CN206828512U - A kind of Combined fermentation pot - Google Patents
A kind of Combined fermentation pot Download PDFInfo
- Publication number
- CN206828512U CN206828512U CN201720596570.0U CN201720596570U CN206828512U CN 206828512 U CN206828512 U CN 206828512U CN 201720596570 U CN201720596570 U CN 201720596570U CN 206828512 U CN206828512 U CN 206828512U
- Authority
- CN
- China
- Prior art keywords
- tank body
- pipe
- discharge nozzle
- main
- air inlet
- 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.)
- Active
Links
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
It the utility model is related to a kind of Combined fermentation pot, include at least two tank bodies, each tank body is connected with feed pipe one, feed pipe two, discharge nozzle and air inlet pipe, all feed pipes one connect main feed pipe, all feed pipes two connect main discharge nozzle with discharge nozzle, all air inlet pipe connection main air inlet pipes and all tank bodies, the main feed pipe, main discharge nozzle and main air inlet pipe are respectively connected with pump, and a valve is equipped with each feed pipe one, feed pipe two, discharge nozzle and air inlet pipe.Oxygen contact surface can be effectively increased using the present apparatus, balance the fermenting speed in single tank body and different tank bodies, keep strain quantity balance, the quality of zymotic fluid is improved, in the case where producing equivalent zymotic fluid, greatly improves fermenting speed, simple and practical, cost is cheap, is easy to produce.
Description
Technical field
A kind of installation for fermenting is the utility model is related to, particularly a kind of Combined fermentation pot.
Background technology
Acetic fermentation is a kind of oxidative fermentation, it is necessary to which substantial amounts of oxygen, when oxygen deficiency or uneven stirring, can lead
The reproduction speed of microorganism is not quite identical in cause fermentation tank, and in tank bottom, tank and tank angle all has obvious difference, causes to ferment
Rate reduction, zymotic fluid quality is unstable, influences ferment effect.
Existing fermentation tank generally use 10t capacity, but to ensure oxygen supply space, the solution that 5t is only housed in tank is carried out
Fermentation, but due to the more oxygenating inconvenience of solution in tank body, stirring is difficult, oxygen contact surface deficiency, causes fermenting speed slow, ferments
Quality is unstable.
Utility model content
Goal of the invention of the present utility model is to overcome existing apparatus to cause fermenting speed to delay due to oxygen contact surface deficiency
Slowly, the above-mentioned deficiencies such as fermented quality is unstable, there is provided a kind of Combined fermentation pot, it is simple in construction, reasonable in design, effectively improve hair
Ferment speed, ensure fermented quality.
To achieve these goals, the technical solution adopted in the utility model is：
A kind of Combined fermentation pot, comprising at least two tank bodies, each tank body is connected with feed pipe one, feed pipe
2nd, discharge nozzle and air inlet pipe, all feed pipes one connect main feed pipe, and the feed pipe two connects master with discharge nozzle and gone out
Expects pipe, all the air inlet pipe connection main air inlet pipes and the tank body, the main feed pipe, main discharge nozzle and main air inlet pipe connect
Pump is connected to, a valve is equipped with each feed pipe one, feed pipe two, discharge nozzle and air inlet pipe.
Using a kind of Combined fermentation pot of the present utility model, comprising at least two tank bodies, each tank body is connected with
Feed pipe one, feed pipe two, discharge nozzle and air inlet pipe, the feed pipe one be used for added materials into the tank body, it is described enter
Tracheae is used to be used for the single tank body or any two tank body to the tank Invivo oxyger-supply, the feed pipe two and discharge nozzle
Interior material carries out circulation mixing, when the attenuation degree in some described tank body differs greatly, one tank body of unlatching
Feed pipe two and discharge nozzle, open the pump on the main discharge nozzle, and the material in the tank body is extracted out from the discharge nozzle, is passed through
The feed pipe two enters the tank body, promotes being mutually mixed for the material of diverse location in single tank body, balances single tank body
Interior reaction speed；When the attenuation degree in two tank bodies differs greatly, the discharging of a tank body is opened
The feed pipe two of pipe and another tank body, after the zymotic fluid in two tank bodies is mixed, then will wherein one
Divide and be withdrawn into the original tank body, to ensure overall fermenting speed, balance the strain quantity in different tank bodies, same to phase
Compared with an original large tank, when material storage storage keeps constant, oxygen contact surface greatly increases, and is advantageous to improve material
Fermenting speed, oxygen contact surface can be effectively increased using the present apparatus, balance the fermenting speed in single tank body and different tank bodies, protected
Strain quantity balance is held, the quality of zymotic fluid is improved, in the case where producing equivalent zymotic fluid, greatly improves fermenting speed, is tied
Structure is simple and practical, and cost is cheap, is easy to produce.
Preferably, each tank body is disposed with material bed, interlayer and heat-insulation layer from inside to outside.
Because fermentation is needed in certain preference temperature, be advantageous to accelerate reaction speed, be provided with using above-mentioned beneficial to dimension
Hold the temperature needed for fermentation.
It is further preferred that also including heater block, the heater block includes steam inlet tube and return pipe, each described
Steam inlet tube connects the interlayer of a tank body with return pipe, all steam inlet tube connection main steam pipes, owns
The return pipe connects main water return tube, and the steam (vapor) outlet connected with the interlayer is provided with the outside of each tank body, each described
Valve is equipped with steam inlet tube, steam (vapor) outlet and return pipe.
The temperature in the tank body is adjusted by the steam inlet tube and steam (vapor) outlet, to ensure most preferably to ferment
Temperature, the water that steam liquefied is formed are discharged by the return pipe.
It is further preferred that it is connected with a ball valve and a magnetic valve on each steam inlet tube.
Preferably, the feed pipe two is connected to the top of the tank body, and the discharge nozzle is connected to the bottom of the tank body
Portion.
Preferably, the air inlet pipe is connected to the bottom of the tank body.
It is easy to material more fully to be contacted with oxygen, is advantageous to improve fermenting speed.
Preferably, all tank body size shape all sames, arranged along same vertical axis parallel interval.
The tank body is stacked, is advantageous to space arrangement, is easy to the material between different tank bodies to mix, reduce connecting tube
Road, save cost.
It is further preferred that the tank body has three.
Preferably, the main discharge nozzle is also associated with water inlet pipe.
Water inlet pipe is connected with, is easy to clean the tank body using the feed pipe two and discharge nozzle.
Preferably, each tank body is additionally provided with thermometer, liquid level gauge, sampling valve and agitating device.
In summary, by adopting the above-described technical solution, the beneficial effects of the utility model are：
1st, using a kind of Combined fermentation pot of the present utility model, oxygen contact surface can be effectively increased, balances single tank body
And the fermenting speed in different tank bodies, strain quantity balance is kept, improves the quality of zymotic fluid, ensures that acidity, pol are unified,
In the case of producing equivalent zymotic fluid, fermenting speed is greatly improved, simple and practical, cost is cheap, is easy to produce.
2nd, using a kind of Combined fermentation pot of the present utility model, be advantageous to maintain the temperature needed for fermentation, accelerate fermentation
Speed.
3rd, using a kind of Combined fermentation pot of the present utility model, by the steam inlet tube and steam (vapor) outlet to the tank
Internal temperature is adjusted, and to ensure optimum fermentation temp, the water that steam liquefied is formed is discharged by the return pipe.
4th, using a kind of Combined fermentation pot of the present utility model, it is easy to material more fully to be contacted with oxygen, further
Be advantageous to improve fermenting speed.
5th, using a kind of Combined fermentation pot of the present utility model, water inlet pipe is connected with, is easy to utilize the feed pipe two
The tank body is cleaned with discharge nozzle.
Brief description of the drawings
Fig. 1 is a kind of structural representation of Combined fermentation pot in the utility model.
Fig. 2 is the structural representation of the pipeline connection of a tank body in the utility model.
Marked in figure：1- tank bodies, 11- is material bed, 12- interlayers, 13- heat-insulation layers, 2- main feed pipes, 21- feed pipes one, 3-
Main discharge nozzle, 31- feed pipes two, 32- discharge nozzles, 4- main air inlet pipes, 41- air inlet pipe, 5- pumps, 6- valves, 7- main steam pipes,
71- steam inlet tubes, 72- steam (vapor) outlets, 8- main water return tubes, 81- return pipes, 9- water inlet pipes.
Embodiment
Below in conjunction with the accompanying drawings, the utility model is described in detail.
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining this
Utility model, it is not used to limit the utility model.
Embodiment 1
Such as Fig. 1-2, a kind of Combined fermentation pot, comprising three tank bodies 1, all size shape all sames of tank body 1, edge
Same vertical axis parallel interval is arranged on three layers of support, and each tank body 1 is disposed with material from inside to outside
Layer 11, interlayer 12 and heat-insulation layer 13, each tank body 1 are connected with feed pipe 1, feed pipe 2 31, discharge nozzle 32 and air inlet
Pipe 41, the feed pipe 1 and feed pipe 2 31 are all connected to the top of the tank body 1, and the discharge nozzle 32 is connected to described
The bottom centre of tank body 1, all feed pipes 1 connect main feed pipe 2, and the feed pipe 2 31 and discharge nozzle 32 connect
Lead to main discharge nozzle 3, the air inlet pipe 41 is connected to the bottom of the tank body 1, and all air inlet pipe 41 connect the He of main air inlet pipe 4
The tank body 1, the main feed pipe 2, main discharge nozzle 3 and main air inlet pipe 4 are respectively connected with pump 5, each feed pipe 1, enter
A valve 6 is equipped with expects pipe 2 31, discharge nozzle 32 and air inlet pipe 41, is also included comprising heater block, the heater block
Steam inlet tube 71 and return pipe 81, each steam inlet tube 71 connect the interlayer of a tank body 1 with return pipe 81
12, all steam inlet tubes 71 connect main steam pipe 7, and all return pipes 81 connect main water return tube 8, each tank body
1 outside is provided with the steam (vapor) outlet 72 connected with the interlayer 12, each steam inlet tube 71, steam (vapor) outlet 72 and return pipe 81
On be equipped with valve 6, be connected with a ball valve and a magnetic valve on each steam inlet tube 71.
Three tank bodies 1 are vertically arranged, when the inside attenuation degree of some tank body 1 differs greatly, unlatching pair
The feed pipe 2 31 and discharge nozzle 32 of the tank body 1 are answered, opens the pump 5 on the main discharge nozzle 3, to the corresponding tank body
Zymotic fluid in 1 is circulated, and is easy to adjust the strain balance inside the tank body 1, is adjusted the fermentation inside the tank body 1 and put down
Weighing apparatus；If when needing circulation between tank body 1 described in any two, open the discharge nozzle 32 of one of them tank body 1 with
The feed pipe 2 31 of another tank body 1, the pump 5 on the main discharge nozzle 3 is opened, makes two tank bodies 1
After interior zymotic fluid mixing, then a portion is withdrawn into the original tank body 1, kept with a batch of zymotic fluid
Strain quantity balances, and attenuation degree is consistent.
When each tank body 1 is 3T capacity, three tank bodies 1 can ferment about 5T solution simultaneously altogether, compared to original
A 10T tank body, in the case that amount of fermentation is consistent, greatly increased using present apparatus oxygen contact surface, while oxygenating, heating side
Just and targetedly, faster, attenuation degree is unified in tank body for fermenting speed, is advantageous to keep strain quantity balance, ensures same
Batch produces the acidity of zymotic fluid, pol unification, advantageously ensures that steady quality, lifts products taste.
Preferred embodiment of the present utility model is the foregoing is only, it is all at this not to limit the utility model
All any modification, equivalent and improvement made within the spirit and principle of utility model etc., should be included in the utility model
Protection domain within.
Claims (10)
- A kind of 1. Combined fermentation pot, it is characterised in that comprising at least two tank bodies (1), each tank body (1) be connected with into Expects pipe one (21), feed pipe two (31), discharge nozzle (32) and air inlet pipe (41), all feed pipe one (21) connection main feeds Manage (2), all feed pipes two (31) connect main discharge nozzle (3) with discharge nozzle (32), and all air inlet pipe (41) are even Logical main air inlet pipe (4) and all tank bodies (1), the main feed pipe (2), main discharge nozzle (3) and main air inlet pipe (4) are all connected with There is pump (5), one is equipped with each feed pipe one (21), feed pipe two (31), discharge nozzle (32) and air inlet pipe (41) Valve (6).
- 2. a kind of Combined fermentation pot according to claim 1, it is characterised in that each tank body (1) is from inside to outside It is disposed with material bed (11), interlayer (12) and heat-insulation layer (13).
- 3. a kind of Combined fermentation pot according to claim 2, it is characterised in that also comprising heater block, the heating Part includes steam inlet tube (71) and return pipe (81), and each steam inlet tube (71) is connected described in one with return pipe (81) The interlayer (12) of tank body (1), all steam inlet tube (71) connection main steam pipes (7), all return pipes (81) Main water return tube (8) is connected, is provided with the steam (vapor) outlet (72) connected with the interlayer (12) on the outside of each tank body (1), each Valve (6) is equipped with the steam inlet tube (71), steam (vapor) outlet (72) and return pipe (81).
- 4. a kind of Combined fermentation pot according to claim 3, it is characterised in that be connected with each steam inlet tube (71) One ball valve and a magnetic valve.
- 5. a kind of Combined fermentation pot according to claim 1, it is characterised in that the feed pipe two (31) is connected to institute The top of tank body (1) is stated, the discharge nozzle (32) is connected to the bottom of the tank body (1).
- 6. a kind of Combined fermentation pot according to claim 1, it is characterised in that the air inlet pipe (41) is connected to described The bottom of tank body (1).
- 7. according to a kind of any described Combined fermentation pots of claim 1-6, it is characterised in that all tank bodies (1) are big Small shape all same, arranged along same vertical axis parallel interval.
- 8. a kind of Combined fermentation pot according to claim 7, it is characterised in that the tank body (1) has three.
- 9. according to a kind of any described Combined fermentation pots of claim 1-6, it is characterised in that the main discharge nozzle (3) is also It is connected with water inlet pipe (9).
- 10. according to a kind of any described Combined fermentation pots of claim 1-6, it is characterised in that each tank body (1) is also Provided with thermometer, liquid level gauge, sampling valve and agitating device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720596570.0U CN206828512U (en) | 2017-05-25 | 2017-05-25 | A kind of Combined fermentation pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720596570.0U CN206828512U (en) | 2017-05-25 | 2017-05-25 | A kind of Combined fermentation pot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206828512U true CN206828512U (en) | 2018-01-02 |
Family
ID=60773467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720596570.0U Active CN206828512U (en) | 2017-05-25 | 2017-05-25 | A kind of Combined fermentation pot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206828512U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113214957A (en) * | 2021-06-22 | 2021-08-06 | 苏州好唯加食品有限公司 | White vinegar production equipment and white vinegar production process |
-
2017
- 2017-05-25 CN CN201720596570.0U patent/CN206828512U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113214957A (en) * | 2021-06-22 | 2021-08-06 | 苏州好唯加食品有限公司 | White vinegar production equipment and white vinegar production process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205368314U (en) | Device is made to home -use white spirit of multi -functional quadruple | |
| CN201012920Y (en) | Upright solid material fermentation tank | |
| CN206196639U (en) | A kind of liquid feeds machine | |
| CN206828512U (en) | A kind of Combined fermentation pot | |
| CN107118946A (en) | The biogas generator and its operating method of dry and wet coupling | |
| CN110656043A (en) | Microbial fermentation tank for producing liquid feed additive | |
| CN206157155U (en) | Anaerobic fermentation device | |
| CN208151356U (en) | A kind of installation for fermenting of two-way stirring | |
| CN206866607U (en) | A kind of novel foodstuff fermentation tank | |
| CN209702758U (en) | A kind of microorganism tank with sampling bactericidal unit | |
| JP5756284B2 (en) | Microbial material culture and manufacturing equipment | |
| CN207699573U (en) | A kind of installation for fermenting | |
| CN110117530A (en) | Fruits and vegetables rubbish half dry type anaerobic fermentation based on horizontal mixer stores integrated apparatus | |
| CN216764879U (en) | Liquid microbial fermentation reaction equipment | |
| CN211814366U (en) | Intelligent mouldy bran preparation machine | |
| CN212199047U (en) | Novel liquid bacterial manure fermentation equipment | |
| CN205295344U (en) | Super set -retarding agent is produced marsh gas and is store marsh gas device | |
| CN210151084U (en) | Constant temperature fermentation or enzymolysis reaction device | |
| CN217077560U (en) | Shallow tray type solid bioreactor | |
| CN207079239U (en) | Solid state fermentation system | |
| CN113604355A (en) | High-turbulence small wet anaerobic digestion reactor and operation control method | |
| CN208617840U (en) | A kind of effectively optimizing type microbial ferment device | |
| CN203112810U (en) | Cellar oxygen adjusting device | |
| CN218710388U (en) | Novel probiotic fermentation tank | |
| CN207845613U (en) | A kind of wine brewing steamer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |