CN200968766Y - High-temperature circulating flue gas agitating drying machines - Google Patents
High-temperature circulating flue gas agitating drying machines Download PDFInfo
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- CN200968766Y CN200968766Y CN 200620036031 CN200620036031U CN200968766Y CN 200968766 Y CN200968766 Y CN 200968766Y CN 200620036031 CN200620036031 CN 200620036031 CN 200620036031 U CN200620036031 U CN 200620036031U CN 200968766 Y CN200968766 Y CN 200968766Y
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Abstract
The utility model discloses a high temperature circulation smoke stirring drying machine, which consists of an electric motor, gears, a cabinet with a feed hole and a discharge hole, two hollow stirring axis positioned on the cabinet, groups of hollow stirring blades arranged on the stirring axis, and a steam pipe communicated with the internal cavity. Wherein, the mentioned cabinet is a hollow jacket, and the hollow stirring axis between the jacket and the outer wall is provided with a plurality of blowholes, the cabinet is provided with an air inlet port and an air outlet port communicated with the jacket internal cavity; as further improvement of the utility model, a heating furnace circulation air distributing room and an air fan are provided in addition. The air inlet port on the cabinet are orderly connected in series with the air fan and the heating furnace circulation air distributing room, and the air outlet port is connected with the air inlet port of the heating furnace circulation air distributing room; Furthermore, a plurality of cold air pipes communicated with the internal cavity. The utility model has advantages of large heat interchanging area, high heat interchanging rate, few environment pollution and perfect safety.
Description
Technical field
The utility model relates to a kind of stirring drier that rubbish is carried out processed.
Background technology
At present, enhancing gradually along with people's environmental consciousness, domestic waste develops to nuisanceless resource direction, it is comparatively ideal waste disposal method that the high humidity composting is made into the granular fuel burning electricity generation, sorting rubbish dehydrated to handle be wherein important step, and stirring drier commonly used now, as shown in Figure 1, comprise motor 31, by belt pulley 32, decelerator 33, the transmission device that gear-box 34 is formed, the casing 37 that has charging aperture 35 and discharging opening 36, bearing 38 by two ends is installed on the casing 37 and is provided with air intake 39 and two shafts 41 of the hollow of venthole 40, be installed in the hollow stirring vane 42 of array on the shaft 41, steam outlet pipe 43 that communicates with casing 37 inner chambers and the chuck 44 that is arranged on the casing Lower Half outside, this chuck 44 also is provided with air intake 45 and venthole 46, wherein the inner chamber of shaft 41 and stirring vane 42 communicates, be installed on the shaft 1 stirring vane 42 axioversions, can control feeding speed; When motor 31, transmission device drives stirring vane 42 rotations, rubbish in the promotion casing 37 is in the time of discharging opening 36 motions, by respectively to feeding heat carrier such as high steams in hollow shaft 41 and the chuck 44, downside inwall by casing 37, hollow shaft 41 and hollow stirring vane 42 carry out heat exchange by the mode and the rubbish of heat conduction and radiation, wherein moisture vaporization, discharge from steam outlet pipe 43, reach the purpose that dehydrates, but the upper inside walls of the casing 37 of this device can not realize and the rubbish heat exchange, heat exchange area is less, influence heat exchange efficiency, reduced water separation capability; And directly enter atmosphere after the thermophore heat exchange, can not be recycling, serious environment pollution.
The utility model content
The purpose of this utility model is the above-mentioned shortcoming at prior art, and the high temperature circulation flue gas that a kind of heat exchange area is big, heat exchange efficiency is high, environmental pollution is little stirring drier is provided.
