CN205860751U - A kind of desiccant inclined kiln of particulate matter - Google Patents
A kind of desiccant inclined kiln of particulate matter Download PDFInfo
- Publication number
- CN205860751U CN205860751U CN201620604904.XU CN201620604904U CN205860751U CN 205860751 U CN205860751 U CN 205860751U CN 201620604904 U CN201620604904 U CN 201620604904U CN 205860751 U CN205860751 U CN 205860751U
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- dividing plate
- particulate matter
- heater
- desiccant
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Abstract
nullThis utility model relates to a kind of desiccant inclined kiln of particulate matter，Belong to particulate matter drying equipment technical field，This kiln includes the body of heater with feeding mouth and discharging opening，Conveyer belt conveying mechanism it is provided with below discharging opening，Furnace interior is divided into one group of drying unit by dividing plate，Dividing plate is hollow structure and there is air vent on surface，Dividing plate top air inlet connects hot-air system，Air outlet is had on body of heater，Dividing plate gradient is 20 40 degree，Dividing plate is provided with air channel valve，Including swing handle and the rotor plate that is positioned at diaphragm internal，The draught area of rotor plate regulation dividing plate，Drying unit has one group of mass flow control valve，Including the spanner being positioned at outside body of heater、Gear support and the turnover panel being positioned in drying unit，The hole, location of spanner is positioned with the gear hole on gear support by bearing pin，Thus control turnover panel rotational angle，After using this kiln，The yield rate of particulate matter is higher，The particulate matter aridity at each position is more consistent，Being dried of single particle is the most uniform.
Description
Technical field
This utility model belongs to particulate matter drying equipment technical field, is specifically related to a kind of particulate matter desiccant inclined
Kiln.
Background technology
A lot of particulate matters are to be bondd by the powder containing moisture to constitute, and such as coal briquette, solid fertilizer etc., coal briquette is by coal
Powder is made, and is then dried by dry kiln.In prior art, dry kiln is divided into two classes, and a kind of is vertical,
A kind of is horizontal.Horizontal is, and one end enters one brings out, and dries by electrically heated mode, temperature and the bad control of speed,
The coal briquette aridity of kiln discharge is inadequate, and during later stage use, efficiency of combustion is relatively low；Vertical is feeds from top, from below defeated
Send band discharging, dry by hot blast, be obviously improved than the drying effect of horizontal kiln, but there is it in drying course
His problem, after top feeds, coal briquette extrudes up and down and easily causes broken, and the coal briquette yield rate causing vertical kiln is relatively low.
Utility model content
The shortcoming that this utility model overcomes prior art, it is provided that a kind of desiccant inclined kiln of particulate matter, should
Dividing plate in kiln is obliquely installed, it is to avoid mutually extrude the phenomenon that the percent defective caused raises after particulate matter pan feeding, additionally, every
Mass flow control valve in the air channel valve arranged on plate and drying unit controls the degree of drying of particulate matter, can either make
Aridity accurately controls, and contributes to again energy-saving and emission-reduction.
Concrete technical scheme of the present utility model is:
A kind of desiccant inclined kiln of particulate matter, is respectively provided with the stove of feeding mouth and discharging opening including upper and lower two ends
Body, discharge outlet is provided with baiting valve, and upright to being provided with conveyer belt conveying mechanism under discharging opening, furnace interior is by arranging one
Organizing parallel dividing plate and be divided into one group of drying unit, dividing plate is hollow structure and surface configuration has uniform air vent, dividing plate top
Being provided with air inlet and connection has hot-air system, sidewall of the furnace body is provided with air outlet, key point is, described dividing plate is with perpendicular
The angle faced directly is 20-40 degree.
Described dividing plate is 30 degree with the angle of vertical plane.
Being provided with one group of air channel valve in described dividing plate, air channel valve includes being positioned at the swing handle outside body of heater and position
In the rotor plate of diaphragm internal, swing handle is connected with rotor plate, rotor plate exterior contour and diaphragm internal cross sectional shape phase
With.
Described air channel valve is set to two on each dividing plate, is respectively arranged at top and the middle part of dividing plate.
Described drying unit is provided with one group of mass flow control valve, and described mass flow control valve includes being positioned at stove
The spanner of external body, gear support and the turnover panel being positioned in drying unit, gear support is arcuate structure and is fixed on outside body of heater
On wall, the end face of gear support being provided with one group of gear hole, spanner one end is provided with rotating shaft and passes in the middle part of body of heater and turnover panel solid
Fixed, the other end is provided with hole, location, and the hole, location of spanner is fixed location by bearing pin and gear hole, thus forms turnover panel
Shift-position changing mechanism.
Described mass flow control valve is set to two on each drying unit, is respectively arranged in drying unit
Portion and bottom.
The described air vent on dividing plate includes vertical aperture layer that interlayer arranges and horizontal aperture layer, and vertical aperture layer includes one group
The vertical hole of laterally homogeneous arrangement, horizontal aperture layer includes the transverse holes of one group of laterally homogeneous arrangement.
The beneficial effects of the utility model are: dividing plate carries out 20 degree to 40 degree be obliquely installed, it is possible to make particulate matter fall
Time a part of action of gravity on dividing plate, alleviate the extruding force of lower floor's particulate matter, greatly reduce particulate matter and be squeezed damage
Ratio, substantially increase yield rate, on dividing plate arrange air channel valve the hot blast ventilation in drying unit can be made to obtain
Zonal control, thus the particulate matter of the different aridity of zones of different is carried out hot-air seasoning, and the material stream in drying unit
Control valve can change the area of section of drying unit, and then changes the speed of dropout, i.e. particulate matter flow, this
Logistics capacity combines hot blast temperature to grain, particulate matter is dried control, the baking of particulate matter by the opening degree of air channel valve accurately
Dry effect is significantly improved, but also can significantly save the usage amount of hot blast, reduces the burning and exhausting producing hot blast, subtracts
Light consumed resource and the pollution level to environment.
Accompanying drawing explanation
Fig. 1 is the structural representation of kiln in this utility model.
Fig. 2 is the structural representation of mass flow control valve.
Fig. 3 is the structural representation of dividing plate.
In accompanying drawing, 1, feeding mouth, 2, discharging opening, 3, body of heater, 4, dividing plate, 5, conveyer belt conveying mechanism, 501, vertical hole,
502, transverse holes, 6, air inlet, 7, air outlet, 8, swing handle, 9, spanner, 10, gear support, 11, turnover panel, 12, gear hole,
13, rotating shaft, 14, hole, location, 15, bearing pin, 16, clean-up port.
Detailed description of the invention
This utility model relates to a kind of desiccant inclined kiln of particulate matter, is respectively provided with feeding mouth including upper and lower two ends
1 and the body of heater 3 of discharging opening 2, be provided with baiting valve at discharging opening 2,2 times Founders of discharging opening to being provided with conveyer belt conveying mechanism 5,
Body of heater 3 inside is divided into one group of drying unit by arranging one group of parallel dividing plate 4, and dividing plate 4 has for hollow structure and surface configuration
Uniform air vent, dividing plate 4 top is provided with air inlet 6 and connection has hot-air system, and body of heater 3 sidewall is provided with air outlet
7, described dividing plate 4 is 20-40 degree with the angle of vertical plane.
Specific embodiment, as depicted in figs. 1 and 2, dividing plate 4 is 30 degree with the angle of vertical plane, when particulate matter falls, one
Part action of gravity, on dividing plate 4 end face, this reduces the degree that is squeezed of lower floor's particulate matter, the overall performance of particulate matter
Access holding, it is to avoid be extruded broken situation, substantially increase the yield rate of particulate matter, the air vent bag on dividing plate 4
Including vertical aperture layer and horizontal aperture layer that interlayer is arranged, vertical aperture layer includes the vertical hole 501 of one group of laterally homogeneous arrangement, transverse holes
Layer includes the transverse holes 502 of one group of laterally homogeneous arrangement, and hot blast leads to adjacent being dried by vertical hole 501 and transverse holes 502
In unit, finally the air outlet 7 from body of heater 3 sidewall blows out, and forms the dry air channel of particulate matter, transverse holes 502 and vertical hole
The interlayer of 501 arranges and can preferably mate with the particulate matter of ball-type, and each position of particulate matter can be more uniformly
Contact with hot blast, for circular port, use vertical hole 501 of the same area and transverse holes 502 to be difficult to make particulate matter card
Live and cannot blanking, and use simple vertical hole 501 or transverse holes 502 can cause each position of particulate matter be dried not
Uniformly, therefore, the interlayer in transverse holes 502 and vertical hole 501 arranges the drying uniformity that can increase particulate matter.
Being provided with one group of air channel valve in dividing plate 4, one group of air channel valve quantity on each dividing plate 4 is two, sets respectively
Be placed in top and the middle part of dividing plate 4, air channel valve include the swing handle 8 being positioned at outside body of heater 3 and be positioned within dividing plate 4 turn
Dynamic plate, swing handle 8 is connected with rotor plate, and rotor plate exterior contour is identical with dividing plate 4 inner cross-sectional shape, turns by rotating
Rotor plate is rotated by dynamic handle 8, and the angle change between rotor plate and dividing plate 4 inner section can cause the change of ventilation
Changing, and then change the ventilation of hot blast, when rotor plate is vertical state, ventilation is maximum, when rotor plate is level, ventilates
Amount minimum, the ventilation of hot blast carries out Flow-rate adjustment respectively in dividing plate 4 upper and lower, and hot blast can be more accurately to needs
The particulate matter dried is dried, and the particulate matter oven-dried condition at each position can either be made to keep consistent, again it can be avoided that each
The unified heat waste caused of ventilating in position is dried excessively with local, and bottom of furnace body is provided with clean-up port 16, by clean-up port 16
Can be to the cleaning carrying out ground product bottom body of heater 3 so that in the particulate matter after discharging, the content of ground product greatly reduces, it is to avoid
Inconvenience during the loaded down with trivial details and use of later stage classification.
Each single drying unit is provided with one group of mass flow control valve, each drying unit is set to two
Individual, it is respectively arranged at middle part and the bottom of drying unit, described mass flow control valve includes being positioned at the spanner outside body of heater 3
9, gear support 10 and the turnover panel 11 that is positioned in drying unit, gear support 10 is for arcuate structure and is fixed on body of heater 3 outer wall,
Being provided with one group of gear hole 12 on the end face of gear support 10, spanner 9 one end is provided with rotating shaft 13 and passes in body of heater 3 and turnover panel 11
Portion is fixed, and the other end is provided with hole 14, location, and the hole, location 14 of spanner 9 is fixed location by bearing pin 15 and gear hole 12,
Thus form the shift-position changing mechanism of turnover panel 11, being rotated by rotating shaft 13 and rotate certain angle of turnover panel 11, turnover panel 11 with
Angle between drying unit inwall is changed, and the sectional area of drying unit is changed therewith, the pan feeding flow of particulate matter
Also can change therewith, during turnover panel level, the maximum flow of particulate matter, during turnover panel 11 vertical state, the flow of particulate matter is minimum.
Mass flow control valve and the combination of air channel valve, it is possible to matched by particulate matter flow and ventilation and realize
The oven-dried condition of particulate matter is stable in the aridity needed, and the hot blast ventilation needed when particulate matter flow is big is relatively big, works as needs
When increasing aridity, the flow of particulate matter, or the ventilation of increase hot blast can be reduced, be finally reached required being dried
Degree.
Transverse holes 502 and vertical hole 501 on dividing plate make being dried of each each position of particulate matter more uniform, air channel
The setting of valve and mass flow control valve can make again the particulate matter aridity of diverse location reach unanimity, and eventually makes whole
The uniform drying of single particle in individual body of heater 3, the aridity of different parts are more consistent, and can bring certain joint
Energy and emission reduction effect, the angle of inclination set-up mode of dividing plate 4 enables to again the yield rate of particulate matter and is maintained at higher level, makes
The particulate matter quality being dried to obtain with this kiln significantly improves.
Claims (7)
1. the desiccant inclined kiln of particulate matter, is respectively provided with feeding mouth (1) and discharging opening (2) including upper and lower two ends
Body of heater (3), discharging opening (2) place is provided with baiting valve, upright to being provided with conveyer belt conveying mechanism (5), body of heater under discharging opening (2)
(3) inside is divided into one group of drying unit, dividing plate (4) to be hollow structure and surface configuration by arranging one group of parallel dividing plate (4)
There are uniform air vent, dividing plate (4) top to be provided with air inlet (6) and connection has hot-air system, body of heater (3) sidewall is arranged
There is air outlet (7), it is characterised in that: described dividing plate (4) is 20-40 degree with the angle of vertical plane.
A kind of desiccant inclined kiln of particulate matter the most according to claim 1, it is characterised in that: described dividing plate
(4) angle with vertical plane is 30 degree.
A kind of desiccant inclined kiln of particulate matter the most according to claim 1, it is characterised in that: described dividing plate
(4) being provided with one group of air channel valve in, air channel valve includes being positioned at the outside swing handle (8) of body of heater (3) and being positioned at dividing plate (4)
Internal rotor plate, swing handle (8) is connected with rotor plate, rotor plate exterior contour and dividing plate (4) inner cross-sectional shape phase
With.
A kind of desiccant inclined kiln of particulate matter the most according to claim 3, it is characterised in that: described air conduit valve
Door is set to two on each dividing plate (4), is respectively arranged at top and the middle part of dividing plate (4).
A kind of desiccant inclined kiln of particulate matter the most according to claim 1, it is characterised in that: described dry list
Being provided with one group of mass flow control valve in unit, described mass flow control valve includes being positioned at the spanner that body of heater (3) is outside
(9), gear support (10) and the turnover panel (11) that is positioned in drying unit, gear support (10) is arcuate structure and is fixed on body of heater
(3) on outer wall, the end face of gear support (10) being provided with one group of gear hole (12), spanner (9) one end is provided with rotating shaft (13)
Fixing with turnover panel (11) middle part through body of heater (3), the other end is provided with hole, location (14), and the hole, location (14) of spanner (9) is passed through
Bearing pin (15) and gear hole (12) are fixed location, thus form the shift-position changing mechanism of turnover panel (11).
A kind of desiccant inclined kiln of particulate matter the most according to claim 5, it is characterised in that: described material stream
Control valve is set to two on each drying unit, is respectively arranged at middle part and the bottom of drying unit.
A kind of desiccant inclined kiln of particulate matter the most according to claim 1, it is characterised in that: described dividing plate
(4) air vent on includes vertical aperture layer that interlayer arranges and horizontal aperture layer, and vertical aperture layer includes one group of laterally homogeneous arrangement
Vertical hole (501), horizontal aperture layer includes the transverse holes (502) of one group of laterally homogeneous arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620604904.XU CN205860751U (en) | 2016-06-20 | 2016-06-20 | A kind of desiccant inclined kiln of particulate matter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620604904.XU CN205860751U (en) | 2016-06-20 | 2016-06-20 | A kind of desiccant inclined kiln of particulate matter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205860751U true CN205860751U (en) | 2017-01-04 |
Family
ID=57637011
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620604904.XU Withdrawn - After Issue CN205860751U (en) | 2016-06-20 | 2016-06-20 | A kind of desiccant inclined kiln of particulate matter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205860751U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105928357A (en) * | 2016-06-20 | 2016-09-07 | 高邑县海侨节能技术有限公司 | Inclined vertical kiln furnace for drying particulate matter |
| CN108180505A (en) * | 2018-01-23 | 2018-06-19 | 佛山市琛意工业设计有限公司 | A kind of outdoor heating stove |
-
2016
- 2016-06-20 CN CN201620604904.XU patent/CN205860751U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105928357A (en) * | 2016-06-20 | 2016-09-07 | 高邑县海侨节能技术有限公司 | Inclined vertical kiln furnace for drying particulate matter |
| CN108180505A (en) * | 2018-01-23 | 2018-06-19 | 佛山市琛意工业设计有限公司 | A kind of outdoor heating stove |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170104 Effective date of abandoning: 20190409 |