CN206119149U - Percolation cylinder burley tobaccoss drying -machine - Google Patents
Percolation cylinder burley tobaccoss drying -machine Download PDFInfo
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- CN206119149U CN206119149U CN201621080067.1U CN201621080067U CN206119149U CN 206119149 U CN206119149 U CN 206119149U CN 201621080067 U CN201621080067 U CN 201621080067U CN 206119149 U CN206119149 U CN 206119149U
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Abstract
The utility model discloses a percolation cylinder burley tobaccoss drying -machine, carry out drying process's drying device including barrel, feed end, discharge end with to the material, the material flows to the discharge end from the feed end, the barrel divide into dry section, cooling space and moisture regain district according to the material flow direction in proper order, the center tube of drying device for making the dry gas body flow through, the center tube runs through dry section, cooling space and moisture regain district, be located center tube lower part evenly distributed in the dry section has dry gas body exhaust bleeder, the bleeder be close to or the material of contact barrel bottom in order to play desiccation. The utility model discloses can carry out drying process to material in the burley tobaccoss production line. The utility model has the advantages of the processing strength reduction, drying rate doubles, and drying time shortens, and equipment is bulky under the same loading and unloading capacity reduces greatly, suit extensively to use widely.
Description
Technical field
This utility model belongs to tobacco equipment technical field, specifically, is related to a kind of percolation cartridge type burley tobaccos dehydrator,
Process can be dried to burley tobaccos production line Leaf, dry section is dried using interior flow-through type, and cooling zone adopts outer percolation
Formula is quickly air-cooled, and moisture regain area realizes uniform moisture regain using harrow nail structure.
Background technology
Burley tobaccos drying plant is one of visual plant in domestic and international tobacco business burley tobaccos production.Commonly use now
Burley tobaccos dehydrator be dried using outer percolation layer paving type, material sends into dryer feeding end by scraper plate feeding machine, feed end
Homogenizing device by its it is loose uniform after, into dry section and be laid in and be dried on carrier bar.In dry section, hot-air first from down to
On through smoked sheet, after from top to bottom pass through smoked sheet.There is series of chemical in smoked sheet, in drying course with during baking
Between increase, the moisture in smoked sheet gradually evaporated, and the moisture with miscellaneous QI for evaporating is discharged to outdoor by blower fan, until being dried
Area exit smoked sheet moisture reaches technological requirement.Smoked sheet from dry section out after, into cooling zone.In cooling zone, using relatively low
The circulated air of temperature makes smoked sheet temperature be down between 35 DEG C～45 DEG C, and for smoked sheet moisture regain process conditions are provided.Last smoked sheet passes through
Longer moisture regain passage.It is first from top to bottom, then from the bottom to top, last to be from top to bottom blown atomized water and steam, thing again in operation
Material is fully absorbed after heat and moisture, delivers to discharge end.
Existing burley tobaccos drying plant service aisle is very long, close 28 meters, and baking temperature is high, and drying time is long, adopts in addition
Cause energy resource consumption larger with percolation outside hot blast.
Therefore, materials quality after being dried is improved, processing intensity is reduced, is improved work efficiency, reduces equipment volume and reduction
Energy resource consumption is always the research topic of burley tobaccos drying plant manufacturer.
In view of this it is special to propose this utility model.
Utility model content
The technical problems to be solved in the utility model is to overcome the deficiencies in the prior art, there is provided one kind can lift drying
Afterwards burley tobaccos quality, improve work efficiency and reduce energy resource consumption percolation cartridge type burley tobaccos dehydrator.
To solve above-mentioned technical problem, this utility model is using the basic conception of technical scheme：
This utility model provides a kind of percolation cartridge type burley tobaccos dehydrator, including cylinder, feed end, discharge end and to material
Withering drying device, material flows from feed end to discharge end, and the cylinder is divided successively by Flow of Goods and Materials direction
For dry section, cooling zone and moisture regain area；The drying device is the central canal that dry gas can be made to flow through, and the central canal is passed through
Wear dry section, cooling zone and moisture regain area；Central canal bottom in the dry section is evenly distributed with discharges dry gas
Branched pipe, the branched pipe comes close to or in contact with the material of cylinder body bottom to play desiccation.
Further, the dry section includes the first dry section and the second dry section, in first dry section
The bottom of heart pipe is evenly distributed with along its length at least row's branched pipe.
Further, also including the second central canal, second central canal is set on portion centers pipe, the second central canal
It is arranged to form the gap flow through for dry gas with central canal；Grow along it the bottom of the central canal in second dry section
Degree direction is evenly distributed with least row's branched pipe；
Wherein, portion centers pipe is through the second dry section, cooling zone and returns intertidal central canal.
Further, also including the first hot-air system and the second hot-air system, first hot-air system and the second hot blast
System corresponds to respectively the temperature and concentration of dry gas in the first dry section of control and the second dry section.
Further, the branched pipe on the central canal and central canal be into 70 °～90 ° angles, on second central canal
Branched pipe and the second central canal into 70 °～90 ° angles.
Further, the end at the on-fixed end of the branched pipe is provided with dry gas spout, the dry gas spout
Bore be not more than the caliber of branched pipe；The dry gas spout be shaped as duckbill either cone or cylinder.
Further, outer percolation ventilating system is provided with the cooling zone, for the relatively low process gas of temperature to be made
Temperature of charge is set to meet process conditions on the material of inner barrel.
Further, harrow nail structure and humidification system are provided with the moisture regain area, the humidification system sprays including steam
Mouth.
Further, the cylinder and central canal are obliquely installed towards the direction of discharge end, cylinder and central canal axial line
With horizontal line into 0 °～10 ° angles.
Further, the cylinder is rotatable, and central canal and branched pipe be not with barrel body rotation.
After above-mentioned technical proposal, this utility model has the advantages that compared with prior art.
This utility model can be dried process to burley tobaccos production line Leaf.Dry section is dried using interior flow-through type,
Cooling zone is quickly air-cooled using outer flow-through type, and moisture regain area realizes uniform moisture regain using harrow nail structure.This utility model with it is traditional
Burley tobaccos dehydrator is compared, and processes intensity decreases, and dry rate is doubled, and drying time shortens, equipment under same production capacity
Volume is greatly reduced, and is suitably widely popularized and is used.
Specific embodiment of the present utility model is described in further detail below in conjunction with the accompanying drawings.
Description of the drawings
Accompanying drawing is further understood from, this practicality for providing as a part of the present utility model to of the present utility model
New schematic description and description is used to explain this utility model, but does not constitute to improper restriction of the present utility model.
Obviously, drawings in the following description are only some embodiments, to those skilled in the art, are not paying creation
Property work on the premise of, can be obtaining other accompanying drawings according to these accompanying drawings.In the accompanying drawings：
Fig. 1 is a kind of schematic diagram of percolation cartridge type burley tobaccos dehydrator in this utility model embodiment；
Fig. 2 is the structural representation that branched pipe is attached to central canal bottom in this utility model embodiment；
Fig. 3 is the side structure schematic diagram that branched pipe is attached to central canal bottom in this utility model embodiment；
Fig. 4 is the structural representation of the conical nozzle of branched pipe in this utility model embodiment；
Fig. 5 is the side structure schematic diagram of the duckbill spout of branched pipe in this utility model embodiment；
Fig. 6 is the structural representation of the cylindrical spout of branched pipe in this utility model embodiment.
In figure：1st, feed end；2nd, the first moisture discharge device；3rd, cylinder；4th, central canal；5th, the second central canal；6th, branched pipe；7、
Second moisture discharge device；8th, outer percolation ventilating system；9th, humidification system；10th, discharge end；11st, supporting leg；12nd, the second hot-air system；
13rd, the first hot-air system；14th, driving means；15th, managing and control system；A, dry section；A1, the first dry section；A2, the second dry section；
B, cooling zone；C, moisture regain area.
