JPH0251977B2 - - Google Patents
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- Publication number
- JPH0251977B2 JPH0251977B2 JP63130584A JP13058488A JPH0251977B2 JP H0251977 B2 JPH0251977 B2 JP H0251977B2 JP 63130584 A JP63130584 A JP 63130584A JP 13058488 A JP13058488 A JP 13058488A JP H0251977 B2 JPH0251977 B2 JP H0251977B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- aluminum alloy
- molten zinc
- shaped steel
- molten
- 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
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- Coating With Molten Metal (AREA)
Description
〔産業上の利用分野〕
本発明は、清浄な大気中又は室内で長期の耐食
寿命を有する外観状態の良好な亜鉛めつきが施さ
れた形鋼材類、特に、軽量形鋼材類を経済的に製
造するための溶融亜鉛めつき方法に関するもので
ある。
〔従来の技術〕
近年、形鋼材類、特に軽量形鋼材類の使用分野
の拡大に伴い、耐食性や外観、塗装性などにおい
て優れた品質のものが要求されている。
そして、耐食性を重視する分野では亜鉛めつき
を施した形鋼材類の使用が増加しているが、この
ような耐食性を備えた亜鉛めつき形鋼材類として
は、従来から次のような種類のものが使用されて
いる。
(a) 形鋼材類に一般的な溶融亜鉛めつき法でめつ
きを施したもの
(b) 形鋼材類に電気亜鉛めつき法で亜鉛めつきを
施したもの
(c) 亜鉛鉄板〔JIS G 3315等)などの亜鉛めつ
き鋼板を成形した製品。
これらの亜鉛めつき形鋼材類のうち、(a)のもの
は「後めつき品」、(b)のものは「電気めつき品」、
(c)のものは「プレめつき品」と呼ばれているが、
上記(a)〜(c)の方法による亜鉛めつき被膜の厚さに
は、夫々の技術性及び経済性等により制限があ
り、一般的な製品の標準的な亜鉛付着量(片面)
は次の通りである。
後めつき品 350〜600g/m2
電気めつき品 30〜100 〃
プレめつき品 30〜150 〃
〔発明が解決しようとする課題〕
しかしながら、亜鉛めつき被膜の通常の大気中
或いは乾燥した室内での年間腐食減量は約10g/
m2であり、5g/m2程度の年間腐食減量での使用
場所が殆どであるため、上記後めつき品の場合に
は耐用年数が必要以上に長く、耐食性としては過
剰品質であり、電気めつき品及びプレめつき品で
は長期耐食材としては耐用寿命に不満足な場合が
多い。
又、プレめつき品ではめつき後に切断、孔ぐり
などの加工が施されるため、該加工部分が耐食上
の欠陥となる場合があり、後めつき品ではめつき
層表面の均一性が劣り、外観的な理由で室内製品
としては不向きな場合が生じる。
さらに、形鋼材類表面に施される溶融亜鉛めつ
き被膜は、鉄素地に接してガンマ晶、デルタワン
晶、ゼータ晶を主成分とする鉄−亜鉛合金層及び
亜鉛層(イータ層)からなつているが、鉄−亜鉛
合金層の成分は鉄原子の拡散が主因であり、亜鉛
層は亜鉛浴からの引き上げ時に付着してくる浴成
分が凝固して生じたものである。
従つて、後めつき品に適用される一般の溶融亜
鉛めつき方法では、一定時間(浴温度と素材温度
が等温になる)以上の亜鉛浴浸漬時間を必要と
し、その上、亜鉛層は重力によるタレ切りにより
平滑面を得ているため、亜鉛付着量の極端に少な
いものを商業的規模で製造することは技術的に困
難であり、通常、鋼材では最小でも亜鉛付着量が
350g/m2程度が限度で、それ以下の亜鉛付着量
にすることができない。
一方、電気めつき品は電解時間により亜鉛被膜
の厚さが増加するが、生産性からみて前記範囲以
上の製品はコストが大幅に増大するばかりでな
く、被膜の内部応力が高くなつて素地とめつき被
膜間の密着力が弱まり、剥離が発生し易くなる。
又、上記プレめつき品はいずれも大規模な連続
式鋼板めつき装置による亜鉛鉄板を原材料とする
ため、めつき層の厚い特殊な製品の製造は困難で
あり、その上、極厚めつき鋼板では成形工程で被
膜剥離を起こす虞れがある。
このような点から鑑みて、通常の大気中或いは
室内における長期耐食材としては、亜鉛付着量が
200〜400g/m2の範囲のものが望まれているが、
この範囲の亜鉛被膜厚さを有する亜鉛めつき形鋼
を得るには、現在一般的に行われているめつき方
法では現実的に困難である。
溶融亜鉛めつき方法を利用して上記範囲の亜鉛
付着層を有する形鋼を得るには、可及的な短時間
溶融亜鉛浴浸漬を可能にし、その上、過剰亜鉛層
の強制的な除去が必要であり、このような目的に
適合するものとして、鋼管の外面めつきを対象と
する連続式めつき装置(特公昭53−25809号公報)
があるが、断面形状の複雑な形鋼材類をこの装置
を利用してめつきすることは不可能と考えられて
いた。
溶融亜鉛めつき工程では、溶融亜鉛浴に浸漬す
る前工程で鋼材表面の残存酸化鉄薄膜を除去する
ためにフラツクス溶液処理を行うが、その際、フ
ラツクス成分(通常、塩化亜鉛アンモン)は溶融
亜鉛と反応して塩酸ガスやアンモニアガス、水蒸
気などが発生し、このガス体は被めつき素材と溶
融亜鉛との直接の接触を阻害して被膜生成反応が
起こらなくなるため、このガス体が亜鉛浴浸漬時
に被めつき素材面に貯溜しないような素材構造や
めつき姿勢をとることが溶融亜鉛めつき操作上、
重要である。
鋼管の外面形状ではこのようなガス体の貯溜が
殆ど生じないが、断面形状の複雑な形鋼材類を軸
線方向に水平移動させる場合には必ずガス体が貯
溜される部分が発生し、良好なめつき被膜を均一
且つ連続的に施すことができない。
このため、亜鉛浴内を移行する過程で、形鋼材
類を軸線を中心として回転させることも考えられ
るが、形鋼材類の断面形状が複雑で種々な形状の
ものがあるため、めつき装置としては機構的に困
難である。
本発明はこのような問題点に鑑みて鋭意研究を
行つた結果、溶融亜鉛浴を流動化することによつ
て形鋼材類に良好な溶融亜鉛めつきが施されるこ
とを見出し、このような手段を採用した形鋼材類
の溶融亜鉛めつき方法の提供を目的とするもので
ある。
〔課題を解決するための手段〕
上記目的を達成するために、本発明の形鋼材類
の溶融亜鉛めつき方法は、溶融亜鉛又は亜鉛アル
ミニウム合金が2m/秒以上の流速でもつて一定
方向に流動しながら充満、溢流しているハウジン
グ内に、フラツクス処理等の前処理を終了した形
鋼材類を前記ハウジングに穿設している形鋼材類
の断面形状と略同大、同形状の孔より前記溶融亜
鉛又は亜鉛アルミニウム合金の流動方向と同一方
向に導入して溶融亜鉛又は亜鉛アルミニウム合金
と接触させることによりめつきを施すと共に、そ
の接触により形鋼材類の表面に塗布したフラツク
ス溶液と溶融亜鉛又は亜鉛アルミニウム合金との
反応で発生するガス体を溶融亜鉛又は亜鉛アルミ
ニウム合金の流れによる前記ハウジングからの溢
流によつて外部に排出し、前記導入孔と対向して
ハウジングに穿設している該導入孔と同大、同形
状の導出孔から形鋼材類を導出した直後に、該形
鋼材類の表面に付着した余分の溶融亜鉛又は亜鉛
アルミニウム合金を吹拭することを特徴とするも
のである。
〔作用〕
上記ハウジング内において、2m/秒以上の流
速で流動している溶融亜鉛浴流中にフラツクス処
理等を終了した形鋼材類を軸線方向に通過させる
と、フラツクス溶液と溶融亜鉛との反応によつて
発生するガス体は溶融亜鉛浴流によつて効果的に
移動させられ、気泡として外部に排除される。
従つて、溶融亜鉛と形鋼材類表面との接触障害
が生じることなく、良好な連続亜鉛めつき被膜が
生成する。
なお、ハウジングに穿設している形鋼材類の導
入、導出孔は、形鋼材類の断面形状と略同大、同
形状に形成しているので、ハウジング内に充満し
て流動している溶融亜鉛又は亜鉛アルミニウム合
金がこれらの導入、導出孔から漏洩するのを最小
限度に抑えることができる。
さらに、流動浴であるため、溶融亜鉛からの形
鋼材類への熱伝導率が、静止浴に比して上昇する
ため、亜鉛浴浸漬時間が大幅に短縮され、鉄−亜
鉛合金層の厚さが減少する。
又、形鋼材類の軸線方向への移行によつてめつ
き処理を行うので、ハウジングから導出した直後
の位置で、圧縮空気等で余分な付着亜鉛の吹拭が
容易に行え、亜鉛層(イータ層)が減少すると共
に非常に美麗な外観の亜鉛めつき被膜が得られる
ものである。
〔実施例〕
本発明の実施例を図面について説明すると、第
1図において、被めつき素材である形鋼材類wの
移行方向に従つて、フラツクス処理設備1、乾燥
余熱炉2、溶融亜鉛めつき設備3、水冷却設備
4、ロール矯正設備5が配設され、さらに、これ
らの設備に形鋼材類wを軸線方向に順次、導入、
導出させるための複数個の搬送回転ロール6が設
けられてある。
上記フラツクス処理設備1は、処理液槽7内の
フラツクス(塩化亜鉛アンモン)水溶液をポンプ
8によつて処理液槽7上の液注出パイプ9に供給
し、該パイプ9から処理液槽7に向かつて噴出さ
せるようにすると共にその前方における処理液槽
7上にワイピンクリング10を配設してなるもの
である。
又、上記乾燥余熱炉2は、炉内温度が150〜250
℃の一定温度に保持できる加熱炉である。
溶融亜鉛めつき設備3は、第2図及び第3図に
示すように、通常の亜鉛溶融炉或いはめつき釜と
同様な構造を有して亜鉛を溶融すると共に溶融亜
鉛を収容している溶融亜鉛浴槽11と、この槽1
1内の上方部に配設されたハウジング12と、該
ハウジング12の前面に近接して配設された環形
状の多数の圧縮空気13噴出小孔を穿設している
鉄管製ワイピングリングを有する吹拭手段14と
からなり、このハウジング12は下部を溶融亜鉛
浴槽11内に設置した外壁カバー15内に前後方
向に長い箱形状の溶融亜鉛流動ケース16を一体
に配設してあり、浴槽11内の溶融亜鉛を亜鉛ポ
ンプ17によつて供給管路18から分流管路1
9,19を通じて前記溶融亜鉛流動ケース16の
底面上の前後両端部内に供給するように構成して
ある。なお、前記ワイピングリングは形鋼材類w
の形状、大きさに対応した形状に設計されたもの
を使用する。
さらに、溶融亜鉛流動ケース16の中央上部に
は浴槽11に連通するオーバフロー孔20が開設
していると共に該ケース16の底面上に近接した
高さ位置におけるこのケース16の前後壁と前記
外壁カバー15の前後壁には、形鋼材類wの導
入、導出孔21,22、23,24が同一軸線上
にして夫々設けられてあり、ケース14に設けら
れた導入、導出孔21,22の形状を、各種形鋼
材類wの断面形状に応じた形状に形成して空〓か
らの溶融亜鉛の漏洩が最小となるように設計して
ある。なお、この空〓からの漏洩亜鉛は浴槽11
内に還流する。
この溶融亜鉛めつき設備3の前方に配設された
前記水冷却設備4は多数本の並列パイプから40〜
90℃の加温水を形鋼材類wに吹き付けるようにし
てある。
又、前記ロール矯正設備5は形鋼材類wの曲が
り矯正を行うのに適当なロール矯正機を採用して
いるものである。
このような構成の設備に、適宜長さの形鋼材類
wを搬送回転ロール6上に供給して、各設備1〜
5に順次連続的に送り込むと、まず、フラツクス
処理設備1において、該設備1内に導入された形
鋼材類wはポンプ8によりパイプ9から噴出する
フラツクス水溶液(塩化亜鉛アンモン)をその表
面に塗布され、圧縮空気を噴出するワイピングリ
ング10で過剰に付着したフラツクス水溶液を除
去されつつ通過して乾燥余熱炉2内で一旦、乾燥
処理される。
次いで、乾燥余熱炉2から導出された形鋼材類
wは、溶融亜鉛めつき設備3内に導入される。
この設備3の浴槽11内に充満している亜鉛浴
組成は、通常の溶融亜鉛めつきと同様で、不可避
的不純物を含む亜鉛地金に微量(0.01%以下)の
アルミニウムを添加したもの、或いは10%以下の
アルミニウムを含む亜鉛合金である。
この設備3の外壁カバー15に穿設している導
入孔21からハウジング12のケース16に穿設
している導入孔23を通じて該ケース16内に導
入された形鋼材類wは、ケース16内を通過中に
その表面全面と溶融亜鉛が接触する。
この溶融亜鉛は、亜鉛ポンプ17によつて浴槽
11内から供給管路18、前後分流管路19,1
9を通じてケース16内を前後方向より2m/秒
以上の一定の流速度でもつて流れ、該形鋼材類w
と接触してめつきを施すと共にケース中央部に開
設しているオーバフロー孔20から浴槽11内に
還流するものである。
この際、形鋼材類wの表面に塗布したフラツク
ス溶液と溶融亜鉛とが反応して塩酸ガスやアンモ
ニアガス、水蒸気等のガス体が発生するが、該ガ
ス体は溶融亜鉛の流れと共に気泡となつて前記オ
ーバーフロー孔20から外部に排出される。
こうして亜鉛めつきを施された形鋼材類wは、
導出孔24を出た直後に吹拭手段14の多数の小
孔(1〜3mm径)から噴出する圧縮空気によつて
付着している余剰の溶融亜鉛を吹拭される。な
お、使用する圧縮空気の圧力は、2〜5Kg/cm2の
ものを調節して使用する。
続いて、めつき処理された形鋼材類wは水冷却
設備4に導入され、加温水の吹き付けによつて溶
融亜鉛被膜が凝固させられ、しかるのち、ロール
矯正設備5内に通過してその形状をロールにより
矯正され、製品となるものである。
次に、上記した本発明による溶融亜鉛めつき方
法と通常の溶融亜鉛めつき方法とによる溶融亜鉛
めつき被膜の比較試験結果を示す。
なお、溶融亜鉛めつきの各条件は次の通りであ
る。
試験材:リツプみぞ形鋼(100×50×20mm、厚
さ2.3mm、長さ5.5m)
めつき前処理
脱脂:オルソ珪酸ナトリウム+表面活性剤、液
温60℃
酸洗:塩酸10%、液温20℃、浸漬時間30分
フラツクス処理:塩化亜鉛アルミニウム30%水
溶液、液温60℃
亜鉛めつき条件
使用亜鉛地金:蒸留亜鉛地金1種、アルミニウ
ム0.005%添加
(1) 本発明により溶融亜鉛めつき方法
亜鉛温度 470℃
亜鉛浴の流動速度 4m/秒
素材移行速度 0.2m/秒
余剰亜鉛吹拭用圧縮空気圧 3Kg/cm2
(2) 通常の溶融亜鉛めつき方法
亜鉛浴温度 460℃
亜鉛浴浸漬時間 60秒
上記の条件で溶融亜鉛めつきを施したリツプみ
ぞ形鋼の外観検査の後、各5本を抜き取り、その
亜鉛付着量を測定した結果を次表に示す。
なお、本発明方法をAとし、通常の方法をBと
する。
[Industrial Application Field] The present invention is an economical method for manufacturing galvanized steel sections, particularly lightweight steel sections, that have a long corrosion-resistant life in clean air or indoors and have a good appearance. The present invention relates to a hot-dip galvanizing method for manufacturing. [Prior Art] In recent years, with the expansion of the field of use of shaped steel materials, especially lightweight shaped steel materials, there has been a demand for products with superior quality in terms of corrosion resistance, appearance, paintability, etc. In fields where corrosion resistance is important, the use of galvanized steel sections is increasing, but the following types of galvanized steel sections with corrosion resistance have traditionally been used: things are used. (a) Steel sections plated using the general hot-dip galvanizing method (b) Steel sections galvanized using the electrogalvanizing method (c) Galvanized steel sheets [JIS G Products made from galvanized steel sheets such as 3315 etc. Among these galvanized steel sections, those in (a) are "post-plated products", those in (b) are "electroplated products",
Item (c) is called a “pre-plated item”,
There are limits to the thickness of the galvanized film obtained by methods (a) to (c) above due to technical and economic considerations, and the standard amount of zinc coating for general products (one side)
is as follows. Post-plated products: 350 to 600 g/ m2 Electroplated products: 30 to 100 Pre-plated products: 30 to 150 [Problem to be solved by the invention] However, the galvanized film cannot be used in normal atmosphere or in a dry room. The annual corrosion weight loss is approximately 10g/
m 2 and most of the places where it is used have an annual corrosion loss of about 5 g/m 2. Therefore, in the case of the above-mentioned post-plated products, the service life is longer than necessary, the corrosion resistance is of excessive quality, and the electrical Plated products and pre-plated products often have unsatisfactory service life in terms of long-term corrosion resistance. In addition, since pre-plated products undergo processing such as cutting and drilling after plating, the processed parts may become corrosion-resistant defects, and post-plated products have poor surface uniformity of the plating layer. There are cases where it is unsuitable as an indoor product for reasons of appearance. Furthermore, the hot-dip galvanized coating applied to the surface of steel sections consists of an iron-zinc alloy layer containing gamma crystals, delta one crystals, and zeta crystals as main components and a zinc layer (eta layer) in contact with the iron base. However, the main cause of the composition of the iron-zinc alloy layer is the diffusion of iron atoms, and the zinc layer is formed by the solidification of bath components that adhere to the zinc bath when the metal is pulled up from the zinc bath. Therefore, in the general hot-dip galvanizing method applied to post-plated products, it is necessary to immerse the zinc bath for a certain period of time (so that the bath temperature and the material temperature become equal), and in addition, the zinc layer is Because the smooth surface is obtained by sagging with
The maximum amount of zinc deposit is around 350g/m2, and it is not possible to reduce the amount of zinc deposited below that. On the other hand, in electroplated products, the thickness of the zinc coating increases depending on the electrolysis time, but from the viewpoint of productivity, products exceeding the above range not only significantly increase costs, but also have high internal stress in the coating, making it difficult to hold the substrate. This weakens the adhesion between the coatings and makes peeling more likely. In addition, since all of the above pre-plated products use galvanized iron sheets produced by large-scale continuous steel sheet plating equipment as raw materials, it is difficult to manufacture special products with thick plating layers. There is a risk that the coating may peel off during the molding process. In view of this, for long-term corrosion resistance in normal atmosphere or indoors, the amount of zinc deposited is
A range of 200 to 400 g/m 2 is desired, but
It is practically difficult to obtain a galvanized section steel having a zinc coating thickness in this range using the plating methods commonly used at present. In order to obtain a section steel having a zinc adhesion layer in the above range using the hot-dip galvanizing method, it is necessary to enable immersion in a hot-dip zinc bath for as short a time as possible, and also to forcibly remove the excess zinc layer. As a device that is necessary and suitable for this purpose, a continuous plating device for plating the external surface of steel pipes (Japanese Patent Publication No. 53-25809) is proposed.
However, it was considered impossible to use this equipment to plate steel sections with complex cross-sectional shapes. In the hot-dip galvanizing process, a flux solution treatment is performed to remove the residual iron oxide thin film on the surface of the steel material before it is immersed in the molten zinc bath. This reaction generates hydrochloric acid gas, ammonia gas, water vapor, etc., and this gas prevents direct contact between the coating material and molten zinc, preventing the film formation reaction from occurring. For hot-dip galvanizing operations, it is important to maintain a material structure and a position that prevents accumulation on the surface of the coated material during dipping.
is important. Due to the external shape of steel pipes, this type of gas accumulation rarely occurs, but when moving steel sections with complex cross-sectional shapes horizontally in the axial direction, there will always be areas where gas accumulation occurs, making it difficult to maintain good maintenance. It is not possible to apply a coating uniformly and continuously. For this reason, it is conceivable to rotate the shaped steel materials around their axis during the process of transferring them in the zinc bath, but since the cross-sectional shapes of the shaped steel materials are complex and there are various shapes, it is difficult to use as a plating device. is mechanically difficult. As a result of extensive research in view of these problems, the present invention has discovered that good hot-dip galvanizing can be applied to steel sections by fluidizing the hot-dip zinc bath, The object of the present invention is to provide a method for hot-dip galvanizing steel sections using this method. [Means for Solving the Problems] In order to achieve the above object, the method for hot-dip galvanizing steel sections of the present invention is such that molten zinc or zinc-aluminum alloy flows in a constant direction at a flow rate of 2 m/sec or more. As the housing fills and overflows, the steel sections that have undergone pretreatment such as flux treatment are inserted into the housing through holes that are approximately the same size and shape as the cross-sectional shape of the section steel that is drilled in the housing. Plating is performed by introducing the molten zinc or zinc-aluminum alloy in the same direction as the flowing direction and bringing it into contact with the molten zinc or zinc-aluminum alloy. A gas body generated by the reaction with the zinc-aluminum alloy is discharged to the outside by overflow from the housing due to the flow of molten zinc or zinc-aluminum alloy, and a hole is provided in the housing opposite to the introduction hole. Immediately after the shaped steel is drawn out from the outlet hole, which has the same size and shape as the introduction hole, excess molten zinc or zinc-aluminum alloy attached to the surface of the shaped steel is blown off. . [Operation] When a shaped steel material that has undergone flux treatment is passed in the axial direction through a molten zinc bath flowing at a flow rate of 2 m/sec or more in the above housing, a reaction between the flux solution and molten zinc occurs. The gas generated by the molten zinc bath is effectively moved by the molten zinc bath flow and expelled to the outside as bubbles. Therefore, a good continuous galvanized film is produced without causing contact failure between the molten zinc and the surface of the shaped steel material. In addition, the introduction and outlet holes for the shaped steel materials drilled in the housing are formed to have approximately the same size and shape as the cross-sectional shape of the shaped steel materials, so that the molten fluid that fills and flows inside the housing can be removed. It is possible to minimize leakage of zinc or zinc-aluminum alloy from these inlet and outlet holes. Furthermore, since it is a fluidized bath, the thermal conductivity from molten zinc to the steel sections increases compared to a static bath, so the immersion time in the zinc bath is significantly shortened, and the thickness of the iron-zinc alloy layer is reduced. decreases. In addition, since the plating process is performed by moving the shaped steel material in the axial direction, excess zinc deposits can be easily wiped off with compressed air immediately after it is removed from the housing, and the zinc layer (eta As a result, a zinc-plated coating with a very beautiful appearance can be obtained. [Embodiment] An embodiment of the present invention will be explained with reference to the drawings. In Fig. 1, a flux treatment equipment 1, a drying preheating furnace 2, a molten galvanized steel plate, etc. A rolling equipment 3, a water cooling equipment 4, and a roll straightening equipment 5 are installed, and furthermore, the steel sections w are sequentially introduced into these equipment in the axial direction.
A plurality of conveyance rotation rolls 6 are provided for the purpose of leading out. The above-mentioned flux treatment equipment 1 supplies a flux (zinc ammonium chloride) aqueous solution in a treatment liquid tank 7 to a liquid pouring pipe 9 on the treatment liquid tank 7 by a pump 8, and from the pipe 9 to the treatment liquid tank 7. A wiper ring 10 is arranged on the processing liquid tank 7 in front of the processing liquid tank 7 so that the liquid is ejected towards the front. In addition, the drying preheating furnace 2 has an internal temperature of 150 to 250°C.
It is a heating furnace that can maintain a constant temperature of ℃. As shown in Figs. 2 and 3, the hot-dip galvanizing equipment 3 has a structure similar to a normal zinc melting furnace or galvanizing pot, and melts zinc and is a molten galvanizing machine that contains the molten zinc. Zinc bath 11 and this tank 1
It has a housing 12 disposed in the upper part of the interior of the housing 1, and a wiping ring made of iron pipe that is disposed close to the front surface of the housing 12 and has a large number of annular compressed air 13 outlet holes. This housing 12 has a box-shaped molten zinc flow case 16 that is long in the front and back direction and is integrally disposed within an outer wall cover 15 whose lower part is installed in the molten zinc bath 11. A zinc pump 17 transfers the molten zinc from the supply pipe 18 to the branch pipe 1.
The molten zinc is supplied to both the front and rear ends of the bottom surface of the flow case 16 through 9 and 19. Note that the wiping ring is made of shaped steel.
Use one designed in a shape and size that corresponds to the shape and size of the Furthermore, an overflow hole 20 communicating with the bathtub 11 is provided at the upper center of the molten zinc flow case 16, and the front and rear walls of the case 16 and the outer wall cover 15 are located at a height close to the bottom surface of the case 16. Introductory and outlet holes 21, 22, 23, and 24 for the shaped steel materials w are provided on the same axis in the front and rear walls of the case 14, respectively. It is designed to minimize the leakage of molten zinc from the cavity by forming it into a shape that corresponds to the cross-sectional shape of various shaped steel materials. In addition, the zinc leaking from this sky is in the bathtub 11.
Reflux within. The water cooling equipment 4 installed in front of the hot-dip galvanizing equipment 3 is connected to a large number of parallel pipes.
Warmed water at 90°C is sprayed onto the steel sections. Further, the roll straightening equipment 5 employs a roll straightening machine suitable for straightening the bends of the shaped steel materials w. To the equipment having such a configuration, the shaped steel materials w of an appropriate length are supplied onto the conveying rotating rolls 6, and each of the equipment 1 to
5, first, in the flux treatment equipment 1, the steel sections w introduced into the equipment 1 are coated with an aqueous flux solution (zinc ammonium chloride) spouted from the pipe 9 by the pump 8. Then, it passes through a wiping ring 10 that blows out compressed air while removing an excessively attached flux aqueous solution, and is once dried in a drying preheating oven 2. Next, the shaped steel materials w led out from the dry preheating furnace 2 are introduced into the hot-dip galvanizing equipment 3. The composition of the zinc bath filled in the bath 11 of this equipment 3 is the same as that of ordinary hot-dip galvanizing, which is a zinc base metal containing unavoidable impurities with a trace amount (0.01% or less) of aluminum added, or It is a zinc alloy containing less than 10% aluminum. Shaped steel materials w are introduced into the case 16 from the introduction hole 21 formed in the outer wall cover 15 of this equipment 3 through the introduction hole 23 formed in the case 16 of the housing 12. During the passage, the entire surface comes into contact with molten zinc. This molten zinc is pumped from inside the bathtub 11 by a zinc pump 17 to a supply pipe line 18, front and rear branch pipe lines 19, 1
9 flows inside the case 16 from the front and rear directions at a constant flow velocity of 2 m/sec or more, and the shaped steel materials w
The water flows back into the bathtub 11 through an overflow hole 20 formed in the center of the case. At this time, the flux solution applied to the surface of the shaped steel materials W reacts with the molten zinc to generate gases such as hydrochloric acid gas, ammonia gas, and water vapor, but these gases become bubbles as the molten zinc flows. and is discharged to the outside from the overflow hole 20. The steel sections that have been galvanized in this way are
Immediately after exiting the outlet hole 24, the excess molten zinc adhering to the molten zinc is blown off by compressed air which is blown out from a large number of small holes (1 to 3 mm diameter) in the wiping means 14. The pressure of the compressed air used is adjusted to 2 to 5 kg/cm 2 . Next, the plated steel sections w are introduced into the water cooling equipment 4, where the molten zinc coating is solidified by spraying heated water, and then passed through the roll straightening equipment 5 to change the shape. It is straightened by rolls and becomes a product. Next, the results of a comparative test of hot-dip galvanized coatings obtained by the above-described hot-dip galvanizing method according to the present invention and the conventional hot-dip galvanizing method will be shown. The conditions for hot-dip galvanizing are as follows. Test material: Rip channel steel (100 x 50 x 20 mm, thickness 2.3 mm, length 5.5 m) Plating pretreatment Degreasing: Sodium orthosilicate + surfactant, liquid temperature 60°C Pickling: 10% hydrochloric acid, liquid Temperature: 20℃, immersion time: 30 minutes Flux treatment: Zinc aluminum chloride 30% aqueous solution, liquid temperature: 60℃ Galvanizing conditions: Zinc ingot used: Distilled zinc ingot: Class 1 distilled zinc ingot, 0.005% aluminum added (1) Molten zinc according to the present invention Plating method Zinc temperature 470℃ Zinc bath flow rate 4m/sec Material transfer speed 0.2m/sec Compressed air pressure for wiping off excess zinc 3Kg/cm 2 (2) Ordinary hot-dip galvanizing method Zinc bath temperature 460℃ Zinc bath Immersion time: 60 seconds After inspecting the appearance of the lip groove steel that was hot-dip galvanized under the above conditions, five of each were taken out and the amount of zinc deposited was measured.The results are shown in the table below. Note that the method of the present invention is designated as A, and the conventional method is designated as B.
以上のように本発明の形鋼材類の力融亜鉛めつ
き方法によれば、ハウジング内において、2m/
秒以上の流速で流動している溶融亜鉛浴流中にフ
ラツクス処理等を終了した形鋼材類を軸線方向に
通過させるので、フラツクス溶液と溶融亜鉛との
反応によつて発生するガス体は溶融亜鉛浴流によ
つて効果的に移動させられ、気泡として外部に確
実に排除させることができ、従つて、溶融亜鉛と
形鋼材類表面との接触障害が生じることなく、良
好な連続亜鉛めつき被膜を生成することができる
ものである。
さらに、流動浴であるため、溶融亜鉛からの形
鋼材類への熱伝導率が、静止浴に比して上昇して
亜鉛浴浸漬時間を大幅に短縮させることができ、
鉄−亜鉛合金層の厚さを減少させることができる
と共に、ハウジングに穿設している形鋼材類の導
入、導出孔は、形鋼材類の断面形状と略同大、同
形状に形成しているので、ハウジング内に充満し
て流動している溶融亜鉛又は亜鉛アルミニウム合
金がこれらの導入、導出孔から漏洩するのを最小
限度に抑えることができ、形鋼材類の溝内などに
余分な溶融亜鉛を滞留させることなくハウジング
を通過させて正常な亜鉛めつき被膜を能率よく確
実に生成し得るものである。
又、形鋼材類の軸線方向への移行によつてめつ
き処理を行うので、ハウジングから導出した直後
の位置で、圧縮空気等で余分な付着亜鉛の吹拭が
容易に行え、この吹拭処理によつて亜鉛層(イー
タ層)を減少させることができると共に、非常に
美麗な外観の亜鉛めつき被膜を得ることができる
ものである。
As described above, according to the method for force-dip galvanizing steel sections of the present invention, galvanizing of 2m/
Since the shaped steel products that have undergone flux treatment are passed in the axial direction through the molten zinc bath flowing at a flow rate of 2 seconds or more, the gas generated by the reaction between the flux solution and the molten zinc is absorbed by the molten zinc. It is effectively moved by the bath stream and can be reliably removed to the outside as bubbles.Therefore, there is no contact failure between the molten zinc and the surface of the section steel, and a good continuous galvanizing film is created. can be generated. Furthermore, since it is a fluidized bath, the thermal conductivity from molten zinc to the steel sections is higher than in a static bath, and the immersion time in the zinc bath can be significantly shortened.
The thickness of the iron-zinc alloy layer can be reduced, and the introduction and outlet holes for the shaped steel materials drilled in the housing can be formed to have approximately the same size and shape as the cross-sectional shape of the shaped steel materials. As a result, it is possible to minimize the leakage of molten zinc or zinc-aluminum alloy flowing inside the housing through the introduction and outlet holes, and prevent excess molten zinc or zinc-aluminum alloy from entering or exiting the grooves of the shaped steel materials. It is possible to efficiently and reliably produce a normal galvanized film by allowing the zinc to pass through the housing without stagnation. In addition, since the plating process is performed by moving the shaped steel material in the axial direction, excess adhering zinc can be easily wiped off with compressed air or the like immediately after it is removed from the housing, and this blowing process By this method, the zinc layer (eta layer) can be reduced and a galvanized coating with a very beautiful appearance can be obtained.
図面は本発明の実施例を示すもので、第1図は
その装置の簡略構成図、第2図は溶融亜鉛めつき
設備の縦断側面図、第3図はその横断面図であ
る。
1……フラツクス処理設備、3……溶融亜鉛め
つき設備、4……水冷却設備、11……溶融亜鉛
浴槽、12……ハウジング、14……吹拭手段、
16……溶融亜鉛流動ケース、17……ポンプ、
19,19……分流管路、20……オーバフロー
孔。
The drawings show an embodiment of the present invention; FIG. 1 is a simplified configuration diagram of the apparatus, FIG. 2 is a vertical side view of the hot-dip galvanizing equipment, and FIG. 3 is a cross-sectional view thereof. 1... Flux processing equipment, 3... Hot-dip galvanizing equipment, 4... Water cooling equipment, 11... Molten zinc bath, 12... Housing, 14... Blowing means,
16... Molten zinc flow case, 17... Pump,
19, 19... Diversion pipe line, 20... Overflow hole.
Claims (1)
秒以上の流速でもつて一定方向に流動しながら充
満、溢流しているハウジング内に、フラツクス処
理等の前処理を終了した形鋼材類を前記ハウジン
グに穿設している形鋼材類の断面形状と略同大、
同形状の孔より前記溶融亜鉛又は亜鉛アルミニウ
ム合金の流動方向と同一方向に導入して溶融亜鉛
又は亜鉛アルミニウム合金と接触させることによ
りめつきを施すと共に、その接触により形鋼材類
の表面に塗布したフラツクス溶液と溶融亜鉛又は
亜鉛アルミニウム合金との反応で発生するガス体
を溶融亜鉛又は亜鉛アルミニウム合金の流れによ
る前記ハウジングからの溢流によつて外部に排出
し、前記導入孔と対向してハウジングに穿設して
いる該導入孔と同大、同形状の導出孔から形鋼材
類を導出した直後に、該形鋼材類の表面に付着し
た余分の溶融亜鉛又は亜鉛アルミニウム合金を吹
拭することを特徴とする形鋼材類の溶融亜鉛めつ
き方法。1 2m/2m of molten zinc or zinc-aluminum alloy
The cross-sectional shape of the shaped steel material that has undergone pre-treatment such as flux treatment is drilled into the housing, which is filled and overflowing while flowing in a constant direction at a flow rate of more than 1 second. Almost the same size,
Plating is applied by introducing the molten zinc or zinc-aluminum alloy in the same direction as the flow direction of the molten zinc or zinc-aluminum alloy through a hole of the same shape and bringing it into contact with the molten zinc or zinc-aluminum alloy, and the contact coats the surface of the shaped steel material. The gas generated by the reaction between the flux solution and the molten zinc or zinc-aluminum alloy is discharged to the outside by overflow from the housing due to the flow of the molten zinc or zinc-aluminum alloy, and the gas is discharged to the outside by the flow of the molten zinc or zinc-aluminum alloy, and the gas is discharged to the outside by the flow of the molten zinc or zinc-aluminum alloy. Immediately after leading out the shaped steel material from an outlet hole of the same size and shape as the inlet hole that has been drilled, be sure to wipe off any excess molten zinc or zinc-aluminum alloy that has adhered to the surface of the shaped steel material. Features: Hot-dip galvanizing method for shaped steel materials.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13058488A JPH01301846A (en) | 1988-05-28 | 1988-05-28 | Hot dip galvanizing method for shapes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13058488A JPH01301846A (en) | 1988-05-28 | 1988-05-28 | Hot dip galvanizing method for shapes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01301846A JPH01301846A (en) | 1989-12-06 |
| JPH0251977B2 true JPH0251977B2 (en) | 1990-11-09 |
Family
ID=15037706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13058488A Granted JPH01301846A (en) | 1988-05-28 | 1988-05-28 | Hot dip galvanizing method for shapes |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01301846A (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4936855A (en) * | 1972-08-22 | 1974-04-05 | ||
| JPS5298629A (en) * | 1976-02-12 | 1977-08-18 | Jiyon Reimondo Ansonii | Coninuous coating method and device therefor |
| JPS5230935A (en) * | 1976-08-11 | 1977-03-09 | Mitsubishi Electric Corp | Inductive heating process |
-
1988
- 1988-05-28 JP JP13058488A patent/JPH01301846A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01301846A (en) | 1989-12-06 |
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