CN207886935U - The drying device of ice cream cone paper complete forming device compressed gas - Google Patents
The drying device of ice cream cone paper complete forming device compressed gas Download PDFInfo
- Publication number
- CN207886935U CN207886935U CN201820011199.1U CN201820011199U CN207886935U CN 207886935 U CN207886935 U CN 207886935U CN 201820011199 U CN201820011199 U CN 201820011199U CN 207886935 U CN207886935 U CN 207886935U
- Authority
- CN
- China
- Prior art keywords
- valve
- reservoir cavity
- ice cream
- reservoir
- drying
- 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.)
- Expired - Fee Related
Links
Landscapes
- Drying Of Gases (AREA)
Abstract
The utility model discloses the drying devices of ice cream cone paper complete forming device compressed gas, including drying tower, with gas point, cooling separator and compressor, the inner cavity of drying tower is equally divided into 4 or 4 or more reservoir cavities by polylith thermal baffle, drier is respectively arranged in reservoir cavity, multiple reservoir cavities are respectively set to renewing zone, cooling zone and dry section successively by sequence clockwise or counter-clockwise in drying tower, breather valve is mounted on every piece of thermal baffle;Air bleeding valve and air outlet valve is respectively set at the top of each reservoir cavity, regeneration valve and intake valve is respectively set in bottom, and air bleeding valve is connected with the bottom of cooling separator, and air outlet valve is connected to with gas point, regeneration valve is connected with compressor, and intake valve is connected with the top of cooling separator;The utility model can ensure that the drying effect of compressed air, device volume reduce, and operating cost reduces, efficient.
Description
Technical field
The utility model is related to drying device technical fields, and in particular to the drying of ice cream cone paper complete forming device compressed gas
Device.
Background technology
Ice cream cone paper complete forming device tends to automation development at present, has multiple positions on ice cream cone paper complete forming device(Packet
Include the blowout etc. of paper advance mechanism, molding die and paper set)It needs to use compressed gas, the compressed gas used has to ensure
It is dry, in order to avoid increasing the moisture in paper products, lead to its deformation, or even influence the rate of drying of glue;And sky is compressed at present
The drying device of gas is varied, most of to use Double-Tower Structure, is dried by two drying towers switchings, one when work
A tower is as drying tower, another tower is as regenerator, when desiccant regeneration in regenerator, needs to be passed through heat in toward regenerator
Gas makes desiccant regeneration, but is passed through in the drier after hot gas in regenerator and also has waste heat, is directly used as drying tower
Drying effect can be produced bigger effect, therefore usually can also using partially dried compressed air come carry out regenerator purging and
It is cooling, it is then vented again, this mode for not only having consumed hot gas but also lose finished product compressed gas so that the operating cost of device is high
And efficiency is low;If in this way, that there are drying effects is poor for existing drying device, bulky, pipeline is intricate
The defects of, it is not suitable for ice cream cone paper complete forming device.Therefore, ice cream cone paper a kind of simple in structure and low operating cost is developed
The drying device of complete forming device compressed gas is desirability.
Utility model content
The purpose of this utility model is to provide ice cream cone paper complete forming device pressures a kind of simple in structure and low operating cost
The drying device of contracting gas.
The purpose of this utility model be achieved in that the utility model include drying tower, with gas point, cooling separator and
Compressor, the inner cavity of drying tower are equally divided into 4 or 4 or more reservoir cavities by polylith thermal baffle, in reservoir cavity
It is respectively arranged with drier, multiple reservoir cavities are respectively set to renewing zone, cooling successively by sequence clockwise or counter-clockwise
Area and dry section are mounted on breather valve on every piece of thermal baffle;It is connected with one on the bottom bulkhead of each reservoir cavity
A regeneration valve, multiple regeneration valves are connected by pressure pipeline with the escape pipe of compressor, on the top end socket of each reservoir cavity
There are one air bleeding valve, multiple air bleeding valves to be connected with the bottom of cooling separator by pressure pipeline for connection, the top of cooling separator
Portion is connected with multiple intake valves by pressure pipeline side by side, and each intake valve is connected to the bottom bulkhead of a reservoir cavity, often
It is also connected on the top end socket of a reservoir cavity there are one air outlet valve, all air outlet valves are connected to by pressure pipeline with gas point.
Further, it is both provided with temperature monitor on the inner wall of each reservoir cavity;Breather valve is all made of cut-off
Valve;Air bleeding valve, air outlet valve, regeneration valve and intake valve are all made of butterfly valve;Multilayer demisting net is provided in cooling separator, it is cooling to divide
Bottom from device is provided with drainpipe, and blowdown valve is provided on drainpipe;Demisting net is tiltedly mounted on the inner wall of cooling separator
On, and multilayer demisting net is arranged in parallel;Drying tower and it is additionally provided with buffer tank between gas point.
There are one drying tower is only arranged in the utility model, and thermal baffle is set, the cavity inside drying tower is divided into 4
A above reservoir cavity, device operation only have 1 renewing zone, a cooling zone, and dry section have 2 or 2 with
On, by the way that air bleeding valve and air outlet valve are respectively set at the top of each reservoir cavity, regeneration valve and air inlet is respectively set in bottom
Valve switches over various valves so that the hot compressed air flowed out in renewing zone is first pass through cooling separator cold always
But just enter cooling zone after being detached with aqueous vapor, compressed air flows in cooling zone, and drier is made to cool off, and then compression is empty
Gas sequentially enters each dry section and is adequately dried again, ensures to reach each position on ice cream cone paper complete forming device
Compressed air drying, because of dry section 2 times or more bigger than the volume of cooling zone and renewing zone always, it can be ensured that compression is empty
The drying effect of gas, the utility model are introduced directly into hot compressed air as regeneration gas, then use cooling and water removal pressure
Contracting air cooling drier so that device whole device volume-diminished, operating cost reduce, the not emptying of drying compressed air
Processing, efficiency improve.
Description of the drawings
Fig. 1 is the utility model overall structure diagram;
Fig. 2 is the inner section schematic diagram of drying tower 1.
In figure:1- drying towers, 11- reservoir cavities, 12- temperature monitors, 2- thermal baffles, 21- breather valves, 3- exhausts
Valve, 4- air outlet valves, 5- gas points, 51- buffer tanks, 6- cooling separators, 61- demisting nets, 62- drainpipes, 63- blowdown valves, 7-
Compressor, 8- regeneration valves, 9- intake valves.
Specific implementation mode
The utility model will be further described below with reference to the accompanying drawings, but is not subject in any way to the utility model
Limitation belongs to the scope of protection of the utility model based on any changes and modifications made by the utility model introduction.
As shown in Figure 1, the utility model includes drying tower 1, with gas point 5, cooling separator 6 and compressor 7, drying tower 1
Inner cavity 4 or 4 or more reservoir cavities 11 are equally divided by polylith thermal baffle 2, be respectively arranged in reservoir cavity 11 dry
Multiple reservoir cavities 11 are respectively set to renewing zone, cooling zone successively by sequence clockwise or counter-clockwise and done by drying prescription
Dry area, the renewing zone, cooling zone and dry section can convert in due course, and breather valve 21 is mounted on every piece of thermal baffle 2;Each
There are one regeneration valves 8, multiple regeneration valves 8 to pass through pressure pipeline and compressor 7 for connection on the bottom bulkhead of the reservoir cavity 11
Escape pipe be connected, there are one air bleeding valve 3, multiple air bleeding valves 3 pass through pressure for connection on the top end socket of each reservoir cavity 11
Pipeline is connected with the bottom of cooling separator 6, and the top of cooling separator 6 is connected with multiple intake valves by pressure pipeline side by side
9, each intake valve 9 is connected to the bottom bulkhead of a reservoir cavity 11, is also connected on the top end socket of each reservoir cavity 11
There are one air outlet valve 4, all air outlet valves 4 are connected to by pressure pipeline with gas point 5.
Be both provided with temperature monitor 12 on the inner wall of each reservoir cavity 11, when temperature monitor 12 detect it is cold
But the temperature in area reduces and renewing zone temperature is when reaching setting value, illustrates that the drier in renewing zone completes regeneration, cooling simultaneously
Desiccant temperature in area also reduces, and has adsorption capacity again, switches corresponding each valve at this time, by original drying
One in area is switched to renewing zone, and renewing zone originally is switched to cooling zone, and cooling zone originally is switched to dry section.
Breather valve 21 is in order to allow compressed air to be flowed between multiple reservoir cavities 11, in order to make drying effect when flowing
More preferably, therefore use valve body long, the shut-off valve with larger flow resistance, while the closing tightness of shut-off valve is good, can reach close
Envelope requires.
Air bleeding valve 3, air outlet valve 4, regeneration valve 8 and intake valve 9 are all made of butterfly valve, are because of valve needed for the valve at these positions
Body length is small, and the flow resistance of butterfly valve is small, simple in structure, small, light-weight, and is adapted for mount on pipeline and only needs
Be rotated by 90 ° can fast opening and closing, it is easy to operate, while there are good fluid handling properties.
Multilayer demisting net 61 is provided in the cooling separator 6, the bottom of cooling separator 6 is provided with drainpipe 62,
Blowdown valve 63 is provided on drainpipe 62;Demisting net 61 is tiltedly mounted on the inner wall of cooling separator 6, and multilayer demisting net 61
It is arranged in parallel.
In the device, the size of drying tower 1 not need to be made to very greatly, so as to each on ice cream cone paper complete forming device
A set of present apparatus is installed at position respectively, but if it is desired to each position on ice cream cone paper complete forming device is allowed to be used in conjunction with a set of drying
Device can also use another mode, drying tower 1 is made as large-size, in drying tower 1 with each with gas point 5
Between be additionally provided with buffer tank 51, buffer tank 51 is stored in after compressed air drying, is supplied respectively with gas point 5 from surge tank 51 to each
Gas ensures the drying of each position compressed gas.
It is according to number consecutively clockwise by taking drying tower 1 has 4 reservoir cavities 11 as an example, and by 4 reservoir cavities 11
A, B, C, D, then air bleeding valve 3, air outlet valve 4, regeneration valve 8 and the intake valve 9 being connected with each reservoir cavity A, B, C, D are also corresponding
It numbers, also number is 21A, 21B, 21C, 21D to the breather valve 21 on thermal baffle 2 clockwise.
When device is just started to work, the drier in all reservoir cavity A, B, C, D of drying tower 1 is all effective
, all reservoir cavity A, B, C, D belong to dry section, and at will one in selected reservoir cavity A, B, C, D is passed through compressor 7
The hot compressed air that conveying comes, it is assumed that selected reservoir cavity A, and set gradually counterclockwise renewing zone, cooling zone and
Dry section, then the regeneration valve 8A that the bottoms reservoir cavity A connect are opened, remaining regeneration valve 8B, 8C, 8D are closed, at the top of reservoir cavity A
Connected air bleeding valve 3A is opened, remaining air bleeding valve 3B, 3C, 3D are closed, and the intake valve 9B of the bottoms reservoir cavity B connection is opened,
Remaining intake valve 9A, 9C, 9D are closed, and breather valve 21A, the 21D communicated with reservoir cavity A is closed, remaining breather valve 21B, 21C are beaten
It opens, the air outlet valve 4D connected at the top of reservoir cavity D is opened, remaining air outlet valve 4A, 4B, 4C are closed;It is in this way drying by compressor 7
The hot compressed air that tower 1 provides enters reservoir cavity A through regeneration valve 8A first, is then transported to 6 bottom of cooling separator again,
After hot compressed air enters cooling separator 6, carried out catching mist water removal by demisting net 61, while hot compressed air is cooled down, it is cold
But compressed air is flowed out from the top of cooling separator 6, and reservoir cavity B is entered after intake valve 9B, and compressed air is flowing through
Reservoir cavity C is entered by breather valve 21B after reservoir cavity B, is entered again by breather valve 21C after flowing through reservoir cavity C
Reservoir cavity D is sent to buffer tank 51 after the desiccation that last compressed air passes through reservoir cavity B, C, D by air outlet valve 4D.
When the temperature of reservoir cavity A outer walls is increased to setting value, because compressed air after cooling is at first by storage
Just enter other reservoir cavities C, D after cavity B, so the moisture that the drier in reservoir cavity B absorbs is most, reservoir cavity B
Interior drier reaches saturation at first, cannot reabsorb moisture after saturation, the drier in reservoir cavity B needs again at this time
Raw, i.e., switch valve is using reservoir cavity B as renewing zone;Simultaneously because last be passed through in the reservoir cavity A of hot compressed air
Drier have surplus heat, therefore need cooling compressed air is passed first into reservoir cavity A to the cooling that agent is dried, then
Compressed air is sent into other reservoir cavities C, D again, processing is dried, therefore set reservoir cavity A to cooling zone, storage is empty
Chamber D and C are then set as dry section;Using reservoir cavity B as when renewing zone, switch corresponding valve, i.e., open regeneration valve 8B,
Regeneration valve 8A is closed, and breather valve 21D is opened, and breather valve 21B is closed, and air bleeding valve 3B is opened, and air bleeding valve 3A is closed, and intake valve 9A is beaten
It opens, intake valve 9B is closed, and air outlet valve 4C is opened, and air outlet valve 4D is closed, remaining all valve remains turned-off, in this way, hot compression is empty
Gas enters renewing zone(Reservoir cavity B)The moisture of the drier absorption in reservoir cavity B is taken away, and hot compressed air is sent into cold
But it carries out catching mist water removal in separator 6 and cooling, cooling compressed air is passed into cooling zone(Reservoir cavity A), storage is empty
Drier in chamber A carries out cooling down, and then compressed air enters dry section, and compressed air obtains in reservoir cavity D and C
After good drying, buffer tank 51 is sent to by air outlet valve 4C.
Work as cooling zone(Reservoir cavity A)Desiccant temperature reduce after and renewing zone(Reservoir cavity B)Temperature reaches setting
Value illustrates that the desiccant regeneration in reservoir cavity B is completed, switches corresponding valve at this time, change renewing zone, cooling zone and drying
Area so that hot compressed air initially enters reservoir cavity C(Renewing zone), reservoir cavity B is sent into after supercooling(Cooling zone), pressure
Contracting air sequentially enters reservoir cavity A from reservoir cavity B and reservoir cavity D is dried, and is finally sent to slow by air outlet valve 4D
Deposit tank 51;Similarly, work as cooling zone(Reservoir cavity B)Desiccant temperature reduce after and renewing zone(Reservoir cavity C)Temperature reaches
Setting value, then switch corresponding valve, change renewing zone, cooling zone and dry section so that hot compressed air initially enters storage
Cavity D(Renewing zone), reservoir cavity C is sent into after supercooling(Cooling zone), compressed air sequentially enters storage from reservoir cavity B
Cavity B and reservoir cavity A are dried, and are finally sent to buffer tank 51 by air outlet valve 4A.
Work as cooling zone(Reservoir cavity C)Desiccant temperature reduce after and renewing zone(Reservoir cavity D)Temperature reaches setting
Value, then switch corresponding valve, change renewing zone, cooling zone and dry section so that hot compressed air initially enters reservoir cavity A
(Renewing zone), reservoir cavity D is sent into after supercooling(Cooling zone), compressed air sequentially enters reservoir cavity C from reservoir cavity D
It is dried with reservoir cavity B, is finally sent to buffer tank 51 by air outlet valve 4B;Work as cooling zone(Reservoir cavity D)Drier
After temperature reduces and renewing zone(Reservoir cavity A)Temperature reaches setting value, again switch valve, and reservoir cavity B becomes renewing zone,
Reservoir cavity A becomes cooling zone, so repeats.
It should be noted that when device start-up operation makes, reservoir cavity A is not used as renewing zone, only plays one
The effect of transition, so when compressed air flow direction be then arrive reservoir cavity B 6 from reservoir cavity A to cooling separator, then
To reservoir cavity C, finally arrive reservoir cavity D, and when hereafter reservoir cavity A is as renewing zone, the flow direction of compressed air be exactly from
Then reservoir cavity A arrives reservoir cavity D, then arrive reservoir cavity C, finally arrives reservoir cavity B to cooling separator 6.
Claims (7)
1. the drying device of ice cream cone paper complete forming device compressed gas, including drying tower(1), with gas point(5), cooling separator
(6)And compressor(7), it is characterised in that:The drying tower(1)Inner cavity by polylith thermal baffle(2)Be equally divided into 4 or
4 or more reservoir cavities(11), reservoir cavity(11)It is inside respectively arranged with drier, successively by sequence clockwise or counter-clockwise
By multiple reservoir cavities(11)It is respectively set to renewing zone, cooling zone and dry section, every piece of thermal baffle(2)On be mounted on it is logical
Air valve(21);Each reservoir cavity(11)Bottom bulkhead on connection there are one regeneration valve(8), multiple regeneration valves(8)It is logical
Over-pressed hydraulic piping and compressor(7)Escape pipe be connected, each reservoir cavity(11)Top end socket on connection there are one exhaust
Valve(3), multiple air bleeding valves(3)Pass through pressure pipeline and cooling separator(6)Bottom be connected, cooling separator(6)Top
It is connected with multiple intake valves side by side by pressure pipeline(9), each intake valve(9)With a reservoir cavity(11)Bottom bulkhead
Connection, each reservoir cavity(11)Top end socket on be also connected with there are one air outlet valve(4), all air outlet valves(4)Pass through pressure
Pipeline and use gas point(5)Connection.
2. the drying device of ice cream cone paper complete forming device compressed gas according to claim 1, it is characterised in that:Each storage
Deposit cavity(11)Inner wall on be both provided with temperature monitor(12).
