CN205048915U - Belt -Type furnace of aeration stirring - Google Patents
Belt -Type furnace of aeration stirring Download PDFInfo
- Publication number
- CN205048915U CN205048915U CN201520811279.1U CN201520811279U CN205048915U CN 205048915 U CN205048915 U CN 205048915U CN 201520811279 U CN201520811279 U CN 201520811279U CN 205048915 U CN205048915 U CN 205048915U
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- China
- Prior art keywords
- belt
- mesh
- foraminous conveyer
- aeration
- belt kiln
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Abstract
The utility model discloses a belt -Type furnace of aeration stirring, include the belt -Type furnace body and be used for conveying mesh belt (1) to this internal transported substance material of belt -Type furnace, the transport face of conveying mesh belt (1) has the roller bearing that is used for supporting conveying mesh belt (1), the transport face below of conveying mesh belt (1) is equipped with at least one and is used for jet -propelled aeration mouth (2), the utility model discloses can effectively make the material turn, even dry or burn till to can utilize the air -blower to send into the tuber pipe again by the high -pressure hot -air of aeration mouth blowout with the hot -air of belt -Type furnace body inner chamber, the air current drives the material and stirs, accelerates with homogeneous material's drying in the time of reducible energy loss or burns till, the length of significantly reduced production time and kiln, thereby increase of production, quality, reduction in production cost.
Description
Technical field
The utility model relates to a kind of mesh-belt kiln of aeration stirring.
Background technology
Mesh-belt kiln belongs to consecutive production kiln, is widely used in glass-ceramic and chemical industry, is mainly used in the drying of product and burns till.Traditional mesh-belt kiln is foraminous conveyer bottom or top and the bottom heating, and material is layered on foraminous conveyer and remains static relative to foraminous conveyer, and foraminous conveyer at the uniform velocity travels through kiln.Under normal circumstances for pursuing production capacity, solid accumulation thickness is about about 40mm, and such material is just easily heated uneven, occurs half-cooked phenomenon, affects the uniformity of product quality.If reduction material thickness, then need the length lengthening mesh-belt kiln to meet production capacity demand, cause equipment cost to increase substantially and increase operating cost.
Material is static relative to foraminous conveyer on foraminous conveyer, and it is heated by solid conduction, if solid accumulation thickness is large, it is half-cooked just to there will be, dry or firing temperature is too high, surface can be caused overheated, and affect dry materials or burn till quality.
Utility model content
Technical problem to be solved in the utility model is, overcomes the shortcoming of above prior art: provide a kind of and effectively can make material turning, the evenly dry or mesh-belt kiln of aeration stirring that burns till.
Technical solution of the present utility model is as follows: a kind of mesh-belt kiln of aeration stirring, comprise mesh-belt kiln body with for the foraminous conveyer to convey materials in mesh-belt kiln body, the conveyor surface of described foraminous conveyer has the roller bearing for supporting foraminous conveyer, is provided with at least one for jet aeration opening below the conveyor surface of described foraminous conveyer.
As optimization, below the conveyor surface of described foraminous conveyer, be interval with multiple aeration opening be communicated with airduct along foraminous conveyer transmission direction.
As optimization, described airduct is communicated with air blast delivery outlet.
As optimization, the inner space of described air blast input port and mesh-belt kiln body.
As optimization, described aeration opening is rectangle puff prot.
As optimization, the long limit of described rectangle puff prot is parallel with the width of foraminous conveyer.
As optimization, the fumarole array that described aeration opening is arranged by the width along foraminous conveyer forms.
The beneficial effects of the utility model are: the mesh-belt kiln of the utility model aeration stirring, effectively can make material turning, evenly drying or burn till, and can utilize air blast that the hot-air of mesh-belt kiln chamber body is sent into airduct and spray high-pressure hot air by aeration opening again, air-flow drives material turning, while can energy loss being reduced accelerate and homogeneous material drying or burn till, greatly reduce the length of production time and kiln, thus improve Yield and quality, reduce production cost.
Accompanying drawing explanation
Fig. 1 is the mesh-belt kiln delivered inside guipure part-structure schematic diagram of the utility model aeration stirring.
Fig. 2 is that the utility model looks down from foraminous conveyer the structural representation of aeration opening.
Fig. 3 is that the utility model looks down from foraminous conveyer the structural representation of aeration opening.
Fig. 4 is existing mesh-belt kiln structural representation.
In figure: 1, foraminous conveyer; 2, aeration opening; 3, airduct.
Detailed description of the invention
With specific embodiment, the utility model is described in further details below, but the utility model is not only confined to following specific embodiment.
Embodiment
As Figure 1-3, a kind of mesh-belt kiln of aeration stirring, comprise for the mesh-belt kiln body of material drying and for the foraminous conveyer 1 to convey materials in mesh-belt kiln body, the conveyor surface of described foraminous conveyer 1 has the roller bearing for supporting foraminous conveyer 1, described conveyor surface refers to that foraminous conveyer 1 is for carrying, transmitting material and the upper surface contacted with material, is provided with at least one for jet aeration opening 2 below the conveyor surface of described foraminous conveyer 1.Be interval with multiple aeration opening 2 be communicated with airduct 3 along foraminous conveyer 1 transmission direction below the conveyor surface of described foraminous conveyer 1, describedly multiplely refer to two or more.As shown in Figure 1, be spaced a distance along foraminous conveyer 1 transmission direction below the conveyor surface of described foraminous conveyer 1 and be provided with two or more aeration opening 2 be communicated with airduct 3.Described airduct 3 is communicated with air blast delivery outlet.The inner space of described air blast input port and mesh-belt kiln body.As shown in Figure 3, described aeration opening 2 can be rectangle puff prot, and the long limit of described rectangle puff prot is parallel with the width of foraminous conveyer 1.Or the fumarole array that as shown in Figure 2, described aeration opening 2 is arranged by the width along foraminous conveyer 1 forms.
Below be only that feature of the present utility model implements example, the utility model protection domain is not constituted any limitation.The technical scheme that all employings exchange on an equal basis or equivalence is replaced and formed, all drops within the utility model rights protection scope.
Claims (7)
1. the mesh-belt kiln of an aeration stirring, comprise mesh-belt kiln body with for the foraminous conveyer (1) to convey materials in mesh-belt kiln body, the conveyor surface of described foraminous conveyer (1) has the roller bearing for supporting foraminous conveyer (1), it is characterized in that: be provided with at least one below the conveyor surface of described foraminous conveyer (1) for jet aeration opening (2).
2. the mesh-belt kiln of aeration stirring according to claim 1, is characterized in that: be interval with multiple aeration opening (2) be communicated with airduct (3) along foraminous conveyer (1) transmission direction below the conveyor surface of described foraminous conveyer (1).
3. the mesh-belt kiln of aeration stirring according to claim 2, is characterized in that: described airduct (3) is communicated with air blast delivery outlet.
4. the mesh-belt kiln of aeration stirring according to claim 3, is characterized in that: the inner space of described air blast input port and mesh-belt kiln body.
5. the mesh-belt kiln of aeration stirring according to claim 1 and 2, is characterized in that: described aeration opening (2) is rectangle puff prot.
6. the mesh-belt kiln of aeration stirring according to claim 5, is characterized in that: the long limit of described rectangle puff prot is parallel with the width of foraminous conveyer (1).
7. the mesh-belt kiln of aeration stirring according to claim 1 and 2, is characterized in that: the fumarole array that described aeration opening (2) is arranged by the width along foraminous conveyer (1) forms.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520811279.1U CN205048915U (en) | 2015-10-19 | 2015-10-19 | Belt -Type furnace of aeration stirring |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520811279.1U CN205048915U (en) | 2015-10-19 | 2015-10-19 | Belt -Type furnace of aeration stirring |
Publications (1)
Publication Number | Publication Date |
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CN205048915U true CN205048915U (en) | 2016-02-24 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201520811279.1U Active CN205048915U (en) | 2015-10-19 | 2015-10-19 | Belt -Type furnace of aeration stirring |
Country Status (1)
Country | Link |
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CN (1) | CN205048915U (en) |
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2015
- 2015-10-19 CN CN201520811279.1U patent/CN205048915U/en active Active
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C14 | Grant of patent or utility model | ||
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