CN208485863U - Two-way binder fermenter system - Google Patents

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

Two-way binder fermenter system

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.