JPS6043420B2 - Surface treatment material for heat exchangers - Google Patents
Surface treatment material for heat exchangersInfo
- Publication number
- JPS6043420B2 JPS6043420B2 JP11473381A JP11473381A JPS6043420B2 JP S6043420 B2 JPS6043420 B2 JP S6043420B2 JP 11473381 A JP11473381 A JP 11473381A JP 11473381 A JP11473381 A JP 11473381A JP S6043420 B2 JPS6043420 B2 JP S6043420B2
- Authority
- JP
- Japan
- Prior art keywords
- corrosion
- weight
- surface treatment
- treatment material
- gas
- 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
- 239000000463 material Substances 0.000 title claims description 25
- 238000004381 surface treatment Methods 0.000 title claims description 11
- 230000007797 corrosion Effects 0.000 description 25
- 238000005260 corrosion Methods 0.000 description 25
- 239000007789 gas Substances 0.000 description 14
- 229910045601 alloy Inorganic materials 0.000 description 11
- 239000000956 alloy Substances 0.000 description 11
- 239000000047 product Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 239000000567 combustion gas Substances 0.000 description 7
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 238000002844 melting Methods 0.000 description 5
- 229910000861 Mg alloy Inorganic materials 0.000 description 4
- 229910020220 Pb—Sn Inorganic materials 0.000 description 3
- 229910020944 Sn-Mg Inorganic materials 0.000 description 3
- 239000003350 kerosene Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007598 dipping method Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- UBAZGMLMVVQSCD-UHFFFAOYSA-N carbon dioxide;molecular oxygen Chemical compound O=O.O=C=O UBAZGMLMVVQSCD-UHFFFAOYSA-N 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Description
【発明の詳細な説明】
本発明は都市ガス、液化ガス、灯油などの燃料ガスを熱
源として利用する熱交換器に耐食性を付与する表面処理
材に関するものてある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a surface treatment material that imparts corrosion resistance to a heat exchanger that uses fuel gas such as city gas, liquefied gas, and kerosene as a heat source.
都市ガス、プロパンガスおよび灯油などの燃料による燃
焼ガス中には多量の窒素、酸素、二酸化炭素、水蒸気と
微量の一酸化炭素、二酸化イオウ、一酸化窒素、二酸化
窒素などが含まれている。Combustion gas from fuels such as city gas, propane gas, and kerosene contains large amounts of nitrogen, oxygen, carbon dioxide, water vapor, and trace amounts of carbon monoxide, sulfur dioxide, nitrogen monoxide, and nitrogen dioxide.
熱交換面の腐食現象は、急激な熱交換によるために、伝
熱面上で燃焼ガス中の水蒸気が結露し、その結露水中へ
燃焼ガス中の成分が溶解することに起因する。燃焼ガス
バーナー消火後、伝熱面に発生した結露水が蒸発するた
め、その結果伝熱面上へ結露水に溶解したガス成分であ
る金属の炭酸塩、硫酸塩、硝酸塩などの腐食生成物が析
出する。このサイクルの繰り返しによつて熱交換器表面
の腐食は進行する。従来、燃焼ガス雰囲気中で使用され
る熱交換器の防錆を目的とした表面処理材としては、S
n含量1重量%程度のPb−Sn合金が用いられ、溶融
メッキにより熱交換器の表面に被覆するのが一般的であ
つた。The corrosion phenomenon of the heat exchange surface is caused by water vapor in the combustion gas condensing on the heat transfer surface due to rapid heat exchange, and components in the combustion gas dissolving into the condensed water. After the combustion gas burner is extinguished, the condensed water generated on the heat transfer surface evaporates, resulting in the formation of corrosion products such as metal carbonates, sulfates, and nitrates, which are gas components dissolved in the condensed water, on the heat transfer surface. Precipitate. As this cycle is repeated, corrosion on the heat exchanger surface progresses. Conventionally, S
A Pb-Sn alloy with an n content of about 1% by weight was used, and it was common to coat the surface of the heat exchanger by hot-dip plating.
しかし、Pb−Sn系合金より成る表面処理材は、燃焼
ガス中で使用していくに従い、前述の如く結露水へのガ
ス成分の溶解、腐食生成物の析出の繰り返しサイクルに
よつて白色の腐食生成物が生成し、このようにして腐食
が徐々に進行し、熱交換器の表面処理材および熱交換器
素材生地や熱交換器に巻回したパイプなどに孔があき、
使用不能になつたり、あるいは熱交換フィン上への腐食
生成物の析出のための目詰まりにより不完全燃焼を起こ
すなどの問題があつた。本発明は、上記のような欠点を
なくし、都市ガス、液化ガス、燃料および灯油などの燃
料ガスに対する耐食性の優れた表面処理材を堤供するも
のである。However, as surface treated materials made of Pb-Sn alloys are used in combustion gas, white corrosion occurs due to repeated cycles of dissolving gas components in dew condensation water and precipitation of corrosion products as described above. Products are formed, and corrosion progresses gradually, causing holes in the heat exchanger surface treatment material, heat exchanger material fabric, and pipes wrapped around the heat exchanger.
There were problems such as the heat exchanger becoming unusable or clogging due to precipitation of corrosion products on the heat exchange fins, resulting in incomplete combustion. The present invention eliminates the above-mentioned drawbacks and provides a surface-treated material that has excellent corrosion resistance against fuel gases such as city gas, liquefied gas, fuel, and kerosene.
すなわち、本発明の処理材は、0.01〜4踵量%の川
と0.01〜15重量%のMgと残部Snよりなること
を特徴とする。That is, the treated material of the present invention is characterized by comprising 0.01 to 4% by weight of river, 0.01 to 15% by weight of Mg, and the balance Sn.
以下、本発明をその実施例により説明する。Hereinafter, the present invention will be explained with reference to examples thereof.
まず、溶融したSnに種々の割合でAlを添加して母合
金をつくり、これにMgを添加してAl−Sn−Mg合
金を作製した。この合金を銅板に溶融メッキしてテスト
ピースを作製した。これらのテストピースについて、以
下のようにして腐食試験を行つた。First, Al was added in various proportions to molten Sn to create a master alloy, and Mg was added to this to create an Al-Sn-Mg alloy. A test piece was prepared by hot-dip plating this alloy onto a copper plate. Corrosion tests were conducted on these test pieces as follows.
腐食性ガスとしては、Co、5%、N0010pμmお
よび5020.1pμmを含む空気を用いた。このガス
組成は、ガス瞬間湯沸器などに用いられる都市ガスの燃
焼ガスの分析結果に・もとづいて設定した。また、前述
の如く熱交換器の腐食は、燃焼ガス中の水蒸気の結露、
乾燥サイクルが加わるために発生するもので、この状態
を近似的に再現するために、腐食試験は前記のガス雰囲
気下において、50′Cで1時間結露させた後、25℃
において乾燥を3時間行うというステップを1サイクル
とし、これらのサイクルを繰り返すことにより行つた。
第1図はA1−Sn−Mg合金のMg含量を1重量%、
5重量%および10重量%と変えた場合のA1含量と上
記試験条件で20サイクル試験後の腐食量との関係を示
す。As the corrosive gas, air containing Co, 5%, N0010 pμm and 5020.1 pμm was used. This gas composition was set based on the analysis results of city gas combustion gas used in gas instantaneous water heaters. In addition, as mentioned above, corrosion of heat exchangers is caused by condensation of water vapor in combustion gas.
This occurs due to the addition of a drying cycle, and in order to approximately reproduce this condition, the corrosion test was performed in the gas atmosphere described above, after condensing at 50'C for 1 hour, at 25°C.
The step of drying for 3 hours was defined as one cycle, and these cycles were repeated.
Figure 1 shows the Mg content of A1-Sn-Mg alloy at 1% by weight.
The relationship between the A1 content when changed to 5% by weight and 10% by weight and the amount of corrosion after 20 cycle tests under the above test conditions is shown.
なお、腐食量は、腐食による増量で表している。第1図
から、通常不純物として含まれている量以上のNを含む
もの、すなわちA1含量0.01重量%以上のN−Sn
−Mg合金は、A1含量が増すと耐食性の向上すること
がわかる。Note that the amount of corrosion is expressed as an increase in amount due to corrosion. From Figure 1, it can be seen that N-Sn contains more than the amount of N normally contained as an impurity, that is, N-Sn with an A1 content of 0.01% by weight or more.
It can be seen that the -Mg alloy has improved corrosion resistance as the A1 content increases.
また、Mg含量は多くなるに従つて耐食性は劣る傾向に
ある。第2図は、1重量%のNと1重量%のMgと残部
のSnよりなる合金Aと、従来の表面処理材であるSn
含量1重量%のPb−Sn合金Bについて、前記と同様
にして試験した場合の腐食量を比較したものである。Furthermore, as the Mg content increases, corrosion resistance tends to deteriorate. Figure 2 shows alloy A consisting of 1% by weight N, 1% by weight Mg, and the balance Sn, and the conventional surface treatment material Sn.
The amount of corrosion is compared when Pb-Sn alloy B having a content of 1% by weight was tested in the same manner as above.
第2図から、本発明の合金Aは従来品Bに比べて著しく
耐食性の優れていることがわかる。次に、5重量%のA
1と1重量%のMgと残部のSnよりなるA1−Sn−
Mg合金A″と、従来の合金Bとをそれぞれ銅素地の熱
交換器に溶融メッキした後、この熱交換器をガス瞬間湯
沸器に組み込んで−通常の使用状態で動作させた。From FIG. 2, it can be seen that alloy A of the present invention has significantly better corrosion resistance than conventional product B. Next, 5% by weight of A
A1-Sn- consisting of 1 and 1% by weight of Mg and the balance Sn
After hot-dipping Mg alloy A'' and conventional alloy B onto a copper-based heat exchanger, the heat exchanger was installed in a gas instantaneous water heater and operated under normal operating conditions.