It should be noted that these accompanying drawings and word description are not intended as limiting design of the present utility model by any way
Scope, but be that those skilled in the art illustrate concept of the present utility model by reference to specific embodiment.
Specific embodiment
It is new below in conjunction with this practicality to make purpose, technical scheme and the advantage of this utility model embodiment clearer
Accompanying drawing in type embodiment, is clearly and completely described to the technical scheme in embodiment, and following examples are used to illustrate this
Utility model, but it is not limited to scope of the present utility model.
In description of the present utility model, it should be noted that term " on ", D score, "front", "rear", "left", "right",
The orientation or position relationship of the instruction such as " vertical ", " interior ", " outward " be based on orientation shown in the drawings or position relationship, merely to
It is easy to describe this utility model and simplifies description, rather than indicates or imply that the device or element of indication there must be specific side
Position, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.
In description of the present utility model, it should be noted that unless otherwise clearly defined and limited, term " peace
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected, or be detachably connected, or integratedly
Connection；Can be mechanically connected, or electrically connect；Can be joined directly together, it is also possible to be indirectly connected to by intermediary.
For the ordinary skill in the art, above-mentioned term specifically containing in this utility model can be understood with concrete condition
Justice.
The material that this utility model is mentioned can be understood as any one in smoked sheet, tobacco shred or stem.
As shown in Figures 1 to 6, this utility model provides a kind of percolation cartridge type burley tobaccos dehydrator, including cylinder 3, charging
Hold 1, discharge end 10 and to the withering drying device of material, material flows from feed end 1 to discharge end 10, the cylinder
Body 3 is divided into dry section A, cooling zone B and moisture regain area C by Flow of Goods and Materials direction；The drying device is dried gas to make
The central canal 4 that body flows through, the central canal 4 is through dry section A, cooling zone B and moisture regain area C；In in the dry section A
The bottom of heart pipe 4 is evenly distributed with the branched pipe 6 for discharging dry gas, and the branched pipe 6 comes close to or in contact with the thing of the bottom of cylinder 3
Expect to play desiccation.Dry gas are ejected into the bottom of cylinder 3 from the branched pipe 6 of the bottom of central canal 4 in this utility model
On material, material strong movements are made, it is ensured that the full contact between dry gas and material, so as to reach the sufficient mesh of drying
's.
Embodiment one
Not shown in figure, a kind of percolation cartridge type burley tobaccos dehydrator described in the present embodiment, including cylinder 3, feed end 1,
Discharge end 10 and to the withering drying device of material, the feed end 1 is located at the side of cylinder 3, discharge end 10
In the opposite side of cylinder 3.Material flows from feed end 1 to discharge end 10, and the dehydrator is divided into by Flow of Goods and Materials direction
Dry section A, cooling zone B and moisture regain area C.The drying device is the central canal 4 that dry gas can be made to flow through, the central canal
4 through dry section A, cooling zone B and moisture regain area C.The two ends of central canal 4 are respectively and fixedly installed on feed end 1 and discharge end 10,
The dry gas entrance of central canal 4 is arranged on discharge end 10.The bottom of central canal 4 positioned at dry section A is equal along its length
Even that at least row's branched pipe 6 is distributed with, the branched pipe 6 comes close to or in contact with the material of the bottom of cylinder 3 to play desiccation.Such as
Shown in Fig. 2, branched pipe 6 is uniformly distributed along the length direction of central canal 4, and the circumferencial direction along central canal 4 is then mainly concentrated
It is centrally located on the periphery relative with the bottoms material of cylinder 3 of the bottom of pipe 4.Such as Fig. 3, central canal 4 and branched pipe 6 are shown
Side view, from terms of side view, branched pipe 6 is in the bottom of central canal 4 in fan-shaped distribution, so, the dry gas energy in central canal 4
It is enough to be injected in by different directions on the material of the bottom of cylinder 3 in branched pipe 6 so that material can sufficiently and dry gas
Come in contact, so as to obtain dried.
