JPH0438958B2 - - Google Patents
Info
- Publication number
- JPH0438958B2 JPH0438958B2 JP18388387A JP18388387A JPH0438958B2 JP H0438958 B2 JPH0438958 B2 JP H0438958B2 JP 18388387 A JP18388387 A JP 18388387A JP 18388387 A JP18388387 A JP 18388387A JP H0438958 B2 JPH0438958 B2 JP H0438958B2
- Authority
- JP
- Japan
- Prior art keywords
- tube
- paint
- coating
- heat transfer
- film
- 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
Links
- 238000000576 coating method Methods 0.000 claims description 53
- 239000011248 coating agent Substances 0.000 claims description 49
- 239000003973 paint Substances 0.000 claims description 47
- 238000005260 corrosion Methods 0.000 claims description 25
- 239000000049 pigment Substances 0.000 claims description 22
- 229910000881 Cu alloy Inorganic materials 0.000 claims description 19
- 229920003002 synthetic resin Polymers 0.000 claims description 7
- 239000012809 cooling fluid Substances 0.000 claims description 6
- 239000000057 synthetic resin Substances 0.000 claims description 6
- 229910045601 alloy Inorganic materials 0.000 claims 1
- 239000000956 alloy Substances 0.000 claims 1
- 238000012546 transfer Methods 0.000 description 24
- 229920005989 resin Polymers 0.000 description 21
- 239000011347 resin Substances 0.000 description 21
- 230000007797 corrosion Effects 0.000 description 16
- 238000012360 testing method Methods 0.000 description 13
- 230000006866 deterioration Effects 0.000 description 11
- 239000013535 sea water Substances 0.000 description 10
- 238000004210 cathodic protection Methods 0.000 description 9
- 239000003513 alkali Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 229910001369 Brass Inorganic materials 0.000 description 6
- 239000010951 brass Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 5
- ZCDOYSPFYFSLEW-UHFFFAOYSA-N chromate(2-) Chemical compound [O-][Cr]([O-])(=O)=O ZCDOYSPFYFSLEW-UHFFFAOYSA-N 0.000 description 5
- 230000006872 improvement Effects 0.000 description 5
- 230000010287 polarization Effects 0.000 description 5
- 239000010949 copper Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 238000010422 painting Methods 0.000 description 4
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000002390 adhesive tape Substances 0.000 description 3
- 229920000180 alkyd Polymers 0.000 description 3
- 230000003373 anti-fouling effect Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 229920001225 polyester resin Polymers 0.000 description 3
- 239000004645 polyester resin Substances 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229920000620 organic polymer Polymers 0.000 description 2
- 239000002952 polymeric resin Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000005488 sandblasting Methods 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 239000004606 Fillers/Extenders Substances 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229940075397 calomel Drugs 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical compound Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 238000003703 image analysis method Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920005749 polyurethane resin Polymers 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 230000009291 secondary effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- -1 sulfur ions Chemical class 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 230000008685 targeting Effects 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Laminated Bodies (AREA)
- Protection Of Pipes Against Damage, Friction, And Corrosion (AREA)
- Rigid Pipes And Flexible Pipes (AREA)
Description
(技術分野)
本発明は、熱交換器用内面防食塗装皮膜付き銅
合金管に係り、特に管内面に形成される塗膜の防
食皮膜としての特性を何等損ねることなく、その
耐電気防食性を改善し、またその伝熱性能を向上
せしめた、伝熱管としての銅合金管に関するもの
である。
(従来技術とその問題点)
従来より、火力発電所や科学工場、或いは船舶
等の復水器やその他の各種熱交換器には、伝熱管
として、黄銅に、アルミニウム、砒素、その他ケ
イ素等を添加した、所謂特殊黄銅管や、銅、ニツ
ケル、鉄よりなる、所謂キユプロニツケル管の如
き銅合金管が広く使用されてきているが、それら
熱交換器においては、冷却水として、海水或いは
河海水を使用する関係上、それら伝熱管の内面に
は種々の腐食が発生する。そして、このような腐