その結果第3図に示す。第3図から、従来の表面処理材
に比べて本発明の表面処理材A″が著しく耐食性を有し
ていることがわかる。第4図は、NxSn−Mg系合金
中におけるN含一量と融点の関係を示す。The results are shown in Figure 3. From Figure 3, it can be seen that the surface treated material A'' of the present invention has significantly higher corrosion resistance than conventional surface treated materials. Figure 4 shows the N content in the NxSn-Mg alloy and Shows the relationship between melting points.
第4図から、Al含量を増加すると融点が上昇すること
がわかる。一般に熱交換器の素地としては銅を用いるが
、銅素地に表面処理材を溶融メッキする場合、溶融表面
処理材の温度が600′C以上になると銅が軟化して変
形する等の問題があることから、安全性を考慮して融点
が55(代)以下の表面処理材を用いることが望ましい
。この点を考慮すれば、第4図から、本発明の表面処理
材のAl含量は40重量%以下にすることが必要である
。一方、Mg含量を増加すると腐食量が増える傾向にあ
り、また、MgはA1およびZnに比べて高価であるな
どを考慮すると、通l常不純物として含まれているMg
含量0.01重量%以上、15重量以下が望ましい。す
なわち、0.01〜4鍾量%のNと0.01〜15重量
%のMgと残部のSnよりなる材料が熱交換器用の表面
処理材として適している。From FIG. 4, it can be seen that increasing the Al content increases the melting point. Copper is generally used as the base material for heat exchangers, but when hot-dipping a surface treatment material onto a copper base, there are problems such as the copper softening and deforming if the temperature of the molten surface treatment material exceeds 600'C. Therefore, in consideration of safety, it is desirable to use a surface treatment material with a melting point of 55 (s) or lower. Considering this point, as shown in FIG. 4, the Al content of the surface treatment material of the present invention needs to be 40% by weight or less. On the other hand, increasing the Mg content tends to increase the amount of corrosion, and considering that Mg is more expensive than A1 and Zn, Mg, which is usually included as an impurity,
The content is desirably 0.01% by weight or more and 15% by weight or less. That is, a material consisting of 0.01 to 4 weight percent N, 0.01 to 15 weight percent Mg, and the balance Sn is suitable as a surface treatment material for a heat exchanger.
熱交換器用表面処理材の具備すべき条件として耐食性が
良いこと、熱伝導率が良いこと、融点がある程度高いこ
となどが要求される。Conditions that a surface treatment material for a heat exchanger should have include good corrosion resistance, good thermal conductivity, and a somewhat high melting point.
本発明の表面処理材の熱伝導率と従来の表面処理材の熱
伝導率とを比較すると、従来品は250℃において26
〜30Kca1/M.hr・℃であるのに対し、本発明
品は50〜160Kca1/m−Hr・℃と従来品に比
べ2〜5倍程度大きい。Comparing the thermal conductivity of the surface treated material of the present invention with that of the conventional surface treated material, the conventional product has a thermal conductivity of 26% at 250°C.
~30Kca1/M. hr·°C, whereas the product of the present invention has a heat resistance of 50 to 160 Kcal/m-Hr·°C, which is about 2 to 5 times larger than that of the conventional product.
以上述べたように、本発明の表面処理材は、従来の表面
処理材に比べ、耐食性に優れるとともに熱伝導率が大き
く、熱交換器用表面処理材としてすぐれた特徴をもつも
のである。As described above, the surface-treated material of the present invention has superior corrosion resistance and higher thermal conductivity than conventional surface-treated materials, and has excellent characteristics as a surface-treated material for heat exchangers.
第1図は、N−Sn−Mg合金のA1含量と腐食量との
関係を示す図、第2図および第3図は本発明の表面処理
材と従来品との腐食量を比較した図、第4図はN−Sn
−Mg合金のA1含量と融点との関係を示す。FIG. 1 is a diagram showing the relationship between A1 content and corrosion amount of N-Sn-Mg alloy, FIGS. 2 and 3 are diagrams comparing the corrosion amount between the surface treated material of the present invention and a conventional product, Figure 4 shows N-Sn
- Shows the relationship between A1 content and melting point of Mg alloy.
Claims (1)
gと残部Snからなることを特徴とする熱交換器用表面
処理材。1 0.01-40 weight Al and 0.01-15 weight M
A surface treatment material for a heat exchanger characterized by comprising g and the remainder Sn.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11473381A JPS6043420B2 (en) | 1981-07-22 | 1981-07-22 | Surface treatment material for heat exchangers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11473381A JPS6043420B2 (en) | 1981-07-22 | 1981-07-22 | Surface treatment material for heat exchangers |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5816045A JPS5816045A (en) | 1983-01-29 |
| JPS6043420B2 true JPS6043420B2 (en) | 1985-09-27 |
Family
ID=14645264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11473381A Expired JPS6043420B2 (en) | 1981-07-22 | 1981-07-22 | Surface treatment material for heat exchangers |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6043420B2 (en) |
-
1981
- 1981-07-22 JP JP11473381A patent/JPS6043420B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5816045A (en) | 1983-01-29 |
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