CN2921738Y - Formed coke drying kiln - Google Patents
Formed coke drying kiln Download PDFInfo
- Publication number
- CN2921738Y CN2921738Y CN 200620026087 CN200620026087U CN2921738Y CN 2921738 Y CN2921738 Y CN 2921738Y CN 200620026087 CN200620026087 CN 200620026087 CN 200620026087 U CN200620026087 U CN 200620026087U CN 2921738 Y CN2921738 Y CN 2921738Y
- Authority
- CN
- China
- Prior art keywords
- kiln
- hot
- formed coke
- formcoke
- 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
Images
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
A formed coke drying kiln relating to a device for drying and solidifying molded formcoke solidifies in-kiln formcoke by use of smoke gas generated from hot-blast stove combustion, which comprises a kiln body, a kiln car, a carrier, a rail, a drying system and an electrical control system, wherein, the smoke gas generated from burner combustion of the drying system enters into a wind mixing chamber and meanwhile, the hot blast after heat exchange in the kiln body also flows into the wind mixing chamber; the smoke gas and the hot blast are mixed in the wind mixing chamber to generate hot air in accordance with required temperature; the hot air is blown into the kiln through a warm air duct by a recirculating fan and solidifies the formcoke therein. The utility model is characterized in that: the solidified formcoke possesses physical characteristics similar to that of coke, thereby saving energy and realizing clean production.
Description
Affiliated technical field
The utility model relates to a kind of drying device, refers more particularly to a kind of with device dry after the formed coke moulding and that curing is used.
Background technology
Curing to formed coke mainly contains high temperature carbonization method and low-temperature oxidation method at present, and concerning the high temperature carbonization method, its temperature is higher, can realize the formed coke drying fast, but often causes the formed coke quality to destroy.And low-temperature oxidation method is higher to temperature control requirement, otherwise will produce destruction to the formed coke inner oxidizing agent.
Summary of the invention
The purpose of this utility model provides a kind of formed coke dry kiln, and it is to utilize the flue gas of Combustion of Hot Air Furnace that formed coke in the kiln is cured, and comprises kiln body, kiln car, carrier, track, drying system and electric-control system.
Described kiln body is the cell-type structure, and its madial wall is connected with hot air duct, and the top is provided with circulation airduct and exhaust duct, and its front portion is provided with heat insulation wicket, is equipped with track on wicket kiln body of living in ground, is used for kiln car and enters the kiln body.
Described carrier is the rectangle steel shelf structure, and around it and bottom is welded with steel wire, and inside is used to load formed coke, and carrier steelframe top is welded with suspension ring, during for the loading and unloading formed coke lifting used, kiln car is used for transport carrier, is provided with wheel, walking freely in orbit bottom it.
The carrier of filling formed coke is overlayed on the kiln car, and push in the kiln body, put down heat insulation wicket, with the roof door handwheel heat insulation wicket is held out against, heat insulation wicket top is connected with steel wire rope, the steel wire rope other end is connected with balancing weight by pulley, because the effect of balancing weight is convenient and strength-saving when heat insulation wicket rises and falls.
Described drying system comprises hot-air system and dehumidification system, described hot-air system comprises combustion furnace, wind mixed chamber, hot air duct, circulating fan and circulation airduct, the flue gas that the combustion furnace burning is produced enters wind mixed chamber, simultaneously, hot blast in the kiln body after the heat exchange enters wind mixed chamber by the circulation airduct, flue gas mixes the hot-air that obtains meeting temperature with hot blast in wind mixed chamber, sent in the kiln by hot air duct by circulating fan.
Described dehumidification system comprises wet-emitting blower and exhaust duct, and it can be external with discharge kiln after dedusting through the hot blast after the heat exchange.
The utility model is provided with electric-control system, and it can realize that simultaneously for energy savings and easy to adjust, the native system blower fan all adopts variable frequency regulating speed control to the control of native system blower fan with to the detection of temperature in the kiln body.
