CN106630302A - Emulsion treatment equipment - Google Patents
Emulsion treatment equipment Download PDFInfo
- Publication number
- CN106630302A CN106630302A CN201710070825.4A CN201710070825A CN106630302A CN 106630302 A CN106630302 A CN 106630302A CN 201710070825 A CN201710070825 A CN 201710070825A CN 106630302 A CN106630302 A CN 106630302A
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- China
- Prior art keywords
- tank
- water inlet
- reaction tank
- delivery port
- processing equipment
- Prior art date
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- 239000000839 emulsion Substances 0.000 title abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 95
- 238000006243 chemical reaction Methods 0.000 claims abstract description 33
- 238000002156 mixing Methods 0.000 claims abstract description 25
- 239000002351 wastewater Substances 0.000 claims abstract description 11
- 239000002893 slag Substances 0.000 claims description 40
- 238000007790 scraping Methods 0.000 claims description 26
- 238000005192 partition Methods 0.000 claims description 21
- 238000009287 sand filtration Methods 0.000 claims description 17
- 210000005056 cell body Anatomy 0.000 claims description 16
- 238000004945 emulsification Methods 0.000 claims description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 14
- 230000007246 mechanism Effects 0.000 claims description 14
- 230000005540 biological transmission Effects 0.000 claims description 12
- 229910052799 carbon Inorganic materials 0.000 claims description 12
- 238000001914 filtration Methods 0.000 claims description 12
- 238000010992 reflux Methods 0.000 claims description 9
- 238000007667 floating Methods 0.000 claims description 7
- 239000003814 drug Substances 0.000 claims description 6
- 230000008676 import Effects 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 229940079593 drug Drugs 0.000 claims 1
- 239000008394 flocculating agent Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000004065 wastewater treatment Methods 0.000 abstract description 2
- 239000003153 chemical reaction reagent Substances 0.000 abstract 5
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 13
- 239000002699 waste material Substances 0.000 description 10
- 239000000203 mixture Substances 0.000 description 9
- 239000004519 grease Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 229920002401 polyacrylamide Polymers 0.000 description 5
- 239000012528 membrane Substances 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000006837 decompression Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000013528 metallic particle Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 230000001086 cytosolic effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000012208 gear oil Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 239000010721 machine oil Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/005—Processes using a programmable logic controller [PLC]
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses emulsion treatment equipment. The equipment comprises a tank body, a chemical reagent adding tank, a reaction tank and a clean water tank, wherein a waste water inlet and a chemical reagent adding opening are formed in the upper part of the chemical reagent adding tank; the chemical reagent adding opening is externally connected with a flocculating agent box; a residue separating basket is arranged at the upper part of the chemical reagent adding tank and positioned below the waste water inlet; a mixing tank and a residue scraper are arranged in the reaction tank; the mixing tank is provided with a water inlet, a dissolved air water inlet and a water outlet; the dissolved air water inlet of the mixing tank is externally connected with a dissolved air tank through a dissolved air water release pipe; a residue collecting tank is arranged below one end of the residue scraper; an oil baffle plate is arranged at the bottom of the reaction tank; a water outlet is formed in the lower part of the clean water tank. The equipment is skillful in design and simple in structure, has the waste water treatment efficiency higher than that in the national regulated discharge standard, and is low in manufacture cost, reduces the operation cost of enterprises, and is applicable to large and small enterprises.
Description
Technical field
The invention belongs to technical field of waste water processing, more particularly to a kind of emulsion processing equipment.
Background technology
Emulsion is a kind of high performance semi-synthetic metal working fluid, in machine-building and processing industry, the cutting of metal
With grinding a large amount of emulsions need to be used to be used as lubrication, machine oil and surfactant are mainly contained in emulsion, be to use
As needed dilute with water adds what emulsifying agent was formulated to oil emulsion.
Emulsion through multiple Reusability and with air contact after, it may occur that it is different degrees of become sour, rot etc. become
Matter phenomenon, performance is reduced, and to regularly replace new emulsion, causes to generate substantial amounts of waste emulsified mixture.Contain in waste emulsified mixture
High concentration oil, high-enriched organics, and a large amount of metallic particles are incorporated in metal cutting process, containing metallic particles pollution
Thing, arbitrarily discharge can cause serious environmental pollution, it is therefore necessary to carry out effectively processing the discharge restriction for reaching public sewage
Require.
At present, for the processing method of waste emulsified mixture mainly has Physical and microbial method.Physical common are ultrafiltration
Method, is a kind of membrane separation technique, and it is much like with counter-infiltration, also with UF membrane of the pellicle using pressure differential as motive force
Process, by selective film, the particulate of the different molecular weight in solution is separated, under pressure medium, less than hole
The particulate in footpath, through the micropore on film, is trapped with solvent more than the particulate in aperture.The size and shape of micropore is determined on film
The separating property of film is determined.The particulate being trapped can not form filter cake, be still retained in filtrate with cytosolic form.But useless breast
Change the high concentration oil that contains in liquid and easily cause film blocking, reduce the service life of film, and it is higher to change the cost of membrane module,
The operation cost of enterprise can be increased;Microbial method is, by the suitable bacteria culture of culture, to realize the degraded and decomposition of emulsion,
But do not allow easily biological-degradable, therefore the process of waste emulsified mixture to be difficult to reach discharge mark containing high-enriched organics in emulsion
It is accurate.
The content of the invention
The invention mainly solves the technical problem of a kind of emulsion processing equipment is provided, equipment deft design, the structure
Simplify, waste water treatment efficiency is higher than state emission standard, device fabrication low cost reduces the operation cost of enterprise, is suitable for
Use in large and small type enterprise.
To solve above-mentioned technical problem, one aspect of the present invention is:A kind of emulsion processing equipment is provided,
Including the second partition of first dividing plate and longitudinal direction in cell body, the cell body with longitudinal direction, first dividing plate and described second
The cell body is isolated into dividing plate dosing pond, reaction tank and the clear water reserviors arranged successively along flow direction;
The top in the dosing pond has waste water inlet and a dosing mouth, the external flocculant medicine-chest of the dosing mouth, it is described plus
The top in medicine pond and have every slag basket positioned at the lower section of waste water inlet, the delivery port in the dosing pond is located at bottom;
There is mixing pit and Slag Scraping Device, the mixing pit is located at the bottom of the reaction tank, described to scrape in the reaction tank
Slag machine is located at the top of the reaction tank;The mixing pit has water inlet, dissolved air water import and delivery port, the mixing pit
Water inlet is connected with the delivery port in the dosing pond, and the dissolved air water import of the mixing pit is by the external molten gas of dissolved air water release pipe
Tank, the delivery port of the mixing pit is communicated with the reaction tank;Dreg collecting slot is provided with below one end of the Slag Scraping Device, it is described to scrape
Slag machine scrapes slag by the reaction tank towards the dreg collecting slot;The delivery port of the reaction tank be located at the second partition bottom and
Connect with the clear water reserviors;The bottom of the reaction tank is provided with oil baffle, and the oil baffle is located at the second partition and described
Between mixing pit;
The bottom of the clear water reserviors has delivery port.
Further say, the bottom of the clear water reserviors has circulation port, and the dissolving has water inlet and air inlet, institute
The water inlet for stating dissolving is connected by circulation pipe with the circulation port of the clear water reserviors, and the circulation pipe is provided with reflux pump, institute
State the external high-pressure air source of air inlet of dissolving.
Further say, be additionally provided with sandfiltration pot and carbon filtration tank, the delivery port of the clear water reserviors connects the sand by pipeline
The water inlet of filter tank, the delivery port of the sandfiltration pot connects the water inlet of the carbon filtration tank by pipeline, and connects the clear water
On the pipeline of pond and the sandfiltration pot or connect the pipeline of the sandfiltration pot and the carbon filtration tank and be provided with suction pump.
Further say, be provided with PLC, the Slag Scraping Device, the magnetic valve of the flocculant medicine-chest, the dissolving
Magnetic valve, the reflux pump and the suction pump all electrically connect with PLC respectively.
Further say, the height of the oil baffle is 55-65cm.
Further say that there is interval, the interval structure between the bottom surface of the lower end of the second partition and the cell body
Into the delivery port of the reaction tank, the height at the interval is 10-15cm.
Further say, floating ball lever meter, the floating ball lever meter and PLC electricity are provided with the clear water reserviors
Connection.
Further say, the dreg collecting slot is located at the top of the clear water reserviors.
Further say, the Slag Scraping Device is chain type Slag Scraping Device, the chain type Slag Scraping Device includes motor, linked transmission
Mechanism and scum board, the chain type transmission mechanism is connected with the motor, and the scum board is fixed on the linked transmission
Mechanism, the scum board is moved under chain type transmission mechanism drive, and the motor is electrically connected with the PLC
Connect.
