CN207854947U - A kind of saturating ferment installation for fermenting of spiral - Google Patents
A kind of saturating ferment installation for fermenting of spiral Download PDFInfo
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- CN207854947U CN207854947U CN201721707003.4U CN201721707003U CN207854947U CN 207854947 U CN207854947 U CN 207854947U CN 201721707003 U CN201721707003 U CN 201721707003U CN 207854947 U CN207854947 U CN 207854947U
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Abstract
The utility model provides a kind of saturating ferment installation for fermenting of spiral, the holder of regulating device, the tank body of class cylinder, the power plant at the top of installation for fermenting, breathing equipment and peep hole are carried including bottom, and the agitating device positioned at tank interior center, it is characterized in that, further including the ventilation channel, numerical control system and cleaning device of tank body side；The agitating device is the rotation axis equipped with agitating auger paddle, and the rotation axis is fixed on stirring retarder bottom；The numerical control system is located at tank base, and mainly each inductive probe is set and detected to the items such as temperature, pressure, PH, acidity fermentation parameter in device.The utility model realizes the timely exclusion of the accurate supply and carbon dioxide of aseptic oxygen, make feed liquid uniform fermentation simultaneously, improves mouthfeel, chromaticness, the stability of koumiss product, extend the shelf life of product, for koumiss storage, transport, industrialized production provides technical guarantee.
Description
Technical field
The utility model belongs to field of fermentation equipment, and in particular to a kind of saturating ferment installation for fermenting of spiral.
Background technology
With comprehensive rapid development of " Chinese horse is all " Xilin Hot horse industry, possess the koumiss front of history in 2000
Face from tradition to modern transition and upgrade.However koumiss fermentation is different from milk, is aerobic fermentation, that is, fermentation process
Middle needs constantly filling oxygen, is constantly discharged carbon dioxide.
Past koumiss fermentation filling oxygen, relies primarily on container open and is contacted with air to realize, both unhygienic in this way,
It cannot guarantee that the clean-up performance of air simultaneously, excluding carbon dioxide, mainly manually wooden blender moves up and down and realizes,
Time, the frequency and the intensity of stirring cannot be accurately controlled, it is difficult to ensure that the mouthfeel of koumiss, quality and effect.
Koumiss ferments at home at present, relies primarily on traditional wooden stir device, manually stirs koumiss up and down, often
Day stirs 2-3 times, under each 800-1000, opens wide cylinder mouth to contact oxygen, in order to meet the parameters such as fermentation temperature, fermentation is held
Device is put into 20-30 centimetres of underground, when the temperature increases, is cooled down with cold water, and winter adds thermal insulation material in container surroundings, to expire
Sufficient fermentation condition.This traditional zymotic, it cannot be guaranteed that the time stirred needed for product fermentation, the frequency, intensity, required temperature of fermenting
Technological requirement is not achieved in degree, environment.
At abroad, koumiss fermentation mostly uses the stirring of automatic circumference movement, this agitating mode, although can mix
Material, but only moved in same plane, it cannot move up and down, the carbon dioxide for generation of fermenting cannot be exhausted fully, required oxygen
It cannot be replenished in time, in terms of strain fermentation, the fermentation condition of different phase different fermentations strain cannot be met.
Invention content
Aiming at the deficiencies in the prior art, the saturating ferment installation for fermenting of a kind of spiral of the utility model.The utility model is not
It only can accurately supply aseptic oxygen and exclude carbon dioxide in time, and various parameters in zymotechnique can be controlled
And detection.
For above-mentioned purpose, technical solutions of the utility model are as follows：
A kind of saturating ferment installation for fermenting of spiral, including bottom carry the holder of regulating device, the tank body of class cylinder, positioned at hair
Power plant, breathing equipment at the top of ferment device and peep hole, and the agitating device positioned at tank interior center, are also wrapped
Include the ventilation channel, numerical control system and cleaning device of tank body side；The power plant includes motor and stirring retarder；
The agitating device is the rotation axis equipped with agitating auger paddle, and the rotation axis is fixed on stirring retarder bottom；
The numerical control system is located at tank base, mainly each inductive probe, to temperature, pressure, PH, acid in device
Every fermentation parameter such as degree is set and is detected.
Further, the motor is three alternating current generators, provides stirring power.
Further, rotating speed is converted to a lower rotating speed by the stirring retarder；It is arrived again by Frequency Converter Control
Specifically used rotating speed；By the setting of PLC program, the open frequency stirred in entire fermentation stage, and each week are controlled
The length of phase, this period frequency can be adjusted according to different products.
Further, the agitating auger paddle is up to three, and highest agitating auger paddle is less than highest liquid level piece 300mm
It is advisable.
Further, the tank body is designed using chuck, and 30-40 DEG C of warm water is led in chuck, maintains hair during the fermentation
The temperature of zymotic fluid, due to there is a large amount of filtrated air to be passed through in fermentation process, by volatilizing, heat absorption can take away partial heat, cause
The temperature of fermentation can reduce, therefore lead to warm water in chuck, and when tank body broth temperature is less than setting value, inlet valve is beaten
It opens, warm water automatic cycle, cycle is automatically closed after reaching temperature.
Further, the ventilation channel is to establish a filtrated air system in installation for fermenting region, with anhydrous, oil-free
Compressed air is power source, by three layers of pre-filtering, clean compressed air is made, then by 0.1 μm of sterilizing filter, obtain nothing
Bacterium air；Filtrated air is mixed into during stirring in zymotic fluid by multigroup aeration head；The pressure of filtrated air controls
In 0.2~0.3bar.
Further, the cleaning device is automatic cleaning, including three pressure for washing ball and device bottom that tank body is equipped with
Purge valve；It is described that wash one, ball right for top and peep hole, other two lower parts for being distributed in agitating auger paddle in cleaning device
Blade is cleaned；The pressure wash valve configures on stockline, increases the cleaning flow velocity for stockline.
Further, the numerical control system includes temp probe and sensor；Sensor include high liquid level sensor,
Low liquid level sensor realizes automatically controlling for zymotechnique.
Further, the bottom of the tank body is equipped with discharge port and sterile sampling mouth.
Further, breathing equipment breathing tube control valve during ventilation is opened, and makes the CO2 in installation for fermenting
Discharge in time；Breathing tube control valve door is closed when not being aerated, and the filtrated air tonifying Qi valve at the top of device is opened, and ensures tank body
Barotropic state, while safety valve is also equipped at the top of device automatically opens when pressure is excessive or negative pressure, opens guarantee tank body
Safety.
Advantageous effect：The utility model realizes the accurate supply of aseptic oxygen, while making feed liquid uniform fermentation, avoids fat
Fat floats and albumen precipitation, improves mouthfeel, chromaticness, the stability of koumiss product, extends the shelf life of product, for sour horse
Milk storage, transport, industrialized production provide technical guarantee.The utility model not only ensures the cleaning that mare's milk fermentation air uses
Degree, the timely exclusion of carbon dioxide, and so that feed liquid is fully merged, thermally equivalent, to prevent product fat floating and albumen heavy
It forms sediment, while utilizing computer numeral system control process fermentation parameter, ensure that different strain fermentations can reach optimised process
Parameter.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the partial structural diagram of part on the utility model.
Fig. 3 is the partial structural diagram of the utility model lower part.
Specific implementation mode
Illustrate the utility model referring to specific embodiment.It will be appreciated by those skilled in the art that these are implemented
Example is merely to illustrate the utility model, does not limit the scope of the utility model in any way.
A kind of saturating ferment installation for fermenting of spiral, as shown in Figure 1, including holder (1) of the bottom with regulating device (101), class
The tank body (2) of cylinder, the power plant (3) at the top of installation for fermenting, breathing equipment (4) and peep hole (5), and be located at
The agitating device (6) of tank body (2) inner hub location, which is characterized in that further include the ventilation channel (7), number of tank body (2) side
Word control system (8) and cleaning device (9)；The power plant includes motor (301) and stirring retarder (302)；
Above-mentioned breathing equipment (4) breathing tube control valve during ventilation is opened, and the CO in installation for fermenting is made2Row in time
Go out；Breathing tube control valve door is closed when not being aerated, and the filtrated air tonifying Qi valve at the top of device is opened, and ensures the positive pressure shape of tank body
State, while safety valve is also equipped at the top of device automatically opens when pressure is excessive or negative pressure, opens the peace for ensureing tank body
Entirely；
Above-mentioned agitating device (6) is the rotation axis (601) equipped with agitating auger paddle (602), and the rotation axis (601) is fixed
In stirring retarder (302) bottom, the present embodiment agitating auger paddle (602) is three；
Above-mentioned numerical control system (8) is located at tank body (2) bottom, mainly each inductive probe, to temperature, pressure in device
The items fermentation parameter such as power, PH, acidity is set and is detected.
As shown in Fig. 2, tank body (2) using chuck design, include positioned at top of the tank interlayer inlet pipeline (201) and into
Penstock (202)；Highest agitating auger paddle (602) is less than at highest liquid level piece (203) 300mm；
Ventilation channel (7) includes the sterile sky for being located at filtrated air inlet port (701) and tank body (2) inside at the top of device
Gas aeration head (702), filtrated air aeration head (702) are located at the obliquely downward of agitating auger paddle (602), therefore the nothing of the present embodiment
Bacterium air aeration head (702) is three；Cleaning spray head (9) is also set up at the top of device.
As shown in figure 3, numerical control system (8) includes temp probe (801) and sensor (802)；The tank body (2)
Bottom is equipped with drawing mechanism (204) and sterile sampling mouth (205).
Claims (10)
1. a kind of saturating ferment installation for fermenting of spiral, including bottom carry the holder of regulating device, the tank body of class cylinder, positioned at fermentation
Power plant, breathing equipment at the top of device and peep hole, and the agitating device positioned at tank interior center, feature
It is, further includes the ventilation channel, numerical control system and cleaning device of tank body side；The power plant includes motor and stirs
Mix retarder；
The agitating device is the rotation axis equipped with agitating auger paddle, and the rotation axis is fixed on stirring retarder bottom；
The numerical control system is located at tank base, mainly each inductive probe, to temperature, pressure, PH, acidity etc. in device
Every fermentation parameter is set and is detected；
The tank body is designed using chuck, and 30-40 DEG C of warm water, the set temperature for maintaining zymotic fluid are led in chuck.
2. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the motor is three alternating currents
Machine provides stirring power.
3. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the stirring retarder turns rotating speed
Change to a lower rotating speed；Pass through Frequency Converter Control to specifically used rotating speed again；By the setting of PLC program, control exists
The open frequency of entire fermentation stage stirring, and each length in period, this period frequency can be according to different products
It is adjusted.
4. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the agitating auger paddle is up to three
A, highest agitating auger paddle is advisable less than highest liquid level piece 300mm.
5. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that lead to warm water in the tank body chuck,
Include the interlayer inlet pipeline and inlet valve positioned at top of the tank；When tank body broth temperature is less than setting value, inlet valve
Door is opened, and cycle is automatically closed after reaching temperature in warm water automatic cycle.
6. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the ventilation channel further includes being located at
The filtrated air aeration head of filtrated air inlet port and tank interior at the top of device, filtrated air aeration head are located at agitating auger
The obliquely downward of paddle, filtrated air are mixed into during stirring in zymotic fluid by aeration head；The pressure of filtrated air controls
In 0.2~0.3bar.
7. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the cleaning device is automatic clear
Wash, including tank body be equipped with three wash ball and the pressure wash valve at device bottom；It is described wash one, ball for top in cleaning device and
Peep hole, other two lower parts for being distributed in agitating auger paddle, cleans blade；The pressure wash valve configures stockline
On, increase the cleaning flow velocity for stockline.
8. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the numerical control system includes temperature
Degree probe and sensor；Sensor includes high liquid level sensor, low liquid level sensor, realizes automatically controlling for zymotechnique.
9. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the bottom of the tank body is equipped with discharging
Mouth and sterile sampling mouth.
10. a kind of saturating ferment installation for fermenting of spiral as described in claim 1, which is characterized in that the breathing equipment is in ventilation
Breathing tube control valve is opened in the process, makes the CO in installation for fermenting2Discharge in time；Breathing tube control valve door is closed when not being aerated,
Filtrated air tonifying Qi valve at the top of device is opened, and ensures the barotropic state of tank body, while safety is also equipped at the top of device
Valve is automatically opened when pressure is excessive or negative pressure, opens the safety for ensureing tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721707003.4U CN207854947U (en) | 2017-11-30 | 2017-11-30 | A kind of saturating ferment installation for fermenting of spiral |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721707003.4U CN207854947U (en) | 2017-11-30 | 2017-11-30 | A kind of saturating ferment installation for fermenting of spiral |
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| CN207854947U true CN207854947U (en) | 2018-09-14 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109205128A (en) * | 2018-10-29 | 2019-01-15 | 上海外高桥造船有限公司 | The big packing jar of one pack system |
| CN112088938A (en) * | 2020-09-18 | 2020-12-18 | 袁龙生 | Vortex oxygenation fermenting installation |
-
2017
- 2017-11-30 CN CN201721707003.4U patent/CN207854947U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109205128A (en) * | 2018-10-29 | 2019-01-15 | 上海外高桥造船有限公司 | The big packing jar of one pack system |
| CN112088938A (en) * | 2020-09-18 | 2020-12-18 | 袁龙生 | Vortex oxygenation fermenting installation |
| CN112088938B (en) * | 2020-09-18 | 2024-04-16 | 袁龙生 | Vortex oxygenation fermentation device |
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