CN106110730A - Emulsion reuse integrating device - Google Patents
Emulsion reuse integrating device Download PDFInfo
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- CN106110730A CN106110730A CN201610715370.2A CN201610715370A CN106110730A CN 106110730 A CN106110730 A CN 106110730A CN 201610715370 A CN201610715370 A CN 201610715370A CN 106110730 A CN106110730 A CN 106110730A
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- pneumatic operated
- operated valve
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- blowdown
- valve
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- 239000000839 emulsion Substances 0.000 title claims abstract description 75
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000004140 cleaning Methods 0.000 claims abstract description 54
- 239000007788 liquid Substances 0.000 claims abstract description 40
- 239000002699 waste material Substances 0.000 claims description 31
- 239000000203 mixture Substances 0.000 claims description 29
- 238000001914 filtration Methods 0.000 claims description 13
- 239000002351 wastewater Substances 0.000 claims description 10
- 238000011045 prefiltration Methods 0.000 claims description 9
- 238000010992 reflux Methods 0.000 claims description 7
- 230000000740 bleeding effect Effects 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- 230000001804 emulsifying effect Effects 0.000 claims description 2
- 230000006835 compression Effects 0.000 claims 1
- 238000007906 compression Methods 0.000 claims 1
- 238000012545 processing Methods 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 239000003344 environmental pollutant Substances 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 206010021143 Hypoxia Diseases 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 206010003497 Asphyxia Diseases 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 210000000481 breast Anatomy 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000004027 cell Anatomy 0.000 description 1
- 210000005056 cell body Anatomy 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 239000002173 cutting fluid Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000007954 hypoxia Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000009287 sand filtration Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/56—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/606—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by pressure measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D29/661—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps by using gas-bumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/02—Combinations of filters of different kinds
-
- 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
- C02F1/02—Treatment of water, waste water, or sewage by heating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
-
- 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
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- 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
- C02F2303/14—Maintenance of water treatment installations
Abstract
Present invention is disclosed a kind of emulsion reuse integrating device, including the emulsified liquid collection device being connected by pipeline, pre-filtrating equipment, self-cleaning filter device, and blowdown apparatus, described self-cleaning filter device includes self-cleaning filter, and the several valves being connected with described self-cleaning filter, it is provided with filter element in described self-cleaning filter, described valve includes into water pneumatic operated valve, water outlet pneumatic operated valve, backwash pneumatic operated valve, blowdown pneumatic operated valve, described self-cleaning filter is by closing water inlet pneumatic operated valve and water outlet pneumatic operated valve, control the open and close of backwash pneumatic operated valve and blowdown pneumatic operated valve simultaneously, realize the automatic cleaning to filter element.Described emulsion reuse integrating device also includes the thermostat making clean emulsion keep uniform temperature.Emulsion reuse integrating device of the present invention has the advantages such as automaticity is high, emulsion recycles, device is not easily blocked.
Description
Technical field
The present invention relates to a kind of emulsion reuse integrating device realizing emulsion recycling.
Background technology
Along with the development of machinery manufacturing industry, the cutting fluid used in machine cuts, belong to emulsion the most typical.Emulsion is
A kind of high performance semi-synthetic metal working fluid, is particularly well-suited to the processing of aluminum metal and alloy thereof.Emulsion has cooling, profit
Cunning, cleaning, antirust effect, therefore, emulsion is widely used in mechanical processing industry.
Along with being widely used of emulsion, containing substantial amounts of emulsion in the waste water produced in machining production process,
These emulsions have certain harm to producing, living.Such as, if emulsion is discharged in water, water quality can be deteriorated, endanger Aquatic product
Resource, emulsion easily diffuses into oil film, and related data is recorded, and 4.5 cubic decimeters can form 2.8x10-4Thick for mm oil film, cover
Lid 2.0x104m2Water surface so that water hypoxia, produce stench, cause aquatile because of anoxia death by suffocation.
At present, emulsion filtering recovering system is less, to the emulsion in industrial wastewater in mechanical processing industry application
Process and mainly processed by microbial degradation, physical filtering etc..As Chinese patent literature CN 201704166 U is open
A kind of device processing waste emulsified mixture, including pond, ground, holding vessel, pretreatment tank, mechanical air flotation device, regulating reservoir, ferrum carbon electricity
Solve unit, sewage-collecting well, distributing reservoir, sloping plate oil separation tank, microbial cleaning processing system, Sedimentation tank, Sand Filtration System, pond, ground and storage
Between tank, between holding vessel and pretreatment tank, between pretreatment tank and ferrum carbon electrolysis cells, also set between sewage-collecting well and distributing reservoir
It is equipped with elevator pump, is connected by pipeline between each device.Described waste emulsified mixture processing means, by using microorganism to emulsion
Processing, physical filtering device filters, so that the waste water energy after Chu Liing accesses re-using, but this device
Emulsion cannot be recycled, cause the waste of emulsion.
It addition, the emulsion filtering product sold on market is mainly separate unit filter, does not provide relevant and supporting set
Execute, lack integrated processing means.Plugged filter frequency is high, and after blocking, easy cleaning or self-cleaning frequency height do not cause
Can not outwards supply emulsion by continuous print, automaticity is low.Simultaneously as self-cleaning weak effect, filter core is caused to use the longevity
Ordering short, emulsion replacement frequency is high, ultimately results in operating cost high.
Summary of the invention
It is an object of the invention to overcome the defect of prior art, it is provided that a kind of emulsion reuse integrating device so that breast
Changing liquid reclaiming system more integrated, automaticity is higher, and emulsion can recycle, and is not susceptible to blocking.
For achieving the above object, the present invention proposes following technical scheme: a kind of emulsion reuse integrating device, including passing through
Emulsified liquid collection device, pre-filtrating equipment, self-cleaning filter device and the blowdown apparatus that pipeline is connected, described self-cleaning
Defecator includes self-cleaning filter, and the several valves being connected with described self-cleaning filter, described self-cleaning
Being provided with filter element in filter, described valve includes into water pneumatic operated valve, water outlet pneumatic operated valve, backwash pneumatic operated valve, blowdown pneumatic operated valve, described from
Cleaned filter, by cutting out water inlet pneumatic operated valve and water outlet pneumatic operated valve, controls the unlatching of backwash pneumatic operated valve and blowdown pneumatic operated valve simultaneously
With closedown, it is achieved the automatic cleaning to filter element.
Preferably, described backwash pneumatic operated valve is connected with compressed air, and when blowdown pneumatic operated valve cuts out, backwash pneumatic operated valve is beaten
Open, be passed through compressed air and described filter element is carried out.
Preferably, described water inlet pneumatic operated valve is connected with pre-filtrating equipment, and described water outlet pneumatic operated valve fills with emulsified liquid collection
Putting and be connected, described blowdown pneumatic operated valve is connected with blowdown apparatus by pipeline.
Preferably, the pipeline that described water inlet pneumatic operated valve is connected with pre-filtrating equipment is provided with for detecting pipeline pressure
Electro connecting pressure gauge.
Preferably, described emulsified liquid collection device includes clean emulsified liquid collection groove and waste emulsified mixture collecting tank, described dry
Being provided with for clean emulsion exports the several charging pumps reused in clean emulsified liquid collection groove, described waste emulsified mixture is collected
Groove is provided with for waste emulsified mixture being received the several filtered water pumps being delivered in pre-filtrating equipment.
Preferably, described emulsion reuse integrating device also includes the constant temperature dress being located in described clean emulsified liquid collection groove
Put, described thermostat include for heating steam pipe coil, for cooling condensed water coil pipe, be located at steam pipe coil, condensation
Electric proportional-regulation valve on water coil, and for controlling the temperature sensor of described electric proportional-regulation valve.
Preferably, described blowdown apparatus includes blowdown collecting tank, dredge pump, and is arranged in described blowdown collecting tank
Liquid level controller, described dredge pump is connected with waste emulsified mixture collecting tank and waste water station by pipeline.
Preferably, described dredge pump and waste emulsified mixture collecting tank together with pipeline be provided with several reflux inlet, with waste water
The pipeline that station is connected is provided with several blowoff valve.
Preferably, described pre-filtrating equipment includes several for the preliminary prefilter filtering waste emulsified mixture.
Preferably, described valve also includes that air bleeding valve, described air bleeding valve are connected by pipeline with blowdown pneumatic operated valve.
The invention has the beneficial effects as follows:
Emulsion reuse integrating device of the present invention has that automaticity is high, emulsion recycles, device not
The advantages such as easy blocking.
Accompanying drawing explanation
Fig. 1 is the total integrated figure schematic diagram of the present invention；
Fig. 2 is the emulsified liquid collection device schematic diagram of the present invention；
Fig. 3 is the pre-filtrating equipment schematic diagram of the present invention；
Fig. 4 is the self-cleaning filter device schematic diagram of the present invention；
Fig. 5 is the blowdown apparatus schematic diagram of the present invention；
Fig. 6 is the thermostat schematic diagram of the present invention.
Reference: 10, emulsified liquid collection device, 20, pre-filtrating equipment, 30, self-cleaning filter device, 40, blowdown dress
Put, 50, thermostat, 101, clean emulsion collecting tank, 102, waste emulsified mixture collecting tank 102,201, prefilter, 301, from
Cleaned filter, 302, filter element, 303, water inlet pneumatic operated valve, 304, water outlet pneumatic operated valve, 305, backwash pneumatic operated valve, 306, blowdown pneumatic
Valve, 307, air bleeding valve, 401, blowdown collecting tank, 402, dredge pump, 403, liquid level controller, 404, blowoff valve, 405, reflux inlet,
501, steam pipe coil, 502, condensed water coil pipe, 503, electric proportional-regulation valve, 504, temperature sensor, 60, charging pump, 70, from
Carry out water filter, 80, filtered water pump, 90, electro connecting pressure gauge.
Detailed description of the invention
Below in conjunction with the accompanying drawing of the present invention, the technical scheme of the embodiment of the present invention is carried out clear, complete description.
Shown in Fig. 1, disclosed a kind of emulsion reuse integrating device, including emulsified liquid collection device
10, pre-filtrating equipment 20, self-cleaning filter device 30, blowdown apparatus 40, described emulsified liquid collection device 10 and pre-filtrating equipment
Lead between 20, between pre-filtrating equipment 20 and self-cleaning filter device 30, between blowdown apparatus 40 and emulsified liquid collection device 10
Piping is connected；Wherein, described emulsified liquid collection groove 10 is connected with extraneous tap water, and the pipeline being connected is provided with from the beginning
Water filter 70；Several filtered water pump 80 it is provided with between described emulsified liquid collection device 10 and described pre-filtrating equipment；Described enter
Electro connecting pressure gauge 90 it is additionally provided with, for detecting the pressure in pipe between water pneumatic operated valve 303 and prefilter 201.
Shown in Fig. 1, Fig. 2, described emulsified liquid collection device 10 includes clean emulsified liquid collection groove 101 and waste emulsified mixture
Collecting tank 102, in the present embodiment, in order to reduce the area occupied of emulsion reuse integrating device, described clean emulsified liquid collection
Groove 101 and waste emulsified mixture collecting tank 102 are arranged in same tank, are separated with a barrier sheet, and side is used for collecting dry
Clean emulsion, opposite side is used for collecting waste emulsified mixture.Described clean emulsified liquid collection groove 101 is provided with several charging pump 60, will
Emulsion output in clean emulsified liquid collection groove 101 again with.In the present embodiment, first carry out the configuration of emulsion, beat
Opening running water valve and carry out moisturizing, tap water enters clean emulsion collecting tank 101 He after running water filter 70 filters
Waste emulsified mixture collecting tank 102, treats that clean emulsified liquid collection groove 101 full water and waste emulsified mixture collecting tank 102 water level reach cell body one
When half, close running water valve, open or close relevant valve, automatically start emulsion elevator pump and emulsion charging pump enters
Row circulation, is stirred emulsion, adds certain emulsion to clean emulsified liquid collection groove, and fed circulation 30min,
Complete configuration.Emulsion output after having configured uses, and the emulsion after using turns again to waste emulsified mixture collecting tank
In in 102, wait further filtration treatment.
Shown in Fig. 1, Fig. 3, described pre-filtrating equipment 20 includes several prefilter 201, described prefilter 201 energy
Enough metal impurities oarse-grained in waste emulsified mixture are adsorbed, to reduce self-cleaning frequency, it is ensured that the stable operation of system.Number
In individual prefilter 201, generally employing one, as standby, when a certain prefilter breaks down, can start standby pre-mistake
Filter, it is ensured that system properly functioning.Pre-filtrating equipment 20 and the waste emulsified mixture collecting tank 102 in emulsified liquid collection device 10 it
Between arrange several filtered water pumps 80, it is possible to the waste emulsified mixture in waste emulsified mixture collecting tank 102 is delivered to pre-filtrating equipment 20
In prefilter 201, the pollutant in waste emulsified mixture are tentatively filtered, emulsion after pre-filtering enters self-cleaning
Filter 30 filters again.
Shown in Fig. 1, Fig. 4, self-cleaning filter device 30 includes self-cleaning filter 301, and with described self-cleaning
Several valves that filter 301 is connected, described self-cleaning filter 301 is the tank body of hollow sealing, and inside is provided with filter element
302, use the filter element 302 of 20um that the pollutant in waste emulsified mixture are intercepted, the pollutant in waste emulsified mixture are intercepted
The surface of filter element 302, thus reach the effect filtered, the emulsion after filtration can reach the standard of reuse.Self-cleaning filter
The housing of 301 is provided with several opening, and each opening part is designed with valve.Described valve includes into water pneumatic operated valve 303, goes out aqueous vapor
Dynamic valve 304, backwash pneumatic operated valve 305, blowdown pneumatic operated valve 306, air bleeding valve 307.Wherein, water inlet pneumatic operated valve 303 passes through pipeline with pre-
The outfan of defecator 20 is connected, thus the emulsion after tentatively filtering is delivered in self-cleaning filter 301 carry out
Again filter, by the emulsion after secondary filter at water outlet pneumatic operated valve 304, emulsion is delivered to clean emulsifying by pipeline
In liquid collecting tank 101, clean emulsion is finally exported by charging pump 60.Backwash pneumatic operated valve 305 is connected with air compressor
Connect, for self-cleaning filter 301 is passed through compressed air during self-cleaning.Described blowdown pneumatic operated valve 306 is by pipeline and blowdown
Device 40 is connected, and the sewage after self-cleaning, pollutant transportation is further processed to blowdown apparatus 40.Described aerofluxus
Valve 307 and blowdown pneumatic operated valve 306, by pipeline communication, the compressed gas that will produce during blowdown pneumatic operated valve 306 blowdown, carry again
To self-cleaning filter 301, compressed gas is recycled, reduce the waste of resource.
When the pollutant that the filter element 302 in self-cleaning filtering dress device filters get more and more, filter element 302 can block gradually,
Owing to filtered water pump 80 is carrying waste emulsified mixture always, now, pipe content is easily generated certain intake pressure, electro connecting pressure gauge
After 90 detect that intake pressure exceeds pre-set value, self-cleaning filter device 30 is started working, in self-cleaning filter 301
Filter element 302 is carried out.Self-cleaning filter 301 uses airblasting cleaning technique, utilizes compressed air release to produce
The energy of jet and shock wave, makes the medium of surrounding loosen, crush, thus reaches the purpose of cleaning and descaling, have pollution-free, hold
Continuous work, the advantage saving water power.In the present embodiment, (during backwash, emulsion elevator pump stops, not shown) backwash includes following
Step, can also carry out self-defined to cleaning certainly as required, as control be passed through compressed-air actuated duration, valve open or
The duration etc. closed.Concrete, step is as follows:
A () closes water inlet pneumatic operated valve 303, water outlet pneumatic operated valve 304, and blowdown pneumatic operated valve 306, backwash pneumatic operated valve 305 dozens
Open, carry compressed air, time a length of 8s；
B () blowdown pneumatic operated valve 306 is opened 15s and is carried out onepull cleaning；
C () blowdown pneumatic operated valve 306 cuts out 8s, now continue to be passed through compressed air；
D () blowdown pneumatic operated valve 306 is opened 8s and is carried out secondary blasting cleaning；
E () blowdown pneumatic operated valve 306 cuts out 5s and continues air inlet；
F () blowdown pneumatic operated valve 306 is opened 8s and is carried out three separate explosion cleanings；
G () backwash pneumatic operated valve 305 cuts out, stop air inlet；
H () blowdown pneumatic operated valve 306 cuts out；
I () water inlet pneumatic operated valve 303 is opened, water outlet pneumatic operated valve 304 is opened.
Can produce emulsion in self-cleaning filter 301 cleaning process, described emulsion includes emulsion and a large amount of impurity,
Described emulsion enters blowdown apparatus 40, as it is shown in figure 5, blowdown apparatus 40 includes blowdown collecting tank 401, dredge pump 402 and liquid
Level controller 403, described dredge pump 402 connects has plural blowoff valve 404 and reflux inlet 405, described dredge pump 402 to pass through pipeline
It is connected with blowdown collecting tank 401 and waste water station.Described reflux inlet 405 is arranged on dredge pump 402 and connects with blowdown collecting tank 401
Pipeline on, blowoff valve 404 is arranged on the pipeline that dredge pump 402 connects with waste water station.Described liquid level controller 403 is used for
Liquid height in monitoring blowdown collecting tank 401, when liquid level reaches preset height, performs corresponding instruction.Self-cleaning
During produce waste water in blowdown collecting tank 401, stands a period of time after, it may appear that be layered, impurity swims on emulsion
Side.After standing completes, open reflux inlet 405, start dredge pump 402, bottom emulsion is delivered to waste emulsified mixture collecting tank 102
In, when the liquid level in blowdown collecting tank 401 reaches default height, sewage draining valve 404 quits work, now, and reflux inlet 405
Closing, blowoff valve 404 is opened, and dredge pump 402 is again started up, and is emitted in waste water station by impurity, is further processed.
Further, for needing to keep the situation of constant temperature, as shown in Figure 6, the present invention uses thermostat 50, protects
Hold constant temperature.Run winter and be mainly as the criterion with heating, be cooled to auxiliary；Summer is mainly main to be cooled to, and is heated to be auxiliary, thus ensures
Stablizing of temperature.Described thermostat 50 includes steam pipe coil 501, the condensation being arranged in clean emulsified liquid collection groove 101
The electric proportional-regulation valve 503 arranged on water coil 502, and steam pipe coil 501 and condensed water coil pipe 502, described steam disc
In pipe 501, circulation is passed through steam, in the present embodiment, preferably 170 DEG C steam, can constantly heat emulsion；Institute
State and condensed water coil pipe 502 is passed through cooling water, can constantly emulsion be cooled down.Described electric proportional-regulation valve 503
Perform to operate accordingly by the feedback of temperature sensor 504.In the present embodiment, use fully automatic operation, without adjusting valve
Door, only need to switch to related valve knob automatically, can keep temperature stabilization in ± 1 DEG C.
Further, as a example by maintaining the temperature at 40 ± 1 DEG C.
Winter operation: when temperature is less than 37 DEG C, and the electric proportional-regulation valve 503 on steam pipe coil 501 is opened, and is passed through 170
DEG C steam, heats emulsion, is heated to 39 DEG C；Now, the electric proportional-regulation valve on condensed water coil pipe 503 dozens
Opening, thorough fare cooling water, 170 DEG C of steam and cooling water exist simultaneously, thus ensure constant temperature 40 ± 1 DEG C.
Summer operation: when temperature is higher than 42 DEG C, and the electric proportional-regulation valve 503 on cooling water coil loop is opened, cooling
To 39 DEG C, now, the electric proportional-regulation valve 503 on steam pipe coil loop is opened, and is passed through 170 DEG C of steam, steam and cooling water
Open, it is ensured that temperature is at 40 ± 1 DEG C simultaneously.
Emulsion reuse integrating device of the present invention has that automaticity is high, emulsion recycles, device not
The advantages such as easy blocking.
The technology contents of the present invention and technical characteristic have revealed that as above, but those of ordinary skill in the art still may base
All replacements without departing substantially from spirit of the present invention and modification, therefore, scope is made in teachings of the present invention and announcement
The content disclosed in embodiment should be not limited to, and the various replacement without departing substantially from the present invention and modification should be included, and be this patent Shen
Please claim be contained.
Claims (10)
1. an emulsion reuse integrating device, it is characterised in that the emulsified liquid collection device that includes being connected by pipeline, pre-
Defecator, self-cleaning filter device and blowdown apparatus, described self-cleaning filter device includes self-cleaning filter, and
The several valves being connected with described self-cleaning filter, are provided with filter element in described self-cleaning filter, described valve include into
Water pneumatic operated valve, water outlet pneumatic operated valve, backwash pneumatic operated valve, blowdown pneumatic operated valve, described self-cleaning filter is by closing water inlet pneumatic operated valve
With water outlet pneumatic operated valve, control the open and close of backwash pneumatic operated valve and blowdown pneumatic operated valve, it is achieved the automatic cleaning to filter element simultaneously.
Emulsion reuse integrating device the most according to claim 1, it is characterised in that described backwash pneumatic operated valve and compression sky
Gas phase connects, and when blowdown pneumatic operated valve cuts out, backwash pneumatic operated valve is opened, and is passed through compressed air and is carried out described filter element.
Emulsion reuse integrating device the most according to claim 1, it is characterised in that described water inlet pneumatic operated valve and pre-filtering
Device is connected, and described water outlet pneumatic operated valve is connected with emulsified liquid collection device, and described blowdown pneumatic operated valve passes through pipeline and blowdown
Device is connected.
Emulsion reuse integrating device the most according to claim 3, it is characterised in that described water inlet pneumatic operated valve and pre-filtering
The pipeline that device is connected is provided with the electro connecting pressure gauge for detecting pipeline pressure.
Emulsion reuse integrating device the most according to claim 1, it is characterised in that described emulsified liquid collection device includes
Clean emulsified liquid collection groove and waste emulsified mixture collecting tank, be provided with for by defeated for clean emulsion in described clean emulsified liquid collection groove
Go out the several charging pumps reused, described waste emulsified mixture collecting tank is provided with for waste emulsified mixture receipts are delivered to pre-filtering dress
Several filtered water pumps in putting.
Emulsion reuse integrating device the most according to claim 5, it is characterised in that described emulsion reuse integrating device is also
Including the thermostat being located in described clean emulsified liquid collection groove, described thermostat include for heating steam pipe coil,
For the condensed water coil pipe of cooling, it is located at the electric proportional-regulation valve on steam pipe coil, condensed water coil pipe, and is used for controlling institute
State the temperature sensor of electric proportional-regulation valve.
Emulsion reuse integrating device the most according to claim 5, it is characterised in that described blowdown apparatus includes that blowdown is received
Collection groove, dredge pump, and it is arranged on the liquid level controller in described blowdown collecting tank, described dredge pump is by pipeline and useless emulsifying
Liquid collecting tank is connected with waste water station.
Emulsion reuse integrating device the most according to claim 7, it is characterised in that described dredge pump is received with waste emulsified mixture
Collection groove together with pipeline be provided with several reflux inlet, the pipeline being connected with waste water station is provided with several blowoff valve.
Emulsion reuse integrating device the most according to claim 1, it is characterised in that described pre-filtrating equipment includes several
For the preliminary prefilter filtering waste emulsified mixture.
Emulsion reuse integrating device the most according to claim 1, described valve also includes air bleeding valve, described air bleeding valve
It is connected by pipeline with blowdown pneumatic operated valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610715370.2A CN106110730A (en) | 2016-08-24 | 2016-08-24 | Emulsion reuse integrating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610715370.2A CN106110730A (en) | 2016-08-24 | 2016-08-24 | Emulsion reuse integrating device |
Publications (1)
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| CN106110730A true CN106110730A (en) | 2016-11-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610715370.2A Pending CN106110730A (en) | 2016-08-24 | 2016-08-24 | Emulsion reuse integrating device |
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| CN (1) | CN106110730A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110314946A (en) * | 2019-06-06 | 2019-10-11 | 铜陵精迅特种漆包线有限责任公司 | A kind of aluminium bar climbs pipe cooling device |
| CN110340162A (en) * | 2019-06-06 | 2019-10-18 | 铜陵精迅特种漆包线有限责任公司 | A kind of aluminium bar production system |
| CN111137960A (en) * | 2020-01-13 | 2020-05-12 | 宁波渤川废液处置有限公司 | Air-float separation method and device for solid-liquid separation in waste emulsion |
| CN114011894A (en) * | 2021-10-28 | 2022-02-08 | 保定天威线材制造有限公司 | Processing device and method for drawing machine emulsion for producing electromagnetic wire bare conductor |
| CN114949998A (en) * | 2022-06-14 | 2022-08-30 | 江苏大学镇江流体工程装备技术研究院 | Emulsion online preparation and cyclic regeneration complete equipment in steel rolling production process |
| CN115518454A (en) * | 2022-08-08 | 2022-12-27 | 黄山艾肯机械制造有限公司 | Main shaft center goes out water system |
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| CN115518454A (en) * | 2022-08-08 | 2022-12-27 | 黄山艾肯机械制造有限公司 | Main shaft center goes out water system |
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Application publication date: 20161116 |