CN208362072U - Purification uses emulsion integrated apparatus online - Google Patents
Purification uses emulsion integrated apparatus online Download PDFInfo
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- CN208362072U CN208362072U CN201820420308.5U CN201820420308U CN208362072U CN 208362072 U CN208362072 U CN 208362072U CN 201820420308 U CN201820420308 U CN 201820420308U CN 208362072 U CN208362072 U CN 208362072U
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- 239000000839 emulsion Substances 0.000 title claims abstract description 68
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- 239000007788 liquid Substances 0.000 claims abstract description 96
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000001914 filtration Methods 0.000 claims abstract description 37
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- 238000004062 sedimentation Methods 0.000 claims abstract 8
- 230000001105 regulatory effect Effects 0.000 claims description 46
- 230000007704 transition Effects 0.000 claims description 12
- 238000005070 sampling Methods 0.000 claims description 8
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
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Abstract
本实用新型涉及工业废水净化再生技术领域，具体公开了一种净化在线使用乳化液一体化装置，包括第一驱动泵、沉淀分离室、过滤分离室、臭氧气浮分离室、电凝聚分离室、固液分离室、浮渣分离室、第二驱动泵、臭氧发生器、净液箱、第三驱动泵和过滤箱，第一驱动泵与过滤箱及沉淀分离室连接，沉淀分离室、过滤分离室、臭氧气浮分离和电凝聚分离室从下到上依次连接，固液分离室设在电凝聚分离室和臭氧气浮分离室的外部，浮渣分离室设在固液分离室的外部，第二驱动泵与过滤分离室、固液分离室及臭氧气浮分离室连接，臭氧发生器与第二驱动泵连接，固液分离室与净液箱连接，第三驱动泵与净液箱及工作区连接，过滤箱与工作区连接用于收集工作区回流的乳化液。
The utility model relates to the technical field of purification and regeneration of industrial wastewater, and specifically discloses an integrated device for purifying on-line use of emulsion, comprising a first driving pump, a sedimentation separation chamber, a filtration separation chamber, an ozone air flotation separation chamber, an electrocoagulation separation chamber, Solid-liquid separation chamber, scum separation chamber, second driving pump, ozone generator, clean liquid tank, third driving pump and filter box, the first driving pump is connected with filter box and sedimentation separation chamber, sedimentation separation chamber, filter separation chamber The chamber, the ozone air flotation separation and the electrocoagulation separation chamber are connected in sequence from bottom to top, the solid-liquid separation chamber is set outside the electrocoagulation separation chamber and the ozone air flotation separation chamber, and the scum separation chamber is set outside the solid-liquid separation chamber. The second drive pump is connected to the filtration separation chamber, the solid-liquid separation chamber and the ozone air flotation separation chamber, the ozone generator is connected to the second drive pump, the solid-liquid separation chamber is connected to the clean liquid tank, the third drive pump is connected to the clean liquid tank and The working area is connected, and the filter box is connected with the working area to collect the emulsion backflowing from the working area.
Description
Technical field
The present invention relates to industrial waste water purifying technical field of regeneration more particularly to a kind of purifications online using emulsion one
Makeup is set.
Background technique
Emulsion plays cooling, lubrication, cleaning and antirust etc. during machining, steel and iron manufacturing, bearing machining etc.
Effect.Emulsion is one of locomotive, the biggish metal working lubricant of auto manufacturing's dosage, has good lubricity, cold concurrently
But property and cleaning are widely used in various cutting technologies.However, it is maximum the disadvantage is that perishable in use
Lose that rotten, stability is poor, service life is short, after putrid and deteriorated, it has to more renew liquid, generate waste emulsified mixture.Waste emulsified mixture
It (HW09) is one of National Industrial hazardous waste, processing cost is fairly expensive.
