CN104180630A - Kelp dryer - Google Patents
Kelp dryer Download PDFInfo
- Publication number
- CN104180630A CN104180630A CN201410409535.4A CN201410409535A CN104180630A CN 104180630 A CN104180630 A CN 104180630A CN 201410409535 A CN201410409535 A CN 201410409535A CN 104180630 A CN104180630 A CN 104180630A
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- chamber
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- air
- baking oven
- hydrofuge
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- 241000512259 Ascophyllum nodosum Species 0.000 title abstract description 6
- 230000008676 import Effects 0.000 claims description 16
- 238000007599 discharging Methods 0.000 claims description 13
- 241001466453 Laminaria Species 0.000 claims description 11
- 238000007791 dehumidification Methods 0.000 claims description 8
- 230000008878 coupling Effects 0.000 claims description 4
- 238000010168 coupling process Methods 0.000 claims description 4
- 238000005859 coupling reaction Methods 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 abstract description 27
- 238000005192 partition Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 230000005540 biological transmission Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000007246 mechanism Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000007605 air drying Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- 241000238366 Cephalopoda Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000238557 Decapoda Species 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241000206607 Porphyra umbilicalis Species 0.000 description 1
- 206010053615 Thermal burn Diseases 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Landscapes
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to a kelp dryer comprising a plurality of drying ovens internally provided with baking chambers, a plurality of radiators in heat conduction connection with a heat source device, a plurality of circulating fans, a plurality of moisture exhausting fans and a conveyor which are sequentially arranged. The kelp dryer is characterized in that a wind collecting plate is fixed on the lower portion of the baking chamber of each drying oven, the top of each drying oven is divided into a temperature exhausting chamber and a circulating wind chamber by a partition, heat exchanging boxes are correspondingly arranged outside the drying ovens with the baking chambers, the radiators are arranged in the heat exchanging boxes, the circulating wind chambers are communicated with the heat exchanging boxes through the circulating fans, and the heat exchanging boxes are communicated with the baking chambers of the drying ovens; the moisture exhausting chambers are communicated with a public moisture exhausting pipe through the moisture exhausting fans; the upper conveying face of a conveying belt of the conveyor penetrates the baking chambers of the drying ovens, and the lower conveying face of the conveying belt of the conveyor penetrates the lower portions outside the baking chambers. The kelp dryer has the advantages that constantly feeding is achieved, drying efficiency is high, heat utilization rate is high, and drying degree is accurately controlled.
Description
Technical field
The present invention relates to the dry processing of edible seaweed, especially a main laminaria dryer.
Background technology
We know, sea-tangle is a kind of raw brown alga plant in large-scale sea growing in low temperature seawater, is the vegetables that nutritive value is very high, has certain medical value simultaneously.The deep processing of sea-tangle mainly comprise fresh sea-tangle scald boil with salt marsh process, the modes such as dry processing of fresh sea-tangle.The dry processing of traditional sea-tangle is mainly sea-tangle is dried or dry.Wherein, it is that sea-tangle is suspended on drying frame that sea-tangle is dried, and utilizes sunshine to be dried to water content and is no more than setting, and it is backward in technique that this dries mode, and the airing time is long, and working (machining) efficiency is low, and labor strength is large; It is that sea-tangle is placed in and is dried on the net that sea-tangle is dried, drying net overlays on the stoving rack of drying go-cart, send into again in drying chamber and carry out in heated-air drying, after dry by its taking-up, now put into another batch and treat dry sea-tangle, this main laminaria drying mode cannot be realized the serialization mode of production of the continuous discharging of continuous charging, and drying efficiency is low, the degree of drying cannot precisely be controlled simultaneously, exists and dries inhomogeneous deficiency.
Summary of the invention
For overcome in prior art sea-tangle be placed on drying vehicle, enter in drying chamber heated-air drying exist drying efficiency low, dry inhomogeneous deficiency, the invention provides a kind of reasonable in design, realize serialization production, drying efficiency is high, heat energy loss is little, oven dry degree is controlled sea-tangle dryer.
The technical solution adopted for the present invention to solve the technical problems is: a main laminaria dryer, it comprises and being arranged in order, inside is provided with some baking ovens in baking chamber, the some radiators that are connected with heat power supply device thermal conductivity, some circulating fans, some wet-emitting blowers and a device for transporting objects, described device for transporting objects comprises conveying motor, speed governing drive disk assembly, drive roll, driven voller, conveyer belt, pan feeding frame and discharging frame, described pan feeding frame is arranged on the top of the baking oven being arranged in order, described discharging machine frame is arranged on the end of the baking oven being arranged in order, described drive roll, driven voller respectively corresponding rotation is assemblied in pan feeding frame, in discharging frame, described conveyer belt is around being assemblied on drive roll and driven voller, described conveying motor is through speed governing drive disk assembly driving coupling drive roll, drive conveyer belt at drive roll conveyor surface and lower conveyor surface with driven voller last time then in formation, it is characterized in that:
In the same outside of casing of each baking oven, correspondence is provided with heat exchange box, and described radiator respectively correspondence is arranged in heat exchange box, on the casing of the top of each heat exchange box, offers air inlet, on the casing of the bottom of each heat exchange box, offers air outlet;
Baking top of chamber at each baking oven is vertically fixed a dividing plate, described dividing plate is by baking top of chamber spatial separation wet chamber in a row and a circulated air chamber of each baking oven, in the hydrofuge import in each hydrofuge chamber and the circulation air inlet place level in circulated air chamber, fix a wind deflector, the hydrofuge import in corresponding hydrofuge chamber on wind deflector, the circulation air inlet in circulated air chamber has air-guiding hole, on the top casing of the baking oven in corresponding each hydrofuge chamber, offer hydrofuge outlet, on the top casing of the baking oven in corresponding each circulated air chamber, offer and recycle air port, an air gathering plate is fixed in bottom, baking chamber at each baking oven,
Described circulating fan is corresponding being arranged on the casing upper surface of each baking oven respectively, and the air intake of each circulating fan, outlet air end are connected with the air inlet that recycles air port, heat exchange box in corresponding circulated air chamber respectively;
Described wet-emitting blower is corresponding being arranged on the casing upper surface of each baking oven respectively, the air intake of each wet-emitting blower is connected with the hydrofuge outlet in corresponding hydrofuge chamber respectively, and the outlet air end of each wet-emitting blower is connected with a public dehumidification tube through communicating pipe respectively;
The upper conveyor surface of described conveyer belt passes the baking chamber of the baking oven being arranged in order, the lower conveyor surface of described conveyer belt passes the Qiang Wai bottom, baking chamber of the baking oven being arranged in order, on the side box body of each baking oven below the upper conveyor surface of corresponding conveyer belt, offer hot blast import, described hot blast import is corresponding to be respectively connected with the air outlet of heat exchange box.
In each hydrofuge chamber, be provided with temperature controller, described temperature controller is controlled respectively the wet-emitting blower that is communicated with corresponding hydrofuge chamber.
Described air gathering plate that is fixed on each baking bottom, chamber is with the gradient, on the casing of each baking oven of bottom, corresponding air gathering plate slope, offers an impurities removal door.
On the casing of each baking oven of heat exchange box respective side, offer the case chamber door in a connection baking chamber.
Described heat power supply device is heat conducting oil boiler.
The present invention has the warm chamber of row and circulated air chamber by the baking top of chamber of each baking oven by a baffle for separating, heat exchange box is established in baking oven outside in each band baking chamber of correspondence, each is located in heat exchange box with the radiator that thermal source spring device thermal conductivity is connected, each circulating fan is communicated with between circulated air chamber and heat exchange box, heat exchange box is connected with the baking chamber of baking oven, the overfire air of radiator heat exchange acts on heat exchange box and baking chamber, circulated air circulate between chamber through circulating fan, effectively improve heat source utilization efficiency, greatly reduce the loss of heat energy; At each wet-emitting blower, be communicated with between hydrofuge chamber and public dehumidification tube, in dry run, produce a large amount of high-temperature water vapors and discharged by public dehumidification tube through wet-emitting blower effect, its good drying effect; The upper conveyor surface of the conveyer belt of its convey materials passes the baking chamber of baking oven, and the lower conveyor surface of conveyer belt passes the Qiang Wai bottom, baking chamber of baking oven, has realized the serialization drying mode of the continuous discharging of the continuous charging of material, has improved drying efficiency.The present invention is not only applicable to the oven dry of the raw algae in sea such as sea-tangle, opotism, laver, is equally applicable to the oven dry of the aquatic/marine animals such as fish, shrimp, squid or other food.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the present invention will be further described.