Further say, the medicament added in the flocculant medicine-chest is PAM (polyacrylamide), and the flocculant medicine
Case is provided with rabbling mechanism.
Beneficial effects of the present invention at least have it is following some:
First, the flocculant that the present invention is added can form larger with the macromolecular particle in waste emulsified mixture or small molecule particle
Flocculate, while in dissolving dissolved air water decompression release after micro-bubble is formed in water body, due to the density of flocculate
It is less than hydrone, so can float to form scum layer after micro-bubble adhesion flocculate, and scraped to dreg collecting slot by Slag Scraping Device, so as to
The polluter in water is rapidly removed, the purpose of water purification is reached;In addition the oil baffle that the present invention is provided with can stop with water (flow) direction
The part grease of flowing so as to float up to the top in central reaction pond, and scraped by Slag Scraping Device, it is to avoid part not with flocculant
The grease for forming flocculate enters clear water reserviors;
2nd, the present invention is additionally provided with sandfiltration pot and carbon filtration tank, and the water body in clear water reserviors can further remove water through sandfiltration pot
Silt and metal ion in body etc., the activated carbon filled in carbon filtration tank can other impurities and ozone in adsorbed water body, it is and right
Pigment in water body is adsorbed, it is ensured that to the treatment effect of waste emulsified mixture be higher than state emission standard;
3rd, the water part in clear water reserviors is introduced into pressure air-dissolving in dissolving by the reflux pump that the present invention is provided with, after decompression
Mixing pit is directly entered, using partial reflux method of pressed dissolved-air release, the water yield of pressurization is few, can save the power consumption of equipment,
And do not promote emulsification, treatment effect to be better than full method of pressed dissolved-air release during air supporting;
4th, the interval with 10-15cm between second partition of the present invention and the bottom surface of cell body, and the height being spaced is less than clear
The minimum liquid level face in pond, the purpose of the design is, due to the density of the density ratio water of grease it is big, therefore ought not by gear oil
When the grease that plate stops flows through second partition, macromolecular grease can be accumulated in the lower end of second partition, so as to float simultaneously
Scraped by Slag Scraping Device, the water body that inflow clear water reserviors are effectively ensured does not contain grease;
5th, using PLC to whole equipment whole-process control and monitoring, automation intensity is high, reduces artificial for the present invention
Workload, can effectively improve the purified treatment efficiency of equipment;And PLC carries hardware fault self-monitoring function, breaks down
When can send a warning in time, it is ensured that the equipment reliability of operation.
Description of the drawings
Fig. 1 is the structural representation of the present invention;
The mark of each part is as follows in accompanying drawing:
Cell body 1, the first dividing plate 2, second partition 3, dosing pond 4, reaction tank 5, clear water reserviors 6, flocculant medicine-chest 7, every slag basket
8th, mixing pit 9, Slag Scraping Device 10, dissolving 11, dreg collecting slot 12, oil baffle 13, reflux pump 14, sandfiltration pot 15, carbon filtration tank 16, draw water
Pump 17, floating ball lever meter 18, waste water inlet 41, dosing mouth 42, delivery port 61, circulation port 62 and scum board 101.
Specific embodiment
Presently preferred embodiments of the present invention is described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, apparent clearly defines so as to make to protection scope of the present invention.
Embodiment:A kind of emulsion processing equipment, as shown in figure 1, the present invention includes having in cell body 1, the cell body 1 indulging
To the first dividing plate 2 and longitudinal direction second partition 3, first dividing plate 2 and the second partition 3 are isolated into the cell body 1
Dosing pond 4, reaction tank 5 and the clear water reserviors 6 arranged successively along flow direction;
The top in the dosing pond 4 has waste water inlet 41 and dosing mouth 42, the external flocculant medicine-chest of the dosing mouth 42
7, the top in the dosing pond 4 and positioned at the lower section of waste water inlet 41 have every slag basket 8, the delivery port in the dosing pond 4 is located at
Bottom;
There is mixing pit 9 and Slag Scraping Device 10, the mixing pit 9 is located at the bottom of the reaction tank 5 in the reaction tank 5,
The Slag Scraping Device 10 is located at the top of the reaction tank 5;The mixing pit 9 has water inlet, dissolved air water import and delivery port, institute
The water inlet for stating mixing pit 9 is connected with the delivery port in the dosing pond 4, and the dissolved air water import of the mixing pit 9 passes through dissolved air water
The external dissolving 11 of release pipe, the delivery port of the mixing pit 9 is communicated with the reaction tank 5;One end of the Slag Scraping Device 10
Lower section is provided with dreg collecting slot 12, and the Slag Scraping Device 10 scrapes slag by the reaction tank 5 towards the dreg collecting slot 12;The reaction tank 5
Delivery port is located at the bottom of the second partition 3 and connects with the clear water reserviors 6;The bottom of the reaction tank 5 is provided with oil baffle
13, the oil baffle 13 is located between the second partition 3 and the mixing pit 9;
The bottom of the clear water reserviors 6 has delivery port 61.
