CN207175427U - A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer - Google Patents
A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer Download PDFInfo
- Publication number
- CN207175427U CN207175427U CN201720841829.3U CN201720841829U CN207175427U CN 207175427 U CN207175427 U CN 207175427U CN 201720841829 U CN201720841829 U CN 201720841829U CN 207175427 U CN207175427 U CN 207175427U
- Authority
- CN
- China
- Prior art keywords
- carbon dioxide
- temperature control
- casing
- exchanging part
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Bakery Products And Manufacturing Methods Therefor (AREA)
Abstract
It the utility model is related to a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer, including carbon dioxide air source and sealing mechanism, the carbon dioxide temperature control mechanism that the carbon dioxide air source is connected with the sealing mechanism, carbon dioxide temperature control mechanism includes water tank, first heat exchanger tube and the heater for being heated to the water body in water tank, first heat exchanger tube has first end, the first heat exchanging part of second end and formation between the first and second ends, first end is connected with the port of export of the carbon dioxide air source, second end is connected with the gas input of the sealing mechanism, first heat exchanging part is arranged in water tank.After the technical solution of the utility model, the temperature of carbon dioxide is lifted by carbon dioxide temperature control mechanism, reduce its density, volume increase, so as under identical pressure and volume flow, use the lower carbon dioxide of density, the dosage of carbon dioxide can be reduced, reaches cost-effective effect.
Description
Technical field
It the utility model is related to a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer.
Background technology
The canned technological process of beer is：Unpiler from plastic pallet is unloaded the slack tank of code layer down, shifts polymer chain onto
On plate, done into rinsing maching with hot water injection, leaching, reach sterile.Then carbon dioxide isobar filling is used, utilizes carbon dioxide
Air in displacement tank, after canned, spray carbon dioxide draws the air that foam blows down tank mouth end, rapid capping.Examined using automatic liquid level
Instrument measurement capacity is surveyed, is pasteurize (spray sterilizing) afterwards.Tank base after sterilization is air cured machine drying, then by coding
Machine sprays the production time in tank bottom.During sealed cans after canned bakery food is filling, the broken bubbler using carbon dioxide to tin seamer
And lower end cap supply, the air of removal tank mouth end, carbon dioxide usage amount directly affect the oxygenation amount of beer, are related to product
Quality, in order to control extremely low oxygenation, it is necessary to substantial amounts of carbon dioxide is consumed, as the raising of canned bakery food yield, company are every
Year needs the substantial amounts of food-grade carbon-dioxide of outsourcing, and this necessarily increases the production cost of company.
In view of this, inventor furthers investigate to above mentioned problem, there is this case generation then.
Utility model content
The purpose of this utility model is to provide one kind in the case where ensureing quality of finished, can be cost-effective tinned
The carbon dioxide temperature control consumption reducing device of beer tin seamer.
In order to achieve the above object, technical scheme as the utility model use：
A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer, including carbon dioxide air source and tin seamer
Structure, carbon dioxide temperature control mechanism, carbon dioxide temperature control mechanism bag are provided between the carbon dioxide air source and the sealing mechanism
Include water tank, the first heat exchanger tube and the heater for being heated to the water body in water tank.First heat exchanger tube have first end,
The first heat exchanging part of second end and formation between the first and second ends, first end and the outlet of the carbon dioxide air source
End linking, the second end are connected with the gas input of the sealing mechanism, and the first heat exchanging part is arranged in water tank.
As a kind of preferred embodiment of the present utility model, the water tank includes the first casing and the second casing, and described first
Heat exchanging part is arranged in the first casing, and the heater includes vapor source of the gas and the second heat exchanger tube, and the second heat exchanger tube has
Admission end, steam output end and the second heat exchanging part formed between admission end and steam output end, the second heat exchanging part are arranged on the second case
In body, the first casing is connected with the second casing by circulation line.
As a kind of preferred embodiment of the present utility model, first heat exchanger tube is in the first end and the described first heat exchange
Position between portion is provided with check valve and the first control valve, and first heat exchanger tube is in second end and the described first heat exchange
Position between portion is provided with constant pressure valve and the second control valve.
As a kind of preferred embodiment of the present utility model, in addition to controller, in the admission end and the described second heat exchange
Pneumatic operated valve is provided between portion, pneumatic operated valve is electrically connected to controller, and temperature sensor, TEMP are provided with second casing
Device is electrically connected to controller.
As a kind of preferred embodiment of the present utility model, the circulating line includes the first pipeline, second pipe and followed
Ring pump；The first water inlet and the first delivery port are provided with first casing；The second water inlet is provided with second casing
Mouth and the second delivery port；The both ends of first pipeline connect the first delivery port and the second water inlet respectively；The both ends of second pipe point
The second delivery port and the first water inlet, centre connection circulating pump are not connected.
After the technical solution of the utility model, the density of carbon dioxide reduces as temperature increases, and passes through
Carbon dioxide temperature control mechanism lifts the temperature of carbon dioxide, reduces its density, volume increase, so as in identical pressure and body
Under product flow, using the lower carbon dioxide of density, the dosage of carbon dioxide can be reduced, reaches cost-effective
Effect；Meanwhile the utility model is rested in water tank for a long time by hot water indirectly heat, gas, its temperature is more held
Easily keep constant, be not in overheat or the situation that drastically cools, ensure the quality of product.
Brief description of the drawings
Fig. 1 is structure diagram of the present utility model；
In figure：
10- carbon dioxide air source 20- sealing mechanisms
30- water tanks the first casings of 31-
32- the second casing the first heat exchanger tubes of 40-
The second ends of 41- first ends 42-
43- the first heat exchanging part the first control valves of 44-
45- the second control valve 46- check valves
47- constant pressure valves the second heat exchanger tubes of 50-
51- inlet end 52- outlet sides
53- the second heat exchanging part 54- pneumatic operated valves
60- controller 70- temperature sensors
81- the first pipeline the second pipelines of 82-
83- circulating pumps
Embodiment
In order to which the technical solution of the utility model is explained further, it is described in detail below in conjunction with the accompanying drawings.
Reference picture 1, a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer, including carbon dioxide air source
And sealing mechanism, carbon dioxide temperature control mechanism, carbon dioxide temperature are provided between the carbon dioxide air source and the sealing mechanism
Control mechanism includes water tank 30, the first heat exchanger tube 40 and the heater for being heated to the water body in water tank 30, and first changes
Heat pipe 40 has first end 41, the second end 42 and the first heat exchanging part 43 formed between the end 42 of first end 41 and second, the
One end 41 is connected with the port of export of the carbon dioxide air source 10, the second end 42 and the gas input of the sealing mechanism 20
Linking, is specifically connected to the broken bubbler and lower end cap of tin seamer, and the first heat exchanging part 43 is arranged in water tank 30.In this reality
Snakelike tubular construction can be used with the first heat exchanging part 43 in new, to increase the time of contact of carbon dioxide and hot water.It is suitable
For the electric heater device of the filling tin seamer carbon dioxide of canned bakery food, 20 are up to plus the investment cost of control element
More than ten thousand yuan, and the power of this heater is larger, volume is smaller, carbon dioxide is rapidly heated and be heated equal
Even to need longer time, particularly filling tin seamer of short duration shutdown just needs manually regulation of carbon dioxide gas when restarting
Flow, it is unfavorable for the stability contorting of the oxygen content of canned bakery food, therefore, the utility model is using hot water indirectly to carbon dioxide gas
Body heats.
As a kind of preferred embodiment of the present utility model, the water tank 30 includes the first casing 31 and the second casing 32, institute
State the first heat exchanging part 43 to be arranged in the first casing 31, the heater includes water vapor source (not shown) and second
Heat exchanger tube 50, water vapour is conveyed by the second heat exchanger tube 50, the second heat exchanger tube 50 has admission end 51, steam output end 52 and shape
Into the second heat exchanging part 53 between admission end 51 and steam output end 52, the second heat exchanging part 53 is arranged in the second casing 32, and first
Casing 31 is connected with the second casing 32 by circulation line, and in embodiment, the second heat exchanger tube 50 uses snakelike tubular construction.