In the present embodiment, moisture discharge device is provided between dry section A and cooling zone B, for material in dry section A to be dried
Moisture afterwards is discharged outside cylinder 3.In the present embodiment, the humidity discharging of moisture discharge device can be using suitable, adverse current switching or while work.
In the present embodiment, outer percolation ventilating system 8 is provided with the B of cooling zone, the outer percolation ventilating system 8 has for inside
The screen drum of mesh structure, for from outside cylinder 3 through the screen drum and the relatively low dry gas of temperature to be applied to into material,
So that temperature of charge is reduced to standard temperature, so as to provide process conditions for follow-up material moisture regain.Rake is provided with moisture regain area C
Pin structure and humidification system 9, the humidification system 9 includes steam nozzle.Uniformly sprayed water on material using steam nozzle, make thing
Material reaches the moisture of technological requirement, so as to realize the purpose of uniform moisture regain.
In order that the material of the bottom of cylinder 3 is more stable sliding towards the discharge end 10 of cylinder 3 glibly.In the present embodiment, a side
Face, cylinder 3 and central canal 4 are obliquely installed towards the direction of discharge end 10.Preferably, cylinder 3 and the axial line of central canal 4 and horizontal line
Into 0 °～10 ° angles.On the other hand, the central canal 4 and 6 one-tenth of branched pipe, 70 °～90 ° angles, from the drying that branched pipe 6 is discharged
Gas to the bottom of cylinder 3 material provide an active force towards the direction of discharge end 10 so that material inside cylinder 3 glibly
Slide.This cylinder 3 be obliquely installed and central canal 4 and branched pipe 6 between appropriate angle arrange, both can guarantee that material was smooth
Slip, can guarantee that again material slide speed be unlikely to too fast.Material is same by abundant dry, sufficiently cool and uniform moisture regain
When, smoothly can discharge from discharge end 10 again.
Embodiment two
As shown in figure 1, a kind of flow-through type burley tobaccos dehydrator described in the present embodiment, mainly by cylinder 3, drying device,
Moisture discharge device, chiller and conditioning device composition.Cylinder 3 is arranged on supporting leg 11, and the side of cylinder 3 is the feed end of material
1, opposite side is the discharge end 10 of material, and material flows from feed end 1 to discharge end 10.The cylinder 3 presses Flow of Goods and Materials direction
Dry section A, cooling zone B and moisture regain area C are divided into, the process of the drying, cooling and moisture regain of material is completed.Wherein, it is dried dress
The central canal 4 that dry gas can be made to flow through is set to, the second central canal 5, second central canal 5 are arranged with the central canal 4
It is arranged to form certain gap with central canal 4.One end of second central canal 5 is fixed on central canal 4, and the other end is fixed on
On discharge end 10.One end of the central canal 4 is fixedly mounted on feed end 1, and the other end is fixedly mounted on discharge end 10, is gone out
Material is provided with dry gas entrance on end 10.Dry gas carry out the central canal 5 of central canal 4 and second by dry gas entrance
It is interior, complete follow-up to be dried work.
In the present embodiment, the dry section A includes the first dry section A1 and the second dry section A2, and the first dry section A1 is close
Feed end 1, the second dry section A2 is near cooling zone B.Second central canal 5 runs through the second dry section A2, cooling zone B and moisture regain area C,
Second central canal 5 is just the demarcation line of the first dry section A1 and the second dry section A2 with the junction of central canal 4.Positioned at first
The bottom of the central canal 4 in dry section A1 is evenly distributed with along its length at least row's branched pipe 6, and the branched pipe 6 is leaned on
Near or contact cylinder 3 bottom material is playing desiccation.The bottom edge of the second central canal 5 in the second dry section A2
Its length direction is evenly distributed with least row's branched pipe 6, and the branched pipe 6 comes close to or in contact with the material of the bottom of cylinder 3 to rise
To desiccation.As shown in Fig. 2 the branched pipe 6 on central canal 4 is uniformly distributed along the length direction of central canal 4, and along center
The circumferencial direction of pipe 4 then main integrated distribution on the periphery relative with the bottoms material of cylinder 3 of the bottom of central canal 4.In second
Branched pipe 6 on heart pipe 5 is also same distribution.Such as Fig. 3, the side view of central canal 4 and branched pipe 6 is shown, from side view
See, in the bottom of central canal 4 in fan-shaped distribution, so, the dry gas in central canal 4 can lead to branched pipe 6 in branched pipe 6
Cross different directions to be injected on the material of the bottom of cylinder 3 so that material sufficiently can come in contact with dry gas, so as to
To dried.In the same manner, as the second central canal 5 is also with the side view of branched pipe 6 thereon.
In the present embodiment, the bottom of cylinder 3 is provided with the first hot-air system 13 and the second hot-air system 12, the first hot-air system
The temperature and flow of the dry gas of the central canal 4 in 13 the first dry section A1 of control.The control second of second hot-air system 12 is dry
The temperature and flow of the dry gas of the second central canal 5 in dry area A2.For example：When needs are in the first dry section A1
When material carries out the drying and processing of high temperature, first hot-air system 13 can be to the dry of the central canal 4 in the first dry section A1
Dryness body is heated to preset temperature, when reaching preset temperature, stops the heating to dry gas.Likewise, when needs are to being in
When material in second dry section A2 carries out the drying and processing of low temperature, second hot-air system 12 can be to the second dry section A2
The dry gas of the second interior central canal 5 are heated to preset temperature, and when reaching the preset temperature, stopping adds to dry gas
Heat.The dried of different temperatures is carried out to material using two different dry sections, the material moisture flowed out from dry section A is made
Technological requirement is reached, also process conditions is provided for follow-up cooling moisture regain.
The moisture discharge device includes the first moisture discharge device 2 and the second moisture discharge device 7, and the front end of cylinder 3 is provided with the first humidity discharging
Device 2, for material in the first dry section A1 to be discharged outside cylinder 3 by dried moisture.Second dry section A2 and cooling
The second moisture discharge device 7 is provided between area B, for material in the second dry section A2 to be discharged outside cylinder 3 by dried moisture.
In the present embodiment, the humidity discharging of the first moisture discharge device 2 and the second moisture discharge device 7 can be using suitable, adverse current switching or while work.
In the present embodiment, outer percolation ventilating system 8 is provided with the B of cooling zone, the outer percolation ventilating system 8 has for inside
The screen drum of mesh structure, for from outside cylinder 3 through the screen drum and the relatively low dry gas of temperature to be applied to into material,
So that temperature of charge is reduced to standard temperature, so as to provide process conditions for follow-up material moisture regain.Rake is provided with moisture regain area C
Pin structure and humidification system 9, the humidification system 9 includes steam nozzle.Uniformly sprayed water on material using steam nozzle, make thing
Material reaches the moisture of technological requirement, so as to realize the purpose of uniform moisture regain.
In order that the material of the bottom of cylinder 3 is more stable sliding towards the discharge end 10 of cylinder 3 glibly.In the present embodiment, a side
Face, cylinder 3 and central canal 4 are obliquely installed towards the direction of discharge end 10.Preferably, cylinder 3 and the axial line of central canal 4 and horizontal line
Into 0 °～10 ° angles.On the other hand, the branched pipe 6 on the central canal 4 and 4 one-tenth of central canal, 70 °～90 ° angles, described second
6 and second 5 one-tenth of central canal of branched pipe, 70 °～90 ° angles on central canal 5.Dry gas from the discharge of branched pipe 6 are to cylinder 3
The material of bottom provides an active force towards the direction of discharge end 10 so that material slides glibly inside cylinder 3.This cylinder
Body 3 be obliquely installed and central canal 4 and branched pipe 6 between appropriate angle arrange, both can guarantee that the smooth slip of material, and energy
Ensure that the speed that material slides is unlikely to too fast.Material, and can be steadily by fully drys, sufficiently cool and while uniformly get damp again
Discharge from discharge end 10 on ground.
In the present embodiment, also including driving means 14, the driving means 14 drive cylinder 3 to rotate around the axial line of cylinder 3.
When cylinder 3 is rotated, central canal 4, the second central canal 5 and branched pipe 6 are not rotated with cylinder 3.Cylinder 3 turns around the axial line of cylinder 3
Kinetic energy enough makes Nicotiana tabacum L. sufficiently contact with the dry gas stream ejected from branched pipe 6, and drying effect becomes apparent from.
In the present embodiment, the work process of burley tobaccos dehydrator is as follows：
Need to be dried material, get damp again process when, start dehydrator, cylinder 3 starts to rotate.Managing and control system 15 is controlled
Blower fan and heat exchanger are operated, and carry out heat exchange to obtain dry gas (for example with air：Hot blast or superheated steam).Wind
Dry gas are delivered to discharge end 10 by machine, and dry gas respectively enter the He of central canal 4 from the dry gas entrance of discharge end 10
In second central canal 5.When the temperature in the second central canal 5 reaches preset temperature, the control material of managing and control system 15 is from feed end 1
Into inside cylinder 3, material due to the effect of self gravitation, all the time in the bottom of cylinder 3, because cylinder 3 is rotated, material with
Cylinder 3 rotates and rolling agitation occurs, so as to completely attach to the dry gas discharged from branched pipe 6 so that material is filled
The dried divided.The material entered from feed end 1 is contacted and done with the high-temperature dry air discharged from central canal 4 first
Dry process, then contacts and obtains further dried with the cold drying gas discharged from the second central canal 5, due to
Temperature in two central canals 5 is less than the temperature in central canal 4 so that after material is contacted with the dry gas in the second central canal 5
Temperature is reduced, and is that follow-up cooling is prepared.In the dry run for carrying out material, the flow direction phase of dry gas stream and material
Instead, more it is proximate to the dry gas speed maximum that the branched pipe 6 of feed end 1 is discharged.The dry gas discharged from branched pipe 6 and cylinder
The tobacco of the bottom of body 3 is fully contacted, and material occurs a series of chemical reaction, with drying time in dry run
Increase, the moisture in material gradually evaporated, and the moisture with miscellaneous QI for evaporating is by the first moisture discharge device 2 and second row
Damp device 7 discharges cylinder 3.After being fully dried in the dry section A, Flow of Goods and Materials to cooling zone B, by cooling zone B in outer wear
It is quickly air-cooled that circulation wind system 8 carries out outer flow-through type to the material of the bottom of cylinder 3, and moisture regain area C is entered back into afterwards, in moisture regain area C
Pass through discharge end 10 after interior uniform moisture regain again to discharge outside cylinder 3.
In the present embodiment, as shown in Figures 4 to 6, the end at the on-fixed end of the branched pipe 6 is provided with dry gas spray
Mouthful, the bore of the dry gas spout is not more than the caliber of branched pipe 6；The dry gas spout be shaped as duckbill or
Person's cone or cylinder.So, it is ensured that dry gas spray and improve the speed that dry gas spray towards specified direction.
The above is only preferred embodiment of the present utility model, not makees any pro forma to this utility model
Limit, although this utility model is disclosed above with preferred embodiment, but is not limited to this utility model, it is any to be familiar with
The technical staff of this patent in the range of without departing from technical solutions of the utility model, when using above-mentioned prompting technology contents make
Go out a little change or be modified to the Equivalent embodiments of equivalent variations, as long as being the content without departing from technical solutions of the utility model,
Any simple modification, equivalent variations and the modification made to above example according to technical spirit of the present utility model, still belongs to
In the range of this utility model scheme.
Claims (10)
1. a kind of percolation cartridge type burley tobaccos dehydrator, including cylinder (3), feed end (1), discharge end (10) and material is done
The drying device of dry process, material flows from feed end (1) to discharge end (10), the cylinder (3) by Flow of Goods and Materials direction according to
It is secondary to be divided into dry section (A), cooling zone (B) and moisture regain area (C)；It is characterized in that：The drying device is can to make dry gas
The central canal (4) for flowing through, the central canal (4) is through dry section (A), cooling zone (B) and moisture regain area (C)；Positioned at the drying
Central canal (4) bottom in area (A) be evenly distributed with by dry gas discharge branched pipe (6), the branched pipe (6) near or
The material of cylinder (3) bottom is contacted to play desiccation.
2. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 1, it is characterised in that：Dry section (A) bag
Include the first dry section (A1) and the second dry section (A2), positioned at first dry section (A1) central canal (4) bottom along it
Length direction is evenly distributed with least row's branched pipe (6).
3. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 2, it is characterised in that：Also include the second central canal
(5), second central canal (5) is set on portion centers pipe (4), and the second central canal (5) is arranged to form confession with central canal (4)
The gap that dry gas flow through；The bottom of the second central canal (5) in second dry section (A2) is along its length
It is evenly distributed with least row's branched pipe (6)；
Wherein, portion centers pipe (4) is through the central canal in the second dry section (A2), cooling zone (B) and moisture regain area (C)
(4)。
4. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 3, it is characterised in that：Also include the first hot blast system
System (13) and the second hot-air system (12), first hot-air system (13) and the second hot-air system (12) are corresponding respectively to control the
The temperature and flow of one dry section (A1) and the interior dry gas of the second dry section (A2).
5. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 4, it is characterised in that：On the central canal (4)
Branched pipe (6) and central canal (4) into 70 °～90 ° angles, the branched pipe (6) on second central canal (5) and the second center
Pipe (5) is into 70 °～90 ° angles.
6. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 5, it is characterised in that：The branched pipe (6)
The end at on-fixed end is provided with dry gas spout, and the bore of the dry gas spout is not more than the caliber of branched pipe (6)；Institute
That states dry gas spout is shaped as duckbill either cone or cylinder.
7. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 1, it is characterised in that：In the cooling zone (B)
Outer percolation ventilating system (8) is provided with, is made for the relatively low dry gas of temperature to be acted on the internal material of cylinder (3)
Temperature of charge meets process conditions.
8. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 1, it is characterised in that：In the moisture regain area (C)
Harrow nail structure and humidification system (9) are provided with, the humidification system (9) is including steam nozzle.
9. according to a kind of arbitrary described percolation cartridge type burley tobaccos dehydrator of claim 1-8, it is characterised in that：The cylinder
(3) be obliquely installed with direction of the central canal (4) towards discharge end (10), cylinder (3) and central canal (4) axial line and horizontal line into
0 °～10 ° angles.
10. a kind of percolation cartridge type burley tobaccos dehydrator according to claim 9, it is characterised in that：The cylinder (3) can turn
Move, central canal (4) and branched pipe (6) are not rotated with cylinder (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621080067.1U CN206119149U (en) | 2016-09-26 | 2016-09-26 | Percolation cylinder burley tobaccoss drying -machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621080067.1U CN206119149U (en) | 2016-09-26 | 2016-09-26 | Percolation cylinder burley tobaccoss drying -machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206119149U true CN206119149U (en) | 2017-04-26 |
Family
ID=58569949
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621080067.1U Active CN206119149U (en) | 2016-09-26 | 2016-09-26 | Percolation cylinder burley tobaccoss drying -machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206119149U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106307598A (en) * | 2016-09-26 | 2017-01-11 | 秦皇岛烟草机械有限责任公司 | Crossflow cylinder type burley tobacco drying machine |
-
2016
- 2016-09-26 CN CN201621080067.1U patent/CN206119149U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106307598A (en) * | 2016-09-26 | 2017-01-11 | 秦皇岛烟草机械有限责任公司 | Crossflow cylinder type burley tobacco drying machine |
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