CN206244780U - A kind of fermentation system - Google Patents
A kind of fermentation system Download PDFInfo
- Publication number
- CN206244780U CN206244780U CN201621345434.6U CN201621345434U CN206244780U CN 206244780 U CN206244780 U CN 206244780U CN 201621345434 U CN201621345434 U CN 201621345434U CN 206244780 U CN206244780 U CN 206244780U
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- China
- Prior art keywords
- reactor
- pipe
- blow
- valve
- discharge nozzle
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Abstract
The utility model discloses a kind of fermentation system, including the first reactor, the second reactor and storage tank, the first reactor, the outside of the second reactor are coated with chuck, and the first reactor, the top of the second reactor are provided with heating tube；First reactor, the bottom of the second reactor are provided with outlet pipe, discharge nozzle and blow-off pipe；Outlet pipe is T-shaped, and two ports connect with the chuck of the first reactor, the second reactor, and another port is condensed water delivery port, and outlet pipe is respectively arranged with valve on the first reactor, one end of the second reactor.Blow-off pipe and the first reactor, the inner space of the second reactor, discharge nozzle is by the inner space of the first reactor, the second reactor and storage tank.The utility model fermentation system, sets reasonable, cost-effective, easy to operate.
Description
Technical field
The utility model is specifically related to a kind of fermentation system.
Background technology
Biotechnological industries quickly grow in recent years, and many biological products such as medicine, health products etc. are commercially produced.It is raw
The fermentation method production process of produce product is a combined process for extremely complex chemical change and physiological change, how will fermentation
The pipeline optimization designs such as system heating, discharging, blowdown are extremely important.
The content of the invention
The purpose of this utility model is to provide a kind of fermentation system, solves fermentation system pipeline in the prior art and sets multiple
Miscellaneous technical problem.
In order to solve the above-mentioned technical problem, the utility model is adopted the following technical scheme that：
A kind of fermentation system, including the first reactor, the second reactor and storage tank, it is first reactor, second anti-
Answer kettle identical, for being fermented to raw material, the first reactor, the outside of the second reactor are coated with chuck, the first reaction
Kettle, the top of the second reactor are provided with heating tube, and the heating tube is T-shaped, with three ports, two of which port difference
Chuck with the first reactor, the second reactor is connected, and another port is the input port of steam, can by the entrance of heating tube
In steam is input into the first reactor, the chuck of the second reactor, and heating tube is near the first reactor, the second reactor
One end on be respectively arranged with valve；Steam can be input to by the first reactor, the second reactor by the entrance of heating tube
Chuck in, reach in the first reactor, the second reactor material heating, insulation purpose, it is ensured that fermentation process normally enters
OK.Thermometer and pressure gauge are provided with first reactor, the second reactor, for measuring the first reactor, second
Temperature and pressure in reactor, and according to measurement situation, the valve in adjustment heating tube, the flow of steam in control heating tube
And pressure.
First reactor, the bottom of the second reactor are provided with outlet pipe, discharge nozzle and blow-off pipe；Wherein outlet pipe
T-shaped, two ports connect with the chuck of the first reactor, the second reactor, and another port is condensed water delivery port, and is gone out
Water pipe is respectively arranged with valve on the first reactor, one end of the second reactor, from water outlet after the steam condensation in chuck
Flowed out in pipe, controlled respectively by setting valve, be easy to operation.
The blow-off pipe and the first reactor, the inner space of the second reactor, sewage, sludge after fermentation are from blow-off pipe
Middle discharge, the delivery port of the outlet pipe is connected with blow-off pipe, and condensed water enters in blow-off pipe through outlet pipe, makes the steaming of chuck
Vapour, condensed water are in flow regime, and steam constantly feeds input, it is ensured that heating effect.
The discharge nozzle by the inner space of the first reactor, the second reactor and storage tank, by discharge nozzle by first
Product after being fermented in reactor, the second reactor is transported in storage tank, and valve is provided with discharge nozzle；On the discharge nozzle
Branch pipe is provided with, branch pipe is connected with blow-off pipe, valve is installed on branch pipe, it is convenient by discharge nozzle during cleaning pipeline after parking
Dirt is discharged.
Further improve, bypass pipe is communicated with the blow-off pipe, set on the corresponding section blow-off pipe in parallel with bypass pipe
There is hand-operated valve, motor-driven valve is provided with bypass pipe, the diameter of bypass pipe is less than blow-off pipe.The normal fermentation stage of reaction, hand-operated valve
Close, the motor-driven valve in bypass is opened, bypass pipe conducting, dirt is discharged through bypass pipe, because the normal fermentation stage of reaction, dirt
Discharge rate is small, so from bypass pipe discharge, the open and close of motor-driven valve can, high degree of automation easy to operate with remote control；When
Cleaning during shutdown reactor, blowdown flow rate is big, then open hand-operated valve, increases delivery flow, improves efficiency.
Further improve, first reactor, the blow-off pipe connection of the second reactor, by the first reactor, second anti-
Discharged after answering sewage, the sludge Correspondent after fermenting in kettle, and side is provided with the first reactor, the blow-off pipe of the second reactor
Siphunculus, shortens blow-off pipe path, cost-effective.
Further improve, the branch pipe is connected by ring flange with discharge nozzle, blow-off pipe passes through ring flange and first respectively
Reactor, the connection of the second reactor, just there is demolition, repair, replacement.
The utility model compared with prior art, has the advantages that：
The utility model fermentation system, sets reasonable, cost-effective, easy to operate.
Brief description of the drawings
Fig. 1 shows the structural representation of fermentation system described in the utility model.
Specific embodiment
To make the purpose of this utility model and technical scheme clearer, below in conjunction with the utility model embodiment to this
The technical scheme of utility model is clearly and completely described.
As shown in figure 1, a kind of fermentation system, including the first reactor 1, the second reactor 1 and storage tank 3, described first
Reactor 1, the second reactor 2 are identical, and for being fermented to raw material, the first reactor 1, the outside of the second reactor 2 are wrapped
Chuck is covered with, the first reactor 1, the top of the second reactor 2 are provided with heating tube 4, and the heating tube is T-shaped, with three
Port, chuck of the two of which port respectively with the first reactor 1, the second reactor 2 is connected, and another port is defeated for steam
Entrance, and heating tube is respectively arranged with valve on the first reactor, one end of the second reactor；By entering for heating tube 4
During steam can be input to the first reactor 1, the chuck of the second reactor 2 by mouth, reach and reacted to the first reactor 1, second
Material heating, the purpose of insulation in kettle 2, it is ensured that fermentation process is normally carried out.On first reactor 1, the second reactor 2
Thermometer and pressure gauge are provided with, for measuring temperature and pressure in the first reactor, the second reactor, and according to measurement feelings
Condition, the valve in adjustment heating tube, the flow and pressure of steam in control heating tube.
First reactor 1, the bottom of the second reactor 2 are provided with outlet pipe 5, discharge nozzle and 6 blow-off pipes 7；Wherein
Outlet pipe 5 is T-shaped, and two ports connect with the chuck of the first reactor 1, the second reactor 2, and another port goes out for condensed water
The mouth of a river, and outlet pipe 5 is respectively arranged with valve on the first reactor 1, one end of the second reactor 2.
The reactor 1 of the blow-off pipe 7 and first, the inner space of the second reactor 2, sewage, sludge after fermentation are from row
Discharged in dirty pipe 7, the delivery port of the outlet pipe 5 is connected with blow-off pipe 7, condensed water enters in blow-off pipe 7 through outlet pipe, makes folder
The steam of set, condensed water are in flow regime, and steam constantly feeds input, it is ensured that heating effect.
The discharge nozzle 6, will by discharge nozzle 6 by the inner space of the first reactor 1, the second reactor 2 and storage tank 3
Product after being fermented in first 1 kettle of reaction, the second reactor 2 is transported in storage tank 3, and valve is provided with discharge nozzle 3；It is described
Discharge nozzle 6 is provided with branch pipe 9, and branch pipe 9 is connected with blow-off pipe 7, and valve is provided with branch pipe 9, after parking, during cleaning pipeline, and side
Just the dirt in discharge nozzle is discharged..
In the present embodiment, bypass pipe 10 is communicated with the blow-off pipe, corresponding section 11 blow-off pipe in parallel with bypass pipe
On be provided with hand-operated valve 14, be provided with motor-driven valve 13 on bypass pipe 10, the diameter of bypass pipe 10 is less than blow-off pipe.Normal fermentation is anti-
Answer the stage, hand-operated valve 14 is closed, the motor-driven valve 13 in bypass is opened, bypass pipe conducting, dirt is discharged through bypass pipe, because normally
Fermentation reaction stage, dirt discharge rate is small, so from bypass pipe discharge, the open and close of motor-driven valve can be with remote control, operation side
Just, high degree of automation；When cleaning during shutdown reactor, blowdown flow rate are big, then hand-operated valve is opened, increase delivery flow, improve efficiency.
In the present embodiment, first reactor 1, the blow-off pipe 7 of the second reactor 2 are connected, by the first reactor 1,
Discharged after sewage, sludge Correspondent after being fermented in second reactor 2, and on the first reactor 1, the blow-off pipe of the second reactor 2
Bypass pipe 10 is provided with, shortens blow-off pipe path, it is cost-effective.
In the present embodiment, the branch pipe 9 is connected by ring flange 8 with discharge nozzle 6, and blow-off pipe 7 passes through ring flange 8 respectively
It is connected with the first reactor 1, the second reactor 2, just there are demolition, repair, replacement.
Do not done in the utility model illustrate be prior art or be capable of achieving by prior art, Er Qieben
It is only preferable case study on implementation of the present utility model that case is embodied described in utility model, not for limiting this practicality
New practical range.The equivalence changes that i.e. all contents according to present utility model application the scope of the claims are made and modification, should all make
It is technology category of the present utility model.
Claims (4)
1. a kind of fermentation system, it is characterised in that including the first reactor, the second reactor and storage tank, first reaction
Kettle, the second reactor are identical, and for being fermented to raw material, the first reactor, the outside of the second reactor are coated with chuck,
First reactor, the top of the second reactor are provided with heating tube, and the heating tube is T-shaped, with three ports, two of which
Chuck of the port respectively with the first reactor, the second reactor is connected, and another port is leaned on for the input port of steam, and heating tube
Valve is respectively arranged with nearly first reactor, one end of the second reactor；
First reactor, the bottom of the second reactor are provided with outlet pipe, discharge nozzle and blow-off pipe；Wherein outlet pipe is in T
Shape, two ports connect with the chuck of the first reactor, the second reactor, and another port is condensed water delivery port, and water outlet
Pipe is respectively arranged with valve on the first reactor, one end of the second reactor；
The blow-off pipe and the first reactor, the inner space of the second reactor, sewage, sludge after fermentation are arranged from blow-off pipe
Go out, the delivery port of the outlet pipe is connected with blow-off pipe；
The discharge nozzle reacts the inner space of the first reactor, the second reactor and storage tank by discharge nozzle by first
Product after being fermented in kettle, the second reactor is transported in storage tank, and valve is provided with discharge nozzle；The discharge nozzle is provided with
Branch pipe, branch pipe is connected with blow-off pipe, and valve is provided with branch pipe.
2. fermentation system according to claim 1, it is characterised in that bypass pipe is communicated with the blow-off pipe, with bypass
Hand-operated valve is provided with pipe corresponding section blow-off pipe in parallel, motor-driven valve is provided with bypass pipe, the diameter of bypass pipe is less than blowdown
Pipe.
3. fermentation system according to claim 2, it is characterised in that first reactor, the blowdown of the second reactor
Pipe is connected, and will be discharged after sewage, sludge Correspondent after being fermented in the first reactor, the second reactor, and the first reactor, second
Bypass pipe is provided with the blow-off pipe of reactor.
4. the fermentation system according to any one of claim 1-3, it is characterised in that the branch pipe is by ring flange and goes out
Expects pipe is connected, and blow-off pipe is connected by ring flange with the first reactor, the second reactor respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621345434.6U CN206244780U (en) | 2016-12-08 | 2016-12-08 | A kind of fermentation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621345434.6U CN206244780U (en) | 2016-12-08 | 2016-12-08 | A kind of fermentation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206244780U true CN206244780U (en) | 2017-06-13 |
Family
ID=59005799
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621345434.6U Expired - Fee Related CN206244780U (en) | 2016-12-08 | 2016-12-08 | A kind of fermentation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206244780U (en) |
-
2016
- 2016-12-08 CN CN201621345434.6U patent/CN206244780U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170613 Termination date: 20201208 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |