CN204923691U - Granule raw -food material drying device - Google Patents
Granule raw -food material drying device Download PDFInfo
- Publication number
- CN204923691U CN204923691U CN201520557774.4U CN201520557774U CN204923691U CN 204923691 U CN204923691 U CN 204923691U CN 201520557774 U CN201520557774 U CN 201520557774U CN 204923691 U CN204923691 U CN 204923691U
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- China
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- food material
- slanted screen
- fluid bed
- drying device
- screen plate
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Abstract
The patent discloses a granule raw -food material drying device, including drying chamber, horizontal fluidized bed in the middle part of the drying chamber, fluidized bed one end sets up the feed inlet, and the other end is provided with the discharge gate, the lower surface of fluidized bed is provided with the vibrator, the fluidized bed middle part is provided with the slanted screen board, the slanted screen board is divided into first fluidization section and second fluidization section with the fluidized bed, first fluidization section below is provided with first air intake, is provided with the second air intake below the second fluidization section, the top of first fluidization section still is provided with the backward flow swash plate, the backward flow swash plate is in the feed inlet of slanted screen board, the top of backward flow swash plate is less than the top of slanted screen board, and the beneficial effect of this patent lies in: it is dry to fall into two duangan with the granule raw -food material, earlier through evaporating the material surface moisture no longer than 100 DEG C hot -blast, can prevent effectively that the material from destroying in first section.
Description
Technical field
The utility model relates to the drying equipment of food processing, particularly a kind of particulate food material drying device.
Background technology
In food processing, use beans comparatively common as raw-food material, the such as common food such as mung bean, red bean raw material, in order to ensure the healthy and safe of food, needs to clean material before processing, dries for the particulate food material after cleaning.Extensively adopt big-and-middle-sized tower dryer tool equipment at present.In tower dryer tool, the granule materials such as moistening beans are poured in dry channel, hot blast is blasted in dry channel, usually the dry channel of inside is made inclination, be convenient to beans like this and drop out hothouse according to gravity oneself, in order to the moisture in moistening beans granule materials being down to safety value during storage, need to blast the higher hot blast of temperature, the temperature of general hot blast is between 120 DEG C-160 DEG C, 12-16% can be reached like this by disposable for water content, because baking temperature is generally higher than after 100 DEG C, easily cause the explosion of granule materials, broken, be inverted material color and luster not nature, the problem that quality declines.
Utility model content
The utility model is intended to provide a kind of particulate food material drying device, to solve the problem that the higher hot blast of present tower baker serviceability temperature easily causes raw-food material to destroy.
Particulate food material drying device in this programme, comprise hothouse, be horizontally placed on the fluid bed in the middle part of hothouse, described fluid bed one end arranges charging aperture, the other end is provided with discharging opening, the lower surface of described fluid bed is provided with vibrator, slanted screen plate is provided with in the middle part of described fluid bed, fluid bed is divided into first class section and the second fluidisation section by described slanted screen plate, the first air inlet is provided with below described first class section, the second air inlet is provided with below second fluidisation section, the top of described first class section is also provided with backflow swash plate, described backflow swash plate is in the charging aperture of slanted screen plate, the top of described backflow swash plate is lower than the top of slanted screen plate, return flow line is formed between backflow swash plate and slanted screen plate, the width of return flow line is 3 ~ 5cm, the top of described hothouse is provided with waste gas outlet.
The drying principles of this programme is: put into by particulate food material in hothouse, Vibration on Start-up device makes material can move to discharging opening from charging aperture gradually, first particulate food material is in the first class section on fluid bed, first class section is by the first air inlet heat supply, the hot blast of 80 DEG C is passed into the first air inlet, evaporated by the water of this hot blast by particulate food material surface, after the water evaporation on material surface, because adhesive force reduces, the second fluidisation section can be entered by slanted screen plate, the hot blast passing into 100 ~ 120 DEG C to the second air inlet carries out internal moisture drying, because the granule materials epidermis entering the second fluidisation section can not exist Free water, the raising of temperature can not cause the destruction of particulate food material.Particulate food material surface also being remained to water can be moved upward by slanted screen plate, is then back to first class section by the swash plate that confluxes and continues dry.
The advantage of this programme is: particulate food material is divided into Two stage dryer, first removes surperficial Free water, can prevent high-temperature material gelatinization, avoids the situation that particulate food material damages; 2, form material return flow line by the cooperation of slanted screen plate and backflow swash plate, make surface only have the undried particulate food material of water to be back to first class section and carry out continuation drying, ensure that the completeness of dry materials.
Further, the upper surface of described fluid bed, slanted screen plate is provided with unhurried current tooth; By unhurried current tooth, granule materials is produced unhurried current, make material can stop the more time in drier, realize fully dry.
Further, described charging aperture is provided with feed hopper, and described feed hopper is connected with charging aperture by corrugated flexible hose, and the below of feed hopper is provided with filtration sieve plate.First carry out prefiltration to particulate food material surface water by filtering sieve plate, owing to being provided with vibrator in hothouse, when drying, vibration can produce coupling part and destroy, and can be cushioned by bellows to vibration, prevents coupling part from occurring damaging.
Further, described first air inlet is connected with the first heat exchanger, and the second air inlet is connected with the second heat exchanger, and the first heat exchanger and the second heat exchanger are connected on air blast by collecting pipe.When carrying out drying, 80 DEG C are set to the temperature upper limit of the first heat exchanger, ensure that the stream temperature of first class section is relatively low, only the moisture on material surface is evaporated, raw-food material can not be too high by the gelatinization of material epidermis because of steam temperature, is set to 120 DEG C to the temperature upper limit of the second heat exchanger; Because material surface moisture now is evaporated, add the temperature of air flow, material epidermis can not be affected.
Finally, the charging aperture of described hothouse is provided with scavenging conduit, and described scavenging conduit, collecting pipe are connected by reversal valve with air blast.After drying completes, the air after being will speed up by reversal valve enters to be switched in scavenging conduit, is cleared up by the material remained in hothouse by scavenging conduit, ensures the drying work of material next time.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model particulate food material drying device.
Detailed description of the invention
Below by detailed description of the invention, the utility model is described in further detail:
Reference numeral in Figure of description comprises: hothouse 1, feed hopper 2, filtration sieve plate 21, reversal valve 3, air blast 4, first heat exchanger 5, second heat exchanger 6, vibrator 7, fluid bed 8, discharging opening 9, cyclone separator 10, backflow swash plate 11, slanted screen plate 12.
Particulate food material drying device as shown in Figure 1, comprise hothouse 1, be horizontally placed on fluid bed 8 in the middle part of hothouse 1, fluid bed 8 one end arranges charging aperture, the other end is provided with discharging opening 9, described charging aperture is provided with feed hopper 2, feed hopper 2 is connected with charging aperture by corrugated flexible hose, and the below of feed hopper 2 is provided with filters sieve plate 21.First the filter of particulate food material surface water is walked by filtering sieve plate 21.
The lower surface of fluid bed 8 is provided with vibrator 7, slanted screen plate 12 is provided with in the middle part of fluid bed 8, fluid bed 8 is divided into first class section and the second fluidisation section by slanted screen plate 12, the first air inlet is provided with below first class section, the second air inlet is provided with below second fluidisation section, the top of first class section is also provided with backflow swash plate 11, backflow swash plate 11 is in the charging aperture of slanted screen plate 12, the top of backflow swash plate 11 is lower than the top of slanted screen plate 12, form return flow line between backflow swash plate 11 and slanted screen plate 12, the width of return flow line is 3cm.The top of hothouse 1 is provided with waste gas outlet, and waste gas outlet is connected on cyclone separator 10, effectively dust also residual in mung bean raw material can be carried out separation cleaning.
In dry run, the present embodiment carries out drying to mung bean, first the wet mung bean of cleaning is put in hothouse, Vibration on Start-up device makes material can move to discharging opening from charging aperture gradually, first mung bean will be in the first class section on fluid bed, first class section is by the first air inlet heat supply, the hot blast of 80 DEG C is passed into the first air inlet, evaporated by the water of this hot blast by mung bean surface, after the water evaporation on mung bean surface, because adhesive force reduces, mung bean can enter the second fluidisation section by slanted screen plate, the hot blast passing into 100 ~ 120 DEG C to the second air inlet carries out internal moisture drying.The upper surface of fluid bed, slanted screen plate is provided with unhurried current tooth; By unhurried current tooth, granule materials is produced unhurried current, make material can stop the more time in drier, realize fully dry.Can not there is Free water in the mung bean epidermis entering the second fluidisation section, the raising of temperature can not cause the destruction of mung bean epidermis.Mung bean surface also being remained to water can be moved upward by slanted screen plate, is then back to first class section by the swash plate that confluxes and carries out continuation drying.
When drying, vibration can produce coupling part and destroy, and can be cushioned by bellows to vibration, prevents coupling part from occurring damaging.First air inlet is connected with the first heat exchanger 5, second air inlet is connected with the second heat exchanger 6, first heat exchanger 5 and the second heat exchanger 6 are connected on air blast 4 by collecting pipe, 80 DEG C are set to the temperature upper limit of the first heat exchanger 5, ensure that the stream temperature of first class section is relatively low, only evaporated by the moisture on material surface, raw-food material can not be too high by the gelatinization of material epidermis because of steam temperature, is set to 120 DEG C to the temperature upper limit of the second heat exchanger 6; Because material surface moisture now is evaporated, add the temperature of air flow, material epidermis can not be affected.
The charging aperture of hothouse 1 is provided with scavenging conduit, and scavenging conduit, collecting pipe are connected by reversal valve 3 with air blast.After drying completes, enter to be switched in scavenging conduit by the air after reversal valve 3 will speed up, by scavenging conduit, the material remained in hothouse 1 is cleared up, ensure the drying work of material next time.
Above-described is only embodiment of the present utility model, and in scheme, the general knowledge such as known concrete structure and characteristic does not do too much description at this.Should be understood that; for a person skilled in the art, under the prerequisite not departing from the utility model structure, some distortion and improvement can also be made; these also should be considered as protection domain of the present utility model, and these all can not affect effect and the practical applicability of the utility model enforcement.The protection domain that this application claims should be as the criterion with the content of its claim, and the detailed description of the invention in description etc. record the content that may be used for explaining claim.
Claims (5)
1. particulate food material drying device, comprise hothouse, be horizontally placed on the fluid bed in the middle part of hothouse, described fluid bed one end arranges charging aperture, the other end is provided with discharging opening, the lower surface of described fluid bed is provided with vibrator, it is characterized in that: in the middle part of described fluid bed, be provided with slanted screen plate, fluid bed is divided into first class section and the second fluidisation section by described slanted screen plate, the first air inlet is provided with below described first class section, the second air inlet is provided with below second fluidisation section, the top of described first class section is also provided with backflow swash plate, described backflow swash plate is in the charging aperture of slanted screen plate, the top of described backflow swash plate is lower than the top of slanted screen plate, return flow line is formed between backflow swash plate and slanted screen plate, the width of return flow line is 3 ~ 5cm, the top of described hothouse is provided with waste gas outlet.
2. particulate food material drying device according to claim 1, is characterized in that: the upper surface of described fluid bed, slanted screen plate is provided with unhurried current tooth.
3. particulate food material drying device according to claim 2, it is characterized in that: described charging aperture is provided with feed hopper, described feed hopper is connected with charging aperture by corrugated flexible hose, and the below of feed hopper is provided with filtration sieve plate.
4. particulate food material drying device according to claim 3, it is characterized in that: described first air inlet is connected with the first heat exchanger, second air inlet is connected with the second heat exchanger, and the first heat exchanger and the second heat exchanger are connected on air blast by collecting pipe.
5. particulate food material drying device according to claim 4, it is characterized in that: the charging aperture of described hothouse is provided with scavenging conduit, described scavenging conduit, collecting pipe are connected by reversal valve with air blast.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520557774.4U CN204923691U (en) | 2015-07-29 | 2015-07-29 | Granule raw -food material drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520557774.4U CN204923691U (en) | 2015-07-29 | 2015-07-29 | Granule raw -food material drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204923691U true CN204923691U (en) | 2015-12-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520557774.4U Expired - Fee Related CN204923691U (en) | 2015-07-29 | 2015-07-29 | Granule raw -food material drying device |
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| Country | Link |
|---|---|
| CN (1) | CN204923691U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108195139A (en) * | 2017-12-29 | 2018-06-22 | 寿县弘祥家纺有限公司 | A kind of natural feather fluidization drying device |
-
2015
- 2015-07-29 CN CN201520557774.4U patent/CN204923691U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108195139A (en) * | 2017-12-29 | 2018-06-22 | 寿县弘祥家纺有限公司 | A kind of natural feather fluidization drying device |
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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 |
Granted publication date: 20151230 Termination date: 20160729 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |