CN209885600U - Aseptic carbonating device for carbonated beverage - Google Patents
Aseptic carbonating device for carbonated beverage Download PDFInfo
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- CN209885600U CN209885600U CN201920130718.0U CN201920130718U CN209885600U CN 209885600 U CN209885600 U CN 209885600U CN 201920130718 U CN201920130718 U CN 201920130718U CN 209885600 U CN209885600 U CN 209885600U
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Abstract
The utility model discloses an aseptic carbonator of carbonated beverage, include: aseptic tank and material conveying pipe, the bottom of aseptic tank is provided with acidizing material output tube, material conveying pipe's input is linked together with the discharging pipe of ultra-high temperature instantaneous sterilization machine, still including the carbon dioxide pipeline that is provided with a plurality of bacteria filter, carbon dioxide pipe connection has reserve pressure conveyer pipe and mixed conveyer pipe, reserve pressure conveyer pipe connection is to aseptic tank, be provided with on the reserve pressure conveyer pipe and reserve pressure pipeline control valve, material conveying pipe and mixed conveyer pipe's output all are linked together with the input of blender, be provided with mixed transport control valve on the mixed conveyer pipe, the output and the aseptic tank of blender are linked together. The utility model has the advantages that: firstly, carbon dioxide is sterilized and filtered by an aseptic filter and then mixed with feed liquid, so that the carbon dioxide can be effectively prevented from escaping from the feed liquid, the requirement on the pressure bearing capacity of an aseptic tank can be reduced, the production steps are simplified, and the production cost is effectively reduced.
Description
Technical Field
The utility model relates to a carbonated beverage filling production facility technical field, concretely relates to aseptic acidizing device of carbonated beverage.
Background
Carbonated beverages refer to those beverages in which carbon dioxide is dissolved in a material. The current carbonic acid beverage is prepared by the following steps: after dissolving carbon dioxide in the material, sterilizing. Such disadvantages are: after the material is heated, the carbon dioxide overflows from the liquid material easily, and for preventing the carbon dioxide from overflowing, great pressure just needs to be exerted to the temperature is higher, and pressure is higher, and this not only requires equipment to have higher bearing capacity, has still increased and has carried out the step that steps down to the material, need will be in the material of higher pressure state dissolved with carbon dioxide step down to lower pressure state during the filling promptly. Therefore, the existing carbonated beverage has complex preparation process and high preparation cost.
SUMMERY OF THE UTILITY MODEL
The utility model discloses the technical problem that needs to solve is: provides a carbonated beverage sterile carbonator which can effectively prevent carbon dioxide from escaping from materials and greatly reduce the pressure-bearing requirement on equipment.
In order to solve the above problem, the utility model adopts the following technical scheme: a carbonated beverage aseptic carbonation apparatus comprising: aseptic tank and material conveying pipe, the bottom of aseptic tank is provided with acidizing material output tube, material conveying pipe's input is linked together with the discharging pipe of ultra-high temperature instantaneous sterilization machine, still including the carbon dioxide pipeline that is linked together with the carbon dioxide air supply, be provided with a plurality of bacteria filter on the carbon dioxide pipeline, carbon dioxide pipe connection has reserve pressure conveyer pipe and mixed conveyer pipe, reserve pressure conveyer pipe connection to aseptic tank, be provided with reserve pressure pipeline control valve on the reserve pressure conveyer pipe, the output of material conveyer pipe and mixed conveyer pipe all is linked together with the input of blender, be provided with mixed transport control valve on the mixed conveyer pipe, the output and the aseptic tank of blender are linked together.
Further, in the above-mentioned aseptic carbonator for carbonated beverages, the mixing delivery pipe is further provided with a first aseptic regulating valve and a first flow meter.
Further, in the above sterile carbonation device for carbonated beverages, the pressure-reducing valve and the sterile air inlet regulating valve are further arranged on the pressure-preparing delivery pipe of the sterile tank, the top of the sterile tank is connected with the exhaust pipe, and the exhaust pipe is provided with the pressure sensor, the safety valve and the sterile exhaust regulating valve.
Further, in the aseptic carbonator for carbonated beverages, the material conveying pipe is provided with a cooler, an aseptic pump and a material flow meter, and the material entering the material conveying pipe from the ultrahigh-temperature instant sterilizer enters the cooler to be cooled and then enters the mixer.
Further, the aseptic carbonator for carbonated beverage, wherein the ultra-high temperature instant sterilizer is connected to the material conveying pipe through an aseptic technique cross anti-mixing valve, and the aseptic technique cross anti-mixing valve comprises: the valve comprises a valve seat, wherein a first interface, a second interface, a third interface, a fourth interface, a fifth interface and a sixth interface are arranged on the valve seat, a valve cavity, a first valve core, a second valve core and a third valve core are arranged in the valve seat, the second interface and the third interface are normally communicated, the fifth interface and the sixth interface are normally communicated, the first valve core can control the first interface to be communicated with or disconnected from the valve cavity under the control of the second valve core, the second interface and the third interface can be communicated with or disconnected from the valve cavity, and the fifth interface and the sixth interface can be communicated with or disconnected from the valve cavity; the third valve core can drive the fourth interface to be communicated with or disconnected from the valve cavity; the first interface is connected with the shielding steam conveying pipe, the second interface is connected with the cleaning pipeline, a cleaning control valve is arranged on the cleaning pipeline, the cleaning pipeline is used for conveying cleaning solution and sterilizing steam, and the third interface is connected with the material conveying pipe; the fourth interface is connected with a drain pipe, and a drain valve is arranged on the drain pipe; the fifth interface is connected with a discharge pipe of the ultra-high temperature instantaneous sterilization machine, and the sixth interface is connected with a liquid return pipe of the ultra-high temperature instantaneous sterilization machine.
Further, in the above-mentioned aseptic carbonator for carbonated beverages, the mixer is a venturi tube mixer.
Furthermore, in the above aseptic carbonator for carbonated beverages, a cleaning ball with a plurality of nozzles is disposed at the top of the aseptic tank, the mixer is communicated with the aseptic tank through a feeding pipe, an aseptic feeding regulating valve is disposed on the feeding pipe, an aseptic tank cleaning pipeline is connected to the feeding pipe between the output end of the mixer and the aseptic feeding regulating valve, the aseptic tank cleaning pipeline is connected to the cleaning ball, and an aseptic tank cleaning control valve is disposed on the aseptic tank cleaning pipeline.
Still further, in the aseptic carbonator for carbonated beverages, at least two sterilizing filters are connected in series on the carbon dioxide pipeline, and a filter drain pipe with a valve is connected to each filter.
Further, the above-mentioned aseptic carbonator for carbonated beverages, wherein the input end of the carbon dioxide pipe is provided with a first check valve, and the output end of the mixing delivery pipe is provided with a second check valve.
The utility model has the advantages that: firstly, carbon dioxide is sterilized and filtered by an aseptic filter and then mixed with feed liquid, so that the carbon dioxide can be effectively prevented from escaping from the feed liquid, the requirement on the pressure bearing capacity of an aseptic tank can be reduced, the production steps are simplified, and the production cost is effectively reduced. Secondly, the ultrahigh-temperature instantaneous sterilizer is connected with the material conveying pipe through a cross anti-mixing valve in an aseptic process, and washing liquid, sterilizing steam and shielding steam are connected into the whole acidification device, wherein the washing liquid and the sterilizing steam can wash and sterilize pipelines of the acidification device and all parts on the pipelines, so that the acidification device is clean and aseptic; when the ultrahigh-temperature instantaneous sterilizer interrupts feeding, the shielding steam is isolated between the ultrahigh-temperature instantaneous sterilizer and the sterile tank, so that the sterility of the acidification device can be further ensured.
Drawings
Fig. 1 is a schematic structural diagram of the carbonated beverage aseptic carbonator according to the present invention.
Detailed Description
The invention will be described in further detail with reference to the drawings and preferred embodiments.
As shown in fig. 1, a carbonated beverage aseptic carbonator, comprising: the sterile tank 1, the material conveying pipe 2 and a carbon dioxide pipeline 4 communicated with a carbon dioxide gas source. The input end of the material conveying pipe 2 is communicated with a discharge pipe 31 of the ultrahigh-temperature instant sterilizer 3. The carbon dioxide pipeline 4 is provided with a plurality of sterilizing filters 41, the carbon dioxide pipeline 4 is at least provided with two sterilizing filters 41 in series, and the carbon dioxide pipeline 4 is provided with two sterilizing filters 41 in series in this embodiment. The sterilizing filter 41 functions to: the carbon dioxide gas is sterilized and filtered. The input end of the carbon dioxide pipe 4 is provided with a first check valve 42, and the first check valve 42 is arranged to effectively prevent the fluid in the carbon dioxide pipe 4 from flowing out of the input end of the carbon dioxide pipe 4.
The carbon dioxide line 4 is connected to a pressure preparation duct 5 and a mixing duct 6. The pressure-prepared delivery pipe 5 is connected to the aseptic tank 1, and the pressure-prepared delivery pipe 5 is provided with a pressure-prepared pipeline control valve 51, and the pressure-prepared pipeline control valve 51 in the embodiment adopts a manual ball valve. In this embodiment, the pressure-preparation delivery pipe 5 is further provided with a pressure-reducing valve 52 and an aseptic air intake regulating valve 53. The top of the sterile tank 1 is also connected with an exhaust pipe 12, and the exhaust pipe 12 is provided with a pressure sensor 121, a safety valve 122 and a sterile exhaust regulating valve 123.
The output ends of the material conveying pipe 2 and the mixing conveying pipe 6 are both communicated with the input end of the mixer. In this embodiment, the mixer is a venturi mixer 7. The material conveying pipe 2 is provided with a cooler 21, a sterile pump 22 and a material flow meter 23, and the material liquid entering the material conveying pipe 2 from the ultrahigh-temperature instantaneous sterilization machine 3 firstly enters the cooler 21 to be cooled and then enters the Venturi tube mixer 7. The cooler 21 cools the feed liquid, and also has a purpose of preventing carbon dioxide from overflowing. The mixing and conveying pipe 6 is provided with a mixing and conveying control valve 61, the mixing and conveying control valve 61 is a diaphragm valve, and in the embodiment, in order to adjust and meter the flow rate of the gas in the mixing and conveying pipe 6, the mixing and conveying pipe 6 is further provided with a first aseptic adjusting valve 62 and a first flow meter 63. The output end of the mixing duct 6 is provided with a second non-return valve 64. The output end of the venturi mixer 7 is communicated with the sterile tank 1 through a feeding pipe 11, and the feeding pipe 11 is provided with a sterile feeding regulating valve 110. The top in aseptic tank 1 is provided with the cleaning ball 13 of taking a plurality of nozzles, is connected with aseptic tank cleaning pipeline 111 on the inlet pipe 11 between venturi blender 7 output and aseptic feeding governing valve 110, and aseptic tank cleaning pipeline 111 is connected to cleaning ball 13, is provided with aseptic tank cleaning control valve 112 on the aseptic tank cleaning pipeline 111, and aseptic tank cleaning control valve 112 adopts the diaphragm valve.
In this embodiment, be connected through aseptic technology cross anti-mixing valve 8 between superhigh temperature instantaneous sterilization machine 3 and the material conveying pipe 2, aseptic technology cross anti-mixing valve 8's structure includes: the valve seat 80 is provided with a first port 81, a second port 82, a third port 83, a fourth port 84, a fifth port 85, and a sixth port 86. The valve seat 80 is provided with a valve cavity, a first valve core, a second valve core and a third valve core, the second interface 82 and the third interface 83 are normally communicated, and the fifth interface 85 and the sixth interface 86 are normally communicated. The first valve core can control the first interface 81 to be communicated with or disconnected from the valve cavity, the second interface 82 and the third interface 83 can be communicated with or disconnected from the valve cavity, and the fifth interface 85 and the sixth interface 86 can be communicated with or disconnected from the valve cavity. The third spool action can actuate the fourth port 84 into and out of communication with the valve chamber. The first interface 81 is connected with the shielding steam delivery pipe 91, the second interface 82 is connected with the cleaning pipeline 92, a cleaning control valve 921 is arranged on the cleaning pipeline 92, the cleaning control valve 921 adopts a diaphragm valve, and the cleaning pipeline 92 is used for delivering cleaning solution and sterilizing steam. The third port 83 is connected to the input end of the material conveying pipe 2. The fourth port 84 is connected to a drain pipe 93, and a drain valve 931 is provided in the drain pipe 93. The fifth port 85 is connected with the discharge pipe 31 of the ultra-high temperature instantaneous sterilizer 3, and the sixth port 86 is connected with the liquid return pipe 32 of the ultra-high temperature instantaneous sterilizer 3.
The wash liquor Cleaning (CIP) procedure was as follows: the cleaning control valve 921 is opened, the fifth port 85 and the sixth port 86 of the aseptic technique cross anti-mixing valve 8 are both in a state of being disconnected from the valve cavity, and the second port 82 and the third port 83 are intermittently communicated with the valve cavity.
The cleaning solution enters the material conveying pipe 2 from the cleaning pipeline 92 through the second interface 82 and the third interface 83, and the cleaning solution sequentially enters the aseptic tank 1 through the cooler 21, the aseptic pump 22, the material flow meter 23, the venturi tube mixer 7, the feeding pipe 11 and the aseptic feed adjusting valve 110, so that the cleaning of the material conveying pipe 2 and the components on the material conveying pipe 2, namely the material conveying pipe 2 and the subcooler 21, the aseptic pump 22, the material flow meter 23 and the venturi tube mixer 7 thereon, and the cleaning of the feeding pipe 11 and the components on the feeding pipe 11, namely the aseptic feed adjusting valve 110 are realized.
Meanwhile, the cleaning solution enters the cleaning ball 13 through the aseptic tank cleaning line 111, and is sprayed out from the nozzle of the cleaning ball 13, thereby performing spray cleaning on the aseptic tank 1. The washing liquid in the aseptic tank 1 is discharged from an acidified material output pipe 101 at the bottom of the aseptic tank 1. During CIP cleaning, the opening of the aseptic feed regulating valve 110 ensures that most of the cleaning solution can enter the aseptic tank cleaning pipeline 111, thereby ensuring the cleaning effect of the cleaning solution on the aseptic tank 1.
Meanwhile, the second interface 82 and the third interface 83 are intermittently communicated with the valve cavity, so that a part of washing liquid enters the valve cavity, and the valve cavity is cleaned. The third valve core is actuated to connect the fourth port 84 to the valve chamber, and the drain valve 931 on the drain pipe 93 is opened, so that the washing liquid in the valve chamber is drained through the drain pipe 93.
The steam Sterilization (SIP) process is as follows: the cleaning control valve 921 is opened, the fifth port 85 and the sixth port 86 of the aseptic technique cross anti-mix valve 8 are both in a state of being disconnected from the valve cavity, and the second port 82 and the third port 83 are also in a state of being disconnected from the valve cavity.
The sterilizing steam enters the material conveying pipe 2 through the second interface 82 and the third interface 83, and then sequentially enters the sterile tank 1 through the cooler 21, the sterile pump 22, the material flow meter 23, the venturi tube mixer 7, the feeding pipe 11 and the sterile feeding regulating valve 110, so that the sterilization of the material conveying pipe 2, all parts on the material conveying pipe 2 and the interior of the sterile tank 1 is realized.
The sterilizing steam in the aseptic tank 1 passes through the pressure-preparing delivery pipe 5, sequentially passes through the sterile air inlet adjusting valve 53, the pressure reducing valve 52 and the pressure-preparing pipeline control valve 51, and then enters the carbon dioxide pipeline 4 from the pressure-preparing delivery pipe 5, so that the two sterilizing filters 41 in the carbon dioxide pipeline 4 are sterilized at high temperature, and the water vapor generated after sterilization in the sterilizing filters 41 is discharged from the filter drain pipe 411 of the sterilizing filters 41.
The carbon dioxide acidification process is as follows.
The carbon dioxide in the carbon dioxide pipeline 4 is sterilized and filtered by two sterilizing filters 41 in sequence to become sterile and clean carbon dioxide.
First, the pressure preparation line control valve 51 and the aseptic air intake regulating valve 53 of the pressure preparation delivery pipe 5 are opened, and the sterile and clean carbon dioxide enters the aseptic tank 1 through the pressure preparation line control valve 51, the pressure reducing valve 52 and the aseptic air intake regulating valve 53 of the pressure preparation delivery pipe 5. When the pressure sensor 121 detects that the pressure inside the aseptic tank 1 reaches the design production pressure value, the aseptic air intake adjustment valve 53 is closed.
Then, the mixing and feeding control valve 61 and the first aseptic regulating valve 62 are opened, and the sterile and clean carbon dioxide enters the input end of the venturi mixer 7 from the mixing and feeding pipe 6 through the first flow meter 63, the first aseptic regulating valve 62 and the second check valve 64. At this time, the fifth port 85 and the sixth port 86 of the aseptic process cross anti-mixing valve 8 are in a state of being communicated with the valve cavity, the second port 82 and the third port 83 are in a state of being communicated with the valve cavity, and the cleaning control valve 921 is in a closed state. The sterilized feed liquid in the ultra-high temperature instantaneous sterilizer 3 enters the material conveying pipe 2 through the discharge pipe 31, the fifth interface 85 of the aseptic technique cross anti-mixing valve 8, the valve cavity of the aseptic technique cross anti-mixing valve 8 and the third interface 83 of the aseptic technique cross anti-mixing valve 8, and the feed liquid continuously enters the input end of the venturi tube mixer 7 under the action of the aseptic pump 22. The aseptic pump 22 pressurizes the feed liquid, thereby improving the mixing effect of the carbon dioxide and the feed liquid.
The carbon dioxide entering the venturi tube mixer 7 is dissolved with the feed liquid, and the feed liquid dissolved with the carbon dioxide enters the sterile tank 1 from the output end of the mixer 7 through the feed pipe 11. Carbon dioxide is dissolved in the feed liquid after being filtered and sterilized, so that the advantages are as follows: can effectively prevent carbon dioxide from escaping from the feed liquid, and can reduce the requirement on the pressure bearing capacity of the sterile tank, thereby having energy efficiency and reducing the production cost.
The liquid level in the aseptic tank 1 rises, and the pressure in the aseptic tank 1 will be constantly grow, and in case pressure sensor 121 detects when the pressure in the aseptic tank 1 is greater than the design value of production pressure, aseptic air discharge regulating valve 123 on exhaust pipe 12 will then open, and the gas in the aseptic tank 1 will then be discharged through exhaust pipe 12 to ensure that the pressure value in the aseptic tank 1 maintains the design value of production pressure all the time. On the contrary, when the feed liquid dissolved with carbon dioxide in the aseptic tank 1 is output from the acidified material output pipe 101, the liquid level in the aseptic tank 1 is reduced, the pressure in the aseptic tank 1 is continuously reduced, once the pressure sensor 121 detects that the pressure in the aseptic tank 1 is smaller than the design value of the production pressure, the aseptic air inlet adjusting valve 53 is opened, and the aseptic clean carbon dioxide is supplemented into the aseptic tank 1, so as to ensure that the pressure in the aseptic tank 1 is always maintained at the design value of the production pressure. The aseptic tank 1 adopts the pressure adjusting mode, so that the production pressure design value is always kept in the aseptic tank 1, the storage time of the feed liquid dissolved with carbon dioxide can be greatly prolonged, the carbon dioxide in the feed liquid is effectively prevented from escaping, and the acidification quality of the feed liquid is further improved.
When the ultrahigh-temperature instantaneous sterilizer 3 interrupts feeding, the fifth interface 85 and the sixth interface 86 of the aseptic technique cross anti-mixing valve 8 are in a state of being disconnected from the valve cavity, and the second interface 82 and the third interface 83 are in a state of being disconnected from the valve cavity, at the moment, the first interface 81 is communicated with the valve cavity, and the shielding steam conveying pipe 91 conveys the shielding steam into the valve cavity, so that the ultrahigh-temperature instantaneous sterilizer 3 is isolated from the aseptic tank 1. After the fourth port 84 is connected to the valve chamber, the water condensed from the shield steam in the valve chamber can be discharged through the drain pipe 93 of the fourth port 84.
The utility model has the advantages that: firstly, carbon dioxide is sterilized and filtered by the sterile filter 41 and then mixed with the feed liquid, so that the carbon dioxide can be effectively prevented from escaping from the feed liquid, the requirement on the pressure bearing capacity of the sterile tank can be reduced, the production steps are simplified, and the production cost is effectively reduced. Secondly, the ultrahigh-temperature instantaneous sterilizer 3 is connected with the material conveying pipe 2 through a cross anti-mixing valve 8 in an aseptic process, and washing liquid, sterilizing steam and shielding steam are connected into the whole acidification device, wherein the washing liquid and the sterilizing steam can wash and sterilize pipelines of the acidification device and parts on the pipelines, so that the acidification device is clean and aseptic; when the feeding of the ultra-high temperature instantaneous sterilizer 3 is interrupted, the shielding steam is cut off between the ultra-high temperature instantaneous sterilizer 3 and the aseptic tank 1, so that the asepsis of the acidification device can be further ensured.
Claims (9)
1. A carbonated beverage aseptic carbonation apparatus comprising: aseptic jar and material conveying pipe, the bottom of aseptic jar is provided with acidizing material output tube, and the input of material conveying pipe is linked together its characterized in that with the discharging pipe of ultra-high temperature instantaneous sterilization machine: still including the carbon dioxide pipeline that is linked together with the carbon dioxide air supply, be provided with a plurality of sterilization filters on the carbon dioxide pipeline, carbon dioxide pipe connection has and is equipped with pressure conveyer pipe and mixed conveyer pipe, is equipped with and presses duct connections to aseptic tank, is provided with on the pressure conveyer pipe and is equipped with and presses the pipeline control valve, and the output of material conveyer pipe and mixed conveyer pipe all is linked together with the input of blender, is provided with on the mixed conveyer pipe and mixes the transport control valve, and the output and the aseptic tank of blender are linked together.
2. The aseptic carbonation device for carbonated beverages according to claim 1, characterized in that: the mixing delivery pipe is also provided with a first aseptic adjusting valve and a first flow meter.
3. The aseptic carbonation device for carbonated beverages according to claim 1, characterized in that: the pressure reducing valve and the sterile air inlet adjusting valve are further arranged on the pressure preparing conveying pipe of the sterile tank, the top of the sterile tank is connected with an exhaust pipe, and the exhaust pipe is provided with a pressure sensor, a safety valve and a sterile exhaust adjusting valve.
4. The aseptic carbonation device for carbonated beverages according to claim 1, characterized in that: the material conveying pipe is provided with a cooler, an aseptic pump and a material flowmeter, and the material entering the material conveying pipe from the ultrahigh-temperature instantaneous sterilization machine enters the cooler to be cooled and then enters the mixer.
5. The aseptic carbonation device for carbonated beverages according to claim 1 or 2 or 3 or 4, characterized in that: be connected through aseptic technology cross anti-mixing valve between ultrahigh temperature instantaneous sterilization machine and the material conveying pipe, aseptic technology cross anti-mixing valve's structure includes: the valve comprises a valve seat, wherein a first interface, a second interface, a third interface, a fourth interface, a fifth interface and a sixth interface are arranged on the valve seat, a valve cavity, a first valve core, a second valve core and a third valve core are arranged in the valve seat, the second interface and the third interface are normally communicated, the fifth interface and the sixth interface are normally communicated, the first valve core can control the first interface to be communicated with or disconnected from the valve cavity under the control of the second valve core, the second interface and the third interface can be communicated with or disconnected from the valve cavity, and the fifth interface and the sixth interface can be communicated with or disconnected from the valve cavity; the third valve core can drive the fourth interface to be communicated with or disconnected from the valve cavity; the first interface is connected with the shielding steam conveying pipe, the second interface is connected with the cleaning pipeline, a cleaning control valve is arranged on the cleaning pipeline, the cleaning pipeline is used for conveying cleaning solution and sterilizing steam, and the third interface is connected with the material conveying pipe; the fourth interface is connected with a drain pipe, and a drain valve is arranged on the drain pipe; the fifth interface is connected with a discharge pipe of the ultra-high temperature instantaneous sterilization machine, and the sixth interface is connected with a liquid return pipe of the ultra-high temperature instantaneous sterilization machine.
6. The aseptic carbonation device for carbonated beverages according to claim 1 or 2 or 3 or 4, characterized in that: the mixer is a Venturi tube mixer.
7. The aseptic carbonation device for carbonated beverages according to claim 5, characterized in that: the top in the aseptic tank is provided with the cleaning ball of taking a plurality of nozzles, is linked together through the inlet pipe between blender and the aseptic tank, is provided with aseptic feeding governing valve on the inlet pipe, is connected with aseptic tank cleaning pipeline on the inlet pipe between the output of blender and the aseptic feeding governing valve, and aseptic tank cleaning pipeline is connected to the cleaning ball, is provided with aseptic tank cleaning control valve on the aseptic tank cleaning pipeline.
8. The aseptic carbonation device for carbonated beverages according to claim 5, characterized in that: the carbon dioxide pipeline on at least establish ties and be provided with two degerming filters, all be connected with the filter drain pipe of taking the valve on every filter.
9. The aseptic carbonation device for carbonated beverages according to claim 1 or 2 or 3 or 4, characterized in that: the input of carbon dioxide pipeline is provided with first check valve, and the output of mixing the conveyer pipe is provided with the second check valve.
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| CN201920130718.0U CN209885600U (en) | 2019-01-25 | 2019-01-25 | Aseptic carbonating device for carbonated beverage |
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| CN201920130718.0U CN209885600U (en) | 2019-01-25 | 2019-01-25 | Aseptic carbonating device for carbonated beverage |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113142442A (en) * | 2021-03-12 | 2021-07-23 | 江苏新美星包装机械股份有限公司 | Preparation process of sterile fruit grain carbonated beverage |
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2019
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113142442A (en) * | 2021-03-12 | 2021-07-23 | 江苏新美星包装机械股份有限公司 | Preparation process of sterile fruit grain carbonated beverage |
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Effective date of registration: 20220401 Address after: 215600 South District of Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province (Xinjing East Road) Patentee after: Jiangsu xinmeixing Industrial Research Institute Co.,Ltd. Address before: 215600 Jiangsu xinmeixing Packaging Machinery Co., Ltd., Xinjing East Road, South District, Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province Patentee before: JIANGSU NEWAMSTAR PACKAGING MACHINERY Co.,Ltd. |
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