CN201983448U - High-temperature section heat exchanger - Google Patents

High-temperature section heat exchanger Download PDF

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Publication number
CN201983448U
CN201983448U CN2011200565757U CN201120056575U CN201983448U CN 201983448 U CN201983448 U CN 201983448U CN 2011200565757 U CN2011200565757 U CN 2011200565757U CN 201120056575 U CN201120056575 U CN 201120056575U CN 201983448 U CN201983448 U CN 201983448U
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CN
China
Prior art keywords
heat exchanger
temperature section
flue gas
fin
main heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN2011200565757U
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Chinese (zh)
Inventor
叶远璋
代先锋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Vanward New Electric Co Ltd
Original Assignee
Guangdong Vanward New Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Application filed by Guangdong Vanward New Electric Co Ltd filed Critical Guangdong Vanward New Electric Co Ltd
Priority to CN2011200565757U priority Critical patent/CN201983448U/en
Application granted granted Critical
Publication of CN201983448U publication Critical patent/CN201983448U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

A high-temperature section heat exchanger includes a main heat exchanger and a water tank casing; the main heat exchanger includes tube bundles and fins and is fixed above a combustor; the main technical characteristic is that the high-temperature section heat exchanger further includes an auxiliary heat exchanger and a smoke spoiler; the auxiliary heat exchanger includes tube bundles and fins; the tube bundles of the main heat exchanger are arranged in one layer, so are the tube bundles of the auxiliary heat exchanger; the smoke spoiler is fixed on the inner wall of the water tank casing and placed above the main heat exchanger; and the auxiliary heat exchanger is fixed above the smoke spoiler, and can effectively enhance convective heat exchange and improve heat exchange performance, therefore, a gas water heater under the same rated heat load can use fewer fins, the length of the heat exchanger can be shortened, the copper consumption is reduced, and the cost of the gas water heater is lowered.

Description

The high temperature section heat exchanger
Technical field: the utility model relates to the high temperature section heat exchanger in a kind of gas heater.
Background technology: the heat exchanger major part of existing big flow gas heater is to adopt the copper material of two-layer tube bank, but the copper resource rare resource that is China, and international copper valency rises steadily, price occupies highly, and this causes the cost of water heater too high.For overcoming these defectives, the high temperature section heat exchanger in the gas heater is improved.
Summary of the invention: technical problem to be solved in the utility model be to provide a kind of in big flow gas heater the heat exchanger of enhanced heat exchange, it can satisfy on the basis of performance requirement, improve heat exchange property effectively, make gas heater under identical rated heat input, rated heat load, reduce the usage quantity of fin, shortening heat interchanger length, thereby the use of minimizing copper, the cost of reduction gas heater.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of high temperature section heat exchanger, it comprises main heat exchanger, tank shell, main heat exchanger contains tube bank and fin, and be fixed on the burner top, it is characterized in that it also comprises supplementary heat exchanger, flue gas spoiler, described supplementary heat exchanger contains tube bank and fin, the tube bank of main heat exchanger and supplementary heat exchanger is one deck tube bank, the flue gas spoiler is fixed on the tank shell inwall and is positioned at the top of main heat exchanger, and supplementary heat exchanger is fixed on flue gas spoiler top.
The length of the fin gas approach end of described supplementary heat exchanger is than the long 0.5-10mm of length of the fin gas approach end of main heat exchanger.
The length of the fin gas approach end of described supplementary heat exchanger is than the long 2-5mm of length of the fin gas approach end of main heat exchanger.
The fin transversion malposition of the fin of described main heat exchanger and supplementary heat exchanger is arranged.
Described main heat exchanger, supplementary heat exchanger are welded by copper or aluminium alloy or stainless steel material.
Described main heat exchanger be installed in burner directly over, the flue gas spoiler be installed in main heat exchanger directly over, supplementary heat exchanger be installed in the flue gas spoiler directly over.
The plates that described flue gas spoiler is made by stainless steel material are welded, and are fixed on the tank shell inwall by welding or riveted joint or screw.
The utility model is compared the beneficial effect that is produced with background technology:
Because adopting, the utility model is divided into two independently heat exchangers by original two-layer tube bank at the high temperature section heat exchanger, put into the flue gas spoiler in the centre, change the angle that the velocity of flue gas field enters supplementary heat exchanger, make velocity field vertical with thermoisopleth, improve flue gas heat exchange in the velocity field of supplementary heat exchanger and the overall coordination degree in temperature field, thereby heat convection is strengthened, improve heat exchange property, make gas heater under identical rated heat input, rated heat load, reduce the quantity of fin, shortening heat interchanger length reduces the use of copper, reduces the cost of gas heater.
Description of drawings: Fig. 1 is a structural representation of the present utility model.
Fig. 2 looks schematic diagram for structure master of the present utility model.
Fig. 3 looks schematic diagram for a structure of the present utility model left side.
Fig. 4 is a syndeton schematic diagram of the present utility model.
Fig. 5 is the structure for amplifying schematic diagram at the utility model heat exchanger place.
The specific embodiment:
Shown in accompanying drawing 1, accompanying drawing 2, present embodiment comprises shell 1, first magnetic valve 2, second magnetic valve 3, burner assembly 4, main heat exchanger 5, flue gas spoiler 6, supplementary heat exchanger 7, exhaust fume collecting hood assembly 8, pulse igniter 9, blast switch 10, Switching Power Supply 11, blower fan assembly 12, controller 13, tank shell 14.Main heat exchanger 5 adopts one deck tube bank, be installed in directly over the burner 4, flue gas spoiler 6 is made by exotic material, as stainless steel material, is installed in directly over the main heat exchanger 5, flue gas spoiler 6 is fixed in the tank shell 14, supplementary heat exchanger 7 adopts one deck tube bank, is installed in directly over the flue gas spoiler 6, and high-temperature flue gas enters supplementary heat exchanger 7 through main heat exchanger 5 and flue gas spoiler 6, exhaust fume collecting hood assembly 8 is installed in supplementary heat exchanger 7 tops, and flue gas is outside exhaust fume collecting hood assembly 8 discharge machines.
The principle of described high temperature section heat exchanger: shown in accompanying drawing 1, accompanying drawing 2, accompanying drawing 3, accompanying drawing 4 and accompanying drawing 5, water heater normally starts, 12 work of blower fan assembly, controller 13 control impuls igniters 9 discharge ignitings, magnetic valve 2, magnetic valve 3 are opened simultaneously, and combustion gas enters the fire row burning of burner assembly 4 through each nozzle.High-temperature flue gas through flue gas spoiler 6, makes velocity field vertical with thermoisopleth after flowing out through main heat exchanger 5 heat exchange, improves flue gas heat exchange in the velocity field of supplementary heat exchanger 7 and the overall coordination degree in temperature field, thereby heat convection is strengthened.By prolonging the fin 71 gas approach end length (being D1) of supplementary heat exchanger 7, the length (being D1) of fin 71 gas approach ends that makes supplementary heat exchanger 7 is than the long 0.5-10mm of length (being D2) of the fin 51 gas approach ends of main heat exchanger 5, as 2mm, 5mm, 8mm, the area that makes the flue gas front wash away heat exchanger increases, hot-fluid is higher, thereby heat convection is strengthened.By the fin 51 of main heat exchanger 5 is arranged with fin 71 transversion malpositions of supplementary heat exchanger 7, the flue gas that flows out main heat exchanger 5 is divided right and left laterally to stream, thereby heat convection is strengthened, improve heat exchange property, make gas heater under identical rated heat input, rated heat load, reduce the usage quantity of fin, shortening heat interchanger length, reduce the use of copper, reduce the cost of gas heater.

Claims (10)

1. high temperature section heat exchanger, it comprises main heat exchanger (5), tank shell (14), main heat exchanger (5) contains tube bank and fin (51), and be fixed on burner (4) top, it is characterized in that it also comprises supplementary heat exchanger (7), flue gas spoiler (6), described supplementary heat exchanger (7) contains tube bank and fin (71), the tube bank of main heat exchanger (5) and supplementary heat exchanger (7) is one deck tube bank, flue gas spoiler (6) is fixed on tank shell (14) inwall and is positioned at the top of main heat exchanger (5), and supplementary heat exchanger (7) is fixed on flue gas spoiler (6) top.
2. high temperature section heat exchanger according to claim 1, the length of fin (71) gas approach end that it is characterized in that described supplementary heat exchanger (7) is than the long 0.5-10mm of length of fin (51) the gas approach end of main heat exchanger (5).
3. high temperature section heat exchanger according to claim 1 and 2, the length of fin (71) gas approach end that it is characterized in that described supplementary heat exchanger (7) is than the long 2-5mm of length of fin (51) the gas approach end of main heat exchanger (5).
4. high temperature section heat exchanger according to claim 1 and 2 is characterized in that fin (71) the transversion malposition arrangement of fin (51) with the supplementary heat exchanger (7) of described main heat exchanger (5).
5. high temperature section heat exchanger according to claim 1 and 2 is characterized in that described main heat exchanger (5), supplementary heat exchanger (7) are welded by copper or aluminium alloy or stainless steel material.
6. high temperature section heat exchanger according to claim 4 is characterized in that described main heat exchanger (5), supplementary heat exchanger (7) are welded by copper or aluminium alloy or stainless steel material.
7. high temperature section heat exchanger according to claim 1 and 2, it is characterized in that described main heat exchanger (5) be installed in burner (4) directly over, flue gas spoiler (6) be installed in main heat exchanger (5) directly over, supplementary heat exchanger (7) be installed in flue gas spoiler (6) directly over.
8. high temperature section heat exchanger according to claim 6, it is characterized in that described main heat exchanger (5) be installed in burner (4) directly over, flue gas spoiler (6) be installed in main heat exchanger (5) directly over, supplementary heat exchanger (7) be installed in flue gas spoiler (6) directly over.
9. high temperature section heat exchanger according to claim 1 and 2 is characterized in that the plates that described flue gas spoiler (6) is made by stainless steel material are welded, and is fixed on tank shell (14) inwall by welding or riveted joint or screw.
10. high temperature section heat exchanger according to claim 8 is characterized in that the plates that described flue gas spoiler (6) is made by stainless steel material are welded, and is fixed on tank shell (14) inwall by welding or riveted joint or screw.
CN2011200565757U 2011-03-03 2011-03-03 High-temperature section heat exchanger Expired - Lifetime CN201983448U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011200565757U CN201983448U (en) 2011-03-03 2011-03-03 High-temperature section heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011200565757U CN201983448U (en) 2011-03-03 2011-03-03 High-temperature section heat exchanger

Publications (1)

Publication Number Publication Date
CN201983448U true CN201983448U (en) 2011-09-21

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011200565757U Expired - Lifetime CN201983448U (en) 2011-03-03 2011-03-03 High-temperature section heat exchanger

Country Status (1)

Country Link
CN (1) CN201983448U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107328263A (en) * 2017-05-25 2017-11-07 广东顺德巴林电器制造有限公司 A kind of efficient energy-saving gas thermoconverter

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107328263A (en) * 2017-05-25 2017-11-07 广东顺德巴林电器制造有限公司 A kind of efficient energy-saving gas thermoconverter

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Granted publication date: 20110921