CN102620538B - Vertical dryer - Google Patents
Vertical dryer Download PDFInfo
- Publication number
- CN102620538B CN102620538B CN201210123208.3A CN201210123208A CN102620538B CN 102620538 B CN102620538 B CN 102620538B CN 201210123208 A CN201210123208 A CN 201210123208A CN 102620538 B CN102620538 B CN 102620538B
- Authority
- CN
- China
- Prior art keywords
- conveying chamber
- rotation
- rotation conveying
- drying chamber
- chamber housing
- 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
Images
Abstract
The invention discloses a vertical dryer, which comprises a feed hopper (1), a stand (2), a rotary conveying chamber (3), a driving motor (4), a discharge port (5) and an internal fixation drying chamber (6), and is characterized in that: a plurality of grooves (9) for circulating hot air are formed on cylindrical surfaces of a shell (8) of the rotary conveying chamber and a shell (12) of the internal fixation drying chamber. Compared with the prior art, the vertical dryer has the advantages of simple structure, low energy consumption and high dehydration efficiency.
Description
Technical field
The present invention relates to a kind of drying unit, particularly relate to a kind of tower drier for dry iron ore concentrate.
Background technology
Iron ore becomes iron extract mine producation after processing, wet concentration.At ore in sand form intergranular, have a large amount of Interstitial Waters, if do not do processed, in transit, iron sand easily outflows with water, and causes enterprises' loss, and also pollutes environment in way.When prior art is carried out processed to iron ore concentrate, conventionally adopt the dehydration of sedimentation basin precipitation, or adopt filtering equipment filtering means dehydration.Wherein, sedimentation basin deposition dehydrating is applied in small-sized ore dressing plant mostly, and to be 50 orders use with interior iron ore concentrate dehydration applicable granularity, although the method production cost is lower, the sedimentation time is long, and is difficult to nature and deviates from for being less than 50 object granularities; Relatively large ore dressing plant generally adopts filtering equipment dehydration, and the dehydration indexes of filter-pressing method is good, but equipment investment is large, and production cost is high, again because the parts such as filter screen easily stop up, damage, need to shut down repairing, change part, thereby continuous production is poor.
The present invention, in order to solve the problems of the technologies described above, provides a kind of novel vertical dryer, and this drying machine structure is simple, energy consumption is low, dewatering efficiency is high, and good drying effect.
Summary of the invention
For achieving the above object, the invention provides following technical scheme: a kind of tower drier, it comprises: feed hopper, frame, rotation conveying chamber, drive motors, discharging opening, interior fixedly drying chamber; Wherein, feed hopper is positioned at frame top, is funnel-form, and its lower ending opening joins with rotation conveying chamber; Rotation conveying chamber is vertical type cylinder structure, it comprises rotation conveying chamber housing, spiral pusher plate and rotation fluted disc, rotation fluted disc related whole rotation conveying chamber under the driving of drive motors rotates, the indoor iron ore concentrate of rotation conveying transports from top to bottom under the promotion of spiral pusher plate, and discharges dryer by the discharging opening of lower end; Interior fixedly drying chamber is positioned at rotation conveying chamber interior, for hollow circuit cylinder structure, it comprises interior fixedly drying chamber housing, heating stove and exhaust outlet, bottom and the heating stove of interior fixedly drying chamber housing are affixed, the hot gas of dry iron ore concentrate can flow therein from bottom to top, the interior fixedly top of drying chamber housing is connected with exhaust outlet 13, for thermal current is discharged to dryer; On the face of cylinder of rotation conveying chamber housing and interior fixedly drying chamber housing, have the groove of a plurality of circulation hot gas.
Further, described rotation conveying chamber 3 upper and lower sides also comprise a plurality of revolution support wheels, and described revolution support wheel is provided support by the supporting seat in frame.
The present invention has following advantages and effect:
1, tower drier of the present invention is simple in structure, easy to operate, can be widely used in the fields such as chemical industry, metallurgy;
2, in implementing the process of dehydration, thermal current flows from bottom to top in interior fixedly drying chamber, and conveying is indoor moves from top to bottom in rotation for iron ore concentrate, and heat exchange is evenly abundant, and dewatering efficiency is high;
3, on the face of cylinder of rotation conveying chamber housing and interior fixedly drying chamber housing, open innovatively the groove of a plurality of circulation hot gas, thermal current can enter in rotation conveying chamber by this groove, and by the gap between iron ore concentrate material, be penetrated into the inside of mineral aggregate, thereby make dehydration more thorough, drying effect obviously improves.
Accompanying drawing explanation
Fig. 1 is the structural representation of tower drier of the present invention;
Fig. 2 is the top view of tower drier of the present invention.
The specific embodiment
Now 1,2 elaborate the present invention by reference to the accompanying drawings.
As shown in accompanying drawing 1,2, tower drier of the present invention comprises: feed hopper 1, frame 2, rotation conveying chamber 3, drive motors 4, discharging opening 5, interior fixedly drying chamber 6; Wherein, feed hopper 1 is positioned at frame 2 tops, is funnel-form, and its lower ending opening joins with rotation conveying chamber 3; Rotation conveying chamber 3 is vertical type cylinder structure, it comprises rotation conveying chamber housing 8, spiral pusher plate 10 and rotation fluted disc 11, rotation fluted disc 11 related whole rotation conveying chamber 3 under the driving of drive motors 4 rotates, iron ore concentrate in rotation conveying chamber 3 transports from top to bottom under the promotion of spiral pusher plate 10, and discharges dryer by the discharging opening 5 of lower end; Interior fixedly drying chamber 6 is positioned at rotation 3 inside, conveying chamber, for hollow circuit cylinder structure, it comprises interior fixedly drying chamber housing 12, heating stove 7 and exhaust outlet 13, bottom and the heating stove 7 of interior fixedly drying chamber housing 12 are affixed, the hot gas of dry iron ore concentrate can flow therein from bottom to top, the interior fixedly top of drying chamber housing 12 is connected with exhaust outlet 13, for thermal current is discharged to dryer; It is characterized in that: on the face of cylinder of rotation conveying chamber housing 8 and interior fixedly drying chamber housing 12, have the groove 9 of a plurality of circulation hot gas, and the groove 9 on interior fixedly drying chamber housing 12 is downward-sloping setting, to prevent that mineral aggregate from entering groove 9, the setting that is inclined upwardly of groove 9 on rotation conveying chamber housing 8, be conducive to water vapour and discharge, prevent descending mineral aggregate effusion simultaneously.Described rotation conveying chamber 3 upper and lower sides also comprise a plurality of revolution support wheels 14, and described revolution support wheel 14 is provided support by the supporting seat 15 in frame 2.
The course of work of this tower drier is as follows:
1, light heating stove 7 endogenous pyrogens, thermal current occurs to flow by interior fixedly drying chamber 6 from bottom to top;
2, by feed hopper 1, pack iron ore concentrate material into rotation conveying chamber 3, in rotation conveying chamber 3, under the appendix of spiral pusher plate 10, mineral aggregate is moved along helical orbit from top to down equably;
3, thermal current enters in rotation conveying chamber 3 by the surface groove of interior fixedly drying chamber housing 12, come in contact with descending mineral aggregate, and the moisture gasification in mineral aggregate, via the groove on rotation conveying chamber housing 8, discharge dryer, the thermal current that does not see through interior fixedly drying chamber housing 12 is discharged dryer by exhaust outlet 13;
4, through the iron ore concentrate material of abundant processed, through discharging opening 5, discharge tower stove.
From feed hopper, constantly inwardly fixedly drying chamber, feed intake, after drying, mineral aggregate is constantly discharged through discharging opening, realized the lasting drying course to iron ore concentrate material, improved the operating efficiency of processing mineral aggregate.
Finally it should be noted that, above embodiment is only unrestricted in order to technical scheme of the present invention to be described, although the present invention is had been described in detail with reference to preferred embodiment, those of ordinary skill in the art is to be understood that, can modify or be equal to replacement technical scheme of the present invention, and not departing from the spirit and scope of technical solution of the present invention, it all should be encompassed in the middle of claim scope of the present invention.
Claims (2)
1. a tower drier, is characterized in that: it comprises feed hopper (1), frame (2), rotation conveying chamber (3), drive motors (4), discharging opening (5), interior fixedly drying chamber (6); Wherein, feed hopper (1) is positioned at frame (2) top, is funnel-form, and its lower ending opening joins with rotation conveying chamber (3); Rotation conveying chamber (3) is vertical type cylinder structure, it comprises rotation conveying chamber housing (8), spiral pusher plate (10) and rotation fluted disc (11), rotation fluted disc (11) related whole rotation conveying chamber (3) under the driving of drive motors (4) rotates, iron ore concentrate in rotation conveying chamber (3) transports from top to bottom under the promotion of spiral pusher plate (10), and discharges dryer by the discharging opening (5) of lower end; Interior fixedly drying chamber (6) is positioned at rotation inside, conveying chamber (3), for hollow circuit cylinder structure, it comprises interior fixedly drying chamber housing (12), heating stove (7) and exhaust outlet (13), bottom and the heating stove (7) of interior fixedly drying chamber housing (12) are affixed, the hot gas of dry iron ore concentrate can flow therein from bottom to top, the interior fixedly top of drying chamber housing (12) is connected with exhaust outlet (13), for thermal current is discharged to dryer; On the face of cylinder of rotation conveying chamber housing (8) and interior fixedly drying chamber housing (12), have the groove (9) of a plurality of circulation hot gas.
2. tower drier according to claim 1, it is characterized in that: the upper and lower end of described rotation conveying chamber housing (8) outer surface also comprises a plurality of revolution support wheels (14), described revolution support wheel (14) is provided support by the supporting seat (15) in frame (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210123208.3A CN102620538B (en) | 2012-04-25 | 2012-04-25 | Vertical dryer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210123208.3A CN102620538B (en) | 2012-04-25 | 2012-04-25 | Vertical dryer |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102620538A CN102620538A (en) | 2012-08-01 |
CN102620538B true CN102620538B (en) | 2014-03-26 |
Family
ID=46560615
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210123208.3A Expired - Fee Related CN102620538B (en) | 2012-04-25 | 2012-04-25 | Vertical dryer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102620538B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104006645A (en) * | 2013-12-13 | 2014-08-27 | 昆山洛博格机械技术咨询有限公司 | Vertical tea dryer |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2573493Y (en) * | 2002-09-30 | 2003-09-17 | 向立和 | Internal heating dustless dryer |
CN202008278U (en) * | 2011-03-18 | 2011-10-12 | 宋志强 | Gravity type baking dryer |
CN202547310U (en) * | 2012-04-25 | 2012-11-21 | 隋鑫 | Vertical drying machine |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4224642B2 (en) * | 2005-01-20 | 2009-02-18 | 有限会社金井事務所 | Drying apparatus for drying object and drying method thereof |
JP4287888B2 (en) * | 2007-03-16 | 2009-07-01 | 哲郎 池田 | Vertical dryer |
-
2012
- 2012-04-25 CN CN201210123208.3A patent/CN102620538B/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2573493Y (en) * | 2002-09-30 | 2003-09-17 | 向立和 | Internal heating dustless dryer |
CN202008278U (en) * | 2011-03-18 | 2011-10-12 | 宋志强 | Gravity type baking dryer |
CN202547310U (en) * | 2012-04-25 | 2012-11-21 | 隋鑫 | Vertical drying machine |
Non-Patent Citations (2)
Title |
---|
JP特开2006-200795A 2006.08.03 |
JP特开2008-232471A 2008.10.02 |
Also Published As
Publication number | Publication date |
---|---|
CN102620538A (en) | 2012-08-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN204757615U (en) | High -efficient drying -machine is used in chemical fertilizer processing | |
CN101769675A (en) | Paddy dryer with heat return type heat pump | |
CN202547310U (en) | Vertical drying machine | |
CN103252207B (en) | Method for continuously preparing activated clay | |
CN104197667B (en) | The dry breaker of a kind of industrial divided chamber | |
CN209128299U (en) | A kind of garbage sludge anhydration system | |
CN102620538B (en) | Vertical dryer | |
CN208205677U (en) | A kind of efficient grain dryer | |
CN210176710U (en) | Sludge treatment device | |
CN110849104A (en) | Mineral powder drying device | |
CN111981828A (en) | Environment-friendly tectorial membrane sand core sand clay sand quick drying device | |
CN208187026U (en) | A kind of sludge dehumidification type multistage recuperation of heat anhydration system | |
CN208751200U (en) | A kind of lithium battery production line water removal drying device | |
CN212481950U (en) | Hydroextractor is used in production of green type PET bottle piece | |
CN104236278A (en) | Drying machine | |
CN203881084U (en) | Vertical drying machine used for chemical production | |
CN208642592U (en) | A kind of fertilizer production prilling granulator with cooling function | |
CN206281320U (en) | A kind of air circulation device for tunnel microwave dryer | |
CN204930206U (en) | A kind of concentrator for milk powder producing | |
CN204555588U (en) | A kind of Novel disc-type continuous dryer | |
CN205940017U (en) | Mineral drying -machine | |
CN203540210U (en) | Separating and drying integrated machine | |
CN204502998U (en) | A kind of heating and dehumidification granulator | |
CN219897315U (en) | Dewatering device is used in concentrate powder processing | |
CN212657998U (en) | Quick dehumidification drying system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20191108 Address after: 225300 Jiangsu Taizhou Binjiang Industrial Park A2-A3 Patentee after: Taizhou Tianyin Plastic Industry Co., Ltd. Address before: 067000 Hebei Province, Chengde City Stone ditch Fu villa a building office Patentee before: Xin Xin |
|
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140326 Termination date: 20200425 |