CN100412461C - Heat exchanger for fuel oil heater with heat exchange pipe - Google Patents

Heat exchanger for fuel oil heater with heat exchange pipe Download PDF

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Publication number
CN100412461C
CN100412461C CNB2006100689611A CN200610068961A CN100412461C CN 100412461 C CN100412461 C CN 100412461C CN B2006100689611 A CNB2006100689611 A CN B2006100689611A CN 200610068961 A CN200610068961 A CN 200610068961A CN 100412461 C CN100412461 C CN 100412461C
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China
Prior art keywords
heat exchanger
exchanger tube
dividing plate
heat exchanging
base plate
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Expired - Fee Related
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CNB2006100689611A
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Chinese (zh)
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CN1928454A (en
Inventor
毛华永
李国祥
王伟
白书战
潘世艳
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Shandong University
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Shandong University
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Publication of CN100412461C publication Critical patent/CN100412461C/en
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Abstract

The invention provides a heat exchanging equipment for fuel oil heater with heat exchanging pipe, comprising heat exchanging body, heat-conducting plate, shell, heat exchanging pipe, insulation board and helical guiding plate. Heat-conducting plate is distributed on the inside wall of heat exchanging body and helical guiding plate is set on the outside wall of heat exchanging body; the bottom of heat exchanging body is sealed by board and heat exchanging pipe is set on the board; shell is mounted on the heat exchanging body and helical guiding plate is set between them; the frontal end of shell is connected with heat exchanging body together and there is a plug at the back end; helical water cavity is formed by helical guiding plate between heat exchanging body and shell, heat exchanging pipe is connected to the end of helical water cavity in series; insulation board is set between plug and board; inlet and outlet pipes are set at two ends of shell respectively. The heat exchanging pipe can improve heat exchanging area and strengthen heat exchanging so that heat efficiency of heater is improved in the invention. Heat efficiency of fuel oil heater can improve more than 8% and bigger transporting declared power is gained in the invention.

Description

A kind of heat exchanger for fuel oil heater with heat exchanger tube
Technical field
The present invention relates to the heat exchanger that the liquid-type fuel heater is used, belong to the fuel heater technical field.
Background technology
Fuel heater is as a kind of independently heating plant, has been widely used in that various conveying mechanicals such as automobile, boats and ships are warmed oneself and engine prewarming etc. under low temperature environment.As the heat exchanger of fuel heater critical component, the height of its heat exchange efficiency has great influence to heat efficiency of heater and other performance.Most liquid type fuel heater adopts spiral water cavity to carry out heat exchange at present.Because of the heat exchange area of such heat exchanger is restricted,, promptly under same energy consumption, can not obtain the sufficiently high thermal efficiency so thermal loss is still bigger than normal.Particularly, when fuel heater is installed in high size-constrained vehicle of length and width or device as a subsystem, provide a kind of thermal power volume ratio higher fuel heater, just seem particularly important.
Summary of the invention
The present invention is directed to the existing deficiency of heat exchanger of existing fuel heater, the heat exchanger for fuel oil heater of the higher band heat exchanger tube of a kind of heat exchange efficiency is provided.This kind heat exchanger is remarkable energy savings not only, and can satisfy the equipment that is heated that installing space is little, the thermal power demand is high.
The heat exchanger for fuel oil heater of band heat exchanger tube of the present invention adopts following technical solution:
The heat exchanger for fuel oil heater of band heat exchanger tube comprises heat exchanger, heat transfer sheet, shell, heat exchanger tube, dividing plate, water inlet pipe, outlet pipe and helical form flow deflector; The heat exchanger inwall is distributed with heat transfer sheet, and outer wall is provided with the helical form flow deflector; The heat exchanger bottom seals by base plate; Heat exchanger tube is installed on the base plate; Outer cover suit is on heat exchanger, and the helical form flow deflector is wrapped between the two, the front end and the heat exchanger of shell link together, and the rear end is provided with plug, form spiral water cavity by the helical form flow deflector between heat exchanger and the shell, heat exchanger tube is series at the end of spiral water cavity; Be provided with dividing plate between plug and the base plate, be used for the entery and delivery port of heat exchanger tube is separated; One end of shell is provided with water inlet pipe, and the other end is provided with outlet pipe.
The cross sectional shape of helical form flow deflector is rectangle, triangle, one of trapezoidal, circular.
Heat exchanger tube has three kinds of installation forms:
1. heat exchanger tube is the U type, each heat exchanger tube is along base plate center radial arrangement, the inlet end of all heat exchanger tubes is positioned at the inboard and formed water inlet cavity of base plate of dividing plate, and the water outlet end of all heat exchanger tubes is positioned at the dividing plate outside, base plate and the formed water chamber of plug.
2. heat exchanger tube is the U type, and each heat exchanger tube is along being installed on the base plate with the baseplate vertical direction spaced and parallel, and the inlet end of all heat exchanger tubes is positioned at the intake antrum of dividing plate below, and the water outlet end of all heat exchanger tubes is positioned at the water chamber of dividing plate top.
3. heat exchanger tube shape in the shape of a spiral, its inlet end is positioned at the center of base plate, and is in the intake antrum of dividing plate below, and the water outlet end of all heat exchanger tubes then is positioned at the water chamber of dividing plate top.
When heat exchanger tube influences discharge, can on dividing plate, offer by-pass prot.
The heat exchanger tube that is provided with in the heat exchanger of the present invention is arranged in the burner flame tube, and this one side can increase the heat exchange area of heater, fully absorbs the heat energy of high-temperature fuel gas, improves the thermal efficiency of heater integral body; On the other hand, because heat exchanger tube directly contacts with combustion flame, can in pipe, produce foam boiling, thereby enhanced heat exchange significantly improves the thermal efficiency.In addition, such layout also can make low-temperature circulating water in the initial start stage heater obtain the heat energy of high-temperature fuel gas rapidly, shortens the recirculated water temperature rise time of heater, makes heater faster to engine prewarming, and is rapider.The present invention also has a significant advantage to be, only need corresponding transformation is carried out in the heat exchanger bottom of existing heater, the double effects that just can realize improving the thermal efficiency and shorten preheating time, and the appearance and size that has kept former having heaters can reduce greatly like this and produce and the technological transformation cost.The present invention can make the thermal efficiency of fuel heater improve more than 8%.Because the raising of the thermal efficiency, under the constant situation of the appearance and size of heater, can obtain bigger output nominal power.
Description of drawings
Fig. 1 is the structural representation of first embodiment of the present invention.
Fig. 2 is a set of heat exchange tubes left view among first embodiment.
Fig. 3 is the structural representation of second embodiment of the present invention.
Fig. 4 is a set of heat exchange tubes left view among second embodiment.
The structural representation of Fig. 5 the 3rd embodiment of the present invention.
Fig. 6 is a set of heat exchange tubes left view among the 3rd embodiment.
Among the figure, 1, shell, 2, spiral water cavity, 3, the helical form flow deflector, 4, heat exchanger, 5, heat transfer sheet, 6, outlet pipe, 7, plug, 8, base plate, 9, heat exchanger tube, 10, dividing plate, 11, the burner flame tube, 12, blast pipe, 13, water inlet pipe, 14, by-pass prot.
The specific embodiment
Embodiment 1
Fig. 1 has provided the structure of present embodiment, comprises heat exchanger 4, heat transfer sheet 5, spiral flow deflector 3, base plate 8, heat exchanger shell 1, water inlet pipe 13, outlet pipe 6, plug 7, dividing plate 10 and heat exchanger tube 9.The inwall of heat exchanger 4 is welded with the heat transfer sheet 5 that distributes along circumferentially, and each heat transfer sheet welds vertically.The outer wall of heat exchanger 4 is welded with helical form flow deflector 3, and the cross section of helical form flow deflector 3 can be rectangle, triangle, trapezoidal or circular.The bottom of heat exchanger 4 is welded with base plate 8, makes heat exchanger 4 sealings, and high-temperature fuel gas in the combustion chamber and recirculated water are isolated.Heat exchanger tube 9 is installed on the base plate 8, and is in the high-temperature fuel gas side.Shell 1 is sleeved on the outside of heat exchanger 4, and helical form flow deflector 3 is wrapped between shell 1 and the heat exchanger 4, forms spiral water cavity 2.The front end of the front end of shell 1 and heat exchanger 4 welds together, and its rear end is welded with plug 7, and the front and back end of shell 1 is sealed up.Dividing plate 10 is fixed between plug 7 and the base plate 8, is used for the going out of heat exchanger tube 9, water inlet are separated.Water inlet pipe 13 and outlet pipe 6 lay respectively at the front-end and back-end of shell 1.
Heat exchanger tube 9 is the U type, and one group of heat exchanger tube that a plurality of heat exchanger tubes 9 are formed is series at the spiral water cavity end of heater, as shown in Figure 1.In the inside of burner flame tube 11, set of heat exchange tubes radially is installed in (referring to Fig. 2) on the base plate 8 around the center of burner inner liner.Dividing plate 10 and base plate 8 and plug 7 parallel installations, the inlet end of all heat exchanger tubes 9 are positioned at dividing plate 10 inboard and base plate 8 formed water inlet cavitys, and water outlet end is positioned at dividing plate 10 outsides, base plate 8 and plug 7 formed water outlet cavitys.
Embodiment 2
Fig. 3 has provided the structure of present embodiment, and the difference of present embodiment and embodiment 1 is that each heat exchanger tube 9 in the present embodiment adopts the end that is connected on the spiral water cavity in burner inner liner with certain spaced and parallel, and each heat exchanger tube is vertical with base plate 8, as shown in Figure 4.Dividing plate 10 is close to heat exchanger tube water inlet upper edge, joins with base plate 8 and plug 7, and the dividing plate top forms water cavity, and the below forms intake antrum.Dividing plate 10 can adopt straight plate level to arrange, also can adopt slightly high being in tilted layout of by-pass prot 14 ends, so that exhaust.
Embodiment 3
Fig. 5 has provided the structure of present embodiment, and the difference of present embodiment and embodiment 1 and embodiment 2 is that present embodiment adopts spiral helicine heat exchanger tube 9, shown in Fig. 5,6.The dead in line of its helix tube center and burner flame tube 11, inlet end is positioned at the center of base plate 8, and dividing plate 10 is close to heat exchanger tube water inlet upper edge and is connected to form into and out of water cavity with base plate 8 and plug 7.
In concrete the application, if the flame flow section of burner flame tube is certain, too much when heat exchanger tube, perhaps caliber is crossed and the high-temperature fuel gas flow resistance increased when thick, and back pressure raises, thereby influences the normal combustion of burner.Can suitably reduce the number of heat exchanger tube or dwindle heat exchange tube diameter this moment.The discharge of bringing therefrom reduces and can solve by open some by-pass prots 14 on dividing plate 10.But the number of by-pass prot and aperture thereof be control accurately, in order to avoid cause the serious short circuit of heat exchanger tube, the heat exchanger tube burning phenomenon occurs.
The course of work of the present invention is:
Start heater, after lighting a fire successfully, high-temperature fuel gas (shown in dotted arrow among Fig. 1, Fig. 3, Fig. 5) in the burner is turned back through the base plate 8 of heat exchanger of the present invention, by the circular passage of being made up of heat exchanger 4 internal faces and burner flame tube 11 outer surfaces, constantly heat release is after enter atmosphere by blast pipe 12.Recirculated water (shown in solid arrow among Fig. 1, Fig. 3, Fig. 5) after 2 heat absorptions of spiral water cavity, enters the heat exchanger tube 9 that is in the high-temperature fuel gas district by water inlet pipe 13, through after the high-intensity foam boiling heat exchange, is flowed out by outlet pipe 6, is vehicle or other device heat supply.

Claims (6)

1. the heat exchanger for fuel oil heater with heat exchanger tube comprises heat exchanger, heat transfer sheet, shell, heat exchanger tube, dividing plate, water inlet pipe, outlet pipe and helical form flow deflector; It is characterized in that: the heat exchanger inwall is distributed with heat transfer sheet, and outer wall is provided with the helical form flow deflector; The heat exchanger bottom seals by base plate; Heat exchanger tube is installed on the base plate; Outer cover suit is on heat exchanger, and the helical form flow deflector is wrapped between the two, the front end and the heat exchanger of shell link together, and the rear end is provided with plug, form spiral water cavity by the helical form flow deflector between heat exchanger and the shell, heat exchanger tube is series at the end of spiral water cavity; Be provided with dividing plate between plug and the base plate, be used for the entery and delivery port of heat exchanger tube is separated; One end of shell is provided with water inlet pipe, and the other end is provided with outlet pipe.
2. the heat exchanger for fuel oil heater of band heat exchanger tube according to claim 1 is characterized in that: the cross sectional shape of described helical form flow deflector is rectangle, triangle, one of trapezoidal, circular.
3. the heat exchanger for fuel oil heater of band heat exchanger tube according to claim 1, it is characterized in that: described heat exchanger tube is the U type, each heat exchanger tube is along base plate center radial arrangement, the inlet end of all heat exchanger tubes is positioned at the inboard and formed water inlet cavity of base plate of dividing plate, and the water outlet end of all heat exchanger tubes is positioned at the dividing plate outside, base plate and the formed water outlet cavity of plug.
4. the heat exchanger for fuel oil heater of band heat exchanger tube according to claim 1, it is characterized in that: described heat exchanger tube is the U type, each heat exchanger tube is along being installed on the base plate with the baseplate vertical direction spaced and parallel, the inlet end of all heat exchanger tubes is positioned at the intake antrum of dividing plate below, and the water outlet end of all heat exchanger tubes is positioned at the water chamber of dividing plate top.
5. the heat exchanger for fuel oil heater of band heat exchanger tube according to claim 1, it is characterized in that: described heat exchanger tube is shape in the shape of a spiral, its inlet end is positioned at the center of base plate, and is in the intake antrum of dividing plate below, and the water outlet end of all heat exchanger tubes then is positioned at the water chamber of dividing plate top.
6. according to claim 1 or 2 or 3 or the heat exchanger for fuel oil heater of 4 or 5 described band heat exchanger tubes, it is characterized in that: dividing plate is provided with by-pass prot.
CNB2006100689611A 2006-09-28 2006-09-28 Heat exchanger for fuel oil heater with heat exchange pipe Expired - Fee Related CN100412461C (en)

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CNB2006100689611A CN100412461C (en) 2006-09-28 2006-09-28 Heat exchanger for fuel oil heater with heat exchange pipe

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Application Number Priority Date Filing Date Title
CNB2006100689611A CN100412461C (en) 2006-09-28 2006-09-28 Heat exchanger for fuel oil heater with heat exchange pipe

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CN100412461C true CN100412461C (en) 2008-08-20

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Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100491860C (en) * 2007-11-30 2009-05-27 河北宏业机械股份有限公司 Gas flow equalizing ring for oil heater
CN112283936B (en) * 2020-09-16 2022-07-29 北京北机机电工业有限责任公司 High-efficient heat transfer device

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1263845A (en) * 1969-07-04 1972-02-16 Hovalwerk Ag Ospelt Water heating boiler
DE3504225A1 (en) * 1984-06-01 1985-12-05 Bélmegyeri Ujbarázda MGTSZ, Bélmegyer Atmospheric hot-water boiler with combustion chamber arranged at the bottom, in particular for gas firing
CN85105231A (en) * 1985-07-08 1987-01-07 韦巴斯托沃克W·贝勒有限公司 Water heater
CN2287211Y (en) * 1996-11-19 1998-08-05 刘成金 Heater for fuel oil of vehicle
CN2295054Y (en) * 1997-07-10 1998-10-21 泊头市仪表总厂 Independent fuel-oil heater
EP1445552A1 (en) * 2003-02-10 2004-08-11 J. Eberspächer GmbH Co. KG Heat exchanger for a heater, especially for car heating.
DE10358016B3 (en) * 2003-12-11 2005-01-27 J. Eberspächer GmbH & Co. KG Heat-exchanger system for a motor vehicle's heater has magnesium outer and aluminum inner heat-exchanger housings
CN200946916Y (en) * 2006-09-28 2007-09-12 山东大学 Heat exchanger for fuel heater with heat-exchanging pipe

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1263845A (en) * 1969-07-04 1972-02-16 Hovalwerk Ag Ospelt Water heating boiler
DE3504225A1 (en) * 1984-06-01 1985-12-05 Bélmegyeri Ujbarázda MGTSZ, Bélmegyer Atmospheric hot-water boiler with combustion chamber arranged at the bottom, in particular for gas firing
CN85105231A (en) * 1985-07-08 1987-01-07 韦巴斯托沃克W·贝勒有限公司 Water heater
CN2287211Y (en) * 1996-11-19 1998-08-05 刘成金 Heater for fuel oil of vehicle
CN2295054Y (en) * 1997-07-10 1998-10-21 泊头市仪表总厂 Independent fuel-oil heater
EP1445552A1 (en) * 2003-02-10 2004-08-11 J. Eberspächer GmbH Co. KG Heat exchanger for a heater, especially for car heating.
DE10358016B3 (en) * 2003-12-11 2005-01-27 J. Eberspächer GmbH & Co. KG Heat-exchanger system for a motor vehicle's heater has magnesium outer and aluminum inner heat-exchanger housings
CN200946916Y (en) * 2006-09-28 2007-09-12 山东大学 Heat exchanger for fuel heater with heat-exchanging pipe

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C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Assignee: Wuxi Longsheng Technology Co., Ltd.

Assignor: Shandong University

Contract fulfillment period: 2009.3.1 to 2014.2.28 contract change

Contract record no.: 2009320000229

Denomination of invention: Heat exchanger for fuel oil heater with heat exchange pipe

Granted publication date: 20080820

License type: Exclusive license

Record date: 2009.3.5

LIC Patent licence contract for exploitation submitted for record

Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2009.3.1 TO 2014.2.28; CHANGE OF CONTRACT

Name of requester: WUXI LONGSHEN TECHNOLOGY CO., LTD.

Effective date: 20090305

EC01 Cancellation of recordation of patent licensing contract

Assignee: Wuxi Longsheng Technology Co., Ltd.

Assignor: Shandong University

Contract record no.: 2009320000229

Date of cancellation: 20120607

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080820

Termination date: 20130928