CN208485863U - Two-way binder fermenter system - Google Patents
Two-way binder fermenter system Download PDFInfo
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- CN208485863U CN208485863U CN201820758786.7U CN201820758786U CN208485863U CN 208485863 U CN208485863 U CN 208485863U CN 201820758786 U CN201820758786 U CN 201820758786U CN 208485863 U CN208485863 U CN 208485863U
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- fermentation tank
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- 239000011230 binding agent Substances 0.000 title claims abstract description 12
- 238000000855 fermentation Methods 0.000 claims abstract description 67
- 230000004151 fermentation Effects 0.000 claims abstract description 67
- 238000007599 discharging Methods 0.000 claims abstract description 20
- 238000011169 microbiological contamination Methods 0.000 abstract description 3
- 238000010899 nucleation Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002457 bidirectional effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
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Abstract
The utility model discloses a kind of two-way binder fermenter systems, beginning fermentor, several continuous fermentation tanks and end fermentor including successively sequence setting, beginning fermentor is connected with forward feeding pipe, is sequentially connected between beginning fermentor, each continuous fermentation tank and end fermentor by forward direction conveying pipeline；End fermentor is connected with reversed feed pipe, is sequentially connected between end fermentor, each continuous fermentation tank and beginning fermentor by reverse-feeding pipe；The bottom of beginning fermentor, end fermentor and each continuous fermentation tank has been respectively communicated with discharging branch pipe, and discharging branch pipe is communicated with discharge header pipe, is respectively arranged with control valve on forward feeding pipe, positive conveying pipeline, reversed feed pipe, reverse-feeding pipe and discharging branch pipe；It realizes forward and reverse charging, the prior art is substituted and needs batch turning among from seeding tank to other fermentors, reduces power consumption, reduces microbiological contamination chance, realize and continuously ferment and ferment uniformly, improve fermentor utilization rate and fermentation efficiency.
Description
Technical field
The utility model relates to alcoholic fermentation equipment technical field more particularly to a kind of two-way binder fermenter systems.
Background technique
Traditional Alcohol Production uses fermentation method, and the generally existing row's of falling time is long, and fermentation time is short, the energy consumptions such as electric power
Greatly and the discontinuous situation of production is easily caused, with the continuous improvement of production level, there is an urgent need to improve equipment for enterprise's production
Utilization rate, improve fermentation efficiency.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of high utilization rates of equipment and installations, the Bidirectional pressure of high fermentation efficiency
Expect fermenter system.
In order to solve the above technical problems, the technical solution of the utility model is: two-way binder fermenter system, including successively
Beginning fermentor, several continuous fermentation tanks and the end fermentor of sequence setting, the beginning fermentor be connected with it is positive into
Expects pipe, between the beginning fermentor, each continuous fermentation tank and the end fermentor by the positive conveying pipeline according to
Secondary connection；The end fermentor is connected with reversed feed pipe, the end fermentor, each continuous fermentation tank and the beginning
It is sequentially connected between the fermentor of end by the reverse-feeding pipe；The beginning fermentor, the end fermentor and each described
The bottom of continuous fermentation tank has been respectively communicated with discharging branch pipe, and the discharging branch pipe is communicated with discharge header pipe, the forward feeding pipe,
Control valve is respectively arranged on the forward direction conveying pipeline, the reversed feed pipe, the reverse-feeding pipe and the discharging branch pipe.
The beginning fermentor is two as a preferred technical solution, and successively sequence is arranged, and sends out close to the beginning
The continuous fermentation tank of the one of fermentation tank is sequentially connected with the two beginning fermentors by the reverse-feeding pipe；It is described it is positive into
It is separately connected at the top of expects pipe and the two beginning fermentors, the two beginning fermenter bases pass through the positive conveying pipeline respectively
It is connect with the continuous fermentation tank top close to beginning fermentor.
The end fermentor is two as a preferred technical solution, and successively sequence is arranged, and sends out close to the end
The continuous fermentation tank of the one of fermentation tank and the two end fermentors are sequentially connected by the positive conveying pipeline；It is described reversely into
It is separately connected at the top of expects pipe and the two end fermentors, the two end fermenter bases pass through the reverse-feeding pipe respectively
It is connect with the continuous fermentation tank top close to the end fermentor.
The continuous fermentation tank is six as a preferred technical solution,.
The forward feeding pipe, the reversed feed pipe, the positive conveying pipeline, described as a preferred technical solution,
Flow-rate adjustment pump is mounted on reverse-feeding pipe and the discharging branch pipe.
By adopting the above-described technical solution, two-way binder fermenter system, the beginning fermentation including successively sequence setting
Tank, several continuous fermentation tanks and end fermentor, the beginning fermentor are connected with forward feeding pipe, the beginning fermentation
It is sequentially connected between tank, each continuous fermentation tank and the end fermentor by the positive conveying pipeline；The end hair
Fermentation tank is connected with reversed feed pipe, passes through between the end fermentor, each continuous fermentation tank and the beginning fermentor
The reverse-feeding pipe is sequentially connected；The bottom of the beginning fermentor, the end fermentor and each continuous fermentation tank
Be respectively communicated with discharging branch pipe, the discharging branch pipe is communicated with discharge header pipe, the forward feeding pipe, the positive conveying pipeline,
Control valve is respectively arranged on the reversed feed pipe, the reverse-feeding pipe and the discharging branch pipe；The utility model has
Beneficial effect is: since the utility model can be realized simultaneously forward and reverse into material liquid, existing fermentor charging, which is substituted, to be needed
To add relay pump batch turning in centre from seeding tank to other fermentors, reduce power consumption, reduce microbiological contamination chance, realize continuous hair
Ferment and fermentation more evenly, improve the utilization rate of idle fermentor, substantially increase utilization rate of equipment and installations and fermentation efficiency.
Detailed description of the invention
Following drawings are only intended to schematically illustrate and explain the present invention, does not limit the model of the utility model
It encloses.Wherein:
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the partial enlarged view in Fig. 1 at A；
Fig. 3 is the partial enlarged view in Fig. 1 at B；
Fig. 4 is the structural schematic diagram of the utility model beginning fermentor；
Fig. 5 is the structural schematic diagram of the utility model end fermentor；
Fig. 6 is the structural schematic diagram of the utility model continuous fermentation tank；
In figure: the beginning 1- fermentor；2- continuous fermentation tank；The end 3- fermentor；4- forward feeding pipe；5- forward direction conveying
Pipe；The reversed feed pipe of 6-；7- reverse-feeding pipe；8- discharging branch pipe；9- discharge header pipe；10- control valve.
Specific embodiment
With reference to the accompanying drawings and examples, the utility model is further described.In the following detailed description, only pass through
Bright mode describes certain exemplary embodiments of the utility model.Undoubtedly, those skilled in the art can be with
It recognizes, it, can be with a variety of different modes to described without departing from the spirit and scope of the utility model
Embodiment is modified.Therefore, attached drawing and description are regarded as illustrative in nature, rather than the protection for limiting claim
Range.
As shown in Figures 1 to 6, two-way binder fermenter system, the beginning fermentor 1, several including successively sequence setting
Continuous fermentation tank 2 and end fermentor 3, the beginning fermentor 1 are connected with forward feeding pipe 4, the beginning fermentor 1,
It is sequentially connected between each continuous fermentation tank 2 and the end fermentor 3 by the positive conveying pipeline 5；The end hair
Fermentation tank 3 is connected with reversed feed pipe 6, between the end fermentor 3, each continuous fermentation tank 2 and the beginning fermentor 1
It is sequentially connected by the reverse-feeding pipe 7；The beginning fermentor 1, the end fermentor 3 and each continuous fermentation tank
2 bottom has been respectively communicated with discharging branch pipe 8, and the discharging branch pipe 8 is communicated with discharge header pipe 9, the forward feeding pipe 4, described
Control valve is respectively arranged on positive conveying pipeline 5, the reversed feed pipe 6, the reverse-feeding pipe 7 and the discharging branch pipe 8
10；
Since the utility model can be realized simultaneously forward and reverse charging, when forward feeding, feed liquid is sent out from the beginning
The forward feeding pipe 4 charging at 1 top of fermentation tank, after then fermenting in the beginning fermentor 1, from the beginning fermentor
The positive conveying pipeline 5 of 1 bottom is transported to the top of the continuous fermentation tank 2, and feed liquid is fermented in the continuous fermentation tank 2
Afterwards, from the positive conveying pipeline 5 of 2 bottom of continuous fermentation tank be transported to next continuous fermentation tank 2 carry out it is subsequent
Fermentation, fermentation liquid after fermentation are pooled to the discharge header pipe 9 from the discharging branch pipe of each fermenter base
Inside it is collected.The control valve 10 can control the opening and closing of each pipeline, facilitate process adjustments and control, this is practical
It is novel that existing fermentor charging needs centre plus relay pump batch turning from seeding tank to other fermentors is substituted, power consumption is reduced,
Reduce microbiological contamination chance, realize and continuously ferment and ferment more evenly, improves the utilization rate of idle fermentor, substantially increase
Utilization rate of equipment and installations and fermentation efficiency.
The beginning fermentor 1 is two and successively sequence is arranged, close to a continuous hair of the beginning fermentor 1
Fermentation tank 2 is sequentially connected with the two beginning fermentors 1 by the reverse-feeding pipe 7；The forward feeding pipe 4 and two beginnings
It is separately connected at the top of the fermentor 1 of end, two 1 bottoms of beginning fermentor pass through the positive conveying pipeline 5 and close beginning respectively
2 top of the continuous fermentation tank connection of the one of fermentor 1.Two beginning fermentors 1 ferment, then feed liquid respectively from
Forward direction conveying pipeline 5 described in the bottom of two beginning fermentors 1 flows out in the continuous fermentation tank 2, improves fermentation effect
Rate.
The end fermentor 3 is two and successively sequence is arranged, close to a continuous hair of the end fermentor 3
Fermentation tank 2 and the two end fermentors 3 are sequentially connected by the positive conveying pipeline 5；The reversed feed pipe 6 and two ends
It is separately connected at the top of the fermentor 3 of end, two 3 bottoms of end fermentor pass through the reverse-feeding pipe 7 and respectively close to described
2 top of the continuous fermentation tank connection of the one of end fermentor 3.Two end fermentors 3 ferment, then feed liquid point
It is not flowed out in the continuous fermentation tank 2 from forward direction conveying pipeline 5 described in the bottom of two beginning fermentors 1, improves hair
Ferment efficiency.
The beginning fermentor 1 and the end fermentor 3 are also not limited to two.
The continuous fermentation tank 2 is six, also can according to need the quantity for adjusting the continuous fermentation tank 2.
The forward feeding pipe 4, the reversed feed pipe 6, the positive conveying pipeline 5, the reverse-feeding pipe 7 and described
Flow-rate adjustment pump is mounted on discharging branch pipe 8.The flow-rate adjustment pump can effectively adjust the stream of feed liquid inside each pipeline
Speed, preferably control fermentation process, improve working efficiency.
Each beginning fermentor 1, several continuous fermentation tanks 2 and the end fermentor 3, are conventional knot
Structure is fed using bottom discharge top.
The advantages of basic principles and main features and the utility model of the utility model have been shown and described above.Current row
The technical staff of industry is described in above embodiments and description it should be appreciated that the present utility model is not limited to the above embodiments
Only illustrate the principles of the present invention, on the premise of not departing from the spirit and scope of the utility model, the utility model is also
It will have various changes and improvements, these various changes and improvements fall within the scope of the claimed invention.The utility model
Claimed range is defined by the appending claims and its equivalent thereof.
Claims (5)
1. two-way binder fermenter system, beginning fermentor, several continuous fermentation tanks and end including successively sequence setting
Fermentor, it is characterised in that: the beginning fermentor is connected with forward feeding pipe, the beginning fermentor, each continuous hair
It is sequentially connected between fermentation tank and the end fermentor by forward direction conveying pipeline；The end fermentor is connected with reversed charging
Pipe, is sequentially connected between the end fermentor, each continuous fermentation tank and the beginning fermentor by reverse-feeding pipe；
The bottom of the beginning fermentor, the end fermentor and each continuous fermentation tank has been respectively communicated with discharging branch pipe, described
Discharging branch pipe is communicated with discharge header pipe, the forward feeding pipe, the positive conveying pipeline, the reversed feed pipe, described reversed
Control valve is respectively arranged on conveying pipeline and the discharging branch pipe.
2. two-way binder fermenter system as described in claim 1, it is characterised in that: the beginning fermentor be two and according to
Secondary sequence setting passes through described reversed close to a continuous fermentation tank of the beginning fermentor and the two beginning fermentors
Conveying pipeline is sequentially connected；It is separately connected at the top of the forward feeding pipe and the two beginning fermentors, the two beginning fermentors
Bottom passes through the positive conveying pipeline respectively and connect with the continuous fermentation tank top close to beginning fermentor.
3. two-way binder fermenter system as described in claim 1, it is characterised in that: the end fermentor be two and according to
Secondary sequence setting, passes through the forward direction close to a continuous fermentation tank of the end fermentor and the two end fermentors
Conveying pipeline is sequentially connected；It is separately connected at the top of the reversed feed pipe and the two end fermentors, the two end fermentors
Bottom passes through the reverse-feeding pipe respectively and connect with the continuous fermentation tank top close to the end fermentor.
4. two-way binder fermenter system as described in claim 1, it is characterised in that: the continuous fermentation tank is six.
5. two-way binder fermenter system as described in claim 1, it is characterised in that: the forward feeding pipe, described reversed
Flow-rate adjustment pump is mounted on feed pipe, the positive conveying pipeline, the reverse-feeding pipe and the discharging branch pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820758786.7U CN208485863U (en) | 2018-05-21 | 2018-05-21 | Two-way binder fermenter system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820758786.7U CN208485863U (en) | 2018-05-21 | 2018-05-21 | Two-way binder fermenter system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208485863U true CN208485863U (en) | 2019-02-12 |
Family
ID=65253485
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820758786.7U Active CN208485863U (en) | 2018-05-21 | 2018-05-21 | Two-way binder fermenter system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208485863U (en) |
-
2018
- 2018-05-21 CN CN201820758786.7U patent/CN208485863U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240530 Address after: 276599, west of Chengyang Road and south of Zibo Road, Juxian Economic Development Zone, Rizhao City, Shandong Province, passing west of Dingchang Iron Tower Factory Patentee after: Guofu City Investment Co.,Ltd. Country or region after: China Address before: 276500 Shandong Fulaichun Biochemical Co., Ltd., Chengbei Industrial Park, Juxian County, Rizhao City, Shandong Province Patentee before: SHANDONG FULAICHUN BIOCHEMISTRY CO.,LTD. Country or region before: China |