食が生じると、伝熱管内面には腐食生成物を含む
付着物が付き、熱交換器の熱貫流率を低下させる
のである。
このため、かかる銅合金管を伝熱管として使用
するために、その内面を防食するための各種の手
法が提案されているが、そのなかでも、本発明者
らが、特公昭56−45079号公報、特開昭56−
166271号公報等に明らかにしたように、所定の樹
脂塗料を用いて、防食塗膜を所定の厚さで管内面
に形成させる手法は、防食性や作業性等の点にお
いて、他の手法に比べて優れており、今日、既に
実用化に至つている。
ところで、熱交換器の腐食は、かかる熱交換器
用管(伝熱管)たる銅合金管のみに止まらず、そ
の水室を構成する他の材料、例えば水室壁、弁、
管板等についても考慮する必要があるのであり、
またかかる熱交換器用管内面に所定の防食塗膜が
形成された場合といえども、該熱交換器用管内を
流通せしめられる伝熱流体(冷却流体)中に混入
する流入異物の殴打による管端部分の塗膜の剥離
を完全に防止し得ず、そしてそのような剥離が惹
起された場合に、当該剥離部には潰食、所謂イン
レツトアタツクが惹起されるところから、それら
の問題を解決するために、一般に、熱交換器の水
室には電気防食(陰極防食)装置が設置されてい
るのである。
しかしながら、そのような陰極電気防食環境下
に、所定の内面防食塗装皮膜を設けた銅合金管を
置いた場合において、かかる電気防食の条件如何
によつては、かかる内面防食塗膜に当該電気防食
作用によつて生じるアルカリ(OH-)により、
塗膜膨れ、換言すればアルカリ劣化が惹起され、
そしてこれによつて塗膜の剥離が加速される問題
が内在しており、また塗膜の伝熱抵抗値も大きく
なつて、熱貫流率が10%前後も低下することが経
験されているのである。
而して、かかるアルカリ劣化は、塗膜内を浸透
し、塗膜下の金属表面に到達した、冷却流体とし
ての海水等の中に存在するH2OやO2が、陰極電
気防食により、金属内部より金属表面に供給され
た電子と反応し、アルカリ(OH-)を発生する
ことにより惹起せしめられる塗膜劣化現象である
が、従来の塗膜では、そのような劣化現象を防止
することは困難であつたのである。
(発明の構成)
ここにおいて、本発明者らは、上記のアルカリ
劣化の対策として、塗膜内における分子、イオン
等の通過性に着目し、それを向上せしめることに
よつて、上記の反応にて生成したOH-は出来る
だけ早く塗膜から冷却流体(海水等の冷却水)側
に排除することが望ましく、そのためには、従来
の塗膜設計とは逆に極力塗膜内に欠陥を増やすこ
とが有効と考え、そしてその手段として、塗膜を
形成する樹脂塗料中に含まれる顔料分を増加せし
めて、種々検討を行なつた結果、通常の樹脂塗料
に含まれる以上に顔料分を増大せしめることによ
り、塗膜のアルカリ劣化が効果的に抑制されると
同時に、伝熱性能の向上も達成され得る事実を見
い出し、本発明を完成するに至つたのである。
すなわち、本発明は、熱交換器用内面防食塗装
皮膜付き銅合金管における内面塗膜につき、その
防食皮膜としての特性を損ねることなく、その耐
電気防食性を改善し、且つその伝熱性能を向上さ
せることを、その目的とするものであり、そのた
めに、熱交換器に取り付けられて、管内に所定の
冷却流体が流通せしめられる、伝熱管としての内
面防食塗装皮膜付き銅合金管において、かかる内
面防食塗膜皮膜を、塗料中の顔料分(P)と樹脂
固形分(B)との比率(P/B)が重量比で3〜10の
範囲内にある合成樹脂塗料を用いて形成したこと
を特徴とするものである。
このように、本発明に従う内面防食塗膜皮膜付
き銅合金管にあつては、従来の顔料分と樹脂固形
分との比率(P/B)が2〜2.5程度である樹脂
塗料に代えて、顔料分を増加させたP/B=3〜
10の合成樹脂塗料を用いて、かかる銅合金管の内
面に塗膜が形成せしめられたものであつて、管の
金属表面において発生するアルカリ(OH-)を
効果的に冷却流体側に排出し得る構造の塗膜が有
利に形成されたものであり、これによつて、アル
カリ劣化を抑制し、また熱貫流率の有効な向上を
図り得たのである。
(構成の具体的説明)
ところで、かかる本発明に用いられる銅合金管
材料としては、従来からの伝熱管として用いられ
ている管材料が何れも対象とされるものである
が、特に本発明にあつては、アルミニウム黄銅
管、例えばJIS−H−3300−C−6870、6871、
6872等のアルミニウム黄銅材料や、JIS−H−
3300−C−7060−、7150等のキユプロニツケル材
料からなる管が好適に用いられるのである。そし
て、このような銅合金管は、例えば内径が10〜40
mm程度、特に15〜25mm程度、長さが4〜40m、特
に5〜25m程度の長尺細管として用いられること
となる。
そして、このような小孔径、長尺の銅合金管に
は、その管内面に対してスプレー塗装等の塗装手
法によつて所定の樹脂塗料が均一に塗装せしめら
れ、そこに所定厚さの膜厚の防食塗膜が形成され
のであるが、本発明においては、そのような防食
塗膜が、顔料分の含有割合が増大せしめられた合
成樹脂塗料を用いた塗装操作によつて、形成され
るのである。
すなわち、このような防食塗装操作に用いられ
る合成樹脂塗料としては、一般に、常乾型(常温
乾燥型)の塗料が好適に用いられ、またそのよう
な塗料においては、皮膜形成要素として、アルキ
ツド樹脂、ビニル樹脂(塩化ビニル系、酢酸ビニ
ル系等)、ポリウレタン樹脂、エポキシ樹脂、ポ
リエステル樹脂及びアクリル樹脂(アクリル酸エ
ステル系等)からなる有機重合体樹脂(変性物を
も含む)の1種または2種以上が用いられる。か
かる有機重合体樹脂が、それに対する適当な溶剤
(例えば、アルコール系、エステル系、エーテル
系、ケトン系樹脂族或いは芳香族炭化水素系等)
に溶解され、更に顔料として、亜鉛系、酸化クロ
ム系等の防錆顔料、酸化鉄等の着色顔料、
CaCO3、Al2O3、SiO2等の体質顔料、Cu2O、Cu
等の防汚顔料等が配合されて、常温乾燥型の皮膜
形成性の液状組成物(塗料)に調製されるのであ
るが、本発明にあつては、かかる塗料中の全顔料
成分の合計量(P)と樹脂固形分(B)との比率
(P/B)が、重量比で3〜10の範囲内にある
(合成)樹脂塗料を用いるようにしたのである。
要するに、本発明は、銅合金管の内面に塗布さ
れて、目的とする防食塗膜を形成する樹脂塗料中
の前顔料分と樹脂固形分との比率(P/B)が重
量比において3〜10となるように、顔料の含有割
合を増大せしめた合成樹脂塗料を用いることによ
つて、かかる銅合金管の内面に形成される塗膜の
防食皮膜としての特性を何等損ねることなく、そ
の耐電気防食性(アルカリ劣化)の改善を図り、
更に伝熱性の向上を有利に達成し得たものであつ
て、かかるP/Bの値が3よりも小さくなると、
そのような塗膜の耐電気防食性の改良や伝熱性の
向上を充分に図り得ないのであり、またP/B値
が10よりも大きくなると、顔料の分散が不均一と
なり、塗膜の形成性が劣り、且つ塗膜が粉末化し
て、耐摩耗性に劣る等の問題を惹起することとな
る。
なお、かくの如き所定の樹脂塗料を用いて、通
常の塗装操作によつて銅合金管内面に形成される
防食塗装皮膜の厚さとしては、一般に、大きな伝
熱抵抗値を与えないような厚さにおいて、樹脂塗
料の種類に応じて適宜に決定されるものであり、
例えば最大限50〜300μm以下の塗膜厚みにおい
て、特に30μm以下の塗膜厚みにおいて、より低
い伝熱抵抗を有する内面防食塗装皮膜が形成され
ることとなる。
(実施例)
以下に、本発明の幾つかの実施例を示し、本発
明を更に具体的に明らかにすることとするが、本
発明が、そのような実施例の記載によつて何等の
制約をも受けるものでないことは、言うまでもな
いところである。
また、本発明には、以下の実施例の他にも、更
には上記の具体的記述以外にも、本発明の趣旨を
逸脱しない限りにおいて、当業者の知識に基づい
て種々なる変更、修正、改良等を加え得るもので
あることが、理解されるべきである。
なお、以下の実施例中の比及び百分率は、特に
断わりのない限り、何れも重量基準によつて示さ
れるものである。
先ず、外径:25.4mm、肉厚:1.25mm、長さ:
2500mmのアルミニウム黄銅管(JIS−H−3300−
C−6871)を供試管として、その内面に、(a)高温
DXガス(12%CO2+N2)焼鈍、(b)サンドブラス
ト処理(アルミナ粒子:150μm使用)、(c)クロメ
ート処理(2%NaCr2O7、15分間浸漬)の何れ
かの内面処理を施した。
次いで、下記第1表及び第2表に記すフタール
酸系ポリエステル樹脂塗料またはエポキシ変性ア
ルキツド樹脂塗料をベースとする22種類の塗料
(樹脂固形分は何れも50%とした)を用いて、上
記の内面処理された供試管の内面に、エアースプ
レー塗装機にて、膜厚:20μmを目標に塗装を施
し、揮発する溶剤分を強制的に管外に排除しつ
つ、塗膜形成を行なつた。なお、何れの塗料も、
室温にて硬化する常温硬化型の樹脂を用いたもの
である。
また、フタール酸系ポリエステル樹脂塗料系を
示す第1表において、試料No.1〜3が市販されて
いる塗料組成のものであつて、正規の配合比のも
のであり、これに、主として着色顔料であるベン
ガラの配合量を増大させ、且つ塗膜形成が充分に
行ない得るように体質顔料量を変化させて、試料
No.4〜13の塗料が調製された。なお、この調製さ
れた塗料は、総顔料分(P)対樹脂固形分(B)の割
合において2.2〜11.5のものである。P/Bが5.8
よりも大きくなると、粉末化の傾向が生じ始め、
11.5では有機樹脂皮膜として不適と見做された。
さらに、エポキシ変性アルキツド樹脂塗料系を
示す第2表において、試料No.14〜16が市販の塗料
組成であり、これに着色顔料(ベンガラ)、防汚
顔料(Cu)を添加して、その配合量を増大させ、
P/Bの値を3.5〜3.7付近まで増大させて、試料
No.17〜22のものが調製された。
なお、第1表及び第2表中の供試管表面仕上記
号は以下の意味を示すものである。
D:DXガス焼鈍面
S:サンドブラスト面
C:クロメート面
(Technical field) The present invention relates to a copper alloy tube with an inner surface anticorrosive coating for heat exchangers, and in particular improves the electrical corrosion resistance of the coating formed on the inner surface of the tube without impairing its properties as an anticorrosive coating. The present invention also relates to a copper alloy tube as a heat transfer tube, which has improved heat transfer performance. (Prior art and its problems) Traditionally, heat transfer tubes made of brass, aluminum, arsenic, silicon, etc. have been used in condensers and other heat exchangers for thermal power plants, scientific factories, ships, etc. So-called special brass tubes with additives and copper alloy tubes made of copper, nickel, and iron, such as so-called Cypronickel tubes, have been widely used, but in these heat exchangers, seawater or river seawater is used as cooling water. Due to usage, various types of corrosion occur on the inner surfaces of these heat transfer tubes. When such corrosion occurs, deposits containing corrosion products adhere to the inner surfaces of the heat exchanger tubes, reducing the heat transfer coefficient of the heat exchanger. For this reason, in order to use such copper alloy tubes as heat transfer tubes, various methods have been proposed to prevent corrosion on the inner surface of the tubes. , Japanese Patent Publication No. 1983-
As disclosed in Publication No. 166271, etc., the method of forming an anticorrosive coating film on the inner surface of a pipe with a predetermined thickness using a predetermined resin paint is superior to other methods in terms of corrosion resistance and workability. It is superior in comparison and has already been put into practical use today. By the way, corrosion of a heat exchanger is not limited to the copper alloy tube that is the heat exchanger tube (heat transfer tube), but also to other materials that make up the water chamber, such as the water chamber wall, valves,
It is also necessary to consider the tube plate, etc.
In addition, even if a predetermined anticorrosion coating film is formed on the inner surface of the heat exchanger tube, the end portion of the tube may be damaged due to damage caused by inflow foreign matter mixed into the heat transfer fluid (cooling fluid) flowing through the heat exchanger tube. If peeling of the paint film cannot be completely prevented, and if such peeling occurs, erosion, so-called inlet attack, will occur in the peeled area, so these problems can be solved. To do this, a cathodic protection device is generally installed in the water chamber of the heat exchanger. However, when a copper alloy pipe with a predetermined inner surface anti-corrosion coating is placed in such a cathodic protection environment, depending on the conditions of the cathodic protection, the inner surface corrosion protection coating may Due to the alkali (OH - ) produced by the action,
Paint film blistering, in other words, alkali deterioration is caused,
This has the inherent problem of accelerating the peeling of the paint film, and also increases the heat transfer resistance of the paint film, which has been experienced as reducing the heat transfer coefficient by around 10%. be. Such alkaline deterioration is caused by cathodic protection caused by H 2 O and O 2 present in seawater, etc. as a cooling fluid that penetrates the paint film and reaches the metal surface under the paint film. This is a paint film deterioration phenomenon that is caused by reacting with electrons supplied to the metal surface from inside the metal and generating alkali (OH - ), but with conventional paint films, such deterioration phenomenon cannot be prevented. It was difficult. (Structure of the Invention) Here, as a countermeasure against the above-mentioned alkali deterioration, the present inventors focused on the permeability of molecules, ions, etc. within the coating film, and by improving it, the above-mentioned reaction could be prevented. It is desirable to remove the generated OH - from the paint film to the cooling fluid (cooling water such as seawater) as quickly as possible.To do this, it is necessary to increase defects in the paint film as much as possible, contrary to conventional paint film design. We thought that this would be effective, and as a means to do so, we increased the pigment content in the resin paint that forms the coating film.As a result of various studies, we decided to increase the pigment content beyond that contained in ordinary resin paints. The inventors discovered the fact that by increasing the amount of heat transfer, the alkali deterioration of the coating film can be effectively suppressed, and at the same time, the heat transfer performance can be improved, leading to the completion of the present invention. That is, the present invention improves the electrical corrosion resistance and heat transfer performance of the internal coating film of a copper alloy tube with an internal anticorrosive coating for a heat exchanger, without impairing its properties as an anticorrosive coating. For this purpose, in a copper alloy tube with an inner surface anti-corrosion coating as a heat transfer tube, which is installed in a heat exchanger and allows a prescribed cooling fluid to flow inside the tube, such inner surface is The anticorrosion coating film is formed using a synthetic resin paint in which the ratio (P/B) of the pigment content (P) to the resin solid content (B) in the paint is within the range of 3 to 10 by weight. It is characterized by: As described above, in the case of the copper alloy tube with the inner surface anticorrosion coating film according to the present invention, instead of the conventional resin paint having a ratio of pigment content to resin solid content (P/B) of about 2 to 2.5, P/B with increased pigment content = 3~
A coating film is formed on the inner surface of such a copper alloy tube using synthetic resin paint No. 10, which effectively discharges alkali (OH - ) generated on the metal surface of the tube to the cooling fluid side. The resulting coating film was advantageously formed, thereby suppressing alkali deterioration and effectively improving the heat transfer coefficient. (Specific explanation of the structure) By the way, as the copper alloy tube material used in the present invention, any tube material conventionally used for heat exchanger tubes is applicable, but the present invention particularly In some cases, aluminum brass tubes, such as JIS-H-3300-C-6870, 6871,
Aluminum brass materials such as 6872, JIS-H-
Tubes made of Cypronickel materials such as 3300-C-7060- and 7150 are preferably used. And such copper alloy tubes, for example, have an inner diameter of 10~40
It will be used as a long thin tube with a length of about mm, especially about 15 to 25 mm, and a length of about 4 to 40 m, especially about 5 to 25 m. Then, on such a long copper alloy tube with a small hole diameter, a prescribed resin paint is uniformly applied to the inner surface of the tube by a painting method such as spray painting, and a film of a prescribed thickness is applied thereto. A thick anti-corrosion coating film is formed, but in the present invention, such an anti-corrosion coating film is formed by a coating operation using a synthetic resin paint with an increased content of pigments. It is. In other words, as the synthetic resin paint used in such anticorrosive coating operations, an air-drying type (normal temperature drying type) is generally suitably used, and in such a paint, an alkyd resin is used as a film-forming element. , one or two organic polymer resins (including modified products) consisting of vinyl resins (vinyl chloride, vinyl acetate, etc.), polyurethane resins, epoxy resins, polyester resins, and acrylic resins (acrylic esters, etc.) More than one species is used. Such an organic polymer resin may be treated with a suitable solvent (for example, alcohol, ester, ether, ketone resin, aromatic hydrocarbon, etc.)
Further, as pigments, rust preventive pigments such as zinc-based and chromium oxide-based pigments, coloring pigments such as iron oxide, etc.
Extender pigments such as CaCO 3 , Al 2 O 3 , SiO 2 , Cu 2 O, Cu
A film-forming liquid composition (paint) that dries at room temperature is prepared by blending antifouling pigments such as A (synthetic) resin paint having a ratio (P/B) of (P) to resin solid content (B) in the range of 3 to 10 by weight was used. In short, the present invention provides a resin coating that is applied to the inner surface of a copper alloy tube to form the desired anticorrosion coating, and the ratio (P/B) of the pre-pigment content to the resin solid content is 3 to 3 in terms of weight ratio. 10, by using a synthetic resin paint with an increased pigment content, the corrosion resistance of the paint film formed on the inner surface of the copper alloy pipe can be improved without impairing its properties as an anti-corrosion film. In order to improve cathodic corrosion protection (alkali deterioration),
Furthermore, when the heat transfer property can be advantageously improved and the value of P/B is smaller than 3,
It is not possible to sufficiently improve the cathodic protection and heat transfer properties of such a coating film, and if the P/B value is greater than 10, the pigment dispersion becomes uneven and the formation of a coating film becomes difficult. This results in problems such as poor properties and powdery coating, resulting in poor abrasion resistance. The thickness of the anticorrosive coating film formed on the inner surface of the copper alloy pipe by normal coating operations using such a prescribed resin coating is generally a thickness that does not give a large heat transfer resistance value. In this case, it is determined appropriately depending on the type of resin paint,
For example, at a maximum coating thickness of 50 to 300 μm or less, particularly at a coating thickness of 30 μm or less, an inner surface anticorrosion coating film having lower heat transfer resistance will be formed. (Examples) Below, some examples of the present invention will be shown to clarify the present invention more specifically, but the present invention will not be limited in any way by the description of such examples. Needless to say, this is not something that can be accepted. In addition to the following examples and the above-mentioned specific description, the present invention includes various changes, modifications, and changes based on the knowledge of those skilled in the art, as long as they do not depart from the spirit of the present invention. It should be understood that improvements and the like may be made. Note that all ratios and percentages in the following examples are expressed on a weight basis unless otherwise specified. First, outer diameter: 25.4mm, wall thickness: 1.25mm, length:
2500mm aluminum brass tube (JIS-H-3300-
C-6871) as a test tube, and (a) high temperature
The inner surface was treated with either DX gas (12% CO 2 + N 2 ) annealing, (b) sandblasting (alumina particles: 150 μm), or (c) chromate treatment (immersed in 2% NaCr 2 O 7 for 15 minutes). did. Next, using 22 types of paints based on phthalic acid-based polyester resin paints or epoxy-modified alkyd resin paints listed in Tables 1 and 2 below (resin solid content was 50% in each case), the above method was applied. Painting was applied to the inner surface of the treated test tube using an air spray coating machine, aiming for a film thickness of 20 μm, and the coating was formed while forcibly removing the volatile solvent from the tube. . In addition, both paints
It uses a room-temperature curing resin that hardens at room temperature. In addition, in Table 1 showing phthalic acid-based polyester resin paint systems, Samples Nos. 1 to 3 are commercially available paint compositions with a regular blending ratio, and mainly include color pigments. The sample was prepared by increasing the amount of Red Garla, which is a
Paints No. 4 to 13 were prepared. The paint thus prepared has a ratio of total pigment content (P) to resin solid content (B) of 2.2 to 11.5. P/B is 5.8
When it becomes larger than , it starts to have a tendency to powder,
11.5 was deemed unsuitable as an organic resin film. Furthermore, in Table 2 showing epoxy-modified alkyd resin paint systems, Samples No. 14 to 16 are commercially available paint compositions, to which a coloring pigment (Red Garla) and an antifouling pigment (Cu) are added. increase the amount,
By increasing the P/B value to around 3.5 to 3.7,
Nos. 17 to 22 were prepared. The test tube surface finish symbols in Tables 1 and 2 have the following meanings. D: DX gas annealed surface S: Sandblast surface C: Chromate surface
【表】【table】
【表】
そして、この22種類の塗料を用いて内面防食塗
装皮膜の形成された供試管について、その性能を
評価し、内面塗膜の防食皮膜として有効性を検討
し、その結果を、下記第3表に示した。なお、そ
れぞれの性能評価は、以下の方法に従つて行なつ
た。
(イ) 分極抵抗値(R)
各供試管内面に海水を流速:2m/秒にて通過
させ、この状態で、試料を自然電位より−
200mV陰分極せしめ、その際必要とされた陰分
極電流(Ip)より、次式に従い分極抵抗値を算出
する。
R=200/Ip×〔2π2a3/ρ〕
但し、a:供試管半径、
ρ:海水の比抵抗値
(ロ) 汚染海水耐食性
硫黄イオンを0.1ppmの濃度において含有する
海水を、流速:2m/秒にて供試管内面に3ケ月
間連続して流通せしめる一方、管内径より3mm径
の大きなスポンジボールを、試験期間中、合計
250回通過させた。
(ハ) スポンジボール通過耐久性
供試管内に海水を流速:2m/秒にて流し、そ
の際、上記と同様な管内径より3mm径の大きなス
ポンジボールを、ボール径の過大分が3mmから2
mmに減耗した時点で新しいボールに交換しつつ、
10万回通過させ、塗膜の減耗量を測定した。そし
て、その試験後、試料を半割し、その表面を乾燥
させた後、その上に粘着テープを貼り付け、そし
てそれを勢いよく剥がすことにより、該粘着テー
プのテープ面に塗膜が付着するか否かを観察し
た。
(ニ) 耐電気防食性
供試管を陰極とし、管端電位が−650、−800、−
950mV(カロメル電極基準)になるように、定電
位法にて陰分極させる。管内流速は2m/秒とし
た。各電位にて1ケ月間試験した後、水洗、乾燥
し、そして供試管を縦割した後、管端より100mm
位置において、粘着テープを貼り付け、そしてそ
れを勢いよく剥がす操作を同一場所において3回
繰り返した後、5cm×1cmの面積について、画像
解析法にて剥離面積を求めた。
(ホ) 塗膜の伝熱抵抗値(r)
熱貫流率測定装置により、無塗装アルミニウム
黄銅管と試料管との熱貫流率を同時に測定し、
(k0,k1)、次式にて、塗膜の伝熱抵抗値(r)を
算出する。
r=1/k1−1/k0
なお、第3表中の「テープ面への塗膜付着」評
価における記号は、以下の意味を有するものであ
る。
○:テープ面への塗膜付着なし
〓:テープ面に軽微であるが、塗膜の付着が認
められる
●:テープ面に全面的に塗膜付着[Table] Then, we evaluated the performance of the test tubes on which the inner surface anticorrosive coating was formed using these 22 types of paints, examined their effectiveness as anticorrosive coatings for the inner surface, and summarized the results in the table below. It is shown in Table 3. In addition, each performance evaluation was performed according to the following method. (a) Polarization resistance value (R) Seawater is passed through the inner surface of each test tube at a flow rate of 2 m/sec, and in this state, the sample is lowered from the natural potential to -
200 mV of cathode polarization is applied, and the polarization resistance value is calculated from the cathode polarization current (I p ) required at that time according to the following formula. R=200/I p × [2π 2 a 3 /ρ] However, a: radius of the test tube, ρ: specific resistance value of seawater (b) Contaminated seawater corrosion resistance Seawater containing sulfur ions at a concentration of 0.1 ppm was : While the flow was made to flow continuously over the inner surface of the test tube for 3 months at 2 m/sec, a sponge ball with a diameter 3 mm larger than the inner diameter of the tube was
Passed 250 times. (c) Sponge ball passage durability Seawater was flowed into the test tube at a flow rate of 2 m/sec, and at that time, a sponge ball with a diameter 3 mm larger than the inner diameter of the tube similar to the above was inserted.
While replacing the ball with a new one when it wears down to mm,
It was passed through 100,000 times and the amount of loss of the coating film was measured. After the test, the sample is cut in half, its surface is dried, adhesive tape is pasted on top of it, and by peeling it off vigorously, a coating film adheres to the tape surface of the adhesive tape. I observed whether or not. (d) Electrolytic corrosion resistance The test tube is used as a cathode, and the tube end potential is -650, -800, -
Negatively polarize using the constant potential method to 950mV (calomel electrode reference). The flow velocity in the pipe was 2 m/sec. After testing for one month at each potential, washing with water, drying, and cutting the test tube vertically, 100mm from the end of the tube.
After repeating the operation of attaching an adhesive tape and peeling it off vigorously three times at the same location, the peeled area was determined using an image analysis method for an area of 5 cm x 1 cm. (E) Heat transfer resistance value of coating film (r) Using a heat transfer coefficient measuring device, measure the heat transfer coefficient of the unpainted aluminum brass tube and the sample tube at the same time.
(k 0 , k 1 ), the heat transfer resistance value (r) of the coating film is calculated using the following formula. r=1/k 1 -1/k 0 The symbols used in the evaluation of "coating film adhesion to tape surface" in Table 3 have the following meanings. ○: No paint film adhering to the tape surface 〓: Minor paint film adhesion is observed on the tape surface ●: Paint film adhering entirely to the tape surface
【表】【table】
【表】
かかる第3表の結果から明らかなように、比較
材(No.1〜3及びNo.14〜16;P/B=2.2,2.3)
は、何れの樹脂塗料を用いた場合にあつても、耐
食性、耐久性については問題ないが、電気防食性
において劣ることが認められるのである。しか
も、供試管の表面仕上げ法によつて、その差は大
きく、サンドブラスト面は著しく劣り、またクロ
メート仕上げ面は優れているが、かかるクロメー
ト仕上げは大幅なコスト増を招き、実用的ではな
いのである。
一方、試料No.4(P/B=2.6)では、耐電気防
食性、伝熱性の改善効果は認められるものの、そ
れ程顕著であるとは言えないが、試料No.5〜13に
おいてP/B値が3以上となると、両特性の改善
効果は著しいことが認められるのである。更に
P/B=3.8,5.8の試料(No.6,7;9,10)に
おいては、サンドプラスト面であつても、両特性
の改善効果が認められるのである。
しかしながら、P/B値の増大と共に、塗膜の
密着性(耐久性)は劣化の傾向にあつて、P/B
=5.8にてやや劣化の兆候が生じ、P/B=11.5
(No.13)では、実用上において、その信頼性が問
題となるのである。なお、分極抵抗値、塗膜下腐
食に関しては、P/B=2.2〜11.5の範囲で大幅
な差異は認められなかつた。
また、P/B値を3.6付近に保ち、顔料の内容
を変えた試料No.17〜22においては、何れの性能
共、防食皮膜として極めて優れたものであって、
従来品に比べて、顕著な性能向上が認められるの
である。従つて、塗膜形成が行なわれ得るなら
ば、選定される顔料種は問われないものと考えら
れる。なお、試料No.19〜22にて添加したCu粉末
は、防汚効果を有し、管内面への海生生物付着を
抑制することから、長期間使用後の伝熱性能を高
い値に保ち得る特徴を発揮する。
さらに、上記のP/B値の効果は、通常実用化
されている樹脂塗料であれば、上記実施例にて示
された2種類のもの以外にも認められるのであ
る。
そして、上記の如きP/B値の上昇によつて、
特に耐電気防食性が向上した理由としては、塗膜
中の欠陥が増大し、その結果電気防食下で塗膜下
にて生成したOH-が塗膜内の欠陥部を通つて系
外に排除され、塗膜下海水の高PH化が抑制される
ことにあると考えられるのである。
(発明の効果)
以上の説明から明らかなように、本発明によれ
ば、塗装物体にとつて不可避と見做されてきた陰
極防食下における有機樹脂塗膜のアルカリ劣化が
大幅に低減され得ることとなつたのであり、同時
に内面防食塗装皮膜付き銅合金管の欠点であつた
伝熱性能の低下が改善され、それが向上せしめら
れるという副次的効果ももたらされるに至つたの
である。
しかも、本発明に従う内面防食塗装皮膜付き銅
合金管にあつては、コスト、生産性の点では従来
品と全く同様であつて、何等問題はなく、また、
従来の塗装系においては、素材の下地処理が極め
て重要であつて、場合によつてはクロメート処理
後、塗装が行なわれており、更に既設管を対象に
した場合、実施するサンドブラスト面について
は、良好な密着性が得られない場合が多かつたの
であるが、本発明の場合にあつては、下地面の影
響を受ける度合いが少なく、サンドブラスト面に
も適用可能である特徴を有しているのである。[Table] As is clear from the results in Table 3, the comparative materials (No. 1 to 3 and No. 14 to 16; P/B = 2.2, 2.3)
No matter which resin paint is used, there is no problem in terms of corrosion resistance and durability, but it is recognized that the electrolytic corrosion protection is inferior. Moreover, the difference is large depending on the surface finishing method of the test tube: the sandblasted surface is significantly inferior, and the chromate finished surface is superior, but such a chromate finish causes a significant increase in cost and is not practical. . On the other hand, in sample No. 4 (P/B = 2.6), although the improvement effect of cathodic protection and heat conductivity is recognized, it cannot be said that it is so remarkable, but in sample No. 5 to 13, the P/B When the value is 3 or more, it is recognized that the improvement effect on both characteristics is significant. Furthermore, in the samples (No. 6, 7; 9, 10) with P/B = 3.8, 5.8, improvements in both properties were observed even on the sandblasted surface. However, as the P/B value increases, the adhesion (durability) of the paint film tends to deteriorate, and the P/B value tends to deteriorate.
= 5.8, some signs of deterioration occurred, P/B = 11.5
(No. 13), its reliability becomes a problem in practical use. In addition, regarding the polarization resistance value and corrosion under the coating film, no significant difference was observed in the range of P/B = 2.2 to 11.5. In addition, in sample Nos. 17 to 22, in which the P/B value was kept around 3.6 and the pigment content was changed, all performances were extremely excellent as anticorrosion coatings.
A significant performance improvement is observed compared to conventional products. Therefore, it is considered that the type of pigment selected does not matter as long as a coating film can be formed. In addition, the Cu powder added in samples No. 19 to 22 has an antifouling effect and suppresses the adhesion of marine organisms to the inner surface of the tube, so it maintains the heat transfer performance at a high value after long-term use. Demonstrate the characteristics you gain. Furthermore, the effect of the P/B value described above can be observed in other types of resin paints that are commonly put into practical use, other than the two types shown in the examples above. And, due to the increase in P/B value as mentioned above,
In particular, the reason for the improved cathodic protection is that defects in the coating film increase, and as a result, OH - generated under the coating film during cathodic protection is eliminated from the system through the defects in the coating film. This is thought to be due to the fact that the high PH level of the seawater under the coating film is suppressed. (Effects of the Invention) As is clear from the above description, according to the present invention, alkaline deterioration of organic resin coatings under cathodic protection, which has been considered inevitable for coated objects, can be significantly reduced. At the same time, the deterioration in heat transfer performance, which had been a drawback of copper alloy tubes with internal anticorrosion coatings, was improved, and the secondary effect was that this was improved. Moreover, the copper alloy tube with the inner surface anti-corrosion coating according to the present invention is exactly the same as conventional products in terms of cost and productivity, and there are no problems.
In conventional painting systems, the surface treatment of the material is extremely important, and in some cases, painting is performed after chromate treatment.Furthermore, when targeting existing pipes, the sandblasting surface is In many cases, it was not possible to obtain good adhesion, but in the case of the present invention, it is less affected by the underlying surface and has the feature that it can be applied to sandblasted surfaces. It is.
Claims (1)
却流体が流通せしめられる、伝熱管としての内面
防食塗装皮膜付き胴合金管にして、かかる内面防
食塗装皮膜が、塗料中の顔料分(P)と樹脂固形
分(B)との比率(P/B)が重量比で3〜10の範囲
内にある合成樹脂塗料を用いて形成されているこ
とを特徴とする熱交換器内面防食塗装皮膜付き銅
合金管。1. A body alloy tube with an inner surface anti-corrosion coating as a heat exchanger tube, which is attached to a heat exchanger and allows a prescribed cooling fluid to flow through the tube, and the inner surface anti-corrosion coating has a pigment content (P) in the paint. A heat exchanger with an anti-corrosion paint film on the inner surface, characterized in that it is formed using a synthetic resin paint having a ratio (P/B) of 3 to 10 by weight. Copper alloy tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18388387A JPS6430997A (en) | 1987-07-23 | 1987-07-23 | Copper alloy pipe with inner-surface corrosionproof coated film for heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18388387A JPS6430997A (en) | 1987-07-23 | 1987-07-23 | Copper alloy pipe with inner-surface corrosionproof coated film for heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6430997A JPS6430997A (en) | 1989-02-01 |
| JPH0438958B2 true JPH0438958B2 (en) | 1992-06-26 |
Family
ID=16143491
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18388387A Granted JPS6430997A (en) | 1987-07-23 | 1987-07-23 | Copper alloy pipe with inner-surface corrosionproof coated film for heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6430997A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20020084061A1 (en) * | 2001-01-03 | 2002-07-04 | Rosenfeld John H. | Chemically compatible, lightweight heat pipe |
| US8845930B2 (en) * | 2004-11-29 | 2014-09-30 | Pigmentan Ltd. | Methods of preventing corrosion |
| KR101717675B1 (en) * | 2015-05-14 | 2017-03-17 | 한국주철관공업주식회사 | A method of manufacturing corrosion protected iron pipe |
| CN107309129A (en) * | 2017-08-10 | 2017-11-03 | 合肥达科环保科技有限公司 | A kind of gas row of furniture spray painting clearing machine inhales the processing technology of component |
-
1987
- 1987-07-23 JP JP18388387A patent/JPS6430997A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6430997A (en) | 1989-02-01 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |