CN209039454U - A kind of full-automatic pressure-controlled type novel fermentation equipment - Google Patents
A kind of full-automatic pressure-controlled type novel fermentation equipment Download PDFInfo
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- CN209039454U CN209039454U CN201820436272.XU CN201820436272U CN209039454U CN 209039454 U CN209039454 U CN 209039454U CN 201820436272 U CN201820436272 U CN 201820436272U CN 209039454 U CN209039454 U CN 209039454U
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Abstract
The utility model discloses a kind of full-automatic pressure-controlled type novel fermentation equipment, belong to fermentation mechanical equipment technical field, including shell and tank body, interlayer is provided between the shell and the tank body, heating tube is provided in the interlayer, bottom is provided with oxygen supervisor in the tank body, multiple oxygen supply gas branch pipes are vertically provided on the oxygen supervisor, multiple first apertures are evenly arranged on each oxygen supply gas branch pipe, the oxygen supply mechanism connection of the oxygen supervisor and the outer side of shell, it is intermediate in tank body to be vertically provided with telescopic rod, the telescopic rod bottom end is provided with disk, the telescopic rod top end is provided with motor, multiple second orifices are provided on the disk, and the diameter for supplying oxygen gas branch pipe is less than the diameter of the second orifice, feed inlet is provided on the shell, electromagnetic valve and controller, tank base It is provided with discharge port.The application is mixed material uniformly and effectively with oxygen, and mixture homogeneity is high, and fermentation efficiency is high, consumes energy low.
Description
Technical field
The utility model relates to mechanical equipment technical fields of fermenting, and relate particularly to a kind of novel hair of full-automatic pressure-controlled type
Ferment equipment.
Background technique
Aerobic fermentation is carried out to raw material in the fermentation manufacturing techniques such as fertilizer, feed, food, due to the micro- life of aerobic fermentation
Oxygen required for the breathing of object, the oxidation of matrix is the oxygen dissolved in liquid phase, therefore the gas-liquid of oxygen passes during aerobic fermentation
Matter is particularly significant, needs for air to be constantly passed through in fermentation liquid during the fermentation, for oxygen consumed by microorganism.Microorganism
The oxygen uptake of group is very big, usually 10-50 × 103mol/ (Lh), but solubility of the oxygen in fermentation liquid is very low,
1.013 × 105Pa, at 25 DEG C, saturation solubility of the oxygen in fermentation liquid is only 0.2 × 103mol/L in air, and dissolved oxygen is insufficient
The respiratory metabolism of microorganism can be seriously affected.Maintain eupnea metabolism that must supplement the dissolved oxygen in culture solution rapidly, because
This oxygen solution rate becomes the limiting factor of aerobic fermentation process.
The normal formula air blow tank with machinery agitation that China generallys use, i.e. bottom ventilation at present, then by reinforcing stirring
To realize the purpose of dissolved oxygen.
Defect existing for existing normal formula air blow tank with machinery agitation has: stirring unshapeliness causes oxygen equal
It is even to be effectively mixed with material, cause fermentation time too long, production efficiency is low, additionally due to only setting in fermenter base
It is equipped with heating plate, causes heating uneven, influences ferment effect, furthermore since some sticky materials easily bond, close to fermentor
Because poor fluidity easily adheres at inner wall, lead to the inefficiency of stirring, incorporation time is long, and material mixture homogeneity is low.
Utility model content
It cannot be uniformly and effectively mixed with material for above-mentioned oxygen, cause fermentation time too long, production efficiency is low
Under defect, the utility model provides a kind of full-automatic pressure-controlled type novel fermentation equipment, the technical solution of the application make material with
Oxygen can be uniformly and effectively mixed, and keep material mixture homogeneity high, and fermentation efficiency is high, and consume energy low, high production efficiency, and tank
Internal pressure is automatic control, safe and easy to operate.
The utility model specifically uses a kind of following technical scheme: full-automatic novel hair of pressure-controlled type to achieve the goals above
Ferment equipment, including shell and tank body are provided with interlayer, heating are provided in the interlayer between the shell and the tank body
It manages, bottom is provided with oxygen supervisor in the tank body, is vertically provided with multiple oxygen supply gas branch pipes on the oxygen supervisor, often
Multiple first apertures, the aerator of the oxygen supervisor and the outer side of shell are evenly arranged on a oxygen supply gas branch pipe
Structure is connected to, and intermediate in the tank body to be vertically provided with telescopic rod, the telescopic rod bottom end is provided with disk, the telescopic rod top end
The outer side of shell is extended to, the telescopic rod top end is provided with motor, and multiple second orifices are provided on the disk, described
Second orifice is matched with the oxygen supply gas branch pipe, and the diameter of the oxygen supply gas branch pipe is less than the diameter of the second orifice,
Feed inlet, electromagnetic valve and controller are provided on the shell, the tank body inner sidewall is provided with pressure sensor, described
Electromagnetic valve and the pressure sensor are electrically connected with the controller respectively, and the tank base is provided with discharge port.
Working principle: closing discharge port, opens feed inlet, and the material for needing to ferment and microorganism fungus kind is added to feed inlet
That is fermentation materials, close feed inlet, oxygen mechanism to oxygen be responsible in input oxygen, oxygen by after oxygen supervisor from
The first aperture on oxygen supply gas branch pipe enters in the intracorporal fermentation materials of tank, and motor drives telescopic rod flexible up and down, telescopic rod band
Dynamic disk stirs fermentation materials up and down, makes the contact of fermentation materials with oxygen uniform high-efficiency, and pressure sensor detects tank body internal pressure
Power simultaneously reaches controller, and when pressure is excessive in tank body, controller controls electromagnetic valve and opens, and guarantees safety.By above
Technical solution, by the setting of telescopic rod, disk and second orifice, telescopic rod is flexible up and down to hit disk back and forth in material
It hits, second orifice, which is formed, to be shunted, then is mixed again under the effect of gravity, and fermentation materials and fermentation materials and oxygen can be sufficiently
Contact is repeated several times, and is uniformly mixed fermentation materials, and keep fermentation raw material uniform with oxygen mix, and stirring efficiency is high, energy consumption
It is low, fermentation time is shortened, ferment effect is good, high production efficiency, solves in the prior art due to stirring unshapeliness, leads to oxygen
Gas cannot be uniformly and effectively mixed with material, cause fermentation time too long, the low defect of production efficiency.
Further, the oxygen supply mechanism includes being responsible for the oxygen supply tracheae being connected to, the oxygen supply tracheae with the oxygen
The oxygen supply gas tank of end and the endotracheal blower of oxygen supply.Start blower, the oxygen supplied oxygen in gas tank passes through oxygen supply tracheae
And enter in fermentor, oxygen needed for fermentation is provided.
Further, the heating tube ring-type inclination is wound in interlayer, described heating tube one end and the shell exterior
Water inlet pipe connection, the heating tube other end is connected to the outlet pipe of the shell exterior, and the is provided on the water inlet pipe
One valve is provided with the second valve on the outlet pipe.When fermentation needs to heat, the first valve is opened, closes the second valve, to
Water is added in heating tube, closes the first valve, and heating tube is begun to warm up, and heats to tank body, after fermentation, opens the second valve,
Hot water in heating tube is released and recycled, cold water is constantly injected into heating tube, accelerates the speed that material cools down in fermentor
Degree, saves the time, high production efficiency.
Further, multiple second hairbrush are evenly arranged on the second orifice inner wall.The setting of second hairbrush, in circle
Disk stirs material up and down, and when oxygen supply gas branch pipe passes through or is pierced by second orifice, the second hairbrush can brush away to be bonded on the first aperture
Material prevents the first aperture of feed blocking in fermentation.
Further, the disk periphery is provided with first hairbrush of circle, first hairbrush and the inner tank wall phase
Contact.First hairbrush prevents materials from bonding in fermentation top tank structure, keeps stirring efficiency high, incorporation time is short, material mixture homogeneity
It is high.
Further, the tank body internal upper part is fixed with defoaming disk, and the defoaming pan bottom is provided with multiple defoaming items, institute
State defoaming item matched with the second orifice, and it is described defoaming item diameter less than the second orifice diameter, it is described into
Material mouth and the electromagnetic valve are respectively positioned on the lower section of the defoaming disk.Defoaming item is crushed fermentation materials foam top,
Telescopic rod drives disk to be raised above, and defoaming item passes through the second orifice on disk, make foam at the top of material defoaming disk with
Disk contact is crushed in squeezing, and defoaming effect is good, keeps tunning homogeneity high, and quality is good, and quality is high.
The beneficial effects of the utility model are as follows: (1) by the setting of telescopic rod, disk and second orifice, on telescopic rod
Lower stretch hits disk back and forth in material, and second orifice, which is formed, to be shunted, then is mixed again under the effect of gravity, ferments
Material and fermentation materials can come into full contact with oxygen, be repeated several times, and be uniformly mixed fermentation materials, and make fermentation raw material and oxygen
It is uniformly mixed, stirring efficiency is high, consumes energy low, shortens fermentation time, ferment effect is good, high production efficiency；(2) fermentation needs to add
When hot, the first valve is opened, closes the second valve, water is added to heating tube, closes the first valve, heating tube is begun to warm up, right
Tank body heating opens the second valve, the hot water in heating tube is released and recycled, is constantly infused into heating tube after fermentation
Enter cold water, accelerates the speed that material cools down in fermentor, save the time, high production efficiency；(3) stirring thing above and below disk
Material, when oxygen supply gas branch pipe passes through or is pierced by second orifice, the second hairbrush can brush away the material bonded on the first aperture, prevent from fermenting
Middle the first aperture of feed blocking；(4) first hairbrush prevent materials from bonding in fermentation top tank structure, keep stirring efficiency high, incorporation time
Short, material mixture homogeneity is high；(5) defoaming item is crushed fermentation materials foam top, and telescopic rod drives disk to ramp up
It rises, defoaming item passes through the second orifice on disk, is crushed the foam at the top of material in defoaming disk and disk contact squeeze, disappears
It is good to steep effect, keeps tunning homogeneity high, quality is good, and quality is high.
Detailed description of the invention
Fig. 1 is a kind of structure chart of herein described full-automatic pressure-controlled type novel fermentation equipment；
Fig. 2 is the structure chart of part A enlarged drawing in Fig. 1.
Appended drawing reference: 1- shell, 2- tank body, 3- heating tube, 4- oxygen supervisor, 5- supply oxygen gas tank, and 6- supplies oxygen tracheae, 7-
Blower, 8- oxygen supply gas branch pipe, the first aperture of 9-, 10- telescopic rod, 11- motor, 12- disk, 13- second orifice, first mao of 14-
Brush, the second hairbrush of 15-, 16- defoam disk, and 17- defoams item, 18- water inlet pipe, the first valve of 19-, 20- outlet pipe, the second valve of 21-
Door, 22- feed inlet, 23- electromagnetic valve, 24- discharge port, 25- interlayer, 26- pressure sensor, 27- controller.
Specific embodiment
In order to which those skilled in the art better understand the utility model, with reference to the accompanying drawing with following embodiment to this
Utility model is described in further detail.
Embodiment 1
As shown in Figure 1, a kind of full-automatic pressure-controlled type novel fermentation equipment, including shell 1 and tank body 2, the shell 1 and institute
It states and is provided with interlayer 25 between tank body 2, heating tube 3 is provided in the interlayer 25, bottom is provided with oxygen in the tank body 2
Supervisor 4, the oxygen are responsible on 4 and are vertically provided with multiple oxygen supply gas branch pipes 8, uniformly set on each oxygen supply gas branch pipe 8
Be equipped with multiple first apertures 9, the oxygen supply mechanism connection of the oxygen supervisor 4 and 1 outside of shell, in the tank body 2 in
Between be vertically provided with telescopic rod 10,10 bottom end of telescopic rod is provided with disk 12, and 10 top of telescopic rod extends to described
1 outside of shell, 10 top of telescopic rod is provided with motor 11, multiple second orifices 13 is provided on the disk 12, described
Second orifice 13 is matched with the oxygen supply gas branch pipe 8, and the diameter of the oxygen supply gas branch pipe 8 is less than the second orifice 13
Diameter is provided with feed inlet 22, electromagnetic valve 23 and controller 27 on the shell 1, and the tank body inner sidewall is provided with pressure
Force snesor 26, the electromagnetic valve 23 and the pressure sensor 26 are electrically connected with the controller 27 respectively, the tank
2 bottom of body is provided with discharge port 24.
Working principle: closing discharge port 24, opens feed inlet 22, and the material for needing to ferment and micro- life is added to feed inlet 22
Object strain, that is, fermentation materials closes feed inlet 22, and oxygen mechanism inputs oxygen into oxygen supervisor 4, and oxygen passes through oxygen supply
Enter in the fermentation materials in tank body 2 after gas supervisor 4 from the first aperture 9 on oxygen supply gas branch pipe 8, motor 11 drives telescopic rod 10
Flexible up and down, telescopic rod 10 drives about 12 disk to stir fermentation materials, makes the contact of fermentation materials with oxygen uniform high-efficiency, presses
Force snesor 26 detects pressure in tank body 2 and reaches controller 27, and when pressure is excessive in tank body 2, controller 27 controls electromagnetism
Safety valve 23 is opened, and guarantees safety.By above technical scheme, by the setting of telescopic rod 10, disk 12 and second orifice 13,
About 10 telescopic rod is flexible to hit disk 12 back and forth in material, and second orifice 13, which is formed, to be shunted, then under the effect of gravity again
It mixing, fermentation materials and fermentation materials can come into full contact with oxygen, be repeated several times, and fermentation materials are uniformly mixed, and
Keep fermentation raw material uniform with oxygen mix, stirring efficiency is high, consumes energy low, shortens fermentation time, ferment effect is good, production efficiency
Height solves in the prior art due to stirring unshapeliness, causes oxygen that cannot uniformly and effectively be mixed with material, cause to send out
Ferment overlong time, the low defect of production efficiency.
Embodiment 2
Based on embodiment 1, as shown in Figure 1, the oxygen supply mechanism includes the oxygen supply tracheae being connected to oxygen supervisor 4
6, the oxygen supply gas tank 5 and the blower 7 supplied oxygen in tracheae 6 of oxygen supply 6 end of tracheae.
Start blower 7, supplies oxygen the oxygen in gas tank 5 and pass through oxygen supply tracheae 6 and enter in fermentor, provide needed for fermentation
Oxygen.
Embodiment 3
Based on embodiment 1, as shown in Figure 1, the cyclic annular inclination of the heating tube 3 is wound in interlayer 25, the heating tube 3 one
End is connected to the water inlet pipe 18 outside the shell 1, and the outlet pipe 20 outside 3 other end of heating tube and the shell 1 connects
It is logical, it is provided with the first valve 19 on the water inlet pipe 18, the second valve 21 is provided on the outlet pipe 20.
When fermentation needs to heat, the first valve 19 is opened, closes the second valve 21, water is added to heating tube 3, closes first
Valve 19, heating tube 3 are begun to warm up, and are heated to tank body 2, after fermentation, the second valve 21 are opened, by the heat in heating tube 3
Water is released and is recycled, and constantly injects cold water into heating tube 3, is accelerated the speed that material cools down in fermentor, is saved the time, raw
It produces high-efficient.
Embodiment 4
Based on embodiment 1, as shown in Figure 1, being evenly arranged with multiple second hairbrush 15 on 13 inner wall of the second orifice.
The setting of second hairbrush 15 stirs material in about 12 disk, and oxygen supply gas branch pipe 8 passes through or be pierced by second orifice 13
When, the second hairbrush 15 can brush away the material bonded on the first aperture 9, prevent the first aperture of feed blocking 9 in fermentation.
Embodiment 5
Based on embodiment 1, as shown in Figure 1,12 periphery of the disk is provided with first hairbrush of circle 14, first hairbrush
14 are in contact with 2 inner wall of tank body.
First hairbrush 14 prevents materials from bonding in fermentation top tank structure, keeps stirring efficiency high, and incorporation time is short, and material mixing is equal
Evenness is high.
Embodiment 6
Based on embodiment 1, as shown in Figure 1,2 internal upper part of the tank body is fixed with defoaming disk 16,16 bottom of defoaming disk
Multiple defoaming items 17 are provided with, the defoaming item 17 is matched with the second orifice 13, and the diameter of the defoaming item 17 is small
In the diameter of the second orifice 13, the feed inlet 22 and the electromagnetic valve 23 are respectively positioned under the defoaming disk 16
Side.
Defoaming item 17 is crushed fermentation materials foam top, and telescopic rod 10 drives disk 12 to be raised above, and defoams item
17 pass through the second orifice 13 on disk 12, are crushed the foam at the top of material in defoaming disk 16 and 12 contact squeeze of disk,
Defoaming effect is good, keeps tunning homogeneity high, and quality is good, and quality is high.
The above, the only preferred embodiment of the utility model, are not intended to limit the utility model, the utility model
Scope of patent protection be subject to claims, it is equivalent made by all specifications and accompanying drawing content with the utility model
Structure change similarly should be included in the protection scope of the utility model.
Claims (6)
1. a kind of full-automatic pressure-controlled type novel fermentation equipment, including shell (1) and tank body (2), it is characterised in that: the shell
(1) it is provided with interlayer (25), is provided with heating tube (3) in the interlayer (25), the tank body (2) between the tank body (2)
Interior bottom is provided with oxygen supervisor (4), is vertically provided with multiple oxygen supply gas branch pipes (8) on the oxygen supervisor (4), each
Multiple first apertures (9) are evenly arranged on the oxygen supply gas branch pipe (8), the oxygen supervisor (4) and the shell (1) is outside
The oxygen supply mechanism connection of side, intermediate in the tank body (2) to be vertically provided with telescopic rod (10), telescopic rod (10) the bottom end setting
Have disk (12), telescopic rod (10) top extends on the outside of the shell (1), and telescopic rod (10) top is provided with electricity
Machine (11) is provided with multiple second orifices (13) on the disk (12), the second orifice (13) and the oxygen supply gas branch pipe
(8) it matches, and the diameter of oxygen supply gas branch pipe (8) is less than the diameter of the second orifice (13), sets on the shell (1)
It is equipped with feed inlet (22), electromagnetic valve (23) and controller (27), the tank body inner sidewall is provided with pressure sensor (26),
The electromagnetic valve (23) and the pressure sensor (26) are electrically connected with the controller (27) respectively, the tank body (2)
Bottom is provided with discharge port (24).
2. a kind of full-automatic pressure-controlled type novel fermentation equipment according to claim 1, it is characterised in that: the oxygen supply mechanism
Including the oxygen supply tracheae (6) being connected to oxygen supervisor (4), the oxygen supply gas tank (5) of described oxygen supply tracheae (6) end, with
And the blower (7) in oxygen supply tracheae (6).
3. a kind of full-automatic pressure-controlled type novel fermentation equipment according to claim 1, it is characterised in that: the heating tube
(3) cyclic annular inclination is wound in interlayer (25), and the water inlet pipe (18) of described heating tube (3) one end and the shell (1) outside is even
Logical, heating tube (3) other end outlet pipe (20) external with the shell (1) is connected to, and is arranged on the water inlet pipe (18)
Have the first valve (19), is provided with the second valve (21) on the outlet pipe (20).
4. a kind of full-automatic pressure-controlled type novel fermentation equipment according to claim 1, it is characterised in that: the second orifice
(13) multiple second hairbrush (15) are evenly arranged on inner wall.
5. a kind of full-automatic pressure-controlled type novel fermentation equipment according to claim 1, it is characterised in that: the disk (12)
Periphery is provided with first hairbrush of circle (14), and first hairbrush (14) is in contact with the tank body (2) inner wall.
6. a kind of full-automatic pressure-controlled type novel fermentation equipment according to claim 1, it is characterised in that: the tank body (2)
Internal upper part is fixed with defoaming disk (16), and defoaming disk (16) bottom is provided with multiple defoaming items (17), the defoaming item (17)
It is matched with the second orifice (13), and the diameter of defoaming item (17) is less than the diameter of the second orifice (13), institute
It states feed inlet (22) and the electromagnetic valve (23) is respectively positioned on the lower section of defoaming disk (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820436272.XU CN209039454U (en) | 2018-03-29 | 2018-03-29 | A kind of full-automatic pressure-controlled type novel fermentation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820436272.XU CN209039454U (en) | 2018-03-29 | 2018-03-29 | A kind of full-automatic pressure-controlled type novel fermentation equipment |
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| Publication Number | Publication Date |
|---|---|
| CN209039454U true CN209039454U (en) | 2019-06-28 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820436272.XU Active CN209039454U (en) | 2018-03-29 | 2018-03-29 | A kind of full-automatic pressure-controlled type novel fermentation equipment |
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| CN (1) | CN209039454U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115231970A (en) * | 2022-08-05 | 2022-10-25 | 东营金海岸肥业有限责任公司 | Fermentation equipment and fermentation process for biological fertilizer |
-
2018
- 2018-03-29 CN CN201820436272.XU patent/CN209039454U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115231970A (en) * | 2022-08-05 | 2022-10-25 | 东营金海岸肥业有限责任公司 | Fermentation equipment and fermentation process for biological fertilizer |
| CN115231970B (en) * | 2022-08-05 | 2024-01-23 | 东营金海岸肥业有限责任公司 | Fermentation equipment and fermentation process of biological fertilizer |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211110 Address after: 450000 No. 8302, floor 3, building 1, No. 65, science Avenue, high tech Zone, Zhengzhou City, Henan Province Patentee after: Zhengzhou Shiwei Intelligent Technology Co., Ltd Address before: No. 1501, floor 15, block a, No. 7, Dongqing street, high tech Industrial Development Zone, Zhengzhou, Henan 450001 Patentee before: Zhengzhou yingborui Electronic Technology Co., Ltd |