Fig. 1 is a kind of structural front view of the present invention;
Fig. 2 is along A-A line cutaway view in Fig. 1;
Fig. 3 is the syndeton schematic diagram of heat power supply device of the present invention and radiator.
Mark in figure: 1. baking oven, 101. baking chambeies, 1011. hot blast import, 102. hydrofuge chambeies, 1021. hydrofuge import, 1022. hydrofuge outlet, 103. circulated air chambeies, 1031. circulation air inlet, 1032. recycle air port, 2. device for transporting objects, 201. carry motor, 202. speed governing drive disk assemblies, 203. drive roll, 204. driven voller, 205. conveyer belt, 2051. upper conveyor surface, 2052. lower conveyor surface, 206. pan feeding frames, 207. discharging frames, 3. wet-emitting blower, 4. communicating pipe, 5. public dehumidification tube, 6. temperature controller, 7. case chamber door, 8. impurities removal door, 9. heat power supply device, 10. radiator, 11. circulating fans, 12. heat exchange box, 1201. air inlet, 1202. air outlet, 13. air gathering plates, 14. dividing plates, 15. wind deflectors, 1501. the first air-guiding hole, 1502. the second air-guiding hole.
The specific embodiment
In Fig. 1, Fig. 2, a main laminaria dryer, it comprises some baking ovens 1, some circulating fans 11, some wet-emitting blowers 3 and the device for transporting objects 2 being arranged in order.As shown in Figure 2, baking oven 1 inside is provided with baking chamber 101.
The number of baking oven 1 is determined according to the technological design length of drying line, and the number of units of circulating fan 11, wet-emitting blower 3 is corresponding with the number of baking oven 1.In Fig. 1, only provide two baking ovens, omitted other baking ovens.
As shown in Figure 1, device for transporting objects 2 comprises conveying motor 201, speed governing drive disk assembly 202, drive roll 203, driven voller 204, conveyer belt 205, pan feeding frame 206 and discharging frame 207.
In Fig. 1, pan feeding frame 206 is arranged on the top of the baking oven 1 being arranged in order, and 207 of discharging machines are arranged on the end of the baking oven 1 being arranged in order.
Drive roll 203, driven voller 204 adopt respectively bearing and bearing block in the usual way corresponding rotation be assemblied in pan feeding frame 206, discharging frame 207.
What conveyer belt 205 was selected is stainless steel guipure, and it assembles mode routinely around being assemblied on drive roll 203 and driven voller 204.
Speed governing drive disk assembly can adopt commercially available gear driven type decelerator, also can adopt belt wheel transmission mechanism or other conventional reduction gearing mechanisms, will carry motor and drive roll to realize driving coupling.As shown in Figure 1, what the speed governing drive disk assembly 202 of the present embodiment adopted is belt wheel transmission mechanism, by changing the gearratio of driven wheel, realizes deceleration transmission.
As shown in Figure 1, carry motor 201 through speed governing drive disk assembly 202 driving coupling drive rolls 203, drive conveyer belt 205 at drive roll 203 conveyor surface 2051 and lower conveyor surface 2052 with 204 last times of driven voller then on forming.
In Fig. 3, a main laminaria dryer also comprises the some radiators 10 that are connected with heat power supply device 9 thermal conductivity.The number of radiator 10 is also corresponding with the number of baking oven 1.Wherein, heat power supply device 9 can adopt heat conducting oil boiler, also can adopt steam boiler.Because heat conducting oil boiler liquid phase is carried heat energy, heat loss is little, energy-saving effect is remarkable, and under the condition of normal pressure almost, can obtain very high operating temperature and wider temperature range (100-400 ℃), can meet the process requirements of different temperatures, so the 9 preferential employings of the present embodiment heat power supply device is heat conducting oil boiler.Heat conducting oil boiler can adopt the mode of electrical heating or gas heating or coal-fired heating.As shown in Figure 3, the parts that its thermal conductivity connects comprise conventional tube connector, oil spilling case, oil circulating pump, filter and valve.
In Fig. 2, in the same outside of casing of each baking oven 1, correspondence is provided with heat exchange box 12, and radiator 10 respectively correspondence is arranged in heat exchange box 12.The tube connector that conduction oil in heat conducting oil boiler connects through thermal conductivity enters radiator 10, and the air in the heat that radiator 10 distributes and heat exchange box 12 carries out exchange heat and generates the overfire air as thermal source.
As shown in Figure 2, on the casing of the top of each heat exchange box 12, offer air inlet 1201, on the casing of the bottom of each heat exchange box 12, offer air outlet 1202.
As shown in Figure 2, at 101 tops, baking chamber of each baking oven 1, vertically fix a dividing plate 14, dividing plate 14 is separated into a hydrofuge chamber 102 and a circulated air chamber 103 by baking chamber 101 headrooms of each baking oven 1.
In Fig. 2, the accent place in each hydrofuge chamber 102 is hydrofuge import 1021, on the top casing of the baking oven 1 in corresponding each hydrofuge chamber 102, offers hydrofuge outlet 1022.The accent place in each circulated air chamber 103 is circulation air inlet 1031, on the top casing of the baking oven 1 in corresponding each circulated air chamber 103, offers and recycles air port 1032.
In Fig. 1, in hydrofuge import 1021 and circulation air inlet 1031 place's levels in circulated air chamber 103 in each hydrofuge chamber 102, fix a wind deflector 15.As shown in Figure 2, on wind deflector 15 the hydrofuge import 1021 in corresponding hydrofuge chamber, the circulation air inlet 1031 in circulated air chamber has the first air-guiding hole 1501, the second air-guiding hole 1502.The first air-guiding hole 1501, the second air-guiding hole 1502 can play even importing effect to entering into the moving air in hydrofuge chamber 102, circulated air chamber 103.
As shown in Figure 2, in 101 bottoms, baking chamber of each baking oven 1, fix an air gathering plate 13.
In Fig. 2, circulating fan 11 is corresponding being arranged on the casing upper surface of each baking oven 1 respectively, and the air intake of each circulating fan 11, outlet air end are connected with the air inlet 1201 that recycles air port 1032, heat exchange box 12 in corresponding circulated air chamber 103 respectively.The overfire air of radiator 10 heat exchange acts on heat exchange box 12 and toasts between chamber 101, circulated air chamber 103 through circulating fan 11 and circulates, and effectively improves heat source utilization efficiency, greatly reduces the loss of heat energy.
In Fig. 1, Fig. 2, wet-emitting blower 3 is corresponding being arranged on the casing upper surface of each baking oven 1 respectively.What wet-emitting blower 3 was selected is axial fan.As shown in Figure 2, the air intake of each wet-emitting blower 3 is connected with the hydrofuge outlet 1022 in corresponding hydrofuge chamber 102 respectively.As shown in Figure 1 and Figure 2, the outlet air end of each wet-emitting blower 3 is connected with a public dehumidification tube 5 through communicating pipe 4 respectively, and the output of this public dehumidification tube 5 is connected with atmosphere.In dry run, a large amount of high-temperature water vapors of the baking interior generation in chamber 101 are discharged by public dehumidification tube 5 through communicating pipe 4 in time through wet-emitting blower 3 effects, its good drying effect.
In Fig. 1, Fig. 2, the upper conveyor surface 2051 of conveyer belt passes the baking chamber 101 of the baking oven 1 being arranged in order, and the lower conveyor surface 2052 of conveyer belt passes the Qiang Wai bottom, baking chamber of the baking oven 1 being arranged in order.Conveyer belt 205 is constantly revolution on drive roll 203 and driven voller 204, has realized the serialization drying mode of the continuous discharging of the continuous charging of material, has improved drying efficiency.
As shown in Figure 2, on the side box body of each baking oven 1 below the upper conveyor surface 2051 of corresponding conveyer belt, offer hot blast import 1011, hot blast import 1011 is corresponding to be connected with the air outlet 1202 of heat exchange box 12.Overfire air blows out from the air outlet 1202 of heat exchange box 12, through hot blast import 1011, enter baking chamber 101, the upper conveyor surface 2051 that is upward through conveyer belt from upper conveyor surface 2051 belows of conveyer belt, is dried the sea-tangle of the high humidity on the upper conveyor surface 2051 of conveyer belt, and it is dried evenly.
In Fig. 1, Fig. 2, in each hydrofuge chamber 102, be provided with temperature controller 6, temperature controller 6 is electrically connected to respectively with the wet-emitting blower 3 in corresponding connection hydrofuge chamber 102 in a conventional manner, temperature in 6 pairs of hydrofuge chambeies 102 of temperature controller detects automatically, according to the technological temperature of setting, control wet-emitting blower 3 start and stop in good time, realized oven dry degree is precisely controlled.
On sea-tangle drying course, can produce kelp residue, for kelp residue is cleared up easily, as shown in Figure 2, the air gathering plate 13 that is fixed on each baking 101 bottom, chamber is designed to certain slope.In Fig. 1, Fig. 2, on the casing of each baking oven 1 of corresponding air gathering plate 13 bottoms, slope, offer an impurities removal door 8.
In Fig. 1, Fig. 2, on the casing of each baking oven 1 of heat exchange box 12 respective side, offer the case chamber door 7 in a connection baking chamber 101, so that observe at any time the situation of baking in casing, simultaneously convenient parts in baking chamber 101 are overhauled.
The present invention has realized the feeding manner that constantly enters constantly to go out, and has changed the modes to be baked such as original, makes bake process realize the possibility of automatic production line, greatly improved product efficiency, baking degree is even, and the sea-tangle moisture after baking is controlled accurately, simple to operate.
Claims (5)
1. a main laminaria dryer, it comprises and being arranged in order, inside is provided with some baking ovens in baking chamber, the some radiators that are connected with heat power supply device thermal conductivity, some circulating fans, some wet-emitting blowers and a device for transporting objects, described device for transporting objects comprises conveying motor, speed governing drive disk assembly, drive roll, driven voller, conveyer belt, pan feeding frame and discharging frame, described pan feeding frame is arranged on the top of the baking oven being arranged in order, described discharging machine frame is arranged on the end of the baking oven being arranged in order, described drive roll, driven voller respectively corresponding rotation is assemblied in pan feeding frame, in discharging frame, described conveyer belt is around being assemblied on drive roll and driven voller, described conveying motor is through speed governing drive disk assembly driving coupling drive roll, drive conveyer belt at drive roll conveyor surface and lower conveyor surface with driven voller last time then in formation, it is characterized in that:
In the same outside of casing of each baking oven, correspondence is provided with heat exchange box, and described radiator respectively correspondence is arranged in heat exchange box, on the casing of the top of each heat exchange box, offers air inlet, on the casing of the bottom of each heat exchange box, offers air outlet;
Baking top of chamber at each baking oven is vertically fixed a dividing plate, described dividing plate is by baking top of chamber spatial separation wet chamber in a row and a circulated air chamber of each baking oven, in the hydrofuge import in each hydrofuge chamber and the circulation air inlet place level in circulated air chamber, fix a wind deflector, the hydrofuge import in corresponding hydrofuge chamber on wind deflector, the circulation air inlet in circulated air chamber has air-guiding hole, on the top casing of the baking oven in corresponding each hydrofuge chamber, offer hydrofuge outlet, on the top casing of the baking oven in corresponding each circulated air chamber, offer and recycle air port, an air gathering plate is fixed in bottom, baking chamber at each baking oven,
Described circulating fan is corresponding being arranged on the casing upper surface of each baking oven respectively, and the air intake of each circulating fan, outlet air end are connected with the air inlet that recycles air port, heat exchange box in corresponding circulated air chamber respectively;
Described wet-emitting blower is corresponding being arranged on the casing upper surface of each baking oven respectively, the air intake of each wet-emitting blower is connected with the hydrofuge outlet in corresponding hydrofuge chamber respectively, and the outlet air end of each wet-emitting blower is connected with a public dehumidification tube through communicating pipe respectively;
The upper conveyor surface of described conveyer belt passes the baking chamber of the baking oven being arranged in order, the lower conveyor surface of described conveyer belt passes the Qiang Wai bottom, baking chamber of the baking oven being arranged in order, on the side box body of each baking oven below the upper conveyor surface of corresponding conveyer belt, offer hot blast import, described hot blast import is corresponding to be respectively connected with the air outlet of heat exchange box.
2. a main laminaria dryer according to claim 1, is characterized in that: in each hydrofuge chamber, be provided with temperature controller, described temperature controller is controlled respectively the wet-emitting blower that is communicated with corresponding hydrofuge chamber.
3. a main laminaria dryer according to claim 1, is characterized in that: described air gathering plate that is fixed on each baking bottom, chamber is with the gradient, on the casing of each baking oven of bottom, corresponding air gathering plate slope, offers an impurities removal door.
4. a main laminaria dryer according to claim 1, is characterized in that: the case chamber door of offering a connection baking chamber on the casing of each baking oven of heat exchange box respective side.
5. a main laminaria dryer according to claim 1, is characterized in that: described heat power supply device is heat conducting oil boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410409535.4A CN104180630B (en) | 2014-08-20 | 2014-08-20 | One main laminaria dehydrator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410409535.4A CN104180630B (en) | 2014-08-20 | 2014-08-20 | One main laminaria dehydrator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104180630A true CN104180630A (en) | 2014-12-03 |
| CN104180630B CN104180630B (en) | 2016-09-07 |
Family
ID=51961846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410409535.4A Expired - Fee Related CN104180630B (en) | 2014-08-20 | 2014-08-20 | One main laminaria dehydrator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104180630B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091554A (en) * | 2015-09-13 | 2015-11-25 | 安徽省葛根生产力促进中心有限公司 | Automatic temperature control dryer |
| CN106766797A (en) * | 2016-11-24 | 2017-05-31 | 防城港市海洋局 | A kind of marine product hothouse |
| CN107865456A (en) * | 2017-12-14 | 2018-04-03 | 无锡市尚德干燥设备有限公司 | The marine alga drying machine of electrical deinsectization guard is installed |
| CN107906910A (en) * | 2017-10-19 | 2018-04-13 | 安徽工程大学 | A kind of high efficiency drying mechanism for Weaving device |
| CN112629225A (en) * | 2021-03-11 | 2021-04-09 | 山东汤润食品科技有限公司 | Food drying device |
| CN117898444A (en) * | 2024-03-15 | 2024-04-19 | 福州亿达食品有限公司 | Kelp crisp production processing device and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103090654B (en) * | 2011-11-02 | 2015-05-06 | 上海远跃制药机械股份有限公司 | Drying device and drying method for pills |
| CN102823640B (en) * | 2012-09-24 | 2013-09-04 | 陈锦权 | Energy-conservation drying device for drying vegetables and seaweed type products and drying method thereof |
| CN103767052B (en) * | 2014-01-21 | 2015-09-16 | 潍坊舜天机电设备有限公司 | Sea-tangle plate dish double-vane multilayer can lift rack drying vehicle |
| CN204007023U (en) * | 2014-08-20 | 2014-12-10 | 王波 | One main laminaria dryer |
-
2014
- 2014-08-20 CN CN201410409535.4A patent/CN104180630B/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105091554A (en) * | 2015-09-13 | 2015-11-25 | 安徽省葛根生产力促进中心有限公司 | Automatic temperature control dryer |
| CN106766797A (en) * | 2016-11-24 | 2017-05-31 | 防城港市海洋局 | A kind of marine product hothouse |
| CN107906910A (en) * | 2017-10-19 | 2018-04-13 | 安徽工程大学 | A kind of high efficiency drying mechanism for Weaving device |
| CN107865456A (en) * | 2017-12-14 | 2018-04-03 | 无锡市尚德干燥设备有限公司 | The marine alga drying machine of electrical deinsectization guard is installed |
| CN112629225A (en) * | 2021-03-11 | 2021-04-09 | 山东汤润食品科技有限公司 | Food drying device |
| CN112629225B (en) * | 2021-03-11 | 2021-06-04 | 山东汤润食品科技有限公司 | Food drying device |
| CN117898444A (en) * | 2024-03-15 | 2024-04-19 | 福州亿达食品有限公司 | Kelp crisp production processing device and preparation method thereof |
| CN117898444B (en) * | 2024-03-15 | 2024-05-31 | 福州亿达食品有限公司 | Kelp crisp production processing device and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104180630B (en) | 2016-09-07 |
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