CN206430528U - A kind of calcium propionate drying device - Google Patents
A kind of calcium propionate drying device Download PDFInfo
- Publication number
- CN206430528U CN206430528U CN201720084547.3U CN201720084547U CN206430528U CN 206430528 U CN206430528 U CN 206430528U CN 201720084547 U CN201720084547 U CN 201720084547U CN 206430528 U CN206430528 U CN 206430528U
- Authority
- CN
- China
- Prior art keywords
- big
- basin
- small
- calcium propionate
- rotating shaft
- 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.)
- Active
Links
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The utility model discloses a kind of calcium propionate drying device, including feed arrangement, dehydrating unit, housing, hot air circulating system, small rake arms, small basin, big rake arms, big basin, central rotating shaft, rotating shaft drive device, feed opening and hot water cyclesystem, described feed arrangement is arranged on the top of housing, described small basin is disposed alternately on central rotating shaft with big basin, described rotating shaft drive device is arranged on housing bottom, the feed opening is arranged on housing bottom, described dehydrating unit is the vavuum pump for being arranged on case top, described hot water cyclesystem is arranged on enclosure interior.Compared with prior art, a kind of calcium propionate drying device of the present utility model, by way of hot blast or steam interior circulation, simultaneously heating is aided in using circulating hot water, and extracted out internal moisture using vavuum pump, the drying to calcium propionate is realized, steam consumption is reduced, the dustiness in moisture is reduced, the thermal efficiency is high.
Description
Technical field
The utility model is related to Chemical Industry Drying apparatus field, is specifically exactly a kind of calcium propionate production drying device.
Background technology
Calcium propionate is a kind of new food developed in recent years and feed anticorrosion agent, the acid mould inhibitor of category, to mould
Bacterium, aerobic bacillus and Gram-negative bacteria all have good killing action, can suppress the generation of aflatoxins, to people
Body is nontoxic, is widely used in terms of the mould proof and fresh-keeping of vegetables of the food such as bread, cake, plant protection.Calcium propionate is white
Lightweight flake-like crystal particle or powder, odorless, tasteless or slightly peculiar smell are soluble in water, be slightly soluble in ethanol and methanol, hardly
Acetone and benzene are dissolved in, the easy deliquescence in humid air is heated to losing the crystallization water at 120 DEG C.The drying of country's calcium propionate at present
Pneumatic conveying drying being used method, the moisture content before calcium propionate drying is used substantial amounts of in the drying process 20% or so more
Steam, but the thermal efficiency is low, thermal loss is big, and dust concentration is high in drier, easily causes airborne dust.Simultaneously as in steam originally
Body moisture is big, contains substantial amounts of dust along with the air-flow of moisture outlet, it is necessary to follow-up cleaner is handled,
The loss of material is caused, and substantial amounts of use steam also result in waste.
The content of the invention
The purpose of this utility model is to provide a kind of calcium propionate drying device, the side that the device passes through steam interior circulation
Formula, while aiding in heating using the circulating hot water in factory, reduces steam consumption, and take out internal moisture using vavuum pump
Go out, there is provided a kind of high calcium propionate drying device of uniform, thermal efficiency for drying of the realization to calcium propionate.
The technical scheme in the invention for solving the technical problem is：
A kind of calcium propionate drying device, including it is feed arrangement, dehydrating unit, housing, hot air circulating system, small rake arms, small
Basin, big rake arms, big basin, central rotating shaft, rotating shaft drive device, feed opening and hot water cyclesystem, described charging
Device is arranged on the top of housing, and described small basin is disposed alternately on central rotating shaft with big basin, and described is small dry
The top of dry disk, which is provided with small rake arms, described small rake arms, is provided with small plectrum, and the top of described big basin is provided with
Big plectrum is provided with big rake arms, described big rake arms, described rotating shaft drive device is arranged on housing bottom, and the center turns
One end of axle is fixed with rotating shaft drive device, and the feed opening is arranged on housing bottom, and described dehydrating unit is to be arranged on shell
Vavuum pump at the top of body, described hot air circulating system includes air inlet main pipe, winding pipe, air-out branch pipe and air-out supervisor, institute
The one end of the winding pipe stated respectively with large and small basin is connected, and described air-out branch pipe is another with large and small basin respectively
End connection, with winding pipe formation hot air circulation, described hot water cyclesystem is arranged on enclosure interior, for shift to an earlier date waste heat and
Keep the temperature in housing, it is possible to reduce the consumption of hot blast or steam, reduce energy consumption.
As optimization, the circumferencial direction of described small plectrum along small basin is inclined in small rake arms, for by third
Sour calcium is delivered to the outward flange of small basin and fallen on the big basin of lower section.
As optimization, the direction of described big plectrum along the big basin center of circle is inclined in big rake arms, for by third
Sour calcium is delivered to the centre bore of big basin and falls into the small basin of lower section.
As optimization, described housing bottom basin is big basin, and the big plectrum of the bottom basin is done along big
The direction of dry disk circumference is inclined in big rake arms, and calcium propionate is delivered in feed opening.
As optimization, air-quantity adjusting valve is provided with described blast pipe, can be according to the waste heat of hot water circuit pipeline
The usage amount of situation, adjustment hot blast or steam.
As optimization, in described each winding pipe on be provided with air-quantity adjusting valve, in section of tubing or basin
When failure or problem, other air quantity parameters can be adjusted with closing fault part valve, it is ensured that the lasting progress of production.
As optimization, described hot water cyclesystem is arranged in internal interlayer in tubulation form.
The beneficial effects of the utility model are：Compared with prior art, a kind of calcium propionate drying device of the present utility model,
Without blowing hot blast in hothouse, by way of hot blast or steam interior circulation, while aid in heating using circulating hot water,
And utilize vavuum pump to extract internal moisture out, the drying to calcium propionate is realized, steam consumption is reduced, the aqueous of finished product is reduced
Amount, reduces the dustiness in moisture, and the thermal efficiency is high.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Wherein, 1 feed arrangement, 2 dehydrating units, 3 housings, 4 discharge pipes, 41 air-out branch pipes, 5 air inlet main pipes, 51 air intake branch
Pipe, 6 central rotating shafts, 7 big basins, 8 small basins, 9 rotating shaft drive devices, 10 feed openings, 11 big rake arms, 111 big plectrums, 12
Small rake arms, 121 small plectrums, 13 bottom basins, 14 hot water cyclesystems.
Embodiment
It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer
Accompanying drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that retouched
The embodiment stated is a part of embodiment of the utility model, rather than whole embodiments.Generally here described in accompanying drawing and
The component of the utility model embodiment shown can be arranged and designed with a variety of configurations.Therefore, below to attached
The detailed description of the embodiment of the present utility model provided in figure is not intended to limit claimed scope of the present utility model,
But it is merely representative of selected embodiment of the present utility model.Based on the embodiment in the utility model, ordinary skill people
The every other embodiment that member is obtained under the premise of creative work is not made, belongs to the model of the utility model protection
Enclose.
A kind of calcium propionate drying device, including feed arrangement 1, dehydrating unit 2, housing 3, hot air circulating system, small rake arms
12nd, small basin 8, big rake arms 11, big basin 7, central rotating shaft 6, rotating shaft drive device 9, feed opening 10 and hot water circuit system
System 14, described feed arrangement 1 is arranged on the top of housing 3, during described small basin 8 is disposed alternately at big basin 7
In heart rotating shaft 6, the top of described small basin 8, which is provided with small rake arms 12, described small rake arms 12, is provided with small plectrum
121, the top of described big basin 7, which is provided with big rake arms 11, described big rake arms 11, is provided with big plectrum 111, described
Rotating shaft drive device 9 be arranged on the bottom of housing 3, one end and the rotating shaft drive device 9 of the central rotating shaft 6 are fixed, it is described under
Material mouth 10 is arranged on housing bottom, and described dehydrating unit 2 is the vavuum pump for being arranged on case top, described hot air circulation system
System includes air inlet main pipe 5, winding pipe 51, air-out branch pipe 41 and air-out supervisor 4, and described winding pipe 51 is dried with big respectively
One end connection of disk 7, small basin 8, described air-out branch pipe 41 connects with the other end of big basin 7, small basin 8 respectively
Connect, with the formation hot air circulation of winding pipe 51, described hot water cyclesystem 14 is arranged on enclosure interior, for shift to an earlier date waste heat and
Keep housing inner question.
In embodiment, the circumferencial direction of described small plectrum 121 along small basin 8 is inclined in small rake arms 12,
For calcium propionate is delivered to the outward flange of small basin 8 and fall into lower section big basin 7.The described edge of big plectrum 111
The direction in the big center of circle of basin 7 is inclined in big rake arms 11, for calcium propionate to be delivered to the centre bore of big basin 7 simultaneously
Fall into the small basin 8 of lower section.Described housing bottom basin 13 is big basin, the plectrum edge of the bottom basin 13
The direction of big basin circumference is inclined in big rake arms, and calcium propionate is delivered in feed opening 10.In described blast pipe
Air-quantity adjusting valve is provided with road, for adjusting valve size according to temperature conditions.
In the present embodiment, calcium propionate feed arrangement is continuously added on the first layer basin of calcium propionate drier top,
Small rake arms with small plectrum makes rake arms make rake leaf continuously turn over as gyration to copy material as gyration, and calcium propionate is along index
Helix flows through dry panel surface, and the material on small basin is shifted into outer rim, and falls on the big drying of lower section in outer rim
Disk outer rim, calcium propionate is moved and fallen from middle blanking port as in the small basin of next layer inwards on big basin.Size is dried
Disk is arranged alternatively up and down, and calcium propionate is able to continuously flow through whole drier.The heat of saturation is passed through in hollow size basin
Wind or steam, hot blast are entered by blast pipe by winding pipe one end of basin, from the output of the air-out branch pipe other end.Formed
Hot air circulation.Dry calcium propionate material falls on the bottom of housing from last layer of basin, is finally transplanted on discharging opening by plectrum
Discharge.Wet part is overflowed from calcium propionate, is discharged by the vacuum pump port being located on top cover.The dry calcium propionate material discharged from bottom can
Directly pack.In order to which using other thermals source in plant area, hot water cyclesystem is preferably designed with housing, using useless
The temperature of water carries out continuing heating, temperature keeping in advance to housing, can save the consumption of the heat energy such as other hot blasts.
Calcium propionate drying device of the present utility model is dried in conduction heat transfer mode, is dried in calcium propionate drying process
Very small amount is only passed through in device（Or be not passed through）Air, seldom, the thermal efficiency is high for its tail gas carrying amount, and calcium propionate is heated evenly, heat energy
Loss is low, and product quality is stable, it is to avoid because waste gas contacts the change that may occur with calcium propionate.
General principle of the present utility model and principal character and advantage of the present utility model has been shown and described above.One's own profession
The technology people of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply illustrate principle of the present utility model, on the premise of the utility model spirit and scope are not departed from, the utility model can also
There are various changes and modifications, these changes and improvements are both fallen within the range of claimed the utility model.The utility model will
Protection domain is sought by appended claims and its equivalent thereof.
Claims (6)
1. a kind of calcium propionate drying device, including it is feed arrangement, dehydrating unit, housing, hot air circulating system, small rake arms, small dry
Dry disk, big rake arms, big basin, central rotating shaft, rotating shaft drive device, feed opening and hot water cyclesystem, described charging dress
The top for being arranged on housing is put, described small basin is disposed alternately on central rotating shaft with big basin, described small drying
The top of disk, which is provided with small rake arms, described small rake arms, is provided with small plectrum, and the top of described big basin is provided with greatly
Big plectrum is provided with rake arms, described big rake arms, described rotating shaft drive device is arranged on housing bottom, the central rotating shaft
One end fixed with rotating shaft drive device, the feed opening is arranged on housing bottom, it is characterised in that：Described dehydrating unit is
The vavuum pump of case top is arranged on, described hot air circulating system includes air inlet main pipe, winding pipe, air-out branch pipe and air-out
Supervisor, the one end of described winding pipe respectively with large and small basin is connected, described air-out branch pipe respectively with large and small drying
The other end connection of disk, with winding pipe formation hot air circulation, described air inlet main pipe is provided with air-quantity adjusting valve, described
Hot water cyclesystem is arranged on enclosure interior.
2. a kind of calcium propionate drying device according to claim 1, it is characterised in that：Described small plectrum is along small basin
Circumferencial direction be inclined in small rake arms.
3. a kind of calcium propionate drying device according to claim 1, it is characterised in that：Described big plectrum is along big basin
The direction in the center of circle is inclined in big rake arms.
4. a kind of calcium propionate drying device according to claim 1, it is characterised in that：Described housing bottom basin is
Big basin, the direction of the big plectrum of the bottom basin along big basin circumference is inclined in big rake arms.
5. a kind of calcium propionate drying device according to claim 1, it is characterised in that：Set in described each winding pipe
There is air-quantity adjusting valve.
6. a kind of calcium propionate drying device according to claim 1, it is characterised in that：Described hot water cyclesystem is to arrange
Form of tubes is arranged in enclosure interior interlayer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720084547.3U CN206430528U (en) | 2017-01-23 | 2017-01-23 | A kind of calcium propionate drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720084547.3U CN206430528U (en) | 2017-01-23 | 2017-01-23 | A kind of calcium propionate drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206430528U true CN206430528U (en) | 2017-08-22 |
Family
ID=59591376
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720084547.3U Active CN206430528U (en) | 2017-01-23 | 2017-01-23 | A kind of calcium propionate drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206430528U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107782120A (en) * | 2017-12-05 | 2018-03-09 | 江西太升实业有限公司 | A kind of layered continuous powder ore drying furnace |
-
2017
- 2017-01-23 CN CN201720084547.3U patent/CN206430528U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107782120A (en) * | 2017-12-05 | 2018-03-09 | 江西太升实业有限公司 | A kind of layered continuous powder ore drying furnace |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105466157B (en) | Used heat is used for the vacuum tube bank drying system of multiple-effect evaporation and pneumatic conveying drying | |
| JP3181483U (en) | Equipment for drying sludge with air | |
| CN209445754U (en) | A kind of cloth drying device of uniform drying sterilization | |
| CN105466174B (en) | Vacuum pipe bundle drier | |
| CN208667148U (en) | A kind of high-salt wastewater crystalline mother solution drying device | |
| CN206430528U (en) | A kind of calcium propionate drying device | |
| CN105660903A (en) | Tea leaf drying machine and tea leaf drying method | |
| CN109945611A (en) | A kind of tray drying device of moisture reuse and combined heated | |
| CN106430898A (en) | Sludge drying system and method | |
| CN105466171B (en) | Used heat is used for the vacuum tube bank drying system of pneumatic conveying drying | |
| CN206927781U (en) | A kind of differential sludge drier | |
| CN207515382U (en) | One boar food production drying device | |
| CN206847324U (en) | A kind of dryer | |
| CN207512062U (en) | A kind of vacuum and low temperature anhydration system for variform material | |
| CN207659295U (en) | Double helix channel-type heat exchanger tube and sludge heating drop stick device | |
| CN207035736U (en) | A kind of high efficiency composition molysite drying unit | |
| CN212673650U (en) | Phenylacetic acid drying waste gas treatment device | |
| CN211177763U (en) | Abelmoschus manihot flower drying equipment | |
| CN213841526U (en) | Spray drying device for heat spray cleaning tablet | |
| CN209359242U (en) | A kind of recyclegas purification device of sheep sheep hurdle | |
| CN208998501U (en) | A kind of spiral hollow shaft and the material drying machine including the hollow shaft | |
| CN209147630U (en) | Cork dries deodorizing device | |
| CN106705297A (en) | Gas-gas heat exchange type energy-saving air-dehumidification fresh water maker | |
| CN207778965U (en) | Full-automatic wheat grain dewaterer | |
| CN112146357A (en) | Spray drying device and method for Relinqing tablets |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: 277200 No.1, Yinshan Industrial Park, economic development zone, Shanting District, Zaozhuang City, Shandong Province Patentee after: Shandong tongtaiweirun Food Technology Co., Ltd Address before: 277200 Shandong city of Zaozhuang province Shanting District City Town waterlogging Stephen East Village Patentee before: SHANDONG TONGTAIWEIRUN FOOD SCIENCE TECH Co.,Ltd. |
|
| CP03 | Change of name, title or address |