CN206192081U - Dry bed of ramp type solid material - Google Patents
Dry bed of ramp type solid material Download PDFInfo
- Publication number
- CN206192081U CN206192081U CN201621229914.6U CN201621229914U CN206192081U CN 206192081 U CN206192081 U CN 206192081U CN 201621229914 U CN201621229914 U CN 201621229914U CN 206192081 U CN206192081 U CN 206192081U
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- slope
- solid material
- shuttle groove
- cell body
- ramp type
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Abstract
The utility model discloses a dry bed of ramp type solid material, belong to drying equipment technical field, the cell body that it was put including the inclined that inclines, bottom at the cell body is equipped with the discharge gate, be equipped with in the cell body in the same direction as slope baffle (2) that inclined put of inclining, baffle (2) are separated the cell body and are the slope shuttle groove (1) more than two, the tank bottom is equipped with sinuous coil (3) in slope shuttle groove (1), the high -end of sinuous coil (3) is connected with the vapour source, the low side is connected with water tank (5), support bar (4) of vertical baffle (2) are equipped with at slope shuttle groove (1) tank bottom, the mobile type electrothermal drying case belongs to the technical field of drying devices, sinuous coil (3) are apart from slope shuttle groove (1) 50~100mm of tank bottom, have effluent water sump (6) in slope shuttle groove (1) lower part. The utility model discloses can abundant dry solid material to be favorable to solid material's slip, practice thrift and carry power, simultaneously can also avoid environmental pollution.
Description
Technical field
The utility model is related to a kind of ramp type solid material drying bed, belongs to drying equipment technical field.
Background technology
With industrial expansion, particularly in chemical field production, in order to meet storage, transport, process and use
The different needs of aspect, to the solid material being related in Chemical Manufacture, typically to its hygroscopic water, such as moisture or other volatile liquid
The content of body composition has certain requirement.In existing solid material dried process, usually using hot-air drier, hot air drying
Dry device uses air blower, hot blast is blown into the device for containing solid material to be dried, hygroscopic water therein is gasified and will be generated
Hygroscopic water steam take away, solid material is dried, but there is problems with this drier：Solids in drying process
Material is packed together, and causes to be deposited in innermost solid material hardly resulting in sufficient drying, if additionally, wind-force is excessive,
Easily outer skin materials are caused damage；Meanwhile, when the hygroscopic water of solid material to be dried is larger, if containing solid material to be dried
Device use horizontal positioned, solid material can not natural drainage, cause lower floor's material to be difficult drying because immersion is difficult to discharge,
Additionally, the modes of emplacement is also unfavorable for that the slip of solid material conveys the conveying power, it is necessary to extra.Therefore, design can be fully
A kind of ramp type solid material drying bed for drying, saving conveying power seems particularly necessary.
The content of the invention
This practical technical problem to be solved is to provide a kind of ramp type solid that can fully dry, save conveying power
Dry materials bed, to overcome the deficiencies in the prior art.
The technical solution of the utility model is：A kind of ramp type solid material drying bed, it includes tilted-putted cell body,
Discharging opening is provided with the bottom of cell body, it is characterised in that：It is provided with cell body along the gradient tilted-putted baffle plate, baffle plate is by cell body
It is divided into more than two pieces of slope shuttle groove, shuttle groove bottom land is provided with serpentine coil, the high-end and vapour source phase of serpentine coil on slope
Connection, low side is connected with water tank.
Above-mentioned ramp type solid material drying bed is that on slope, shuttle groove bottom land is provided with the support bar of vertical baffle, snakelike
Coil pipe is fixed on the shuttle groove of slope.
Above-mentioned ramp type solid material drying bed is that the gradient of the slope shuttle groove is 45~65 degree.
Above-mentioned ramp type solid material drying bed is that the groove width of the slope shuttle groove is in 1000~1500mm.
Above-mentioned ramp type solid material drying bed is, serpentine coil is away from 50~100mm of slope shuttle groove bottom land.
Above-mentioned ramp type solid material drying bed is to have cesspool in slope Suo Cao bottoms.
Compared with the prior art, the utility model is set apart from slope shuttle groove on the slope shuttle groove that the gradient is 45~65 degree
The serpentine coil of 50~100mm of bottom land, the high-end of serpentine coil is connected with vapour source, and low side is connected with water tank, so both
Can abundant drying solid material, and can easy solid material slide from top to bottom, save conveying power, meanwhile, be also beneficial to steam
The recycling of vapour condensed water.Cesspool is built in slope Suo Cao bottoms, is so easy to produced sewage in solid material to be dried
Collection, it is to avoid pollution environment.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Specific embodiment
Embodiment 1. is as shown in figure 1, a kind of ramp type solid material drying bed, it includes tilted-putted cell body, in groove
The bottom of body is provided with discharging opening, it is characterised in that：It is provided with cell body along the tilted-putted baffle plate 2 of the gradient, baffle plate 2 divides cell body
More than two pieces of slope shuttle groove 1 is divided into, serpentine coil 3, the high-end and vapour source of serpentine coil 3 are provided with the bottom land of slope shuttle groove 1
It is connected, low side is connected with water tank 5.The support bar 4 of vertical baffle 2 is provided with the bottom land of slope shuttle groove 1, serpentine coil 3 is fixed
On slope shuttle groove 1.The gradient of the slope shuttle groove 1 is 45~65 degree.The groove width of the slope shuttle groove 1 1000~
1500mm.Serpentine coil 3 is away from the 50~100mm of bottom land of slope shuttle groove 1.Cesspool 6 is had in the bottom of slope shuttle groove 1.Open snakelike
The steam valve at the high-end place of coil pipe 3, allows steam to enter serpentine coil 3, is exchanged heat with wet solid material by tube wall, solids
Hygroscopic water in material receives thermal evaporation, and solid material progressively reaches dry requirement；After steam releases heat, water is condensed into, along tube wall
Water tank 5 is flowed to, when the liquid level of water tank 5 is to certain altitude, water pump is opened by condensation water recovery and use.In the minimum of slope shuttle groove 1
Place, if a cesspool 6, collects in solid material stacking and drying process, along the sewage of shuttle bottom land outflow, when the water of cesspool 6
When position is high, starts sewage pump and get to Sewage Disposal treatment, it is ensured that treatment scene does not have sewage pollution environment.
Claims (6)
1. a kind of ramp type solid material drying bed, it includes tilted-putted cell body, discharging opening is provided with the bottom of cell body, its
It is characterised by：It is provided with cell body along the tilted-putted baffle plate of the gradient（2）, baffle plate（2）Cell body is divided into more than two pieces oblique
Slope shuttle groove (1), in slope shuttle groove（1）Bottom land is provided with serpentine coil（3）, serpentine coil（3）It is high-end be connected with vapour source, it is low
End and water tank（5）It is connected.
2. ramp type solid material drying bed according to claim 1, it is characterised in that：In slope shuttle groove（1）Bottom land sets
There is vertical baffle（2）Support bar（4）, serpentine coil（3）It is fixed on slope shuttle groove（1）On.
3. ramp type solid material drying bed according to claim 1 and 2, it is characterised in that：The slope shuttle groove（1）'s
The gradient is 45~65 degree.
4. ramp type solid material drying bed according to claim 3, it is characterised in that：The slope shuttle groove（1）Groove
It is wide in 1000~1500mm.
5. ramp type solid material drying bed according to claim 1, it is characterised in that：Serpentine coil（3）Away from slope shuttle
Groove（1）50~100mm of bottom land.
6. ramp type solid material drying bed according to claim 1, it is characterised in that：In slope shuttle groove（1）Bottom is built
There is cesspool（6）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621229914.6U CN206192081U (en) | 2016-11-16 | 2016-11-16 | Dry bed of ramp type solid material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621229914.6U CN206192081U (en) | 2016-11-16 | 2016-11-16 | Dry bed of ramp type solid material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206192081U true CN206192081U (en) | 2017-05-24 |
Family
ID=58725768
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621229914.6U Active CN206192081U (en) | 2016-11-16 | 2016-11-16 | Dry bed of ramp type solid material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206192081U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362614A (en) * | 2017-08-18 | 2017-11-21 | 贵州赤天化股份有限公司 | A kind of recoverying and utilizing method and its device of coal water slurry gasification fine slag |
-
2016
- 2016-11-16 CN CN201621229914.6U patent/CN206192081U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362614A (en) * | 2017-08-18 | 2017-11-21 | 贵州赤天化股份有限公司 | A kind of recoverying and utilizing method and its device of coal water slurry gasification fine slag |
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