CN218900251U - Pipeline connecting mechanism between ultrahigh temperature sterilizer and degassing tank - Google Patents
Pipeline connecting mechanism between ultrahigh temperature sterilizer and degassing tank Download PDFInfo
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- CN218900251U CN218900251U CN202222777885.9U CN202222777885U CN218900251U CN 218900251 U CN218900251 U CN 218900251U CN 202222777885 U CN202222777885 U CN 202222777885U CN 218900251 U CN218900251 U CN 218900251U
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- degassing tank
- pipe
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- high temperature
- sterilizer
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Abstract
The utility model discloses a pipeline connecting mechanism between an ultra-high temperature sterilizer and a degassing tank, which comprises the following components: the output pipe of the sterilizer is connected with the feed pipe of the degassing tank, the discharge pipe of the degassing tank is connected with the return pipe of the sterilizer, a T-shaped single seat valve, a first control valve and a flow regulating valve are sequentially arranged on the feed pipe of the degassing tank, and a liquid discharge valve, a second control valve and a discharge pump of the degassing tank are sequentially arranged on the discharge pipe of the degassing tank; the other valve port of the T-shaped single seat valve is connected to a degassing tank discharging pipe, and in the opening state of the T-shaped single seat valve, a sterilizer output pipe on the ultra-high temperature sterilizer is communicated with the degassing tank discharging pipe through the T-shaped single seat valve, and in the closing state of the T-shaped single seat valve, the sterilizer output pipe on the ultra-high temperature sterilizer is disconnected with the degassing tank discharging pipe. The utility model has the advantages that: the consumption of materials required by the jacking water in the pipeline is greatly reduced, so that the cost is effectively saved, and meanwhile, the required production preparation time is effectively shortened, so that the production efficiency is effectively improved.
Description
Technical Field
The utility model relates to the technical field of ultra-high temperature sterilization equipment, in particular to a pipeline connecting mechanism between an ultra-high temperature sterilizer and a degassing tank.
Background
Ultra high temperature sterilization equipment is commonly referred to as ultra high temperature sterilizer (UHT), which also includes a degassing tank when degassing of the material is required. Before filling production, the ultra-high temperature sterilization equipment needs to perform in-situ Sterilization (SIP), and then water is used for replacing materials to circulate and wait for production, and the sterile state is always maintained. When receiving production instructions, water in ultra-high temperature sterilizer (UHT) equipment needs to be discharged after being replaced by materials and returned to UHT by means of material top water. Because of the existence of the degassing tank, the water in the degassing tank needs a large amount of materials to replace after the SIP passes through the degassing tank, which not only results in long replacement time, but also results in large material loss.
Disclosure of Invention
The technical problems to be solved by the utility model are as follows: the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank can reduce the loss in the material water ejection process and can rapidly finish the material water ejection.
In order to solve the problems, the utility model adopts the following technical scheme: a pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank, comprising: the device comprises a sterilizer output pipe and a sterilizer return pipe which are arranged on an ultra-high temperature sterilizer, a degasser tank feeding pipe and a degasser tank discharging pipe which are arranged on a degasser tank, wherein the sterilizer output pipe is connected with the degasser tank feeding pipe; the other valve port of the T-shaped single seat valve on the degassing tank feeding pipe is connected to a degassing tank discharging pipe between the second control valve and the discharging pump, and in the opening state of the T-shaped single seat valve, a sterilizer output pipe on the ultra-high temperature sterilizer is communicated with the degassing tank discharging pipe through the T-shaped single seat valve, and in the closing state of the T-shaped single seat valve, the sterilizer output pipe on the ultra-high temperature sterilizer is disconnected with the degassing tank discharging pipe.
Further, the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank is characterized in that the degassing tank is provided with an electronic liquid level meter.
Further, the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank is characterized in that a one-way valve for preventing the material from moving from the ultra-high temperature sterilizer to the degassing tank is arranged at the output end of the discharging pipe of the degassing tank.
Further, the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank is characterized in that a spray header is arranged in the degassing tank, and a feed pipe of the degassing tank is communicated with the spray header in the degassing tank.
Further, the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank is characterized in that the first control valve and the second control valve are pneumatic butterfly valves.
Further, the pipeline connecting mechanism between the ultra-high temperature sterilizer and the degassing tank is characterized in that the discharging pipe of the degassing tank is connected to the bottom of the degassing tank.
The utility model has the advantages that: the device has the advantages of simple structure, ingenious structure, greatly reduced consumption of materials required by the material ejection water in the pipeline, thereby effectively saving cost, and effectively shortening the required production preparation time, thereby effectively improving production efficiency. In addition, the setting of flow control valve to and with first control valve, the cooperation of second control valve, can effectively avoid the ultra-temperature sterilization machine to lead to by a wide margin temperature fluctuation because of flow fluctuation by a wide margin, thereby effectively avoid the sterility in the ultra-temperature sterilization machine to be destroyed, further effectively practiced thrift manufacturing cost, effectively ensure product quality.
Drawings
Fig. 1 is a schematic structural view of a pipe connection mechanism between an ultra-high temperature sterilizer and a degassing tank according to the present utility model.
Detailed Description
The utility model will be described in further detail with reference to the drawings and the preferred embodiments.
As shown in fig. 1, the pipeline connection mechanism between the ultra-high temperature sterilizer and the degassing tank comprises: a sterilizer output pipe 11 and a sterilizer return pipe 12 which are arranged on the ultra-high temperature sterilizer 1, a deaeration tank feeding pipe 21 and a deaeration tank discharging pipe 22 which are arranged on the deaeration tank 2. The degassing tank 2 is internally provided with a spray header 23, and the degassing tank feeding pipe 21 is communicated with the spray header 23 in the degassing tank 2. To facilitate monitoring of the liquid level in the degassing tank 2, an electronic level gauge 24 is provided on the degassing tank 2. In order to facilitate the removal of the liquid from the degassing tank 2, the degassing tank discharge pipe 22 is connected to the bottom of the degassing tank 2. The sterilizer output pipe 11 is connected with a degasser feed pipe 21, and a degasser discharge pipe 22 is connected with a sterilizer return pipe 12.
In this embodiment, a T-type single seat valve 211, a first control valve 212, and a flow rate regulating valve 213 are provided in this order on the feed pipe 21 of the degassing tank in the flow direction of the liquid from the ultra-high temperature sterilizer 1 to the degassing tank 2. The degassing tank discharging pipe 22 is provided with a degassing tank discharging valve 221, a second control valve 222 and a discharging pump 223 in sequence along the flowing direction of the liquid from the degassing tank 2 to the ultra-high temperature sterilizer 1, and the output end of the degassing tank discharging pipe 22 is provided with a one-way valve 224 for preventing the material from moving from the ultra-high temperature sterilizer 1 to the degassing tank 1 in the embodiment. For ease of control, the first control valve 212 and the second control valve 222 are each pneumatic butterfly valves in this embodiment.
The other valve port of the T-shaped single seat valve 211 on the degassing tank feeding pipe 21 is connected to a degassing tank discharging pipe 22 between the second control valve 222 and the discharging pump 223, and when the T-shaped single seat valve 211 is in an open state, a sterilizer output pipe 11 on the ultra-high temperature sterilizer 1 is communicated with the degassing tank discharging pipe 22 through the T-shaped single seat valve 211; in the closed state of the T-shaped single seat valve 211, the sterilizer output pipe 11 on the ultra-high temperature sterilizer 1 is disconnected from the degassing tank discharge pipe 22.
The working principle is as follows: after the ultra-high temperature sterilization equipment completes in-situ Sterilization (SIP), a sterile water circulation state is carried out. The aseptic water circulation process is as follows: the T-shaped single seat valve 211 is opened and the first control valve 212 and the second control valve 222 are closed. Sterile water is output from the sterilizer output pipe 11 of the ultra-high temperature sterilizer 1, enters the degassing tank discharge pipe 22 through the T-shaped single seat valve 211, then flows back into the ultra-high temperature sterilizer 1 through the sterilizer return pipe 12 after passing through the discharge pump 223 and the one-way valve 224, and the process is continuously circulated for production.
When preparing for feed production, the top water is first fed and the degassing tank 8 is emptied, in particular as follows: the T-shaped single seat valve 211 is still in an open state, the first control valve 212 and the second control valve 222 are still in a closed state, materials are output from the sterilizer output pipe 11 of the ultra-high temperature sterilizer 1, after a period of time, the materials reach the T-shaped single seat valve 211, then enter the degassing tank discharging pipe 22 through the T-shaped single seat valve 211, then flow back into the ultra-high temperature sterilizer 1 from the sterilizer return pipe 12 through the discharging pump 223 and the one-way valve 224, and the ultra-high temperature sterilizer 1 discharges unqualified materials until the materials discharged by the ultra-high temperature sterilizer 1 are detected to be qualified. In the process, the water in the pipeline is pushed back to the high-temperature sterilizer 1 to be discharged, so that the material water ejection is completed. In addition, the evacuation in the degassing tank 2 is performed by simply opening the degassing tank drain valve 221, and when the liquid level detected by the electronic liquid level meter 24 is 0, it is indicated that the degassing tank 2 is completely evacuated, and the degassing tank drain valve 221 is closed.
After the material components discharged by the ultra-high temperature sterilizer 1 are qualified, namely the pipeline material water ejection is finished, and the discharge of the degassing tank 2 is finished, at the same time, the T-shaped single seat valve 211 is still in an open state, the first control valve 212 and the second control valve 222 are still in a closed state, and the flow regulating valve 213 is also in a closed state. Then the first control valve 212 is opened, the flow regulating valve 213 is opened, the opening is gradually increased, and after the materials are output from the sterilizer output pipe 11 of the ultra-high temperature sterilizer 1, a small part of the materials enter the degassing tank 2 through the T-shaped single seat valve 211, the first control valve 212, the flow regulating valve 213 and the spray header 23, and a large part of the materials still flow back into the ultra-high temperature sterilizer 1 from the sterilizer return pipe 12 through the T-shaped single seat valve 211, the degassing tank discharge pipe 22, the discharge pump 223 and the one-way valve 224. The aim of ensuring a small portion of the material split is to: the material temperature is prevented from being changed excessively due to the overlarge change of the flow of the material backflow, so that the temperature fluctuation of the ultrahigh temperature sterilizer is avoided greatly due to the large flow fluctuation, and the sterility in the ultrahigh temperature sterilizer is effectively prevented from being destroyed.
When the liquid level detected by the electronic liquid level meter 24 reaches a set value, the second control valve 222 is opened, after a period of time, the opening of the flow regulating valve 213 reaches the set opening value, the T-shaped single seat valve 211 is closed, so that the material is output from the sterilizer output pipe 11 of the ultra-high temperature sterilizer 1, sequentially enters the degassing tank 2 through the T-shaped single seat valve 211, the first control valve 212, the flow regulating valve 213 and the spray header 23, and then flows into the degassing tank 2 through the degassing tank discharging pipe 22, sequentially flows into the ultra-high temperature sterilizer 1 through the second control valve 222, the discharging pump 223 and the one-way valve 224, and then flows back into the ultra-high temperature sterilizer 1 through the sterilizer return pipe 12, and reaches a feeding state after the material circulates for a period of time.
The utility model has the advantages that: the device has the advantages of simple structure, ingenious structure, greatly reduced consumption of materials required by the material ejection water in the pipeline, thereby effectively saving cost, and effectively shortening the required production preparation time, thereby effectively improving production efficiency. In addition, the setting of the flow regulating valve 213 and the cooperation with the first control valve 212 and the second control valve 222 can effectively avoid the ultra-high temperature sterilizer from causing great temperature fluctuation due to great flow fluctuation, thereby effectively avoiding the destruction of the sterility in the ultra-high temperature sterilizer, further effectively saving the production cost and effectively ensuring the product quality.
Claims (6)
1. A pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank, comprising: the sterilizing machine output pipe and the sterilizing machine reflux pipe arranged on the ultra-high temperature sterilizing machine are connected with the degassing tank feed pipe and the degassing tank discharge pipe arranged on the degassing tank, and the degassing tank discharge pipe is connected with the sterilizing machine reflux pipe, and is characterized in that: a T-shaped single seat valve, a first control valve and a flow regulating valve are sequentially arranged on a feed pipe of the degassing tank along the flow direction of the liquid from the ultra-high temperature sterilizer to the degassing tank, and a degassing tank drain valve, a second control valve and a discharge pump are sequentially arranged on a discharge pipe of the degassing tank along the flow direction of the liquid from the degassing tank to the ultra-high temperature sterilizer; the other valve port of the T-shaped single seat valve on the degassing tank feeding pipe is connected to a degassing tank discharging pipe between the second control valve and the discharging pump, and in the opening state of the T-shaped single seat valve, a sterilizer output pipe on the ultra-high temperature sterilizer is communicated with the degassing tank discharging pipe through the T-shaped single seat valve, and in the closing state of the T-shaped single seat valve, the sterilizer output pipe on the ultra-high temperature sterilizer is disconnected with the degassing tank discharging pipe.
2. The line connection between an ultra-high temperature sterilizer and a degasser tank according to claim 1, wherein: an electronic liquid level meter is arranged on the degassing tank.
3. The pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank according to claim 1 or 2, wherein: the output end of the degassing tank discharging pipe is provided with a one-way valve for preventing the material from moving from the ultra-high temperature sterilizer to the degassing tank.
4. The pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank according to claim 1 or 2, wherein: the degassing tank is internally provided with a spray header, and the feed pipe of the degassing tank is communicated with the spray header in the degassing tank.
5. The pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank according to claim 1 or 2, wherein: the first control valve and the second control valve are pneumatic butterfly valves.
6. The pipeline connection mechanism between an ultra-high temperature sterilizer and a degassing tank according to claim 1 or 2, wherein: the discharging pipe of the degassing tank is connected to the bottom of the degassing tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222777885.9U CN218900251U (en) | 2022-10-21 | 2022-10-21 | Pipeline connecting mechanism between ultrahigh temperature sterilizer and degassing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222777885.9U CN218900251U (en) | 2022-10-21 | 2022-10-21 | Pipeline connecting mechanism between ultrahigh temperature sterilizer and degassing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218900251U true CN218900251U (en) | 2023-04-25 |
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ID=86049290
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222777885.9U Active CN218900251U (en) | 2022-10-21 | 2022-10-21 | Pipeline connecting mechanism between ultrahigh temperature sterilizer and degassing tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218900251U (en) |
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2022
- 2022-10-21 CN CN202222777885.9U patent/CN218900251U/en active Active
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