CN217997184U - Fermentation ingredient adding system of pharmaceutical equipment - Google Patents
Fermentation ingredient adding system of pharmaceutical equipment Download PDFInfo
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- CN217997184U CN217997184U CN202222282274.7U CN202222282274U CN217997184U CN 217997184 U CN217997184 U CN 217997184U CN 202222282274 U CN202222282274 U CN 202222282274U CN 217997184 U CN217997184 U CN 217997184U
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Abstract
The utility model relates to a pharmaceutical equipment's fermentation batching addition system relates to the technical field of fermentation batching, and it includes metering tank, the inside feed supplement house steward of both ends intercommunication metering tank, sets up circulating pump and the feed supplement branch pipe of one end intercommunication feed supplement house steward on the feed supplement house steward, and the position that feed supplement branch pipe and feed supplement house steward communicate is located between metering tank and the circulating pump export, and the feed supplement branch pipe other end intercommunication fermentation cylinder, the last intercommunication of feed supplement house steward has the first steam pipe that is located between the feed supplement branch pipe and the circulating pump export, the feed supplement house steward still communicates has first drain pipe, and first drain pipe is located the feed supplement house steward end of circulating pump export one side. This application has the waste of material when reducing the fermentation cylinder feed supplement, improves the effect of feed supplement efficiency.
Description
Technical Field
The application relates to the technical field of fermentation ingredients, in particular to a fermentation ingredient adding system of pharmaceutical equipment.
Background
The fermentation tank in the pharmaceutical equipment is widely applied to the industries of dairy products, beverages, bioengineering, pharmacy, fine chemical engineering and the like, various thalli are cultured and fermented in the fermentation tank, and various products are obtained by utilizing the thalli to carry out microbial fermentation.
When fermentation is carried out in the fermentation tank, a large amount of nutrient substances are consumed, and materials need to be supplemented in time. The conventional fermentation tank feeding mode is that the feeding tank is connected with a main pipe, and the main pipe is divided into a plurality of branch pipes which are respectively introduced into each fermentation tank for feeding.
To the correlation technique among the above-mentioned, the inventor finds that, stopping to being responsible for the feed after the feed supplement is accomplished, can remain more material in the pipeline, and the material is retained and to have the possibility of rotting more than a period of time, so can only discharge the material of reserving in the pipeline earlier when next feed supplement, again to being responsible for the feed, complex operation and extravagant material.
SUMMERY OF THE UTILITY MODEL
In order to reduce the waste of material, improve feed supplement efficiency, this application provides a pharmaceutical equipment's fermentation batching addition system.
The application provides a pharmacy equipment's fermentation batching addition system adopts following technical scheme:
the utility model provides a pharmaceutical equipment's fermentation batching addition system, includes metering tank, both ends intercommunication metering tank inside feed supplement house steward, sets up circulating pump and the feed supplement branch pipe of one end intercommunication feed supplement house steward on feed supplement house steward, and the position that feed supplement branch pipe and feed supplement house steward communicate is located between metering tank and the circulating pump export, and the feed supplement branch pipe other end communicates the fermentation cylinder.
By adopting the technical scheme, materials pumped by the circulating pump flow in the material circulation of the metering tank, the feeding main pipe, the circulating pump, the feeding main pipe and the metering tank, and the feeding main pipe supplies materials to the communicated feeding branch pipes. The material can make the rotten speed of material slow down in the system mesocycle, and the circulation pipeline does not have the dead angle simultaneously, does not reserve the material, reduces the waste of material. The material supplementing branch pipe directly receives materials from material circulation, and the material supplementing of the fermentation tank is more convenient.
Optionally, the feed supplementing header pipe is communicated with a first steam pipe located between the feed supplementing branch pipes and the outlet of the circulating pump, and is further communicated with a first drain pipe located at the tail end of the feed supplementing header pipe on one side of the outlet of the circulating pump.
By adopting the technical scheme, when the pipeline needs to be emptied, steam can be introduced into the feeding main pipe through the first steam pipe, and the steam can push materials in the feeding main pipe to be discharged from the first liquid discharge pipe, so that the material retention in the feeding main pipe is effectively reduced; high-temperature steam can disinfect the pipeline flowing through, and is convenient and efficient.
Optionally, one end of the feeding branch pipe, which is far away from the feeding main pipe, is communicated with a second steam pipe.
Through adopting above-mentioned technical scheme, when the feed supplement branch pipe need be emptied, can let in steam in the feed supplement branch pipe through the second steam pipe, steam promotes the material in the feed supplement branch pipe and gets into the feed supplement house steward, and the first drain outlet of rethread is discharged.
Optionally, one end of the feed supplementing branch pipe close to the distribution main pipe is communicated with a second liquid discharge pipe.
By adopting the technical scheme, when only the feeding branch pipe is exhausted, the material in the feeding branch pipe can be pushed to be discharged from the second liquid discharge pipe through the steam of the second steam pipe without passing through the feeding main pipe.
Optionally, the feeding branch pipe is connected with a flow meter and a regulating valve.
Through adopting above-mentioned technical scheme, flowmeter and the governing valve cooperation on the feed supplement branch pipe are used, can carry out accurate feed supplement to the fermentation cylinder, reduce the material extravagant.
Optionally, a detection branch pipe is communicated with the outlet of the circulating pump on the feeding main pipe, and a pressure gauge is connected to the detection branch pipe.
Through adopting above-mentioned technical scheme, the manometer is used for detecting the pressure size in the feed supplement main pipe, detects the setting of branch pipe, can avoid the manometer to receive the impact of the interior material of feed supplement main pipe for a long time, increases manometer life, reduces the maintenance to the manometer.
Optionally, a drain pipe is communicated with a position of the feed supplementing main pipe, which is positioned at the outlet of the circulating pump.
Through adopting above-mentioned technical scheme, the evacuation pipe can be with the metering tank evacuation, also evacuation circulating pump and the preceding partly feed supplement house steward of circulating pump simultaneously.
Optionally, a filter is disposed on the feeding main pipe between the metering tank and the inlet of the circulating pump.
Through adopting above-mentioned technical scheme, can reduce debris behind the material in the measurement jar passing through the filter, make the material in the whole batching addition system purer.
In summary, the present application includes at least one of the following beneficial technical effects:
1. the circulating pump pumps materials to flow in the circulation of the metering tank, the feeding main pipe, the circulating pump, the feeding main pipe and the metering tank, and meanwhile, the feeding main pipe supplies materials to the communicated feeding branch pipes. The material is circulated in the system, so that the deterioration speed of the material is reduced, no dead angle exists in a circulating pipeline, the material is not left, and the waste of the material is reduced;
2. when the pipeline needs to be emptied, steam can be introduced into the feeding main pipe through the first steam pipe, and the steam can push materials in the feeding main pipe to be discharged from the first liquid discharge pipe, so that material retention in the feeding main pipe is effectively reduced;
3. the high-temperature steam can disinfect the pipeline flowing through, so that the steam is convenient and efficient;
4. the flowmeter and the regulating valve on the feed supplement branch pipe are matched for use, so that the fermentation tank can be supplemented accurately, and the material waste is reduced.
Drawings
FIG. 1 is an overall schematic view of the ingredient addition system of the present application;
in the figure, 1, a metering tank; 2. a main feeding pipe; 21. a first steam pipe; 22. a first drain pipe; 23. emptying the pipe; 3. a circulation pump; 4. a branch pipe for feeding; 41. a second steam pipe; 42. a second drain pipe; 43. a flow meter; 44. adjusting a valve; 5. detecting a branch pipe; 6. a pressure gauge; 7. a filter; 8. and (4) fermenting the mixture.
Detailed Description
The present application is described in further detail below with reference to fig. 1.
The application provides a fermentation batching addition system of pharmaceutical equipment, refers to figure 1, including metering tank 1, feed supplement house steward 2, circulating pump 3, feed supplement branch pipe 4, detection branch pipe 5 and filter 7.
Metering tank 1 is used for storing and supplying with the material, both ends about feed supplement house steward 2 intercommunication metering tank 1, and circulating pump 3 sets up on feed supplement house steward 2, is equipped with filter 7 between the export of circulating pump 3 and metering tank 1. The circulating pump 3 provides power, materials enter the feeding main pipe 2 from the outlet at the lower end of the metering tank 1, flow through the filter 7 to be filtered and then enter the circulating pump 3, the materials are pumped back to the metering tank 1 through the circulating pump 3, and the material circulation of the metering tank 1-the feeding main pipe 2-the filter 7-the circulating pump 3-the feeding main pipe 2-the metering tank 1 is continuously carried out. The feed branch 4 receives feed from the feed circulation and feeds the fermenter 8.
The materials circularly flow in the circulating line, so that the materials are not easy to deteriorate; the material supplementing branch pipes 4 directly receive materials from the material circulation line, so that the material supplementing process is more efficient and convenient.
Circulating pump 3 is the diaphragm pump in this application embodiment, and during the diaphragm pump sending liquid, the liquid material does not have the shear flow, and the material throughput performance is good. The position of the feed supplement header pipe 2 at the outlet of the circulating pump 3 is communicated with one end of the detection branch pipe 5, the other end of the detection branch pipe 5 is connected with a pressure gauge 6, and a valve is arranged on the detection branch pipe 5 between the feed supplement header pipe 2 and the pressure gauge 6.
Manometer 6 is used for detecting the material and follows the pressure of interior material of circuit, detects the valve on branch pipe 5 and opens when manometer 6 needs use, closes when manometer 6 need not use, can avoid manometer 6 to receive the impact of material in the feed supplement house steward 2 for a long time and damage.
The position of the feed supplementing header pipe 2 corresponding to one end of the outlet of the circulating pump 3 is communicated with an emptying pipe 23, the emptying pipe 23 is used when the metering tank 1 needs to be emptied, and materials in the metering tank 1 are discharged through the emptying pipe 23.
The feeding main pipe 2 between the detection branch pipe 5 and the emptying pipe 23 is communicated with a first steam pipe 21, one end of the feeding main pipe 2 returning to the metering tank 1 is communicated with a first drainage pipe 22, a valve is arranged on the first steam pipe 21 to control the flow and the communication state of steam in the first steam pipe 21, and a valve is also arranged on the first drainage pipe 22.
The first steam pipe 21 is used for feeding steam into the feeding main pipe 2, and the first drain pipe 22 is used for discharging the material in the feeding main pipe 2. Steam is introduced into the feeding main pipe 2, and the feeding main pipe 2 can also be sterilized.
One end of the branch feeding pipe 4 is communicated with the main feeding pipe 2, the communication position is positioned between the first steam pipe 21 and the first drainage pipe 22, and the other end of the branch feeding pipe 4 is communicated with the fermentation tank 8 needing feeding. The feeding branch pipes 4 can be provided with a plurality of groups, and in the embodiment of the application, the feeding branch pipes 4 are provided with four groups.
The direction of following towards fermentation cylinder 8 on the feed supplement branch pipe 4 is connected with governing valve 44 and flowmeter 43 in proper order, and flowmeter 43 detects the flow in the feed supplement branch pipe 4, and governing valve 44 carries out flow control to the material in the feed supplement branch pipe 4, and the accurate feed is carried out fermentation cylinder 8 to work efficiency height.
A second steam pipe 41 is communicated with the feeding branch pipe 4 between the flowmeter 43 and the fermentation tank 8, a valve is arranged on the second steam pipe 41, and a second liquid discharge pipe 42 is communicated with the feeding branch pipe 4 between the regulating valve 44 and the feeding main pipe 2.
The second steam pipe 41 is used for introducing steam into the branch feeding pipe 4, and the second liquid discharging pipe 42 is used for discharging the material in the branch feeding pipe 4. Steam is introduced into the branch feeding pipe 4, and the branch feeding pipe 4 can also be disinfected.
The feeding main pipe 2 between the emptying pipe 23 and the first liquid discharging pipe 22 is also communicated with a feeding pipe which is used for feeding other equipment or devices needing materials.
The implementation principle of the embodiment of the application is as follows: the material in the metering tank 1 is circulated in the feeding main pipe 2 by the circulating pump 3, the feeding branch pipes 4 receive the material from the feeding main pipe 2, and the material enters the fermentation tank 8 after the flow is regulated by the regulating valve 44 to complete feeding.
When the feeding main pipe 2 needs to be emptied, a valve on the first steam pipe 21 and a valve on the first drainage pipe 22 are opened, steam is filled into the feeding main pipe 2 through the first steam pipe 21, the steam pushes the materials out of the first drainage pipe 22, and meanwhile the steam also sterilizes the passing pipelines.
When the branch feeding pipe 4 and the main feeding pipe 2 need to be exhausted, the valve on the second steam pipe 41 is opened, the valve on the second liquid discharge pipe 42 is kept closed, the steam can push the materials in the branch feeding pipe 4 into the main feeding pipe 2 to be discharged through the first liquid discharge port, and meanwhile, the steam sterilizes the interior of the pipeline; when only the branch feeding pipe 4 needs to be exhausted, the communication between the branch feeding pipe 4 and the main feeding pipe 2 is cut off, the second steam pipe 41 and the second liquid discharge pipe 42 are opened, steam enters the branch feeding pipe 4 from the second steam pipe 41, the material is pushed to be discharged from the second liquid discharge pipe 42, and meanwhile, the steam sterilizes the interior of the pipeline.
The embodiments of the present invention are preferred embodiments of the present application, and the protection scope of the present application is not limited thereby, wherein like parts are denoted by like reference numerals. Therefore, the method comprises the following steps: all equivalent changes made according to the structure, shape and principle of the present application shall be covered by the protection scope of the present application.
Claims (8)
1. The utility model provides a pharmaceutical equipment's fermentation batching addition system, a serial communication port, including metering tank (1), both ends intercommunication metering tank (1) inside feed supplement house steward (2), set up circulating pump (3) and feed supplement branch pipe (4) of one end intercommunication feed supplement house steward (2) on feed supplement house steward (2), the position that feed supplement branch pipe (4) and feed supplement house steward (2) communicate is located between metering tank (1) and circulating pump (3) export, feed supplement branch pipe (4) other end intercommunication fermentation cylinder (8).
2. Fermentation ingredient adding system of pharmaceutical equipment according to claim 1, characterized in that the feeding main (2) is connected with a first steam pipe (21) between the feeding branch pipe (4) and the outlet of the circulating pump (3), the feeding main (2) is further connected with a first drain pipe (22), and the first drain pipe (22) is located at the end of the feeding main (2) on the outlet side of the circulating pump (3).
3. The fermentation ingredient adding system of the pharmaceutical equipment is characterized in that one end of the feeding branch pipe (4) far away from the feeding main pipe (2) is communicated with a second steam pipe (41).
4. The fermentation ingredient adding system of the pharmaceutical equipment as claimed in claim 3, wherein the feeding branch pipe (4) is connected with a second liquid discharge pipe (42) at one end close to the feeding main pipe (2).
5. The fermentation ingredient adding system of the pharmaceutical equipment according to claim 1, characterized in that a flow meter (43) and a regulating valve (44) are connected to the feeding branch pipe (4).
6. The fermentation ingredient adding system of the pharmaceutical equipment as claimed in claim 1, wherein the feeding main pipe (2) is connected with a detection branch pipe (5) at the outlet of the circulating pump (3), and the detection branch pipe (5) is connected with a pressure gauge (6).
7. The fermentation ingredient adding system of the pharmaceutical equipment as claimed in claim 1, wherein the feeding main pipe (2) is connected with a drain pipe (23) at the outlet of the circulating pump (3).
8. Fermentation ingredient adding system of pharmaceutical equipment according to claim 1, characterized in that a filter (7) is arranged on the feeding main (2) between the metering tank (1) and the inlet of the circulation pump (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222282274.7U CN217997184U (en) | 2022-08-26 | 2022-08-26 | Fermentation ingredient adding system of pharmaceutical equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222282274.7U CN217997184U (en) | 2022-08-26 | 2022-08-26 | Fermentation ingredient adding system of pharmaceutical equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217997184U true CN217997184U (en) | 2022-12-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222282274.7U Active CN217997184U (en) | 2022-08-26 | 2022-08-26 | Fermentation ingredient adding system of pharmaceutical equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217997184U (en) |
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2022
- 2022-08-26 CN CN202222282274.7U patent/CN217997184U/en active Active
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