CN206266584U - Fermentation tank overflow collection separating and reclaiming device - Google Patents
Fermentation tank overflow collection separating and reclaiming device Download PDFInfo
- Publication number
- CN206266584U CN206266584U CN201621308964.3U CN201621308964U CN206266584U CN 206266584 U CN206266584 U CN 206266584U CN 201621308964 U CN201621308964 U CN 201621308964U CN 206266584 U CN206266584 U CN 206266584U
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- China
- Prior art keywords
- whizzer
- cyclone separator
- liquid
- fermentation tank
- tank
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Abstract
The utility model is related to microbial ferment device, especially fermentation tank overflow collection separating and reclaiming device.It includes fermentation tank, blast pipe on tank body, its structural feature is, also include Vapor-liquid cyclone separator and whizzer, Vapor-liquid cyclone separator is connected between blast pipe and the outer blast pipe of tank, Vapor-liquid cyclone separator lower section connection liquid material collecting pipe, sets whizzer in liquid material collecting pipe, whizzer drives backspin to turn in motor.Separated through cyclone separator one-level and whizzer the second-order separation, in time by the foam of the zymotic fluid of overflow and entrained with while completing to separate, collecting, flow back, promote zymotic fluid that breeding is cultivated under good process conditions, it is ensured that the yield and quality of microorganism kind.
Description
Technical field
The utility model is related to microbial ferment device, especially fermentation tank overflow collection separating and reclaiming device.
Background technology
Microorganism breeds in the whole technological process of fermentation in the Zymolysis Equipment drafted, to the sorption enhanced mistake of supplementary material
Cheng Zhong, can discharge certain energy under specific process conditions, influence the flourish of thalline, and it is mainly shown as：Hair
The increase of zymotic fluid material, when liquid material amount is held more than tank, just occurs canful discharge opeing phenomenon, and term is referred to as " jump liquid ".Jumping liquid one is
Tank product quality and yield are worked as in influence, and two is to jump liquid process contamination environment.Equally, microorganism breed fermentation process in,
Foam can be produced in many kinds.Repetition generation foam can equally surpass tank and hold and produce and jump liquid, influence yield and quality and pollute
Environment.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, and provides fermentation tank overflow collection separation and recovery dress
Put.Overflow zymotic fluid and the foam of overflow can simultaneously collect, separated by the device, be back in fermentation tank and promote zymotic fluid to keep
The flourish under good process conditions.
The purpose of this utility model is realized by following approach.
Fermentation tank overflow collection separating and reclaiming device, including fermentation tank, the blast pipe on tank body, its structural feature exist
In, also including Vapor-liquid cyclone separator and whizzer, Vapor-liquid cyclone separator is connected between blast pipe and the outer blast pipe of tank,
Vapor-liquid cyclone separator lower section connection liquid material collecting pipe, sets whizzer in liquid material collecting pipe, whizzer is in motor
Drive lower rotation.
So, in normal production process, by the air of fermentation tank discharge with the liquid taken out of through vapour-liquid whirlwind
Separator carries out vapor-liquid separation.Air is collected through the outer emission by exhaust pipe of tank, liquid through liquid material collecting pipe, flows back into tank, supplements water
Part, keep fermenter volume.
Show mercy under shape in super tank, the overflow of generation completes one-level and separates through cyclonic separation, then the rotation for being centrifuged device
Further the vapour-liquid that end is kept completely separate is centrifuged.Through secondary separation, vapor-liquid separation efficiency is improved.
The overflow caused for foam produced in microculture fermentation process is similarly by one cyclonic point
From rear discharge air, liquid material is flowed into whizzer, and whizzer rotates produced centrifugal force by liquid by high speed
Material is sprayed in vapour-liquid secondary separation on outer tube wall, is realized, material flows back into jar fermenter along collecting pipe, and air is through in cyclone separator
After sleeve pipe enters observation pipeline section, discharged by blast pipe.Complete the foam that disappears with frothy overflow and separate backflow.
Overflow is collected, separates, is flowed back, it is ensured that the operation of technological condition for fermentation by gas-liquid separation once, secondary.
The whizzer is drum closed-in construction, and staving periphery dot matrix is covered with diameter 5-6 millimeters of through hole.
So, under the high speed rotation of whizzer, liquid material, by being thrown out of in through hole, is produced by centrifugal force with outer tube wall
After raw strong injection, flash is fully finished gas-liquid separation.
Fermentation tank overflow collection separating and reclaiming device also includes exhaust observation pipeline section, and observation pipeline section middle part is provided with visor,
Between exhaust observation pipeline section is installed on the outer blast pipe of cyclone separator and tank, observation pipeline section top and reductor assembly and joining
Motor couples.
Visor is used to observe gas-liquid separation degree.Improve separator rotating speed, you can improve gas-liquid separation effect.
The utility model has the advantages that in time the foam of the zymotic fluid of overflow and entrained with can be completed to separate simultaneously, received
Collection, backflow, promote zymotic fluid that breeding is cultivated under good process conditions, it is ensured that the yield and quality of microorganism kind.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
The utility model is described in further detail below in conjunction with the accompanying drawings.
Embodiment
Such as Fig. 1, fermentation tank overflow collection separating and reclaiming device, including fermentation tank 10, the end of blast pipe 1 peace on tank body
Dress Vapor-liquid cyclone separator 2, separator 2 is connected with liquid material collecting pipe 41, there is whizzer 3 in liquid material collecting pipe, and liquid material is received
Manifold end connects return duct 42, accesses fermentation tank.Exhaust observation pipeline section 5 is set on cyclone separator 2, pipeline section and tank is observed
Outer blast pipe 9 is connected.Observation pipeline section top is installed and carries reductor assembly 7 and motor 8, the rotary shaft connection on reductor assembly
Whizzer, drives whizzer rotation, reductor assembly adjustment motor speed.Reductor assembly is intersegmental with observation tube to be adopted
Sealed with end surface mechanical sealing 6, prevent leakage.Whizzer is drum closed-in construction, and staving side face is covered with diameter 5-6 millimeters
Through hole.
The utility model idiographic flow is as follows：
Under normal process conditions, the air discharged by fermentation tank enters Vapor-liquid cyclone separator 2 by blast pipe 1, air by
Exhaust observation tube 5 enters the outer blast pipe 9 of tank.Liquid flows through return duct 42 and is back in fermentation tank by liquid material collecting pipe 41 after separation
Tank is kept to hold.
When the super tank of zymotic fluid holds, excess zymotic fluid is entered into Vapor-liquid cyclone separator 2 by the overflow of blast pipe 1, air is through row
After gas observation pipeline section, the outer blast pipe 9 of tank is entered.Material flows into whizzer 3 after cyclonic separation, and material is collected through liquid material
Pipe 41 flows through return duct 42 and flows into fermentation tank.
In fermentation process, suitable part biological variety can produce foam during flourish, when foam exceedes tank
Rong Shi, produces overflow.Overflow foam flows into Vapor-liquid cyclone separator 2 and carries out first stage separation by blast pipe 1, partial air by
Observation pipeline section 5 enters the outer blast pipe 9 of tank and concentrates discharge.After cyclonic separation, material flows into whizzer 3.By to by seeing
The observation in the space of pipeline section 5 is examined, if still containing partial material, whizzer rotating speed is illustrated not enough, it is total by adjusting reductor
Into 1500--4500 revs/min of turn up, whizzer rotating speed is improved.Liquid material completes second stage centrifugation point through centrifugal rotation
From material flows through return duct 42 and flows into fermentation tank by liquid material collecting pipe 41.Air is still discharged by blast pipe.
So, repeat centrifugation incessantly, it is ensured that normal tank holds, keep thalline to be grown under normal process conditions.
Claims (3)
1. fermentation tank overflow collection separating and reclaiming device, including fermentation tank, the blast pipe on tank body, it is characterised in that also wrap
Vapor-liquid cyclone separator is included, Vapor-liquid cyclone separator is connected between blast pipe and the outer blast pipe of tank, Vapor-liquid cyclone separator lower section
Connection liquid material collecting pipe, sets whizzer in liquid material collecting pipe, whizzer drives backspin to turn in motor.
2. fermentation tank overflow collection separating and reclaiming device according to claim 1, it is characterised in that the whizzer
It is drum closed-in construction, diameter 5-6 millimeters of through hole is covered with staving side face.
3. fermentation tank overflow collection separating and reclaiming device according to claim 1, it is characterised in that also observed including exhaust
Pipeline section, observation pipeline section middle part is provided with visor, and exhaust observation pipeline section is installed between cyclone separator and the outer blast pipe of tank, observation tube
Section top couples with reductor assembly and joining motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621308964.3U CN206266584U (en) | 2016-12-01 | 2016-12-01 | Fermentation tank overflow collection separating and reclaiming device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621308964.3U CN206266584U (en) | 2016-12-01 | 2016-12-01 | Fermentation tank overflow collection separating and reclaiming device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206266584U true CN206266584U (en) | 2017-06-20 |
Family
ID=59042422
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621308964.3U Active CN206266584U (en) | 2016-12-01 | 2016-12-01 | Fermentation tank overflow collection separating and reclaiming device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206266584U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635741A (en) * | 2016-12-01 | 2017-05-10 | 沈奇光 | Fermentation tank overflow collecting, separating and recycling device |
-
2016
- 2016-12-01 CN CN201621308964.3U patent/CN206266584U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106635741A (en) * | 2016-12-01 | 2017-05-10 | 沈奇光 | Fermentation tank overflow collecting, separating and recycling device |
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