For achieving the above object, high temperature circulation flue gas stirring drier of the present utility model, comprise motor, transmission device, have charging aperture and discharging opening casing, be installed in the hollow on the casing two shafts, be installed in the hollow stirring vane of array on the shaft, the steam outlet pipe that communicates with chassis cavity, it is characterized in that described casing is the chuck of hollow, on the hollow shaft between the inside and outside wall of chuck, be provided with several passages, on casing, also be provided with the air inlet and the gas outlet that communicate with its chuck inner chamber; By feeding heat carrier from air inlet, and pass through the inner chamber of whole chuck, shaft, stirring vane respectively, discharge by the gas outlet, whole inwall, shaft and the stirring vane of chuck carry out heat exchange by the mode and the rubbish of heat conduction and radiation in this process, wherein moisture vaporization, discharge from steam outlet pipe, reach the purpose that dehydrates; Owing to increased heat exchange area, improved heat exchange efficiency;
As further improvement of the utility model, this high temperature circulation flue gas stirring drier also comprises heating furnace circulation distribution plenum and blower fan, and heating furnace circulation distribution plenum comprises casing, charge door, air inlet, burner, air inlet and air outlet; Air inlet on the casing is connected in series with the air outlet of blower fan and heating furnace circulation distribution plenum successively by airduct, and the gas outlet on the casing connects by the air inlet of airduct with heating furnace circulation distribution plenum; This structure directly feeds in the chuck by the high-temperature flue gas that fuel combustion is obtained, and reclaim to enter once more in the heating furnace circulation distribution plenum from the gas outlet and be heated, can improve the utilization rate of baking temperature and fuel, realize the recycling of flue gas simultaneously, significantly reduced the exhaust gas discharging amount, environmental pollution is little;
As further improvement of the utility model, on casing, also be provided with the several cool air hoses that communicate with its inner chamber; Because the utility model is in the constant temperature duty substantially, gasification cracking and then burning the partial material hot-spot may appear and in material in dry run, feeding cold air by cool air hose for chassis cavity in case of necessity, can suitably lower the temperature to material, and accelerate the discharging of water vapour and material is carried out effective deodorizing, guarantee the security of operation;
In sum, high temperature circulation flue gas stirring drier of the present utility model has the advantage that heat exchange area is big, heat exchange efficiency is high, environmental pollution is little and security is good, and can carry out effective deodorizing to rubbish.
Description of drawings
Fig. 1 is the structural representation of existing stirring drier.
Fig. 2 is the structural representation of the utility model embodiment.
Fig. 3 is the A-A cutaway view of Fig. 2.
Fig. 4 is the B-B cutaway view of Fig. 2.
Fig. 5 is the structural representation of heating furnace circulation distribution plenum.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is further described.
By Fig. 2, Fig. 3 and shown in Figure 4, this high temperature circulation flue gas stirring drier, comprise motor 1, by belt pulley 2, decelerator 3, the transmission device that gear-box 4 is formed, the casing 7 that has charging aperture 5 and discharging opening 6, two cool air hoses 8 that are installed in casing 7 both sides respectively and communicate with its inner chamber, be installed in two shafts 10 of the hollow on the casing 7 by the bearing 9 at two ends, be installed in many groups of hollow stirring vanes 11 on the shaft 10 axioversion, the steam outlet pipe 12 that communicates with casing 7 inner chambers, heating furnace circulation distribution plenum 13 and blower fan 14, wherein said casing 7 is the chuck of hollow, be positioned at chuck, outer wall 7a, hollow shaft 10 between the 7b is provided with a plurality of passages 15, on casing 7, also be provided with the air inlet 16 and the gas outlet 17 that communicate with its chuck inner chamber, for ease of maintenance, casing 7 is by last, lower casing connects by flange and forms; Cool air hose 8 communicates with the inner chamber of casing 7 by many arm 8a, and by shown in Figure 5, heating furnace circulation distribution plenum 13 comprises casing 18, charge door 19, air inlet 20, burner 21, air inlet 22 and air outlet 23; Air inlet 16 on the casing 7 is connected in series with the air outlet 23 of blower fan 14 and heating furnace circulation distribution plenum 13 successively by airduct, and the gas outlet 16 on the casing 7 connects by the air inlet 22 of airduct with heating furnace circulation distribution plenum 13.
The utility model is by producing high-temperature flue gas in heating furnace circulation distribution plenum combust fuel, under the effect of blower fan, high-temperature flue gas is sent in the inner chamber of the chuck inner chamber of casing and shaft 10, stirring vane 11, promote in the process of rubbish at stirring vane 11, carry out heat exchange by chuck inwall 7a, shaft 10 and stirring vane 11 with high wet refuse, the water vapour that produces is discharged by steam outlet pipe 12, and the flue gas after the heat exchange enters heating furnace circulation distribution plenum by gas outlet 17 and utilizes once more; Can in cool air hose 8, feed cold air in case of necessity, rubbish is suitably lowered the temperature.
Claims (3)
1. high temperature circulation flue gas stirring drier, comprise motor, transmission device, have charging aperture and discharging opening casing, be installed in the hollow on the casing two shafts, be installed in the hollow stirring vane of array on the shaft, the steam outlet pipe that communicates with chassis cavity, it is characterized in that described casing is the chuck of hollow, on the hollow shaft between the inside and outside wall of chuck, be provided with several passages, on casing, also be provided with the air inlet and the gas outlet that communicate with its chuck inner chamber.
2. high temperature circulation flue gas stirring drier according to claim 1, it is characterized in that this high temperature circulation flue gas stirring drier also comprises heating furnace circulation distribution plenum and blower fan, heating furnace circulation distribution plenum comprises casing, charge door, air inlet, burner, air inlet and air outlet; Air inlet on the casing is connected in series with the air outlet of blower fan and heating furnace circulation distribution plenum successively by airduct, and the gas outlet on the casing connects by the air inlet of airduct with heating furnace circulation distribution plenum.
3. high temperature circulation flue gas stirring drier according to claim 1 and 2 is characterized in that also being provided with the several cool air hoses that communicate with its inner chamber on casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620036031 CN200968766Y (en) | 2006-10-30 | 2006-10-30 | High-temperature circulating flue gas agitating drying machines |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620036031 CN200968766Y (en) | 2006-10-30 | 2006-10-30 | High-temperature circulating flue gas agitating drying machines |
Publications (1)
| Publication Number | Publication Date |
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| CN200968766Y true CN200968766Y (en) | 2007-10-31 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN 200620036031 Expired - Fee Related CN200968766Y (en) | 2006-10-30 | 2006-10-30 | High-temperature circulating flue gas agitating drying machines |
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| CN (1) | CN200968766Y (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197651A (en) * | 2014-08-12 | 2014-12-10 | 德清县兴拓木板厂（普通合伙） | Wood bit dryer |
| CN105439416A (en) * | 2016-01-06 | 2016-03-30 | 王良源 | Sludge treatment system |
| CN105502881A (en) * | 2016-01-28 | 2016-04-20 | 王海龙 | Sludge treatment system |
| CN105565641A (en) * | 2016-01-06 | 2016-05-11 | 王良源 | Solid-liquid mixture processing system |
| CN105585237A (en) * | 2016-01-06 | 2016-05-18 | 王良源 | Improved solid-liquid mixed material treatment system |
| CN105605892A (en) * | 2016-01-06 | 2016-05-25 | 王良源 | High-efficiency solid-liquid mixture processing system |
| CN105621850A (en) * | 2016-01-28 | 2016-06-01 | 王海龙 | Improved sludge treatment system |
| CN105668976A (en) * | 2016-01-06 | 2016-06-15 | 王良源 | Solid-liquid mixture processing method |
| CN105712604A (en) * | 2016-01-28 | 2016-06-29 | 王海龙 | Improved material processing system |
| CN106120527A (en) * | 2016-08-19 | 2016-11-16 | 长沙伟诺机电有限公司 | A kind of pavement maintenance truck |
| CN106196992A (en) * | 2016-08-22 | 2016-12-07 | 北京神雾环境能源科技集团股份有限公司 | The water vapour that refuse pyrolysis produces is used for the system and method for garbage drying after heating up |
| CN106196955A (en) * | 2016-08-31 | 2016-12-07 | 义乌市悦源环境科技有限公司 | A kind of High-efficiency dryer |
| CN106765162A (en) * | 2016-12-20 | 2017-05-31 | 四川雷鸣生物环保工程有限公司 | Circulating flue gas stirring drier |
| CN107200457A (en) * | 2017-06-27 | 2017-09-26 | 苏州克莱尔环保科技有限公司 | A kind of sludge vacuum drying machine |
| CN107270673A (en) * | 2017-06-13 | 2017-10-20 | 成都赋阳技术开发有限公司 | A kind of medical pharmacy and industrial chemicals stirring drying device |
| CN111550998A (en) * | 2020-06-06 | 2020-08-18 | 新昌县盈启自动化设备有限公司 | Dewatering device for waste incineration power generation |
| CN112066678A (en) * | 2020-09-18 | 2020-12-11 | 潢川县鹏升畜产品有限公司 | Enteric protein powder drying system |
-
2006
- 2006-10-30 CN CN 200620036031 patent/CN200968766Y/en not_active Expired - Fee Related
Cited By (27)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104197651A (en) * | 2014-08-12 | 2014-12-10 | 德清县兴拓木板厂（普通合伙） | Wood bit dryer |
| CN105585237B (en) * | 2016-01-06 | 2018-08-03 | 王良源 | A kind of improved Solid-liquid mixture processing system |
| CN105439416A (en) * | 2016-01-06 | 2016-03-30 | 王良源 | Sludge treatment system |
| CN105668976B (en) * | 2016-01-06 | 2018-12-28 | 王良源 | A kind of Solid-liquid mixture processing method |
| CN105565641A (en) * | 2016-01-06 | 2016-05-11 | 王良源 | Solid-liquid mixture processing system |
| CN105585237A (en) * | 2016-01-06 | 2016-05-18 | 王良源 | Improved solid-liquid mixed material treatment system |
| CN105605892A (en) * | 2016-01-06 | 2016-05-25 | 王良源 | High-efficiency solid-liquid mixture processing system |
| CN105668976A (en) * | 2016-01-06 | 2016-06-15 | 王良源 | Solid-liquid mixture processing method |
| CN105565641B (en) * | 2016-01-06 | 2018-12-28 | 王良源 | A kind of Solid-liquid mixture processing system |
| CN105605892B (en) * | 2016-01-06 | 2018-09-25 | 王良源 | A kind of high efficiency Solid-liquid mixture processing system |
| CN105439416B (en) * | 2016-01-06 | 2018-08-03 | 王良源 | Sludge treating system |
| CN105621850A (en) * | 2016-01-28 | 2016-06-01 | 王海龙 | Improved sludge treatment system |
| CN105502881A (en) * | 2016-01-28 | 2016-04-20 | 王海龙 | Sludge treatment system |
| CN105712604B (en) * | 2016-01-28 | 2019-03-19 | 乐清市拓展机械科技有限公司 | A kind of improved material handling system |
| CN105712604A (en) * | 2016-01-28 | 2016-06-29 | 王海龙 | Improved material processing system |
| CN105621850B (en) * | 2016-01-28 | 2018-07-17 | 乐清市足资初生物科技有限公司 | A kind of improved sludge treating system |
| CN105502881B (en) * | 2016-01-28 | 2018-07-17 | 乐清市足资初生物科技有限公司 | A kind of sludge treating system |
| CN106120527A (en) * | 2016-08-19 | 2016-11-16 | 长沙伟诺机电有限公司 | A kind of pavement maintenance truck |
| CN106120527B (en) * | 2016-08-19 | 2019-03-29 | 长沙伟诺汽车制造有限公司 | A kind of pavement maintenance truck |
| CN106196992A (en) * | 2016-08-22 | 2016-12-07 | 北京神雾环境能源科技集团股份有限公司 | The water vapour that refuse pyrolysis produces is used for the system and method for garbage drying after heating up |
| CN106196955A (en) * | 2016-08-31 | 2016-12-07 | 义乌市悦源环境科技有限公司 | A kind of High-efficiency dryer |
| CN106765162A (en) * | 2016-12-20 | 2017-05-31 | 四川雷鸣生物环保工程有限公司 | Circulating flue gas stirring drier |
| CN107270673A (en) * | 2017-06-13 | 2017-10-20 | 成都赋阳技术开发有限公司 | A kind of medical pharmacy and industrial chemicals stirring drying device |
| CN107270673B (en) * | 2017-06-13 | 2019-09-13 | 广西科伦制药有限公司 | A kind of medical pharmacy and industrial chemicals stirring drying device |
| CN107200457A (en) * | 2017-06-27 | 2017-09-26 | 苏州克莱尔环保科技有限公司 | A kind of sludge vacuum drying machine |
| CN111550998A (en) * | 2020-06-06 | 2020-08-18 | 新昌县盈启自动化设备有限公司 | Dewatering device for waste incineration power generation |
| CN112066678A (en) * | 2020-09-18 | 2020-12-11 | 潢川县鹏升畜产品有限公司 | Enteric protein powder drying system |
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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: 20071031 Termination date: 20121030 |