CN206315513U - A kind of new oily-water seperating equipment - Google Patents
A kind of new oily-water seperating equipment Download PDFInfo
- Publication number
- CN206315513U CN206315513U CN201621376246.XU CN201621376246U CN206315513U CN 206315513 U CN206315513 U CN 206315513U CN 201621376246 U CN201621376246 U CN 201621376246U CN 206315513 U CN206315513 U CN 206315513U
- Authority
- CN
- China
- Prior art keywords
- storage tank
- seperating equipment
- water seperating
- oily
- membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model is related to fine chemistry industry purification ＆ isolation technical field, and in particular to a kind of new oily-water seperating equipment.It is characterized in that including NF membrane oily-water seperating equipment 1 and negative pressure evaporation purifying plant 2, the discharging opening of NF membrane oily-water seperating equipment 1 is connected with the charging aperture of negative pressure evaporation purifying plant 2, nanofiltration membrane aperture used by the NF membrane oily-water seperating equipment 1 is more than hydrone and less than oil molecule, and NF membrane oily-water seperating equipment 1 can separate the hydrone in raw material；The negative pressure evaporation purifying plant 2 is reclaimed to feedstock purification by heating evaporation under negative pressure and condensation.The utility model is adapted to industrial mass production, and production efficiency height can be adapted to automated production.
Description
Technical field
The utility model is related to fine chemistry industry purification ＆ isolation technical field, and in particular to a kind of new oily-water seperating equipment.
Background technology
Fine chemistry industry to using multi_layer extraction method water-oil separating more, and the method is time-consuming, and the production cycle is long, and efficiency is low；In order to
Promote profit layering, promote water-oil separating plus flocculant to promote water-oil separating using ultrasonic wave again, although this process accelerates oil
Moisture interval velocity, but will oil and water it is completely isolated there is presently no more effective way, and add flocculant and can also draw
Enter new impurity.
The content of the invention
The purpose of this utility model be solve the above problems there is provided a kind of suitable industrial mass production high efficiency oil
Water separation device.
To solve the above problems, the utility model provides following technical scheme：
A kind of new oily-water seperating equipment, it is characterized in that including NF membrane oily-water seperating equipment 1 and negative pressure evaporation purification dress
2 are put, the NF membrane oily-water seperating equipment 1 is self-loopa separator, and the discharging opening of NF membrane oily-water seperating equipment 1 is with bearing
Pressure evaporation purifying plant 2 charging aperture connection, the discharging opening of NF membrane oily-water seperating equipment 1 is provided with densimeter 11 and valve 12,
Nanofiltration membrane aperture used by the NF membrane oily-water seperating equipment 1 is more than hydrone and less than oil molecule, NF membrane water-oil separating dress
The hydrone in raw material can be separated by putting 1；The negative pressure evaporation purifying plant 2 is by heating evaporation under negative pressure and condenses back
Receive to feedstock purification.
Optimization of the present utility model, according to a kind of new oily-water seperating equipment described above, it is characterized in that the nanofiltration
Film oily-water seperating equipment 1 includes dnockout pumps 13, nano filter membrance device 14, circulating pump I15, intermediate material storage tank 16, concentration liquid storage tank
17, the dnockout pumps 13 is connected with the import of nano filter membrance device 14, and the outlet of nano filter membrance device 14 connects with the import of intermediate material storage tank 16
Connect, intermediate material storage tank 16 outlet be connected with the imports of circulating pump I 15, circulating pump I 15 export and the import of nano filter membrance device 14 and
The concentration import of liquid storage tank 17 is connected respectively, in circulating pump I15 outlets and the import of nano filter membrance device 14 and the concentration import of liquid storage tank 17
Valve I 18 and valve II 12 are respectively equipped with connecting line respectively.
Further, a kind of new oily-water seperating equipment according to the top, it is characterized in that the negative pressure evaporation is purified
Device 2 includes vavuum pump 21, the evaporation storage tank 22 provided with chuck, condenser 23, condensate liquid and reclaims storage tank 24, described to be provided with chuck
The charging aperture of evaporation storage tank 22 be connected with the outlet of concentration liquid storage tank 17, the discharging opening of evaporation storage tank 22 provided with chuck and circulating pump II
25 imports are connected, and the outlets of circulating pump II 25 are connected with the charging aperture of evaporation storage tank 22 provided with chuck, the evaporation provided with chuck
The tank bottom of storage tank 22 is provided with sewage draining exit 221, and the steam (vapor) outlet of the evaporation storage tank 22 provided with chuck is connected with the import of condenser 23, institute
State the outlet of condenser 23 to be connected with the condensate liquid recovery charging aperture of storage tank 24, the condensate liquid reclaims storage tank 24 and with vavuum pump 21 connected
Connect.
The beneficial effects of the utility model are：The utility model is adapted to industrial mass production, and material is in NF membrane profit
Constantly separation water outlet is circulated in separator, material is continuously increased due to oil content, and proportion constantly declines, and is set when proportion is reduced to
During definite value, the oil content in material reaches requirement, and material now enters concentration liquid storage tank；Utilize negative pressure evaporation purifying plant pair
Material carries out distilation, impurity is remained in final concentrate, arranged outside with concentrate.The utility model technical approach
Suitable for automatic industrial production.
Brief description of the drawings
Fig. 1 is a kind of structural representation of new oily-water seperating equipment of the utility model；
Reference：NF membrane oily-water seperating equipment -1, densimeter -11, valve I -18, valve II -12, dnockout pumps -
13rd, nano filter membrance device -14, circulating pump I -15, intermediate material storage tank -16, concentration liquid storage tank -17, negative pressure evaporation purifying plant -
2nd, vavuum pump -21, the evaporation storage tank -22 provided with chuck, sewage draining exit -221, condenser -23, condensate liquid reclaim storage tank -24, circulation
Pump II -25.
Embodiment
In order that technological means of the present utility model, creation characteristic, reached purpose and effect are easy to understand, in conjunction with
Specific embodiments and the drawings, the utility model is further elaborated.
Refer to Figure of description 1, a kind of new oily-water seperating equipment, including NF membrane oily-water seperating equipment 1 and negative pressure
Purifying plant 2 is evaporated, the NF membrane oily-water seperating equipment 1 is self-loopa separator, the NF membrane oily-water seperating equipment 1
Discharging opening is connected with the charging aperture of negative pressure evaporation purifying plant 2, and the discharging opening of NF membrane oily-water seperating equipment 1 is provided with densimeter
11, nanofiltration membrane aperture used by the NF membrane oily-water seperating equipment 1 is more than hydrone and less than oil molecule, NF membrane water-oil separating
Device 1 can separate the hydrone in raw material；The negative pressure evaporation purifying plant 2 passes through heating evaporation under negative pressure and condensation
Reclaim to feedstock purification.
The beneficial effects of the utility model are：The utility model is adapted to industrial mass production, and material is in NF membrane profit
Constantly separation water outlet is circulated in separator, material is continuously increased due to oil content, and proportion constantly declines, and is set when proportion is reduced to
During definite value, the oil content in material reaches requirement；Distilation is carried out to material using negative pressure evaporation purifying plant, impurity is residual
Stay in final concentrate, arranged outside with concentrate.
Optimization of the present utility model, the NF membrane oily-water seperating equipment 1 includes dnockout pumps 13, nano filter membrance device 14, followed
Ring pump I 15, intermediate material storage tank 16, concentration liquid storage tank 17, the dnockout pumps 13 are connected with the import of nano filter membrance device 14, nanofiltration
The outlet of film device 14 is connected with the import of intermediate material storage tank 16, and the outlet of intermediate material storage tank 16 is connected with the imports of circulating pump I 15,
Circulating pump I15 export with the import of nano filter membrance device 14 and concentration the import of liquid storage tank 17 is connected respectively, circulating pump I 15 export and
The import of nano filter membrance device 14 and concentration liquid storage tank 17 import are respectively equipped with valve I-18 and valve II 12 on connecting line respectively.
Using the utility model when material proportion is not up to setting value, valve II 12 is closed, and valve I18 is opened, material
The self-loopa in NF membrane oily-water seperating equipment, constantly separates water outlet, when material proportion is not up to setting value, valve II 12
Open, valve I 18 is closed, material enters after concentration liquid storage tank buffering, to be prepared into negative pressure evaporation purifying plant 2.
Further, the negative pressure evaporation purifying plant 2 includes vavuum pump 21, the evaporation storage tank 22 provided with chuck, condenser
23rd, condensate liquid reclaims storage tank 24, and the charging aperture of evaporation storage tank 22 provided with chuck is connected with the outlet of concentration liquid storage tank 17, is provided with
The discharging opening of evaporation storage tank 22 of chuck is connected with circulating pump II25 imports, and the outlets of circulating pump II 25 are stored up with the evaporation provided with chuck
The charging aperture of tank 22 is connected, and the tank bottom of the evaporation storage tank 22 provided with chuck is provided with sewage draining exit 221, the evaporation storage tank provided with chuck
22 steam (vapor) outlet is connected with the import of condenser 23, and the outlet of condenser 23 is reclaimed the charging aperture of storage tank 24 with condensate liquid and is connected,
The condensate liquid reclaims storage tank 24 and is connected with vavuum pump 21.Condenser of the present utility model is plate type heat exchanger, and condensate liquid is water.
Using the utility model, material obtains distilation, separating and removing impurities.Select to evaporate under negative pressure, reduction evaporation
Temperature, reduces damage of the temperature to material structure, and improves evaporation rate, improves production efficiency.
General principle of the present utility model, principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, retouching in above-described embodiment and specification
Preference only of the present utility model is stated, the utility model is not limited by above-mentioned preference, is not departing from the utility model
On the premise of spirit and scope, the utility model can also have various changes and modifications, and these changes and improvements both fall within this practicality
In new claimed scope.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (3)
1. a kind of new oily-water seperating equipment, it is characterized in that including NF membrane oily-water seperating equipment（1）Purify and fill with negative pressure evaporation
Put（2）, the NF membrane oily-water seperating equipment（1）For self-loopa separator, the NF membrane oily-water seperating equipment（1）Discharging
Mouth and negative pressure evaporation purifying plant（2）Charging aperture is connected, the NF membrane oily-water seperating equipment（1）Discharging opening is provided with densimeter
（11）, the NF membrane oily-water seperating equipment（1）Nanofiltration membrane aperture used is more than hydrone and less than oil molecule, NF membrane profit
Separator（1）Hydrone in raw material can be separated；The negative pressure evaporation purifying plant（2）Steamed by being heated under negative pressure
Hair and condensation are reclaimed to feedstock purification.
2. a kind of new oily-water seperating equipment according to claim 1, it is characterized in that the NF membrane oily-water seperating equipment
（1）Including dnockout pumps（13）, nano filter membrance device（14）, circulating pump（15）, intermediate material storage tank（16）, concentration liquid storage tank
（17）, the dnockout pumps（13）With nano filter membrance device（14）Import is connected, nano filter membrance device（14）Outlet and intermediate material storage tank
（16）Import is connected, intermediate material storage tank（16）Outlet and circulating pump（15）Import is connected, circulating pump（15）Outlet and nanofiltration
Film device（14）Import and concentration liquid storage tank（17）Import is connected respectively, in circulating pump（15）Outlet and nano filter membrance device（14）
Import and concentration liquid storage tank（17）Import is respectively equipped with valve on connecting line respectively（18）And valve（12）.
3. a kind of new oily-water seperating equipment according to claim 1, it is characterized in that the negative pressure evaporation purifying plant（2）
Including vavuum pump（21）, evaporation storage tank provided with chuck（22）, condenser（23）, condensate liquid reclaim storage tank（24）, it is described to be provided with
The evaporation storage tank of chuck（22）Charging aperture and concentration liquid storage tank（17）Outlet connection, the evaporation storage tank provided with chuck（22）Discharging opening
With circulating pump（25）Import is connected, circulating pump（25）Outlet and the evaporation storage tank provided with chuck（22）Charging aperture is connected, described
Evaporation storage tank provided with chuck（22）Tank bottom be provided with sewage draining exit（221）, the evaporation storage tank provided with chuck（22）Steam (vapor) outlet
With condenser（23）Import is connected, the condenser（23）Storage tank is reclaimed with condensate liquid in outlet（24）Charging aperture is connected, described cold
Lime set reclaims storage tank（24）With vavuum pump（21）Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621376246.XU CN206315513U (en) | 2016-12-15 | 2016-12-15 | A kind of new oily-water seperating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621376246.XU CN206315513U (en) | 2016-12-15 | 2016-12-15 | A kind of new oily-water seperating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206315513U true CN206315513U (en) | 2017-07-11 |
Family
ID=59267371
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621376246.XU Expired - Fee Related CN206315513U (en) | 2016-12-15 | 2016-12-15 | A kind of new oily-water seperating equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206315513U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108774582A (en) * | 2018-06-12 | 2018-11-09 | 合肥丰洁生物科技有限公司 | A kind of film condensing device for plant oil extract |
| CN109011715A (en) * | 2018-08-30 | 2018-12-18 | 安徽乐锦记食品有限公司 | A kind of bread processing oil water treatment facilities |
-
2016
- 2016-12-15 CN CN201621376246.XU patent/CN206315513U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108774582A (en) * | 2018-06-12 | 2018-11-09 | 合肥丰洁生物科技有限公司 | A kind of film condensing device for plant oil extract |
| CN109011715A (en) * | 2018-08-30 | 2018-12-18 | 安徽乐锦记食品有限公司 | A kind of bread processing oil water treatment facilities |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203428934U (en) | Concentrating and crystallizing system of copper sulfate solution | |
| CN106938178A (en) | Multi-effect plate type film distilling seawater desalination system based on both vapor compression | |
| CN106241961A (en) | A kind of water treatment facilities utilizing residual heat of electric power plant and method | |
| CN206553207U (en) | It is a kind of to be used for the apparatus system of cobaltous sulfate efficient concentration and continuous crystallisation | |
| CN105217703A (en) | A kind of sextuple-effect evaporation crystallization apparatus and technique thereof being applied to zero discharge of industrial waste water | |
| CN204034286U (en) | Board-like mechanical vapour recompression evaporator | |
| CN206315513U (en) | A kind of new oily-water seperating equipment | |
| CN103253819B (en) | Production technology for treating ternary-monomer wastewater and extracting sodium sulfate | |
| CN205990257U (en) | Strong brine zero discharge treatment evaporated crystallization device | |
| CN106145487A (en) | A kind of technique processing rare-earth trade high-concentration ammonia nitrogenous wastewater reuse | |
| BR112017000545B1 (en) | system and method for producing an organic compound from a sugar source by fermentation | |
| CN206395988U (en) | A kind of system handled for high level salt solution continuous dehydration | |
| CN205662335U (en) | Two -stage forced circulation evaporation crystal system among MVR | |
| CN108128831A (en) | Solar heat pump desalination plant | |
| CN204939142U (en) | Treatment facility of desulfurization waste water that flue gas desulfurization system discharged | |
| CN109133465A (en) | A kind of Waste Heat Reuse vacuum membrane distillation zero discharge treatment device and method | |
| CN106587479A (en) | Industrial electroplating wastewater zero-discharge treatment equipment and treatment process thereof | |
| CN106186201A (en) | A kind of device and method of water-electricity cogeneration | |
| CN206033294U (en) | Seawater desalination processing apparatus of power plant | |
| CN209161730U (en) | A kind of reverse osmosis concentrated water Pure-water Making device | |
| CN101874983A (en) | Method and device for evaporation concentration of depressurized membrane | |
| CN207645990U (en) | The device of extraction saturation saline solution in a kind of industrial wastewater | |
| CN204644036U (en) | The combination treatment equipment of a kind of wastewater treatment for fuel-burning power plant and sea water desaltination | |
| CN207685056U (en) | It handles high-salt wastewater skid-mounted unit and its is concentrated by evaporation structure | |
| CN207986949U (en) | A kind of diluent production condensing crystallizing processing high salinity waste water processing unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170711 Termination date: 20181215 |