Heat exchanger
09581398 ยท 2017-02-28
Assignee
Inventors
Cpc classification
F28D2021/0085
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D1/05333
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B23K35/362
PERFORMING OPERATIONS; TRANSPORTING
F28F21/084
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B32B15/017
PERFORMING OPERATIONS; TRANSPORTING
B23K35/282
PERFORMING OPERATIONS; TRANSPORTING
F28D2021/0094
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F19/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B23K1/012
PERFORMING OPERATIONS; TRANSPORTING
B32B15/01
PERFORMING OPERATIONS; TRANSPORTING
B23K1/19
PERFORMING OPERATIONS; TRANSPORTING
B32B15/016
PERFORMING OPERATIONS; TRANSPORTING
F28D2021/0084
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B23K1/20
PERFORMING OPERATIONS; TRANSPORTING
B23K1/203
PERFORMING OPERATIONS; TRANSPORTING
International classification
F28D21/00
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28F19/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
C21C5/00
CHEMISTRY; METALLURGY
B32B15/01
PERFORMING OPERATIONS; TRANSPORTING
F28F21/08
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F28D1/053
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B22F1/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Heat exchange tubes of a heat exchanger are formed of an alloy containing Mn (0.2 to 0.3 mass %), Cu (0.1 mass % or less), and Fe (0.2 mass % or less), the balance being Al and unavoidable impurities. A Zn diffused layer is formed in an outer surface layer portion of the peripheral wall of each heat exchange tube. T200, 0.57A1.5, D/T0.55, and 0.0055A/D0.025 are satisfied, where T is the thickness [m] of the peripheral wall of the heat exchange tube, A is the Zn concentration [mass %] at the outermost surface of the outer surface layer portion, and D is the maximum depth [m] of the Zn diffused layer. The spontaneous potential of the Zn diffused layer is lower than that of a portion of the peripheral wall located on the inner side of the Zn diffused layer.
Claims
1. A heat exchanger comprising heat exchange tubes formed of aluminum, and fins formed of aluminum and brazed to the heat exchange tubes, wherein each heat exchange tube is formed of an alloy which contains Mn in an amount of 0.2 to 0.3 mass %, Cu in an amount of 0.1 mass % or less, Fe in an amount of 0.2 mass % or less, and Si in an amount of 0.2 mass % or less, the balance being Al and unavoidable impurities; a Zn diffused layer is formed in an outer surface layer portion of the heat exchange tube; conditions of T200, 0.57A1.5, D/T0.55, and 0.0055A/D0.025 are satisfied, where T is a thickness [m] of a peripheral wall of the heat exchange tube, A is a Zn concentration [mass %] at an outermost surface of the outer surface layer portion of the heat exchange tube, and D is a maximum depth [m] of the Zn diffused layer; and a spontaneous potential of the Zn diffused layer is lower than a spontaneous potential of an inner portion of the peripheral wall of the heat exchange tube, the inner portion being located on the inner side of the Zn diffused layer.
2. A heat exchanger according to claim 1, wherein the spontaneous potential of the Zn diffused layer is 100 to 150 mV lower than that of the inner portion of the peripheral wall of the heat exchange tube, the inner portion being located on the inner side of the Zn diffused layer.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
DESCRIPTION OF THE PREFERRED EMBODIMENT
(3) An embodiment of the present invention will next be described with reference to the drawings. In the embodiment, a heat exchanger according to the present invention is applied to a condenser for a car air conditioner.
(4)
(5) Notably, in the following description, the upper, lower, left-hand, and right-hand sides of
(6) As shown in
(7) The left header tank 2 is divided by a partition member 7 into upper and lower header sections 2a and 2b, at a position higher than the center of the left header tank 2 in the height direction. The right header tank 3 is divided by another partition member 7 into upper and lower header sections 3a and 3b, at a position lower than the center of the right header tank 3 in the height direction. A fluid inlet (not shown) is formed at the upper header section 2a of the left header tank 2, and an aluminum inlet member 8 having a fluid inflow passage 8a communicating with the fluid inlet is brazed to the upper header section 2a. A fluid outlet (not shown) is formed at the lower header section 3b of the right header tank 3, and an aluminum outlet member 9 having a fluid outflow passage 9a communicating with the fluid outlet is brazed to the lower header section 3b.
(8) Each of the left and right header tanks 2 and 3 is composed of a tank body 11 having a plurality of tube insertion holes elongated in the front-rear direction, and aluminum closing members 12 brazed to opposite ends of the tank body 11 so as to close the openings at the opposite ends. The tank body 11 is composed of an aluminum pipe having a brazing material layer at least on the outer surface of the pipe; for example, a tubular member manufactured as follows. A blank plate formed of an aluminum brazing sheet having a brazing material layer on each of opposite surfaces thereof is formed into a tubular shape, and opposite side edge portions of the blank plate are caused to overlap partially, and are brazed to each other. Notably, the details of the header tank bodies 11 are not shown. Also, each of the header tank bodies 11 may be an aluminum extruded tube having a brazing material which is thermal-splayed onto the outer circumferential surface thereof.
(9) As shown in
(10) The condenser 1 is manufactured by, for example, the following method.
(11) First, the heat exchange tubes 4, the fins 5, the side plates 6, the partition members 7, a pair of tubular header tank body members each formed of aluminum and having a brazing material layer at least on the outer surface thereof, the closing members 12, the inlet member 8, and the outlet member 9 are prepared. A plurality of tube insertion holes are formed in each of the header tank body members.
(12) Each of the heat exchange tubes 4 is formed through extrusion of an alloy which contains Mn in an amount of 0.2 to 0.3 mass %, Cu in an amount of 0.1 mass % or less, Fe in an amount of 0.2 mass % or less, and Si in an amount of 0.2 mass % or less, the balance being Al and unavoidable impurities. The peripheral wall of each heat exchange tube 4 has a thickness of 200 M or less. In some cases, the thickness of the peripheral wall of each heat exchange tube 4 is not constant over the entire tube and changes locally. The expression the peripheral wall of each heat exchange tube 4 has a thickness of 200 m or less means that the thickness of the thickest portion of the peripheral wall is 200 m or less. Each of the fins 5 is formed of a brazing sheet composed of a core formed of aluminum and a skin layer formed of aluminum brazing material and covering opposite surfaces of the core.
(13) Also, a dispersion is prepared by mixing and dispersing flux powder and Zn powder into a binder. The Zn powder has an average particle size of 3 to 5 m and a maximum particle size of less than 10 m. The flux powder is a non-corrosive fluoride-based flux mainly formed of a mixture of KAlF.sub.4 and KAlF.sub.5. The binder is a solution obtained by, for example, dissolving acrylic resin into 3-methoxy-3-methyl-1-butanol. Notably, in order to adjust the viscosity of the binder, 3-methoxy-3-methyl-1-butanol is added to the dispersion as a diluent.
(14) Next, the dispersion is applied to the outer surface of each heat exchange tube 4, and the liquid component of the dispersion is evaporated, whereby the Zn powder and the flux powder are caused to adhere to the outer surface of each heat exchange tube 4 in such a manner that the adhering amount of the Zn powder becomes 1 to 3 g/m.sup.2, the adhering amount of the flux powder becomes 15 g/m.sup.2 or less, and the ratio of the adhering amount of the flux powder to the adhering amount of the Zn powder becomes (the flux powder adhering amount/the Zn powder adhering amount) becomes 1 or greater. The following two methods can be used so as to cause the Zn powder and the flux powder to adhere to the outer surface of each heat exchange tube 4. According to the first method, the dispersion is applied to the outer surface of each heat exchange tube 4 by mean of spraying, and the heat exchange tube 4 is then heated and dried so as to evaporate the liquid component of the dispersion, to thereby cause the Zn powder and the flux powder to adhere to the outer surface of the heat exchange tube 4. According to the second method, the outer surface of each heat exchange tube 4 is heated in advance, the dispersion is applied to the outer surface of the heat exchange tube 4 by mean of roll coating, and the heat exchange tube 4 is then heated and dried so as to evaporate the liquid component of the dispersion, to thereby cause the Zn powder and the flux powder to adhere to the outer surface of the heat exchange tube 4.
(15) Next, the pair of header tank body members each having tube insertion holes are disposed in such a manner that they are spaced from each other. Subsequently, the closing members 12 are disposed at the opposite ends of the header tank body members, and the partition members 7 are disposed in the header tank body members. Thus, header tank members are prepared. Also, the heat exchange tubes 4 and the fins 5 are disposed alternatingly, and opposite end portions of the heat exchange tubes 4 are inserted into the tube insertion holes of the header tank members. Further, the side plates 6 are disposed on the outer sides of the fins 5 at the opposite ends, and the inlet member 8 and the outlet member 9 are disposed.
(16) Subsequently, the header tank members, each of which is composed of the header tank body member, the closing members 12, and the partition member 7, the heat exchange tubes 4, the fins 5, the side plates 6, the inlet member 8, and the outlet member 9 are provisionally fixed together, whereby a provisionally fixed assembly is formed.
(17) After that, the provisionally fixed assembly is disposed in a brazing furnace, and is heated to a predetermined temperature within the furnace. Notably, when necessary, flux is applied to components other than the heat exchange tubes 4 by means of brush coating.
(18) When the temperature of the provisionally fixed assembly reaches a brazing temperature as a result of the heating, the flux powder melts. As a result, the fins 5, the heat exchange tubes 4, and the side plates 6 are brazed together by making use of the molten flux and the skin layers of the fins 5. Also, by making use of the brazing material of the header tank body members, the heat exchange tubes 4 are brazed to the header tank body members, and the closing members 12 and the partition members 7 are brazed to the header tank body members. Simultaneously, the molten flux on the outer surface of each heat exchange tube 4 flows and spreads, and the molten Zn on the outer surface of each heat exchange tube 4 also flows and spreads. As a result, Zn diffuses into an outer surface layer portion of the peripheral wall 13 of each heat exchange tube 4, whereby the Zn diffused layer 14 is formed. In this manner, the condenser 1 is manufactured.
(19) Next, concrete examples of the present invention will be described together with a comparative example.
EXAMPLES
(20) Heat exchange tubes formed of extrudate, having a cross-sectional shape shown in
(21) Also, there were prepared a non-corrosive fluoride-based flux powder containing a mixture of KAlF.sub.4 and KAlF.sub.5 (the amount of KAlF.sub.5 in the mixture: 10 to 40 mass %) in an amount of 90 mass % or more; a Zn powder having an average particle size of 3 to 5 m and a maximum particle size of 10 m (the Zn powder contained zinc oxide in amount of 5 mass %); a binder which was a solution obtained by dissolving acrylic resin into 3-methoxy-3-methyl-1-butanol; and a diluent composed of 3-methoxy-3-methyl-1-butanol. The Zn powder and the non-corrosive flux powder were mixed and dispersed into the binder and the diluent, whereby a dispersion was obtained. The weight ratio of all the components of the dispersion is such that the Zn powder:the non-corrosive flux powder:the binder:the diluent are 15 parts by weight: 45 parts by weight: 40 parts by weight: 27 parts by weight.
(22) Subsequently, the dispersion was applied to the outer surface of each heat exchange tube by means of spraying, and was dried in a drier so as to evaporate the liquid component of the dispersion, whereby the Zn powder and the flux powder were caused to adhere to the outer surface of each heat exchange tube in such a manner that the adhering amount of the Zn powder became 1 to 3 g/m.sup.2, and the adhering amount of the flux powder became 9 g/m.sup.2 or less. At that time, the dispersion was applied to the outer surface of each heat exchange tube by means of spraying in such a manner that the adhering amount of the Zn powder became 1 g/m.sup.2, 2 g/m.sup.2, or 3 g/m.sup.2.
(23) After that, the plurality of heat exchange tubes and the plurality of corrugated fins were alternatively stacked and combined, and the heat exchange tubes and the corrugated fins were heated within a furnace filled with nitrogen gas in such a manner that the heat exchange tubes and the corrugated fins were maintained at 580 to 600 C. (actual temperature) for 3 minutes. Thus, the heat exchange tubes and the corrugated fins were brazed together, whereby a brazed assembly was obtained. The brazed assembly was obtained for each of three different Zn powder adhering amounts.
(24) The Zn diffused layer formed in the outer surface layer portion of each heat exchange tube in each of the obtained three brazed assemblies was investigated. As a result, it was found that the Zn concentration at the outermost surface falls within a range of 0.57 to 1.4 mass %, and the thickness of the Zn diffused layer falls within a range of 60 to 105 m.
(25) Also, it was found that the spontaneous potential of the Zn diffused layer formed in the outer surface layer portion of each heat exchange tube in each of the three brazed assemblies falls within a range of 914 to 868 mV, and the spontaneous potential of a portion of the peripheral wall of each heat exchange tube located on the inner side of the Zn diffused layer is 766 mV.
Comparative Example
(26) Heat exchange tubes formed of an aluminum extrudate, having a cross-sectional shape shown in
(27) Subsequently, a Zn film is formed on the outer surface of each heat exchange tube by means of thermal spraying.
(28) After that, a plurality of heat exchange tubes and a plurality of corrugated fins having the same configuration as that used in the above-described example were alternatively stacked and combined, and the heat exchange tubes and the corrugated fins were heated within a furnace filled with nitrogen gas in such a manner that the heat exchange tubes and the corrugated fins were maintained at 580 to 600 C. (actual temperature) for 3 minutes. Thus, the heat exchange tubes and the corrugated fins were brazed together.
(29) The Zn diffused layer formed in the outer surface layer portion of each heat exchange tube in the obtained brazed assembly was investigated. As a result, it was found that the Zn concentration at the outermost surface falls within a range of 1.0 to 2.5 mass %, and the thickness of the Zn diffused layer falls within a range of 85 to 105 m.
(30) Evaluation Test:
(31) For the brazed assembly of the heat exchange tubes and the corrugated fins obtained in the example (the case where the Zn powder adhering amount is 2 g/m.sup.2) and the brazed assembly of the heat exchange tubes and the corrugated fins obtained in the comparative example, a salt spray text prescribed in JASO (Japanese Automotive Standards Organization) M609 and M610 was performed for 336 days, and the state of corrosion was investigated. Table 1 shows the results of the test.
(32) TABLE-US-00001 TABLE 1 Test period (days) 56 84 112 168 336 Examples Maximum 55 55 55 55 55 corrosion depth (m) Maximum 0.077 0.140 0.164 0.207 corrosion volume (mm.sup.3) Zn diffusion 8.3 19.8 23.5 30.6 layer dissipa- tion ratio (%) Comparative Maximum 75 75 75 75 75 Example corrosion depth (m) Maximum 0.221 0.324 corrosion volume (mm.sup.3) Zn diffusion 19.7 22.5 layer dissipa- tion ratio (%)
(33) As shown in Table 1, the developed product is smaller in the maximum corrosion depth at which the progress of corrosion of the Zn diffused layer stops and the speed at which the corrosion volume increases, as compared with the comparative product, and the Zn diffused layer dissipation ratio of the developed product is approximately equal to that of the comparative product. Accordingly, it is found that the developed product has an enhanced pitting corrosion resistance as compared with the comparative product, and can prolong the period during which occurrence of pitting corrosion is prevented.
(34) The heat exchanger according to the present invention can be preferably used as a condenser for a car air conditioner mounted on an automobile.