CN204100823U - Equitemperature heat exchanger tube radiation type electric heater - Google Patents
Equitemperature heat exchanger tube radiation type electric heater Download PDFInfo
- Publication number
- CN204100823U CN204100823U CN201420588603.3U CN201420588603U CN204100823U CN 204100823 U CN204100823 U CN 204100823U CN 201420588603 U CN201420588603 U CN 201420588603U CN 204100823 U CN204100823 U CN 204100823U
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- China
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- heat exchanger
- exchanger tube
- heater
- equitemperature
- type electric
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Abstract
The utility model relates to industrial process electric-heating technology field, especially a kind of radiation type electric heater.Comprise body of heater, described body of heater shell one end is provided with anti-explosion terminal box, the heat exchanger tube of surperficial isothermal is provided with in described body of heater, the inboard wall of furnace body of described heat exchanger tube both sides is provided with some electrical heating elements, described heat exchanger tube surface is provided with temperature sensor, described heat exchanger tube is snakelikely be arranged in body of heater, and the inlet of described heat exchanger tube and liquid outlet are positioned at same one end of body of heater.Described electrical heating elements is divided into several regions and arranges, and power reduces from the inlet of heat exchanger tube successively to liquid outlet direction, and this aspect can reduce the length of heat exchanger tube, reduces material cost; Simultaneously can improve heat exchanger efficiency, extend heater service life.
Description
Technical field
The utility model relates to industrial process electric-heating technology field, especially a kind of radiation type electric heater.
Background technology
Existing industrial radiant electric heater often adopts body of heater, is arranged on the heating in body of heater and is used for forming with the heat exchange coil of process fluid heat exchange; Heat exchange coil often adopt helical structure or upper lower burrs around serpentine configuration, the major defect of this structure is:
1, have employed a large amount of heat exchanger tubes, the cost of heat exchanger tube will account for the 60-70% of whole device, and material cost is very high;
2, heat exchange tube structure often adopts the mode of coiling or welding processing, and processing and manufacturing cost is also very high;
3, heat exchange tube wall temperature is high, have impact on the service life of heat exchanger tube.
4, heat exchanger tube adopts the mode that one side is heated, and is heated uneven.
5, in pipe, hydrops is not easy blowdown.
6, volume is very large, and external hear rate is high, and the thermal efficiency is low.
7, Heavy Weight, volume is large, adds cost of transportation.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of equitemperature heat exchanger tube radiation type electric heater, can reduce heat exchanger tube length, reduces difficulty of processing, saves manufacturing cost.
In order to solve the problems of the technologies described above, the utility model comprises body of heater, described body of heater shell one end is provided with anti-explosion terminal box, the heat exchanger tube of surperficial isothermal is provided with in described body of heater, the inboard wall of furnace body of described heat exchanger tube both sides is provided with some electrical heating elements, described heat exchanger tube surface is provided with temperature sensor, and described heat exchanger tube is snakelikely be arranged in body of heater, and the inlet of described heat exchanger tube and liquid outlet are positioned at same one end of body of heater.
Described electrical heating elements is divided into several regions and arranges, and power reduces from the inlet of heat exchanger tube successively to liquid outlet direction.Described heat exchanger tube is made up of some straight tubes and bridge piece.
Described body of heater be provided with nitrogen inlet and breathe valve port, in described body of heater, being filled with nitrogen.
Also be provided with the guide rail for supporting heat exchanger tube and grip block in described body of heater, described heat exchanger tube to be positioned on guide rail and to be slidably connected, and described grip block is positioned at the both sides of heat exchanger tube.
Described heat exchanger tube is provided with sewage draining exit.
Advantageous Effects of the present utility model is:
1, by the inlet of the power of electrical heating elements from heat exchanger tube is reduced successively to liquid outlet direction, the length of heat exchanger tube can be reduced, reduce material cost;
2, heat exchanger tube is made up of straight tube and bridge piece, simplifies the procedure of processing of heat exchanger tube, reduces processing cost.
3, all heat exchanger tubes are positioned at opposing parallel some planes, add the heating surface area of heat exchanger tube, have effect that is energy-conservation and the prolongation heat exchanger tube life-span.
4, due to the minimizing of heat exchange tube material, decrease the thermal starting time of system, that is, than traditional scheme, there is very fast time arrival operating temperature.
5, volume is compared with traditional simultaneously, and volume is less, and external energy consumption reduces, and improves the thermal efficiency of system.
6, the setting of guide rail and grip block, heat exchanger tube is easy to put into and take out, and is convenient to the maintenance of heat exchanger tube and the maintenance of heating.
Accompanying drawing explanation
Fig. 1 is front section view of the present utility model;
Fig. 2 is top plan view of the present utility model;
Fig. 3 is side sectional view of the present utility model;
Fig. 4 is the relation schematic diagram of conventional heater heat exchanger tube length and tube wall temperature;
Fig. 5 is the relation schematic diagram of heater heat exchanger tube length described in the utility model and tube wall temperature.
Detailed description of the invention
Embodiment cited by the utility model; just understand the utility model for helping; should not be construed as the restriction to the utility model protection domain; for those skilled in the art; under the prerequisite not departing from the utility model thought; can also improve the utility model and modify, these improve and modification also falls in the scope of the utility model claim protection.
As shown in Figure 1, Figure 2 and Figure 3, the utility model comprises body of heater 1, and described body of heater 1 shell one end is provided with anti-explosion terminal box 8, and two chambers are arranged in described body of heater 1 inside, certainly also can be arranged to multiple chamber as required.Be provided with the heat exchanger tube 3 be interconnected in described chamber, the inboard wall of furnace body of described heat exchanger tube 3 both sides is provided with some electrical heating elements 6.
Traditional heat exchanger tube is spirality, and therefore electrical heating elements 6 is heated for one side, and such heating surface area is little, have impact on heating effect.Heat exchanger tube 3 described in the utility model is in the snakelike chamber being arranged in body of heater 1, and the inlet 31 of heat exchanger tube 3 and liquid outlet 32 are positioned at same one end of body of heater 1, there is electrical heating elements 6 both sides of such heat exchanger tube 3, heat exchanger tube 3 heats by the electrical heating elements 6 of both sides, adds the heating surface area between heat exchanger tube 3 and electrical heating elements 6.
In order to improve the heat insulation effect of body of heater 1, the inner surface of described body of heater 1 can also arrange heat-insulation layer 2, and electrical heating elements 6 is arranged on heat-insulation layer.Described body of heater 1 be also provided with nitrogen inlet 41 and breathe valve port 42, in described body of heater, being filled with nitrogen, and making to keep micro-positive air pressure in body of heater 1.
In order to reduce heat exchanger tube length, and reach energy-conservation object, described electrical heating elements 6 is divided into several regions and arranges, the power of described electrical heating elements 6 reduces from the inlet 31 of heat exchanger tube 3 successively to liquid outlet 32 direction, described heat exchanger tube 3 surface is provided with temperature sensor 7, and described heat exchanger tube 3 surface temperature carries out equitemperature control by temperature sensor 7.
Heat exchanger tube 3 described in the utility model is made up of the bridge piece 34 of some straight tubes 33 and standard, and need the procedure of processing of whole heat exchanger tube bending when eliminating original processing spiral heat exchange tube, processing is than being easier to like this, reduces processing cost.
In heat exchanger tube 3, foreign material precipitation, described heat exchanger tube 3 is provided with sewage draining exit 35, is drained by the foreign material in heat exchanger tube 3 for regular.
In order to support and be convenient to change heat exchanger tube 3, be also provided with guide rail 51 and grip block 52 in described body of heater 1, described heat exchanger tube 3 to be positioned on guide rail 51 and to be slidably connected, and described grip block 52 is positioned at the both sides of heat exchanger tube 3.Such heat exchanger tube can be extracted out by guide rail, is also convenient to the maintenance to the maintenance of electrical heating elements in stove 6 and exchange heat pipe 3.
Introduce the principle that the utility model can reduce heat exchanger tube length below.
As everyone knows, traditional radiative process electric heater, the surface temperature of heat exchanger tube exceeds about 100 DEG C than medium temperature in pipe usually, such as medium temperature is heated to 550 DEG C from 160 DEG C, the surface temperature of heat exchanger tube is now respectively 260 DEG C to 650 DEG C, real heat exchange mean temperature difference only 100 DEG C from the importer of fluid to the temperature of the Way out to fluid, we are at the classical formulas of fluid heat transfer as everybody knows: Q=α A (T
tube wall-T
fluid), wherein α is the coefficient of heat transfer, relevant with the physical property of fluid and flow velocity, A is heat exchanger tube heat exchange area, T
tube wallthe surface temperature of heat exchanger tube, T
fluidit is the temperature of fluid, but when adopting the utility model, the direction of flowing along fluid due to the power division of electrical heating elements is distributed from high to low, and control to make fluid in heating process by the temperature sensor on heat exchanger tube surface, the temperature on heat exchanger tube surface can remain certain temperature from the beginning to the end, such as 650 DEG C, at this moment the MTD of heat exchanger tube and fluid is 650-(160+550)/2=295 DEG C, according to above-mentioned classical formulas, identical heat exchange amount Q, heat exchange area can drop to close to former heat exchange area 1/3, the length of heat exchanger tube can be reduced to original 1/3 like this, the material cost of heat exchanger tube can reduce by 2/3.
Certainly, the principle that the utility model can reduce heat exchanger tube length also can be found out from Fig. 4 and Fig. 5, wherein Fig. 4 is the relation schematic diagram of conventional heater heat exchanger tube length and tube wall temperature, and Fig. 5 is the relation schematic diagram of heater heat exchanger tube length described in the utility model and tube wall temperature.When heat exchanger tube 3 maximum surface temperature is identical, traditional heat exchanger tube length is obviously greater than heat exchanger tube length of the present utility model.
We not only can reduce manufacturing cost by reducing heat exchanger tube length like this, and, reaching in identical heat transfer effect situation, we also both can reduce the length of heat exchanger tube, the tube wall temperature of heat exchanger tube can be reduced again, so not only can be energy-conservation, and the life-span of heating tube can be extended.
Claims (6)
1. equitemperature heat exchanger tube radiation type electric heater, comprise body of heater (1), described body of heater (1) shell one end is provided with anti-explosion terminal box (8), the heat exchanger tube (3) of surperficial isothermal is provided with in described body of heater (1), it is characterized in that, the inboard wall of furnace body of described heat exchanger tube (3) both sides is provided with some electrical heating elements (6), described heat exchanger tube (3) surface is provided with temperature sensor (7), described heat exchanger tube (3) is arranged in body of heater (1) in snakelike, the inlet (31) of described heat exchanger tube (3) and liquid outlet (32) are positioned at same one end of body of heater (1).
2. equitemperature heat exchanger tube radiation type electric heater according to claim 1, is characterized in that, described electrical heating elements (6) is divided into several regions and arranges, and power reduces from the inlet (31) of heat exchanger tube (3) successively to liquid outlet (32) direction.
3. equitemperature heat exchanger tube radiation type electric heater according to claim 1 and 2, is characterized in that, described heat exchanger tube (3) is made up of some straight tubes (33) and bridge piece (34).
4. equitemperature heat exchanger tube radiation type electric heater according to claim 3, is characterized in that described body of heater (1) being provided with nitrogen inlet (41) and breathing valve port (42), is filled with nitrogen in described body of heater.
5. equitemperature heat exchanger tube radiation type electric heater according to claim 4, it is characterized in that, the guide rail (51) for supporting heat exchanger tube and grip block (52) is also provided with in described body of heater (1), described heat exchanger tube (3) is positioned at guide rail (51) and goes up and be slidably connected, and described grip block (52) is positioned at the both sides of heat exchanger tube (3).
6. equitemperature heat exchanger tube radiation type electric heater according to claim 5, is characterized in that, described heat exchanger tube (3) is provided with sewage draining exit (35).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420588603.3U CN204100823U (en) | 2014-10-11 | 2014-10-11 | Equitemperature heat exchanger tube radiation type electric heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420588603.3U CN204100823U (en) | 2014-10-11 | 2014-10-11 | Equitemperature heat exchanger tube radiation type electric heater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204100823U true CN204100823U (en) | 2015-01-14 |
Family
ID=52269243
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420588603.3U Withdrawn - After Issue CN204100823U (en) | 2014-10-11 | 2014-10-11 | Equitemperature heat exchanger tube radiation type electric heater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204100823U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104266493A (en) * | 2014-10-11 | 2015-01-07 | 华能无锡电热器材有限公司 | Radiant electric heater with isothermal heat exchange pipe |
| CN104791987A (en) * | 2015-05-08 | 2015-07-22 | 华能无锡电热器材有限公司 | Low-flow equal-temperature field electric heater |
-
2014
- 2014-10-11 CN CN201420588603.3U patent/CN204100823U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104266493A (en) * | 2014-10-11 | 2015-01-07 | 华能无锡电热器材有限公司 | Radiant electric heater with isothermal heat exchange pipe |
| CN104266493B (en) * | 2014-10-11 | 2016-05-18 | 华能无锡电热器材有限公司 | Equitemperature heat exchanger tube radiation type electric heater |
| CN104791987A (en) * | 2015-05-08 | 2015-07-22 | 华能无锡电热器材有限公司 | Low-flow equal-temperature field electric heater |
| CN104791987B (en) * | 2015-05-08 | 2017-09-19 | 华能无锡电热器材有限公司 | Low discharge equitemperature electric heater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150114 Effective date of abandoning: 20160518 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |