CN107557146A - A kind of egg oil extracting system for carrying cleaning function - Google Patents
A kind of egg oil extracting system for carrying cleaning function Download PDFInfo
- Publication number
- CN107557146A CN107557146A CN201710892520.1A CN201710892520A CN107557146A CN 107557146 A CN107557146 A CN 107557146A CN 201710892520 A CN201710892520 A CN 201710892520A CN 107557146 A CN107557146 A CN 107557146A
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- CN
- China
- Prior art keywords
- storage tank
- heat exchanger
- water storage
- cleaning function
- egg oil
- 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.)
- Granted
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 238000003860 storage Methods 0.000 claims abstract description 44
- 238000000605 extraction Methods 0.000 claims abstract description 27
- 238000001816 cooling Methods 0.000 claims abstract description 24
- 238000004891 communication Methods 0.000 claims abstract description 8
- 239000000498 cooling water Substances 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 18
- 238000001514 detection method Methods 0.000 claims description 14
- 238000000889 atomisation Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 10
- 239000002904 solvent Substances 0.000 claims description 7
- 230000001502 supplementing effect Effects 0.000 claims 1
- 238000012856 packing Methods 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000008676 import Effects 0.000 description 4
- 230000002101 lytic effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000007792 addition Methods 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000006052 feed supplement Substances 0.000 description 1
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 235000013599 spices Nutrition 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Meat, Egg Or Seafood Products (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention discloses a kind of egg oil extracting system for carrying cleaning function, including the CO being sequentially connected2Storage tank, compressor, First Heat Exchanger, extraction kettle, forecooler, the first separating still and the second separating still；Two primary sides of First Heat Exchanger are connected to hot water storage tank and cold water storage tank, and hot water storage tank and cold water storage tank are also associated with boilers heated electrically；The cooling water input of forecooler and output port connect cold water storage tank and cooling tower, the output end connection cold water storage tank of cooling tower respectively；The secondary end of First Heat Exchanger is also communicated with atomising device, the secondary end alternate communication CO of First Heat Exchanger2Storage tank and atomising device；The output end of second separating still is serially connected with dirt collecting tank.Steam is obtained by atomising device, heats to obtain high-temperature steam by the primary side of heat exchanger, compressor provides steam power and pressure, the steam of HTHP dissolve dirt in the equipment such as extraction kettle and separating still and exports dirt into dirt collecting tank.
Description
Technical field
The present invention relates to a kind of biological extracting system, and system is extracted more particularly, to a kind of egg oil for carrying cleaning function
System.
Background technology
In egg oil extracting system, the equipment such as extraction kettle and separating still accumulates dirt after a certain period of use time, causes to extract
Take the production efficiency of the equipment such as kettle and separating still low.In existing equipment cleaning method, lytic agent is imported using system pipeline,
Lytic agent dissolves to the residual soil in equipment and discharged with lytic agent.
However, this kind of mode can not dissolve part dirt, the effect of lytic agent export dirt is also not high enough, and part dirt is still
Residual is in a device.
The content of the invention
For overcome the deficiencies in the prior art, it is an object of the invention to provide a kind of egg oil extraction for carrying cleaning function
System, solve First Heat Exchanger output absorbed heat after water and preheater output be heated after water conservancy with it is bad, cool down
The problem of tower needs workload larger.
The present invention is to solve the technical scheme that its technical problem uses to be：
A kind of egg oil extracting system for carrying cleaning function, including the CO being sequentially connected2Storage tank, compressor, first are changed
Hot device, extraction kettle, forecooler, the first separating still and the second separating still；Two primary sides of the First Heat Exchanger connect respectively
There are hot water storage tank and cold water storage tank, hot water storage tank and cold water storage tank are also associated with boilers heated electrically；The cooling water of the forecooler is defeated
Enter and output port connects cold water storage tank and cooling tower, the output end connection cold water storage tank of cooling tower respectively；First heat exchange
The secondary end of device is also communicated with atomising device, the secondary end alternate communication CO of First Heat Exchanger2Storage tank and atomising device；Described
The output end of two separating stills is serially connected with dirt collecting tank.
Preferably, the CO2Storage tank and atomising device are changed by the first valve body and the second valve body alternate communication first respectively
The secondary end of hot device.
Preferably, the atomising device includes atomization box, is arranged on the defeated of the interior connection First Heat Exchanger secondary end of atomization box
Outlet pipe, the atomizer for being arranged on output pipe port one side.
Preferably, the atomising device includes the atomization generator tube of connection First Heat Exchanger secondary end, is located in atomization hair
Atomizer on raw pipe perisporium.
Preferably, the dirt collecting tank is connected with solvent input pipe and blow-off pipe.
Preferably, the dirt collecting tank also connects compressor.
Preferably, the extraction kettle, the first separating still and the second separating still are respectively arranged with exhaust-valve.
Preferably, the hot water storage tank is also associated with the second heat exchanger, the secondary end connection hot water of second heat exchanger
Storage tank, the primary side of the second heat exchanger are communicated with gas furnace.
Preferably, in addition to automatic feeding device, the automatic feeding device include Material disintegrator, the agitator being sequentially connected
And extraction kettle, automatic feeding device also include controller, the pressure detection means being arranged on extraction kettle, are arranged in agitator
Liquid level detection device；Material disintegrator connects mixer by mateiral pump, and mixer connects extraction kettle by drawing liquid pump, and agitator connects
It is connected with small pump；The pressure detection means, liquid level detection device, small pump, mateiral pump and drawing liquid pump electrically connect controller.
A kind of egg oil extracting system for carrying cleaning function that the present invention uses, has the advantages that：Heat exchanger
Secondary end be also associated with atomising device, by atomising device obtain steam, heat to obtain high temperature by the primary side of heat exchanger
Steam, compressor provides steam power and pressure, the steam of HTHP dissolve dirt in the equipment such as extraction kettle and separating still
And export dirt into dirt collecting tank, settled in the solvent of dirt collecting tank.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the structural representation of automatic feeding device of the present invention；
Fig. 3 is the connection diagram of the second heat exchanger of the invention.
Embodiment
Below in conjunction with accompanying drawing and example, the invention will be further described.
As shown in figure 1, a kind of egg oil extracting system for carrying cleaning function of the present invention, including the CO being sequentially connected2
Storage tank 1, compressor 2, First Heat Exchanger 3, extraction kettle 4, forecooler 5, the first separating still 6 and the second separating still 7；Described first changes
Two primary sides of hot device 3 are connected to hot water storage tank 9 and cold water storage tank 10, and hot water storage tank 9 and cold water storage tank 10 are also connected with
There is boilers heated electrically 11；The cooling water input of the forecooler 5 and output port connect cold water storage tank 10 and cooling tower 12 respectively, cold
But the output end connection cold water storage tank 10 of tower 12；The secondary end of the First Heat Exchanger 3 is also communicated with atomising device 13, and first changes
The secondary end alternate communication CO of hot device 32Storage tank 1 and atomising device 13；The output end of second separating still 7 is serially connected with dirt collecting tank
8。
The secondary end alternate communication CO of First Heat Exchanger 32Storage tank 1 and atomising device 13, in First Heat Exchanger 3, pass through heat
Water is to CO2And steam heating, mode of heating stability and high efficiency.
In egg oil extracting system, when performing egg oil extraction process, CO2From CO2Storage tank 1 imports, and compressor 2 provides CO2
Circulation power and pressure in system pipeline.Work as CO2Flow to First Heat Exchanger 3, the hot water pair of the primary side of First Heat Exchanger 3
The CO of secondary end2Heated, the water of the primary side of First Heat Exchanger 3 output more low temperature, the part water is directed at cold water storage tank 10
Or cooling tower 12；In extraction kettle 4, the CO of HTHP2Parcel egg oil functionality is simultaneously discharged, and egg oil main component is defeated
Deliver to separating still；In forecooler 5, CO is reduced2Temperature, forecooler 5 export the water of more high temperature, and the part water is directed at cooling tower 12
Or boilers heated electrically 11；CO in separating still2Temperature and pressure are relatively low, realize the CO in separating still2Isolate.
In egg oil extracting system, during execution system equipment line clear, input CO is closed2And heat exchanger secondary end connects
Atomising device 13.Atomising device 13 produces atomized steam, and steam enters heat exchanger secondary end and heated by primary side, heat exchanger
Level end output high-temperature steam；Meanwhile compressor 2 provides high-temperature steam power and pressure, the high temperature and high pressure steam is in equipment and pipe
Flow and dissolve and carry dirt in road.Dirt is finally connected to dirt collecting tank 8, and is settled in dirt collecting tank 8.
Further have, the CO2Storage tank 1 and atomising device 13 pass through the first valve body and the second valve body alternate communication respectively
The secondary end of First Heat Exchanger 3；First valve body and the second valve body are switch valve.When extracting system performs egg oil extraction work
During skill, close the second valve body and open the first valve body, CO2From CO2Storage tank 1 exports and compressor 2 provides CO2Circulation power, CO2
The extraction of egg oil main component is completed in circulation in system.When extracting system performs cleaning, close the first valve body and beat
The second valve body is opened, atomising device 13 imports atomized steam, and steam enters heat exchanger secondary end and heated by primary side and be changed into high
Warm steam, compressor 2 provide high-temperature steam circulation power and pressure, the steam of HTHP circulate in systems and dissolve and
Carry dirt.
Preferably, the atomising device 13 includes atomization box, is arranged on the connection secondary end of First Heat Exchanger 3 in atomization box
Efferent duct, the atomizer for being arranged on output pipe port one side.Atomizer is atomized in output pipe port to water, and steam is from output
Pipe is connected to heat exchanger.Atomization box is set, improves absorptivity of the efferent duct to steam.
Preferably, the dirt collecting tank 8 is connected with solvent input pipe and blow-off pipe；The separation of connection second in the dirt collecting tank 8
The port of kettle 7 is higher than liquid level less than solvent liquid level, ventilation mouth.When execution system equipment line clear, close the first valve body and
While opening the second valve body, dirt collecting tank 8 imports solvent.
Further have, the dirt collecting tank 8 also connects compressor 2.When execution system extraction process, lead in dirt collecting tank 8
Cross blow-off pipe to discharge dirt and solvent, the CO of the second separating still 7 discharge2Compressor 2, CO is drained into by dirt collecting tank 82Obtain
Cycling and reutilization.
Preferably, the extraction kettle 4, the first separating still 6 and the second separating still 7 are respectively arranged with exhaust-valve.Execution system
In equipment cleaning, the steam for carrying dirt can be outwards discharged by exhaust-valve.Preferably, the exhaust-valve passes through snap joint
Conduit is connected with, conduit is communicated with sewage sump.
As shown in figure 3, the hot water storage tank 9 is also associated with the second heat exchanger 18, the secondary end of second heat exchanger 18
Hot water storage tank 9 is connected, the primary side of the second heat exchanger 18 is communicated with gas furnace 19.The gas furnace 19 for obtaining hot water, hot water are set
Acquisition have alternative plan.
As shown in Fig. 2 further have, in addition to automatic feeding device, the automatic feeding device include being sequentially connected
Material disintegrator, agitator and extraction kettle 4, automatic feeding device also include controller, be arranged on extraction kettle 4 pressure detection dress
The liquid level detection device put, be arranged in agitator；Material disintegrator passes through drawing liquid by mateiral pump 17c connection mixers, mixer
Pump 17d connections extraction kettle 4, agitator is communicated with small pump；The pressure detection means, liquid level detection device, small pump, take out material
Pump 17c and drawing liquid pump 17d electrically connect controller.When extraction kettle 4 exports material and relatively low pressure to separating still, controller connects
Receive pressure detection means signal and control drawing liquid pump 17d to import egg oil material solution from agitator；When liquid level is low in agitator
When certain position, controller receives liquid level detection signal and controls suction pump and mateiral pump 17c to extract powder out from Material disintegrator
Egg oil raw material.The mateiral pump 17c and drawing liquid pump 17d are connected with filter.Automatic feeding device is designed, realizes extraction kettle 4
Feed supplement automates, and improves production efficiency, reduces production cost.
Cooling tower 12 includes the first cooling chamber and the second cooling chamber, and packing layer is provided with the first cooling chamber；First cooling
The perisporium of room opens up the first air inlet, and the first air inlet is less than packing layer；The first air outlet is provided with the top of first cooling chamber,
First air outlet is provided with the first blower fan；Packing layer is respectively arranged with water-locator and water leg over and under.First blower fan
Air force is provided, air enters from the first air inlet, exported through spice layer and from the first air outlet；The water that cools down is needed from cloth
Hydrophone is sprayed to packing layer and air-cooled in packing layer.Second cooling chamber includes upper chambers and lower chamber, upper chambers and bottom
Chamber is respectively arranged with the second air outlet and the second air inlet, and the second air inlet is provided with the second blower fan；The lower chamber is provided with
The cooling tube of water leg is connected, the cooling tube is in the shape of a spiral；It is dividing plate between the upper chambers and water leg.Set spiral helicine
Cooling tube, increase air-cooled film-cooled heat；Be dividing plate between upper chambers and water leg, the second cooling chamber it is distinguished and admirable through upper chambers and to collection
Water in tank is absorbed heat.The design of the first cooling chamber and the second cooling chamber of cooling tower 12, the water in tower can be carried out
Three steps cool down, larger raising cooling effect.
It is described above, it is not limitation of the present invention, the present invention is also not limited to above-mentioned embodiment, as long as at this
The variations, modifications, additions or substitutions made in the essential scope of invention, so as to reach the technique effect of the present invention, it should all belong to
In protection scope of the present invention.
Claims (9)
- A kind of 1. egg oil extracting system for carrying cleaning function, it is characterised in that：Including the CO being sequentially connected2Storage tank (1), pressure Contracting machine (2), First Heat Exchanger (3), extraction kettle (4), forecooler (5), the first separating still (6) and the second separating still (7)；Described Two primary sides of one heat exchanger (3) are connected to hot water storage tank (9) and cold water storage tank (10), hot water storage tank (9) and cold water Storage tank (10) is also associated with boilers heated electrically (11)；The cooling water input of the forecooler (5) and output port connect cold water respectively Storage tank (10) and cooling tower (12), the output end connection cold water storage tank (10) of cooling tower (12)；Time of the First Heat Exchanger (3) Level end is also communicated with atomising device (13), the secondary end alternate communication CO of First Heat Exchanger (3)2Storage tank (1) and atomising device (13)；The output end of second separating still (7) is serially connected with dirt collecting tank (8).
- A kind of 2. egg oil extracting system for carrying cleaning function according to claim 1, it is characterised in that：The CO2Storage Tank (1) and atomising device (13) pass through the first valve body and the secondary end of the second valve body alternate communication First Heat Exchanger (3) respectively.
- 3. according to a kind of any described egg oil extracting system for carrying cleaning function of claim 1 and 2, it is characterised in that： The atomising device (13) includes atomization box, is arranged on the efferent duct of connection First Heat Exchanger (3) secondary end in atomization box, sets Atomizer in output pipe port one side.
- 4. according to a kind of any described egg oil extracting system for carrying cleaning function of claim 1 and 2, it is characterised in that： The atomising device (13) includes the atomization generator tube of connection First Heat Exchanger (3) secondary end, is located in atomization generator tube perisporium On atomizer.
- A kind of 5. egg oil extracting system for carrying cleaning function according to claim 1, it is characterised in that：The dirt collection Tank (8) is connected with solvent input pipe and blow-off pipe.
- 6. according to a kind of any described egg oil extracting system for carrying cleaning function of claim 1 and 5, it is characterised in that： The dirt collecting tank (8) also connects compressor (2).
- A kind of 7. egg oil extracting system for carrying cleaning function according to claim 1, it is characterised in that：The extraction Kettle (4), the first separating still (6) and the second separating still (7) are respectively arranged with exhaust-valve.
- A kind of 8. egg oil extracting system for carrying cleaning function according to claim 1, it is characterised in that：The hot water Storage tank (9) is also associated with the second heat exchanger (18), the secondary end connection hot water storage tank (9) of second heat exchanger (18), and second The primary side of heat exchanger (18) is communicated with gas furnace (19).
- A kind of 9. egg oil extracting system for carrying cleaning function according to claim 1, it is characterised in that：Also include certainly Dynamic feed supplementing device, the automatic feeding device include Material disintegrator, agitator and the extraction kettle (4) being sequentially connected, automatic feeding dress Putting also includes controller, the pressure detection means being arranged on extraction kettle (4), the liquid level detection device being arranged in agitator； Material disintegrator connects mixer by mateiral pump (17c), and mixer connects extraction kettle (4), agitator connection by drawing liquid pump (17d) There is small pump；The pressure detection means, liquid level detection device, small pump, mateiral pump (17c) and drawing liquid pump (17d) are electrically connected Connect controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710892520.1A CN107557146B (en) | 2017-09-27 | 2017-09-27 | Yolk oil extraction system with cleaning function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710892520.1A CN107557146B (en) | 2017-09-27 | 2017-09-27 | Yolk oil extraction system with cleaning function |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107557146A true CN107557146A (en) | 2018-01-09 |
| CN107557146B CN107557146B (en) | 2024-03-12 |
Family
ID=60983469
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710892520.1A Active CN107557146B (en) | 2017-09-27 | 2017-09-27 | Yolk oil extraction system with cleaning function |
Country Status (1)
| Country | Link |
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| CN (1) | CN107557146B (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
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| DE102008041733A1 (en) * | 2008-09-01 | 2010-03-25 | Voith Patent Gmbh | Process for tank cleaning |
| CN202161830U (en) * | 2011-05-20 | 2012-03-14 | 青岛利和萃取科技有限公司 | Supercritical carbon dioxide extraction device |
| CN204824121U (en) * | 2015-07-31 | 2015-12-02 | 山东新华医疗器械股份有限公司 | It washs and online sterilization system to blow integrative equipment on -line of embedment |
| CN204874446U (en) * | 2015-06-22 | 2015-12-16 | 临泉县华丰农植物炼油有限公司 | Ginger oil distillation extraction element that cleaned and filtrated in area |
| CN105695087A (en) * | 2016-03-08 | 2016-06-22 | 深圳市华之粹生态科技有限公司 | Subcritical fluid extraction device and method |
| CN205641676U (en) * | 2016-04-11 | 2016-10-12 | 中山市曜禾生物技术有限公司 | Board trades formula water supply installation and plant essential oil extraction system |
| CN207391368U (en) * | 2017-09-27 | 2018-05-22 | 珠海澳盈生物科技有限公司 | A kind of egg oil extracting system for carrying cleaning function |
-
2017
- 2017-09-27 CN CN201710892520.1A patent/CN107557146B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1648224A (en) * | 2004-12-31 | 2005-08-03 | 东营广元生物工程有限公司 | Super critical CO2 precision separating process device |
| DE102008041733A1 (en) * | 2008-09-01 | 2010-03-25 | Voith Patent Gmbh | Process for tank cleaning |
| CN201337830Y (en) * | 2009-01-06 | 2009-11-04 | 钱如树 | Super-critical CO* fluid extracting device |
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| CN204824121U (en) * | 2015-07-31 | 2015-12-02 | 山东新华医疗器械股份有限公司 | It washs and online sterilization system to blow integrative equipment on -line of embedment |
| CN105695087A (en) * | 2016-03-08 | 2016-06-22 | 深圳市华之粹生态科技有限公司 | Subcritical fluid extraction device and method |
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| CN107557146B (en) | 2024-03-12 |
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