The bottom of the clear water reserviors 6 has circulation port 62, and the dissolving 11 has water inlet and air inlet, the molten gas
The water inlet of tank 11 is connected by circulation pipe with the circulation port 62 of the clear water reserviors, and the circulation pipe is provided with reflux pump 14, institute
State the external high-pressure air source of air inlet of dissolving 11.
Sandfiltration pot 15 and carbon filtration tank 16 are additionally provided with, the delivery port of the clear water reserviors 6 connects the sandfiltration pot 15 by pipeline
Water inlet, the delivery port of the sandfiltration pot 15 connects the water inlet of the carbon filtration tank 16 by pipeline, and connects the clear water
The pipeline of pond 6 and the sandfiltration pot 15 is provided with suction pump 17.
It is provided with PLC, the Slag Scraping Device 10, the magnetic valve of the flocculant medicine-chest 7, the electromagnetism of the dissolving 11
Valve, the reflux pump 14 and the suction pump 17 are all electrically connected with PLC respectively.
The height of the oil baffle 13 is 55-65cm.
There is interval, the interval constitutes the reaction between the bottom surface of the lower end of the second partition 3 and the cell body 1
The delivery port in pond 5, the height at the interval is 10-15cm.
Floating ball lever meter 18 is provided with the clear water reserviors 6, the floating ball lever meter 18 is electrically connected with the PLC.
The minimum liquid level of the floating ball lever meter is 25-35cm.
The dreg collecting slot 12 is located at the top of the clear water reserviors 6.
The Slag Scraping Device 10 is chain type Slag Scraping Device, and the chain type Slag Scraping Device includes motor, chain type transmission mechanism and scrapes
Slag plate 101, the chain type transmission mechanism is connected with the motor, and the scum board 101 is fixed on the linked transmission machine
Structure, the scum board 101 is moved under chain type transmission mechanism drive, and the motor is electrically connected with the PLC
Connect.
The medicament added in the flocculant medicine-chest 7 is PAM, and the flocculant medicine-chest 7 is provided with rabbling mechanism.
The operation principle of the present invention is as follows:When waste emulsified mixture is from waste water inlet into cell body, first passes through and blocked automatically every slag basket
Debris and bulky grain waste residue variously-shaped in emulsifying liquid waste water are cut and removed, and is entered in reaction tank by pipeline, enter anti-
The waste emulsified mixture of Ying Chizhong contains PAM flocculants, and PAM flocculants form larger flocculate with the particulate matter in water body, while
The dissolved air water that discharges in dissolving forms micro-bubble, floats after micro-bubble adhesion flocculate and forms scum layer and by scraping slag
Machine is scraped, in addition, the grease in waste emulsified mixture is stopped by oil baffle, floated, is equally scraped by Slag Scraping Device;After purifying again
Water body enters clear water reserviors by the bottom of second partition, because the minimum liquid level face in clear water reserviors is higher than second partition and cell body bottom
Distance between the two, therefore the small molecule grease in water body can be suspended in the lower end of second partition, be accumulated into macromolecular oil
Float after shape thing, scraped by Slag Scraping Device;When the liquid level in clear water reserviors is higher than 25-30cm, the suction pump in clear water reserviors exit is opened
It is dynamic, pull water out and respectively enter and discharge after sandfiltration pot and the purification of carbon filtration tank;In addition, the water in clear water reserviors some pass through back
Stream pump enters dissolving, and forms dissolved air water with into the compressed air in dissolving, can be recycled.
Embodiments of the invention are the foregoing is only, the scope of the claims of the present invention is not thereby limited, it is every using this
The equivalent structure transformation that bright specification and accompanying drawing content are made, or other related technical fields are directly or indirectly used in,
It is included within the scope of the present invention in the same manner.
