Secondary air supply structure in energy-saving fermentation system tank

By using air-cooled compressed air preparation and airlift units in the fermenter, the high cost problem caused by water cooling was solved, the fermentation speed was accelerated and the dissolved oxygen rate was increased, and the production cost was reduced.

CN223813481UActive Publication Date: 2026-01-20YANCHENG DAMING CHEM MACHINERY
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Patent Information

Application Number
CN202520190373.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-02-07
Publication Date
2026-01-20
Estimated Expiration
2035-02-07

AI Technical Summary

Technical Problem

Existing fermenters use water cooling during the cooling process, which increases water consumption and raises the cost of microbial fermentation.

Method used

Air cooling is used instead of water cooling to prepare compressed air. The compressed air is introduced into the fermentation body through an airlift unit to ensure uniform oxygen distribution. The addition of a ring pipe increases the dissolved oxygen rate. The heated air is reused to dry the fermentation residue, reducing thermal pollution and steam costs.

Benefits of technology

This has resulted in faster fermentation, increased dissolved oxygen levels, reduced circulating water and steam costs, reduced thermal pollution, and lower production costs.

✦ Generated by Eureka AI based on patent content.

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Patent Text Reader

Abstract

The utility model discloses a secondary air supply structure in an energy-saving fermentation system tank, and relates to the technical field of fermentation. The secondary air supply structure in the energy-saving fermentation system tank comprises a fermentation tank, a supporting plate is fixedly installed at the bottom of the fermentation tank, an annular base is fixedly installed at the bottom of the supporting plate, supporting legs are fixedly installed at the bottom of the inner side of the fermentation tank, an annular cylinder is fixedly installed at the tops of the supporting legs, and the annular cylinder is located in the center of the annular base. The airlift unit is arranged on the fermentation tank and the annular base. According to the secondary air supply structure in the energy-saving fermentation system tank, compressed air can be guided into a fermented object, so that oxygen is uniformly dispersed, the fermentation speed is accelerated, oxygen limitation is prevented, the technology of preparing compressed air through air cooling instead of water cooling is adopted, the circulating water amount is saved, and the energy consumption is reduced. And the heated air is used as effective heat energy for secondary utilization to dry mushroom dregs generated by fermentation, so that the heat pollution is reduced, and the steam cost is saved.
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Description

TECHNICAL FIELD

[0001] The utility model relates to fermentation technical field, especially relate to a kind of secondary air supply structure in energy-saving fermentation system tank. BACKGROUND

[0002] The fermentation tank is an industrial equipment for microbial fermentation, which is mainly composed of a cylindrical body made of stainless steel plate, with a volume usually between 1 cubic meter and several hundred cubic meters. The fermentation tank plays a core role in industrial production, by controlling temperature, pH value and oxygen supply conditions, to provide ideal growth environment for microorganisms, so as to promote the efficient production of target products.

[0003] However, the existing fermentation tank in the process of cooling, through water cooling to reduce the temperature inside the fermentation tank, increase the water consumption, improve the cost of microbial fermentation. UTILITY MODEL CONTENT

[0004] The utility model aims at providing a kind of secondary air supply structure in energy-saving fermentation system tank to solve the problems and defects proposed in the above background technology.

[0005] To achieve the above object, the utility model provides the following technical scheme: a kind of secondary air supply structure in energy-saving fermentation system tank, including fermentation tank, the bottom of fermentation tank is fixedly installed with support plate, the bottom of support plate is fixedly installed with annular base, the inner bottom of fermentation tank is fixedly installed with support leg, the top of support leg is fixedly installed with annular cylinder, annular cylinder is located at the center of annular base, further including the gas lift unit being set on fermentation tank, annular base, the top of gas lift unit is provided with hot gas pipe, by gas lift unit, for accelerating the fermentation speed of fermentation material inside fermentation tank, liquid level transparent tube is fixedly installed in the front side of fermentation tank, by liquid level transparent tube, for observing the liquid level inside fermentation tank.

[0006] Preferably, the air-lifting unit comprises a compressor, a tee pipe, a first annular pipe, a second annular pipe, air nozzles, and a pressure relief pipe, the compressor is fixedly installed on the top outer wall of the fermentation tank, the main end of the tee pipe is fixedly installed on the output end of the compressor, the two branch ends of the tee pipe respectively penetrate one side of the fermentation tank and one side of the annular cylinder and extend to the inside of the annular cylinder, the first annular pipe is fixedly connected to one branch end of the tee pipe, the second annular pipe is fixedly connected to the other branch end of the tee pipe, the air nozzles are divided into two groups, and the two groups of air nozzles are fixedly installed on the top of the first annular pipe and the top of the second annular pipe, respectively, and the pressure relief pipe is fixedly installed on the top of the fermentation tank, so that the compressed air can be introduced into the inside of the fermentation object, the oxygen is uniformly dispersed, the fermentation speed is accelerated, and oxygen limitation is prevented, the air-cooling is adopted to replace the water-cooling to prepare the compressed air, the circulating water amount is saved, the heated air is used as effective heat energy for secondary utilization, the fungus residue generated in the fermentation is dried, heat pollution is reduced, steam cost is saved, the first annular pipe is arranged in the upper part of the annular base, the air is brought back to the air nozzles by the circulating liquid in the fermentation tank, and then the air is mixed with the fermentation liquid to be sprayed upward, so that the oxygen dissolution rate of the fermentation liquid and the air utilization rate are improved, and the production cost is further reduced.

[0007] Preferably, the surface of the liquid level transparent pipe is provided with a liquid level scale.

[0008] Preferably, the bottom of the annular base is movably provided with casters, and the support plates and the casters are both arranged in a ring array and have four.

[0009] Preferably, the side of the fermentation tank is fixedly provided with a feeding pipe, and the bottom of the fermentation tank is fixedly provided with a discharging pipe.

[0010] Preferably, the feeding pipe is provided with a valve A, and the discharging pipe is provided with a valve B.

[0011] Preferably, the hot air pipe is fixedly connected to the heat dissipation end of the compressor.

[0012] Compared with the prior art, the energy-saving fermentation system tank secondary air supply structure has the following beneficial effects:

[0013] The energy-saving fermentation system tank secondary air supply structure can introduce the compressed air into the inside of the fermentation object through the air-lifting unit, so that the oxygen is uniformly dispersed, the fermentation speed is accelerated, and oxygen limitation is prevented, the air-cooling is adopted to replace the water-cooling to prepare the compressed air, the circulating water amount is saved, the heated air is used as effective heat energy for secondary utilization, the fungus residue generated in the fermentation is dried, heat pollution is reduced, and steam cost is saved.

[0014] And in the annular base upper part increases the first annular pipe, air is taken back to the air nozzle by circulating liquid in the fermenter, and then mixes with the fermentation liquid to spray upward, which improves the oxygen dissolution rate of the fermentation liquid and the air utilization rate, and further reduces the production cost. BRIEF DESCRIPTION OF DRAWINGS

[0015] The utility model is further explained below by combining with the drawings and examples:

[0016] Figure 1 It is the structure schematic view of the utility model;

[0017] Figure 2 It is another side structure schematic view of the utility model Figure 1 ;

[0018] Figure 3 It is the sectional view of the utility model fermenter;

[0019] Figure 4 It is another side structure schematic view of the utility model Figure 3 .

[0020] Reference signs: 1, fermenter; 2, annular base; 3, support plate; 4, caster; 5, support leg; 6, annular cylinder; 7, compressor; 8, tee pipe; 9, first annular pipe; 10, second annular pipe; 11, air nozzle; 12, pressure relief pipe; 13, hot gas pipe; 14, feed pipe; 15, discharge pipe; 16, liquid level transparent pipe. DETAILED DESCRIPTION

[0021] This part will describe the specific embodiments of the utility model in detail, and the preferred embodiments of the utility model are shown in the drawings, and the drawings are used to supplement the description of the text part in the form of graphics, so that people can intuitively and visually understand each technical feature and the overall technical scheme of the utility model, but it cannot be understood as the limitation of the protection scope of the utility model.

[0022] Please refer to Figures 1-4 , the utility model provides a kind of technical scheme: a kind of energy-saving fermentation system tank secondary air structure, including fermenter 1, the bottom of fermenter 1 is fixedly installed with support plate 3, the bottom of support plate 3 is fixedly installed with annular base 2, the bottom of the inboard of fermenter 1 is fixedly installed with support leg 5, the top of support leg 5 is fixedly installed with annular cylinder 6, annular cylinder 6 is located at the center of annular base 2, further including setting on fermenter 1, annular base 2 gas lift unit, the top of gas lift unit is provided with hot gas pipe 13, for accelerating the fermentation speed of fermenter 1 internal fermentation material by gas lift unit, liquid level transparent pipe 16 fixedly installed in the front side of fermenter 1, for observing the liquid level in fermenter 1 by liquid level transparent pipe 16.

[0023] Further, the air lifting unit comprises a compressor 7, a tee pipe 8, a first annular pipe 9, a second annular pipe 10, air nozzles 11, a pressure relief pipe 12, the compressor 7 is fixedly installed on the top outer wall of the fermentation tank 1, the main end of the tee pipe 8 is fixedly installed on the output end of the compressor 7, the two branch ends of the tee pipe 8 respectively penetrate one side of the fermentation tank 1 and one side of the annular cylinder 6 and extend to the inside of the annular cylinder 6, the first annular pipe 9 is fixedly connected to one branch end of the tee pipe 8, the second annular pipe 10 is fixedly connected to the other branch end of the tee pipe 8, the air nozzles 11 are divided into two groups, and the two groups of air nozzles 11 are fixedly installed on the top of the first annular pipe 9 and the top of the second annular pipe 10 respectively, and the pressure relief pipe 12 is fixedly installed on the top of the fermentation tank 1 and can guide the compressed air into the inside of the fermentation object, so that the oxygen is dispersed more uniformly, thereby accelerating the fermentation speed and preventing the occurrence of oxygen limitation, and the air cooling is adopted to replace the water cooling to prepare the compressed air technology, which not only saves the circulating water amount, but also secondarily utilizes the heated air as effective heat energy to dry the fermentation residue, thereby reducing the heat pollution and saving the steam cost, and the first annular pipe 9 is additionally arranged in the upper part of the annular base 2, the air is brought back to the air nozzle by the circulating liquid in the fermentation tank, and then mixed with the fermentation liquid to be sprayed upward, so that the oxygen dissolution rate of the fermentation liquid and the air utilization rate are improved, and the production cost is further reduced.

[0024] Further, the surface of the liquid level transparent pipe 16 is provided with a liquid level scale.

[0025] Further, the bottom of the annular base 2 is movably provided with casters 4, and the support plates 3 and the casters 4 are both four and arranged in an annular array.

[0026] Further, one side of the fermentation tank 1 is fixedly provided with a feeding pipe 14, and the bottom of the fermentation tank 1 is fixedly provided with a discharging pipe 15.

[0027] Further, the feeding pipe 14 is provided with a valve A, and the discharging pipe 15 is provided with a valve B.

[0028] Further, the hot gas pipe 13 is fixedly connected to the heat dissipation end of the compressor 7.

[0029] Working principle: mainly relies on the high-speed air sprayed by the air nozzles 11, the air is dispersed in the liquid in the form of bubbles, on the aeration side, the average density of the liquid will decrease, and on the non-aeration side, the density of the liquid is larger, so as to form a density difference, and then a liquid circulation is generated in the fermentation tank, specifically, the air is sprayed into the fermentation liquid through the nozzle or the jet hole, the formed gas-liquid mixture has a reduced density and moves upward, and the fermentation liquid with a smaller gas content sinks, thereby forming a circulating flow, so as to realize mixing and oxygen dissolution mass transfer.

[0030] High efficiency and energy saving: through the optimization of gas flow and liquid circulation design, the oxygen transfer rate and fermentation efficiency are improved, thereby reducing the energy consumption. Meanwhile, the Venturi tube injection stirring action can replace the traditional stirring motor, further saving the energy.

[0031] Convenient operation: by adjusting the flow and pressure of compressed air, the fermentation operation of different fermentation materials can be realized.

[0032] Uniform air dispersion: the system introduces compressed air into the inside of the fermentation object, so that the oxygen is dispersed more uniformly, thereby accelerating the fermentation speed and preventing the occurrence of oxygen limitation and other problems.

[0033] The above embodiment of the utility model is described in detail in combination with the drawings, but the utility model is not limited to the above embodiment, and various changes can be made within the knowledge range possessed by those skilled in the art in the technical field without departing from the purpose of the utility model.

Claims

1. An energy-saving fermentation system tank secondary air supply structure, comprising a fermentation tank (1), a support plate (3) is fixedly installed at the bottom of the fermentation tank (1), an annular base (2) is fixedly installed at the bottom of the support plate (3), a support leg (5) is fixedly installed at the inner bottom of the fermentation tank (1), an annular cylinder (6) is fixedly installed at the top of the support leg (5), and the annular cylinder (6) is located at the center of the annular base (2), characterized in that, Also include: The gas lift unit is arranged on the fermentation tank (1), the annular base (2), the top of the gas lift unit is provided with hot gas pipe (13), through the gas lift unit, for accelerating the fermentation speed of the fermentation material in the fermentation tank (1); The liquid level transparent tube (16) is fixedly installed on the front side of the fermentation tank (1), and the liquid level transparent tube (16) is used for observing the liquid level in the fermentation tank (1).

2. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 1, characterized in that: The gas lift unit includes compressor (7), tee pipe (8), first annular pipe (9), second annular pipe (10), air nozzle (11), pressure relief pipe (12), compressor (7) is fixedly installed on the top outer wall of fermentation tank (1), the main end of tee pipe (8) is fixedly installed on the output end of compressor (7), two branch ends of tee pipe (8) respectively penetrate one side of fermentation tank (1), one side of annular cylinder (6) and extend to the inside of annular cylinder (6), first annular pipe (9) is fixedly connected with one branch end of tee pipe (8), second annular pipe (10) is fixedly connected with the other branch end of tee pipe (8), air nozzle (11) has eight and is divided into two groups, two groups of air nozzle (11) are fixedly installed on the top of first annular pipe (9) and the top of second annular pipe (10), pressure relief pipe (12) is fixedly installed on the top of fermentation tank (1).

3. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 2, characterized in that: The surface of the liquid level transparent tube (16) is provided with liquid level scale line.

4. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 3, characterized in that: The bottom of the annular base (2) is movably installed with the casters (4), the supporting plate (3) and the casters (4) are all four and are arranged in annular array.

5. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 4, characterized in that: One side of the fermentation tank (1) is fixedly installed with the feeding pipe (14), and the bottom of the fermentation tank (1) is fixedly installed with the discharge pipe (15).

6. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 5, characterized in that: The feeding pipe (14) is provided with valve A, and the discharge pipe (15) is provided with valve B.

7. The secondary air supply structure in the tank of the energy-saving fermentation system according to claim 6, characterized in that: The hot gas pipe (13) is fixedly connected with the heat dissipation end of the compressor (7).