Environment and human body can be polluted and be damaged just because of emulsion, the use of emulsion and liquid waste processing by
The restriction increasingly strict to environmental regulation.The effective emulsion cleaning equipment of research promotion and reasonable waste emulsified mixture handle skill
Art a, it has also become heat subject of emulsion application study.
Some researchs are carried out to the service life for how extending emulsion both at home and abroad, it is believed that need from routine use and determine
It works well on period management, periodically addition fungicide, preservative can generate certain effect in use, but due to micro- life
The effects of gradually drug resistance of object, effect is worse and worse, and inconvenient for operation in actual application, so, actually answer
Used in reduction.Existing emulsion cleaning equipment is mainly used to reduce particulate matter therein, main to use precipitating, Magneto separate, Jie
The means such as matter filtering, centrifugation, effect is preferable, and still, the rotten the reason of changing of research emulsion is deep not enough comprehensively, takes synthesis
Means purification, which makes it keep the cleaning equipment of service index for a long time also, to be needed further to research and develop.In addition, prior art device is logical
Be commonly present the device is complicated, volume is larger, energy consumption is high, greasy filth inferior separating effect, microorganism removal function are poor, tiny particles content with
In place of the deficiencies of dope purification separation low efficiency.
Summary of the invention
The object of the present invention is to provide a kind of purifications to use emulsion integrated apparatus online, right in the prior art to overcome
The poor problem of the purified treatment effect of emulsion.
In order to solve the above-mentioned technical problems, the present invention provides a kind of purifications to use emulsion integrated apparatus, packet online
The first transfer tube, precipitation and separation room are included, room is separated by filtration, ozone air-float separation chamber, electrocoagulation separation chamber, is separated by solid-liquid separation room, is floating
Slag separation chamber, the second transfer tube, ozone generator, net liquid case, third transfer tube and Rose Box；The import of first transfer tube
It is connect with the Rose Box by the first inlet tube to obtain filtered emulsion, the outlet of first transfer tube passes through the
One outlet tube is connect with the precipitation and separation room；The upper end of the precipitation and separation room is connect with the room of being separated by filtration, the mistake
It filters and is equipped with filter screen in separation chamber, the upper end for being separated by filtration room is connect with the ozone air-float separation chamber, the ozone gas
The upper end of floating separation chamber is connect with the electrocoagulation separation chamber, and electrode group, the solid-liquid point are equipped in the electrocoagulation separation chamber
From the outside that room is located at the electrocoagulation separation chamber and ozone air-float separation chamber, and the upper end opening for being separated by solid-liquid separation room is higher than
The upper end opening of the electrocoagulation separation chamber, the dross separation chamber are located at the outside for being separated by solid-liquid separation room；Described second drives
The import of dynamic pump is connect by the second inlet tube with the top for being separated by filtration room and the lower part for being separated by solid-liquid separation room, described
The outlet of second transfer tube is connect by the second outlet tube with the lower end of the ozone air-float separation chamber, the ozone generator and
The second transfer tube connection；The lower part for being separated by solid-liquid separation room is connect by collecting pipe with the net liquid case, and the third is driven
The import of dynamic pump connect by third inlet tube with the net liquid case, the outlet of the third transfer tube pass through third outlet tube and
Purified emulsion is sent into the online use of workspace circulation, the Rose Box passes through return pipe and work for workspace connection
Area is connected to collect the emulsion of reflux.
Preferably, first transfer tube is diaphragm self priming pump, and first inlet tube is equipped with regulating valve, and described first goes out
Liquid pipe is equipped with regulating valve, sampling valve and pressure gauge, and second outlet tube is equipped with cloth liquid in the indoor end of the precipitation and separation
Pipe.
Preferably, the precipitation and separation room is bucket-shaped, and lower end is equipped with discharge gate.
Preferably, the lower end for being separated by filtration room is equipped with supporting plate, and the filter screen is located on the supporting plate.
Preferably, second transfer tube is multiphase medium pump, and second inlet tube is equipped with vacuum meter and regulating valve, institute
It states the end that the second inlet tube is connect with the room of being separated by filtration and is equipped with regulating valve, second inlet tube and the separation of solid and liquid
The end of room connection is equipped with regulating valve, and second outlet tube is equipped with regulating valve, flowmeter, sampling valve and pressure gauge, described smelly
Oxygen Generator is connect with the second inlet tube close to the end of second transfer tube by pipeline.
Preferably, the side wall of the dross separation chamber is equipped with form and drain valve.
Preferably, the collecting pipe is connect by drain pipe with the room of being separated by filtration, and the drain pipe is equipped with regulating valve.
It preferably, further include that liquid level reconciles room, the collecting pipe is divided into the first regulation pipe and the second regulation pipe and the liquid
Room connection is reconciled in position, and second regulation pipe is equipped with regulating valve, and the liquid level is reconciled room and connected by discharge pipe and the net liquid case
It connects.
Preferably, the Rose Box includes filter frame and transition case, and the filter frame is located at the upper end of the transition case, institute
It states return pipe to connect with the top of the filter frame, first inlet tube is connect with the lower part of the transition case.
Purification of the invention uses having the beneficial effect that for emulsion integrated apparatus online
By precipitation and separation room, it is separated by filtration room, ozone air-float separation chamber, electrocoagulation separation chamber and the company for being separated by solid-liquid separation room
Continuous purification separation separates online each pollutant using in emulsion, selected by each separative unit exist
During purifying various pollutants, new pollutant is not introduced, it is ensured that the original composition of emulsion does not change,
Realize the circulating purification and continuous use of emulsion；
The ozone generated using ozone generator is sucked before the second transfer tube, is controlled by pressure, improves ozone in cream
Change the concentration in liquid, a large amount of micro-bubbles are generated by decompression release, promote bactericidal effect, and can be with oil slick, miscellaneous oil and tiny
Suspended matter collide to be formed wadding grain and bubble complex and be removed, and can to emulsion progress iterative cycles purification, in addition,
For the sterilizer used for ozone generator, effect is very good, and does not introduce any chemical substance, therefore it will not be to emulsion
Secondary pollution is generated with ambient enviroment, working environment can also be improved；
It, can be very tiny particles content and colloid pollution object in emulsion, by electrocoagulation using electrocoagulation separation means
Effect forms larger particles, then forms bubble wadding grain complex by ozone air-float and be removed, simultaneously, moreover it is possible to put on emulsification
The pH value of liquid can also play bactericidal effect；
Whole each section, which is constituted, carries out integrated design, makes small occupation area of equipment, low manufacture cost, good purification,
Also mountable in moving trolley, it is used convenient for scene, is convenient for daily maintenance and cleaning, so, it is easy in equipment manufacturing field
Wide popularization and application.
Detailed description of the invention
Fig. 1 is that the purification of the embodiment of the present invention uses the connection schematic diagram of emulsion integrated apparatus online.
In figure；1: the second transfer tube；2: the second inlet tubes；3: vacuum meter；4: regulating valve；5: regulating valve；6: regulating valve；7:
Regulating valve；8: ozone generator；9: pipeline；10: the second outlet tubes；11: regulating valve；12: flowmeter；13: sampling valve；14: pressure
Power table；15: regulating valve；16: regulating valve；17: drain valve；18: drain valve；19: form；20: electrode group；21: partition；22: receiving
Collector；23: the first regulation pipes；24: the second regulation pipes；25: regulating valve；26: discharge pipe；27: regulating valve；28: regulating valve；29:
Drain pipe；30: filter screen；31: supporting plate；32: liquid distributor；33: pressure gauge；34: regulating valve；35: sampling valve；Go out at 36: the first
Liquid pipe；37: the first transfer tubes；38: the first inlet tubes；39: regulating valve；40: net liquid case；41: third transfer tube；42: workspace；
43: return pipe；44: filter frame；45: transition case；101: precipitation and separation room；102: being separated by filtration room；103: ozone air-float separation
Room；104: electrocoagulation separation chamber；105: being separated by solid-liquid separation room；106: dross separation chamber；107: liquid level regulation room.
Specific embodiment
Embodiments of the present invention are described in further detail with reference to the accompanying drawings and examples.Following embodiment is used for
Illustrate the present invention, but cannot be used to limit the scope of the invention.
In the description of the present invention, it should be noted that term " center ", " longitudinal direction ", " transverse direction ", "upper", "lower",
The orientation or positional relationship of the instructions such as "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside" is
It is based on the orientation or positional relationship shown in the drawings, is merely for convenience of description of the present invention and simplification of the description, rather than instruction or dark
Show that signified device or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as pair
Limitation of the invention.Term " first ", " second " are used for description purposes only, and are not understood to indicate or imply relatively important
Property.Furthermore unless specifically defined or limited otherwise, term " installation ", " connected ", " connection " shall be understood in a broad sense, for example, can
To be to be fixedly connected, may be a detachable connection, or be integrally connected；It can be mechanical connection, be also possible to be electrically connected；It can
To be to be connected directly, the connection inside two elements can also be can be indirectly connected through an intermediary.For this field
For those of ordinary skill, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
As shown in Figure 1, the purification of the present embodiment includes: online the first transfer tube 37 using emulsion integrated apparatus, sinks
Shallow lake separation chamber 101 is separated by filtration room 102, ozone air-float separation chamber 103, electrocoagulation separation chamber 104, is separated by solid-liquid separation room 105, is floating
Slag separation chamber 106, the second transfer tube 1, ozone generator 8, net liquid case 40, third transfer tube 41 and Rose Box.
The import of first transfer tube 37 is connect with Rose Box by the first inlet tube 38 to obtain filtered emulsion, the
The outlet of one transfer tube 37 is connect by the first outlet tube 36 with precipitation and separation room 101；First transfer tube 37 can be for diaphragm certainly
Sucking pump, the first inlet tube 38 are equipped with regulating valve 39, and the first outlet tube 36 is equipped with regulating valve 34, sampling valve 35 and pressure gauge 33, the
End of two outlet tubes 36 in precipitation and separation room 101 is equipped with liquid distributor 32.
Precipitation and separation room 101 be it is bucket-shaped, lower end be equipped with one or two discharge gate, the upper end of precipitation and separation room 101 with
It is separated by filtration the connection of room 102.It is separated by filtration in room 102 and is equipped with filter screen 30, the lower end for being separated by filtration room 102 is equipped with supporting plate
31, filter screen 30 is located on supporting plate 31.It is bottom-up for supporting plate 31, filter screen 30,29 and of drain pipe to be separated by filtration room 102
Second outlet tube 10 is in the port being separated by filtration inside room 102.It is separated by filtration the upper end and ozone air-float separation chamber of room 102
103 connections, ozone air-float separation chamber 103 is surrounded bucket-shaped by partition.The upper end and electrocoagulation separation chamber of ozone air-float separation chamber 103
104 connect, and electrode group 20 are equipped in electrocoagulation separation chamber 104, and surrounded by partition 21.It is separated by solid-liquid separation room 105 and is located at electrocoagulation
The outside of separation chamber 104 and ozone air-float separation chamber 103, and the upper end opening for being separated by solid-liquid separation room 105 is higher than electrocoagulation separation chamber
104 upper end opening.Dross separation chamber 106 is located at the outside for being separated by solid-liquid separation room 105, is used for secondary separation dross, dross separation
Room 106 is surrounded by partition, and the side wall of dross separation chamber 106 is equipped with form 19 and drain valve 17, can also be further added by a discharge
Valve 18.
The import of second transfer tube 1 is by the second inlet tube 2 and is separated by filtration the top of room 102 and is separated by solid-liquid separation room 105
Lower part connection, the outlet of the second transfer tube 1 connect by the second outlet tube 10 with the lower end of ozone air-float separation chamber 103, use
In the emulsion through ozone sterilization is sent into ozone air-float separation chamber 103, ozone generator 8 is connect with the second transfer tube 1, ozone
Generator 8 is sterilizer；Specifically, the second transfer tube 1 can pump for multiphase medium, the second inlet tube 2 is equipped with vacuum meter 3 and adjusts
Valve 4 is saved, or is increasing a regulating valve 5, the second inlet tube 2 is equipped with regulating valve 6 with the end that room 102 is connect is separated by filtration,
For controlling from the end that the amount for being separated by filtration the emulsion that room 102 sucks, the second inlet tube 2 are connect with separation of solid and liquid room 105
Equipped with regulating valve 7, for controlling from the amount for being separated by solid-liquid separation the emulsion that room 105 sucks, the second outlet tube 10 be equipped with regulating valve 11,
Flowmeter 12, sampling valve 13 and pressure gauge 14 and regulating valve 15 and regulating valve 16, ozone generator 8 pass through pipeline 9 and second
Inlet tube 2 is connected close to the end of the second transfer tube 1, for making the second transfer tube 1 provide dissolved air water.
The lower part for being separated by solid-liquid separation room 105 connect 40 with net liquid case by collecting pipe 22, collecting pipe 22 pass through drain pipe 29 and
It is separated by filtration the connection of room 102, drain pipe 29 is equipped with regulating valve 28, and drain pipe 29 is used under special circumstances, will be in collecting pipe 22
Emulsion flow back to and be separated by filtration room 102.It can also include that liquid level reconciles room 107 in the present embodiment, it is first that collecting pipe 22, which divides,
Regulation pipe 23 and the second regulation pipe 24 are reconciled room 107 with liquid level and are connect, and the second regulation pipe 24 is equipped with regulating valve 25, passes through regulating valve
25 switch realizes row's dross, and when regulating valve 25 is opened, dross accumulation when regulating valve 25 is closed, arranges dross, it is logical that liquid level reconciles room 107
It crosses discharge pipe 26 to connect with net liquid case 40, discharge pipe 26 is equipped with regulating valve 27.
The import of third transfer tube 41 is connect by third inlet tube with net liquid case 40, and the outlet of third transfer tube 41 passes through
Third outlet tube is connect so that purified emulsion feeding workspace 42 is recycled online use, third transfer tube with workspace 42
41 i.e. working barrel, Rose Box are connect with workspace 42 by return pipe 43 to collect the emulsion of reflux.Rose Box includes filtering
Frame 44 and transition case 45, filter frame 44 are located at the upper end of transition case 45, and return pipe 43 is connect with the top of filter frame 44, first into
Liquid pipe 38 is connect with the lower part of transition case 45.
The purification for using emulsion integrated apparatus to carry out online using above-mentioned purification uses the liquid integrated side of emulsification online
Method the following steps are included:
S1. preliminary to be separated by solid-liquid separation；
By return pipe 43 being collected into Rose Box using emulsion reflux online, larger in emulsion is filtered out
Grain object；Specifically, by return pipe 43 being flowed into filter frame 44 using emulsified liquid collection online, larger particles filtering point
Emulsion from after flows into the transition case 45 of lower part, and transition case 45 is made of stainless (steel) wire, 100 microns of aperture, fixed
Shi Qingli.
S2. precipitation and separation；
Rose Box internal emulsification liquid is pumped into precipitation and separation room 101 by the first transfer tube 37, carries out precipitation and separation, into
Precipitable particulate matter at one step purification separation.
S3. it is separated by filtration；
Emulsion by precipitation and separation, which is upwardly into, is separated by filtration room 102, filters, further decreases by filter screen 30
Particulate matter therein, 50 microns of filter screen aperture.
S4. ozone air-float separates；
102 top of room is separated by filtration by the second transfer tube 1 and is separated by solid-liquid separation the emulsion extraction of 105 lower part of room, benefit
The ozone generated with sucking ozone generator 8 carries out iterative cycles sterilization to the emulsion of extraction, then by emulsion from ozone
The bottom of flotation separation zone 103 is discharged, and oil slick, miscellaneous oil and fine suspension in micro-bubble and emulsion by being formed
Collision generation cohesion forms bubble particles object complex and is removed, and ozone passes through second after the second transfer tube 1 is cut repeatedly
Outlet tube 10 is sent into the bottom of ozone air-float separation chamber 103, adjusts control by the pressure gauge 14 being arranged on the second outlet tube 10
Pressing pressure is in 0.4Mpa or so.
S5. electrocoagulation separates；
By the electrode group 20 of electrocoagulation separation chamber 104, (electrode group 20 uses aluminium electrode, the aluminium ion generated using anode
The hydroxide ion generated with cathode generates aluminium hydroxide wadding body) very tiny particles content and colloid pollution object in emulsion
Larger particles are gathered by electro-coagulation, then separate the bubble particles object complex of middle formation with ozone air-float, are floated
It is discharged to 104 top of electrocoagulation separation chamber.
S6. two separation of solid and liquid；
Emulsion is by the further separation of separation of solid and liquid room 105, and purified emulsion is by being separated by solid-liquid separation under room 105
The collection of collecting pipe 22 in portion is discharged into net liquid case 40, so far completes emulsion whole purification process, meanwhile, it is separated by solid-liquid separation on room 105
The dross in portion is drained into dross separation chamber 106.Arrange dross method are as follows: the row's of realization dross, regulating valve are switched by regulating valve 25
25 when opening, and dross accumulation when regulating valve 25 is closed, arranges dross, and dross is discharged into dross separation chamber 106, in operational process, according to floating
Slag thickness selects the deslagging time.
Purification of the invention uses having the beneficial effect that for emulsion integrated apparatus online
By precipitation and separation room, it is separated by filtration room, ozone air-float separation chamber, electrocoagulation separation chamber and the company for being separated by solid-liquid separation room
Continuous purification separation separates online each pollutant using in emulsion, selected by each separative unit exist
During purifying various pollutants, new pollutant is not introduced, it is ensured that the original composition of emulsion does not change,
Realize the circulating purification and continuous use of emulsion；
The ozone generated using ozone generator is sucked before the second transfer tube, is controlled by pressure, improves ozone in cream
Change the concentration in liquid, a large amount of micro-bubbles are generated by decompression release, promote bactericidal effect, and can be with oil slick, miscellaneous oil and tiny
Suspended matter collide to be formed wadding grain and bubble complex and be removed, and can to emulsion progress iterative cycles purification, in addition,
For the sterilizer used for ozone generator, effect is very good, and does not introduce any chemical substance, therefore it will not be to emulsion
Secondary pollution is generated with ambient enviroment, working environment can also be improved；
It, can be very tiny particles content and colloid pollution object in emulsion, by electrocoagulation using electrocoagulation separation means
Effect forms larger particles, then forms bubble wadding grain complex by ozone air-float and be removed, simultaneously, moreover it is possible to put on emulsification
The pH value of liquid can also play bactericidal effect；
Whole each section, which is constituted, carries out integrated design, makes small occupation area of equipment, low manufacture cost, good purification,
Also mountable in moving trolley, it is used convenient for scene, is convenient for daily maintenance and cleaning, so, it is easy in equipment manufacturing field
Wide popularization and application.
The embodiment of the present invention is given for the purpose of illustration and description, and is not exhaustively or by this to send out
It is bright to be limited to disclosed form.Many modifications and variations are obvious for the ordinary skill in the art.Choosing
Selecting and describe embodiment is and to make those skilled in the art to more preferably illustrate the principle of the present invention and practical application
It will be appreciated that the present invention is to design various embodiments suitable for specific applications with various modifications.
Claims (9)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
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