Claims (10)
1. a kind of emulsion processing equipment, it is characterised in that:Including cell body, the cell body is interior to be had the first dividing plate of longitudinal direction and indulges
To second partition, first dividing plate and the second partition by the cell body be isolated into it is arranging successively along flow direction plus
Medicine pond, reaction tank and clear water reserviors;
The top in the dosing pond has waste water inlet and a dosing mouth, the external flocculant medicine-chest of the dosing mouth, the dosing pond
Top and have every slag basket positioned at the lower section of waste water inlet, the delivery port in the dosing pond is located at bottom;
There is mixing pit and Slag Scraping Device, the mixing pit is located at the bottom of the reaction tank, the Slag Scraping Device in the reaction tank
Positioned at the top of the reaction tank;The mixing pit has water inlet, dissolved air water import and delivery port, the water inlet of the mixing pit
Mouth is connected with the delivery port in the dosing pond, and the dissolved air water import of the mixing pit manages external dissolving by dissolved air water release,
The delivery port of the mixing pit is communicated with the reaction tank;Dreg collecting slot is provided with below one end of the Slag Scraping Device, it is described to scrape slag
Machine scrapes slag by the reaction tank towards the dreg collecting slot;The delivery port of the reaction tank be located at the second partition bottom and with
The clear water reserviors connection;The bottom of the reaction tank is provided with oil baffle, and the oil baffle is located at the second partition and described mixed
Close between pond;
The bottom of the clear water reserviors has delivery port.
2. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The bottom of the clear water reserviors has to be followed
Collar extension, the dissolving has water inlet and air inlet, and the water inlet of the dissolving is by circulation pipe and the clear water reserviors
Circulation port connects, and the circulation pipe is provided with reflux pump, the external high-pressure air source of air inlet of the dissolving.
3. a kind of emulsion processing equipment according to claim 1, it is characterised in that:Sandfiltration pot and carbon filtration tank are additionally provided with,
The delivery port of the clear water reserviors connects the water inlet of the sandfiltration pot by pipeline, and the delivery port of the sandfiltration pot is connected by pipeline
Meet on the water inlet of the carbon filtration tank, and the pipeline of the connection clear water reserviors and the sandfiltration pot or connect the sandfiltration pot and institute
The pipeline for stating carbon filtration tank is provided with suction pump.
4. a kind of emulsion processing equipment according to claim 1, it is characterised in that:PLC is provided with, it is described to scrape slag
Machine, the magnetic valve of the flocculant medicine-chest, the magnetic valve of the dissolving, the reflux pump and the suction pump all respectively with
PLC is electrically connected.
5. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The height of the oil baffle is 55-
65cm。
6. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The lower end of the second partition and institute
State and have between the bottom surface of cell body interval, the interval constitutes the delivery port of the reaction tank, and the height at the interval is 10-
15cm。
7. a kind of emulsion processing equipment according to claim 4, it is characterised in that:Ball float liquid is provided with the clear water reserviors
Position meter, the floating ball lever meter is electrically connected with the PLC.
8. a kind of emulsion processing equipment according to claim 1, it is characterised in that:The dreg collecting slot is located at the clear water
The top in pond.
9. a kind of emulsion processing equipment according to claim 4, it is characterised in that:The Slag Scraping Device scrapes slag for chain type
Machine, the chain type Slag Scraping Device includes motor, chain type transmission mechanism and scum board, the chain type transmission mechanism and the driving
Motor connection, the scum board is fixed on the chain type transmission mechanism, and the scum board is under chain type transmission mechanism drive
Mobile, the motor is electrically connected with the PLC.
10. a kind of emulsion processing equipment according to claim 1, it is characterised in that:Add in the flocculant medicine-chest
Medicament be PAM, and the flocculant medicine-chest is provided with rabbling mechanism.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710070825.4A CN106630302A (en) | 2017-02-09 | 2017-02-09 | Emulsion treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710070825.4A CN106630302A (en) | 2017-02-09 | 2017-02-09 | Emulsion treatment equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106630302A true CN106630302A (en) | 2017-05-10 |
Family
ID=58844623
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710070825.4A Pending CN106630302A (en) | 2017-02-09 | 2017-02-09 | Emulsion treatment equipment |
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Citations (9)
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CN102249370A (en) * | 2011-05-16 | 2011-11-23 | 云南今业生态建设集团有限公司 | High efficiency integrated processor for oily water |
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