The utility model utilizes the combustion furnace flue gas to adopt the low temperature heat-exchanging method that formed coke is cured, and the physical property and the coke that solidify the back formed coke are similar, have not only saved the energy but also have realized cleaner production, have reached the purpose of this utility model.
Figure of description
Fig. 1 is the utility model dry kiln structural representation.
Fig. 2 is the utility model drying system schematic diagram.
1 kiln body among the figure, 2 kiln cars, 3 carriers, 4 tracks, 5 hot air ducts, 6 circulation airducts, 7 exhaust ducts, 8 heat insulation wickets, 9 take turns, 10 roof door handwheels, 11 balancing weights, 12 combustion furnaces, 13 wind mixed chamber, 14 circulating fans, 15 wet-emitting blowers.
The specific embodiment
By accompanying drawing as can be known, the utility model comprises kiln body 1, kiln car 2, carrier 3, track 4, drying system and electric-control system.
Described kiln body is the cell-type structure, and its madial wall is connected with hot air duct 5, and the top is provided with circulation airduct 6 and exhaust duct 7, and its front portion is provided with heat insulation wicket 8, is equipped with track 4 on wicket 8 kiln body of living in ground, is used for kiln car 2 and enters kiln body 1.
Described carrier 3 is the rectangle steel shelf structure, and around it and bottom is welded with steel wire, and inside is used to load formed coke, carrier 3 steelframe tops are welded with suspension ring, and used for the time lifting of loading and unloading formed coke, kiln car 2 is used for transport carrier 3, its bottom is provided with wheel 9, can be on track 4 walking freely.
The carrier 3 of filling formed coke is overlayed on the kiln car 2, and push in the kiln body 1, put down heat insulation wicket 8, with roof door handwheel 10 heat insulation wicket 8 is held out against, heat insulation wicket top is connected with steel wire rope, the steel wire rope other end is connected with balancing weight 11 by pulley, because the effect of balancing weight 11 is convenient and strength-saving when heat insulation wicket 8 rises and falls.
Described drying system comprises hot-air system and dehumidification system, described hot-air system comprises combustion furnace 12, wind mixed chamber 13, hot air duct 5, circulating fan 14 and circulation airduct 6, the flue gas that combustion furnace 12 burnings are produced enters wind mixed chamber 13, simultaneously, hot blast in kiln body 1 after the heat exchange enters wind mixed chamber 13 by circulation airduct 6, flue gas mixes the hot-air that obtains meeting temperature with hot blast in wind mixed chamber 13, sent in the kiln by hot air duct 5 by circulating fan 14.
Described dehumidification system comprises wet-emitting blower 15 and exhaust duct 7, and it can be external with discharge kiln after dedusting through the hot blast after the heat exchange.
The utility model is provided with electric-control system, and it can be realized to the control of native system blower fan with to the detection of temperature in the kiln body.
Claims (3)
1, a kind of formed coke dry kiln, comprise kiln body (1), kiln car (2), carrier (3), track (4), drying system and electric-control system, it is characterized in that: described kiln body (1) is provided with heat insulation wicket (8), heat insulationly be equipped with track (4) on wicket (8) kiln body of living in ground, described drying system comprises hot-air system and dehumidification system.
2, formed coke dry kiln according to claim 1, it is characterized in that: described hot-air system comprises combustion furnace (12), wind mixed chamber (13), hot air duct (5), circulating fan (14) and circulation airduct (6), and described dehumidification system comprises wet-emitting blower (15) and exhaust duct (7).
3, formed coke dry kiln according to claim 1 is characterized in that: described heat insulation wicket (8) is connected with balancing weight (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620026087 CN2921738Y (en) | 2006-05-19 | 2006-05-19 | Formed coke drying kiln |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620026087 CN2921738Y (en) | 2006-05-19 | 2006-05-19 | Formed coke drying kiln |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2921738Y true CN2921738Y (en) | 2007-07-11 |
Family
ID=38254218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620026087 Expired - Fee Related CN2921738Y (en) | 2006-05-19 | 2006-05-19 | Formed coke drying kiln |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2921738Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102735035A (en) * | 2011-04-01 | 2012-10-17 | 北京华珍烘烤系统设备工程有限公司 | Tunnel curing barn adopting humiture subdivision control of alternate wind direction |
| CN102997631A (en) * | 2012-10-31 | 2013-03-27 | 宜兴市宜刚环保工程材料有限公司 | Continuous drying kiln of honeycomb-type denitration catalyst |
| CN109959257A (en) * | 2017-12-22 | 2019-07-02 | 郑州华祥耐材有限公司 | A kind of high-temperature shuttle kiln |
| CN113670075A (en) * | 2021-08-16 | 2021-11-19 | 邵阳市君伟建材有限公司 | Biomass combustion heating device for heating and solidifying surface of workpiece |
-
2006
- 2006-05-19 CN CN 200620026087 patent/CN2921738Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102735035A (en) * | 2011-04-01 | 2012-10-17 | 北京华珍烘烤系统设备工程有限公司 | Tunnel curing barn adopting humiture subdivision control of alternate wind direction |
| CN102735035B (en) * | 2011-04-01 | 2014-07-16 | 北京华珍烘烤系统设备工程有限公司 | Tunnel curing barn adopting humiture subdivision control of alternate wind direction |
| CN102997631A (en) * | 2012-10-31 | 2013-03-27 | 宜兴市宜刚环保工程材料有限公司 | Continuous drying kiln of honeycomb-type denitration catalyst |
| CN109959257A (en) * | 2017-12-22 | 2019-07-02 | 郑州华祥耐材有限公司 | A kind of high-temperature shuttle kiln |
| CN113670075A (en) * | 2021-08-16 | 2021-11-19 | 邵阳市君伟建材有限公司 | Biomass combustion heating device for heating and solidifying surface of workpiece |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN2921738Y (en) | Formed coke drying kiln | |
| CN203323546U (en) | Sectional type rotary kiln | |
| CN106702143A (en) | Efficiently-energy-saving hot air supply method for belt type roasting machine | |
| CN104197704A (en) | SCR denitration catalyst pre-production experimental device with drying and calcining functions | |
| CN205262100U (en) | Novel high -efficient woollen blanket drying -machine | |
| CN205228024U (en) | Drying system of adobe | |
| CN103925788B (en) | Fired brick production line large cross-section tunnel kiln circulation adjustable ventilating system | |
| CN214172902U (en) | High-efficiency energy-saving tunnel kiln | |
| CN205474492U (en) | Sock dryer | |
| CN204987846U (en) | Guipure gas fritting furnace | |
| CN202035464U (en) | Far infrared heating curing barn | |
| CN201488504U (en) | Cyclic slideway drier | |
| CN205228143U (en) | System for adobe stoving sintering | |
| CN205337425U (en) | Circulated grain drying -machine of sled dress formula | |
| CN212274604U (en) | Chain row type vanadium ore roasting tunnel kiln | |
| CN209339993U (en) | A kind of tunnel shaft ventilation and exhaust device based on monsoon | |
| CN203105578U (en) | Tunnel-type fruit and vegetable dryer | |
| CN102798269B (en) | Method and equipment for drying/cooling large particles of coal in guide duct type packed tower by cyclic utilization of superheated steam | |
| CN207335416U (en) | A kind of sintered porous shale brick cigarette heat separation device | |
| CN201208590Y (en) | Cooling furnace for stator processing | |
| CN106839758B (en) | Annular mobile tunnel furnace production line arragement construction | |
| CN203518560U (en) | Rotary steel kiln pipeline piece circulation air system | |
| CN103925789B (en) | Fired brick production line narrow-bore tunnel kiln circulation adjustable ventilating system | |
| CN219314872U (en) | Bamboo coal granule carbonization forming equipment using bamboo to replace coal | |
| CN2514282Y (en) | Cooling drier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070711 Termination date: 20100519 |