse osmosis that the sewage finally come out from halogen ion treating column enters RO
In membrane treatment appts 36, RO reverse osmosis membrane processings device 36 also belongs to the prior art, and the present invention repeats no more this structure.RO is anti-
Infiltration membrane treatment appts are for further purifying sewage, so that sewage forms drinking water.
Control cabinet 2 is internally provided with controller 2.1, and the present embodiment preferably uses PLC controller.As shown in fig. 7, PLC is controlled
Device processed receives the signal of weight sensor 7, liquid level sensor 14 and floating ball lever meter 21, and controls cylinder 4, bulky grain sedimentation
Blowoff electromagnetic valve, oil trap open and close solenoid valve, dredge pump 23, the first solenoid valve 24, second solenoid valve 25 and third solenoid valve
26 execute corresponding actions.Time, the bulky grain decanting zone bottom of the sedimentation of bulky grain subsider can be set by PLC controller
Weight threshold values, oil trap liquid level threshold values and the liquid level threshold values in sewage discharge area of grain.If the PLC controller record sedimentation time arrives
Up to after the presetting sedimentation time, PLC controller controls cylinder operation, and cylinder drives the overturning of bulky grain subsider, solid sundries
It is disposed to sundries processing unit (plant), solid sundries are handled by sundries processing unit (plant)；If PLC controller receives weight and passes
The gravimetric value of sensor detection is more than PLC controller control bulky grain sedimentation blowoff electromagnetic valve opening after presetting weight threshold values.
If the level value that PLC controller receives liquid level sensor detection is more than oil trap liquid level threshold values, PLC controller control oil trap opens
Close solenoid valve opening.When floating ball lever meter detects that sewage level is higher than the liquid level threshold values in sewage discharge area, PLC controller control
The closing of the first solenoid valve is made, second solenoid valve is opened, while starting dredge pump, and sewage enters from the liquid feeding end in inverse u shape channel,
Then it is discharged from the outlet end in inverse u shape channel；When floating ball lever meter detects that sewage level is less than the liquid level in sewage discharge area
When threshold values, PLC controller controls second solenoid valve and closes, and third solenoid valve is opened, and simultaneously closes off dredge pump, and sewage is from inverted " u "
The import of the liquid feeding end in type channel is directly discharged into after entering in sterilization tank body, is further located to the sewage of discharge by sterilizing groove body
Reason.The advantages of this kind of set-up mode, is：The impurity of sewage discharge area bottom precipitation is discharged by dredge pump first, avoid into
The impure concentration of sewage entered inside sterilization tank body is higher, improves sewage treating efficiency.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any
Those familiar with the art in the technical scope disclosed by the present invention, can easily think of the change or the replacement, and should all contain
Lid is within protection scope of the present invention.Therefore, protection scope of the present invention should be based on the protection scope of the described claims.
Claims (9)
1. a kind of oil-water separation system, it is characterised in that：The oil-water separation system includes oil water separator, receives water-oil separating
Device separation solid sundries and to solid sundries processing sundries processing unit (plant) and receive oil water separator separation sewage simultaneously
The sewage-treatment plant that sewage is handled；Wherein, sundries processing includes at least solid sundries crushing and solid sundries pressure
System, sewage disposal include at least solid impurity processing, organic matter processing, anionic treatments and reverse-osmosis treated.
2. a kind of oil-water separation system according to claim 1, it is characterised in that：The oil water separator includes water-oil separating
Babinet and the control cabinet operated for controlling oil water separator, the water-oil separating babinet are internally provided with several partition boards,
The water-oil separating babinet is separated to form bulky grain decanting zone, microparticle decanting zone, first fluid channel, grease by partition board successively
Disengagement zone, second fluid channel and sewage discharge area；
Feed inlet is provided at the top of the bulky grain decanting zone, the top of bulky grain decanting zone is provided with bulky grain subsider,
Bulky grain subsider is set for receiving bulky grain solid sundries with bulky grain decanting zone described in bulky grain sedimentation groove location corresponding position
It is equipped with solid sundries floss hole, the bottom of bulky grain decanting zone is provided with particle macerator pump, and the particle macerator pump is connected with out
Expects pipe, discharge nozzle one end enter microparticle decanting zone after passing through partition board；
Microparticle decanting zone bottom is provided with microparticle subsider, and microparticle subsider receives micro- in microparticle decanting zone
Grain, oil water mixture enter water-oil separating area by first fluid channel；
The top in the water-oil separating area is provided with oil wiper, is fixed in the water-oil separating babinet at oil wiper position
The bottom of oil trap, oil trap is provided with oil outlet, and oil wiper is discharged after scraping oil to oil trap by oil outlet, water-oil separating
The lower part in area is provided with filtering material, and filtering material is fixed on by the via in bulkhead bracket in water-oil separating area, and water passes through
The second circulation passage is flowed into after filter material material, and sewage discharge area is flowed by second fluid channel；
It is fixed with floating ball lever meter at the top of the sewage discharge area, third fluid channel, sewage are provided in sewage discharge area
It is discharged from third fluid channel.
3. a kind of oil-water separation system according to claim 2, it is characterised in that：The bulky grain subsider includes being set to
The strainer of bottom and with the fixed baffle of strainer, strainer and baffle form " V " type groove body, one end of strainer and oil-water separation tank
Body is hinged, and one end of baffle and the piston rod of cylinder connect, and cylinder is fixed on water-oil separating babinet, and the piston rod in cylinder is drawn
Dynamic bulky grain subsider discharges sundries to solid sundries floss hole.
4. a kind of oil-water separation system according to claim 3, it is characterised in that：The oil wiper includes shaft and shaft
The driving motor of the oil scraping plate of connection, the arc-shaped base abutted with oil scraping plate and drive shaft rotation, the shaft and grease
Babinet rotation connection is detached, the arc-shaped base is fixed on the inside of water-oil separating babinet, and the driving motor is fixed on grease
Detach the outside of babinet.
5. a kind of oil-water separation system according to claim 4, it is characterised in that：The bottom of the bulky grain decanting zone is arranged
There is weight sensor, the bulky grain decanting zone described in the bottom position of bulky grain decanting zone is provided with sewage draining exit, at sewage draining exit
It is provided with bulky grain sedimentation blowoff electromagnetic valve, the weight sensor and bulky grain sedimentation blowoff electromagnetic valve connect with control cabinet
It connects.
6. a kind of oil-water separation system according to claim 2, it is characterised in that：The oil trap is internally provided with liquid level
The oil outlet of sensor, oil trap is connected with flowline, and oil trap is provided in the flowline and opens and closes solenoid valve and stream
Quantity sensor, the liquid level sensor, oil trap open and close solenoid valve and flow sensor is connect with control cabinet.
7. a kind of oil-water separation system according to claim 1, it is characterised in that：The sundries processing unit (plant) includes pulverizer
And solid filter press, the pulverizer receive the bulky grain solid sundries in oil water separator, the bottom of pulverizer is equipped with
Disintegrating mechanism；The solid filter press receives the solid sundries after pulverizer crushes, and first is provided at the top of solid filter press
The discharge outlet of ultraviolet lamp, solid filter press is connect with oil water separator.
8. a kind of oil-water separation system according to claim 1, it is characterised in that：The sewage-treatment plant includes connecting successively
Sterilization groove body, granule foreign treating column, organic matter treating column, sulfate radical treating column, halogen ion treating column and the RO reverse osmosis connect
Permeable membrane processing unit；The sterilization groove body receives the sewage in oil water separator, and the second purple is equipped at the top of sterilization groove body
Outer lamp.
9. a kind of oil-water separation system according to claim 8, it is characterised in that：The sterilization groove body is handled with granule foreign
It is additionally provided with security filter in the connecting line of tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810799123.4A CN108751512A (en) | 2018-07-19 | 2018-07-19 | A kind of oil-water separation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810799123.4A CN108751512A (en) | 2018-07-19 | 2018-07-19 | A kind of oil-water separation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108751512A true CN108751512A (en) | 2018-11-06 |
Family
ID=63970754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810799123.4A Withdrawn CN108751512A (en) | 2018-07-19 | 2018-07-19 | A kind of oil-water separation system |
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| Country | Link |
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| CN (1) | CN108751512A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113072522A (en) * | 2021-03-25 | 2021-07-06 | 浙江智英石化技术有限公司 | Method for removing ethylbenzene hydroperoxide in mixed organic phase |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204529516U (en) * | 2015-04-07 | 2015-08-05 | 合肥宏润环保科技有限公司 | A kind of meal kitchen water-and-oil separator |
| CN106914414A (en) * | 2017-05-04 | 2017-07-04 | 冷国强 | A kind of petroleum coke high throughput screening devices |
| CN107352771A (en) * | 2017-07-20 | 2017-11-17 | 盐城千之诺机械有限公司 | A kind of riverbed sludge reuse means |
| CN207294505U (en) * | 2017-08-14 | 2018-05-01 | 广州中科环保技术有限公司 | A kind of sanitary sewage multistep treatment utilizes device |
-
2018
- 2018-07-19 CN CN201810799123.4A patent/CN108751512A/en not_active Withdrawn
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN204529516U (en) * | 2015-04-07 | 2015-08-05 | 合肥宏润环保科技有限公司 | A kind of meal kitchen water-and-oil separator |
| CN106914414A (en) * | 2017-05-04 | 2017-07-04 | 冷国强 | A kind of petroleum coke high throughput screening devices |
| CN107352771A (en) * | 2017-07-20 | 2017-11-17 | 盐城千之诺机械有限公司 | A kind of riverbed sludge reuse means |
| CN207294505U (en) * | 2017-08-14 | 2018-05-01 | 广州中科环保技术有限公司 | A kind of sanitary sewage multistep treatment utilizes device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113072522A (en) * | 2021-03-25 | 2021-07-06 | 浙江智英石化技术有限公司 | Method for removing ethylbenzene hydroperoxide in mixed organic phase |
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