CN2563443Y - Illiptically rotary unloading garbage incinerator - Google Patents
Illiptically rotary unloading garbage incinerator Download PDFInfo
- Publication number
- CN2563443Y CN2563443Y CN 02266740 CN02266740U CN2563443Y CN 2563443 Y CN2563443 Y CN 2563443Y CN 02266740 CN02266740 CN 02266740 CN 02266740 U CN02266740 U CN 02266740U CN 2563443 Y CN2563443 Y CN 2563443Y
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- Prior art keywords
- elliptic
- tower
- difference
- discharging
- elliptical
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Abstract
The utility model provides an illiptic rotary unloading garbage incinerator, comprising a furnace body, an igniter, a waste-feeding air-inducting and air supply system, and an unloading device (3). The unloading device comprises an elliptic cylinder (12) and an elliptic rotary tower (8), wherein the elliptic rotary tower is arranged in the elliptic cylinder, the elliptic rotary tower and the elliptic cylinder has the same pivot, and the elliptic rotary tower performs 360-degree rotation around the elliptic cylinder. The difference between the long axes, the difference between the short axes and the difference between the long and short axes of the two elliptic orbits are the same. When the elliptic rotary tower rotates in the elliptic cylinder, the clinkers agglomerate and are squeezed and smashed by the lug (9) of the tower and the internal and external jaw plates (10),(11) of the ellipse, which reduces manual intervention. After the smashing status is improved, ventilation status is better, the thermal efficiency is improved, the combustion is complete and full and the waste processing capacity is strengthened.
Description
Technical field
The utility model relates to domestic waste incineration.
Technical background
In the prior art, house refuse is handled stove (patent No. ZL95243443.1) continuously and is disclosed a kind of supply air system that adopts end wind and crosswind input to combine, and its device for discharging is a rotary column, distribution rhombus lug on the body of the tower.Because after the waste incineration slagging scorification becomes piece, has certain compression strength, under the extruding situation of existing rotary column, in case pulverize the granularity that does not reach regulation, discharging is not smooth, will cause performance of ventilating to reduce, and causes end wind air-supply to weaken, sometimes the manual intervention of having to adopt could solve unimpeded problem.
Summary of the invention
In order to allow house refuse in burning process, the incineration firing on upper strata is fully complete, impels supply air system unblocked all the time, and the ability of the crashing steel (iron) slag block of the device for discharging that is bound to is strengthened, the purpose of this utility model is to provide a kind of can strengthen the crashing steel (iron) slag block ability, and the device for discharging of material granularity is unloaded in control.
The utility model is to realize like this, the incinerator of a kind of ELLIPTIC REVOLUTION formula discharging, formed by body of heater, igniter, feeding, air inducing supply air system, device for discharging, its device for discharging is made up of elliptical cylinder and ELLIPTIC REVOLUTION tower, the ELLIPTIC REVOLUTION tower is positioned at elliptical cylinder, ELLIPTIC REVOLUTION tower and elliptical cylinder are same center, and the ELLIPTIC REVOLUTION tower is done 360 ° of rotations around elliptical center.
The incinerator of above-mentioned ELLIPTIC REVOLUTION formula discharging, the difference of the long and short axle of the elliptical orbit of elliptical cylinder 12 equal long and short axle poor of the elliptical orbit 13 of ELLIPTIC REVOLUTION tower 8, and all equate with the difference of the major axis of two elliptical orbits and the difference of minor axis.
The incinerator of above-mentioned ELLIPTIC REVOLUTION formula discharging, the difference of the long and short axle of the elliptical orbit 13 of ELLIPTIC REVOLUTION tower 8 is 50mm.
Operation principle of the present utility model is: the incinerator of a kind of ELLIPTIC REVOLUTION formula discharging, its body of heater are vertical cylindrical shell, and all the other are configured to igniter, feeding, air inducing supply air system, device for discharging.House refuse from hopper from top to bottom, by uniformly dispersings such as upper of furnace body, distributing devices at the body of heater inner chamber.After igniting is burned first, the air supply mode that adopts end wind and crosswind to combine, the grog of grilling thoroughly, through device for discharging, the continuous discharging of dipleg.The rotary column bottom tray changes ellipse into by circle in the device for discharging of the present utility model, and the major axis a of elliptical orbit and the difference of minor axis b are a fixed number h; The major axis A of the elliptical orbit of its peripheral elliptical cylinder concentric with it and the difference of minor axis B also are h, and major axis A, the difference of a and the difference of minor axis B, b are all h.During the discharging program start, under the drive of power transmission shaft, rotary column rotates, broken covering slagging scorification piece is thereon sheared, squeezed to water chestnut shape lug on the body of the tower, clinker is scattered in the gap that the elliptical orbit of rotary column bottom tray and cylindrical shell elliptical orbit form, along with the ELLIPTIC REVOLUTION tower is done 360 ° of rotations, the variation of gap generating period in elliptical cylinder.In the utility model, on long axis direction, the gap variation is controlled between the 25-50mm; On short-axis direction, the gap variation is controlled between the 0-25mm; Other gaps also change size in specific scope.The clinker that is trapped in is wherein done further fragmentation, guaranteed the discharging process.
After the utility model was implemented, discharging was smooth and easy, and ventilation shape mouth improves, and heat is imitated high; Reduced the worry of manual intervention clinker fragmentation.
Description of drawings
Fig. 1 is the incinerator structural representation.Fig. 2 is the ELLIPTIC REVOLUTION formula discharging structure schematic diagram of the incinerator of the utility model ELLIPTIC REVOLUTION formula discharging.Fig. 3 is an ELLIPTIC REVOLUTION formula discharging track schematic diagram.
1 is upper of furnace body among the figure, and 2 is the body of heater middle part, and 3 is device for discharging, and 4 is turning cylinder, and 5 is tube connector, 6 is dipleg, and 7 is motor, and 8 is rotary column, and 9 is lug, and 10 is outer jaw, 11 is interior jaw, and 12 is elliptical cylinder, and 13 is interior jaw elliptical orbit, and 14 is outer jaw elliptical orbit.
Preferred forms
The body of heater height is 12000mm in the present embodiment, and the body of heater external diameter is 3700mm.Upper of furnace body 1, middle part 2 are cylindric, adopt alumina firebrick to be built into, and purpose is insulation, wear-resisting.In the body of heater bottom, promptly near device for discharging 3, body of heater is made the elliptical cylinder 12 that interior lining panel is a steel plate, its major axis is 2500mm, minor axis is 2450mm.The bottom tray top of ELLIPTIC REVOLUTION tower 8 is the body of the tower of the water chestnut shape lug 9 that is evenly distributed in the device for discharging, pallet is oval, the holding tray surface periphery is surrounded by a leg-of-mutton interior jaw 11 of piece, and the elliptical orbit 13 of interior jaw 11 is controlled at major axis 2050mm, minor axis 2000mm; Same with it plane, the corresponding welding-on outer jaw 10 formed elliptical orbits 14 on the elliptical cylinder 12 of steel are controlled at major axis 2100mm, minor axis 2050mm.The height of ELLIPTIC REVOLUTION tower 8 is 1500mm, make the bed of material attenuation in centre, so that the easier shearing when rotating of the water chestnut shape lug 9 on the body of the tower, extruding slagging scorification piece, the slagging scorification piece is scattered in the gap between the inside and outside jaw 11,10 on two elliptical orbits, further is subjected to periodic extruding, fragmentation.By contrast, grinding particle size also is subjected to effective control, is more convenient for falling into dipleg 6.
Claims (3)
1, the incinerator of a kind of ELLIPTIC REVOLUTION formula discharging, it is made up of body of heater, igniter, feeding, air inducing supply air system, device for discharging (3), it is characterized in that its device for discharging (3) is made up of elliptical cylinder (12) and ELLIPTIC REVOLUTION tower (8), ELLIPTIC REVOLUTION tower (8) is positioned at elliptical cylinder (12), ELLIPTIC REVOLUTION tower (8) and elliptical cylinder (12) are same center, and ELLIPTIC REVOLUTION tower (8) is done 360 ° of rotations around elliptical center.
2, the incinerator of ELLIPTIC REVOLUTION formula according to claim 1 discharging, the difference of long and short axle that it is characterized in that the elliptical orbit of elliptical cylinder (12) equals long and short axle poor of the elliptical orbit (13) of ELLIPTIC REVOLUTION tower (8), and all equates with the difference of the major axis of two elliptical orbits and the difference of minor axis.
3, the incinerator of ELLIPTIC REVOLUTION formula according to claim 2 discharging is characterized in that long and short difference of the elliptical orbit (13) of ELLIPTIC REVOLUTION tower (8) is 50mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02266740 CN2563443Y (en) | 2002-08-30 | 2002-08-30 | Illiptically rotary unloading garbage incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02266740 CN2563443Y (en) | 2002-08-30 | 2002-08-30 | Illiptically rotary unloading garbage incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2563443Y true CN2563443Y (en) | 2003-07-30 |
Family
ID=33732488
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02266740 Expired - Fee Related CN2563443Y (en) | 2002-08-30 | 2002-08-30 | Illiptically rotary unloading garbage incinerator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2563443Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100432532C (en) * | 2006-07-04 | 2008-11-12 | 潘云芳 | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator |
-
2002
- 2002-08-30 CN CN 02266740 patent/CN2563443Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100432532C (en) * | 2006-07-04 | 2008-11-12 | 潘云芳 | Combined incineration treatment method for refuse and special vertical oxygen-enriched continuous incinerator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |