CN2255597Y - Rotation-flow dryer - Google Patents
Rotation-flow dryer Download PDFInfo
- Publication number
- CN2255597Y CN2255597Y CN 95226045 CN95226045U CN2255597Y CN 2255597 Y CN2255597 Y CN 2255597Y CN 95226045 CN95226045 CN 95226045 CN 95226045 U CN95226045 U CN 95226045U CN 2255597 Y CN2255597 Y CN 2255597Y
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- cylindrical shell
- cylinder body
- materials
- rotary flow
- inlet
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Abstract
The utility model relates to a rotary flow drier which is composed of a cylinder body, a material outlet, a material inlet, a hot air inlet, etc. The cylinder body is in a layer structure. All layers of the cylinder body are connected by flanges. A rotary flow plate and a taper-shaped turbulent flow plate are arranged in the cylinder body. Wet materials and hot air generates rotary flow and turbulent flow in the cylinder body through the rotary flow plate and the turbulent flow plate, so that the materials are dried more sufficiently. The utility model with simple structure and small volume is suitable for drying various materials in powder, materials in crystalloid and materials with middle and small sizes.
Description
The utility model relates to drying equipment, especially a kind of rotary flow desiccator.
Present drying to various powderies, crystalloid and small particles material, adopt the drying tube drying mostly, its principle is to need dry material to enter drying tube with hot blast, because drying tube is longer, material is able to abundant drying, but long drying tube makes its floor space also bigger, and the also higher and range of application of cost is restricted.
The utility model purpose just provides little, the dry rotary flow desiccator abundant, applied widely of a kind of volume.
The utility model purpose is implemented by following technical scheme:
Rotary flow desiccator is made of cylindrical shell, material outlet, material inlet, hot-wind inlet etc., cylindrical shell is a layer structure, according to actual conditions, cylindrical shell can be provided with the number of plies that needs, adopt flange to connect between each layer, be provided with eddy flow plate and taper turbulence plate in the cylindrical shell, material inlet and hot-wind inlet are arranged on the orlop cylindrical shell, and material outlet is arranged on the side of the superiors' cylindrical shell.When the material of required drying be viscosity big, easily during agglomerated particle, also stirring vane can be set in the orlop cylindrical shell, stirring vane is by driven by motor.
Rotary flow desiccator of the present utility model is owing to be provided with eddy flow plate and taper turbulence plate in cylindrical shell, the mixed airflow that material and hot blast are formed produces eddy flow and turbulent flow in cylindrical shell, undried material can just be discharged cylindrical shell up to drying in cylindrical shell, dry materials is abundant.For viscosity material big, that easily lump, adopt the cylindrical shell of band stirring vane, can make material loose, avoid piling up, can make dry materials abundant equally.This rotary flow desiccator also has the advantage that volume is little, efficient is high, is fit to the drying of various powderies, crystalloid and medium and small material material.
Below in conjunction with accompanying drawing the utility model is elaborated.
Fig. 1 is the utility model structural representation,
Rotary flow desiccator is made of cylindrical shell 2, material outlet 1, material inlet 6, hot-wind inlet 7 etc.Cylindrical shell 2 is a layer structure, adopts flange to connect between each layer cylindrical shell, is provided with eddy flow plate 3 and taper turbulence plate 4 in the cylindrical shell 2.Material inlet 6 and hot-wind inlet 7 are arranged on the orlop cylindrical shell 5, and material outlet 1 is located at the side of the superiors' cylindrical shell, and orlop cylindrical shell 5 adopts the cylindrical shell of band stirring vane, and stirring vane 8 is arranged in the orlop cylindrical shell 5, and stirring vane 8 is driven by motor 9.
Operation principle of the present utility model: wet stock enters orlop cylindrical shell 5 from material inlet 6, and the high temperature drying air enters orlop cylindrical shell 5 from hot-wind inlet 7, because the effect of the temperature difference, wet stock is heated, and water evaporates is come out, thereby reaches dry purpose.Wet stock is under the effect of hot blast, and the eddy flow plate 3 in cylindrical shell 2 produces eddy flow, makes wet stock and hot blast abundant time of contact, produces turbulent flow under taper turbulence plate 4 effects of the air-flow of eddy flow in cylindrical shell.The material that drying proportion is less is because the effect of turbulent flow, mix with hot blast once more and discharge from material outlet 1, and the bigger wet stock of proportion is separated to barrel more greatly because of suffered eddy flow centrifugal force, is blocked to stay by turbulence plate 4 and continues drying in the cylindrical shell, discharges cylindrical shell up to bone dry.When the material of required drying be viscosity big, easily during agglomerated particle, material is under stirring vane 8 effects of orlop cylindrical shell 5, block being blended makes dry materials more abundant.
Claims (2)
1, a kind of rotary flow desiccator is by cylindrical shell (2), material outlet (1), material inlet (6), hot-wind inlet formations such as (7), it is characterized in that: cylindrical shell (2) is layer structure, adopt flange to connect between each layer cylindrical shell, be provided with eddy flow plate (3) and taper turbulence plate (4) in the cylindrical shell (2), material inlet (6) and hot-wind inlet (7) are arranged on the orlop cylindrical shell (5), and material outlet (1) is located at the side of the superiors' cylindrical shell.
2, rotary flow desiccator according to claim 1 is characterized in that: be provided with stirring vane (8) in the orlop cylindrical shell (5), stirring vane (8) is driven by motor (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95226045 CN2255597Y (en) | 1995-11-01 | 1995-11-01 | Rotation-flow dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 95226045 CN2255597Y (en) | 1995-11-01 | 1995-11-01 | Rotation-flow dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2255597Y true CN2255597Y (en) | 1997-06-04 |
Family
ID=33872294
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 95226045 Expired - Fee Related CN2255597Y (en) | 1995-11-01 | 1995-11-01 | Rotation-flow dryer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2255597Y (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105399301A (en) * | 2015-12-19 | 2016-03-16 | 大连大孤山污水处理有限公司 | Novel sludge drying processing device |
-
1995
- 1995-11-01 CN CN 95226045 patent/CN2255597Y/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105399301A (en) * | 2015-12-19 | 2016-03-16 | 大连大孤山污水处理有限公司 | Novel sludge drying processing device |
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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 |