As a kind of preferred embodiment of the present utility model, first heat exchanger tube 40 is in the first end 41 and described the
Position between one heat exchanging part 43 is provided with the control valve 44 of check valve 46 and first, and first heat exchanger tube 40 is in second end
Position between 42 and first heat exchanging part 43 is provided with the control valve 45 of constant pressure valve 47 and second, ensures two by constant pressure valve 47
The stable output of carbonoxide.
As a kind of preferred embodiment of the present utility model, in addition to controller 60, in the admission end 51 and described second
Pneumatic operated valve 54 is provided between heat exchanging part 53, pneumatic operated valve 54 is electrically connected to controller 60, and temperature is provided with second casing 32
Sensor 70, temperature sensor 70 are electrically connected to controller 60.Controller 60 is right by the feedack of temperature sensor 70
Pneumatic operated valve 54 is controlled, and when the hot water temperature in the second water tank 32 is higher, then stops the supply of steam.
As a kind of preferred embodiment of the present utility model, the circulating line include the first pipeline 81, second pipe 82 with
And circulating pump 83, the first water inlet and the first delivery port are provided with first casing 31, is set on second casing 32
There are the second water inlet and the second delivery port, the both ends of the first pipeline 81 connect the first delivery port and the second water inlet respectively, and second
The both ends of pipeline connect the second delivery port and the first water inlet respectively.Hot water is continued from the second casing 32 by circulating pump 83
It is delivered in the first casing 31, the hot water in the first water tank 32 is continually exchanged heat with the first heat exchanging part 43.
In the utility model, normal temperature carbon dioxide enters the first casing 31 by check valve 46 and carries out hot friendship with hot water
Change, hot water temperature is automatically turned off steam pneumatic operated valve 54 according to temperature change by controller 60 and controlled, and hot water temperature is controlled 60 ± 2
DEG C, carbon dioxide gas temperature reaches 55 DEG C after heating, tin seamer mechanism 20 is entered after constant pressure valve 47, by former machine carbon dioxide
Supply control unit automatically controls gas flow, is controlled without manual hand manipulation.
The beneficial effects of the utility model：1st, it makes its temperature reach 55 DEG C, dioxy by heating carbon dioxide
Change carbon volumetric expansion about 15%-20%, for tinned tin seamer under equal operating condition, broken bubbler and lower end cap supply consumption
Carbon dioxide constancy of volume, but carbon dioxide Mass lost 15%-20%, KL (kilolitre) beer save carbon dioxide usage amount
2Kg or so, production cost is saved.2nd, the utility model has the advantages of environmental protection, energy-conservation.3rd, it is indirect using hot-water heater
Carbon dioxide is heated, there is the advantages of stable temperature control, reasonable, easy to operate, meet carbon dioxide temperature requirements, it is right
Beer total oxygen content is controlled without any quality risk.
Product form of the present utility model is not limited to this case diagram and embodiment, and anyone carries out similar thinking to it
Appropriate change or modification, all should be regarded as not departing from patent category of the present utility model.
Claims (6)
1. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer, including carbon dioxide air source and tin seamer
Structure, it is characterised in that：Carbon dioxide temperature control mechanism, carbon dioxide are provided between the carbon dioxide air source and the sealing mechanism
Temperature control mechanism includes water tank, the first heat exchanger tube and the heater for being heated to the water body in water tank, the first heat exchanger tube
With first end, the first heat exchanging part of the second end and formation between the first and second ends, first end and the titanium dioxide
The port of export linking of carbon source of the gas, the second end are connected with the gas input of the sealing mechanism, and the first heat exchanging part is arranged on water tank
It is interior.
2. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer as claimed in claim 1, its feature exist
In：The water tank includes the first casing and the second casing, and first heat exchanging part is arranged in the first casing, the heater bag
Vapor source of the gas and the second heat exchanger tube are included, the second heat exchanger tube has inlet end, outlet side and formed in inlet end and outlet
The second heat exchanging part between end, the second heat exchanging part are arranged in the second casing, and the first casing and the second casing pass through circulation line
Connection.
3. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer as claimed in claim 2, its feature exist
In：Position of first heat exchanger tube between the first end and first heat exchanging part is provided with check valve and the first control valve
Door, position of first heat exchanger tube between second end and first heat exchanging part is provided with constant pressure valve and the second control valve
Door.
4. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer as claimed in claim 3, its feature exist
In：Also include controller, pneumatic operated valve is provided between the inlet end and second heat exchanging part, pneumatic operated valve is electrically connected to control
Device, is provided with temperature sensor in second casing, and temperature sensor is electrically connected to controller.
5. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer as claimed in claim 4, its feature exist
In：The circulating line includes the first pipeline, second pipe and circulating pump, and the first water inlet is provided with first casing
With the first delivery port, the second water inlet and the second delivery port are provided with second casing, the both ends of the first pipeline connect respectively
The first delivery port and the second water inlet are connect, the both ends of second pipe connect the second delivery port and the first water inlet respectively.
6. a kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer as claimed in claim 5, its feature exist
In：The temperature of the carbon dioxide at the second end of first heat exchanger tube is at 55 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720841829.3U CN207175427U (en) | 2017-07-12 | 2017-07-12 | A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720841829.3U CN207175427U (en) | 2017-07-12 | 2017-07-12 | A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207175427U true CN207175427U (en) | 2018-04-03 |
Family
ID=61735811
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720841829.3U Active CN207175427U (en) | 2017-07-12 | 2017-07-12 | A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207175427U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111913513A (en) * | 2020-05-07 | 2020-11-10 | 蚌埠学院 | Multi-loop circulating gas temperature control method |
-
2017
- 2017-07-12 CN CN201720841829.3U patent/CN207175427U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111913513A (en) * | 2020-05-07 | 2020-11-10 | 蚌埠学院 | Multi-loop circulating gas temperature control method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5937655A (en) | Pressure building device for a cryogenic tank | |
| CN203750903U (en) | Rapid ultrasonic spraying and cleaning sterilizer | |
| CN202521581U (en) | Quick steam generation system | |
| CN204072830U (en) | Medical apparatus sterilizer | |
| CN111947029A (en) | Stable supercritical carbon dioxide gas supply system and method | |
| CN207175427U (en) | A kind of carbon dioxide temperature control consumption reducing device of canned bakery food tin seamer | |
| TW201402210A (en) | Evaporative gas generating device and method for producing evaporative gas, and hydrogen bromide production device and method for producing hydrogen bromide | |
| CN205359305U (en) | Liquid batching mechanism | |
| CN105402706B (en) | A kind of dioxygen steam generator | |
| CN110180001A (en) | A kind of medical treatment disinfection steam unit and its application method | |
| CN204582017U (en) | A kind of normal pneumatic high-temperature steam sterilization cabinet | |
| CN108722704A (en) | Dioxygen water atomization plant | |
| CN208703892U (en) | Electric heating assistant cleaning steam generator | |
| CN208746758U (en) | Mobile heat-conducting oil heating system | |
| CN204128162U (en) | A kind of boiler | |
| CN101756339A (en) | Pressure-controlling method of sterilizing kettle in sterilization cooling stage | |
| CN213018900U (en) | Stable supercritical carbon dioxide gas supply system | |
| CN201242260Y (en) | Energy-saving pipe type intrinsic cycle constant-temperature water heater | |
| CN106679167A (en) | Electric heating equipment beneficial to uniform temperature rise of liquid | |
| CN207865348U (en) | A kind of dioxygen steam generator | |
| CN209221042U (en) | Horizontal sterilizer | |
| CN206333745U (en) | Anti- haze hot-water bottle | |
| CN205284885U (en) | Pasteurization machine cooling hot water recovery utilizes device | |
| CN209609772U (en) | A kind of full-service fluid sterilization duct system | |
| CN202993548U (en) | Energy-saving water boiler |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |