CN203181964U - Water medium circulating system drying device - Google Patents
Water medium circulating system drying device Download PDFInfo
- Publication number
- CN203181964U CN203181964U CN 201320200733 CN201320200733U CN203181964U CN 203181964 U CN203181964 U CN 203181964U CN 201320200733 CN201320200733 CN 201320200733 CN 201320200733 U CN201320200733 U CN 201320200733U CN 203181964 U CN203181964 U CN 203181964U
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- water
- hot
- aqueous medium
- heat exchanger
- heat exchange
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Abstract
The utility model relates to a marine food product drying facility, in particular to a water medium circulating system drying device. The water medium circulating system drying device adopts a hot water medium to conduct heat exchange circulating drying and is composed of a hot water medium circulating system and a hot air conveying system. A hot water generator for supplying hot water media is arranged on a heat source part at the initial end of the hot water medium circulating system. A water supplying pipe is connected with the upper portion of a heat exchange water sleeve inside the hot water generator, a water inlet of a heat exchange coil pipe of a heat exchanger is connected with the water supplying pipe, a water outlet of the heat exchange coil pipe of the heat exchanger is connected with a water return pipe, and the hot water medium circulating system is formed. A hot air inlet is formed in the top of one side of a drying chamber, a support is arranged above the hot air inlet, the heat exchanger is placed above the support, an axial flow fan is arranged below the heat exchanger, and the hot air conveying system is formed. The hot water medium circulating system and the hot air conveying system are combined with the axial flow fan through the heat exchanger, and the dual-level heat exchange system drying device is formed. The water medium circulating system drying device reduces production cost, overcomes secondary pollution, eliminates potential safety hazards and improves the energy utilization rate and production efficiency.
Description
Technical field
The utility model relates to a kind of marine product drying facility.
Background technology
Existing drying equipment thermal source part for laver, other dish classes is fuel with fuel oil (diesel oil), makes cylindrical shell produce heat by oil inflame, and heat supply pipeline just hot blast is transported to the oven dry that drying chamber is finished laver.Because oil burning installation is installed in the machine two ends, ignition temperature is not less than 800C °, very easily causes fire in the production process, and damage equipment jeopardizes personal safety; And by air or directly cause the secondary pollution of laver product.
Summary of the invention
The utility model purpose provides a kind of aqueous medium circulatory system drying equipment, easily causes fire to solve in the prior art production process, and damage equipment jeopardizes personal safety; And by air or directly cause the secondary pollution problems of laver product.
The utility model mainly is made up of thermal source part, hot blast conveying equipment, 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 system drying equipment is made up of hot aqueous medium's circulatory system and hot blast induction 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 burning water heating stove or electric heating water heater all can, heat exchanging water-jacket top in the hot water generator connects water supply line, temperature controller and feed pipe stop valve are set on the water supply line, the water inlet of heat exchanger heat exchange coil connects water supply line, the delivery port of heat exchanger heat exchange coil connects water return pipeline, and water circulating inspector and water pump are set on the water return pipeline; Constitute hot aqueous medium's circulatory system; Drying chamber one side roof part arranges the hot blast import, and hot blast import top arranges support, and heat exchanger places the support top, the heat exchanger below arranges axial flow blower, the corresponding heat exchanger in axial flow blower inlet scoop, the import of the corresponding drying chamber top hot blast of axial flow blower exhaust outlet constitutes the hot blast induction system; Hot aqueous medium's circulatory system is combined with axial flow blower by heat exchanger with the hot blast induction system, constitutes system's drying equipment of secondary heat exchange.
Adopting good effect of the present utility model is that this system equipment heats fuel oil and changes the aqueous medium heat exchange into, because of hydrone more stable, thereby make the production temperature equalization, solved the product interior quality defective that causes because of the front and back temperature difference, no matter product quality is able to largest optimization in taste, quality, impression, through the radical change of thermal medium and the change of hot water cyclesystem installation site, overcome the defective of former fuel oil technology.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.
Description of drawings
Below in conjunction with drawings and Examples the utility model is further specified:
Accompanying drawing 1 is the utility model structural representation;
1 hot water generator, 2 temperature controllers, 3 feed pipe stop valves, 4 water supply lines, 5 heat exchangers, 6 water return pipelines, 7 return pipe stop valves, 8 water circulating inspectors, 9 water pumps, 10 axial flow blowers, 11 supports, 12 hot blast imports, 13 drying chambers among the figure.
The specific embodiment
Below in conjunction with the drawings and specific embodiments to this practical being described further:
As shown in the figure; Described system drying equipment is made up of hot aqueous medium's circulatory system and hot blast induction system, its hot aqueous medium's circulatory system top thermal source partly arranges the hot water generator 1 that the hot aqueous medium is provided, hot water generator 1 adopts coal burning water heating stove or electric heating water heater all can, heat exchanging water-jacket top in the hot water generator 1 connects water supply line 4, temperature controller 2 and feed pipe stop valve 3 are set on the water supply line 4, the water inlet of heat exchanger 5 heat exchange coils connects water supply line 4, the delivery port of heat exchanger 5 heat exchange coils connects water return pipeline 6, and water circulating inspector 8 and water pump 9 are set on the water return pipeline 6; Constitute hot aqueous medium's circulatory system; Drying chamber 13 1 side roof parts arrange hot blast import 12, hot blast import 12 tops arrange support 11, heat exchanger 5 places support 11 tops, heat exchanger 5 belows arrange axial flow blower 10, the corresponding heat exchanger 5 in axial flow blower 10 inlet scoops, the corresponding drying chamber top hot blast of axial flow blower 10 exhaust outlets import 12 constitutes the hot blast induction system; Hot aqueous medium's circulatory system is combined with axial flow blower by heat exchanger with the hot blast induction system, constitutes system's drying equipment of secondary heat exchange.
During work, hot water generator is heated to 70-90 ℃ with aqueous medium, under the effect of water pump, the aqueous medium of heating is sent into heat exchanger by water supply line, concentrate heat radiation by the heat exchange coil 8 in the heat exchanger, and become hot blast in the quick heat exchange of air-flow of axial flow blower suction, deliver to drying chamber by axial flow blower, air-flow band after the cooling moisture and is discharged by steam vent, realizes the flash baking of laver.
Claims (5)
1. an aqueous medium circulatory system drying equipment mainly is made up of thermal source part, hot blast conveying equipment, drying chamber, it is characterized in that adopting hot aqueous medium's heat exchange cyclic drying; Described system drying equipment is made up of hot aqueous medium's circulatory system and hot blast induction 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 the hot water generator connects water supply line, the water inlet of heat exchanger heat exchange coil connects water supply line, the delivery port of heat exchanger heat exchange coil connects water return pipeline, constitutes hot aqueous medium's circulatory system; Drying chamber one side roof part arranges the hot blast import, and hot blast import top arranges support, and heat exchanger places the support top, and the heat exchanger below arranges axial flow blower, constitutes the hot blast induction system; Hot aqueous medium's circulatory system is combined with axial flow blower by heat exchanger with the hot blast induction system, constitutes system's drying equipment of secondary heat exchange.
2. aqueous medium circulatory system drying equipment as claimed in claim 1 is characterized in that hot water generator adopts coal burning water heating stove or electric heating water heater all can.
3. aqueous medium circulatory system drying equipment as claimed in claim 1 is characterized in that arranging on the water supply line temperature controller and feed pipe stop valve.
4. aqueous medium circulatory system drying equipment as claimed in claim 1 is characterized in that arranging on the water return pipeline water circulating inspector and water pump.
5. aqueous medium circulatory system drying equipment as claimed in claim 1 is characterized in that the corresponding heat exchanger in axial flow blower inlet scoop, the import of the corresponding drying chamber top hot blast of axial flow blower exhaust outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320200733 CN203181964U (en) | 2013-04-20 | 2013-04-20 | Water medium circulating system drying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320200733 CN203181964U (en) | 2013-04-20 | 2013-04-20 | Water medium circulating system drying device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203181964U true CN203181964U (en) | 2013-09-11 |
Family
ID=49098880
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320200733 Expired - Fee Related CN203181964U (en) | 2013-04-20 | 2013-04-20 | Water medium circulating system drying device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203181964U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106798270A (en) * | 2017-03-23 | 2017-06-06 | 宁波大学 | The hot water constant temperature drying and processing method and device of a kind of porphyra haitanensis |
-
2013
- 2013-04-20 CN CN 201320200733 patent/CN203181964U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106798270A (en) * | 2017-03-23 | 2017-06-06 | 宁波大学 | The hot water constant temperature drying and processing method and device of a kind of porphyra haitanensis |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130911 Termination date: 20160420 |