CN107337707A - A kind of drying enrichment facility of high efficiency extraction Fish protein - Google Patents
A kind of drying enrichment facility of high efficiency extraction Fish protein Download PDFInfo
- Publication number
- CN107337707A CN107337707A CN201710632273.1A CN201710632273A CN107337707A CN 107337707 A CN107337707 A CN 107337707A CN 201710632273 A CN201710632273 A CN 201710632273A CN 107337707 A CN107337707 A CN 107337707A
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- CN
- China
- Prior art keywords
- tank body
- connecting tube
- high efficiency
- fish protein
- enrichment facility
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- 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.)
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Biophysics (AREA)
- Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Medicinal Chemistry (AREA)
- Molecular Biology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Analytical Chemistry (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention discloses a kind of drying enrichment facility of high efficiency extraction Fish protein, including heater, condensing unit and tank body, the tank body is surrounded by internal cavity layer, tank body lower end is provided with and takes out material head, take out to be connected with by connecting tube on the right side of material head and take out pump, take out pump upper end and be provided with connecting tube, connecting tube upper end is provided with electronic three-way valve, finished product discharge nozzle is provided with the right side of electronic three-way valve, electronic three-way valve upper end is provided with feed back pipe, the heater upper end is provided with helix tube, distributing bucket is connected by connecting tube on the right side of helix tube, helix tube lower end is provided with heat-conducting plate, heat-conducting plate lower end is provided with heating plate, heating plate lower end is provided with power supply, motor is provided with the right side of power supply, motor lower end is fixed with rotating shaft, rotating shaft lower end is provided with puddler, the condensing unit is arranged on tank body upper end.The drying enrichment facility of high efficiency extraction Fish protein of the present invention, heat source-contacting surface is big, and moisture evaporation is fast, dries concentration speed height, solves the problems, such as that Fish protein extraction efficiency is low.
Description
Technical field
The present invention relates to a kind of dry enrichment facility, specifically a kind of drying enrichment facility of high efficiency extraction Fish protein.
Background technology
First procedure of fish meal production is exactly the processing procedure of low trash fish raw material, in this process, low trash fish raw material
Part liquid can be oozed out, contains protein and flesh of fish solid content, referred to as protein liquid inside these liquid, flesh of fish solid in protein liquid
The content of thing is 4-5%, if this insufficient utilization of part protein liquid, can cause greatly to waste, and discarded albumen
Liquid also can welding, will in very short time because the protein in fish meal protein liquid is a kind of extremely putrefactive material
Corruption, the gas that corruption comes out later is smelt as of rotten fish, and perverse nose is unpleasant, and persistently drift is dissipated in atmosphere, and great dirt is constituted to air
Dye.And this Partial Protein liquid is similarly obtained fish meal after concentrate drying.
Vacuum concentration equipment, which can not have, at present makes protein liquid and thermal source fully contact, and moisture evaporation is slow, dries thickening efficiency
It is low, it is easy to cause protein liquid corrupt in concentration process.
The content of the invention
It is an object of the invention to provide a kind of drying enrichment facility of high efficiency extraction Fish protein, to solve above-mentioned background
The problem of being proposed in technology.
To achieve the above object, the present invention provides following technical scheme：
A kind of drying enrichment facility of high efficiency extraction Fish protein, including heater, condensing unit and tank body, the tank
Body is surrounded by internal cavity layer, and air inlet is provided with the left of internal cavity layer, and tank body is provided with vacuum-pumping tube on the downside of air inlet, vacuumizes
Connection tank inner chamber inside pipe, internal cavity layer right side are provided with gas outlet, and tank body lower end is provided with and takes out material head, take out and pass through company on the right side of material head
Adapter, which is connected with, takes out pump, takes out pump upper end and is provided with connecting tube, connecting tube is provided with concentration inductive probe, and connecting tube upper end is provided with electronic
Three-way valve, electronic three-way valve right side are provided with finished product discharge nozzle, and electronic three-way valve upper end is provided with feed back pipe, take out material head, take out pump, connection
Pipe, electronic three-way valve and feed back pipe are all disposed within inside internal cavity layer, and the heater is arranged on tank interior, heater
Upper end is provided with helix tube, and helix tube upper end connects back to expects pipe, passes through connecting tube connection distributing bucket, distributing bucket left side on the right side of helix tube
Fixed on the heating by fixed column, helix tube lower end heater is provided with heat-conducting plate, and heat-conducting plate lower end is provided with heating
Plate, heating plate lower end are provided with power supply, and heater is provided with motor on the right side of power supply, and motor lower end is fixed with rotating shaft, rotating shaft lower end
Provided with puddler, the condensing unit is arranged on tank body upper end, vapor collecting box on the left of condensing unit, under vapor collecting box
End is provided with connecting tube, and connecting tube lower end is communicated in tank inner chamber, is provided with cooling cylinder on the right side of steam collecting chamber, cooling cylinder surrounding is set
There is cavity, cavity upper end is provided with delivery port, and cavity lower end is provided with water inlet, and storage tank is provided with the right side of cavity, is set on the right side of storage tank
There is water discharging valve.
As the further scheme of the present invention：Arc is both configured at the top and bottom of the tank body.
As further scheme of the invention：Charging aperture is provided among the helix tube and left side is provided with discharging opening, and
Upper surface is provided with the steam outlet of array distribution.
As further scheme of the invention：Be provided with three-layer screen inside the distributing bucket, in the distributing bucket of screen cloth left side
Provided with heater.
As further scheme of the invention：The outside motor is provided with fixed case.
As further scheme of the invention：Propeller is provided with the upside of the rotating shaft.
As further scheme of the invention：The puddler is provided with the refluence hole of array distribution.
Compared with prior art, the beneficial effects of the invention are as follows：
The drying enrichment facility of high efficiency extraction Fish protein of the present invention, vacuum-pumping tube is connected by tank body by evacuator
Portion is vacuumized, and hot gas is passed through into air inlet, and hot gas heating tank body is discharged from gas outlet after terminating, starts motor and pass through rotating shaft band
Dynamic puddler stirring protein liquid, makes protein liquid be heated evenly quickening water evaporation rate, takes out pump and lead to the protein liquid of tank base
Cross electronic three-way valve to be extracted into helix tube, the tortuous pipeline of helix tube adds the contact area of protein liquid and thermal source, protein liquid
Into distributing bucket, the logical inside of sub-material is provided with three-layer screen, screen cloth shunting protein liquid increase heat source-contacting surface product, extraction Fish protein use
Drying enrichment facility, Fish protein liquid is all that heat source-contacting surface is big in thermal source inner loop, accelerate moisture evaporation, improve drying
Concentration speed, solve the problems, such as that Fish protein extraction efficiency is low.
Brief description of the drawings
Fig. 1 is a kind of structural representation of the drying enrichment facility of high efficiency extraction Fish protein.
Fig. 2 is a kind of structural representation of helix tube in drying enrichment facility of high efficiency extraction Fish protein.
Fig. 3 is a kind of structural representation of distributing bucket in drying enrichment facility of high efficiency extraction Fish protein.
Wherein：Internal cavity layer 1, air inlet 2, vacuum-pumping tube 3, heat-conducting plate 4, heating plate 5, power supply 6, heater 7, motor
8th, rotating shaft 9, puddler 10, take out material head 11, take out pump 12, gas outlet 13, connecting tube 14, concentration inductive probe 15, electronic three-way valve
16th, finished product discharge nozzle 17, feed back pipe 18, condensing unit 19, distributing bucket 20, helix tube 21, tank body 22.
Embodiment
Technical scheme is described in more detail with reference to embodiment.
Refer to Fig. 1-3, a kind of drying enrichment facility of high efficiency extraction Fish protein, including heater 7, condensing unit
19 and tank body 22, the top and bottom of tank body 22 are both configured to arc, and tank body 22 is surrounded by internal cavity layer 1, internal cavity layer 1
Left side is provided with air inlet 2, and the downside tank body 22 of air inlet 2 is provided with vacuum-pumping tube 3, and the inside of vacuum-pumping tube 3 connects the inner chamber of tank body 22,
The right side of internal cavity layer 1 is provided with gas outlet 13, and the lower end of tank body 22 is provided with and takes out material head 11, takes out the right side of material head 11 and is connected with by connecting tube
Pump 12 is taken out, the upper end of pump 12 is taken out and is provided with connecting tube 14, connecting tube 14 is provided with concentration inductive probe 15, and the upper end of connecting tube 14 is provided with electricity
Dynamic three-way valve 16, the electronic right side of three-way valve 16 are provided with finished product discharge nozzle 17, and the electronic upper end of three-way valve 16 is provided with feed back pipe 18, takes out material
First 11, take out pump 12, connecting tube 14, electronic three-way valve 16 and feed back pipe 18 to be all disposed within inside internal cavity layer 1, the heater
7 are arranged on inside tank body 22, and the upper end of heater 7 is provided with helix tube 21, is provided with charging aperture among helix tube 21 and left side is provided with
Discharging opening, and upper surface is provided with the steam outlet of array distribution, the upper end of helix tube 21 connects back to expects pipe 18, the right side of helix tube 21
Distributing bucket 20 is connected by connecting tube, distributing bucket 20 passes on left fixed column and is fixed on heater 7, set inside distributing bucket 20
There is three-layer screen, screen cloth left side distributing bucket 20 is provided with heater, and the lower end heater 7 of helix tube 21 is provided with heat-conducting plate 4, led
The lower end of hot plate 4 is provided with heating plate 5, and the lower end of heating plate 5 is provided with power supply 6, and the right side heater 7 of power supply 6 is provided with motor 8, motor 8
Outside is provided with fixed case, and the lower end of motor 8 is fixed with rotating shaft 9, and the upside of rotating shaft 9 is provided with propeller, and the lower end of rotating shaft 9 is provided with puddler
10, puddler 10 is provided with the refluence hole of array distribution, and the condensing unit 19 is arranged on the upper end of tank body 22, and condensing unit 19 is left
Side vapor collecting box, vapor collecting box lower end are provided with connecting tube, and connecting tube lower end is communicated in the inner chamber of tank body 22, and steam is received
Collection is provided with cooling cylinder on the right side of room, and cooling cylinder is surrounded by cavity, and cavity upper end is provided with delivery port, and cavity lower end is provided with water inlet,
Storage tank is provided with the right side of cavity, water discharging valve is provided with the right side of storage tank, vacuum-pumping tube 3 is connected by tank body 22 by evacuator
Portion is vacuumized, and hot gas is passed through into air inlet 2, and hot gas heating tank body 22 is discharged from gas outlet 13 after terminating, starts motor 8 and pass through
Rotating shaft 9 drives puddler 10 to stir protein liquid, protein liquid is heated evenly quickening water evaporation rate, takes out pump 12 by the bottom of tank body 22
The protein liquid in portion is extracted into helix tube 21 by electronic three-way valve 16, and the tortuous pipeline of helix tube 21 adds protein liquid and thermal source
Contact area, protein liquid enters distributing bucket 20, and logical 20 inside of sub-material is provided with three-layer screen, and screen cloth shunting protein liquid increases thermal source
Contact area, the drying enrichment facility of Fish protein being extracted, Fish protein liquid is all that heat source-contacting surface is big in thermal source inner loop,
Accelerate moisture evaporation, improve and dry concentration speed, solve the problems, such as that Fish protein extraction efficiency is low.
The present invention operation principle be：The drying enrichment facility of high efficiency extraction Fish protein of the present invention, passes through evacuator
Connection vacuum-pumping tube vacuumizes tank interior, and hot gas is passed through into air inlet, and hot gas heating tank body is arranged after terminating from gas outlet
Go out, start motor and drive puddler to stir protein liquid by rotating shaft, protein liquid is heated evenly quickening water evaporation rate, take out pump
The protein liquid of tank base is extracted into helix tube by electronic three-way valve, the tortuous pipeline of helix tube adds protein liquid and heat
The contact area in source, protein liquid enter distributing bucket, and the logical inside of sub-material is provided with three-layer screen, and screen cloth shunting protein liquid increase thermal source connects
Contacting surface is accumulated, and extracts the drying enrichment facility of Fish protein, Fish protein liquid is all that heat source-contacting surface is big in thermal source inner loop, is added
Fast moisture evaporation, improve and dry concentration speed, solve the problems, such as that Fish protein extraction efficiency is low.
The better embodiment of the present invention is explained in detail above, but the present invention is not limited to above-mentioned embodiment party
Formula, can also be on the premise of present inventive concept not be departed from one skilled in the relevant art's possessed knowledge
Various changes can be made.
Claims (7)
1. a kind of drying enrichment facility of high efficiency extraction Fish protein, including heater (7), condensing unit (19) and tank body
(22), it is characterised in that the tank body (22) is surrounded by internal cavity layer (1), and air inlet (2) is provided with the left of internal cavity layer (1),
Tank body (22) is provided with vacuum-pumping tube (3) on the downside of air inlet (2), and tank body (22) inner chamber, internal cavity are connected inside vacuum-pumping tube (3)
Gas outlet (13) are provided with the right side of layer (1), tank body (22) lower end is provided with and takes out material head (11), takes out and connects on the right side of material head (11) by connecting tube
It is connected to and takes out pump (12), take out pump (12) upper end and be provided with connecting tube (14), connecting tube (14) is provided with concentration inductive probe (15), connection
Pipe (14) upper end is provided with electronic three-way valve (16), and finished product discharge nozzle (17), electronic three-way valve are provided with the right side of electronic three-way valve (16)
(16) upper end is provided with feed back pipe (18), takes out material head (11), takes out pump (12), connecting tube (14), electronic three-way valve (16) and feed back pipe
(18) it is internal to be all disposed within internal cavity layer (1), the heater (7) is arranged on tank body (22) inside, heater (7) upper end
Provided with helix tube (21), helix tube (21) upper end connects back to expects pipe (18), and helix tube (21) right side connects sub-material by connecting tube
Bucket (20), distributing bucket (20) pass on left fixed column and are fixed on heater (7), helix tube (21) lower end heater (7)
Heat-conducting plate (4) is provided with, heat-conducting plate (4) lower end is provided with heating plate (5), and heating plate (5) lower end is provided with power supply (6), and power supply (6) is right
Side heater (7) is provided with motor (8), and motor (8) lower end is fixed with rotating shaft (9), and rotating shaft (9) lower end is provided with puddler
(10), the condensing unit (19) is arranged on tank body (22) upper end, condensing unit (19) left side vapor collecting box, and vapor is received
Header lower end is provided with connecting tube, and connecting tube lower end is communicated in tank body (22) inner chamber, and cooling cylinder is provided with the right side of steam collecting chamber, cold
Solidifying case is surrounded by cavity, and cavity upper end is provided with delivery port, and cavity lower end is provided with water inlet, storage tank is provided with the right side of cavity, stores up
Water discharging valve is provided with the right side of water tank.
A kind of 2. drying enrichment facility of high efficiency extraction Fish protein according to claim 1, it is characterised in that the tank
Arc is both configured at the top and bottom of body (22).
A kind of 3. drying enrichment facility of high efficiency extraction Fish protein according to claim 1, it is characterised in that the spiral shell
Charging aperture is provided among coil (21) and left side is provided with discharging opening, and upper surface is provided with the steam outlet of array distribution.
4. the drying enrichment facility of a kind of high efficiency extraction Fish protein according to claim 1, it is characterised in that described point
Three-layer screen is provided with inside charging basket (20), distributing bucket (20) is provided with heater on the left of screen cloth.
A kind of 5. drying enrichment facility of high efficiency extraction Fish protein according to claim 1, it is characterised in that the electricity
Fixed case is provided with outside machine (8).
6. the drying enrichment facility of a kind of high efficiency extraction Fish protein according to claim 1, it is characterised in that described turn
Propeller is provided with the upside of axle (9).
7. the drying enrichment facility of a kind of high efficiency extraction Fish protein according to claim 1, it is characterised in that described to stir
Mix the refluence hole that bar (10) is provided with array distribution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710632273.1A CN107337707A (en) | 2017-07-28 | 2017-07-28 | A kind of drying enrichment facility of high efficiency extraction Fish protein |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710632273.1A CN107337707A (en) | 2017-07-28 | 2017-07-28 | A kind of drying enrichment facility of high efficiency extraction Fish protein |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107337707A true CN107337707A (en) | 2017-11-10 |
Family
ID=60216030
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710632273.1A Withdrawn CN107337707A (en) | 2017-07-28 | 2017-07-28 | A kind of drying enrichment facility of high efficiency extraction Fish protein |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107337707A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108771880A (en) * | 2018-06-27 | 2018-11-09 | 胡永超 | honey concentrating device and method |
| CN115286157A (en) * | 2021-12-30 | 2022-11-04 | 武汉市政环境工程建设有限公司 | Landfill leachate solidification preprocessing device |
-
2017
- 2017-07-28 CN CN201710632273.1A patent/CN107337707A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108771880A (en) * | 2018-06-27 | 2018-11-09 | 胡永超 | honey concentrating device and method |
| CN115286157A (en) * | 2021-12-30 | 2022-11-04 | 武汉市政环境工程建设有限公司 | Landfill leachate solidification preprocessing device |
| CN115286157B (en) * | 2021-12-30 | 2023-11-17 | 武汉市政环境工程建设有限公司 | Landfill leachate solidification preprocessing device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20171110 |