CN212629755U - Sleeve type sterilization device - Google Patents

Sleeve type sterilization device Download PDF

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Publication number
CN212629755U
CN212629755U CN202021257614.5U CN202021257614U CN212629755U CN 212629755 U CN212629755 U CN 212629755U CN 202021257614 U CN202021257614 U CN 202021257614U CN 212629755 U CN212629755 U CN 212629755U
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pipeline
communicated
tank
assembly
circulating
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CN202021257614.5U
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张平峰
张华光
彭伟
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Ningbo Gongcheng Machinery Co ltd
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Ningbo Gongcheng Machinery Co ltd
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Abstract

The utility model relates to a sleeve type sterilization device, which comprises a material tank, a degasser communicated with the material tank through a pipeline, a homogenizer communicated with the degasser through a pipeline, a circulating tank assembly communicated with the homogenizer through a pipeline, a heating assembly for heating the circulating tank assembly, a steam assembly for performing steam treatment on materials in the circulating tank assembly, a sterilizer for sterilizing the materials discharged from the circulating tank assembly, and a discharge tank communicated with the sterilizer through a pipeline; the discharge tank is respectively communicated with the hot filling machine and the return pipe through a pipeline with a pneumatic two-position three-way valve; the material is returned to the material tank through the return pipe through a pipeline. The utility model discloses a bushing type sterilizing equipment through the soft water heating, improves heating efficiency, especially adopts circulating transport mode for the product of temperature up to standard packs the processing, and the product of temperature not up to standard circulates the processing, and is in cycles, and efficiency is higher, does not take place the extravagant condition of falling.

Description

Sleeve type sterilization device
Technical Field
The utility model belongs to the technical field of the fruit juice technique of disinfecting and specifically relates to a bushing type sterilizing equipment.
Background
The working route of the front sterilization machine is generally a working procedure of a raw material buffer tank, a forced material pump, a metering delivery pump, a heating heat exchanger, a sterilization temperature-holding device, a cooler and a filling machine, steam and raw water enter a plate type heat exchanger for heat exchange, heated hot water enters a heating section heat exchanger for partial utilization, then the heated hot water is discharged and enters a recovery system to further circulate into the plate type heat exchanger, the steam is changed into condensed water after meeting the raw water, the temperature of the condensed water is about 132 ℃, and the condensed water is discharged along with the condensed water, so that the energy waste is caused. In addition, the temperature of the material flowing out through the heating section and the sterilization temperature-holding section is about 132 ℃, and then the material enters the cooling section to be cooled to about 40 ℃ suitable for filling, so that a large cooling area is needed, and the manufacturing cost of the equipment is increased while the heat energy is wasted.
SUMMERY OF THE UTILITY MODEL
First, technical problem to be solved
The utility model provides a to the above-mentioned defect that prior art exists, a bushing type sterilizing equipment has especially been proposed, the working route who has solved the sterilization machine before leading to generally is the process of raw materials buffer tank-compulsory material pump-measurement transfer pump-heating heat exchanger-sterilization temperature keeper-cooler-liquid filling machine, steam and raw water get into plate heat exchanger and carry out the heat exchange after, the hot water that is heated gets into the heating section heat exchanger and is partly utilized, get into recovery system and then circulate into plate heat exchanger after being got rid of afterwards, and steam becomes the comdenstion water after meeting the raw water, this comdenstion water temperature is about up to 132 ℃, but discharges thereupon, the waste of the energy has been caused. In addition, the temperature of the material which flows out through the heating section and the sterilization temperature-holding section for heat preservation is about 132 ℃, and the material subsequently enters the cooling section to be cooled to about 40 ℃ suitable for filling, so that a large cooling area is needed, and the technical problem of increasing the manufacturing cost of equipment is also caused while the heat energy is wasted.
Second, technical scheme
The utility model discloses a bushing type sterilization device, which comprises a material tank, a degasser communicated with the material tank through a pipeline, a homogenizer communicated with the degasser through a pipeline, a circulating tank assembly communicated with the homogenizer through a pipeline, a heating assembly for heating the circulating tank assembly, a steam assembly for performing steam treatment on materials in the circulating tank assembly, a sterilizer for sterilizing the materials discharged from the circulating tank assembly, and a discharge tank communicated with the sterilizer through a pipeline; the discharge tank is respectively communicated with the hot filling machine and the return pipe through a pipeline with a pneumatic two-position three-way valve; the material is returned to the material tank through the return pipe through a pipeline.
Furthermore, external materials and soft water are communicated with the material tank through a pipeline with a four-way valve; the output end of the material groove is connected with a pipeline of a first centrifugal pump and a first visual thermometer and communicated with a holding pipe assembly, the holding pipe assembly comprises more than two holding pipes which are communicated with each other, and the output end of each holding pipe is connected with a second visual thermometer and communicated with a degassing machine.
Further, the device also comprises an acidic auxiliary material tank and an alkaline auxiliary material tank; the material tank is respectively communicated with the acidic auxiliary material tank and the alkaline auxiliary material tank through an acidic isolation pump and an alkaline isolation pump.
Further, the homogenizer is communicated with the circulating tank assembly through a pipeline with a multi-stage centrifugal pump.
Furthermore, the circulating tank assembly comprises a plurality of circulating tanks which are communicated with one another; the circulating tank is communicated with the sterilizer through a pipeline with a third visible thermometer.
Furthermore, the heating assembly comprises a soft water pipeline for feeding soft water and a hot water tank communicated with the soft water pipeline; the hot water tank is communicated with the circulating tank assembly through a pipeline and is communicated with the discharge tank through a pipeline with a second centrifugal pump.
The steam assembly comprises a steam pipeline for feeding steam and a brazed heat exchanger communicated with the steam pipeline; the brazed heat exchanger is communicated with the circulating tank assembly through a steam pipeline and is communicated with the discharge tank through a steam pipeline.
Furthermore, the discharge tank is respectively communicated with the hot filling machine and the return pipe through a pneumatic two-position three-way valve with a fourth visible thermometer; and the pneumatic two-position three-way valve is used for shunting the temperature of the material measured by the fourth visible thermometer to a hot filling machine or a return pipe.
Third, beneficial effect
Compared with the prior art, the sleeve type sterilization device has compact structure and good sterilization effect, and the internal circulation is used for carrying out circulating evaporation and separation operation on the final concentrated juice; unprocessed fruit juice can be refrigerated in a condenser, so that the fruit juice is prevented from going bad, and the method has good practicability.
Drawings
Fig. 1 is a schematic view of the whole structure of a bushing type sterilization device of the present invention.
Detailed Description
The following detailed description of the embodiments of the present invention is provided with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
The utility model discloses a bushing type sterilization device, it includes material groove 1, degasser 2 through pipeline and material groove 1 intercommunication, homogenizer 3 through pipeline and degasser 2 intercommunication, circulation jar subassembly 5 through pipeline and homogenizer 3 intercommunication, the heating element 6 that heats usefulness to circulation jar subassembly 5, the steam subassembly 8 that carries out steam treatment to the material in circulation jar subassembly 5, go out sterilizer 4 that the material disinfected usefulness to circulation jar subassembly 5, discharge tank 9 through pipeline and sterilizer 4 intercommunication; the discharge tank 9 is respectively communicated with the hot filling machine 10 and the return pipe 7 through a pipeline with a pneumatic two-position three-way valve 90; the return pipe 7 returns the material to the material tank 1 through a pipeline.
External materials and soft water are communicated with the material tank 1 through a pipeline with a four-way valve 101; the output end of the material tank 1 is connected with a pipeline of a first centrifugal pump 106 and a first visual thermometer 110 and is communicated with a holding pipe assembly 11, the holding pipe assembly 11 comprises more than two holding pipes 111 which are communicated with each other, and the output end of each holding pipe 111 is connected with a second visual thermometer 210 and is communicated with a degassing machine 2.
Also comprises an acidic auxiliary material tank 102 and an alkaline auxiliary material tank 103; the material tank 1 is respectively communicated with an acidic auxiliary material tank 102 and an alkaline auxiliary material tank 103 through an acidic isolation pump 104 and an alkaline isolation pump 105.
The homogenizer 3 is in communication with the circulation tank assembly 5 through a pipeline with a multistage centrifugal pump 31.
The circulation tank assembly 5 comprises a plurality of circulation tanks 51 which are communicated with one another; the circulation tank 51 is communicated with the sterilizer 4 through a pipe with a third visual temperature gauge 310.
The heating assembly 6 comprises a soft water pipeline for feeding soft water and a hot water tank 61 communicated with the soft water pipeline; the hot water tank 61 is connected to the circulation tank assembly 5 via a pipe and to the discharge tank 9 via a pipe with a second centrifugal pump 62.
The steam assembly 8 comprises a steam pipeline for steam inlet and a brazed heat exchanger 81 communicated with the steam pipeline; the brazed heat exchanger 81 is in communication with the circulation tank assembly 5 via a vapor line and in addition is in communication with the discharge tank 9 via a vapor line.
The discharge tank 9 is respectively communicated with the hot filling machine 10 and the return pipe 7 through a fourth visible thermometer 410 and a pneumatic two-position three-way valve 90; the pneumatic two-position three-way valve 90 diverts the temperature of the material to the hot-filling machine 10 or the return pipe 7 according to the temperature measured by the fourth visual temperature gauge 410.
The working principle is as follows:
a sleeve type sterilization device, the feed end of the material trough 1 connects with the four-way valve 101 (not marked in the figure), the pipeline (not marked in the figure) can convey the supplies and soft water into the material trough 1, after the mixture of the supplies and soft water in the material trough 1 is mixed, through its output end through the pipeline (not marked in the figure) with first centrifugal pump 106 to convey to keeping the tube assembly 11, at this moment, measure the temperature of the mixture as 60 degrees centigrade through the first visual thermometer 110 on the pipeline (not marked in the figure), the mixture of 60 degrees centigrade enters two keeping tubes 111 that link together each other;
then, the mixture in the holding tube 111 is primarily heated by the heating unit 6, and the output mixture is displayed at 68 ℃ on the second visual temperature table 210, and the mixture at the temperature is suitable for degassing and homogenizing, so that the mixture at 68 ℃ is sequentially introduced into the degassing unit 2 through the pipeline for degassing and homogenized in the homogenizing unit 3,
then, the homogenized mixture is conveyed to the circulation tank assembly 5 through a pipeline with a multistage centrifugal pump 31, the homogenized mixture can move from left to right in the circulation tank assembly 5 in sequence, at the same time, hot water of the heating assembly 6 heats the homogenized mixture of the circulation tank assembly 5, meanwhile, steam in the steam assembly 8 is conveyed to the circulation tank assembly 5 through a brazed heat exchanger 81 with a steam pipeline to heat the mixture for the second time, after heating, the mixture output at the moment shows 98 ℃ on a third visual temperature gauge 310, the mixture at the temperature is suitable for sterilization, and then the mixture at the 98 ℃ is sterilized through a pipeline (not shown in the figure) by the sterilizer 4;
then, the mixture sterilized by the sterilizer 4 is conveyed into a discharge tank 9 through a pipeline (not marked in the figure), the storage tank 9 is respectively connected with a heating component 6 and a steam component 8, when the mixture is output, the mixture is heated again, so that the mixture can meet the filling temperature requirement of 80-85 ℃, the conveyed mixture is tested in a fourth visual thermometer 410, the mixture with qualified temperature is conveyed into a hot filling machine 10 through the control of a pneumatic two-position three-way valve 90, the mixture with unqualified temperature is conveyed into a return pipe 7, and the unqualified mixture can continuously return to the material tank 1 from the return pipe 7 for the above operation;
finally, the mixture is subjected to a filling and packaging process from the hot-filling machine 10.
Compared with the prior art, the utility model discloses a bushing type sterilizing equipment through the soft water heating, improves heating efficiency, especially adopts circulating transport mode for the product of temperature to reach standard packs the processing, and the product of temperature to reach standard does not circulate and handles, and the cycle is repeated, and efficiency is higher, does not take place the extravagant condition of falling.
The above is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of improvements and decorations can be made without departing from the technical principle of the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.

Claims (8)

1. A bushing type sterilizing equipment, its characteristic is: the device comprises a material tank (1), a degasser (2) communicated with the material tank (1) through a pipeline, a homogenizer (3) communicated with the degasser (2) through a pipeline, a circulating tank assembly (5) communicated with the homogenizer (3) through a pipeline, a heating assembly (6) for heating the circulating tank assembly (5), a steam assembly (8) for carrying out steam treatment on materials in the circulating tank assembly (5), a sterilizer (4) for sterilizing materials discharged from the circulating tank assembly (5), and a discharge tank (9) communicated with the sterilizer (4) through a pipeline; the discharge tank (9) is respectively communicated with the hot filling machine (10) and the return pipe (7) through a pipeline with a pneumatic two-position three-way valve (90); the return pipe (7) returns the materials to the material tank (1) through a pipeline.
2. The telescopic sterilization apparatus as set forth in claim 1, wherein: external materials and soft water are communicated with the material tank (1) through a pipeline with a four-way valve (101); the output end of the material tank (1) is connected with a first centrifugal pump (106) and a pipeline of a first visual thermometer (110) and communicated with a holding pipe assembly (11), the holding pipe assembly (11) comprises more than two holding pipes (111) which are communicated with each other, and the output end of each holding pipe (111) is connected with a second visual thermometer (210) and communicated with a degassing machine (2).
3. The telescopic sterilization apparatus as set forth in claim 2, wherein: also comprises an acidic auxiliary material tank (102) and an alkaline auxiliary material tank (103); the material tank (1) is respectively communicated with the acidic auxiliary material tank (102) and the alkaline auxiliary material tank (103) through an acidic isolation pump (104) and an alkaline isolation pump (105).
4. The telescopic sterilization apparatus as set forth in claim 2, wherein: the homogenizer (3) is communicated with the circulating tank assembly (5) through a pipeline with a multi-stage centrifugal pump (31).
5. The telescopic sterilization apparatus as set forth in claim 4, wherein: the circulating tank assembly (5) comprises a plurality of circulating tanks (51) which are communicated with one another; the circulating tank (51) is communicated with the sterilizer (4) through a pipeline with a third visual thermometer (310).
6. The telescopic sterilization apparatus as set forth in claim 5, wherein: the heating assembly (6) comprises a soft water pipeline for feeding soft water and a hot water tank (61) communicated with the soft water pipeline; the hot water tank (61) is connected with the circulating tank assembly (5) through a pipeline, and is also connected with the discharge tank (9) through a pipeline with a second centrifugal pump (62).
7. The telescopic sterilization apparatus as set forth in claim 5, wherein: the steam assembly (8) comprises a steam pipeline for steam inlet and a brazed heat exchanger (81) communicated with the steam pipeline; the brazed heat exchanger (81) is communicated with the circulating tank assembly (5) through a steam pipeline and is communicated with the discharge tank (9) through a steam pipeline.
8. The telescopic sterilization apparatus as set forth in claim 1, wherein: the discharge tank (9) is respectively communicated with the hot filling machine (10) and the return pipe (7) through a fourth visible thermometer (410) and a pneumatic two-position three-way valve (90); the pneumatic two-position three-way valve (90) shunts the temperature of the material to the hot filling machine (10) or the return pipe (7) according to the temperature of the material measured by the fourth visual thermometer (410).
CN202021257614.5U 2020-07-01 2020-07-01 Sleeve type sterilization device Active CN212629755U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202021257614.5U CN212629755U (en) 2020-07-01 2020-07-01 Sleeve type sterilization device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202021257614.5U CN212629755U (en) 2020-07-01 2020-07-01 Sleeve type sterilization device

Publications (1)

Publication Number Publication Date
CN212629755U true CN212629755U (en) 2021-03-02

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN202021257614.5U Active CN212629755U (en) 2020-07-01 2020-07-01 Sleeve type sterilization device

Country Status (1)

Country Link
CN (1) CN212629755U (en)

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