JPH0628768B2 - Heat exchanger material and heat exchanger manufacturing method - Google Patents
Heat exchanger material and heat exchanger manufacturing methodInfo
- Publication number
- JPH0628768B2 JPH0628768B2 JP6178085A JP6178085A JPH0628768B2 JP H0628768 B2 JPH0628768 B2 JP H0628768B2 JP 6178085 A JP6178085 A JP 6178085A JP 6178085 A JP6178085 A JP 6178085A JP H0628768 B2 JPH0628768 B2 JP H0628768B2
- Authority
- JP
- Japan
- Prior art keywords
- inorganic
- heat exchanger
- coating
- water
- aluminum material
- 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
Links
- 239000000463 material Substances 0.000 title claims description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 22
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 22
- 239000011248 coating agent Substances 0.000 claims description 22
- 238000000576 coating method Methods 0.000 claims description 22
- 229910052816 inorganic phosphate Inorganic materials 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Substances OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 5
- -1 phosphoric acid compound Chemical class 0.000 claims description 5
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 4
- 229910000838 Al alloy Inorganic materials 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims 2
- 238000000034 method Methods 0.000 claims 1
- 238000000465 moulding Methods 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 description 15
- 239000007864 aqueous solution Substances 0.000 description 12
- 239000000243 solution Substances 0.000 description 10
- 238000005238 degreasing Methods 0.000 description 9
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 6
- 229910019142 PO4 Inorganic materials 0.000 description 5
- 238000007602 hot air drying Methods 0.000 description 5
- 239000010452 phosphate Substances 0.000 description 5
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 5
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 4
- 229910001593 boehmite Inorganic materials 0.000 description 4
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 4
- 229910052809 inorganic oxide Inorganic materials 0.000 description 4
- 239000010410 layer Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 235000019832 sodium triphosphate Nutrition 0.000 description 3
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- ACVYVLVWPXVTIT-UHFFFAOYSA-M phosphinate Chemical compound [O-][PH2]=O ACVYVLVWPXVTIT-UHFFFAOYSA-M 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 2
- MOMKYJPSVWEWPM-UHFFFAOYSA-N 4-(chloromethyl)-2-(4-methylphenyl)-1,3-thiazole Chemical compound C1=CC(C)=CC=C1C1=NC(CCl)=CS1 MOMKYJPSVWEWPM-UHFFFAOYSA-N 0.000 description 1
- KWSLGOVYXMQPPX-UHFFFAOYSA-N 5-[3-(trifluoromethyl)phenyl]-2h-tetrazole Chemical compound FC(F)(F)C1=CC=CC(C2=NNN=N2)=C1 KWSLGOVYXMQPPX-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 229910019093 NaOCl Inorganic materials 0.000 description 1
- CYTYCFOTNPOANT-UHFFFAOYSA-N Perchloroethylene Chemical group ClC(Cl)=C(Cl)Cl CYTYCFOTNPOANT-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000004115 Sodium Silicate Substances 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical group [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 239000010407 anodic oxide Substances 0.000 description 1
- 238000002048 anodisation reaction Methods 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 150000007514 bases Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- OPRRNVSAMYPTIT-UHFFFAOYSA-N dicalcium;dioxidophosphanyl phosphite Chemical compound [Ca+2].[Ca+2].[O-]P([O-])OP([O-])[O-] OPRRNVSAMYPTIT-UHFFFAOYSA-N 0.000 description 1
- XPPKVPWEQAFLFU-UHFFFAOYSA-J diphosphate(4-) Chemical compound [O-]P([O-])(=O)OP([O-])([O-])=O XPPKVPWEQAFLFU-UHFFFAOYSA-J 0.000 description 1
- 235000011180 diphosphates Nutrition 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000008235 industrial water Substances 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000010409 ironing Methods 0.000 description 1
