CN103385530A - Drying equipment for aqueous medium circulation system - Google Patents
Drying equipment for aqueous medium circulation system Download PDFInfo
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- CN103385530A CN103385530A CN2013102871604A CN201310287160A CN103385530A CN 103385530 A CN103385530 A CN 103385530A CN 2013102871604 A CN2013102871604 A CN 2013102871604A CN 201310287160 A CN201310287160 A CN 201310287160A CN 103385530 A CN103385530 A CN 103385530A
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- aqueous medium
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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 invention discloses drying equipment for an aqueous medium circulation system, and relates to a drying facility for seafoods. The drying equipment for the aqueous medium circulation system adopts a hot water medium heat exchanging circulation to dry the seafoods, a hot water generator for providing the hot water medium is arranged in the start end heat source part of a hot water medium circulation system, a water supply pipeline is connected with the upper part of a hot water exchanging jacket in the hot water generator, the water supply pipeline is connected with a high-efficient heat changer, a heat exchange coil is arranged in the casing of the heat exchanger, the water inlet of the heat exchange coil is connected with the water supply pipeline, and the water outlet of the heat exchange coil is connected with a water return pipeline; and a water drainage pipeline is connected below the casing of the heat exchanger, the water drainage pipeline is provided with a water drainage device, and the other end of the water drainage pipeline is connected with the water return pipeline to form the hot water medium circulation system. An axial flow fan is arranged on the bottom of the heat exchanger, a hot wind outlet is arranged on top of the heat exchanger, the hot wind outlet is connected with a hot wind conveying pipeline, and the hot wind conveying pipeline is connected with a drying chamber to form a hot wind conveying system. The hot water medium circulation system and the hot wind conveying system are combined through the heat exchanger to form the drying device for a secondary heat exchange system.
Description
Technical field
The present invention relates to a kind of marine product drying facility.
Background technology
Existing drying equipment thermal source for laver, other dish classes part, take fuel oil (diesel oil) as fuel, makes cylindrical shell generation heat by oil inflame, and heat supply pipeline just hot blast is transported to drying chamber and completes the oven dry of 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 object of the invention 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 present invention 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 good effect of the present invention 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 that causes because of the front and back temperature difference, no matter product quality is able to largest optimization on taste, quality, impression., 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.
Description of drawings
The present invention is further described below in conjunction with drawings and Examples:
Accompanying drawing 1 is structural representation of the present invention;
1 hot water generator, 2 water supply lines, 3 temperature controllers, 4 feed pipe stop valves, 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 in figure.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, invention is 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 ℃ with aqueous medium, under the effect of water pump, the aqueous medium of heating is sent into heat exchanger 5 by water supply line 2, concentrate heat radiation by the heat exchange coil 8 in heat exchanger 5 housings, and in the quick heat exchange of air-flow of axial flow blower 14 conveyings, become hot blast, the hot blast conveying pipe road 6 that is arranged by heat exchanger 5 tops is transported to drying chamber 17 with hot blast, air-flow after cooling is discharged by steam vent with moisture, realizes the flash baking of laver.
Claims (6)
1. 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 |
|---|---|---|---|
| CN201310287160.4A CN103385530B (en) | 2013-03-25 | 2013-07-10 | Aqueous medium circulating system drying equipment |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310096833.8 | 2013-03-25 | ||
| CN2013100968338 | 2013-03-25 | ||
| CN201310096833 | 2013-03-25 | ||
| CN201310287160.4A CN103385530B (en) | 2013-03-25 | 2013-07-10 | Aqueous medium circulating system drying equipment |
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| Publication Number | Publication Date |
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| CN103385530A true CN103385530A (en) | 2013-11-13 |
| CN103385530B CN103385530B (en) | 2016-12-28 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201310287160.4A Expired - Fee Related CN103385530B (en) | 2013-03-25 | 2013-07-10 | Aqueous medium circulating system drying equipment |
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| CN (1) | CN103385530B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105495651A (en) * | 2015-12-17 | 2016-04-20 | 江苏杰英能源科技有限公司 | Waste heat recovery mechanism of vegetable dehydration device |
| CN108131956A (en) * | 2017-12-29 | 2018-06-08 | 焱鑫环保科技有限公司 | A kind of method for subtracting furnace charge briquetting moisture and auto feed using the baking of blast furnace shaft water jacket circulating hot water |
| CN108317842A (en) * | 2018-02-07 | 2018-07-24 | 安徽江淮汽车集团股份有限公司 | Coating lifting drying system |
Citations (7)
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| CN101946968A (en) * | 2010-08-26 | 2011-01-19 | 王宁州 | Multifunctional dryer |
| CN201774938U (en) * | 2010-08-18 | 2011-03-30 | 甘肃省机械科学研究院 | Fruit and vegetable drying system adopting combined heat sources of solar energy and heat pump |
| CN201945154U (en) * | 2011-01-07 | 2011-08-24 | 罗政宏 | Hot water circulation heat exchanger |
| CN201957726U (en) * | 2010-12-28 | 2011-09-07 | 塔里木大学 | Novel solar humidity-maintained drying equipment |
| JP2011239691A (en) * | 2010-05-14 | 2011-12-01 | Satake Corp | Ventilation dryer for vegetable or the like |
| US20120247453A1 (en) * | 2011-03-30 | 2012-10-04 | National Cheng Kung University | Dehydration device |
| CN203353638U (en) * | 2013-03-25 | 2013-12-25 | 德州炬创换热器制造有限公司 | Water medium circulating system drying device |
-
2013
- 2013-07-10 CN CN201310287160.4A patent/CN103385530B/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011239691A (en) * | 2010-05-14 | 2011-12-01 | Satake Corp | Ventilation dryer for vegetable or the like |
| CN201774938U (en) * | 2010-08-18 | 2011-03-30 | 甘肃省机械科学研究院 | Fruit and vegetable drying system adopting combined heat sources of solar energy and heat pump |
| CN101946968A (en) * | 2010-08-26 | 2011-01-19 | 王宁州 | Multifunctional dryer |
| CN201957726U (en) * | 2010-12-28 | 2011-09-07 | 塔里木大学 | Novel solar humidity-maintained drying equipment |
| CN201945154U (en) * | 2011-01-07 | 2011-08-24 | 罗政宏 | Hot water circulation heat exchanger |
| US20120247453A1 (en) * | 2011-03-30 | 2012-10-04 | National Cheng Kung University | Dehydration device |
| CN203353638U (en) * | 2013-03-25 | 2013-12-25 | 德州炬创换热器制造有限公司 | Water medium circulating system drying device |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105495651A (en) * | 2015-12-17 | 2016-04-20 | 江苏杰英能源科技有限公司 | Waste heat recovery mechanism of vegetable dehydration device |
| CN108131956A (en) * | 2017-12-29 | 2018-06-08 | 焱鑫环保科技有限公司 | A kind of method for subtracting furnace charge briquetting moisture and auto feed using the baking of blast furnace shaft water jacket circulating hot water |
| CN108317842A (en) * | 2018-02-07 | 2018-07-24 | 安徽江淮汽车集团股份有限公司 | Coating lifting drying system |
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| CN103385530B (en) | 2016-12-28 |
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Inventor after: Liu Wenyu Inventor after: Ma Xudong Inventor after: Wang Ning Inventor before: Wang Ning |
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