CN206410432U - A kind of tower cross-flow drying equipment of novel energy-conserving - Google Patents
A kind of tower cross-flow drying equipment of novel energy-conserving Download PDFInfo
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- CN206410432U CN206410432U CN201621215711.1U CN201621215711U CN206410432U CN 206410432 U CN206410432 U CN 206410432U CN 201621215711 U CN201621215711 U CN 201621215711U CN 206410432 U CN206410432 U CN 206410432U
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- tower
- drier
- drying equipment
- hot air
- novel energy
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- 238000001035 drying Methods 0.000 title claims abstract description 45
- 238000007664 blowing Methods 0.000 claims description 21
- 238000007599 discharging Methods 0.000 claims description 10
- 238000009423 ventilation Methods 0.000 claims description 9
- 230000006698 induction Effects 0.000 claims description 7
- 239000000428 dust Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 abstract description 19
- 238000012384 transportation and delivery Methods 0.000 abstract description 8
- 208000011580 syndromic disease Diseases 0.000 abstract description 2
- 238000001704 evaporation Methods 0.000 description 18
- 230000008020 evaporation Effects 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 18
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000012216 screening Methods 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000005325 percolation Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 244000089698 Zanthoxylum simulans Species 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000011265 semifinished product Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
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- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a kind of tower cross-flow drying equipment of novel energy-conserving, it is related to a kind of drying equipment, the tower cross-flow drying equipment of particularly a kind of novel energy-conserving, including tower hot air through drier, the charging aperture of tower hot air through drier is provided with distributing device, the level detector for detecting the thickness that the bed of material enters in tower hot air through drier is provided with the inwall on the top of tower hot air through drier.Compared with prior art, tower cross-flow drying equipment of the present utility model passes through stable thickness of feed layer and uniform hot blast, each material is set to be heated identical, avoid traditional rower drier uneven drying phenomenon, the material dried for a long time is needed to reach the purpose stopped for a long time in machine by adjusting delivery rate and thickness of feed layer to low wind-warm syndrome of big stem tuber etc..
Description
Technical field
The utility model is related to a kind of drying equipment, the tower cross-flow drying equipment of particularly a kind of novel energy-conserving.
Background technology
There are a variety of drying equipments, including tower type drying apparatus, belt drying equipment, cabinet type drying equipment in the prior art
And fluidized bed drying equipment, applicable field also widely, such as：Corn, paddy rice, Chinese prickly ash, tealeaves in agricultural byproducts
Drying (cooling)；Coal briquette, ore, grain crystalline thing, the drying (cooling) for finished product of pelletizing in coal chemical industry；Doctor
The drying (cooling) of the product after the semi-finished product after Chinese medicine material, boiling, granulation in medicine industry.But in actual applications, pass through
Often occur that drying is insufficient uneven, the problems such as inefficiency.
Application No. CN201310540245.9 patent of invention discloses a kind of fermented feed drying system, and the patent will
Pipe drier and rower drier combine there is provided a kind of drying efficiency is high and fermented feed activity can be kept be
System.Fresh fermented feed and obtain mix after feeder is entered and uniform by the fermented feed tentatively dried, subsequently into
Pipe drier carries out preliminarily dried, enters back into screening conveying equipment and is sieved, oversize reenters feeder, screenings
It is dried from top to bottom into rower drier, air is by becoming hot blast and from lower entrance tower drying after air heater
Machine and screenings carry out pressure regeneration, after enter cyclone separator from top.But material enter rower drier in by
In the phenomenon that too fast and blocking entrance occurs from top to bottom, and hot blast from lower entrance rower drier when wind also occurs
Uneven phenomenon, so as to cause to dry insufficient or uneven situation.
Utility model content
The purpose of this utility model is：The tower cross-flow drying for providing a kind of more preferable novel energy-conserving of drying effect is set
It is standby.
To reach above-mentioned purpose, the technical solution adopted in the utility model is as follows：
A kind of tower cross-flow drying equipment of novel energy-conserving, including tower hot air through drier, it is characterised in that：Worn tower
Flow drying machine charging aperture at be provided with distributing device, be provided with the inwall on the top of tower hot air through drier for detect into
Enter the level detector of the thickness of feed layer in tower hot air through drier.
It is preferred that, charging Blowing stopper is connected with above described charging aperture, the distributing device includes feed pipe, feed pipe
Bottom is connected with passage, and feed pipe is connected with charging Blowing stopper.
It is preferred that, the passage is provided with multigroup, and multigroup passage is along the circumferentially distributed of feed pipe.
It is preferred that, the passage is inclined on feed pipe, and the angle of the axis of passage and feed pipe is arrived at 20 °
Between 70 °.
It is preferred that, the level detector includes being provided with fix bar and leading-off rods at the top of induction end, induction end, fix bar
Top is welded on the top of tower hot air through drier.
It is preferred that, ventilation terminal, hot wind inlet pipe are provided with the pipeline of the hot wind inlet pipe of the tower hot air through drier
It is connected by airduct with air-heater.
It is preferred that, charging Blowing stopper is connected with above the charging aperture of the tower hot air through drier, the tower percolation is dry
Hot-blast outlet is provided with the top of dry machine, charging aperture is connected with feeding the bottom of Blowing stopper, is connected with the top of charging Blowing stopper
Feed hopper；The bottom of the tower hot air through drier is provided with hot wind inlet pipe and discharging opening, and discharge outlet is welded with discharging and closed
Blower fan.
It is preferred that, it is connected with cyclone dust collectors at the hot-blast outlet of the tower hot air through drier.
It is preferred that, the discharging Blowing stopper bottom is provided with conveying device.
In summary, by adopting the above-described technical solution, the beneficial effects of the utility model are：
The utility model is provided with distributing device and level detector on tower hot air through drier, and material is after upper entrance distributing device
Shunted, so as to uniformly spread out, passed signal by lead-out wire after level detector detection material thickness of feed layer by passage
Go out, so as to control the speed into the material of tower hot air through drier so that material can separate thermally equivalent, low to big stem tuber
Wind-warm syndrome etc. needs the material dried for a long time to reach the mesh stopped for a long time in machine by adjusting delivery rate and thickness of feed layer
's.
The utility model is provided with ventilation terminal on the pipeline of the hot wind inlet pipe of tower hot air through drier, and hot blast is by hot blast
Enter ventilation terminal through airduct after machine blowout, enter tower hot air through drier after being shunted in ventilation terminal so that hot blast is worn tower
It is evenly distributed in stream drying machine, and due to the space formed without running gear, hot blast will not form band drier and cabinet type
" hot blast short circuit " phenomenon of drying machine, therefore heat is fully utilized and efficient.
Brief description of the drawings
Fig. 1 is a kind of Facad structure figure of the tower cross-flow drying equipment of novel energy-conserving of the utility model；
Fig. 2 is left view；
Fig. 3 is top view；
Fig. 4 is distributing device structure chart；
Fig. 5 is level detector structure chart；
Marked in figure：1- feed hoppers；2- feeds Blowing stopper；3- cyclone dust collectors；4- hot-blast outlets；The tower cross-flow dryings of 5-
Machine；6- hot wind inlet pipes；7- discharging Blowing stoppers；8- air-heaters；9- conveying devices；10- ventilation terminals；11- distributing devices；1101- enters
Expects pipe；1102- passages；12- level detectors；1201- fix bars；1202- induction end；1203- leading-off rods.
Embodiment
Team's the utility model is further described below in conjunction with the accompanying drawings.
As shown in figure 1, a kind of tower cross-flow drying equipment of novel energy-conserving described by the utility model, it mainly includes
Tower hot air through drier 5, it is characterised in that：Distributing device 11 is provided with the charging aperture of tower hot air through drier 5, is worn tower
The level detector 12 for detecting thickness of feed layer is provided with the inwall on the top for flowing drying machine 5.
Charging Blowing stopper 2 is connected with above the charging aperture of tower hot air through drier 5 described above, the distributing device 11 includes
Feed pipe 1101, the bottom of feed pipe 1101 is connected with the lower end that charging Blowing stopper 2 is placed in passage 1102, charging aperture 1101
And by being welded and fixed.Distributing device 11 reduces the operating cost of system using unpowered.
Above-mentioned passage 1102 is provided with multigroup, and multigroup passage 1102 is along the circumferentially distributed of feed pipe 1101.It is multigroup
Passage 1102 is circumferentially distributed along feed pipe 1101 so that material be able to can disperse when entering tower hot air through drier 5
Come.
Above-mentioned passage 1102 is inclined on charging aperture 1101, the folder of passage 1102 and the axis of feed pipe 1101
Angle is between 20 ° to 70 °.Passage 1102 forms an angle with the shape of feed pipe 1101 so that material can uniformly pave in blanking
On machine orifice plate.
Above-mentioned level detector 12 includes induction end 1202, and the top of induction end 1202 is provided with fix bar 1201 and leading-off rods
1203, the top of fix bar 1201 is welded on the top of tower hot air through drier 5, and the top of leading-off rods 1203 passes through electric wire and material
Machine is connected.Level detector 12 is set in tower hot air through drier 5 so that thickness of feed layer is controlled batcher by level detector and carried out certainly
Dynamic adjustment, with stable in tolerance.
Ventilation terminal 10 is provided with the hot wind inlet pipe 6 of above-mentioned tower hot air through drier 5, hot wind inlet pipe 6 passes through airduct
It is connected with air-heater 8.Hot blast is uniformly moved from bottom to top under the effect of air-heater 8 by bottom through ventilation terminal 10, and due to without fortune
The space of rotation member formation, hot blast will not be formed " the hot blast short circuit phenomenon " of band drier and cabinet type drying machine, therefore heat
It is fully utilized and efficient.
Charging Blowing stopper 2, the tower hot air through drier 5 are connected with above the charging aperture of above-mentioned tower hot air through drier 5
Top be provided with hot-blast outlet 4, charging aperture is connected with feeding the bottom of Blowing stopper 2, feed Blowing stopper 2 top be connected with into
Hopper 1；The bottom of the tower hot air through drier 5 is provided with hot wind inlet pipe 6 and discharging opening, and discharge outlet is welded with discharging and closed
Blower fan 7.Hot blast is forced through material gap to flow through the purpose that surface of material reaches strong convection heat exchange at a high speed, thus makes the machine
With higher high efficiency.
Cyclone dust collectors 3 are connected with the hot-blast outlet 4 of above-mentioned tower hot air through drier 5.Rotation is connected with hot-blast outlet 4
Wind deduster 3 so that hot blast is discharged after treatment, it is therefore prevented that the pollution to environment.
The above-mentioned bottom of discharging Blowing stopper 7 is provided with conveying device 9.
In use, select according to actual needs after corresponding size, it would be desirable to which dry material is from upper end
Feed hopper 1 is put into, and opens air-heater 8, and material is dry into tower percolation by distributing device 11 through feeding Blowing stopper 2 from feed hopper 1
Dry machine 5, and thickness is adjusted by level detector 12, hot blast passes through hot wind inlet pipe from air-heater 8s through airduct and ventilation terminal 10
6 enter tower hot air through drier 5, and material carries out surface forced-convection heat transfer with hot blast in tower hot air through drier 5, so as to reach
To dry purpose, material reaches conveying device 9 through the light blower fan 7 that discharges later, and hot blast enters cyclone dust collectors from hot-blast outlet 4
3。
Embodiment of the present utility model includes but is not limited to the following example：
Embodiment one
From the tower hot air through drier of HGT800, mechanical dimensions (the long wide * of * are high) are 840mm*960mm*2650mm, main frame
Capacity is 3Kw (being free of blower fan), and 20 DEG C of fan deliveries are 1300Kg/h, and 120 DEG C of hot blast water evaporation quantities are 30 --- 40Kg,
220 DEG C of hot blast water evaporation quantities are 60 --- 80Kg, 400 DEG C of hot blast water evaporation quantities are 100 --- 140Kg.
Embodiment two
From the tower hot air through drier of HGT1000, mechanical dimensions (the long wide * of * are high) are 1260mm*1450mm*3800mm, main
Machine capacity is 3.7Kw (being free of blower fan), and 20 DEG C of fan deliveries are 3600Kg/h, and 120 DEG C of hot blast water evaporation quantities are 70 ---
90Kg, 220 DEG C of hot blast water evaporation quantities are 140 --- 180Kg, 400 DEG C of hot blast water evaporation quantities are 240 --- 280Kg.
Embodiment three
From the tower hot air through drier of HGT1200, mechanical dimensions (the long wide * of * are high) are 1480mm*17200mm*4600mm,
Host capacity is 5.4Kw (being free of blower fan), and 20 DEG C of fan deliveries are 5600Kg/h, and 120 DEG C of hot blast water evaporation quantities are 120 ---
150Kg, 220 DEG C of hot blast water evaporation quantities are 240 --- 280Kg, 400 DEG C of hot blast water evaporation quantities are 390 --- 450Kg.
Example IV
From the tower hot air through drier of HGT1600, mechanical dimensions (the long wide * of * are high) are 1920mm*2130mm*5800mm, main
Machine capacity is 7.4Kw (being free of blower fan), and 20 DEG C of fan deliveries are 10000Kg/h, and 120 DEG C of hot blast water evaporation quantities are 220 ---
260Kg, 220 DEG C of hot blast water evaporation quantities are 440 --- 500Kg, 400 DEG C of hot blast water evaporation quantities are 720 --- 800Kg.
Embodiment five
From the tower hot air through drier of HGT2000, mechanical dimensions (the long wide * of * are high) are 2430mm*2650mm*6800mm, main
Machine capacity is 12Kw (being free of blower fan), and 20 DEG C of fan deliveries are 15000Kg/h, and 120 DEG C of hot blast water evaporation quantities are 350 ---
380Kg, 220 DEG C of hot blast water evaporation quantities are 700 --- 750Kg, 400 DEG C of hot blast water evaporation quantities are 1100 --- 1250Kg.
Embodiment six
From the tower hot air through drier of HGT3000, mechanical dimensions (the long wide * of * are high) are 3520mm*3640mm*8230mm, main
Machine capacity is 12Kw (being free of blower fan), and 20 DEG C of fan deliveries are 32000Kg/h, and 120 DEG C of hot blast water evaporation quantities are 760 ---
800Kg, 220 DEG C of hot blast water evaporation quantities are 1500 --- 1600Kg, 400 DEG C of hot blast water evaporation quantities are 2500 ---
2700Kg。
It is embodiment of the present utility model as described above.The utility model is not limited to above-mentioned embodiment, anyone
The structure change made under enlightenment of the present utility model should be learnt, it is every that there is same or like skill with the utility model
Art scheme, each falls within protection domain of the present utility model.
Claims (9)
1. a kind of tower cross-flow drying equipment of novel energy-conserving, including tower hot air through drier (5), it is characterised in that：Tower
Distributing device (11) is provided with the charging aperture of hot air through drier (5), is set on the inwall on the top of tower hot air through drier (5)
There is the level detector (12) for detecting the thickness of feed layer entered in tower hot air through drier (5).
2. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 1, it is characterised in that：It is described tower to wear
Charging Blowing stopper (2) is connected with above the charging aperture of stream drying machine (5), the distributing device (11) includes feed pipe (1101), entered
The bottom of expects pipe (1101) is connected with passage (1102), and feed pipe (1101) is connected with charging Blowing stopper (2).
3. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 2, it is characterised in that：The passage
(1102) it is provided with multigroup, multigroup passage (1102) is along the circumferentially distributed of feed pipe (1101).
4. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 3, it is characterised in that：The passage
(1102) it is inclined on feed pipe (1101), the angle of passage (1102) and the axis of feed pipe (1101) is arrived at 20 °
Between 70 °.
5. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 1, it is characterised in that：The level detector
(12) include being provided with fix bar (1201) and leading-off rods (1203) at the top of induction end (1202), induction end (1202), it is fixed
The top of bar (1201) is welded on the top of tower hot air through drier (5).
6. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 1, it is characterised in that：It is described tower to wear
Ventilation terminal (10) is provided with the pipeline of the hot wind inlet pipe (6) of stream drying machine (5), hot wind inlet pipe (6) passes through airduct and heat
Blower fan (8) is connected.
7. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 1, it is characterised in that：It is described tower to wear
It is connected with the top of charging Blowing stopper (2), the tower hot air through drier (5) and is provided with above the charging aperture of stream drying machine (5)
Hot-blast outlet (4), charging aperture is connected with the bottom of charging Blowing stopper (2), and feed hopper is connected with the top of charging Blowing stopper (2)
(1)；The bottom of the tower hot air through drier (5) is provided with hot wind inlet pipe (6) and discharging opening, and discharge outlet is welded with discharging
Blowing stopper (7).
8. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 7, it is characterised in that：It is described tower to wear
Hot-blast outlet (4) place of stream drying machine (5) is connected with cyclone dust collectors (3).
9. a kind of tower cross-flow drying equipment of novel energy-conserving according to claim 7, it is characterised in that：The discharging is closed
Blower fan (7) bottom is provided with conveying device (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621215711.1U CN206410432U (en) | 2016-11-11 | 2016-11-11 | A kind of tower cross-flow drying equipment of novel energy-conserving |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621215711.1U CN206410432U (en) | 2016-11-11 | 2016-11-11 | A kind of tower cross-flow drying equipment of novel energy-conserving |
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| Publication Number | Publication Date |
|---|---|
| CN206410432U true CN206410432U (en) | 2017-08-15 |
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ID=59548153
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621215711.1U Expired - Fee Related CN206410432U (en) | 2016-11-11 | 2016-11-11 | A kind of tower cross-flow drying equipment of novel energy-conserving |
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| Country | Link |
|---|---|
| CN (1) | CN206410432U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107917579A (en) * | 2017-12-20 | 2018-04-17 | 江苏仅联合智造有限公司 | A kind of medicine wet granular suspension drying process and equipment |
-
2016
- 2016-11-11 CN CN201621215711.1U patent/CN206410432U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107917579A (en) * | 2017-12-20 | 2018-04-17 | 江苏仅联合智造有限公司 | A kind of medicine wet granular suspension drying process and equipment |
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| 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: 20170815 |