CN203353638U - Water medium circulating system drying device - Google Patents
Water medium circulating system drying device Download PDFInfo
- Publication number
- CN203353638U CN203353638U CN2013204073407U CN201320407340U CN203353638U CN 203353638 U CN203353638 U CN 203353638U CN 2013204073407 U CN2013204073407 U CN 2013204073407U CN 201320407340 U CN201320407340 U CN 201320407340U CN 203353638 U CN203353638 U CN 203353638U
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- hot
- water
- heat exchanger
- aqueous medium
- medium circulating
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- 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
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Abstract
The utility model provides a water medium circulating system drying device, and relates to seafood drying facilities. The system drying device conducts circular drying by the adoption of heat exchange of hot water media, a hot water generator supplying the hot water media is arranged on a heat source portion at the starting end of a hot water medium circulating system, the upper portion of a heat exchange water sleeve in the hot water generator is connected with a water supply pipeline which is connected with an efficient heat exchanger, a heat exchange coil pipe is arranged in a heat exchanger shell, a water inlet of the heat exchanger coil pipe is connected with the water supply pipeline, and a water outlet of the heat exchanger coil pipe is connected with a water return pipeline; the lower side of the heat exchanger shell is connected with a drainage pipeline which is provided with a steam trap, the other end of the drainage pipeline is connected with the water return pipeline, and the hot water medium circulating system is constituted. An axial flow fan is arranged at the bottom of the heat exchanger, a hot air outlet is arranged at the top of the heat exchanger and connected with a hot air conveying pipeline which is connected with a drying chamber, and a hot air conveying system is constituted. The hot water medium circulating system and the hot air conveying system are combined through the heat exchanger to constitute the system drying device achieving two-stage heat exchange.
Description
Technical field
The utility model relates to a kind of marine product drying facility.
Background technology
It is fuel that the existing drying equipment thermal source for laver, other dish classes part be take fuel oil (diesel oil), by oil inflame, makes cylindrical shell generation heat, and heat supply pipeline just hot blast is transported to the oven dry that drying chamber completes laver.Because oil burning installation is arranged on the machine two ends, ignition temperature is not less than 800C °, very easily causes fire in production process, and damage equipment, jeopardize personal safety; And by air or directly cause the secondary pollution of laver product.
Summary of the invention
The utility model purpose is to provide a kind of aqueous medium circulating system drying equipment, to solve in the prior art production process, easily causes fire, and damage equipment, jeopardize personal safety; And by air or directly cause the secondary pollution problems of laver product.
The utility model mainly is comprised of thermal source part, hot blast conveying pipe road, drying chamber, and solving the technical scheme that its technical problem adopts is to abandon fuel oil to heat drying, adopts hot aqueous medium's heat exchange cyclic drying, described laver drying system equipment is comprised of hot aqueous medium's circulatory system and hot air delivery system, its hot aqueous medium's circulatory system top thermal source partly arranges the hot water generator that the hot aqueous medium is provided, hot water generator adopts coal-firing water boiler or electric heating water heater all can, heat exchanging water-jacket top in hot water generator connects water supply line, temperature controller and feed pipe stop valve are set on water supply line, water supply line connects high-performance heat exchanger, high-performance heat exchanger is housings close formula structure, heat exchange coil is set in heat exchanger shell, the water inlet of heat exchange coil connects water supply line, the delivery port of heat exchange coil connects water return pipeline, water circulation detector and water pump are set on water return pipeline, the below of heat exchanger problem connects drain water piping, and steam trap is set on drain water piping, and the aqueduct other end connects water return pipeline, forms hot aqueous medium's circulatory system.The heat exchanger bottom arranges axial flow blower, and the heat exchanger top arranges hot-blast outlet, and hot-blast outlet connects the hot blast conveying pipe road, and the hot blast conveying pipe road connects drying chamber, forms hot air delivery system.Hot aqueous medium's circulatory system is combined by heat exchanger with hot air delivery system, forms the laver drying system equipment of secondary heat exchange.
Adopting the good effect of standby utility model is that this system equipment heats fuel oil to change the aqueous medium heat exchange into, because of hydrone more stable, thereby make the production temperature equalization, solved the product interior quality defect caused because of the front and back temperature difference, no matter product quality is able to largest optimization on taste, quality, perception. through the radical change of thermal medium and the change of hot water cyclesystem installation site, overcome the defect of former fuel oil technique.Reduced energy consumption, improved energy utilization rate and production efficiency, product quality obtains largest optimization, has reduced production cost, has overcome the secondary pollution of product, has guaranteed product quality.Thoroughly eliminate safe hidden trouble, safety in production has also obtained guarantee.
The accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Accompanying drawing 1 is the utility model structural representation;
In figure, 2 water supply lines, 3 temperature controllers, 4 feed pipe stop valve 5 heat exchangers, 6 hot blast conveying pipe roads, 7 hot-blast outlets, 8 heat exchange coils, 9 heat exchanger shells, 10 steam traps, 11 return pipe stop valves, 12 drain water pipings, 13 water return pipelines, 14 axial flow blowers, 15 water circulation detectors, 16 water pumps, 17 drying chambers occur in 1 hot water.
The specific embodiment
Below in conjunction with the drawings and specific embodiments to this practical being described further:
As shown in the figure, system drying equipment top thermal source partly arranges the hot water generator 1 that the hot aqueous medium is provided, hot water generator 1 adopts coal-firing water boiler or electric heating water heater all can, heat exchanging water-jacket top in hot water generator connects water supply line 2, temperature controller 3 and feed pipe stop valve 4 are set on water supply line 2, water supply line 2 connects high-performance heat exchanger 5, heat exchanger 5 is the case type structure, the interior heat exchange coil 8 that arranges of heat exchanger shell 9, the water inlet of heat exchange coil 8 connects water supply line 2, the delivery port of heat exchange coil 8 connects water return pipeline 13, water circulation detector 15 and water pump 16 are set on water return pipeline 13, the below of heat exchanger shell 9 connects drain water piping 12, and steam trap 10 is set on drain water piping 12, and aqueduct 12 other ends connect water return pipeline 13, form hot aqueous medium's circulatory system.Heat exchanger 5 bottoms arrange axial flow blower 14, and heat exchanger 5 tops arrange hot-blast outlet 7, and hot-blast outlet 7 connects hot blast conveying pipe road 6, and hot blast conveying pipe road 6 connects drying chamber 17, forms hot air delivery system.Hot aqueous medium's circulatory system is combined by heat exchanger with hot air delivery system, forms the laver drying system equipment of secondary heat exchange.
During work, hot water generator 1 is heated to 70-90 ℃ by aqueous medium, under the effect of water pump, the aqueous medium of heating is sent into to heat exchanger 5 by water supply line 2, concentrate heat radiation by the heat exchange coil 8 in heat exchanger 5 housings, and become hot blast in the quick heat exchange of air-flow of axial flow blower 14 conveyings, the hot blast conveying pipe road 6 arranged by heat exchanger 5 tops is transported to drying chamber 17 by hot blast, air-flow after cooling is discharged by steam vent with moisture, realizes the flash baking of laver.
Claims (6)
1. an aqueous medium circulating system drying equipment, mainly by the thermal source part, the hot blast conveying pipe road, drying chamber forms, it is characterized in that adopting hot aqueous medium's heat exchange cyclic drying, described system drying equipment is comprised of hot aqueous medium's circulatory system and hot air delivery system, its hot aqueous medium's circulatory system top thermal source partly arranges the hot water generator that the hot aqueous medium is provided, heat exchanging water-jacket top in hot water generator connects water supply line, water supply line connects high-performance heat exchanger, heat exchange coil is set in heat exchanger shell, the water inlet of heat exchange coil connects water supply line, the delivery port of heat exchange coil connects water return pipeline, the below of heat exchanger problem connects drain water piping, and steam trap is set on drain water piping, and the aqueduct other end connects water return pipeline, forms hot aqueous medium's circulatory system, the heat exchanger bottom arranges axial flow blower, and the heat exchanger top arranges hot-blast outlet, and hot-blast outlet connects the hot blast conveying pipe road, and the hot blast conveying pipe road connects drying chamber, forms hot air delivery system.
2. aqueous medium circulating system drying equipment according to claim 1, is characterized in that hot water generator adopts coal-firing water boiler or electric heating water heater all can.
3. aqueous medium circulating system drying equipment according to claim 1, is characterized in that on water supply line arranging temperature controller and feed pipe stop valve.
4. aqueous medium circulating system drying equipment according to claim 1, is characterized in that high-performance heat exchanger is housings close formula structure.
5. aqueous medium circulating system drying equipment according to claim 1, is characterized in that on water return pipeline arranging water circulation detector and water pump.
6. aqueous medium circulating system drying equipment according to claim 1, is characterized in that hot aqueous medium's circulatory system is combined by heat exchanger with hot air delivery system, forms the system drying equipment of secondary heat exchange.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013204073407U CN203353638U (en) | 2013-03-25 | 2013-07-10 | Water medium circulating system drying device |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320137852.6 | 2013-03-25 | ||
| CN201320137852 | 2013-03-25 | ||
| CN2013204073407U CN203353638U (en) | 2013-03-25 | 2013-07-10 | Water medium circulating system drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203353638U true CN203353638U (en) | 2013-12-25 |
Family
ID=49801485
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013204073407U Expired - Fee Related CN203353638U (en) | 2013-03-25 | 2013-07-10 | Water medium circulating system drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203353638U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103385530A (en) * | 2013-03-25 | 2013-11-13 | 德州炬创换热器制造有限公司 | Drying equipment for aqueous medium circulation system |
-
2013
- 2013-07-10 CN CN2013204073407U patent/CN203353638U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103385530A (en) * | 2013-03-25 | 2013-11-13 | 德州炬创换热器制造有限公司 | Drying equipment for aqueous medium circulation system |
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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: 20131225 Termination date: 20150710 |
|
| EXPY | Termination of patent right or utility model |