CN109534579A - A kind of euphausia superba powder processing line liquid-phase treatment system - Google Patents
A kind of euphausia superba powder processing line liquid-phase treatment system Download PDFInfo
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- CN109534579A CN109534579A CN201811617903.9A CN201811617903A CN109534579A CN 109534579 A CN109534579 A CN 109534579A CN 201811617903 A CN201811617903 A CN 201811617903A CN 109534579 A CN109534579 A CN 109534579A
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- 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
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- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B13/00—Recovery of fats, fatty oils or fatty acids from waste materials
-
- 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
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/06—Flash evaporation
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- 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
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- 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
- C02F2103/22—Nature of the water, waste water, sewage or sludge to be treated from the processing of animals, e.g. poultry, fish, or parts thereof
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- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Meat, Egg Or Seafood Products (AREA)
Abstract
The present invention provides a kind of euphausia superba powder processing line liquid-phase treatment systems, including the separation of liquid filtering and heating, supercentrifuge, waste water filtering, the utilization of waste water heat cycles, purification, shrimp sauce filling.The present invention takes full advantage of krill meal processing line liquid phase, improves resource recycling rate, avoids wasting, and the configuration of the present invention is simple, and it is convenient to operate, and can be widely popularized in actual use.The available separation and recovery of a small amount of solid in krill meal processing line liquid phase is conducive to the yield for increasing shrimp med.The shrimp sauce that high-purity can also be obtained by this system, effectively increases resource utilization, avoids wasting.It can be used for moisturizing in whole production line process flow after the effluent part filtering separated by three-phase supercentrifuge or be used for processing line water for cleaning, avoid wasting, can be widely popularized in actual use.
Description
Technical field
The present invention relates to euphausia superba powder processing technical field more particularly to a kind of euphausia superba powder processing line liquid phases
Processing system.
Background technique
Krill is a kind of minibeast for living in South Pole sea area, and reserves are about 6 ~ 1,000,000,000 tons, year
Can amount of fishing be about hundred million tons of 0.6-1.0, according to biological characteristis, contain protein 17.56% in krill meat, fat 2.11%,
And containing whole amino acid necessary to human body.The current major product of krill is aboard ship directly processed into after fishing comes up
Shrimp med freezes shrimp or shrimp.
Currently, shrimp med is most important in all products and is most widely used, can both be used to extract krill oil, it can also
To be used as feed or feed addictive.Euphausia superba powder is using krill as raw material, through too fast after catching onto ship
Fast boiling, separation, drying, crushing, cooling etc. are a series of to process obtained product, and krill uses horizontal centrifuge after boiling
Be separated by solid-liquid separation, wherein solid portion by drying, crushing, it is cooling after obtain shrimp med, technical process comparative maturity.
But the big quantity of fluid for generating after being separated by solid-liquid separation, the partially liq contain the egg dissolved in a large amount of shrimp sauce and digestion process
White matter, current most variations are all direct emissions, are not efficiently used to this moieties, and great resource wave is caused
Take.
Summary of the invention
To solve drawbacks described above, the present invention proposes one kind for the liquid phase part generated in euphausia superba powder process
New process and treat system extracts high-purity shrimp sauce.
Make a kind of the first technical solution to realize the present invention: euphausia superba powder processing line liquid-phase treatment system, including
Seperator liquid phase buffer tank, three-phase supercentrifuge, expansion drying tank, shrimp sauce buffer tank, waste water buffer tank, the seperator liquid
Phase buffer tank connects filter I by rotary lobe pump, and I liquid outlet of filter connects three-phase high speed by heater I
Centrifuge, I solid outlet of filter are connected to drier by rotary lobe pump；The three-phase supercentrifuge solid phase goes out
Material mouth is connected to drier by rotary lobe pump, and the three-phase high speed centrifugation machine oil phase discharge port connects shrimp sauce buffer tank, institute
State three-phase supercentrifuge water phase discharge port connection waste water buffer tank；The shrimp sauce buffer tank is sequentially connected heater II, flash distillation
Drying chamber, it is slow that the top steam outlet of the expansion drying tank is connected with cooler, bottom shrimp sauce outlet connection finished product shrimp sauce
Tank is deposited, the cooler is connect with vacuum pump, centrifugal pump II, and rotation is equipped between the expansion drying tank and finished product shrimp sauce buffer tank
Rotating cam pump；The waste water buffer tank is connected with Sewage treatment and is pumped using pump, waste water row's outboard, the Sewage treatment using pump with
Filter II connects, and II solid outlet of filter is connected to drier, II liquid of filter by rotary lobe pump
It exports heater III and connect the vessel Waste circulatory system with centrifugal pump I；The waste water row outboard pump connection ship pollution discharge mouth.
Further, the heater I, heater II, the outlet of heater III setting temperature sensor, the expansion drying
It is equipped with high-low-position pressure sensor in device, is equipped with pressure sensor, the vacuum pump, centrifugal pump in the finished product shrimp sauce buffer tank
II is equipped with check-valves.
Further, it is equipped with insulating layer on the outside of the seperator liquid phase buffer tank, is set in the seperator liquid phase buffer tank
There is pressure sensor.
Further, it is equipped with insulating layer on the outside of the shrimp sauce buffer tank, is equipped with pressure sensor in the shrimp sauce buffer tank,
The shrimp sauce caching pot bottom is equipped with rotary lobe pump.
Further, it is equipped with pressure sensor in the waste water buffer tank, is equipped with insulating layer on the outside of the waste water buffer tank,
The finished product shrimp sauce caching pot bottom connects shrimp sauce filling apparatus.
Make a kind of second of technical solution to realize the present invention: euphausia superba powder processing line liquid-phase treatment system, including
Seperator liquid phase buffer tank, three-phase supercentrifuge I, three-phase supercentrifuge II, shrimp sauce buffer tank, waste water buffer tank, it is described
Seperator liquid phase buffer tank connects filter I by rotary lobe pump, and I liquid outlet of filter is connected by heater I
Three-phase supercentrifuge I, I solid outlet of filter are connected to drier by rotary lobe pump；Three-phase high speed from
The oily phase discharge port of scheming I connects shrimp sauce buffer tank, and the shrimp sauce buffer tank connects three-phase supercentrifuge II by heater II,
The three-phase supercentrifuge I, II solid phase discharge port of three-phase supercentrifuge are connected to drier by rotary lobe pump, described
Three-phase supercentrifuge I, II water phase discharge port of three-phase supercentrifuge connect waste water buffer tank, the three-phase supercentrifuge II
Oily phase discharge port connects finished product shrimp sauce buffer tank；The waste water buffer tank is connected with Sewage treatment and is pumped using pump, waste water row's outboard,
The Sewage treatment is connect using pump with filter II, and II solid outlet of filter is connected to drying by rotary lobe pump
Device, the II liquid outlet heater III of filter connect the vessel Waste circulatory system with centrifugal pump I；The waste water row outboard pump
Connect ship pollution discharge mouth.
Further, the heater I, heater II, the outlet of heater III setting temperature sensor, the finished product shrimp sauce
Pressure sensor is equipped in buffer tank.
Further, it is equipped with insulating layer on the outside of the seperator liquid phase buffer tank, is set in the seperator liquid phase buffer tank
There is pressure sensor.
Further, it is equipped with insulating layer on the outside of the shrimp sauce buffer tank, is equipped with pressure sensor in the shrimp sauce buffer tank,
The shrimp sauce caching pot bottom is equipped with rotary lobe pump.
Further, it is equipped with pressure sensor in the waste water buffer tank, is equipped with insulating layer on the outside of the waste water buffer tank,
The finished product shrimp sauce caching pot bottom connects shrimp sauce filling apparatus.
Beneficial effects of the present invention: taking full advantage of krill meal processing line liquid phase, improves resource recycling rate, avoids wave
Take, and the configuration of the present invention is simple, it is convenient to operate, and can be widely popularized in actual use.Lacking in krill meal processing line liquid phase
The available separation and recovery of solid is measured, the yield for increasing shrimp med is conducive to.The shrimp sauce that high-purity can also be obtained by this system, has
Effect improves resource utilization, and avoids wasting.It can be used for after the effluent part filtering separated by three-phase supercentrifuge whole
Moisturizing or it to be used for processing line water for cleaning in production-line technique process, avoids wasting.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the first technical solution of the invention.
Fig. 2 is the structural schematic diagram of second of technical solution of the invention.
Wherein: 10, seperator liquid phase buffer tank, 11, filter I, 12, heater I, 20, three-phase supercentrifuge I, 21,
Shrimp sauce buffer tank, 30, waste water buffer tank, 31, waste water row outboard pump, 32, Sewage treatment using pump, 33, filter II, 34, plus
Hot device III, 35, centrifugal pump I, 40, heater II, 41, expansion drying tank, 42, cooler, 43, vacuum pump, 44, centrifugal pump II,
45, check-valves, 50, finished product shrimp sauce buffer tank, 51, shrimp sauce filling apparatus, 60, rotary lobe pump, 70, three-phase supercentrifuge
Ⅱ。
Specific embodiment
The invention will be further described with reference to the accompanying drawings and embodiments.
Embodiment one: as shown in Figure 1, a kind of euphausia superba powder processing line liquid-phase treatment system, including seperator liquid phase are slow
Tank 10, three-phase supercentrifuge I 20, expansion drying tank 41, shrimp sauce buffer tank 21, waste water buffer tank 30 are deposited, seperator liquid phase is slow
It deposits tank 10 and filter I 11 is connected by rotary lobe pump 60.The liquid that filter I 11 filters out is flowed out through from liquid outlet to be added
Hot device I 12 flows into three-phase supercentrifuge I 20, and filter I 11 filters remaining solid by rotary lobe pump 60 by solid
It transports to drier outlet.I 20 solid phase discharge port of three-phase supercentrifuge connects drier by rotary lobe pump 60.Three-phase is high
Fast I 20 water phase discharge port of centrifuge connects waste water buffer tank 30.The oily phase discharge port connection shrimp sauce caching of three-phase supercentrifuge I 20
Tank 21, shrimp sauce buffer tank 21 are sequentially connected heater II 40, expansion drying tank 41, the top steam outlet of expansion drying tank 41
It is connected with cooler 42, bottom shrimp sauce outlet connection finished product shrimp sauce buffer tank 50, cooler 42 and vacuum pump 43, centrifugal pump II 44
Connection is equipped with rotary lobe pump 60 between expansion drying tank 41 and finished product shrimp sauce buffer tank 50.
Euphausia superba powder processing line liquid phase enters in seperator liquid phase buffer tank 10, enters filter by rotary lobe pump 60
In I 11.Pressure sensor is equipped in seperator liquid phase buffer tank 10, when liquid level is higher, 60 automatic running of rotary lobe pump, when
When liquid level is lower, rotary lobe pump 60 is automatically stopped.Remaining solid is filtered through filter I 11 to send through rotary lobe pump 60 to dry
Continue to be dried to obtain shrimp med in dry device, the liquid filtered out, which enters in heater I 12, to be heated.Due to containing a large amount of rouge in liquid
Fat, to reach better separating effect, control liquid cannot be below 95 degree before entering three-phase supercentrifuge I 20.Heater I 12
Outlet setting temperature sensor, by temperature sensor adjust steam valve, guarantee heater outlet temperature stablize 95 degree with
On.Wherein, it is equipped with insulating layer on the outside of seperator liquid phase buffer tank 10, better heat insulation effect can be played to liquid.
Liquid after I 20 pairs of three-phase supercentrifuge heating carries out solid, liquid, oily three-phase layering and separates.Isolated
Solid, which is sent by solid phase discharge port through rotary lobe pump 60, continues to be dried to obtain into drier shrimp med, and isolated shrimp sauce is logical
It crosses oily phase discharge port to send into shrimp sauce buffer tank 21, the shrimp sauce into shrimp sauce buffer tank 21 needs further evaporation to reduce moisture
Content is conducive to the long-term preservation of shrimp sauce.Shrimp sauce is transported in heater II 40 and heats by rotary lobe pump 60.Shrimp sauce buffer tank
21 outsides are equipped with insulating layer, can play preferable heat insulation effect.Pressure sensor is equipped in shrimp sauce buffer tank 21 for measuring tank
Interior liquid level, bottom are equipped with rotary lobe pump 60, and rotary lobe pump 60 controls start and stop according to 21 pressure sensor of shrimp sauce buffer tank.
Shrimp sauce after heating enters back into expansion drying tank 41, and wherein the outlet of heater II 40 setting temperature sensor, is passed by temperature
Sensor adjusts steam valve, guarantees that the temperature of heater outlet is stablized.Since expansion drying tank 41 is closed container, in tank
Increase a high-pressure sensor, high-low-position pressure sensor controls the start and stop of rotary lobe pump 60 simultaneously.Centrifugal pump II 44
Check-valves 45 is designed with vacuum pump 43, it is ensured that vacuum pump 43 guarantees to form negative pressure in expansion drying tank 41 in the process of running.
The boiling point of water is evaporated after reducing and enters cooler 42 by pipeline, vapor a part after cooling become condensed water with from
Outboard is discharged in heart pump II 44, and a part of vapor is discharged by vacuum pump 43.Shrimp sauce moisture content after evaporation is lower than 0.1%, and leads to
It crosses rotary lobe pump 60 to be pumped in finished product shrimp sauce buffer tank 50, pressure sensor is equipped in finished product shrimp sauce buffer tank 50 and measures tank
Interior liquid level.Shrimp sauce into finished product shrimp sauce buffer tank 50 is pumped to shrimp sauce filling apparatus 51, shrimp sauce using rotary lobe pump 60
Filling apparatus 51 can control rotary lobe pump 60, and finished product shrimp sauce is filled into finished product shrimp sauce pail pack and is stored.
Isolated waste water is discharged in waste water buffer tank 30 by water phase discharge port, is equipped on the outside of waste water buffer tank 30
Insulating layer is kept the temperature, the liquid level being additionally provided in pressure sensor measurement tank in waste water buffer tank 30 and the start and stop for controlling centrifugal pump.It is useless
The waste water of water buffer tank 30 can be transported into filter II 33 using pump 32 by Sewage treatment and be filtered, the solid filtered out
Be sent in drier by rotary lobe pump 60 and be dried to obtain shrimp med, filtered liquid by heater III 34 heating after with from
The waste water circulatory system that heart pump I 35 is pumped to production line continues to use.The outlet of heater III 34 is provided with temperature sensor.Or
Person when the liquid level in waste water buffer tank 30 is in high-order and the waste water circulatory system does not need work, waste water buffer tank 30
Waste water can arrange outboard pump 31 by waste water, and waste water is drained into outboard or is pumped to other buffer tanks and be concentrated in next step and is steamed
Hair processing.
Embodiment two: as shown in Fig. 2, a kind of euphausia superba powder processing line liquid-phase treatment system, including seperator liquid phase are slow
Deposit tank 10, three-phase supercentrifuge I 20, three-phase supercentrifuge II 70, shrimp sauce buffer tank 21, waste water buffer tank 30, seperator
Liquid phase buffer tank 10 connects filter I 11 by rotary lobe pump 60.The liquid that filter I 11 filters out is flowed out from liquid outlet
Three-phase supercentrifuge I 20 is flowed by heater I 12, filter I 11 filters remaining solid and passes through rotary lobe pump 60
It is transported by solid outlet to drier.The oily phase discharge port of three-phase supercentrifuge I 20 connects shrimp sauce buffer tank 21, shrimp sauce buffer tank
21 connect three-phase supercentrifuge II 70 by heater II 40.Three-phase supercentrifuge I 20, three-phase supercentrifuge II 70 are solid
Phase discharge port is connected to drier by rotary lobe pump 60.Three-phase supercentrifuge I 20, II 70 water phase of three-phase supercentrifuge
Discharge port connects waste water buffer tank 30.The oily phase discharge port of three-phase supercentrifuge II 70 connects finished product shrimp sauce buffer tank 50.
Euphausia superba powder processing line liquid phase enters in seperator liquid phase buffer tank 10, enters filter by rotary lobe pump 60
In I 11.Pressure sensor is equipped in seperator liquid phase buffer tank 10, when liquid level is higher, 60 automatic running of rotary lobe pump, when
When liquid level is lower, rotary lobe pump 60 is automatically stopped.Remaining solid is filtered through filter I 11 to send through rotary lobe pump 60 to dry
Continue to be dried to obtain shrimp med in dry device, the liquid filtered out, which enters in heater I 12, to be heated.Due to containing a large amount of rouge in liquid
Fat, to reach better separating effect, control liquid cannot be below 95 degree before entering three-phase supercentrifuge I 20.Heater I 12
Outlet setting temperature sensor, by temperature sensor adjust steam valve, guarantee heater outlet temperature stablize 95 degree with
On.Wherein, it is equipped with insulating layer on the outside of seperator liquid phase buffer tank 10, better heat insulation effect can be played to liquid.Three-phase high speed
Liquid after I 20 pairs of centrifuge heating carries out solid, liquid, oily three-phase layering and separates.Isolated solid phase is discharged by solid phase
Mouth send through rotary lobe pump 60 and continues to be dried to obtain shrimp med into drier, isolated shrimp sauce by oil phase discharge port send to
In shrimp sauce buffer tank 21, the shrimp sauce into shrimp sauce buffer tank 21 needs further evaporation reduction moisture content to be conducive to shrimp sauce
Long-term preservation.Shrimp sauce is transported in heater II 40 and heats by rotary lobe pump 60.The outlet of heater II 40 setting temperature sensing
Device adjusts steam valve by temperature sensor, guarantees that the temperature of heater outlet is stablized.Heat preservation is equipped on the outside of shrimp sauce buffer tank 21
Layer, can play preferable heat insulation effect.Pressure sensor is equipped in shrimp sauce buffer tank 21 for measuring liquid level in tank, bottom is equipped with
Rotary lobe pump 60, rotary lobe pump 60 control start and stop according to 21 pressure sensor of shrimp sauce buffer tank.Isolated liquid phase
It is discharged in waste water buffer tank 30 by water phase discharge port.Shrimp sauce after heating enters back into three-phase supercentrifuge II 70, and three
The higher shrimp sauce of water content in shrimp sauce buffer tank 21 is carried out further solid, liquid, oily three phase separation by phase supercentrifuge II 70,
The available lower shrimp sauce of water content is conducive to long-term preservation.The isolated liquid phase liquid isolated with three-phase supercentrifuge I 20
It is mutually combined into waste water buffer tank 30, the solid phase merging isolated with three-phase supercentrifuge I 20 of isolated solid phase is pumped to drying
Device, the lower shrimp sauce of the water content separated enter storage in finished product shrimp sauce buffer tank 50.It is set in finished product shrimp sauce buffer tank 50
There is the liquid level in pressure sensor measurement tank.Shrimp sauce into finished product shrimp sauce buffer tank 50 is pumped to shrimp using rotary lobe pump 60
Oily filling apparatus 51, shrimp sauce filling apparatus 51 can control rotary lobe pump 60, and finished product shrimp sauce is filled into finished product shrimp sauce packet
In barrelling and store.
It is equipped with insulating layer on the outside of waste water buffer tank 30 to keep the temperature, is additionally provided in waste water buffer tank 30 in pressure sensor measurement tank
Liquid level and control the start and stop of centrifugal pump.The waste water of waste water buffer tank 30 can utilize 32 transport of pump to filtering by Sewage treatment
It is filtered in device II 33, the solid filtered out is sent in drier by rotary lobe pump 60 and is dried to obtain shrimp med, filtered
Liquid is continued to use after the heating of heater III 34 with the waste water circulatory system that centrifugal pump I 35 is pumped to production line.Heater
III 34 outlet is provided with temperature sensor.Or when the liquid level in waste water buffer tank 30 is in a high position and the waste water circulatory system not
When needing work, the waste water of waste water buffer tank 30 can arrange outboard pump 31 by waste water, and waste water is drained into outboard or pump
It send to other buffer tanks and carries out the processing of next step concentration and evaporation.
The present invention takes full advantage of krill meal processing line liquid phase, improves resource recycling rate, avoids wasting, and the present invention
Structure is simple, and it is convenient to operate, and can be widely popularized in actual use.A small amount of solid in krill meal processing line liquid phase can obtain
To separation and recovery, be conducive to the yield for increasing shrimp med.The shrimp sauce that high-purity can also be obtained by this system, effectively increases resource
Utilization rate avoids wasting.It can be used for whole production line technique after the effluent part filtering separated by three-phase supercentrifuge
In process moisturizing or be used for processing line water for cleaning, avoid wasting.
Claims (10)
1. a kind of euphausia superba powder processing line liquid-phase treatment system, it is characterised in that: high including seperator liquid phase buffer tank, three-phase
Fast centrifuge, expansion drying tank, shrimp sauce buffer tank, waste water buffer tank, the seperator liquid phase buffer tank pass through rotary lobe pump
Filter I is connected, I liquid outlet of filter connects three-phase supercentrifuge, I solid of filter by heater I
Outlet is connected to drier by rotary lobe pump；The three-phase supercentrifuge solid phase discharge port is connected by rotary lobe pump
To drier, the three-phase high speed centrifugation machine oil phase discharge port connects shrimp sauce buffer tank, and the three-phase supercentrifuge water phase goes out
Material mouth connects waste water buffer tank；The shrimp sauce buffer tank is sequentially connected heater II, expansion drying tank, the expansion drying tank
Top steam outlet is connected with cooler, bottom shrimp sauce outlet connection finished product shrimp sauce buffer tank, the cooler and vacuum pump,
Centrifugal pump II connects, and rotary lobe pump is equipped between the expansion drying tank and finished product shrimp sauce buffer tank；The waste water buffer tank
It is connected with Sewage treatment to pump using pump, waste water row's outboard, the Sewage treatment is connect using pump with filter II, the filter
II solid outlet is connected to drier by rotary lobe pump, and the II liquid outlet heater III of filter connects with centrifugal pump I
Connect the vessel Waste circulatory system；The waste water row outboard pump connection ship pollution discharge mouth.
2. euphausia superba powder processing line liquid-phase treatment system according to claim 1, it is characterised in that: the heater I,
Heater II, the outlet of heater III setting temperature sensor, the flash distillation dryer is interior equipped with high-low-position pressure sensor, described
Pressure sensor is equipped in finished product shrimp sauce buffer tank, the vacuum pump, centrifugal pump II are equipped with check-valves.
3. euphausia superba powder processing line liquid-phase treatment system according to claim 1, it is characterised in that: the seperator liquid
It is equipped with insulating layer on the outside of phase buffer tank, is equipped with pressure sensor in the seperator liquid phase buffer tank.
4. euphausia superba powder processing line liquid-phase treatment system according to claim 1, it is characterised in that: the shrimp sauce caching
Equipped with insulating layer on the outside of tank, the shrimp sauce buffer tank is interior to be equipped with pressure sensor, and it is convex that the shrimp sauce caching pot bottom is equipped with rotation
Wheel pump.
5. euphausia superba powder processing line liquid-phase treatment system according to claim 1, it is characterised in that: the waste water caching
It is equipped with pressure sensor in tank, insulating layer is equipped on the outside of the waste water buffer tank, the finished product shrimp sauce caching pot bottom connects shrimp
Oily filling apparatus.
6. a kind of euphausia superba powder processing line liquid-phase treatment system, it is characterised in that: high including seperator liquid phase buffer tank, three-phase
Fast centrifuge I, three-phase supercentrifuge II, shrimp sauce buffer tank, waste water buffer tank, the seperator liquid phase buffer tank pass through rotation
Lobe pump connects filter I, and I liquid outlet of filter connects three-phase supercentrifuge I, the filtering by heater I
I solid outlet of device is connected to drier by rotary lobe pump；The oily phase discharge port connection shrimp sauce of the three-phase supercentrifuge I is slow
Tank is deposited, the shrimp sauce buffer tank connects three-phase supercentrifuge II, the three-phase supercentrifuge I, three-phase by heater II
II solid phase discharge port of supercentrifuge is connected to drier, the three-phase supercentrifuge I, three-phase high speed by rotary lobe pump
II water phase discharge port of centrifuge connects waste water buffer tank, and the oily phase discharge port connection finished product shrimp sauce of the three-phase supercentrifuge II is slow
Deposit tank；The waste water buffer tank is connected with Sewage treatment and is pumped using pump, waste water row's outboard, and the Sewage treatment utilizes pump and filtering
Device II connects, and II solid outlet of filter is connected to drier, II liquid outlet of filter by rotary lobe pump
Heater III connect the vessel Waste circulatory system with centrifugal pump I；The waste water row outboard pump connection ship pollution discharge mouth.
7. euphausia superba powder processing line liquid-phase treatment system according to claim 6, it is characterised in that: the heater I,
Heater II, the outlet of heater III setting temperature sensor, the finished product shrimp sauce buffer tank is interior to be equipped with pressure sensor.
8. euphausia superba powder processing line liquid-phase treatment system according to claim 6, it is characterised in that: the seperator liquid
It is equipped with insulating layer on the outside of phase buffer tank, is equipped with pressure sensor in the seperator liquid phase buffer tank.
9. euphausia superba powder processing line liquid-phase treatment system according to claim 6, it is characterised in that: the shrimp sauce caching
Equipped with insulating layer on the outside of tank, the shrimp sauce buffer tank is interior to be equipped with pressure sensor, and it is convex that the shrimp sauce caching pot bottom is equipped with rotation
Wheel pump.
10. euphausia superba powder processing line liquid-phase treatment system according to claim 6, it is characterised in that: the waste water is slow
It deposits and is equipped with pressure sensor in tank, insulating layer, the finished product shrimp sauce caching pot bottom connection are equipped on the outside of the waste water buffer tank
Shrimp sauce filling apparatus.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811617903.9A CN109534579A (en) | 2018-12-28 | 2018-12-28 | A kind of euphausia superba powder processing line liquid-phase treatment system |
| CN201921914216.3U CN211644935U (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
| CN201911080534.9A CN110981052A (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811617903.9A CN109534579A (en) | 2018-12-28 | 2018-12-28 | A kind of euphausia superba powder processing line liquid-phase treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109534579A true CN109534579A (en) | 2019-03-29 |
Family
ID=65857529
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811617903.9A Withdrawn CN109534579A (en) | 2018-12-28 | 2018-12-28 | A kind of euphausia superba powder processing line liquid-phase treatment system |
| CN201921914216.3U Active CN211644935U (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
| CN201911080534.9A Pending CN110981052A (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921914216.3U Active CN211644935U (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
| CN201911080534.9A Pending CN110981052A (en) | 2018-12-28 | 2019-11-07 | Shrimp meal processing line liquid phase processing system |
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| CA2904232A1 (en) * | 2013-03-14 | 2014-09-18 | Institut De Recherche Sur Les Zones Cotieres (Irzc) | Method for extracting organic solids and oil from marine organisms enriched with astaxanthin |
| CN104479850B (en) * | 2014-12-15 | 2015-10-21 | 中国水产科学研究院黄海水产研究所 | The method of high phospholipid content krill oil is extracted from fresh krill |
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Application publication date: 20190329 |