- 125000005341 metaphosphate group Chemical group 0.000 description 1
- 150000004712 monophosphates Chemical class 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- MPNNOLHYOHFJKL-UHFFFAOYSA-K peroxyphosphate Chemical compound [O-]OP([O-])([O-])=O MPNNOLHYOHFJKL-UHFFFAOYSA-K 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 229940048084 pyrophosphate Drugs 0.000 description 1
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 1
- 229910001379 sodium hypophosphite Inorganic materials 0.000 description 1
- 235000019983 sodium metaphosphate Nutrition 0.000 description 1
- 229940048086 sodium pyrophosphate Drugs 0.000 description 1
- 229910052911 sodium silicate Inorganic materials 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 229950011008 tetrachloroethylene Drugs 0.000 description 1
- RYCLIXPGLDDLTM-UHFFFAOYSA-J tetrapotassium;phosphonato phosphate Chemical compound [K+].[K+].[K+].[K+].[O-]P([O-])(=O)OP([O-])([O-])=O RYCLIXPGLDDLTM-UHFFFAOYSA-J 0.000 description 1
- 235000019818 tetrasodium diphosphate Nutrition 0.000 description 1
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 1
- WODGXFMUOLGZSY-UHFFFAOYSA-J tetrasodium phosphonatooxy phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OOP([O-])([O-])=O WODGXFMUOLGZSY-UHFFFAOYSA-J 0.000 description 1
- SDVHRXOTTYYKRY-UHFFFAOYSA-J tetrasodium;dioxido-oxo-phosphonato-$l^{5}-phosphane Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)P([O-])([O-])=O SDVHRXOTTYYKRY-UHFFFAOYSA-J 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- OHRVKCZTBPSUIK-UHFFFAOYSA-N tridodecyl phosphate Chemical compound CCCCCCCCCCCCOP(=O)(OCCCCCCCCCCCC)OCCCCCCCCCCCC OHRVKCZTBPSUIK-UHFFFAOYSA-N 0.000 description 1
- UNXRWKVEANCORM-UHFFFAOYSA-I triphosphate(5-) Chemical compound [O-]P([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O UNXRWKVEANCORM-UHFFFAOYSA-I 0.000 description 1
- YIMLBCZMANVZLU-UHFFFAOYSA-K tripotassium;oxido phosphate Chemical compound [K+].[K+].[K+].[O-]OP([O-])([O-])=O YIMLBCZMANVZLU-UHFFFAOYSA-K 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Chemical Treatment Of Metals (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、例えば自動車等の熱交換器あるいは家電用冷
熱機器に使用される熱交換器材料及び熱交換器製造法に
関するものである。Description: TECHNICAL FIELD The present invention relates to a heat exchanger material and a heat exchanger manufacturing method used for a heat exchanger such as an automobile or a cooling / heating device for home electric appliances.
アルミニウム又はアルミニウム合金(以下単にアルミニ
ウム)製の熱交換器は、例えばアルミニウム材表面に無
機質、有機質又はこれら複合系の親水性(水濡れ性の良
い)皮膜を形成し、この親水性皮膜の形成されたアルミ
ニウム材をプレス加工して熱交換器用フィンを形成し、
そしてその後プレス加工工程で表面に付着したプレス油
を中性若しくは弱アルカリ性洗剤水溶液又は非水系溶剤
(例えばパークロルエチレン、トリクロルエチレン、ト
リクロルエタン)で脱脂し、そしてこれを組み立てるこ
とによって作られている。A heat exchanger made of aluminum or an aluminum alloy (hereinafter simply referred to as aluminum) forms, for example, an inorganic material, an organic material or a composite type hydrophilic (water wettable) film on the surface of an aluminum material, and the hydrophilic film is formed. The aluminum material is pressed to form the fins for the heat exchanger,
Then, the press oil adhered to the surface in the press working step is degreased with a neutral or weak alkaline detergent aqueous solution or a non-aqueous solvent (for example, perchlorethylene, trichloroethylene, trichloroethane), and then assembled by assembling it. .
ところで、熱交換器の熱交換効率の向上及び小型化の為
に、フィンピッチは縮少する傾向にあり、このような場
合エバポレーターにおいては大気中の水分のフィンへの
凝縮によって通風抵抗の増大、騒音の発生、凝縮水の室
内への吹き出しが生じ、又、冬期においては室外におけ
る除霜エネルギーの増大の問題が大きく起きてくること
より、フィン表面の水濡れ性を良くしておくことが極め
て重要である。By the way, in order to improve the heat exchange efficiency and miniaturization of the heat exchanger, the fin pitch tends to be reduced, and in such a case, in the evaporator, the ventilation resistance is increased due to the condensation of moisture in the atmosphere into the fins, Noise is generated, condensed water is blown out into the room, and the problem of increasing defrosting energy outside the room is a serious problem in winter, so it is extremely important to improve the water wettability of the fin surface. is important.
本発明者は、上記のような点を満足する技術手段を開発
し、先に提案(特開昭58−106396号)したのであるが、
この技術手段にあっても多少の問題点が残されていた。
すなわち、特開昭58−106396号公報提案のプレコートフ
ィン材をプレス成形加工後トリクロルエチレン等の有機
溶剤で洗浄し、組み立ててエバポレーターとした所、脱
脂条件、表面酸化皮膜の形態及び性状によっては良好な
親水性の得られにくいことがわかってきた。The present inventor has developed a technical means satisfying the above points and previously proposed it (Japanese Patent Laid-Open No. 58-106396).
Even with this technical means, some problems remained.
That is, when the pre-coated fin material proposed in JP-A-58-106396 is washed with an organic solvent such as trichloroethylene after press forming and assembled into an evaporator, it is good depending on degreasing conditions, surface oxide film morphology and properties. It has been found that it is difficult to obtain sufficient hydrophilicity.
本発明者は、前記問題点の研究を行なった結果、この問
題点発生の原因は、アルミニウム材表面の無機系皮膜の
多孔性によって洗浄時に微細孔中に侵入かつ吸着したプ
レス油の除去が不充分となり、この為無機系皮膜自身の
良好なる親水性が阻害される為であることを究明し、そ
してさらに研究を続けた結果、アルミニウム材表面に水
濡れ性の良い無機系皮膜を形成し、該無機系皮膜表面に
無機リン酸化合物を介在させておくと、洗浄条件、皮膜
の形態及び性状によらず皮膜自身の親水性が阻害され
ず、前記問題点がほとんど解決されることを見い出し
た。As a result of researching the above-mentioned problems, the present inventor has found that the cause of this problem is that the removal of the press oil that has penetrated into and adsorbed into the fine pores during cleaning due to the porosity of the inorganic coating on the surface of the aluminum material is unsuccessful. Sufficient, for this reason, it was clarified that the good hydrophilicity of the inorganic coating itself is obstructed, and as a result of further research, the inorganic coating with good water wettability was formed on the surface of the aluminum material. It has been found that by interposing an inorganic phosphate compound on the surface of the inorganic coating, the hydrophilicity of the coating itself is not impaired regardless of the washing conditions, the morphology and the properties of the coating, and the above problems are almost solved. .
尚、ここで水濡れ性良好な無機系皮膜とは、例えば陽極
酸化皮膜、ベーマイト系皮膜、ベーマイト処理又は陽極
酸化処理後ケイ酸塩処理した皮膜、若しくはシリカゾル
処理した皮膜、クロメート処理後ケイ酸塩処理した皮
膜、ケイ酸塩塗布皮膜、シリカゾル水溶液による皮膜、
あるいは特開昭58−106397号開示のような酸化剤を添加
した浴で生成した酸化皮膜等があり、これらの無機質系
皮膜は、例えば陽極酸化皮膜の場合にあっては約100〜2
00Åの孔径を、ベーマイト系皮膜の場合にあっては約50
0〜1000Åの孔径を、ケイ酸塩処理した皮膜の場合にあ
っては約3000〜10000Åの孔径を有しているといったよ
うに微細孔を有する多孔性のものであり、そして無機質
系皮膜の厚みは約2〜10mg/dm2のものであることが特に
望ましいものである。Incidentally, the inorganic coating having good water wettability is, for example, an anodized coating, a boehmite coating, a coating treated with silicate after boehmite treatment or anodization, or a coating treated with silica sol, a silicate treated with chromate. Treated film, silicate coating film, silica sol aqueous solution film,
Alternatively, there is an oxide film formed in a bath containing an oxidizing agent as disclosed in JP-A-58-106397, and these inorganic films are, for example, about 100 to 2 in the case of an anodic oxide film.
A hole diameter of 00Å is about 50 for boehmite type film.
It has a pore size of 0 to 1000Å, and in the case of a silicate-treated film, it has a pore size of about 3000 to 10000Å and is porous, and the thickness of the inorganic coating is Is particularly preferred to be about 2-10 mg / dm 2 .
又、上記無機系皮膜表面に介在させられる無機リン酸化
合物は、例えば無機リン酸塩を含有する溶液で処理して
乾燥することによって形成される。The inorganic phosphoric acid compound that is present on the surface of the inorganic coating is formed, for example, by treating with a solution containing an inorganic phosphate and drying.
尚、上記処理は、例えばK、Na、Ca等のリン酸塩を脱イ
オン水、上水、工業用水等の水に溶かし、このリン酸塩
水溶液を用いて浸漬手段、塗布手段あるいはシャワー手
段等によって行なえば良い。In the above treatment, for example, a phosphate such as K, Na or Ca is dissolved in water such as deionized water, tap water or industrial water, and the aqueous phosphate solution is used for dipping, coating or showering. It should be done by.
尚、ここで無機リン酸塩としては、例えば次亜リン酸
塩、オルト亜リン酸塩、ピロ亜リン酸塩、メタ亜リン酸
塩、次リン酸塩、オルトリン酸塩、メタリン酸塩、モノ
ペルオキシリン酸塩、ペルオキシ2リン酸塩、トリポリ
リン酸塩、テトラポリリン酸塩、ピロリン酸塩等1種又
は2種以上の適宜なものが用いられる。Here, as the inorganic phosphate, for example, hypophosphite, orthophosphite, pyrophosphite, metaphosphite, hypophosphite, orthophosphate, metaphosphate, monophosphate One or more appropriate substances such as peroxyphosphate, peroxydiphosphate, tripolyphosphate, tetrapolyphosphate, and pyrophosphate are used.
そして、この際無機リン酸塩溶液としては約50ppm〜溶
解度限、望ましくは約1〜5%の濃度のものを用いて、
温度約10℃〜沸騰温度、望ましくは約約20〜80℃で、時
間約1秒〜10分、望ましくは約5〜20秒で、pH約2〜1
2、望ましくは約4〜9、より一層望ましくは約6〜8
で行なえば良い。尚、pH調整は、リン酸塩の塩基性度又
は酸性度を考慮して、リン酸、NaOH、KOH、Ca(OH)2等の
塩基性化合物を添加して行えば良い。Then, at this time, as the inorganic phosphate solution, use a solution having a concentration of about 50 ppm to the solubility limit, preferably about 1 to 5%,
The temperature is about 10 ° C to the boiling temperature, preferably about 20 to 80 ° C, the time is about 1 second to 10 minutes, preferably about 5 to 20 seconds, and the pH is about 2-1.
2, preferably about 4-9, and more preferably about 6-8
You can do it in. The pH may be adjusted by adding a basic compound such as phosphoric acid, NaOH, KOH or Ca (OH) 2 in consideration of the basicity or acidity of the phosphate.
そして、例えば上記のような処理によって無機系皮膜層
表面に形成される無機リン酸化合物層は、この無機リン
酸化合物層による効果を大きく発揮させる為にはある程
度の厚みがあることが必要であり、この厚みはP付着量
に換算して例えば1mg/m2以上、さらに望ましくは約5
〜150mg/m2あることが望ましい。Then, for example, the inorganic phosphate compound layer formed on the surface of the inorganic coating layer by the treatment as described above needs to have a certain thickness in order to exert the effect of the inorganic phosphate compound layer to a great extent. This thickness is, for example, 1 mg / m 2 or more, more preferably about 5 in terms of the amount of adhered P.
It is desirable to be ~ 150 mg / m 2 .
そして、上記のように水濡れ性の良い無機系皮膜及びこ
の無機系皮膜の表面に無機リン酸化合物層の形成された
アルミニウム材より熱交換器を作るには、上記プレコー
ト処理されたアルミニウム材をドローレスプレス加工、
ドロープレス加工、その他打抜き又はフレアー等適宜な
加工が行なわれて所定形状のフィンに成形し、このプレ
ス加工後に付着しているプレス油を中性又は弱アルカリ
洗剤水溶液若しくはトリクロルエチレン等の有機溶剤で
洗浄除去することによって作られ得る。Then, in order to make a heat exchanger from an inorganic film having good water wettability as described above and an aluminum material having an inorganic phosphate compound layer formed on the surface of the inorganic film, the precoated aluminum material is used. Drawless press processing,
Draw press processing, or other appropriate processing such as punching or flaring is performed to form fins of a predetermined shape, and the press oil attached after this press processing is neutral or weak alkaline detergent aqueous solution or organic solvent such as trichloroethylene. It can be made by washing away.
そして、このようにして製造される熱交換器は、無機系
皮膜の表面に無機リン酸化合物層のある素材が用いられ
たものであることより、微細孔表面の極性が変性され、
プレス油が洗浄中に吸着しにくいものとなっていて、無
機系皮膜表面の水濡れ性があまり低下しておらず、従っ
て熱交換効率の良いものである。又、プレス油除去の為
の煩雑な工程を要しないことより、製造能率よく低コス
トで熱交換器を提供できるようになる。Then, the heat exchanger manufactured in this manner, the material having an inorganic phosphate compound layer on the surface of the inorganic coating is used, the polarity of the micropore surface is modified,
Since the press oil is less likely to be adsorbed during washing, the wettability of the inorganic coating surface with water is not so lowered, and therefore the heat exchange efficiency is good. Further, since the complicated step for removing the press oil is not required, it becomes possible to provide the heat exchanger with high manufacturing efficiency and at low cost.
〔実施例1〕 JIS1200-H26アルミニウム材(巾800mm、長さ8000m、厚
さ0.115mm)を次亜塩素酸ナトリウム水溶液(NaOCl濃度
200ppm、pH10.5)中に約85℃の温度下で浸漬し、次いで
pH11.4の1.5%の水ガラス溶液中に約60℃の温度下で浸
漬し、その後シャワー水洗工程を経て表面に約7mg/dm2
厚の水濡れ性良好な無機系の酸化皮膜を形成する。[Example 1] JIS1200-H26 aluminum material (width 800 mm, length 8000 m, thickness 0.115 mm) was used as a sodium hypochlorite aqueous solution (NaOCl concentration
200ppm, pH 10.5) at a temperature of about 85 ° C, then
It is immersed in a 1.5% water glass solution of pH 11.4 at a temperature of about 60 ° C., and then showered with water to give a surface treatment of about 7 mg / dm 2
A thick inorganic oxide film with good wettability is formed.
次に、上記酸化皮膜の形成されたアルミニウム材表面
に、温度25〜30℃、濃度1000ppmのトリポリリン酸ナト
リウム水溶液を塗布し、その後150℃で10秒間熱風乾燥
を行ない、P付着量としてい10mg/m2厚の無機リン酸化
合物を付着させる。Next, an aqueous solution of sodium tripolyphosphate having a temperature of 25 to 30 ° C. and a concentration of 1000 ppm is applied to the surface of the aluminum material on which the oxide film is formed, and then hot air drying is performed at 150 ° C. for 10 seconds to obtain a P adhesion amount of 10 mg / Deposit m 2 thick inorganic phosphate compound.
そして、上記無機リン酸化合物の付いたアルミニウム材
にしごき加工を中心としたドローレスプレス加工を施し
てフィンを製造し、その後トリクロルエチレンで脱脂処
理(85℃、1分間)を行ない、そして熱交換器に組み立
てる。Then, the aluminum material with the above-mentioned inorganic phosphate compound is subjected to drawless press working mainly on ironing to manufacture fins, and then degreasing treatment (85 ° C, 1 minute) is carried out with trichloroethylene, and the heat exchanger is Assemble to.
〔実施例2〕 実施例1における水濡れ性良好な無機系の酸化皮膜形成
工程と同様な工程を経て同様な酸化皮膜を形成した後、
温度50℃、濃度2000ppmのピロリン酸カリウム及び3000p
pmのテトラポリリン酸カリウムを含有した水溶液を塗布
し、その後150℃で10秒間熱風乾燥を行ない、P付着量
として20mg/m2厚の無機リン酸化合物を付着させる。Example 2 After forming a similar oxide film through the same steps as the inorganic oxide film forming step with good water wettability in Example 1,
Temperature 50 ℃, 2000ppm concentration of potassium pyrophosphate and 3000p
An aqueous solution containing pm of potassium tetrapolyphosphate is applied, followed by hot-air drying at 150 ° C. for 10 seconds to attach an inorganic phosphate compound having a P adhesion amount of 20 mg / m 2 thickness.
そして、上記無機リン酸化合物の付いたアルミニウム材
にドローレスプレス加工を施してフィンを製造し、その
後トリクロルエチレンで脱脂処理(50℃→30℃→70℃、
各1分間浸漬)を行ない、そして熱交換器に組み立て
る。Then, a fin is manufactured by subjecting the aluminum material with the inorganic phosphate compound to drawless press processing, and then degreasing treatment with trichlorethylene (50 ° C → 30 ° C → 70 ° C,
Soak for 1 minute each) and assemble in a heat exchanger.
〔実施例3〕 実施例1と同様なアルミニウム材を弱アルカリエッチン
グした後水洗乾燥し、次いでケイ酸ソーダ水溶液(SiO2
/Na2O=5、SiO2濃度55g/)に60℃で1分間浸漬塗布
後、200℃で60秒間乾燥し、表面に約8mg/dm2厚の水濡
れ性良好な無機系の酸化皮膜を形成する。Example 3 The same aluminum material as in Example 1 was weakly alkali-etched, washed with water and dried, and then an aqueous sodium silicate solution (SiO 2
/ Na 2 O = 5, SiO 2 concentration 55g /) Immersion coating at 60 ℃ for 1 minute, then dry at 200 ℃ for 60 seconds, and an inorganic oxide film of about 8 mg / dm 2 thickness with good wettability on the surface. To form.
次に、上記酸化皮膜の形成されたアルミニウム材表面
に、次亜リン酸ナトリウム、オルトリン酸ナトリウム、
テトラポリリン酸ナトリウムを各々2000ppm含有した水
溶液を塗布し、その後120℃で20秒間熱風乾燥を行な
い、P付着量として50mg/m2厚の無機リン酸化合物を付
着させる。Next, on the surface of the aluminum material on which the oxide film is formed, sodium hypophosphite, sodium orthophosphate,
An aqueous solution containing 2000 ppm each of sodium tetrapolyphosphate is applied, and then hot air drying is performed at 120 ° C. for 20 seconds to attach an inorganic phosphate compound having a P adhesion amount of 50 mg / m 2 thickness.
そして、上記無機リン酸化合物の付いたアルミニウム材
にドローレスプレス加工を施してフィンを製造し、その
後トリクロルエチレンで脱脂処理(60℃→30℃→80℃、
各1分間浸漬)を行ない、そして熱交換器に組み立て
る。And, the fins are manufactured by subjecting the aluminum material with the inorganic phosphate compound to drawless press processing, and then degreasing treatment with trichloroethylene (60 ° C → 30 ° C → 80 ° C,
Soak for 1 minute each) and assemble in a heat exchanger.
〔実施例4〕 実施例1と同様なアルミニウム材を弱アルカリエッチン
グした後水洗乾燥し、次いでトリエタノールアミン0.5
%を含む水溶液中に90℃で60秒間浸漬してベーマイト処
理を行ない、表面に約4mg/dm2厚の水濡れ性良好な無機
系の酸化皮膜を形成する。Example 4 The same aluminum material as in Example 1 was weakly alkali-etched, washed with water and dried, and then triethanolamine 0.5.
% Aqueous solution containing 90% of water for 90 seconds to perform boehmite treatment to form an inorganic oxide film having a good wettability with water and having a thickness of about 4 mg / dm 2 .
次に、上記酸化皮膜の形成されたアルミニウム材表面
に、次リン酸ナトリウム、ピロ亜リン酸カルシウム、モ
ノペルオキシリン酸カリウム、ペルオキシ2リン酸ナト
リウム、オルトリン酸ナトリウム、メタリン酸ナトリウ
ムを各々3000ppm含有した水溶液を塗布した後、80℃で2
0秒間の熱風乾燥を行ない、P付着量として80mg/m2厚の
無機リン酸化合物を付着させる。Next, an aqueous solution containing 3000 ppm each of sodium hypophosphate, calcium pyrophosphite, potassium monoperoxyphosphate, sodium peroxydiphosphate, sodium orthophosphate, and sodium metaphosphate was formed on the surface of the aluminum material on which the oxide film was formed. 2 at 80 ° C after application
Hot air drying is performed for 0 seconds to deposit an inorganic phosphate compound having a P adhesion amount of 80 mg / m 2 in thickness.
そして、上記無機リン酸化合物の付いたアルミニウム材
にドローレスプレス加工を施してフィンを製造し、その
後トリクロルエチレンで脱脂処理(40℃→30℃→ベーパ
ー、各1分間)を行ない、そして熱交換器に組み立て
る。Then, the aluminum material with the above-mentioned inorganic phosphate compound is subjected to drawless pressing to produce fins, and then degreasing treatment (40 ° C → 30 ° C → vapor, 1 minute each) is performed with trichlorethylene, and a heat exchanger Assemble to.
〔実施例5〕 JIS1050−H22アルミニウム材(巾1100mm,長さ5000m、
厚さ0.120mm)にクロメート2%水溶液(日本ペイント
(株)製アロジン#1200)を35℃で20秒間スプレー処理
し、次いで2%シリカゾル水溶液中に35℃で2分間浸漬
し、表面に約5mg/dm2厚の水濡れ性良好な無機系皮膜を
形成する。[Example 5] JIS1050-H22 aluminum material (width 1100 mm, length 5000 m,
Chromate 2% aqueous solution (Nippon Paint Co., Ltd. Alodine # 1200) was spray-treated for 20 seconds at 35 ° C, and then immersed in 2% silica sol aqueous solution for 2 minutes at 35 ° C to give about 5 mg on the surface. / dm 2 Form an inorganic film with good wettability.
次に、上記皮膜の形成されたアルミニウム材表面に、ピ
ロリン酸ナトリウム、トリポリリン酸ナトリウムを各々
25000ppm含有した水溶液を塗布した後、250℃で10秒間
の熱風乾燥を行ない、P付着量として150mg/m2厚の無機
リン酸化合物を付着させる。Next, sodium pyrophosphate and sodium tripolyphosphate are respectively applied to the surface of the aluminum material on which the above film is formed.
After applying an aqueous solution containing 25000 ppm, hot air drying is performed at 250 ° C. for 10 seconds to attach an inorganic phosphate compound having a P adhesion amount of 150 mg / m 2 thickness.
そして、上記無機リン酸化合物の付いたアルミニウム材
にドロープレス加工を施してフィンを製造し、その後ト
リクロルエタンで脱脂処理(50℃→30℃→70℃、各1分
間浸漬)を行ない、そして熱交換器に組み立てる。Then, the aluminum material with the above-mentioned inorganic phosphate compound is subjected to draw press processing to manufacture fins, and then degreasing treatment (50 ° C → 30 ° C → 70 ° C, 1 minute each) is performed with trichloroethane, and heat is applied. Assemble into the exchanger.
〔比較例1〜5〕 実施例1〜5において、無機リン酸塩溶液による処理を
省略し、同様にして熱交換器を得る。[Comparative Examples 1 to 5] In Examples 1 to 5, the heat exchanger was obtained in the same manner by omitting the treatment with the inorganic phosphate solution.
〔比較例6〕 実施例1において、酸化皮膜形成工程を省略して同様に
行ない、熱交換器を得る。[Comparative Example 6] A heat exchanger is obtained in the same manner as in Example 1, except that the oxide film forming step is omitted.
〔比較例7〕 実施例1において、無機リン酸塩溶液の代りに有機系の
リン酸エステル(トリドデシルホスフェイト)5%溶液
を用いて同様に行ない、熱交換器を得る。[Comparative Example 7] A heat exchanger is obtained in the same manner as in Example 1, except that a 5% solution of an organic phosphate (tridodecyl phosphate) is used instead of the inorganic phosphate solution.
上記のようにして得た熱交換器のフィンについて、その
水濡れ性(親水性接触角)を調べると表に示す通りであ
る。The fins of the heat exchanger obtained as described above are examined for water wettability (hydrophilic contact angle), which is as shown in the table.
この表からわかるように、本実施例のものは水濡れ性の
良好なものであり。特にプレス加工後に行なう脱脂処理
が行なわれても水濡れ性は良好であり、かつ脱脂処理後
に行なう流水洗浄500時間後の親水性接触角の値からも
わかるように水濡れ性の耐久性も良いものであるのに対
し、無機リン酸塩溶液による処理を省略した比較例1〜
5、酸化皮膜形成工程を省略した比較例6及びリン酸塩
処理であってもこのリン酸塩が有機系のものである比較
例7のものではプレス加工後に行なう脱脂処理によって
水濡れ性は悪くなり、又、この水濡れ性の耐久性も悪い
ものである。 As can be seen from this table, the material of this example has good water wettability. In particular, the wettability is good even after the degreasing treatment performed after pressing, and the durability of the water wettability is also good as can be seen from the value of the hydrophilic contact angle after 500 hours of running water washing performed after the degreasing treatment. On the other hand, Comparative Example 1 in which the treatment with the inorganic phosphate solution is omitted
5, even in the comparative example 6 in which the oxide film forming step was omitted and in the comparative example 7 in which the phosphate was organic, the water wettability was poor due to the degreasing treatment performed after the press working. Moreover, the durability of this water wettability is also poor.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 金属表面技術協会編「金属表面技術便 覧」(昭和52−12−25)日刊工業新聞社発 行 P.733〜735 ─────────────────────────────────────────────────── ─── Continuation of the front page (56) References “Metal Surface Technology Handbook” edited by Japan Metal Surface Technology Association (Showa 52-12-25) Published by Nikkan Kogyo Shimbun P. 733 ~ 735
Claims (2)
に水濡れ性の良い無機系皮膜を形成し、該無機系皮膜の
表面に無機系リン酸化合物を介在させたことを特徴とす
る熱交換器材料。1. A heat exchanger material comprising an inorganic film having good wettability formed on the surface of an aluminum or aluminum alloy material, and an inorganic phosphoric acid compound being interposed on the surface of the inorganic film.
に水濡れ性の良い無機系皮膜を形成した後、該無機系皮
膜を無機系リン酸塩溶液で処理乾燥することにより無機
系皮膜の表面に無機系リン酸化合物を介在せしめ、その
後所定の成形加工を施し、この成形加工されたものを組
み立てることを特徴とする熱交換器製造法。2. An inorganic coating having good water wettability is formed on the surface of an aluminum or aluminum alloy material, and the inorganic coating is treated and dried with an inorganic phosphate solution to form an inorganic coating on the surface of the inorganic coating. A heat exchanger manufacturing method characterized in that a phosphoric acid compound is interposed, a predetermined molding process is performed thereafter, and the molded product is assembled.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6178085A JPH0628768B2 (en) | 1985-03-28 | 1985-03-28 | Heat exchanger material and heat exchanger manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6178085A JPH0628768B2 (en) | 1985-03-28 | 1985-03-28 | Heat exchanger material and heat exchanger manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61222629A JPS61222629A (en) | 1986-10-03 |
| JPH0628768B2 true JPH0628768B2 (en) | 1994-04-20 |
Family
ID=13180945
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6178085A Expired - Lifetime JPH0628768B2 (en) | 1985-03-28 | 1985-03-28 | Heat exchanger material and heat exchanger manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0628768B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0790614A (en) * | 1993-09-22 | 1995-04-04 | Elna Co Ltd | Aluminum or aluminum alloys and their chemical conversion treatment |
| JP2008038184A (en) * | 2006-08-03 | 2008-02-21 | Denso Corp | Surface treatment method and corrosion resistance structure of aluminum base material |
| JP5534951B2 (en) * | 2010-06-01 | 2014-07-02 | 三菱電機株式会社 | Heat exchanger processing method and heat exchanger |
| WO2017078832A1 (en) * | 2015-11-04 | 2017-05-11 | Illinois Tool Works Inc. | Corrosion inhibitor and water conditioning agent |
-
1985
- 1985-03-28 JP JP6178085A patent/JPH0628768B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| 金属表面技術協会編「金属表面技術便覧」(昭和52−12−25)日刊工業新聞社発行P.733〜735 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61222629A (en) | 1986-10-03 |
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