CN206056120U - The horizontal type fluidized-bed exsiccator of one kind band ramp type - Google Patents
The horizontal type fluidized-bed exsiccator of one kind band ramp type Download PDFInfo
- Publication number
- CN206056120U CN206056120U CN201621088475.1U CN201621088475U CN206056120U CN 206056120 U CN206056120 U CN 206056120U CN 201621088475 U CN201621088475 U CN 201621088475U CN 206056120 U CN206056120 U CN 206056120U
- Authority
- CN
- China
- Prior art keywords
- exsiccator
- gas
- swash plate
- circular hole
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Drying Of Solid Materials (AREA)
Abstract
This utility model is related to the horizontal type fluidized-bed exsiccator of one kind band ramp type of chemical technology field, and it is mainly made up of the outlet of air exhauster, sack cleaner, cyclone dust extractor, gas outlet, exsiccator, wet stock import, wet granular, circular hole swash plate, gas passage, air filter, heater, gas feed and dry material.The exsiccator top is provided with gas outlet, and middle part is provided with circular hole swash plate and gas passage, and left part is provided with dry material outlet, and right part is provided with wet stock import and gas feed；Gas passage makes gas flow to circular hole swash plate from exsiccator bottom.For dedusting and drying are carried out to air, heater enters exsiccator bottom for passing through valve after heating to air to air filter.This utility model is convenient to use, it is easy to manufacture, and equipment investment and maintenance cost are low.
Description
Technical field
This utility model is related to the horizontal type fluidized-bed exsiccator of one kind band ramp type of chemical technology field.
Background technology
Fluidization technique originates from nineteen twenty-one earliest, and it is that the U.S. in 1948 sets up to be applied to earliest be dried industrialized great production
Dorr-solids fluidized the device of Austria's lev, and technique China just started development after 1958.Fluidized bed drying process
Middle bulk material is placed on orifice plate, bottom conveying gas, and material particles are in suspended state when by orifice plate, make material particles
It is fully contacted with gas, carries out quick heat transfer and transmit with moisture.Horizontal multicompartment fluidized bed dryer therein has following
Feature：It is simple to operate, it is easy to operational control；Drying effect is good, residence time destribution narrow range of the material in bed, when being dried
Between be evenly distributed, dry products humidity is uniform；Floor space is little, simple structure, it is easy to manufacture, the low feature of equipment investment.
The content of the invention
This utility model purpose is to be dried medium grain and coarse grained wet stock to be directed to, there is provided a kind of band swash plate
The horizontal type fluidized-bed exsiccator of formula, convenient to use, maintenance cost is low, and drying effect is good.
The technical scheme adopted by this utility model is：
A kind of horizontal type fluidized-bed exsiccator of band ramp type of this utility model, is mainly removed by air exhauster, sack cleaner, whirlwind
Dirt device, gas outlet, exsiccator, wet stock import, wet granular, circular hole swash plate, gas passage, air filter, heater, gas
Import and dry material outlet composition.The exsiccator top is provided with gas outlet, and middle part is provided with circular hole swash plate and gas passage, left part
Dry material outlet is provided with, right part is provided with wet stock import and gas feed；Gas passage makes gas justify from exsiccator bottom flow direction
Hole deviation plate., for carrying out dedusting and drying to air, heater is for passing through valve after heating to air for air filter
Into exsiccator bottom.It is provided with 5 gas passages, the equal diameters of this 5 gas passages in exsiccator altogether；The length of gas passage
Degree increases with the increase of the circular hole swash plate gradient；Circular hole swash plate and horizontal line are into 30 °, and many circular holes are provided with swash plate,
Its Circularhole diameter is less than medium grain diameter.
Advantage of the present utility model：Convenient to use, simple to operate, maintenance cost is low, and drying effect is good.
Description of the drawings
Fig. 1 is a kind of structural representation with the horizontal type fluidized-bed exsiccator of ramp type of this utility model.
Fig. 2 is flow schematic diagram of the air in exsiccator bottom in Fig. 1.
In figure：1. air exhauster, 2. sack cleaner, 3. cyclone dust extractor, 4. gas outlet, 5. exsiccator, 6. wet stock enter
Mouthful, 7. wet granular, 8. circular hole swash plate, 9. gas passage, 10. air filter, 11. heaters, 12. gas outlets, 13. dries
Material outlet.
Specific embodiment
Below in conjunction with the accompanying drawings this utility model is described further.
As shown in Figure 1 and Figure 2, the horizontal type fluidized-bed exsiccator of a kind of band ramp type of this utility model, mainly by air exhauster 1, bag
Formula cleaner unit 2, cyclone dust extractor 3, gas outlet 4, exsiccator 5, wet stock import 6, wet granular 7, circular hole swash plate 8, gas passage
9th, air filter 10, heater 11, gas feed 12 and dry material outlet 13 is constituted.5 top of the exsiccator is provided with outlet
Mouth 4, middle part are provided with circular hole swash plate 8 and gas passage 9, and left part is provided with dry material outlet 13, and it is gentle that right part is provided with wet stock import 6
Body import 12；Gas passage 9 makes gas flow to circular hole swash plate 8 from 5 bottom of exsiccator.Circular hole swash plate 8 with horizontal line into 30 °, and
Many circular holes are provided with swash plate, its Circularhole diameter is less than medium grain diameter；Air filter 10 is for removing to air
Dirt and drying, heater 11 enter 5 bottom of exsiccator for passing through valve after heating to air.It is provided with 5 in exsiccator 5 altogether
Individual gas passage 9, the equal diameters of this 5 gas passages；The length of gas passage 9 increases with the increase of the circular hole swash plate gradient
Plus.Dry material exports 1.25 times that 13 diameters are 6 diameters of wet stock import, can prevent granule from producing blocking in exsiccator 5；5
Hole between individual gas passage 9 and circular hole swash plate 8 is interconnected, it is ensured that the mistake that granule is moved in circular hole swash plate 8
With gas uniform contact in journey.
As shown in Figure 1 and Figure 2, motion schematic diagram and gas in exsiccator 5 of medium grain or coarse granule is in exsiccator 5
The flow schematic diagram of bottom；After air is filtered by air filter 10, heated by heater 11, by valve
Control gas enters the uninterrupted of 5 bottom of exsiccator；When gas enters into the bottom of exsiccator 5, gas is logical by gas
Road 9 is up moved, by being contacted with wet granular 7 after circular hole swash plate 8, dry wet particle 7.Wet granular 7 is from exsiccator right part
Import when initially entering until the whole process for moving to dry material outlet 13 is all being dried, due to using circular hole swash plate 8
Design, so wet stock 7 can rely on the action of gravity of itself and down move, need not increase external force effect.Through dried
Dry material is flowed out from dry material outlet 13, and gas then discharged from gas outlet 4, the gas after discharge pass sequentially through cyclone dust extractor 3,
Recycled after sack cleaner 2 and air exhauster 1.
Claims (3)
1. a kind of with the horizontal type fluidized-bed exsiccator of ramp type, mainly by air exhauster (1), sack cleaner (2), cyclone dust extractor
(3), gas outlet (4), exsiccator (5), wet stock import (6), wet granular (7), circular hole swash plate (8), gas passage (9), air
Filter (10), heater (11), gas feed (12) and dry material outlet (13) composition, it is characterised in that：On exsiccator (5)
Portion is provided with gas outlet (4), and middle part is provided with circular hole swash plate (8) and gas passage (9), and left part is provided with dry material outlet (13), right part
It is provided with wet stock import (6) and gas feed (12)；Gas passage (9) makes gas flow to circular hole swash plate from exsiccator (5) bottom
(8)。
2. according to claim 1 a kind of with the horizontal type fluidized-bed exsiccator of ramp type, it is characterised in that：Circular hole swash plate (8)
With horizontal line into 30 °, and many circular holes are provided with swash plate, its Circularhole diameter is less than medium grain diameter；Air filter
(10) for carrying out dedusting and drying to air, heater (11) is for entering exsiccator by valve after heating to air
(5) bottom.
3. according to claim 1 a kind of with the horizontal type fluidized-bed exsiccator of ramp type, it is characterised in that：In exsiccator (5)
5 gas passages (9), the equal diameters of this 5 gas passages are provided with altogether；The length of gas passage (9) is with circular hole swash plate slope
The increase of degree and increase.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621088475.1U CN206056120U (en) | 2016-09-28 | 2016-09-28 | The horizontal type fluidized-bed exsiccator of one kind band ramp type |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621088475.1U CN206056120U (en) | 2016-09-28 | 2016-09-28 | The horizontal type fluidized-bed exsiccator of one kind band ramp type |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206056120U true CN206056120U (en) | 2017-03-29 |
Family
ID=58367722
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621088475.1U Expired - Fee Related CN206056120U (en) | 2016-09-28 | 2016-09-28 | The horizontal type fluidized-bed exsiccator of one kind band ramp type |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206056120U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106871592A (en) * | 2017-03-30 | 2017-06-20 | 中国建材检验认证集团股份有限公司 | Quick cool dryers and method |
| CN107421240A (en) * | 2017-05-27 | 2017-12-01 | 江苏省翠源食品股份有限公司 | A kind of floated Vegetable drying machine |
-
2016
- 2016-09-28 CN CN201621088475.1U patent/CN206056120U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106871592A (en) * | 2017-03-30 | 2017-06-20 | 中国建材检验认证集团股份有限公司 | Quick cool dryers and method |
| CN107421240A (en) * | 2017-05-27 | 2017-12-01 | 江苏省翠源食品股份有限公司 | A kind of floated Vegetable drying machine |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170329 Termination date: 20170928 |