CN202660739U - Efficient coiler type oil-water heat exchanging evaporator - Google Patents
Efficient coiler type oil-water heat exchanging evaporator Download PDFInfo
- Publication number
- CN202660739U CN202660739U CN 201220137237 CN201220137237U CN202660739U CN 202660739 U CN202660739 U CN 202660739U CN 201220137237 CN201220137237 CN 201220137237 CN 201220137237 U CN201220137237 U CN 201220137237U CN 202660739 U CN202660739 U CN 202660739U
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- cylindrical shell
- heat exchanging
- coil
- water heat
- type oil
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- Expired - Fee Related
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Abstract
The utility model discloses an efficient coiler type oil-water heat exchanging evaporator. Double coilers are composed of an inner-layer spiral coiler and an outer-layer spiral coiler, the double coilers are arranged in a vertical tube body, inlets and outlets of the inner-layer spiral coiler and the outer-layer spiral coiler are connected with a heat conducting oil pipe, and the bottom of the tube body is connected with a water supplying device. The efficient coiler type oil-water heat exchanging evaporator is simple in structure, high in heat exchanging efficiency and convenient to install and maintain.
Description
Technical field
The utility model relates to a kind of heat exchanger, especially relates to a kind of efficient coiled oil water heat exchange evaporimeter.
Background technology
Organic heat carrier furnace is that a kind of novel special boiler claims again heat-conducting oil furnace, has the operating characteristic of low pressure, high temperature, and its heat supply temperature can reach 400 ℃ of 340 ℃ of liquid phases or vapour phases.Every needs heat uniformly and stably, and do not allow flame direct-fired, can adopt the organic heat carrier furnace heat supply in the various production occasions of technique heating-up temperature between 150 ℃-380 ℃.At present, the evaporimeter that organic heat carrier furnace is equipped with is generally the single coil structure, and heat exchange efficiency is lower.
Summary of the invention
The purpose of this utility model is: a kind of simple in structure, efficient coiled oil water heat exchange evaporimeter that heat exchange efficiency is high is provided.
The technical solution of the utility model is: comprise cylindrical shell and coil pipe, coil pipe is the dual coil pipes that the ectonexine spiral coil forms, dual coil pipes is arranged on upright inner barrel, water-level gauge and safety valve are equipped with in cylindrical shell top, the cylindrical shell crown center is equipped with the manhole device, blowoff valve is equipped with in the cylindrical shell bottom, and the import and export of ectonexine spiral coil are connected with heat-conducting oil pipes, and cylinder body bottom connects water supply installation.
The beneficial effects of the utility model are: owing to taking the duplex coil structure, heat exchange area is large, and the coefficient of heat transfer is high, and heat exchange is abundant.Have safe and reliable, compact conformation, easy to installation and maintenance, simple to operate, the characteristics such as easy to use.The upper this evaporimeter of organic heat carrier furnace outfit not only can be the user high-temperature medium is provided, and can satisfy production, living needs for the user provides the steam that needs usefulness again simultaneously, has enlarged the use field.
Description of drawings
Fig. 1 is structural representation of the present utility model.
The specific embodiment
Can find out from structural representation of the present utility model shown in Figure 1, the utility model comprises the dual coil pipes that cylindrical shell 1 and internal layer spiral coil 3 and outer spiral coil 2 form, dual coil pipes is arranged on upright cylindrical shell 1 inside, water-level gauge 5 and safety valve 4 are equipped with in cylindrical shell 1 top, cylindrical shell 1 crown center is equipped with manhole device 6, blowoff valve 7 is equipped with in cylindrical shell 1 bottom, and the import and export of ectonexine spiral coil are connected with heat-conducting oil pipes.High temperature heat conductive oil is by hot oil pump or directly entered in the coil pipe by heat medium heater, and the water heating with 1 of coil pipe and cylindrical shell produces steam, and conduction oil is lowered the temperature, and comes back to heating furnace, makes it to recycle.Cylindrical shell 1 bottom connects water supply installation, uses demineralized water, if through preheating then evaporation capacity can improve.Water enters evaporimeter from the bottom, and water heats under free convection and produces steam at heating surface, becomes unsaturated steam by under water orifice plate and Perforated plate, delivers to a minute drum, and production, gas for domestic use are provided.
The utility model can steam continuously or indirectly according to actual condition, but not the equipment of direct flame heating.Compact conformation, safe and reliable, easy to installation and maintenance, simple to operate, easy to use.
Claims (1)
1. efficient coiled oil water heat exchange evaporimeter, comprise cylindrical shell (1) and coil pipe, it is characterized in that: described coil pipe is the dual coil pipes that internal layer spiral coil (3) and outer spiral coil (2) form, dual coil pipes is arranged on upright cylindrical shell (1) inside, water-level gauge (5) and safety valve (4) are equipped with in cylindrical shell (1) top, cylindrical shell (1) crown center is equipped with manhole device (6), blowoff valve (7) is equipped with in the cylindrical shell bottom, the import and export of ectonexine spiral coil are connected with heat-conducting oil pipes, and cylindrical shell (1) bottom connects water supply installation.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220137237 CN202660739U (en) | 2012-04-03 | 2012-04-03 | Efficient coiler type oil-water heat exchanging evaporator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220137237 CN202660739U (en) | 2012-04-03 | 2012-04-03 | Efficient coiler type oil-water heat exchanging evaporator |
Publications (1)
Publication Number | Publication Date |
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CN202660739U true CN202660739U (en) | 2013-01-09 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220137237 Expired - Fee Related CN202660739U (en) | 2012-04-03 | 2012-04-03 | Efficient coiler type oil-water heat exchanging evaporator |
Country Status (1)
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CN (1) | CN202660739U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106288391A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, steam |
CN106288390A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, hot water and steam |
CN106288386A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, hot water |
-
2012
- 2012-04-03 CN CN 201220137237 patent/CN202660739U/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106288391A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, steam |
CN106288390A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, hot water and steam |
CN106288386A (en) * | 2016-08-12 | 2017-01-04 | 厦门引导热能科技有限公司 | A kind of method supplying deep fat, hot water |
CN106288391B (en) * | 2016-08-12 | 2019-02-26 | 厦门引导热能科技有限公司 | A method of supply hot oil, steam |
CN106288386B (en) * | 2016-08-12 | 2019-02-26 | 厦门引导热能科技有限公司 | A method of supply hot oil, hot water |
CN106288390B (en) * | 2016-08-12 | 2019-02-26 | 厦门引导热能科技有限公司 | A method of supply hot oil, hot water and steam |
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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: 20130109 Termination date: 20170403 |
|
CF01 | Termination of patent right due to non-payment of annual fee |