CN108285476A - A kind of eddy flow extrusion separator - Google Patents
A kind of eddy flow extrusion separator Download PDFInfo
- Publication number
- CN108285476A CN108285476A CN201810345493.0A CN201810345493A CN108285476A CN 108285476 A CN108285476 A CN 108285476A CN 201810345493 A CN201810345493 A CN 201810345493A CN 108285476 A CN108285476 A CN 108285476A
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- CN
- China
- Prior art keywords
- cone
- cylinder
- bullet
- capsul
- discharging
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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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Classifications
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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
Abstract
It is a kind of eddy flow extrusion separator for producing alcohol method protein concentrate the present invention relates to food, chemical field.It is big existing equipment labor intensity can effectively to be solved, it is complicated, automatically control difference, it runs, it emits, drop, leak the more problem of phenomenon, its solve technical solution be, the machine includes decelerating motor, engine base, shaft coupling, hollow shaft, cone spiral vane, cone, bullet, liquid header, cylinder, circular cylinder, gravity door and discharging capsul etc., decelerating motor is mounted on engine base, its output shaft passes through shaft coupling, hollow shaft is connected with cone spiral vane becomes screw extrusion component, and it is located at cone, in bullet, hole is provided in hollow shaft, cylinder is installed on axis, strainer is installed on cylinder；The main body of liquid header, cone, bullet and discharging capsul constitution equipment is equipped with circular cylinder in cone, and cleaning brush is equipped in circular cylinder, and gravity door is mounted in discharging capsul.
Description
Technical field
The present invention relates to food, chemical fields, are a kind of continuous solid-liquid separating equipments producing alcohol method protein concentrate.
Background technology
Protein concentrate is the protein product that a kind of protein content is up to 65% or more, mainly using the degreasing dregs of rice as raw material
（Such as Soybean Meal, peanut meal）, typically by with ethanol solution extract remove the dregs of rice in soluble sugar, ash content and its
His solable matter, to make the content of material protein be increased on 65% from 50~55%；The solid-liquid being related in production technology
Separation equipment mainly has horizontal spiral centrifuge, scraper centrifugal machine, vacuum desolvation machine and Batch Pressure Filtrating Equipment etc.；Horizontal spiral from
Scheming, scraper centrifugal machine, this kind of equipment such as vacuum desolvation machine have equipment noise big, complicated, and power consumption is big, price
Height is unfavorable for promoting the use of；It is big that the filter press of batch production then operates labor intensity, and alcohol solvent consumption is big, production cost
Height is especially detrimental to industrialization and automatically controls；Therefore, the improvement for producing the solid-liquid separating equipment during protein concentrate is mesh
The problem of preceding urgent need to resolve.
Invention content
For the above situation, to solve the defect of existing equipment, the purpose of the present invention is just to provide a kind of production concentrate egg
Eddy flow extrusion separator in vain, it is big effectively to solve intermittently operated labor intensity, is unfavorable for industrialization and automatically controls, easily occurs
The phenomenon that run, drip, leak, and the problem of centrifugation apparatus price is high, complicated, and transmission parts are susceptible to failure.
The technical solution that the present invention solves is that the machine includes decelerating motor, engine base, shaft coupling, hollow shaft, cone-type spiral leaf
Piece, cone, bullet, liquid header, cylinder, circular cylinder, gravity door and discharging capsul etc., decelerating motor is mounted on
On engine base, output shaft is connected as screw extrusion component with cone spiral vane by shaft coupling, hollow shaft and is located at circular cone
In body, bullet, it is provided with hole in hollow shaft, cylinder is installed on axis, strainer is installed on cylinder；Engine base is collected with liquid
Device is connected, and liquid header is connected by flange with cone, has tangential admission mouth on cone, circle is equipped in cone
Tin, cleaning brush is installed in circular cylinder, cone is connected by flange with bullet, and bullet passes through flange and discharging capsul
It is connected, has discharge port, gravity door to be mounted in discharging capsul below discharging capsul.
The beneficial effects of the invention are as follows simple and reasonable, easy to operate, using effect is good.
Description of the drawings
Fig. 1 is the structural front view of the present invention.
Specific implementation mode
The specific implementation mode of the present invention is described in further detail below in conjunction with attached drawing.
It is provided by Fig. 1, the machine includes decelerating motor, engine base, shaft coupling, hollow shaft, cone spiral vane, cone, cone
Body, liquid header, cylinder, circular cylinder, gravity door and discharging capsul etc., decelerating motor 5 are mounted on engine base 4,
Output shaft be connected with cone spiral vane 14 by shaft coupling 6, hollow shaft 7 as screw extrusion component and positioned at cone 2,
In bullet 13, it is provided with hole in hollow shaft 7, cylinder 11 is installed on axis, strainer 12 is fixed by bolts on cylinder 11；Liquid
Liquid outlet 8 is installed, engine base 4 is connected with liquid header 3, and liquid header 3 passes through flange and cone 2 on body collector 3
It is connected, tangential admission mouth 1 is installed on cone 2, circular cylinder 9 is installed in cone 2, cleaning brush is installed in circular cylinder 9
10, cone 2 is connected by flange with bullet 13, and bullet 13 is connected by flange with discharging capsul 16, discharging sealing
16 lower section of shell has discharge port 17, gravity door 15 to be mounted in discharging capsul 16.
The eddy flow extrusion separator is made of centrifugation, filtering and extruding three parts.
The cylinder 11 is rolled by stainless steel screen, closed at both ends manufactured.
The present invention service condition be, in the degreasing dregs of rice be added temperature be 50~55 DEG C, the ethyl alcohol that volumetric concentration is 65~75%
Solution（Solid-liquid ratio is 1:6~7）, after being washed 0.2~0.5 hour in washing facility, it is sent into eddy flow with slush pump and squeezes separation
It is separated by solid-liquid separation in machine, feed liquid is entered in tangential direction by feed inlet 1, solid under the centrifugation force effect generated in cone 2
Liquid is initially separated, and solid-phase material is fallen in bullet 13, can must be contained under the extruding of cone spiral vane 14 and gravity door 15
The protein concentrate of ethyl alcohol 70%~85% is protein concentrate product after being sent to vacuum desolvation drying by conveyer, crushed；Liquid phase object
Material is moved up along 9 inner wall of circular cylinder, and liquid header 3 is come together in into hollow shaft 7 across strainer 12 and cylinder 11, is passed through
Liquid outlet 8 exports, the solid material adhered on strainer 12, and cleaning processing is completed under the action of cleaning brush 10.
The configuration of the present invention is simple is reasonable, easy to operate, using effect is good, can not only effectively solve Batch Pressure Filtrating Equipment operation
Labor intensity is big, and alcohol solvent consumption is big, and production cost is high, is unfavorable for the problem of industrialization automatically controls, moreover it is possible to effectively overcome
This kind of equipment such as centrifugation, vacuum desolvation, noise is big, complicated, power consumption is big, price is high, the problem of being not easy to promote, and has
Good economic and social benefit.
Claims (3)
1. a kind of eddy flow extrusion separator, including decelerating motor, engine base, shaft coupling, hollow shaft, cone spiral vane, cone,
Bullet, liquid header, cylinder, circular cylinder, gravity door and discharging capsul etc., which is characterized in that decelerating motor (5) is pacified
On engine base (4), output shaft is connected by shaft coupling (6), hollow shaft (7) with cone spiral vane (14) to be squeezed as spiral
Splenium part is simultaneously interior positioned at cone (2), bullet (13), and hole is provided in hollow shaft (7), cylinder (11) is equipped on axis, is filtered
Net (12) is fixed by bolts on cylinder (11)；Liquid outlet (8) is installed, engine base (4) is received with liquid on liquid header (3)
Storage (3) is connected, and liquid header (3) is connected by flange with cone (2), and cone is equipped with tangential admission mouth on (2)
(1), circular cylinder (9) is installed in cone (2), cleaning brush (10) is installed, cone (2) passes through flange in circular cylinder (9)
It is connected with bullet (13), bullet (13) is connected by flange with discharging capsul (16), is had below discharging capsul (16)
Discharge port (17), gravity door (15) are mounted in discharging capsul (16).
2. a kind of eddy flow extrusion separator according to claim 1, which is characterized in that the eddy flow extrusion separator is
By centrifugation, filtering and squeeze what three parts formed.
3. a kind of eddy flow extrusion separator according to claim 1, which is characterized in that the cylinder (11) is by not
Rust steel screen rolls, closed at both ends manufactured.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810345493.0A CN108285476A (en) | 2018-04-17 | 2018-04-17 | A kind of eddy flow extrusion separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810345493.0A CN108285476A (en) | 2018-04-17 | 2018-04-17 | A kind of eddy flow extrusion separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108285476A true CN108285476A (en) | 2018-07-17 |
Family
ID=62834628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810345493.0A Pending CN108285476A (en) | 2018-04-17 | 2018-04-17 | A kind of eddy flow extrusion separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108285476A (en) |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH418983A (en) * | 1961-09-25 | 1966-08-15 | Karl Marx Stadt Maschf | Vibrating centrifuge |
| WO2000029090A1 (en) * | 1998-11-12 | 2000-05-25 | Martin Systems Ag | Device for separating waste water |
| JP2004174467A (en) * | 2002-11-29 | 2004-06-24 | Tanaka:Kk | Vertical continuous solid-liquid separator and recovered plastic separation process |
| JP2006198540A (en) * | 2005-01-21 | 2006-08-03 | Mori Plant:Kk | Solid-liquid separator |
| CN1958169A (en) * | 2006-09-07 | 2007-05-09 | 宋蜀江 | Centrifugal machine |
| CN202208116U (en) * | 2011-08-22 | 2012-05-02 | 苏州优耐特机械制造有限公司 | Centrifugal screw extruder |
| CN102784498A (en) * | 2011-05-17 | 2012-11-21 | 宜昌市新丰机电设备制造有限公司 | Vertical centrifugal settling solid-liquid separator and separation method thereof |
| CN203269833U (en) * | 2013-03-08 | 2013-11-06 | 河南工业大学 | Pre-desolventizing extruding machine |
| CN203635340U (en) * | 2013-12-27 | 2014-06-11 | 佳毅(上海)机械设备有限公司 | Super-micro-fine powder separator |
| CN205687844U (en) * | 2016-04-13 | 2016-11-16 | 河南工业大学 | A kind of pre-precipitation screw extruder |
| WO2017107944A1 (en) * | 2015-12-24 | 2017-06-29 | 重庆市农业科学院 | Device and method for feeding methane fermentation material with high solid content |
-
2018
- 2018-04-17 CN CN201810345493.0A patent/CN108285476A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH418983A (en) * | 1961-09-25 | 1966-08-15 | Karl Marx Stadt Maschf | Vibrating centrifuge |
| WO2000029090A1 (en) * | 1998-11-12 | 2000-05-25 | Martin Systems Ag | Device for separating waste water |
| JP2004174467A (en) * | 2002-11-29 | 2004-06-24 | Tanaka:Kk | Vertical continuous solid-liquid separator and recovered plastic separation process |
| JP2006198540A (en) * | 2005-01-21 | 2006-08-03 | Mori Plant:Kk | Solid-liquid separator |
| CN1958169A (en) * | 2006-09-07 | 2007-05-09 | 宋蜀江 | Centrifugal machine |
| CN102784498A (en) * | 2011-05-17 | 2012-11-21 | 宜昌市新丰机电设备制造有限公司 | Vertical centrifugal settling solid-liquid separator and separation method thereof |
| CN202208116U (en) * | 2011-08-22 | 2012-05-02 | 苏州优耐特机械制造有限公司 | Centrifugal screw extruder |
| CN203269833U (en) * | 2013-03-08 | 2013-11-06 | 河南工业大学 | Pre-desolventizing extruding machine |
| CN203635340U (en) * | 2013-12-27 | 2014-06-11 | 佳毅(上海)机械设备有限公司 | Super-micro-fine powder separator |
| WO2017107944A1 (en) * | 2015-12-24 | 2017-06-29 | 重庆市农业科学院 | Device and method for feeding methane fermentation material with high solid content |
| CN205687844U (en) * | 2016-04-13 | 2016-11-16 | 河南工业大学 | A kind of pre-precipitation screw extruder |
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