CN202403498U - Carbon material drying machine - Google Patents
Carbon material drying machine Download PDFInfo
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- CN202403498U CN202403498U CN2011205372500U CN201120537250U CN202403498U CN 202403498 U CN202403498 U CN 202403498U CN 2011205372500 U CN2011205372500 U CN 2011205372500U CN 201120537250 U CN201120537250 U CN 201120537250U CN 202403498 U CN202403498 U CN 202403498U
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- bellows chamber
- temperature
- outer cylinder
- carbon material
- drying
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Abstract
The utility model discloses a carbon material drying machine, which mainly comprises wind bags, a feed lifting machine, a receiving hopper, a material distributing cone, an annular air hole, a draught pipeline, a regulating valve, a wind distributing pipeline, a discharge cone hopper, a discharge vibrator, a switching tee joint, a discharge belt, a material return belt, a temperature control system, an inner cylinder and an outer cylinder, wherein three wind bags, which are a waste gas wind bag, a high-temperature wind bag and a low-temperature wind bag respectively, are welded on the outer cylinder, the carbon material drying machine is divided into three sections, which are a preheating section, a high-temperature drying section and a low-temperature drying section, through the three wind bags, the drying speed and the heat utilization rate are improved by the high-temperature drying section, the operation security of the device is ensured by the low-temperature drying section, the heat is fully utilized by the preheating section, and the crushing rate of the carbon material is reduced through creeping and moving down the materials. The drying machine has the advantages of high heat utilization rate, large yield, safe operation, low crushing rate, small investment, low operation cost and the like, and is particularly suitable for drying inflammable materials such as blue carbon, coke, raw coal and the like.
Description
Technical field
The utility model relates to a kind of carbon material drying plant, especially a kind of carbon material dryer.
Background technology
At present in carbon material drying plant, all have defective in various degree, the rotating drum type drying machine energy consumption is high, and rate of heat exchange is lower, and operating cost is high, and carbon material percentage of damage in continuous rotation process is higher; Tower drier is prone to catch fire, and has big potential safety hazard, and bake out temperature is selected the low energy waste that causes for use.
Summary of the invention
The purpose of the utility model is to overcome the defective that existing dryer exists, and a kind of carbon material dryer is provided, and this device structure is simple, small investment, and the thermal efficiency is higher, and operating cost is low, safeguards that simply life cycle is long.
In order to realize above-mentioned purpose, the utility model has adopted following technical scheme: a kind of carbon material dryer mainly is made up of shake machine, switching three-way, outfeed belt, feed back belt, temperature control system and inner/outer tube of bellows chamber, charging elevator, hopper, material distributing cone, annular tuyere, air inducing pipeline, control valve, air distribution pipeline, reclaiming cone bucket, discharging; This equipment is divided into three oven dry sections, is respectively preheating section, hyperthermia drying section, low temperature drying section from top to bottom; This equipment segmentation oven dry, the heat energy utilization rate is high, is particularly suitable for the oven dry of flammable materials such as blue charcoal, coke, raw coal.
A kind of carbon material dryer, its charging elevator links to each other with the hopper sealing, and the hopper sealing and fixing is on outer cylinder body; Material distributing cone is fixed on the inner barrel, and material is distributed between outer cylinder body and the inner barrel uniformly, makes equipment be full of material all around; The outer cylinder body lower end is fixed with the reclaiming cone bucket, and reclaiming cone bucket bottom is fixed with the discharging machine that shakes, and the discharging machine that shakes is that variable frequency adjustment can be regulated discharging speed; The discharging machine lower end that shakes has switching three-way to be fixed in ground; Two discharging openings of discharging threeway connect outfeed belt and feed back belt respectively, and the feed back belt is connected with the import of charging elevator, with continuing oven dry in the material Returning equipment that does not reach drying requirement; Be welded with three bellows chambers on the outer cylinder body, be respectively waste gas bellows chamber, high temperature bellows chamber, low temperature bellows chamber, have annular tuyere on inner barrel and the outer cylinder body; Be welded with the air inducing pipeline on the waste gas bellows chamber; Be welded with high-temperature pipe on the high temperature bellows chamber, be welded with cryogenic piping on the low temperature bellows chamber, be connected to the air distribution pipeline on the cryogenic piping; On high-temperature pipe, cryogenic piping and the air distribution pipeline control valve is housed, the bake out temperature of control air flow rate proportioning and low temperature drying section; High temperature bellows chamber and low temperature bellows chamber are the air inlet bellows chamber, and the waste gas bellows chamber is divided into three oven dry sections for three bellows chambers of bellows chamber of giving vent to anger with equipment: be respectively preheating section, hyperthermia drying section, low temperature drying section from top to bottom.
It is preheating section, hyperthermia drying section, low temperature drying section that this carbon material dryer is divided into three sections; The hyperthermia drying section has improved drying rate and heat utilization efficiency; The low temperature drying degree has guaranteed the security of operation of equipment, and preheating section has utilized heat energy fully, and the wriggling of material moves down the percentage of damage that has reduced the carbon material; It is high to make this equipment possess the heat energy utilization rate, and output is big, security of operation, and percentage of damage is low, small investment, advantage such as operating cost is low.
Description of drawings
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
Accompanying drawing 1 is the structural representation of the utility model
Accompanying drawing 2 is the local enlarged diagram of the utility model structure
The specific embodiment
The concrete structure of the utility model sees also accompanying drawing 1; Charging elevator 4 links to each other with hopper 5 sealings, and the hopper sealing and fixing is on outer cylinder body 19, and material distributing cone is fixed on the inner barrel 18; Material is distributed between outer cylinder body 19 and the inner barrel 18 uniformly, makes equipment be full of material all around; Outer cylinder body 19 lower ends are fixed with reclaiming cone bucket 13; Reclaiming cone bucket 13 bottoms are fixed with the discharging machine 14 that shakes; The discharging machine 14 that shakes can be regulated discharging speed for variable frequency adjustment, and the discharging machine lower end that shakes has switching three-way 15 to be fixed in ground, and 15 two discharging openings of discharging threeway connect outfeed belt 16 and feed back belt 17 respectively; Feed back belt 17 is connected with the import of charging elevator 4, with continuing oven dry in the material Returning equipment that does not reach drying requirement; Be welded with three bellows chambers on the outer cylinder body 19, be respectively waste gas bellows chamber 3, high temperature bellows chamber 2, low temperature bellows chamber 1, have annular tuyere 7 on inner barrel 18 and the outer cylinder body 19; Be welded with air inducing pipeline 8 on the waste gas bellows chamber 3; Be welded with high-temperature pipe 9 on the high temperature bellows chamber 2, be welded with cryogenic piping 10 on the low temperature bellows chamber 1, be connected to air distribution pipeline 12 on the cryogenic piping; On high-temperature pipe 9, cryogenic piping 10 and the air distribution pipeline 12 control valve 11 is housed, the bake out temperature of control air flow rate proportioning and low temperature drying section; High temperature bellows chamber 2 is the air inlet bellows chamber with low temperature bellows chamber 1, and waste gas bellows chamber 3 is for giving vent to anger bellows chamber, and three bellows chambers are divided into three oven dry sections with dryer: be respectively preheating section, hyperthermia drying section, low temperature drying section from top to bottom.
Material is carried to hopper 5 by charging elevator 4; Be evenly distributed to the dryer circumference through material distributing cone 6; Material leans on own wt slowly to move down, in the folding process through preheating section, hyperthermia drying section, low temperature drying section, through reclaiming cone bucket 13 by discharging machine 14 dischargings of shaking; The material that reaches the oven dry standard is via outfeed belt 16 dischargings, and the material that does not reach the oven dry standard is back to charging elevator 4 via feed back belt 17 and gets into drying machine drying again; Thermal source can be selected the waste heat and the various hot-blast stove of various kilns for use; Hot blast gets into high temperature bellows chamber 2 and low temperature bellows chamber 1 via pipeline; Pass material bed entering dryer inner barrel 18 through annular tuyere 7; Pass material bed entering waste gas bellows chamber 3 through annular tuyere 7 once more at preheating section, draw by air inducing pipeline 8.It is nonflammable when flammable materials moisture is higher; Can adopt hyperthermia drying; Material is in below the burning-point it through the control hot blast temperature, just low temperature drying than easy firing when moisture is reduced to a certain degree; Air distribution pipeline 12 is housed on the cryogenic piping 10 controls hot blast temperature, to guarantee the bake out temperature of low temperature drying section; Thereby guaranteed the safety of oven dry, and farthest saved the energy.
Claims (3)
1. a carbon material dryer mainly is made up of shake machine (14), switching three-way (15), outfeed belt (16), feed back belt (17), temperature control system and inner barrel (18), outer cylinder body (19) of bellows chamber, charging elevator (4), hopper (5), material distributing cone (6), annular tuyere (7), air inducing pipeline (8), control valve (11), air distribution pipeline (12), reclaiming cone bucket (13), discharging; It is characterized in that: charging elevator (4) links to each other with hopper (5) sealing, and the hopper sealing and fixing is on outer cylinder body (19), and material distributing cone (6) is fixed on the inner barrel (18); Be welded with three bellows chambers on the outer cylinder body (19); Be respectively waste gas bellows chamber (3), high temperature bellows chamber (2), low temperature bellows chamber (1), have annular tuyere (7) on inner barrel (18) and the outer cylinder body (19), be welded with air inducing pipeline (8) on the waste gas bellows chamber (3); Be welded with high-temperature pipe (9) on the high temperature bellows chamber (2); Be welded with cryogenic piping (10) on the low temperature bellows chamber (1), be connected to air distribution pipeline (12) on the cryogenic piping (10), on high-temperature pipe (9), cryogenic piping (10) and the air distribution pipeline (12) control valve (11) is housed; Outer cylinder body (19) lower end is fixed with reclaiming cone bucket (13); Reclaiming cone bucket (13) bottom is fixed with the discharging machine (14) that shakes; Discharging machine (14) lower end that shakes has switching three-way (15) to be fixed in ground; Two discharging openings of discharging threeway (15) connect outfeed belt (16) and feed back belt (17) respectively, and feed back belt (17) is connected with the import of charging elevator (4).
2. a kind of carbon material dryer as claimed in claim 1 is characterized in that: high temperature bellows chamber (2) is the air inlet bellows chamber with low temperature bellows chamber (1), and waste gas bellows chamber (3) is the bellows chamber of giving vent to anger.
3. according to claim 1 or claim 2 a kind of carbon material dryer, it is characterized in that: waste gas bellows chamber (3), high temperature bellows chamber (2), low temperature bellows chamber (1) are divided into three oven dry sections with said dryer: be respectively preheating section, hyperthermia drying section, low temperature drying section from top to bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205372500U CN202403498U (en) | 2011-12-21 | 2011-12-21 | Carbon material drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205372500U CN202403498U (en) | 2011-12-21 | 2011-12-21 | Carbon material drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202403498U true CN202403498U (en) | 2012-08-29 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205372500U Expired - Fee Related CN202403498U (en) | 2011-12-21 | 2011-12-21 | Carbon material drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202403498U (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103217003A (en) * | 2013-03-04 | 2013-07-24 | 新乡市格林实业发展有限公司 | Layered energy-saving dryer |
| CN103759516A (en) * | 2014-01-06 | 2014-04-30 | 新乡仲德能源科技有限公司 | Vertical drying machine uniform in air distribution |
| CN103759515A (en) * | 2014-01-06 | 2014-04-30 | 新乡仲德能源科技有限公司 | Novel vertical dryer |
| CN106766824A (en) * | 2017-01-21 | 2017-05-31 | 江苏中圣园科技股份有限公司 | Semi-coke drying system |
| CN107537823A (en) * | 2017-10-30 | 2018-01-05 | 深圳市晟腾企业管理有限公司 | A kind of bituminous concrete building stones device for cleaning and air-drying |
| CN108106403A (en) * | 2017-11-23 | 2018-06-01 | 内蒙古宜化化工有限公司 | A kind of novel charcoal drying unit |
| CN110274490A (en) * | 2019-05-31 | 2019-09-24 | 中信重工机械股份有限公司 | A kind of vertical heat-exchange device for granular material |
| CN115235227A (en) * | 2022-07-26 | 2022-10-25 | 南平市亿泽磨料磨具科技有限公司 | Mixed preheating system and method for producing high-temperature-resistant rare metal material |
-
2011
- 2011-12-21 CN CN2011205372500U patent/CN202403498U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103217003A (en) * | 2013-03-04 | 2013-07-24 | 新乡市格林实业发展有限公司 | Layered energy-saving dryer |
| CN103217003B (en) * | 2013-03-04 | 2015-04-08 | 新乡市格林实业发展有限公司 | Layered energy-saving dryer |
| CN103759516A (en) * | 2014-01-06 | 2014-04-30 | 新乡仲德能源科技有限公司 | Vertical drying machine uniform in air distribution |
| CN103759515A (en) * | 2014-01-06 | 2014-04-30 | 新乡仲德能源科技有限公司 | Novel vertical dryer |
| CN106766824A (en) * | 2017-01-21 | 2017-05-31 | 江苏中圣园科技股份有限公司 | Semi-coke drying system |
| CN107537823A (en) * | 2017-10-30 | 2018-01-05 | 深圳市晟腾企业管理有限公司 | A kind of bituminous concrete building stones device for cleaning and air-drying |
| CN108106403A (en) * | 2017-11-23 | 2018-06-01 | 内蒙古宜化化工有限公司 | A kind of novel charcoal drying unit |
| CN110274490A (en) * | 2019-05-31 | 2019-09-24 | 中信重工机械股份有限公司 | A kind of vertical heat-exchange device for granular material |
| CN115235227A (en) * | 2022-07-26 | 2022-10-25 | 南平市亿泽磨料磨具科技有限公司 | Mixed preheating system and method for producing high-temperature-resistant rare metal material |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: XINXIANG ZHONGDE ENERGY TECHNOLOGY CO., LTD. Assignor: Cen Menghan Contract record no.: 2013410000074 Denomination of utility model: Combination material-lifting unit of three-barrel carbon material dryer Granted publication date: 20120829 License type: Exclusive License Record date: 20130829 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120829 Termination date: 20141221 |
|
| EXPY | Termination of patent right or utility model |