3. the drying device of ice cream cone paper complete forming device compressed gas according to claim 1, it is characterised in that:It is described logical
Air valve(21)It is all made of shut-off valve.
4. the drying device of ice cream cone paper complete forming device compressed gas according to claim 1, it is characterised in that:The row
Air valve(3), air outlet valve(4), regeneration valve(8)And intake valve(9)It is all made of butterfly valve.
5. the drying device of ice cream cone paper complete forming device compressed gas according to claim 1, it is characterised in that:It is described cold
But separator(6)Inside it is provided with multilayer demisting net(61), cooling separator(6)Bottom be provided with drainpipe(62), drainpipe
(62)On be provided with blowdown valve(63).
6. the drying device of ice cream cone paper complete forming device compressed gas according to claim 5, it is characterised in that:It is described to remove
Mist net(61)It is tiltedly mounted on cooling separator(6)Inner wall on, and multilayer demisting net(61)It is arranged in parallel.
7. the drying device of ice cream cone paper complete forming device compressed gas according to claim 1, it is characterised in that:It is described dry
Dry tower(1)With with gas point(5)Between be additionally provided with buffer tank(51).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820011199.1U CN207886935U (en) | 2018-01-04 | 2018-01-04 | The drying device of ice cream cone paper complete forming device compressed gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820011199.1U CN207886935U (en) | 2018-01-04 | 2018-01-04 | The drying device of ice cream cone paper complete forming device compressed gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207886935U true CN207886935U (en) | 2018-09-21 |
Family
ID=63551452
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820011199.1U Expired - Fee Related CN207886935U (en) | 2018-01-04 | 2018-01-04 | The drying device of ice cream cone paper complete forming device compressed gas |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207886935U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112387081A (en) * | 2019-08-16 | 2021-02-23 | 阿特拉斯·科普柯空气动力股份有限公司 | Dryer, compressor installation and method for drying compressed gas |
-
2018
- 2018-01-04 CN CN201820011199.1U patent/CN207886935U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112387081A (en) * | 2019-08-16 | 2021-02-23 | 阿特拉斯·科普柯空气动力股份有限公司 | Dryer, compressor installation and method for drying compressed gas |
CN112387081B (en) * | 2019-08-16 | 2024-02-02 | 阿特拉斯·科普柯空气动力股份有限公司 | Dryer, compressor device and method for drying compressed gas |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101056691B (en) | Method for drying and compressing air and device for using | |
CN203155061U (en) | Compressed air constant pressure purifying system | |
CN104132525A (en) | Powder material drying and cooling integrated device | |
CN207886935U (en) | The drying device of ice cream cone paper complete forming device compressed gas | |
CN104128074B (en) | A kind of compressed air drying adsorption system | |
JP2009508679A (en) | Equipment for drying compressed gas | |
CN207576091U (en) | A kind of zero gas consumption blast heating absorption drier of recovery type heat | |
CN201722353U (en) | Medium-pressure shallow-condensing purification system for oilfield associated gas | |
CN101857812A (en) | Medium-pressure shallow cooling purification system for oilfield associated gas | |
CN105148689A (en) | Adsorption tower for drying compressed air | |
CN102743957A (en) | High temperature oil-containing compressed air waste heat regeneration drying device | |
CN208475491U (en) | A kind of diaphragm type heat tube moisture device | |
CN104128075B (en) | A kind of compressed air drying adsorbent equipment | |
CN201223765Y (en) | Compressed gas residual heat regeneration high-efficient drying mechanism | |
CN101852560A (en) | Pre-cooling type coil heat exchanger used for compressed air drier | |
CN101601959A (en) | A kind of Zero gas consumption low dew point compression heat regeneration absorption compressed air drying method and device thereof | |
CN112050326B (en) | Air conditioning unit for preparing cold air and cold water based on heat pipe-dew point two-stage precooling | |
CN104208988B (en) | The compressed air drier that a kind of window filters | |
CN204865472U (en) | Compressed air drying adsorption tower | |
CN207085645U (en) | A kind of chemical gases drying device | |
CN201342314Y (en) | Compressed air loss-less afterheat drying regenerative device | |
CN206778157U (en) | A kind of waste heat regeneration air drying device | |
CN201493043U (en) | Compression heat regeneration adsorption compressed air dryer with zero air consumption and low dew point | |
CN205598913U (en) | Condensing gas dryer | |
CN217585243U (en) | Drainage device of air pressure air drying tank and air pressure air drying system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180921 Termination date: 20200104 |
|
CF01 | Termination of patent right due to non-payment of annual fee |