CN206019160U - A kind of moving fluid bed drying device - Google Patents
A kind of moving fluid bed drying device Download PDFInfo
- Publication number
- CN206019160U CN206019160U CN201620996411.5U CN201620996411U CN206019160U CN 206019160 U CN206019160 U CN 206019160U CN 201620996411 U CN201620996411 U CN 201620996411U CN 206019160 U CN206019160 U CN 206019160U
- Authority
- CN
- China
- Prior art keywords
- hothouse
- vaporium
- raising plant
- steam raising
- fluid bed
- 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
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a kind of moving fluid bed drying device, its structure includes air blast, vaporium, steam raising plant, pressure gauge, spiral feeder, charging aperture, cyclone separator, hothouse, air-introduced machine, water pump, screen collector, plunger displacement pump, valve and discharging opening, the air blast is connected with vaporium, the steam raising plant is provided with pressure gauge), the steam raising plant is connected with pressure gauge, the vaporium is connected with steam raising plant, the vaporium is below hothouse, the vaporium is connected with hothouse, the spiral feeder respectively with hothouse, charging aperture connects, the cyclone separator is connected with spiral feeder by charging aperture, the hothouse includes that target is in bulk and puts, shower nozzle, built-in pipe, locular wall and connector.A kind of moving fluid bed drying device of the present utility model, by shower nozzle jet, realizes hothouse moisture evaporation faster, and liquid sublimation speed is accelerated.
Description
Technical field
The utility model is a kind of moving fluid bed drying device, belongs to food field of chemical equipment.
Background technology
A large amount of solid particles are suspended among the fluid of motion, so that particle has some appearance features of fluid,
Admittedly contact condition is referred to as fluidization of solid, i.e. fluid bed to this stream.
When fluid is gradually increased to certain value by the speed of bed, loosening occurs in particle, and intergranular space increases, bed
There is expansion in volume.If further improving fluid velocity, bed can not maintain stationary state.Now, particle all hangs
Float in fluid, show quite irregular motion.With the raising of flow velocity, the motion of particle is further violent, bed swollen
Swollen also increase therewith, but particle is still remained in bed and is not taken out of by fluid.This state of bed title similar with liquid
For fluid bed.Wherein, the species of fluid bed has:Minimum fluid bed, bubbling fluidized bed, slugging fluidized bed.
Prior art application number：201420843728.6 a kind of moving fluid bed drying device, the utility model is related to
A kind of drying device, more particularly to a kind of moving fluid bed drying device, which includes constant rate of drying fluid bed section and falling-rate periods of drying
Moving bed section, the constant rate of drying fluid bed section and the falling-rate periods of drying moving bed section are provided with least one set heat exchanger, the drop
The dry moving bed section of rapid-curing cutback is located at below the constant rate of drying fluid bed section；The moving fluid bed drying device is provided with least one
The individual gas distributor for adjusting gas flow rate and pressure；Falling-rate periods of drying moving bed pars infrasegmentalis is provided with logical saturation or superheated steam
Or the pipeline of nitrogen or wet stock hygroscopic water gas or inert gas；Moving fluid bed drying device of the present utility model is divided into constant speed
Drying fluidized-bed section and falling-rate periods of drying moving bed section, wet stock are dry in the efficient rapid moisture removal of constant rate of drying fluid bed section and in reduction of speed
Dry mobile section low energy consumption depth dehumidification, it is achieved that the optimization of dry run energy ezpenditure coupling.But this fluidized bed drying
Speed is very slow, and inefficiency, liquid sublimation are slow.
Utility model content
In view of the shortcomings of the prior art, the utility model purpose is to provide a kind of moving fluid bed drying device,
Its structure includes air blast, vaporium, steam raising plant, pressure gauge, spiral feeder, charging aperture, cyclone separator, dry
Dry room, air-introduced machine, water pump, screen collector, plunger displacement pump, valve and discharging opening, the air blast are connected with vaporium, the steaming
Vapour generating means is provided with pressure gauge), the steam raising plant is connected with pressure gauge, the vaporium and steam raising plant
Connection, below the hothouse, the vaporium is connected the vaporium with hothouse, the spiral feeder respectively with do
Dry room, charging aperture connection, the cyclone separator are connected with spiral feeder by charging aperture, and the cyclone separator passes through
Pipeline is connected with hothouse, air-introduced machine respectively, and the air-introduced machine is connected with screen collector, and the water pump, screen collector connect
Connect, the plunger displacement pump is connected with hothouse, screen collector respectively by valve, the discharging opening is on hothouse, described
Discharging opening is connected with hothouse, the hothouse include target in bulk put, shower nozzle, built-in pipe, locular wall and connector, the locular wall
Inside be provided with target in bulk put, shower nozzle, built-in pipe, be provided with the locular wall target in bulk put, built-in pipe connection, the shower nozzle with interior
Pipeline connection is put, the locular wall is provided with four connectors.
Further, the vaporium is provided with valve with the junction of steam raising plant.
A kind of moving fluid bed drying device of the present utility model, by shower nozzle jet, realizes hothouse moisture evaporation
Faster, liquid sublimation speed is accelerated.
Description of the drawings
By reading the detailed description that non-limiting example is made with reference to the following drawings, other spies of the present utility model
Levy, objects and advantages will become more apparent upon：
Fig. 1 is a kind of overall structure diagram of moving fluid bed drying device of the utility model；
Structural representations of the Fig. 2 for the utility model hothouse；
Structural representations of the Fig. 3 for the utility model valve；
In figure：Air blast -1, vaporium -2, steam raising plant -3, pressure gauge -4, spiral feeder -5, charging aperture -
6th, cyclone separator -7, hothouse -8, air-introduced machine -9, water pump -10, screen collector -11, plunger displacement pump -12, valve -13, discharging
Mouthfuls -14, target is in bulk puts -80, shower nozzle -81, built-in pipe -82, locular wall -83 and connector -84.
Specific embodiment
Technological means, creation characteristic, reached purpose and effect for realizing the utility model is easy to understand, below
In conjunction with specific embodiment, the utility model is expanded on further.
Refer to Fig. 1-3, the utility model provides a kind of moving fluid bed drying device, its structure include air blast 1,
Vaporium 2, steam raising plant 3, pressure gauge 4, spiral feeder 5, charging aperture 6, cyclone separator 7, hothouse 8, air inducing
Machine 9, water pump 10, screen collector 11, plunger displacement pump 12, valve 13 and discharging opening 14, the air blast 1 are connected with vaporium 2, institute
State steam raising plant 3 and be provided with pressure gauge 4, the steam raising plant 3 is connected with pressure gauge 4, the vaporium 2 and steam
Generating means 3 connects, and below hothouse 8, the vaporium 2 is connected the vaporium 2 with hothouse 8, and the spiral send
Material device 5 is connected with hothouse 8, charging aperture 6 respectively, and the cyclone separator 7 is connected with spiral feeder 5 by charging aperture 6
Connect, the cyclone separator 7 is connected with hothouse 8, air-introduced machine 9 respectively by pipeline, the air-introduced machine 9 and screen collector 11
Connection, the water pump 10, screen collector 11 connect, the plunger displacement pump 12 by valve 13 respectively with hothouse 8, water curtain dedusting
Device 11 connects, and on hothouse 8, the discharging opening 14 is connected the discharging opening 14 with hothouse 8, and the hothouse 8 includes
Target is in bulk to put 80, shower nozzle 81, built-in pipe 82, locular wall 83 and connector 84, is provided with that target is in bulk to put 80, shower nozzle in the locular wall 83
81st, it is provided with target 80, built-in pipe 82 of putting in bulk in built-in pipe 82, the locular wall 83 to connect, the shower nozzle 81 and built-in pipe
82 connections, the locular wall 83 are provided with four connectors 84.The vaporium 2 is provided with valve with the junction of steam raising plant 3
13.
When being used, material sends into hothouse by spiral feeder 5, is dried, and last solid passes through
Material mouth 14 is discharged.
General principle of the present utility model and principal character and advantage of the present utility model is had been shown and described above, for
For those skilled in the art, it is clear that the utility model is not limited to the details of above-mentioned one exemplary embodiment, and without departing substantially from this
In the case of the spirit or essential attributes of utility model, the utility model can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, scope of the present utility model is by institute
Attached claim rather than described above restriction, it is intended that will fall in the implication and scope of the equivalency of claim
All changes are included in the utility model.Any reference in claim should not be considered as and limit involved right
Require.
Moreover, it will be appreciated that although this specification is been described by according to embodiment, not each embodiment is only wrapped
Contain an independent technical scheme, this narrating mode of specification is only that those skilled in the art should for clarity
Using specification as an entirety, the technical scheme in each embodiment can also form those skilled in the art through appropriately combined
Understandable other embodiment.
Claims (2)
1. a kind of moving fluid bed drying device, it is characterised in that：Its structure includes air blast (1), vaporium (2), steam
Generating means (3), pressure gauge (4), spiral feeder (5), charging aperture (6), cyclone separator (7), hothouse (8), air inducing
Machine (9), water pump (10), screen collector (11), plunger displacement pump (12), valve (13) and discharging opening (14), air blast (1) with
Vaporium (2) connects, and steam raising plant (3) are provided with pressure gauge (4), steam raising plant (3) and pressure gauge
(4) connect, vaporium (2) are connected with steam raising plant (3), described vaporium (2) are located at below hothouse (8), institute
State vaporium (2) to be connected with hothouse (8), spiral feeder (5) are connected with hothouse (8), charging aperture (6) respectively,
Described cyclone separator (7) are connected with spiral feeder (5) by charging aperture (6), and described cyclone separator (7) pass through pipeline
It is connected with hothouse (8), air-introduced machine (9) respectively, air-introduced machine (9) are connected with screen collector (11), water pump (10),
Screen collector (11) connects, and described plunger displacement pump (12) are connected with hothouse (8), screen collector (11) respectively by valve (13)
Connect, described discharging opening (14), on hothouse (8), discharging opening (14) are connected with hothouse (8), hothouse (8)
Set including in bulk the putting in (80), shower nozzle (81), built-in pipe (82), locular wall (83) and connector (84), locular wall (83) of target
Have that target is in bulk to put (80), shower nozzle (81), built-in pipe (82), in locular wall (83), be provided with that target is in bulk to put (80), built-in pipe
(82) connect, shower nozzle (81) are connected with built-in pipe (82), and locular wall (83) are provided with four connectors (84).
2. a kind of moving fluid bed drying device according to claim 1, it is characterised in that：Vaporium (2) with
The junction of steam raising plant (3) is provided with valve (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620996411.5U CN206019160U (en) | 2016-08-30 | 2016-08-30 | A kind of moving fluid bed drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620996411.5U CN206019160U (en) | 2016-08-30 | 2016-08-30 | A kind of moving fluid bed drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206019160U true CN206019160U (en) | 2017-03-15 |
Family
ID=58254970
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620996411.5U Expired - Fee Related CN206019160U (en) | 2016-08-30 | 2016-08-30 | A kind of moving fluid bed drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206019160U (en) |
-
2016
- 2016-08-30 CN CN201620996411.5U patent/CN206019160U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206019160U (en) | A kind of moving fluid bed drying device | |
| CN102425928A (en) | Double pulse air flow drying machine | |
| CN204648882U (en) | A kind of pulse type pneumatic drier | |
| CN207838339U (en) | The multi-functional centrifugal spray drying tower of multisection type | |
| CN104764296B (en) | A kind of drying equipment and drying means | |
| CN206823206U (en) | Chinese medical concrete drying machine with centrifugal spray | |
| CN207335285U (en) | Fluidized bed type brown coal drying device | |
| CN204359107U (en) | Novel pulse type airflow drying tube | |
| CN204141937U (en) | Fluidized bed drying equipment | |
| Singh et al. | Study of agricultural product drying in a rotating fluidized bed with static geometry | |
| CN205760332U (en) | A kind of environmental protection is with automatically controlling water spray dust elimination device | |
| CN203810396U (en) | Coal distribution device for circulating fluidized bed boiler | |
| CN203771904U (en) | Drying equipment | |
| CN204944128U (en) | A kind of two-stage combined type pneumatic conveying dryer | |
| CN203744240U (en) | Material supplementing type soot blower of circulating fluidized bed boiler | |
| CN207237315U (en) | Atomizing liquid drying machine | |
| CN207815302U (en) | A kind of cycles, economized fluidized-bed combustion boiler | |
| CN105746748A (en) | Tea dryer | |
| CN105478246A (en) | Cyclone separating device used in detergent manufacturing process | |
| CN104180633B (en) | Electrical heating Helmholtz Pulsating Flow tea-drying device | |
| CN204128323U (en) | Electrical heating Helmholtz Pulsating Flow tea-drying device | |
| CN106052357B (en) | Lateral vertical granule drying machine | |
| CN105222526B (en) | A kind of multilayer bubbling fluidization gumming vertical drying device | |
| CN105036510B (en) | For the jet drying stove of Treatment of Sludge | |
| CN204672253U (en) | Spirt wind control structure at the bottom of a kind of fluid bed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20170315 Termination date: 20170830 |