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JPH0133504B2 - - Google Patents
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JPH0133504B2 - - Google Patents

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Publication number
JPH0133504B2
JPH0133504B2 JP58098256A JP9825683A JPH0133504B2 JP H0133504 B2 JPH0133504 B2 JP H0133504B2 JP 58098256 A JP58098256 A JP 58098256A JP 9825683 A JP9825683 A JP 9825683A JP H0133504 B2 JPH0133504 B2 JP H0133504B2
Authority
JP
Japan
Prior art keywords
heat exchanger
heat
coating layer
transfer member
copper
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
Application number
JP58098256A
Other languages
Japanese (ja)
Other versions
JPS59225249A (en
Inventor
Ju Fukuda
Yasunori Kaneko
Masao Maki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP58098256A priority Critical patent/JPS59225249A/en
Publication of JPS59225249A publication Critical patent/JPS59225249A/en
Publication of JPH0133504B2 publication Critical patent/JPH0133504B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/02Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
    • F28F19/06Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings of metal

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Details Of Fluid Heaters (AREA)
  • Paints Or Removers (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は瞬間湯沸器、給湯機器、暖房機器など
に使用される銅製伝熱部材よりなる熱交換器に関
するものである。 従来例の構成とその問題点 従来の瞬間湯沸器に使用されている熱交換器を
第1図に示す。同図に示す如く熱交換器は燃焼室
を内部に設けたドラム1と熱交換される水が通る
熱交換チユーブ2と前記ドラム1の上部に設けら
れた吸熱フイン3の銅製伝熱部材より構成され、
さらにこの表面に鉛を主成分とする溶融金属メツ
キが施されている。 この構成において、燃焼排ガス接触側、特にド
ラム1の熱交換チユーブ2接触付近や吸熱フイン
3の熱交換チユーブ2接触部付近などの低温部分
では燃焼排ガス中に含まれるNOx,SOx,CO,
CO2、水蒸気などが凝縮して酸性の結露水を生成
し、これにより前記溶融金属メツキや母材である
銅が激しく腐食するという問題が発生している。 このような腐食が起こると炭酸鉛、硝酸鉛、緑
青などの腐食生成物が多量に生成するためにこれ
らが吸熱フイン3やドラム1の部分に堆積し、排
ガスの流れが阻害され不完全燃焼を引き起こした
り、熱交換チユーブ2中を通過する水への熱伝導
が悪くなるために熱交換効率が著しく低下すると
ともに、前記腐食生成物が粉状に剥離し周囲が汚
染するなど安全衛生上好ましいものではなかつ
た。 発明の目的 本発明はかかる従来の欠点を解消するもので燃
焼排ガスが溶解した酸性結露水による熱交換器の
腐食を防止することにより、熱交換器の耐久性の
向上を図るとともに、不完全燃焼、熱交換効率の
低下を防止し、機器としての信頼性の向上を図る
ことを目的とする。 発明の構成 この目的を達成するために本発明は、燃焼室を
内部に形成したドラムと熱交換チユーブと吸熱フ
インよりなる銅製伝熱部材表面にニツケル、もし
くは鉛を主成分とする金属メツキ層とこのメツキ
層上にボロシロキサンポリマーとチタン有機化合
物と熱伝導率が30〔kcal/m・hr・deg〕以上の
充填材とからなるコーテイング層を形成したもの
である。 この構成によつて、燃焼排ガスが溶解した酸性
結露水が生じても銅製伝熱部材表面に形成したコ
ーテイング層により腐食を防止することができる
ため腐食生成物の堆積によつて生ずる不完全燃焼
や腐食生成物の飛散、落下による周囲の汚染を防
止することができるとともに前記金属メツキ層と
コーテイング層の熱伝導が損われないために熱交
換効率の低下を防止できる。 実施例の説明 以下、本発明の一実施例について第2図により
説明する。 図において4が燃焼室を内部に形成したドラム
吸熱フイン、熱交換チユーブの銅製伝熱部材であ
り、この表面に金属のメツキ層5とさらにこのメ
ツキ層5の上にコーテイング層6が形成される。 前記メツキ層5に適用される金属は熱交換器の
使用温度が最も高い部分で250〜300℃であるこ
と、また、銅製伝熱部材4と強固な密着性を必要
とすることから、ニツケルもしくは鉛を主成分と
する金属が良く、その形成方法は、電解、無電解
(化学)、溶融メツキなどが適用される。 一方、コーテイング層6はボロシロキサンポリ
マーをバインダーとし、これにチタン有機化合物
と熱伝導率が30〔kcal/m・hr・deg〕以上の充
填材とトルエンやキシレンなどの溶剤を加えて分
散混合することにより塗料化し、これを塗布して
加熱硬化させることにより形成される。前記チタ
ン有機化合物は前記ボロシロキサンポリマーの低
温焼成を目的とし適用されるものでテトライソプ
ロピルチタネート・テトラノルマルブチルチタネ
ート,チタンアセチルアセトネートが挙げられ、
これら単独でも混合物でも良い。また、熱伝導率
が30〔kcal/m・hr・deg〕以上の充填材はコー
テイング層6の熱伝導性の向上を図るために適用
するものであり、熱伝導率が30〔kcal/m・hr・
deg〕以上有する粉末であればその種類に限定さ
れるものではないが、特にコスト、耐食性の点か
らはグラフアイト粉末、アルミニウム粉末、窒化
ホウ素粉末が挙げられ、これら単独でも混合物で
も適用可能である。 この構成において、第1図に示す熱交換器のド
ラム1内の燃焼室下部に配置されたガスバーナが
燃焼した際、ドラム1、吸熱フイン3が熱交換チ
ユーブ2内を流れる水によつて冷却され、これら
表面に燃焼排ガス中に含まれるNOx,SOx,
CO,CO2を溶解した腐食性の強いPH=3〜4の
酸性結露水(HNO3,H2SO4等を含有)が生じる
とともに吸熱フイン3の先端部は250℃以上の高
温に達する。したがつて、前記吸熱フイン3の先
端部は高温になり、しかもドラム1及び吸熱フイ
ン3の熱交換チユーブ2の接触部においては温度
は低いが前記酸性水の結露、酸の濃縮、蒸発の繰
返しが起こり極めて厳しい環境となるが、コーテ
イング層6に用いるボロシロキサンポリマーが
300℃以上の耐熱性と優れた耐酸性を有するため
それ自身の劣化は無く、しかも表面は撥水性を有
し、膜としても緻密であるので酸や水蒸気など腐
食の原因となる物質のコーテイング層6内への侵
入を防止でき、優れた耐食性と耐熱性を実現する
ことができる。したがつて、メツキ層5及び銅製
伝熱部材4の腐食を防止することができるととも
に腐食生成物の吸熱フイン3やドラム1の表面へ
の堆積が無くなるのでそれが原因で起こる不完全
燃焼や汚染を防止でき、燃焼機器としての安全性
の向上が図れる。 また、コーテイング層6内には熱伝導率が30
〔kcal/m・hr・deg〕以上を有するグラフアイ
ト粉末、アルミニウム粉末、窒化ホウ素粉末を充
填材として用いるのでコーテイング層6は従来の
鉛メツキを施したものと同レベルの熱伝導性が実
現でき、しかも従来のような腐食による熱交換効
率の低下が無くなるので長期にわたり優れた熱交
換効率を維持することができる。本実施例に用い
る前記充填材の添加量はコーテイング層6の熱伝
導性、密着性の両立の点から、ボロシロキサンポ
リマー固型分に対し、30〜50wt%の範囲が好ま
しい。 前記ボロシロキサンポリマーは塗膜として優れ
た耐食性、密着性を実現するためには通常400℃
以上の高温で焼成する必要があるが、この場合、
伝熱部材である銅が著しい酸化を起こしこの酸化
被膜が非常に脆いために銅製伝熱部材4とメツキ
層5との間で層間剥離が発生することや銅製伝熱
部材4が焼なまし状態になり機械的強度が著しく
悪くなることやさらにメツキ層5の金属材料が鉛
などの低融点のものが適用できなくなるという欠
点を有する。したがつて、300℃以下で焼成する
必要があるが、本実施例では、チタン有機化合物
を用いることにより、300℃以下で焼成してもコ
ーテイング層6が優れた耐食性、耐熱性、密着性
を実現できることを見い出した。これは、チタン
有機化合物がボロシロキサンポリマーの硬化反応
(重合反応)を促進しているためと考えられる。
このチタン有機化合物は、テトライソプロピルチ
タネート、テトラノルマルブチルチタネート、チ
タンアセチルアセネートのいずれも適用でき、こ
れらの添加量はポリボロシロキサンを主成分とす
る有機ケイ素重合体固型分に対し、5〜15wt%
が望ましい。 一方、ボロシロキサンポリマーは、伝熱部材で
ある銅との密着性が著しく悪く、銅製伝熱部材4
の表面に直接コーテイング層6を形成することが
できなかつたが、これは前記銅製伝熱部材4の表
面に耐酸化性の優れたニツケルもしくは鉛を主成
分とする金属よりなるメツキ層5を設けることに
より、コーテイング層6との優れた密着性が実現
することを見い出した。 次に、本実施例の具体的な効果を表わす実験結
果を説明する。 熱交換器(本発明の実施品) A ボロシロキサンポリマー(固型分50wt%)100
重量部と平均粒径が約10μmのグラフアイト粉末
20重量部とテトライソプロピルチタネート7重量
部とトルエン100重量部をボールミルで24時間分
散混合することにより塗料を調整した。次に、第
1図に示す銅製伝熱部材よりなる熱交換器表面に
膜厚約3μmで無電解によるニツケルメツキを施
し、前記塗料をニツケルメツキ表面に膜厚約10〜
15μmでスプレーにより塗装し、280℃,1時間
の焼成を実施し、コーテイング層を形成した。 熱交換器(本発明の実施品) B 熱交換器Aで用いた有機ケイ素重合体100重量
部と平均粒径が約10μmのフレーク状アルミニウ
ム粉末10重量部と粒径が約0.4〜1μmの窒化ホウ
素粉末10重量部とチタンアセチルアセトネート5
重量部とトルエン100重量部を熱交換器Aと同条
件で塗料を調整した。次に熱交換器Aで用いた熱
交換器表面に膜厚約10μmで鉛97wt%、錫3wt%
の合金の溶融メツキを施し、前記塗料を鉛、錫の
合金メツキ表面に熱交換器Aと同条件でコーテイ
ング層を形成した。 熱交換器(本発明の実施品) C 熱交換器AおよびBで用いたボロシロキサンポ
リマー100重量部とグラフアイト粉末10重量部と
アルミニウム粉末10重量部とイソプロピルチタネ
ート4重量部とテトラノルマルブチルチタネート
3重量部とトルエン100重量部を熱交換器Aと同
条件で塗料を調整し、熱交換器Aで用いたニツケ
ルメツキを施した熱交換器表面に熱交換器Aと同
条件で前記塗料によるコーテイング層を形成し
た。 熱交換器(本発明を実施しない試料) イ 熱交換器Aの塗料構成のうち、テトライソプロ
ピルチタネートを含まない系の塗料を熱交換器A
と同条件で調整し、熱交換器Aで用いたニツケル
メツキを施した熱交換器表面に熱交換器Aと同条
件でコーテイング層を形成した。 熱交換器(本発明を実施しない試料) ロ 熱交換器Aで用いた塗料により、メツキ処理を
施していない熱交換器表面に熱交換器Aと同条件
でコーテイング層を形成した。 熱交換器(従来例) ハ 従来の熱交換器として、第1図に示す銅製伝熱
部材よりなる熱交換器の表面に膜厚約10μmで溶
融鉛メツキを施したものを用いた。 以上述べた本発明である熱交換器A〜Cと熱交
換器イ〜ハをガス瞬間湯沸器(5号タイプ)に組
み込み、すべて同一条件のもとで2分間燃焼、2
分間消火の繰返し燃焼実験した。その結果を表に
記す。
INDUSTRIAL APPLICATION FIELD The present invention relates to a heat exchanger made of a copper heat transfer member used in instantaneous water heaters, hot water supply equipment, heating equipment, and the like. Structure of a conventional example and its problems FIG. 1 shows a heat exchanger used in a conventional instantaneous water heater. As shown in the figure, the heat exchanger is composed of a copper heat transfer member including a drum 1 having a combustion chamber inside, a heat exchange tube 2 through which water to be heat exchanged passes, and heat absorption fins 3 provided on the top of the drum 1. is,
Furthermore, this surface is plated with molten metal whose main component is lead. In this configuration, NOx, SOx, CO contained in the combustion exhaust gas, and
CO 2 , water vapor, and the like condense to produce acidic dew water, which causes severe corrosion of the molten metal plating and the copper base material. When such corrosion occurs, a large amount of corrosion products such as lead carbonate, lead nitrate, and patina are generated, which accumulate on the heat absorption fins 3 and drum 1, obstructing the flow of exhaust gas and causing incomplete combustion. This is unfavorable in terms of health and safety, as the heat exchange efficiency is significantly reduced due to the heat conduction to the water passing through the heat exchange tube 2 becoming worse, and the corrosion products peel off into powder, contaminating the surrounding area. It wasn't. Purpose of the Invention The present invention solves such conventional drawbacks, and improves the durability of the heat exchanger by preventing corrosion of the heat exchanger due to acidic condensation water in which combustion exhaust gas is dissolved. The purpose is to prevent a decrease in heat exchange efficiency and improve the reliability of the device. Structure of the Invention In order to achieve this object, the present invention provides a metal plating layer containing nickel or lead as a main component on the surface of a copper heat transfer member consisting of a drum in which a combustion chamber is formed, a heat exchange tube, and heat absorption fins. A coating layer consisting of a borosiloxane polymer, a titanium organic compound, and a filler having a thermal conductivity of 30 [kcal/m·hr·deg] or more is formed on this plating layer. With this configuration, even if acidic condensation water containing dissolved combustion exhaust gas is generated, the coating layer formed on the surface of the copper heat transfer member can prevent corrosion, thereby preventing incomplete combustion caused by the accumulation of corrosion products. Contamination of the surrounding area due to the scattering and falling of corrosion products can be prevented, and since the heat conduction between the metal plating layer and the coating layer is not impaired, a decrease in heat exchange efficiency can be prevented. DESCRIPTION OF EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. In the figure, numeral 4 indicates a drum heat absorption fin with a combustion chamber formed inside, and a copper heat transfer member of a heat exchange tube.A metal plating layer 5 is formed on the surface of the fin, and a coating layer 6 is further formed on the plating layer 5. . The metal used for the plating layer 5 is nickel or nickel because the operating temperature of the heat exchanger is 250 to 300°C at the highest point, and strong adhesion to the copper heat transfer member 4 is required. A metal whose main component is lead is preferable, and its formation methods include electrolytic, electroless (chemical), and fusion plating. On the other hand, the coating layer 6 is made by using borosiloxane polymer as a binder, and adding and dispersing a titanium organic compound, a filler with a thermal conductivity of 30 [kcal/m・hr・deg] or more, and a solvent such as toluene or xylene. It is formed by turning it into a paint, applying it, and curing it by heating. The titanium organic compound is used for the purpose of low-temperature firing of the borosiloxane polymer, and examples thereof include tetraisopropyl titanate, tetra-normal butyl titanate, and titanium acetylacetonate.
These may be used alone or as a mixture. In addition, the filler having a thermal conductivity of 30 [kcal/m・hr・deg] or more is applied to improve the thermal conductivity of the coating layer 6, and has a thermal conductivity of 30 [kcal/m・hr・deg]. hr・
There are no restrictions on the type of powder as long as the powder has at least 100 degrees, but from the viewpoint of cost and corrosion resistance, graphite powder, aluminum powder, and boron nitride powder can be used, and these powders can be used alone or in combination. . In this configuration, when the gas burner disposed at the bottom of the combustion chamber in the drum 1 of the heat exchanger shown in FIG. , NOx, SOx contained in the combustion exhaust gas,
A highly corrosive acidic condensed water (containing HNO 3 , H 2 SO 4 , etc.) with dissolved CO and CO 2 is produced, and the tip of the endothermic fin 3 reaches a high temperature of 250° C. or higher. Therefore, the tip of the heat absorbing fin 3 becomes high temperature, and the temperature is low at the contact portion of the drum 1 and the heat exchange tube 2 of the heat absorbing fin 3, but condensation of the acidic water, concentration of acid, and evaporation are repeated. This creates an extremely harsh environment, but the borosiloxane polymer used for coating layer 6
It has heat resistance of over 300°C and excellent acid resistance, so it does not deteriorate itself, and the surface is water repellent, and the film is dense, so it can be used as a coating layer for substances that cause corrosion such as acids and water vapor. 6, and excellent corrosion resistance and heat resistance can be achieved. Therefore, corrosion of the plating layer 5 and the copper heat transfer member 4 can be prevented, and the accumulation of corrosion products on the surfaces of the heat absorption fins 3 and the drum 1 is eliminated, thereby preventing incomplete combustion and contamination caused by this. can be prevented, and the safety of combustion equipment can be improved. Furthermore, the thermal conductivity within the coating layer 6 is 30.
Since graphite powder, aluminum powder, and boron nitride powder having a value of more than [kcal/m・hr・deg] are used as fillers, the coating layer 6 can achieve the same level of thermal conductivity as conventional lead plating. Furthermore, since there is no decrease in heat exchange efficiency due to corrosion as in the conventional method, excellent heat exchange efficiency can be maintained over a long period of time. The amount of the filler used in this example is preferably in the range of 30 to 50 wt% based on the solid content of the borosiloxane polymer, from the viewpoint of achieving both thermal conductivity and adhesion of the coating layer 6. The above-mentioned borosiloxane polymer is usually heated at 400℃ in order to achieve excellent corrosion resistance and adhesion as a coating film.
It is necessary to bake at a higher temperature than above, but in this case,
Copper, which is a heat transfer member, undergoes significant oxidation, and this oxide film is extremely brittle, resulting in delamination between the copper heat transfer member 4 and the plating layer 5, and when the copper heat transfer member 4 is in an annealed state. This has the drawback that the mechanical strength is significantly deteriorated, and that a metal material with a low melting point such as lead cannot be used as the metal material for the plating layer 5. Therefore, it is necessary to bake at 300°C or lower, but in this example, by using a titanium organic compound, the coating layer 6 has excellent corrosion resistance, heat resistance, and adhesion even when fired at 300°C or lower. I found out what I can do. This is considered to be because the titanium organic compound promotes the curing reaction (polymerization reaction) of the borosiloxane polymer.
This titanium organic compound can be any of tetraisopropyl titanate, tetra-n-butyl titanate, and titanium acetylacenate, and the amount of these added is 5 to 5 to 15wt%
is desirable. On the other hand, borosiloxane polymer has extremely poor adhesion to copper, which is a heat transfer member, and
Although it was not possible to directly form the coating layer 6 on the surface of the copper heat transfer member 4, this is achieved by providing the plating layer 5 made of nickel or a metal whose main component is lead, which has excellent oxidation resistance, on the surface of the copper heat transfer member 4. It has been found that excellent adhesion with the coating layer 6 can be achieved by this. Next, experimental results showing specific effects of this example will be explained. Heat exchanger (implementation product of the present invention) A Borosiloxane polymer (solid content 50wt%) 100
Graphite powder with weight part and average particle size of approximately 10μm
A paint was prepared by dispersing and mixing 20 parts by weight, 7 parts by weight of tetraisopropyl titanate, and 100 parts by weight of toluene in a ball mill for 24 hours. Next, electroless nickel plating is applied to the surface of the heat exchanger made of the copper heat transfer member shown in FIG.
It was sprayed to a thickness of 15 μm and baked at 280° C. for 1 hour to form a coating layer. Heat exchanger (implementation product of the present invention) B 100 parts by weight of the organosilicon polymer used in heat exchanger A, 10 parts by weight of flaky aluminum powder with an average particle size of about 10 μm, and nitride with a particle size of about 0.4 to 1 μm 10 parts by weight of boron powder and 5 parts by weight of titanium acetylacetonate
A paint was prepared under the same conditions as in heat exchanger A using parts by weight and 100 parts by weight of toluene. Next, on the surface of the heat exchanger used in heat exchanger A, a film thickness of approximately 10 μm was formed using 97 wt% lead and 3 wt% tin.
A coating layer was formed on the lead-tin alloy plating surface under the same conditions as heat exchanger A. Heat exchanger (product of the present invention) C 100 parts by weight of the borosiloxane polymer used in heat exchangers A and B, 10 parts by weight of graphite powder, 10 parts by weight of aluminum powder, 4 parts by weight of isopropyl titanate, and tetra-n-butyl titanate. Prepare a paint using 3 parts by weight and 100 parts by weight of toluene under the same conditions as heat exchanger A, and coat the surface of the nickel-plated heat exchanger used in heat exchanger A with the paint under the same conditions as heat exchanger A. formed a layer. Heat exchanger (sample not implementing the present invention) A. Among the paint compositions of heat exchanger A, a paint that does not contain tetraisopropyl titanate was used in heat exchanger A.
A coating layer was formed on the surface of the nickel-plated heat exchanger used in heat exchanger A under the same conditions as heat exchanger A. Heat exchanger (sample not implementing the present invention) (b) Using the paint used in heat exchanger A, a coating layer was formed on the surface of the heat exchanger that had not been plated under the same conditions as heat exchanger A. Heat Exchanger (Conventional Example) C. As a conventional heat exchanger, a heat exchanger made of a copper heat transfer member shown in FIG. 1 was used, the surface of which was plated with molten lead to a thickness of approximately 10 μm. The heat exchangers A to C and heat exchangers A to C of the present invention described above were incorporated into a gas instantaneous water heater (No. 5 type), and all were burned for 2 minutes under the same conditions.
A combustion experiment was conducted in which the fire was extinguished repeatedly for minutes. The results are shown in the table.

【表】 以上の結果にみられるように、従来の熱交換器
は激しい腐食が発生したが、本実施例の熱交換器
は優れた耐食性を示した。また、熱交換器イで、
コーテイング層の剥離及び下地メツキ層の腐食が
発生した理由は、コーテイング層の形成に用いた
塗料にチタン有機化合物を含有しないため、280
℃、1時間の焼成ではコーテイング層が完全に硬
化していなかつたためと思われる。さらに、熱交
換器ロにおいて、コーテイング層の剥離がみられ
たのもバインダーであるボロシロキサンポリマー
と銅との密着性が非常に悪いことがその原因と思
われる。 また、本実施例である熱交換器A〜Cの熱交換
器は熱交換器ハの従来の熱交換器と同等の熱交換
効率を示し、本実施例のコーテイング層が熱伝導
性に優れていることを確認した。 発明の効果 以上、説明したように本発明は燃焼室を内部に
形成したドラムと吸熱フインと熱交換チユーブよ
りなる銅製伝熱部材の表面に耐酸化性に優れたメ
ツキ層と耐食性、耐熱性、熱伝導性に優れたコー
テイング層を形成しているので、 (1) 銅製伝熱部材の腐食がなくなり熱交換器とし
ての耐久性が大幅に向上する。 (2) ドラム、吸熱フイン部への腐食生成物の堆積
がなくなり、不完全燃焼を防止することができ
るとともに周囲への汚染もなくなる。 (3) 長期にわたり、初期の熱交換効率を維持する
ことができる。 などの効果を有する。
[Table] As seen from the above results, the conventional heat exchanger suffered severe corrosion, but the heat exchanger of this example showed excellent corrosion resistance. Also, in heat exchanger A,
The reason why the coating layer peeled off and the base plating layer corroded was because the paint used to form the coating layer did not contain titanium organic compounds.
This seems to be because the coating layer was not completely cured during baking at ℃ for 1 hour. Furthermore, peeling of the coating layer was observed in heat exchanger B, which is thought to be due to the extremely poor adhesion between the borosiloxane polymer binder and copper. In addition, the heat exchangers A to C of this example exhibited heat exchange efficiency equivalent to that of the conventional heat exchanger of heat exchanger C, and the coating layer of this example had excellent thermal conductivity. I confirmed that there is. Effects of the Invention As explained above, the present invention provides a plating layer with excellent oxidation resistance on the surface of a copper heat transfer member consisting of a drum in which a combustion chamber is formed, heat absorption fins, and a heat exchange tube, and a plating layer with excellent corrosion resistance and heat resistance. Since it forms a coating layer with excellent thermal conductivity, (1) corrosion of the copper heat transfer member is eliminated, greatly improving the durability of the heat exchanger. (2) Accumulation of corrosion products on the drum and heat absorbing fins is eliminated, preventing incomplete combustion and contamination of the surrounding area. (3) The initial heat exchange efficiency can be maintained over a long period of time. It has the following effects.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の瞬間湯沸器の熱交換器を示す外
観斜視図、第2図は本発明の熱交換器の一実施例
を示す要部断面図である。 4…銅製伝熱部材、5…メツキ層、6…コーテ
イング層。
FIG. 1 is an external perspective view showing a conventional heat exchanger for an instantaneous water heater, and FIG. 2 is a sectional view of essential parts showing an embodiment of the heat exchanger of the present invention. 4... Copper heat transfer member, 5... Plating layer, 6... Coating layer.

Claims (1)

【特許請求の範囲】 1 燃焼室を内部に設けたドラムと熱交換チユー
ブと吸熱フインよりなる銅製伝熱部材表面にニツ
ケル、もしくは鉛を主成分とする金属メツキ層と
このメツキ層上にボロシロキサンポリマーとチタ
ン有機化合物と熱伝導率が30〔kcal/m・hr・
deg〕以上の充填材とからなるコーテイング層を
形成してなる熱交換器。 2 チタン有機化合物がテトライソプロピルチタ
ネート、テトラノルマルブチルチタネート、チタ
ンアセチルアセトネートの少なくとも1種以上か
らなる特許請求の範囲第1項記載の熱交換器。 3 熱伝導率30〔kcal/m・hr・deg〕以上の充
填材がグラフアイト粉末、アルミニウム粉末、窒
化ホウ素粉末の少なくとも1種以上からなる特許
請求の範囲第1項記載の熱交換器。
[Scope of Claims] 1. A copper heat transfer member consisting of a drum with a combustion chamber inside, a heat exchange tube, and heat absorption fins, on the surface of which a metal plating layer containing nickel or lead as a main component and a borosiloxane layer on the surface of the copper heat transfer member. The polymer and titanium organic compound have a thermal conductivity of 30 [kcal/m・hr・
A heat exchanger formed by forming a coating layer consisting of a filler of more than deg]. 2. The heat exchanger according to claim 1, wherein the titanium organic compound comprises at least one of tetraisopropyl titanate, tetra-n-butyl titanate, and titanium acetylacetonate. 3. The heat exchanger according to claim 1, wherein the filler having a thermal conductivity of 30 [kcal/m·hr·deg] or more is comprised of at least one of graphite powder, aluminum powder, and boron nitride powder.
JP58098256A 1983-06-01 1983-06-01 Heat exchanger Granted JPS59225249A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58098256A JPS59225249A (en) 1983-06-01 1983-06-01 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58098256A JPS59225249A (en) 1983-06-01 1983-06-01 Heat exchanger

Publications (2)

Publication Number Publication Date
JPS59225249A JPS59225249A (en) 1984-12-18
JPH0133504B2 true JPH0133504B2 (en) 1989-07-13

Family

ID=14214872

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58098256A Granted JPS59225249A (en) 1983-06-01 1983-06-01 Heat exchanger

Country Status (1)

Country Link
JP (1) JPS59225249A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113431264B (en) * 2021-07-28 2022-03-15 日照汇德物联科技有限公司 Solar heat collection composite board and building integrated wind-heat solar system

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55164256A (en) * 1979-06-09 1980-12-20 Tokushu Muki Zairyo Kenkyusho Formation of film on metal substrate
JPS5736168A (en) * 1980-08-13 1982-02-26 Showa Electric Wire & Cable Co Ltd Electrical insulating coating compound having heat resistance
JPS5740414A (en) * 1980-08-25 1982-03-06 Teijin Ltd Novel active type vitamin d3 derivative composition

Also Published As

Publication number Publication date
JPS59225249A (en) 1984-12-18

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