WO2020133958A1 - New heat exchange tube - Google Patents
New heat exchange tube Download PDFInfo
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- WO2020133958A1 WO2020133958A1 PCT/CN2019/091654 CN2019091654W WO2020133958A1 WO 2020133958 A1 WO2020133958 A1 WO 2020133958A1 CN 2019091654 W CN2019091654 W CN 2019091654W WO 2020133958 A1 WO2020133958 A1 WO 2020133958A1
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- WIPO (PCT)
- Prior art keywords
- heat exchange
- boss
- tube body
- exchange tube
- tube
- Prior art date
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
- F28D1/0472—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being helically or spirally coiled
- F28D1/0473—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being helically or spirally coiled the conduits having a non-circular cross-section
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H1/00—Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
- F24H1/22—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
- F24H1/40—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
- F24H1/43—Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes helically or spirally coiled
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/10—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
- F28F1/42—Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
- F28F1/424—Means comprising outside portions integral with inside portions
- F28F1/426—Means comprising outside portions integral with inside portions the outside portions and the inside portions forming parts of complementary shape, e.g. concave and convex
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0024—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for combustion apparatus, e.g. for boilers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
- F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F1/00—Tubular elements; Assemblies of tubular elements
- F28F1/02—Tubular elements of cross-section which is non-circular
- F28F1/04—Tubular elements of cross-section which is non-circular polygonal, e.g. rectangular
Definitions
- the utility model belongs to the technical field of heating equipment, and relates to a heat exchange tube, in particular to a new type of heat exchange tube.
- Traditional gas wall-hung boilers are usually equipped with corresponding devices such as combustion chambers and heat exchangers.
- the heat exchanger absorbs the energy generated by the combustion gas and transfers it to the cold water flowing through the heat exchanger through the inlet pipe. After heat exchange, the water temperature rises. Hot water is discharged from the water outlet pipe to realize the function of heating the water flow; the high-temperature flue gas generated by the combustion is pumped out of the room through the pipe chamber by the fan. Since the water vapor in the flue gas takes a considerable part of the energy, the thermal efficiency of the wall-hung boiler is limited, and the heat utilization rate is difficult to improve.
- the traditional gas-fired wall-hung boiler is limited by the structure and materials, and cannot withstand the corrosive effect of condensed water produced by the liquefaction of steam on the product, and the condensed water cannot be discharged.
- Condensing gas-fired wall-mounted boilers use flue gas heat to heat the water flow, which can withstand the negative effects of condensate on the product and greatly improve the heat utilization rate.
- the Chinese utility model patent with the application number 201720876454.4 discloses a condensing heat exchanger, including a shell and a spiral heat exchange Pipe, slow flow belt, water inlet pipe, water outlet pipe, flue gas heating pipe and condensate water outlet pipe, among them, there is a slow flow belt between the spiral heat exchange tube and the shell, the slow flow belt can guide and delay the flue gas generated by the burner
- the speed of the outward discharge allows the flue gas to further heat the spiral heat exchange tube and improve the heat exchange rate.
- the cross section is a spiral heat exchange tube with a D-shaped cross section.
- the heat exchange tube uses a flat tube, so its strength is not ideal.
- the purpose of the utility model is to solve the above problems in the existing technology, and propose a heat exchange tube with high heat exchange efficiency and high strength.
- a new type of heat exchange tube including a spiral tube body, the two ends of the tube body are respectively the water inlet end and the water outlet end, which is characterized by
- the tube body is a flat tube. Both sides of the cross section of the tube body are arc-shaped.
- the upper and lower side walls of the tube body are evenly provided with a protruding boss 1 and a boss 2 adjacent to each other.
- the boss 1 described above is in close contact with the boss 2 described above.
- the heat exchange area of the pipe body is increased, which has the advantage of higher heat exchange efficiency.
- the boss 1 and the corresponding boss 2 are in close contact , Increase the strength of the new heat exchange tube and improve the service life.
- the ratio of the height and width of the cross section of the tube body is 1:2 to 1:5.
- the tube body has a larger outer surface area, and the heat exchange efficiency is improved.
- the number of turns of the tube body is 8 to 16 turns.
- the water inlet and the water outlet are arranged in parallel and the water inlet and the water outlet are oriented in the same direction. With the above settings, it is easy to install and use the new heat exchange tube.
- the boss 1 is elongated, the outer width of the boss 1 is greater than the inner end width, and the gaps formed by the adjacent bosses are the same .
- the gap of the heat exchange tube is the same, so that the heat exchange is more uniform.
- the boss 1 is symmetrically arranged and the corresponding tangent of the center line of the boss 1 and the spiral of the tube body is 26°-61°.
- the angle formed by the center line of the boss 1 and the center line corresponding to the spiral line of the pipe body is 45°.
- the boss 2 is elongated, and the outer width of the boss 2 is greater than the width of the inner end, and the gaps formed by the adjacent bosses 2 are the same .
- the gap of the heat exchange tube is the same, so that the heat exchange is more uniform.
- the boss 2 is symmetrically arranged and the corresponding tangent of the center line of the boss 2 and the spiral of the tube body is 26°-61°.
- the angle formed by the center line of the boss 2 and the center line corresponding to the spiral line of the pipe body is 45°.
- both ends of the tube body and the water inlet end and the water outlet end are smoothly transitioned. Both ends of the pipe body, the water inlet end and the water outlet end are smooth transitions, which has the advantages of high strength and convenient manufacture.
- the tube body is made of stainless steel.
- the tube body is made of stainless steel, which has the advantages of high strength and long service life.
- the tube body is made of copper.
- the new heat exchange tube has the following advantages:
- the lower side of the tube body is provided with the above-mentioned boss two.
- the boss one abuts on the adjacent boss two, which has a better support effect while maintaining the tube
- the distance between the bodies has the advantages of uniform heat exchange and stable and reliable structure
- the tube body is made of stainless steel, which has the advantages of high strength and long service life.
- FIG. 1 is a schematic perspective view of the new heat exchange tube.
- FIG. 2 is a perspective schematic view of the novel heat exchange tube from another angle.
- Figure 3 is a schematic top view of the new heat exchange tube.
- FIG. 4 is a schematic cross-sectional view taken along line A-A of FIG. 3.
- the new heat exchange tube includes a spiral-shaped tube body 1.
- the two ends of the tube body 1 are the water inlet end 2 and the water outlet end 3.
- the water inlet end 2 and the water outlet end 3 are arranged in parallel and
- the water inlet 2 and the water outlet 3 are oriented in the same direction.
- the tube body 1 is a flat tube. Both sides of the cross section of the tube body 1 are arc-shaped.
- the upper and lower side walls of the tube body 1 are evenly provided with protruding bosses 1 and 4 and bosses 2 and 5 are adjacent 4 is in close contact with boss 2 and 5.
- the ratio of the height H and the width L of the cross section of the pipe body 1 is 1:2 to 1:5, which makes the heat exchange area of the pipe body 1 larger and improves the efficiency of human exchange.
- the boss 4 is elongated and the outer width of the boss 4 is greater than the width of the inner end.
- the gap formed by the adjacent boss 4 is the same.
- the boss 4 is symmetrically arranged and the center line of the boss 4
- the tangent corresponding to the spiral of the tube 1 is 26°-61°.
- the angle formed by the center line of the boss 1 and the center of the spiral of the tube 1 is 45°.
- the bosses 2 and 5 are elongated, and the outer width of the bosses is greater than the inner ends and the gaps formed by the adjacent bosses 2 and 5 are the same.
- the bosses 2 and 5 are symmetrically arranged and the bosses 2 and 5
- the corresponding tangent of the center line and the spiral line of the tube 1 is 26°-61°.
- the angle formed by the center line of the boss 2 and the center line corresponding to the spiral line of the tube 1 is 45°.
- connection parts of the two ends of the pipe body 1 with the water inlet end 2 and the water outlet end 3 are smooth transitions, which have the advantages of high strength and convenient manufacture.
- the tube body 1 is made of stainless steel, which has the advantages of high strength and long service life. As another way, the tube body 1 is made of copper.
- the heat exchange area of the tube body 1 is increased, which has the advantage of higher heat exchange efficiency.
- the boss 1 and the corresponding protrusions Taiwan II 5 is close to each other, which increases the strength of the new heat exchange tube and improves the service life.
- the boss one 4 is elongated and the outer width of the boss one 4 is greater than the inner end width and the gap formed by the adjacent boss one 4 is the same, the boss two 5 is elongated and the boss The width of the outer end is larger than the width of the inner end and the gaps formed by the adjacent bosses 2 and 5 are the same, so that the gap of the heat exchange tube is the same and the heat exchange is more uniform.
Abstract
Provided is a heat exchange tube, comprising a spiral tube body (1), wherein two ends of the tube body (1) are respectively a water inlet end (2) and a water outlet end (3); the tube body (1) is a flat tube; two sides of a cross section of the tube body (1) are both arc-shaped; and upper and lower side walls of the tube body (1) are both evenly provided with protruding first bosses (4) and second bosses (5), with adjacent first bosses (4) and second bosses (5) abutting against each other.
Description
本实用新型属于采暖设备技术领域,涉及一种热交换管,特别是一种新型热交换管。The utility model belongs to the technical field of heating equipment, and relates to a heat exchange tube, in particular to a new type of heat exchange tube.
传统燃气壁挂炉通常配备燃烧室、换热器等相应装置,利用换热器吸收燃烧燃气所产生的能量,传递给由进水管流经换热器的冷水,经热交换后水温升高,热水从出水管排出,实现加热水流的功能;燃烧产生的高温烟气由风机经烟斗室抽出室外。由于烟气中的水蒸汽带走相当大的一部分能量,导致壁挂炉的热效率有限,热量利用率难以提升。传统燃气壁挂炉受结构和材料的限制,不能承受水蒸汽液化后产生的冷凝水对产品的腐蚀作用,且冷凝水无法排出。冷凝式燃气壁挂炉利用了烟气热量加热水流,可以承受冷凝水对产品产生的负面作用,并使热利用率大为提高。Traditional gas wall-hung boilers are usually equipped with corresponding devices such as combustion chambers and heat exchangers. The heat exchanger absorbs the energy generated by the combustion gas and transfers it to the cold water flowing through the heat exchanger through the inlet pipe. After heat exchange, the water temperature rises. Hot water is discharged from the water outlet pipe to realize the function of heating the water flow; the high-temperature flue gas generated by the combustion is pumped out of the room through the pipe chamber by the fan. Since the water vapor in the flue gas takes a considerable part of the energy, the thermal efficiency of the wall-hung boiler is limited, and the heat utilization rate is difficult to improve. The traditional gas-fired wall-hung boiler is limited by the structure and materials, and cannot withstand the corrosive effect of condensed water produced by the liquefaction of steam on the product, and the condensed water cannot be discharged. Condensing gas-fired wall-mounted boilers use flue gas heat to heat the water flow, which can withstand the negative effects of condensate on the product and greatly improve the heat utilization rate.
目前,市场上冷凝式热交换器的热交换组件各部件大都是通过焊接技术拼接而成,如申请号为201720876454.4的中国实用新型专利,公开了一种冷凝热交换器,包括外壳、螺旋热交换管、缓流带、入水管、出水管、烟气加热管和冷凝出水管,其中,螺旋热交换管与外壳之间设有缓流带,缓流带可以疏导并延缓燃烧器产生的烟气向外排出的速度,使得烟气可以对螺旋热交换管进一步加热,提高了热交换率,截面为类似D型状的截面的螺旋热交换管。但该热交换管的采用扁平管,因此其强度不够理想。At present, most of the components of the heat exchange assembly of the condensing heat exchanger on the market are spliced by welding technology. For example, the Chinese utility model patent with the application number 201720876454.4 discloses a condensing heat exchanger, including a shell and a spiral heat exchange Pipe, slow flow belt, water inlet pipe, water outlet pipe, flue gas heating pipe and condensate water outlet pipe, among them, there is a slow flow belt between the spiral heat exchange tube and the shell, the slow flow belt can guide and delay the flue gas generated by the burner The speed of the outward discharge allows the flue gas to further heat the spiral heat exchange tube and improve the heat exchange rate. The cross section is a spiral heat exchange tube with a D-shaped cross section. However, the heat exchange tube uses a flat tube, so its strength is not ideal.
发明内容Summary of the invention
本实用新型的目的是针对现有的技术存在上述问题,提出了一种热交换效率较高且强度较高的热交换管。The purpose of the utility model is to solve the above problems in the existing technology, and propose a heat exchange tube with high heat exchange efficiency and high strength.
本实用新型的目的可通过下列技术方案来实现:新型热交换管,包括呈螺旋状的管体,所述的管体的两端分别为进水端以及出水端,其特征在于,所述的管体为扁平管,所述的管体的截面的两侧均为圆弧形,所述的管体的上下两侧壁均匀设有凸出的凸台一以及凸台二且相邻的所述的凸台一与所述的凸台二相贴靠。The purpose of the utility model can be achieved through the following technical solutions: a new type of heat exchange tube, including a spiral tube body, the two ends of the tube body are respectively the water inlet end and the water outlet end, which is characterized by The tube body is a flat tube. Both sides of the cross section of the tube body are arc-shaped. The upper and lower side walls of the tube body are evenly provided with a protruding boss 1 and a boss 2 adjacent to each other. The boss 1 described above is in close contact with the boss 2 described above.
由于管体的上下两侧壁均匀设有凸台一以及凸台二,增大了管体的热交换面积,具有热交换效率较高的优点,凸台一与对应的凸台二相贴靠,增加了本新型热交换管的强度,提高了使用寿命。Since the upper and lower side walls of the pipe body are provided with bosses 1 and bosses 2 uniformly, the heat exchange area of the pipe body is increased, which has the advantage of higher heat exchange efficiency. The boss 1 and the corresponding boss 2 are in close contact , Increase the strength of the new heat exchange tube and improve the service life.
在上述的新型热交换管中,所述的管体截面的高度和宽度之比为1∶2至1∶5。采用上述设置,使管体具有较大的外表面面积,提高了热交换效率。In the above-mentioned new heat exchange tube, the ratio of the height and width of the cross section of the tube body is 1:2 to 1:5. With the above arrangement, the tube body has a larger outer surface area, and the heat exchange efficiency is improved.
在上述的新型热交换管中,所述的管体的圈数为8至16圈。In the above-mentioned new heat exchange tube, the number of turns of the tube body is 8 to 16 turns.
在上述的新型热交换管中,所述的进水端以及所述的出水端平行设置且所述的进水端与所述的出水端朝向相同。采用上述设置,便于本新型热交换管的安装与使用。In the above-mentioned novel heat exchange tube, the water inlet and the water outlet are arranged in parallel and the water inlet and the water outlet are oriented in the same direction. With the above settings, it is easy to install and use the new heat exchange tube.
在上述的新型热交换管中,所述的凸台一呈长条形且所述的凸台一的外端宽度大于其内端宽度且所述的相邻的凸台一形成的间隙均相同。采用上述设置,使本热交换管的间隙相同,使热交换较为均匀的优点。In the above-mentioned new heat exchange tube, the boss 1 is elongated, the outer width of the boss 1 is greater than the inner end width, and the gaps formed by the adjacent bosses are the same . With the above arrangement, the gap of the heat exchange tube is the same, so that the heat exchange is more uniform.
在上述的新型热交换管中,所述的凸台一呈对称设置且所述的凸台一的中线与所述的管体的螺旋线的对应的切线呈26°-61°。作为优选的,凸台一的中线与管体的螺旋线对应的中线形成的夹角为45°。In the above-mentioned new type heat exchange tube, the boss 1 is symmetrically arranged and the corresponding tangent of the center line of the boss 1 and the spiral of the tube body is 26°-61°. Preferably, the angle formed by the center line of the boss 1 and the center line corresponding to the spiral line of the pipe body is 45°.
在上述的新型热交换管中,所述的凸台二呈长条形且所述的 凸台二的外端宽度大于其内端宽度且所述的相邻的凸台二形成的间隙均相同。采用上述设置,使本热交换管的间隙相同,使热交换较为均匀的优点。In the above-mentioned new type heat exchange tube, the boss 2 is elongated, and the outer width of the boss 2 is greater than the width of the inner end, and the gaps formed by the adjacent bosses 2 are the same . With the above arrangement, the gap of the heat exchange tube is the same, so that the heat exchange is more uniform.
在上述的新型热交换管中,所述的凸台二呈对称设置且所述的凸台二的中线与所述的管体的螺旋线的对应的切线呈26°-61°。作为优选的,凸台二的中线与管体的螺旋线对应的中线形成的夹角为45°。In the above-mentioned novel heat exchange tube, the boss 2 is symmetrically arranged and the corresponding tangent of the center line of the boss 2 and the spiral of the tube body is 26°-61°. Preferably, the angle formed by the center line of the boss 2 and the center line corresponding to the spiral line of the pipe body is 45°.
在上述的新型热交换管中,所述的管体的两端与所述的进水端以及所述的出水端连接部位均为光滑过渡。管体的两端与所述的进水端与所述的出水端均为光滑过渡,具有强度较高且制造较为方便的优点。In the above-mentioned novel heat exchange tube, both ends of the tube body and the water inlet end and the water outlet end are smoothly transitioned. Both ends of the pipe body, the water inlet end and the water outlet end are smooth transitions, which has the advantages of high strength and convenient manufacture.
在上述的新型热交换管中,所述的管体采用不锈钢材料制成。管体采用不锈钢材料制成,具有强度较高且使用寿命较长的优点。作为另一种方式,管体采用铜制成。In the aforementioned new heat exchange tube, the tube body is made of stainless steel. The tube body is made of stainless steel, which has the advantages of high strength and long service life. As another way, the tube body is made of copper.
与现有技术相比,本新型热交换管具有以下优点:Compared with the existing technology, the new heat exchange tube has the following advantages:
1、由于管体的上下两侧壁均匀设有凸台一以及凸台二,增大了管体的热交换面积,具有热交换效率较高的优点,凸台一与对应的凸台二相贴靠,增加了本新型热交换管的强度,提高了使用寿命。1. Since the upper and lower side walls of the pipe body are evenly provided with bosses 1 and bosses 2, the heat exchange area of the pipe body is increased, which has the advantage of higher heat exchange efficiency. Boss 1 and the corresponding boss are in two phases Adherence increases the strength of the new heat exchange tube and improves the service life.
2、管体的下侧面设有上述的凸台二,在管体沿其轴向压扁成型时,凸台一贴靠在相邻的凸台二上,具有较好的支撑效果同时保持管体的间距,具有热交换均匀,同时具有结构稳定可靠的优点;2. The lower side of the tube body is provided with the above-mentioned boss two. When the tube body is flattened along the axial direction, the boss one abuts on the adjacent boss two, which has a better support effect while maintaining the tube The distance between the bodies has the advantages of uniform heat exchange and stable and reliable structure;
3、管体采用不锈钢材料制成,具有强度较高且使用寿命较长的优点。3. The tube body is made of stainless steel, which has the advantages of high strength and long service life.
图1是本新型热交换管的立体示意图。FIG. 1 is a schematic perspective view of the new heat exchange tube.
图2是本新型热交换管的另一角度的立体示意图。FIG. 2 is a perspective schematic view of the novel heat exchange tube from another angle.
图3是本新型热交换管俯视示意图。Figure 3 is a schematic top view of the new heat exchange tube.
图4是图3的A-A剖视示意图。4 is a schematic cross-sectional view taken along line A-A of FIG. 3.
图中,1、管体;2、进水端;3、出水端;4、凸台一;5、凸台二。In the picture, 1. pipe body; 2. water inlet end; 3. water outlet end; 4. boss one; 5. boss two.
以下是本实用新型的具体实施例并结合附图,对本实用新型的技术方案作进一步的描述,但本实用新型并不限于这些实施例。The following are specific embodiments of the utility model and the accompanying drawings to further describe the technical solution of the utility model, but the utility model is not limited to these embodiments.
如图1至4所示,新型热交换管,包括呈螺旋状的管体1,管体1的两端分别为进水端2以及出水端3,进水端2以及出水端3平行设置且进水端2与出水端3朝向相同。管体1为扁平管,管体1的截面的两侧均为圆弧形,管体1的上下两侧壁均匀设有凸出的凸台一4以及凸台二5且相邻凸台一4与凸台二5相贴靠。管体1截面的高度H和宽度L之比为1∶2至1∶5,使管体1的热交换面积较大,提高了人交换效率。As shown in FIGS. 1 to 4, the new heat exchange tube includes a spiral-shaped tube body 1. The two ends of the tube body 1 are the water inlet end 2 and the water outlet end 3. The water inlet end 2 and the water outlet end 3 are arranged in parallel and The water inlet 2 and the water outlet 3 are oriented in the same direction. The tube body 1 is a flat tube. Both sides of the cross section of the tube body 1 are arc-shaped. The upper and lower side walls of the tube body 1 are evenly provided with protruding bosses 1 and 4 and bosses 2 and 5 are adjacent 4 is in close contact with boss 2 and 5. The ratio of the height H and the width L of the cross section of the pipe body 1 is 1:2 to 1:5, which makes the heat exchange area of the pipe body 1 larger and improves the efficiency of human exchange.
凸台一4呈长条形且凸台一4的外端宽度大于其内端宽度且相邻的凸台一4形成的间隙均相同,凸台一4呈对称设置且凸台一4的中线与管体1的螺旋线的对应的切线呈26°-61°,作为优选的,凸台一4的中线与管体1的螺旋线对应的中线形成的夹角为45°。The boss 4 is elongated and the outer width of the boss 4 is greater than the width of the inner end. The gap formed by the adjacent boss 4 is the same. The boss 4 is symmetrically arranged and the center line of the boss 4 The tangent corresponding to the spiral of the tube 1 is 26°-61°. Preferably, the angle formed by the center line of the boss 1 and the center of the spiral of the tube 1 is 45°.
凸台二5呈长条形且所述的凸台的外端宽度大于其内端宽度且相邻的凸台二5形成的间隙均相同,凸台二5呈对称设置且凸台二5的中线与管体1的螺旋线的对应的切线呈26°-61°,作为优选的,凸台二5的中线与管体1的螺旋线对应的中线形成的夹角为45°。The bosses 2 and 5 are elongated, and the outer width of the bosses is greater than the inner ends and the gaps formed by the adjacent bosses 2 and 5 are the same. The bosses 2 and 5 are symmetrically arranged and the bosses 2 and 5 The corresponding tangent of the center line and the spiral line of the tube 1 is 26°-61°. Preferably, the angle formed by the center line of the boss 2 and the center line corresponding to the spiral line of the tube 1 is 45°.
管体1的两端分别与进水端2以及出水端3连接部位均为光滑过渡,具有强度较高且制造较为方便的优点。The connection parts of the two ends of the pipe body 1 with the water inlet end 2 and the water outlet end 3 are smooth transitions, which have the advantages of high strength and convenient manufacture.
管体1采用不锈钢材料制成,具有强度较高且使用寿命较长的优点。作为另一种方式,管体1采用铜制成。The tube body 1 is made of stainless steel, which has the advantages of high strength and long service life. As another way, the tube body 1 is made of copper.
由于管体1的上下两侧壁均匀设有凸台一4以及凸台二5,增大了管体1的热交换面积,具有热交换效率较高的优点,凸台一4与对应的凸台二5相贴靠,增加了本新型热交换管的强度,提高了使用寿命。凸台一4呈长条形且凸台一4的外端宽度大于其内端宽度且相邻的凸台一4形成的间隙均相同,凸台二5呈长条形且所述的凸台的外端宽度大于其内端宽度且相邻的凸台二5形成的间隙均相同,使本热交换管的间隙相同,使热交换较为均匀的优点。Since the upper and lower side walls of the tube body 1 are evenly provided with bosses 1 and 4 and bosses 2 and 5, the heat exchange area of the tube body 1 is increased, which has the advantage of higher heat exchange efficiency. The boss 1 and the corresponding protrusions Taiwan II 5 is close to each other, which increases the strength of the new heat exchange tube and improves the service life. The boss one 4 is elongated and the outer width of the boss one 4 is greater than the inner end width and the gap formed by the adjacent boss one 4 is the same, the boss two 5 is elongated and the boss The width of the outer end is larger than the width of the inner end and the gaps formed by the adjacent bosses 2 and 5 are the same, so that the gap of the heat exchange tube is the same and the heat exchange is more uniform.
本文中所描述的具体实施例仅仅是对本实用新型精神作举例说明。本实用新型所属技术领域的技术人员可以对所描述的具体实施例做各种各样的修改或补充或采用类似的方式替代,但并不会偏离本实用新型的精神或者超越所附权利要求书所定义的范围。The specific embodiments described in this article are only examples of the spirit of the present invention. A person skilled in the art to which the utility model belongs can make various modifications or additions to the described specific embodiments or substitute in a similar manner, but it will not deviate from the spirit of the utility model or exceed the appended claims The defined range.
尽管本文较多地使用了管体1、进水端2、出水端3、凸台一4、凸台二5等术语,但并不排除使用其它术语的可能性。使用这些术语仅仅是为了更方便地描述和解释本实用新型的本质;把它们解释成任何一种附加的限制都是与本实用新型精神相违背的。Although this article uses the terms tube 1, inlet 2, outlet 3, boss one 4, boss two five, etc., the possibility of using other terms is not excluded. These terms are only used to more conveniently describe and explain the essence of the present invention; interpreting them as any kind of additional restrictions is contrary to the spirit of the present invention.
Claims (9)
- 新型热交换管,包括呈螺旋状的管体(1),所述的管体(1)的两端分别为进水端(2)以及出水端(3),其特征在于,所述的管体(1)为扁平管,所述的管体(1)的截面的两侧均为圆弧形,所述的管体(1)的上下两侧壁均匀设有凸出的凸台一(4)以及凸台二(5)且相邻的所述的凸台一(4)与所述的凸台二(5)相贴靠。A new type of heat exchange tube includes a spiral tube body (1). The two ends of the tube body (1) are the water inlet end (2) and the water outlet end (3), respectively, characterized in that the pipe The body (1) is a flat tube, and both sides of the cross section of the tube body (1) are arc-shaped, and the upper and lower side walls of the tube body (1) are provided with convex bosses 1 ( 4) and two bosses (5) and the adjacent boss one (4) is in contact with the boss two (5).
- 根据权利要求1所述的新型热交换管,其特征在于,所述的管体(1)截面的高度和宽度之比为1∶2至1∶5。The novel heat exchange tube according to claim 1, characterized in that the ratio of the height and width of the cross section of the tube body (1) is 1:2 to 1:5.
- 根据权利要求1所述的新型热交换管,其特征在于,所述的进水端(2)以及所述的出水端(3)平行设置且所述的进水端(2)与所述的出水端(3)朝向相同。The novel heat exchange tube according to claim 1, characterized in that the water inlet (2) and the water outlet (3) are arranged in parallel and the water inlet (2) and the The water outlet (3) faces the same direction.
- 根据权利要求1或2或3所述的新型热交换管,其特征在于,所述的凸台一(4)呈长条形且所述的凸台一(4)的外端宽度大于其内端宽度且所述的相邻的凸台一(4)形成的间隙均相同。The novel heat exchange tube according to claim 1 or 2 or 3, characterized in that the boss one (4) is elongated and the outer end width of the boss one (4) is larger than the inner The width of the end and the gap formed by the adjacent boss one (4) are the same.
- 根据权利要求4所述的新型热交换管,其特征在于,所述的凸台一(4)呈对称设置且所述的凸台一(4)的中线与所述的管体(1)的螺旋线的对应的切线呈26°-61°。The new heat exchange tube according to claim 4, characterized in that, the boss one (4) is symmetrically arranged and the center line of the boss one (4) is in line with that of the tube body (1) The corresponding tangent of the helix is 26°-61°.
- 根据权利要求1或2或3所述的新型热交换管,其特征在于,所述的凸台二(5)呈长条形且所述的凸台二(5)的外端宽度大于其内端宽度且所述的相邻的凸台二(5)形成的间隙均相同。The new heat exchange tube according to claim 1 or 2 or 3, characterized in that the boss two (5) is elongated and the outer width of the boss two (5) is larger than the inner The width of the end and the gap formed by the two adjacent bosses (5) are the same.
- 根据权利要求6所述的新型热交换管,其特征在于,所述的凸台二(5)呈对称设置且所述的凸台二(5)的中线与所述的管体(1)的螺旋线的对应的切线呈26°-61°。The new heat exchange tube according to claim 6, characterized in that, the boss two (5) is symmetrically arranged and the center line of the boss two (5) is in line with that of the tube body (1) The corresponding tangent of the helix is 26°-61°.
- 根据权利要求1或2或3所述的新型热交换管,其特征在于,所述的管体(1)的两端与所述的进水端(2)以及所述的出水端(3)连接部位均为光滑过渡。The new heat exchange tube according to claim 1 or 2 or 3, characterized in that the two ends of the tube body (1) and the water inlet end (2) and the water outlet end (3) The connection parts are all smooth transition.
- 根据权利要求1或2或3所述的新型热交换管,其特征在于,所述的管体(1)采用不锈钢材料制成。The novel heat exchange tube according to claim 1 or 2 or 3, characterized in that the tube body (1) is made of stainless steel material.
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CN201822206515.3 | 2018-12-26 | ||
CN201822206515.3U CN209445601U (en) | 2018-12-26 | 2018-12-26 | Novel heat-exchange tube |
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EP2133634A1 (en) * | 2008-06-11 | 2009-12-16 | Aic S.A. | Fire heat exchanger for liquid heaters |
CN105276816A (en) * | 2014-07-12 | 2016-01-27 | 中山市健泰实业有限公司 | Furnace heat exchange coil |
CN106482343A (en) * | 2015-09-02 | 2017-03-08 | 积顿新热能设备无锡有限公司 | A kind of flattened oval spiral heat exchanging water pipe |
CN206420160U (en) * | 2017-01-04 | 2017-08-18 | 广东昊森热能设备有限公司 | A kind of main heat exchanger of fully pre-mixing gas combustion water heater for heating |
CN206670056U (en) * | 2017-03-14 | 2017-11-24 | 广东万家乐燃气具有限公司 | A kind of efficient condensing heat exchanger |
CN107906747A (en) * | 2017-12-14 | 2018-04-13 | 浙江广涛卫厨有限公司 | Heat exchanger |
CN305276242S (en) * | 2018-12-29 | 2019-07-26 |
-
2018
- 2018-12-26 CN CN201822206515.3U patent/CN209445601U/en active Active
-
2019
- 2019-06-18 WO PCT/CN2019/091654 patent/WO2020133958A1/en active Application Filing
- 2019-09-03 DE DE202019104840.9U patent/DE202019104840U1/en active Active
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EP2133634A1 (en) * | 2008-06-11 | 2009-12-16 | Aic S.A. | Fire heat exchanger for liquid heaters |
CN105276816A (en) * | 2014-07-12 | 2016-01-27 | 中山市健泰实业有限公司 | Furnace heat exchange coil |
CN106482343A (en) * | 2015-09-02 | 2017-03-08 | 积顿新热能设备无锡有限公司 | A kind of flattened oval spiral heat exchanging water pipe |
CN206420160U (en) * | 2017-01-04 | 2017-08-18 | 广东昊森热能设备有限公司 | A kind of main heat exchanger of fully pre-mixing gas combustion water heater for heating |
CN206670056U (en) * | 2017-03-14 | 2017-11-24 | 广东万家乐燃气具有限公司 | A kind of efficient condensing heat exchanger |
CN107906747A (en) * | 2017-12-14 | 2018-04-13 | 浙江广涛卫厨有限公司 | Heat exchanger |
CN305276242S (en) * | 2018-12-29 | 2019-07-26 |
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