JP3907656B2 - Hot dip galvanizing method - Google Patents
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- JP3907656B2 JP3907656B2 JP2004369311A JP2004369311A JP3907656B2 JP 3907656 B2 JP3907656 B2 JP 3907656B2 JP 2004369311 A JP2004369311 A JP 2004369311A JP 2004369311 A JP2004369311 A JP 2004369311A JP 3907656 B2 JP3907656 B2 JP 3907656B2
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- 238000000034 method Methods 0.000 title claims description 77
- 238000005246 galvanizing Methods 0.000 title claims description 49
- 230000003647 oxidation Effects 0.000 claims description 135
- 238000007254 oxidation reaction Methods 0.000 claims description 135
- 229910000831 Steel Inorganic materials 0.000 claims description 65
- 239000010959 steel Substances 0.000 claims description 65
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 32
- 239000001301 oxygen Substances 0.000 claims description 32
- 229910052760 oxygen Inorganic materials 0.000 claims description 32
- 238000002485 combustion reaction Methods 0.000 claims description 30
- 230000033116 oxidation-reduction process Effects 0.000 claims description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 26
- 238000007747 plating Methods 0.000 claims description 15
- 238000000137 annealing Methods 0.000 claims description 12
- 230000001590 oxidative effect Effects 0.000 description 25
- 229910001335 Galvanized steel Inorganic materials 0.000 description 14
- 239000008397 galvanized steel Substances 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 12
- 230000000694 effects Effects 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 4
- 230000002349 favourable effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000005275 alloying Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000001678 irradiating effect Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
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Description
本発明は、溶融亜鉛めっき方法に関する技術分野に属するものであり、特には、Si含有量:1.8 質量%以上のSi含有鋼板を、酸化還元法によりめっき性を向上させた後、溶融亜鉛めっきする溶融亜鉛めっき方法に関する技術分野に属するものである。 The present invention belongs to the technical field concerning the galvanizing method, in particular, Si content: 1.8 mass% or more Si-containing steel sheet, after having improved coatability by a redox method, galvanized those belonging to the technical field concerning the galvanized how to.
Siなどの鉄より酸化しやすい元素(金属)を添加した鋼材は、添加量が増えるとめっき前の焼鈍過程(還元炉)において鋼板表面に添加元素が濃化し、溶融亜鉛との濡れ性が悪くなるため、不めっきが発生する問題がある。 Steel materials that contain elements (metals) that are more easily oxidized than iron, such as Si, are concentrated on the steel sheet surface during the annealing process (reduction furnace) before plating, and the wettability with molten zinc is poor. Therefore, there is a problem that non-plating occurs.
この不めっき防止に対して、無酸化炉において鋼板表面に400 〜10000 Åの厚膜の酸化皮膜を形成した後、還元炉で焼鈍する酸化還元法が提案されている(特開昭55-122865 号公報)。しかし、この方法では、無酸化炉を酸化条件で用いており、効果が安定しない問題があった。 To prevent this non-plating, a redox method has been proposed in which a thick oxide film of 400 to 10,000 mm is formed on the surface of a steel sheet in a non-oxidizing furnace and then annealed in a reducing furnace (Japanese Patent Laid-Open No. 55-122865). Issue gazette). However, this method has a problem that the effect is not stable because a non-oxidizing furnace is used under oxidizing conditions.
そこで、この技術を発展させたものとして、特開平4-202630、特開平4-202631、特開平4-202632、特開平4-202633、特開平4-254531、特開平4-254532号公報、特開平6-306561号公報等に多数の改良技術が提案されている。これらの技術には、合金化特性を改善するなどの方法が取られている。つまり、比較的薄い酸化皮膜を成長させて還元し表面に鉄層を形成させ、合金化特性を改善する方法である。 Therefore, as an advancement of this technology, Japanese Patent Laid-Open Nos. H4-202630, H4-202631, H4-202632, H4-202633, H4-254531, H4-254532, Many improved techniques have been proposed in Japanese Laid-Open Patent Publication No. 6-306561. These techniques take measures such as improving alloying characteristics. In other words, it is a method for improving alloying characteristics by growing and reducing a relatively thin oxide film to form an iron layer on the surface.
これらの他に、例えば、特開平7-34210 号公報に記載された技術などがあり、効果を安定させるための方法が多い。しかし、この場合も同様に酸化膜の厚みが薄い条件で、酸化膜厚を制御するために雰囲気ガスの濃度制御が行われている。 In addition to these, for example, there is a technique described in JP-A-7-34210, and there are many methods for stabilizing the effect. However, in this case as well, the concentration of the atmospheric gas is controlled to control the oxide film thickness under the condition that the oxide film is thin.
酸化膜厚みの制御方法については、バーナの空気比や雰囲気のガスの濃度を設定するような制御が多い。
Si含有鋼板では、酸化還元法を用いて表面に酸化皮膜を成長させ還元して鉄層を形成させて、めっき性を確保する。しかし、Si含有量が多いSi含有鋼板の場合は、Feが酸化し難く、還元ではSiの濃化が激しくなる。このため、酸化還元法での酸化により形成する酸化膜厚を厚くする必要がある。この傾向と酸化膜厚を厚くする必要性は、特にSi含有量:1.2 質量%以上のSi含有鋼板の場合に顕著であり、更にSi含有量:1.8 質量%以上のSi含有鋼板の場合に一層顕著である。なお、Siを含有する鋼板だけでなく、Feよりも酸化しやすい元素を含有する鋼板において、このような傾向と酸化膜厚を厚くする必要性がある。 In a Si-containing steel sheet, an oxide film is grown on the surface using a redox method and reduced to form an iron layer, thereby ensuring plating properties. However, in the case of a Si-containing steel sheet having a high Si content, Fe is difficult to oxidize, and the concentration of Si becomes severe during reduction. For this reason, it is necessary to increase the thickness of the oxide film formed by oxidation by the oxidation-reduction method. This tendency and the necessity of increasing the oxide film thickness are particularly remarkable in the case of a Si-containing steel sheet having a Si content of 1.2% by mass or more, and further in the case of a Si-containing steel sheet having a Si content of 1.8% by mass or more. It is remarkable. In addition to a steel sheet containing Si, a steel sheet containing an element that is more easily oxidized than Fe needs to have such a tendency and a thick oxide film.
酸化還元法での酸化により形成する酸化膜厚みを厚くするには、ラインスピードを低下させて酸化帯の滞留時間を大きくする方法も考えられるが、同時に還元帯の滞留時間も大きくなり、還元によりシリコンの濃化が激しくなり、適当な酸化皮膜を還元した鉄層が形成できない。 In order to increase the thickness of the oxide film formed by oxidation in the oxidation-reduction method, a method of increasing the residence time of the oxidation zone by reducing the line speed can be considered, but at the same time, the residence time of the reduction zone also increases and The concentration of silicon becomes intense, and an iron layer obtained by reducing an appropriate oxide film cannot be formed.
そこで、薄い酸化膜厚に対応した還元をするために還元炉での還元能力を低下させる。このためには還元炉での雰囲気ガス濃度の調整が必要である。しかし、雰囲気ガス濃度の調整には雰囲気ガスの置換が必要であり、これには数十分かかるため、種類の違う鋼板を通すラインでは実用的でない。 Therefore, in order to perform the reduction corresponding to the thin oxide film thickness, the reduction ability in the reduction furnace is reduced. For this purpose, it is necessary to adjust the atmospheric gas concentration in the reduction furnace. However, adjustment of the atmospheric gas concentration requires replacement of the atmospheric gas, which takes several tens of minutes, so it is not practical for a line through which different types of steel plates are passed.
なお、酸化炉の長さを長くすれば酸化時間が長くなり、ラインスピードを低下させなくても、酸化膜厚みを厚くすることができる。しかし、ラインではシリコンを含有しない鋼板を通す必要もあり、鋼板の種類により酸化還元のバランスが決まっているため、シリコンを含有する板を酸化させるために酸化炉を長くした場合、酸化能力が大きくなるため、酸化炉で鋼板が酸化しにくい操業をする必要があり、設備は冗長になる問題がある。 If the length of the oxidation furnace is increased, the oxidation time becomes longer, and the thickness of the oxide film can be increased without reducing the line speed. However, it is necessary to pass a steel plate that does not contain silicon in the line, and the balance of oxidation and reduction is determined by the type of steel plate. Therefore, if the oxidation furnace is lengthened to oxidize the plate containing silicon, the oxidation capacity is large. Therefore, it is necessary to perform an operation in which the steel sheet is not easily oxidized in the oxidation furnace, and there is a problem that the equipment becomes redundant.
本発明はこのような事情に鑑みてなされたものであって、その目的は、Si含有量:1.8 質量%以上のSi含有鋼板を酸化還元法により酸化還元した後、溶融亜鉛めっきするに際し、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、前記酸化還元法での酸化により形成する酸化膜の膜厚を厚くすることができる溶融亜鉛めっき方法を提供しようとするものである。また、酸化膜成長速度を大きくさせ酸化膜厚みを厚くさせるために、酸化膜の制御が必要であり、板温や酸素水蒸気添加による酸化膜厚の制御方法も提案する。 The present invention was made in view of such circumstances, and an object, Si content: Upon 1.8 after oxidizing reduced by the mass% or more Si-containing steel sheet oxidation-reduction method, hot dip galvanized, An object of the present invention is to provide a hot dip galvanizing method capable of increasing the thickness of an oxide film formed by oxidation in the oxidation-reduction method without decreasing the line speed and without increasing the length of the oxidation furnace. It is. Further, in order to increase the oxide film growth rate and increase the thickness of the oxide film, it is necessary to control the oxide film, and a method for controlling the oxide film thickness by adding plate temperature or oxygen water vapor is also proposed.
本発明者らは、上記目的を達成するため、鋭意検討した結果、本発明を完成するに至った。本発明によれば上記目的を達成することができる。 As a result of intensive studies to achieve the above object, the present inventors have completed the present invention. According to the present invention, the above object can be achieved.
このようにして完成され上記目的を達成することができた本発明は、溶融亜鉛めっき方法に係わり、これは請求項1〜3記載の溶融亜鉛めっき方法(第1〜3発明に係る溶融亜鉛めっき方法)であり、それは次のような構成としたものである。 The present invention thus completed and capable of achieving the above object relates to a hot dip galvanizing method, which comprises the hot dip galvanizing method according to claims 1 to 3 (the hot dip galvanizing according to the first to third inventions). Method), which has the following configuration.
即ち、請求項1記載の溶融亜鉛めっき方法は、Si含有量:1.8 質量%以上のSi含有鋼板を、酸化還元法によりめっき性を向上させた後、溶融亜鉛めっきする溶融亜鉛めっき方法において、鋼板の温度を無酸化状態で700 ℃以上の温度にした後、前記酸化還元法での酸化を火炎照射により行い、この際に火炎の酸化領域に鋼板を通過させ、鋼板表面に酸化膜を560 〜2000Å/sの酸化膜成長速度で成長させることを特徴とする溶融亜鉛めっき方法である〔第1発明〕。 That is, the hot dip galvanizing method according to claim 1 is a hot dip galvanizing method in which a Si-containing steel plate having a Si content of 1.8% by mass or more is improved in plating property by an oxidation-reduction method and then hot dip galvanized. after the 700 ° C. temperature above without oxidation state temperature of the carried out by flame irradiation oxidation in the oxidation-reduction method, this time is passed through the steel sheet oxidation region of the flame, the oxide film on the steel sheet surface 560 to A hot dip galvanizing method characterized by growing at an oxide film growth rate of 2000 kg / s [first invention].
請求項2記載の溶融亜鉛めっき方法は、前記火炎照射をバーナによる火炎照射により行い、この際にバーナの燃焼空気に酸素および/または水蒸気を、酸素は燃焼空気量に対して0体積%超20体積%以下の流量、水蒸気は燃焼空気量に対して0体積%超40体積%以下の流量で投入する請求項1記載の溶融亜鉛めっき方法である〔第2発明〕。
In the hot dip galvanizing method according to
請求項3記載の溶融亜鉛めっき方法は、溶融亜鉛めっき設備の焼鈍ラインを、無酸化帯または還元帯、酸化帯、還元帯の順に構成して、この酸化帯において酸化還元法での酸化をする請求項1または2記載の溶融亜鉛めっき方法である〔第3発明〕。 In the hot dip galvanizing method according to claim 3, the annealing line of the hot dip galvanizing equipment is configured in the order of a non-oxidation zone or a reduction zone, an oxidation zone, and a reduction zone, and oxidation is performed by the oxidation-reduction method in this oxidation zone. 3. The hot dip galvanizing method according to claim 1 or 2 [third invention].
本発明に係る溶融亜鉛めっき方法によれば、Si含有量:1.8 質量%以上のSi含有鋼板を酸化還元法により酸化還元した後、溶融亜鉛めっきするに際し、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、前記酸化還元法での酸化により形成する酸化膜の膜厚を厚くすることができるようになる。 According to the hot dip galvanizing method of the present invention, the Si content: 1.8% by mass or more of the Si-containing steel plate is oxidized and reduced by the oxidation-reduction method, and then hot-dip galvanized without reducing the line speed. Thus, it is possible to increase the thickness of the oxide film formed by the oxidation / reduction method without increasing the furnace length.
本発明に係る溶融亜鉛めっき方法は、前述のように、Si含有量:1.8 質量%以上のSi含有鋼板を、酸化還元法によりめっき性を向上させた後、溶融亜鉛めっきする溶融亜鉛めっき方法において、鋼板の温度を無酸化状態で700 ℃以上の温度にした後、前記酸化還元法での酸化を火炎照射により行い、この際に火炎の酸化領域に鋼板を通過させ、鋼板表面に酸化膜を560 〜2000Å/sの酸化膜成長速度で成長させることを特徴とする溶融亜鉛めっき方法としている。 As described above, the hot dip galvanizing method according to the present invention is a hot dip galvanizing method in which a Si-containing steel plate having a Si content of 1.8% by mass or more is improved in platability by a redox method and then hot dip galvanized. After the temperature of the steel sheet is set to 700 ° C. or higher in a non-oxidized state, oxidation by the oxidation-reduction method is performed by flame irradiation. At this time, the steel sheet is passed through the oxidation region of the flame, and an oxide film is formed on the steel sheet surface. The hot dip galvanizing method is characterized by growing at an oxide film growth rate of 560 to 2000 Å / s.
このように、鋼板の温度を無酸化状態で700 ℃以上の温度にした後、酸化還元法での酸化を火炎照射により行い、この際に火炎の酸化領域に鋼板を通過させるようにすると、酸化膜成長速度が高くなり、ひいては、酸化膜の膜厚を厚くすることができる。故に、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、酸化膜の膜厚を厚くすることができる。このとき、酸化膜成長速度を560 〜2000Å/sとすることができ、そうすることにより、充分に厚い酸化膜を形成することができる。 As described above, after the temperature of the steel sheet is set to 700 ° C. or higher in a non-oxidized state, oxidation by the oxidation-reduction method is performed by flame irradiation, and at this time, if the steel sheet is passed through the oxidation region of the flame, the oxidation is performed. The film growth rate increases, and as a result, the thickness of the oxide film can be increased. Therefore, the thickness of the oxide film can be increased without decreasing the line speed and without increasing the length of the oxidation furnace. At this time, the growth rate of the oxide film can be set to 560 to 2000 Å / s, and by doing so, a sufficiently thick oxide film can be formed.
従って、本発明に係る溶融亜鉛めっき方法によれば、Si含有量:1.8 質量%以上のSi含有鋼板を酸化還元法により酸化還元した後、溶融亜鉛めっきするに際し、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、前記酸化還元法での酸化により形成する酸化膜の膜厚を厚くすることができるようになる。 Therefore, according to the hot dip galvanizing method according to the present invention, after oxidation reduction of the Si-containing steel sheet having a Si content of 1.8% by mass or more by the oxidation reduction method, without reducing the line speed, Without increasing the length of the oxidation furnace, the thickness of the oxide film formed by oxidation in the oxidation-reduction method can be increased.
上記酸化還元法での酸化の際の酸化膜成長速度:560 〜2000Å/sは、従来技術の場合の酸化膜成長速度(例えば、30〜50Å/sの程度)に比べて、極めて高く、急速な酸化膜成長速度である。つまり、本発明に係る溶融亜鉛めっき方法の場合には、酸化還元法での酸化に際して鋼板表面に酸化膜を急速に成長させるようにしている。なお、酸化膜成長速度は、酸化膜の厚み方向の形成速度のことである。例えば、酸化膜成長速度:2000Å/sの場合は、酸化膜の厚みが2000Å/s(秒)の速度で形成される。これらの速度は、酸化膜が形成される間において、板温の変化や火炎の照射の位置の違いなどにより変化し一定でないため、主に酸化膜が急速に形成される間における平均値を用いる。 Oxide film growth rate during oxidation by the oxidation-reduction method: 560 to 2000 Å / s is extremely high and rapid compared to the oxide film growth rate in the case of the prior art (for example, about 30 to 50 Å / s). The oxide film growth rate is high. That is, in the case of the hot dip galvanizing method according to the present invention, an oxide film is rapidly grown on the surface of the steel sheet during oxidation by the oxidation-reduction method. The oxide film growth rate is the rate of formation of the oxide film in the thickness direction. For example, when the oxide film growth rate is 2000 Å / s, the thickness of the oxide film is formed at a rate of 2000 Å / s (seconds). These velocities change during the formation of the oxide film due to changes in the plate temperature, the difference in the position of the flame irradiation, etc., and are not constant. Therefore, the average value during the rapid formation of the oxide film is mainly used. .
本発明に係る溶融亜鉛めっき方法においては、上記のように酸化還元法での酸化に際して鋼板表面に酸化膜を560 〜2000Å/sの酸化膜成長速度で急速に成長させるようにしているので、一定の滞留時間を達成するライン速度で、厚い酸化皮膜を成長させることが可能である。 In the hot dip galvanizing method according to the present invention, an oxide film is rapidly grown on the steel sheet surface at an oxide film growth rate of 560 to 2000 liters / s during oxidation by the redox method as described above. It is possible to grow a thick oxide film at a line speed that achieves the desired residence time.
鋼板表面の酸化膜成長速度を560 〜2000Å/sとしているのは、560 Å/s未満にすると、充分な酸化膜厚みが達成できなくなり、2000Å/s超にすると、酸化膜の厚みの制御がし難くなって酸化膜の厚みの精度が低下したり、酸化膜厚が厚くなりすぎて還元炉で還元できなくなったりするからである。 The oxide film growth rate on the steel sheet surface is set to 560 to 2000 mm / s because if it is less than 560 m / s, a sufficient oxide film thickness cannot be achieved, and if it exceeds 2000 mm / s, the oxide film thickness can be controlled. This is because it becomes difficult to reduce the accuracy of the thickness of the oxide film, or the oxide film thickness becomes too thick to be reduced in the reduction furnace.
前記火炎照射の前に鋼板の温度を700 ℃以上の温度にした後、前記火炎照射をするようにすることにより、より確実に、酸化膜成長速度を560 〜2000Å/sとすることができ、ひいては、充分に厚い酸化膜を形成することができる。
By making the temperature of the
前記火炎照射をバーナによる火炎照射により行い、この際にバーナの燃焼空気に酸素および/または水蒸気を、酸素は燃焼空気量に対して0体積%超20体積%以下の流量、水蒸気は燃焼空気量に対して0体積%超40体積%以下の流量で投入するようにすると、酸化膜成長速度を560 〜2000Å/sの中でも高い水準にすることが容易にでき、ひいては、充分に厚い酸化膜を形成することが容易にできるようになる〔第2発明〕。 The flame irradiation is performed by flame irradiation with a burner. At this time, oxygen and / or water vapor are supplied to the combustion air of the burner, oxygen is a flow rate of more than 0% by volume and less than 20% by volume, and water vapor is the amount of combustion air. If the flow rate is more than 0% by volume and 40% by volume or less, the growth rate of the oxide film can be easily increased to a high level of 560 to 2000 liters / s. As a result, a sufficiently thick oxide film can be formed. It can be formed easily [second invention].
図5に、板温と酸化皮膜厚みとの関係を示す。板温が高い方が酸化皮膜が厚く成長することがわかる。そのため、酸化皮膜を急速に成長させるには、板を高温で保持することが重要である。なお、このような酸化皮膜の急速成長の点からは板温を高くすることが望ましいが、連続ラインでは板の張力を確保するために板温は約850 ℃以下にすることが望ましい。 FIG. 5 shows the relationship between the plate temperature and the oxide film thickness. It can be seen that the higher the plate temperature, the thicker the oxide film grows. Therefore, it is important to keep the plate at a high temperature in order to rapidly grow the oxide film. Although it is desirable to increase the plate temperature from the viewpoint of such rapid growth of the oxide film, it is desirable that the plate temperature be about 850 ° C. or less in order to ensure the tension of the plate in the continuous line.
図6に、火炎照射のない場合と、火炎照射する場合と、バーナによる火炎照射の際のバーナの燃焼空気に酸素を添加した場合(酸素富化の場合)と、バーナによる火炎照射の際のバーナの燃焼空気に水蒸気添加した場合と、バーナによる火炎照射の際のバーナの燃焼空気に酸素および水蒸気を添加した場合の酸化膜厚の成長比率(酸化膜割合)を示す。この比率は、これが大きいほど酸化膜成長速度が高いことを示すものである。火炎照射のない場合に比して火炎照射する場合は酸化膜成長速度が高く、それに比して酸素富化の場合は酸化膜成長速度が高く、更に水蒸気を添加した場合は酸化膜成長速度が高く、酸素および水蒸気を添加した場合は最も酸化膜成長速度が高い。 In FIG. 6, when there is no flame irradiation, when the flame is irradiated, when oxygen is added to the combustion air of the burner during the flame irradiation by the burner (in the case of oxygen enrichment), when the flame is irradiated by the burner The growth ratio (oxide film ratio) of the oxide film thickness when steam is added to the combustion air of the burner and when oxygen and steam are added to the combustion air of the burner during flame irradiation by the burner is shown. This ratio indicates that the larger the ratio, the higher the oxide film growth rate. Compared to the case without flame irradiation, the oxide film growth rate is higher when the flame irradiation is performed, and compared with that when the oxygen is enriched, the oxide film growth rate is higher. The growth rate of oxide film is highest when oxygen and water vapor are added.
図7に、酸素添加量や水蒸気添加量と酸化膜厚比率との関係を示す。この比率は、これが大きいほど酸化膜成長速度が高いことを示すものである。酸素の添加(酸素富化)や水蒸気の添加により酸化膜厚は成長するが、ある程度投入するとその効果が頭打ちになることがわかる。酸素と水蒸気の添加にはユーティリティ費用がかかるために、効果の頭打ちになる流量より少ない範囲を使うほうが効果的である。 FIG. 7 shows the relationship between the oxygen addition amount and the water vapor addition amount and the oxide film thickness ratio. This ratio indicates that the larger the ratio, the higher the oxide film growth rate. It can be seen that the oxide film thickness grows by the addition of oxygen (oxygen enrichment) or the addition of water vapor, but the effect reaches its peak when a certain amount is added. Since the addition of oxygen and water vapor involves utility costs, it is more effective to use a range that is less than the peak flow rate.
このような点から、前述の第2発明の場合のように酸素の添加量(流量)はバーナの燃焼空気量に対して0体積%超20体積%以下とすることが望ましく、更に5〜10体積%とすることが望ましいこと、及び、前述の第2発明の場合のように水蒸気の添加量はバーナの燃焼空気量に対して0体積%超40体積%以下とすることが望ましいことがわかる。また、酸素の添加のみを行うと火炎温度が上昇する場合や、火炎長さが短くなる場合等があり、板への伝熱量が変わるために板温が変わり、酸化皮膜の成長速度が変化する。また、水蒸気のみの添加では火炎温度が低下するため、板温が低下による酸化皮膜成長速度の低下と水蒸気添加による酸化皮膜成長速度の増加が相殺される場合もある。そのため、酸素と水蒸気を一定の混合割合で添加すると、火炎温度や火炎長さがほぼ一定の条件で酸化皮膜を成長させることが可能であり、板温を安定させて運転させることが可能になる。そのため酸素と水蒸気の添加量対してほぼ一定の割合で酸化膜成長速度が増加するために、酸化膜厚の制御が容易になる。つまり、ある一定量の酸素と水蒸気添加した状態で一定の酸化膜厚を確保できる板温に設定した後、酸素水蒸気の流量の増減により所定の酸化膜厚を制御する運転が可能になる。 From this point of view, it is desirable that the amount of oxygen added (flow rate) is more than 0% by volume and not more than 20% by volume with respect to the amount of combustion air of the burner, as in the case of the second invention described above. It can be seen that the volume% is desirable, and the amount of water vapor added is desirably greater than 0 volume% and not greater than 40 volume% with respect to the amount of combustion air in the burner as in the case of the second invention described above. . In addition, if only oxygen is added, the flame temperature may increase or the flame length may be shortened. The plate temperature changes due to the amount of heat transfer to the plate, and the growth rate of the oxide film changes. . Further, since the flame temperature is lowered by adding only water vapor, the decrease in the oxide film growth rate due to the decrease in the plate temperature may be offset by the increase in the oxide film growth rate due to the water vapor addition. Therefore, when oxygen and water vapor are added at a constant mixing ratio, it is possible to grow an oxide film under conditions where the flame temperature and flame length are substantially constant, and it becomes possible to operate with a stable plate temperature. . Therefore, the oxide film growth rate increases at a substantially constant rate with respect to the added amounts of oxygen and water vapor, and therefore, the oxide film thickness can be easily controlled. In other words, after setting a plate temperature at which a constant oxide film thickness can be secured with a certain amount of oxygen and water vapor added, an operation for controlling a predetermined oxide film thickness by increasing or decreasing the flow rate of oxygen water vapor becomes possible.
図8に、酸化皮膜がない状態から急速酸化させる場合と、酸化皮膜を3000Å成長させてから急速酸化させる場合の酸化皮膜の成長速度を示す。酸化膜の成長速度は膜厚が厚くなると成長速度が低下するために、成長速度が低下することがわかる。 FIG. 8 shows the growth rate of the oxide film when it is rapidly oxidized from the state where there is no oxide film, and when the oxide film is rapidly oxidized after being grown 3,000 mm. It can be seen that the growth rate of the oxide film decreases because the growth rate decreases as the film thickness increases.
酸化帯での板温が高い方が酸化膜の成長が速いために、溶融亜鉛めっき設備の焼鈍ラインを、無酸化帯または還元帯、酸化帯、還元帯の順に構成して、この酸化帯において酸化還元法での酸化をするようにすると、確実に鋼板表面に酸化膜を560 〜2000Å/sの酸化膜成長速度で急速に成長させることができ、また、そのような急速な成長をさせやすく、更に、酸化膜成長速度の上昇がはかりやすくなる〔第3発明〕。このとき、無酸化帯または還元帯において無酸化状態で板温をできるだけ高温にしておき、酸化帯で急速に酸化させて酸化膜厚を形成させると、酸化膜成長速度の上昇がはかりやすい。 Since the oxide film grows faster when the plate temperature in the oxidation zone is higher, the annealing line of the hot dip galvanizing equipment is configured in the order of non-oxidation zone or reduction zone, oxidation zone, reduction zone. When oxidation is performed by the oxidation-reduction method, it is possible to reliably grow an oxide film on the surface of the steel plate at an oxide film growth rate of 560 to 2000 mm / s, and to facilitate such rapid growth. Furthermore, the oxide film growth rate can be easily increased [third invention]. At this time, if the plate temperature is kept as high as possible in the non-oxidation zone or the reduction zone in the non-oxidation state and is oxidized rapidly in the oxidation zone to form an oxide film thickness, the oxide film growth rate is easily increased.
無酸化帯を酸化帯として使う場合、酸化皮膜が徐々に成長して酸素の拡散が妨げられるため、低温では酸化させずに、酸化膜を高温で急速に生成させるほうが酸化膜の成長速度を向上させることが可能である。同様に酸化膜を急速に成長させるためには、前述のようにバーナの燃焼空気に酸素富化や水蒸気添加する方法を用いるとよい。 When the non-oxidation zone is used as the oxidation zone, the oxide film grows gradually and the diffusion of oxygen is hindered. Therefore, it is better not to oxidize at a low temperature but to generate an oxide film rapidly at a high temperature. It is possible to make it. Similarly, in order to grow the oxide film rapidly, it is preferable to use a method of enriching oxygen or adding water vapor to the combustion air of the burner as described above.
バーナの燃焼空気に酸素富化や水蒸気添加する場合、バーナの燃焼量を一定にして、酸素や水蒸気の添加濃度を変化させることにより、酸化膜厚を制御することができる。 When enriching oxygen or adding water vapor to the combustion air of the burner, the oxide film thickness can be controlled by changing the addition concentration of oxygen or water vapor while keeping the amount of combustion of the burner constant.
焼鈍ラインと溶融亜鉛めっき装置とを有する溶融亜鉛めっき設備において、前記焼鈍ラインを、無酸化帯または還元帯、酸化帯、還元帯の順に構成し、この酸化帯において酸化還元法での酸化をすることを特徴とする溶融亜鉛めっき設備によれば、前述したような本発明に係る溶融亜鉛めっき方法を確実に遂行することができる。 In a hot dip galvanizing facility having an annealing line and a hot dip galvanizing apparatus, the annealing line is configured in the order of a non-oxidation zone or a reduction zone, an oxidation zone, and a reduction zone, and oxidation is performed by the oxidation-reduction method in this oxidation zone. According to the hot dip galvanizing facility characterized by this, the hot dip galvanizing method according to the present invention as described above can be reliably performed.
本発明において、酸化還元法での酸化をバーナによる火炎照射により行う場合、バーナを複数本設置して、燃焼しているバーナの本数を変えると、火炎の照射幅を変えることができ、これにより火炎の照射時間を変え、酸化膜厚制御をすることができる。バーナの燃焼量を低下させると火炎長が短くなるため、火炎が鋼板に照射しなくなり、酸化皮膜成長速度が急速に低下する。そのため、バーナを複数本用意して、バーナの燃焼量が低下しても確実に鋼板に火炎を照射させるようにバーナを配置することにより酸化皮膜を安定的に形成させることができる。この場合、火炎の照射効果が低下しない程度までバーナの燃焼量を連続的に低下させ、設定値より小さくなる場合は、複数本のバーナの一部を消火する方法を採用することにより、連続的に酸化膜厚を成長させることが可能になる。 In the present invention, when oxidation in the oxidation-reduction method is performed by flame irradiation with a burner, by installing a plurality of burners and changing the number of burning burners, the flame irradiation width can be changed, thereby The oxide film thickness can be controlled by changing the flame irradiation time. When the burner combustion amount is reduced, the flame length is shortened, so that the flame does not irradiate the steel sheet, and the oxide film growth rate decreases rapidly. Therefore, it is possible to stably form an oxide film by preparing a plurality of burners and arranging the burners so as to surely irradiate the steel plate with a flame even if the burner burns down. In this case, the burner combustion amount is continuously reduced to such an extent that the flame irradiation effect does not decrease, and when it becomes smaller than the set value, a method of extinguishing a part of the plurality of burners is adopted to continuously It becomes possible to grow an oxide film thickness.
酸化還元法での酸化に際し、板温は前述のように酸化膜厚みに影響する(図5)。これよりわかるように、板温を制御すると、酸化膜厚制御をすることができる。このような板温の制御は、前述の溶融亜鉛めっき設備のように無酸化帯または還元帯、酸化帯、還元帯を有する場合には、例えば、次のようにして行うことができる。 In the oxidation by the oxidation-reduction method, the plate temperature affects the oxide film thickness as described above (FIG. 5). As can be seen, the oxide film thickness can be controlled by controlling the plate temperature. Such control of the plate temperature can be performed, for example, as follows when the plate has a non-oxidation zone, a reduction zone, an oxidation zone, or a reduction zone as in the above-described hot dip galvanizing equipment.
即ち、酸化帯の炉温で酸化帯のバーナ燃焼量を制御することにより、板温を制御することができる。この場合、バーナの燃焼量を低下させると、火炎長が短くなり火炎が鋼板に照射する割合も低下するため、板温の低下とともに酸化皮膜成長速度の低下効果が大きい。その効果を少なくし制御性を向上させるためには、次のような方法も考えられる。酸化時の板温を制御するために、酸化帯バーナの燃焼量は一定にしておき、または、酸化帯前の無酸化帯または還元帯の炉温を用い、酸化帯の前帯(無酸化帯または還元帯)の加熱能力を制御して、酸化時の板温を制御することにより行うことができる。あるいは、酸化帯の出口板温または酸化帯の後帯(還元帯)の入側板温で、酸化帯の前帯(無酸化帯または還元帯)の加熱能力を制御して、酸化時の板温を制御することにより行うことができる。これらの方法を組み合わせて酸化時の板温を制御することもできる。 That is, the plate temperature can be controlled by controlling the burner combustion amount in the oxidation zone with the furnace temperature in the oxidation zone. In this case, when the burner combustion amount is reduced, the flame length is shortened, and the rate at which the flame irradiates the steel sheet is also reduced. Therefore, the effect of reducing the oxide film growth rate is great as the plate temperature is lowered. In order to reduce the effect and improve the controllability, the following method can be considered. In order to control the plate temperature during oxidation, the combustion amount of the oxidation zone burner is kept constant, or the furnace temperature of the non-oxidation zone or reduction zone before the oxidation zone is used, and the front zone of the oxidation zone (non-oxidation zone) Alternatively, the heating ability of the reduction zone) can be controlled to control the plate temperature during oxidation. Alternatively, the heating temperature of the front zone (non-oxidation zone or reduction zone) of the oxidation zone is controlled by the exit zone temperature of the oxidation zone or the inlet side plate temperature of the rear zone (reduction zone) of the oxidation zone. This can be done by controlling. These methods can be combined to control the plate temperature during oxidation.
これまでの酸化還元法での酸化では、無酸化帯を酸化帯として運転するのみであり、酸化膜の成長速度を制御するには空気比の制御を行ってきた。また燃焼量は、板の焼鈍条件を達成するために制御されており、酸化時の板温は制御できず、空気比により酸化膜厚を制御していたが、空気比の制御では火炎の状況が大きく変化するため効果が安定しなかった。これに対し、本発明では、無酸化帯の下流に酸化帯を設けることで、バーナの燃焼量をほぼ一定にして、酸化帯への侵入板温を前帯の燃焼量で調整することにより酸化皮膜を制御するようにすると、火炎の照射状態は一定の状態で板温で酸化膜厚制御をするため、酸化皮膜の厚みが安定することがわかった。 In the oxidation by the oxidation-reduction method so far, the non-oxidation zone is only operated as the oxidation zone, and the air ratio has been controlled to control the growth rate of the oxide film. The amount of combustion is controlled in order to achieve the annealing conditions of the plate, and the plate temperature during oxidation cannot be controlled, and the oxide film thickness is controlled by the air ratio. The effect was not stable because of a large change. In contrast, in the present invention, by providing an oxidation zone downstream of the non-oxidation zone, the combustion amount of the burner is made substantially constant, and the intrusion plate temperature to the oxidation zone is adjusted by the combustion amount of the front zone. It was found that when the film was controlled, the thickness of the oxide film was stabilized because the oxide film thickness was controlled at the plate temperature with the flame being in a constant state.
酸化膜厚を厚くしようとする場合、炉長を長くして酸化時間を長くする方法が考えられるが、設備の制約上炉の長さはあまり長くできない。また、設備制約がなく炉長を長くした場合でも、他の酸化しやすい鋼板を通す場合に酸化能力を低下させる必要があり設備が大きくなる。これに対し、本発明では急速に酸化膜を成長させるので、炉長を長くすることなく、また、ラインスピードを低下させることなく、厚い酸化皮膜を形成させることができる。 In order to increase the thickness of the oxide film, a method of lengthening the furnace length to increase the oxidation time is conceivable. However, the length of the furnace cannot be increased due to equipment limitations. Moreover, even when there is no equipment restriction and the furnace length is lengthened, it is necessary to lower the oxidation capacity when passing another easily oxidizable steel sheet, and the equipment becomes large. On the other hand, since an oxide film is rapidly grown in the present invention, a thick oxide film can be formed without increasing the furnace length and without decreasing the line speed.
本発明の場合のように酸化還元法での酸化に際して酸化膜を急速に成長させるための溶融亜鉛めっき設備としては例えば図3に示すような溶融亜鉛めっき設備を用いるとよい。この溶融亜鉛めっき設備においては、その焼鈍ラインを無酸化帯、酸化帯、還元帯の順に構成している。即ち、無酸化帯の後部に酸化帯を設ける構成にしている。 For example, a hot dip galvanizing equipment as shown in FIG. 3 may be used as a hot dip galvanizing equipment for rapidly growing an oxide film upon oxidation by the oxidation-reduction method as in the present invention. In this hot dip galvanizing equipment, the annealing line is configured in the order of a non-oxidation zone, an oxidation zone, and a reduction zone. That is, an oxidation zone is provided at the rear of the non-oxidation zone.
このような酸化帯を設けていない溶融亜鉛めっき設備の例を、図2に示す。 An example of a hot dip galvanizing facility not provided with such an oxidation zone is shown in FIG.
上記図2に示す溶融亜鉛めっき設備を用い、その無酸化帯(無酸化炉)を酸化条件で用いて酸化する場合(通常酸化時)、及び、上記図3に示す溶融亜鉛めっき設備を用い、その酸化帯で急速酸化させる場合(急速酸化時)の酸化膜厚みの炉の長さ方向の分布を図4に示す。なお、この図4において、鋼板の走行方向は図の左から右に向けてであり、ロール位置を示す矢印2本の中、右側の矢印は炉内にあるロールの位置を示すものである。 When using the hot dip galvanizing equipment shown in FIG. 2 and oxidizing the non-oxidizing zone (non-oxidizing furnace) under oxidizing conditions (normal oxidation), and using the hot dip galvanizing equipment shown in FIG. FIG. 4 shows the distribution of the oxide film thickness in the length direction of the furnace when rapid oxidation is performed in the oxidation zone (during rapid oxidation). In FIG. 4, the traveling direction of the steel sheet is from the left to the right in the figure, and the right arrow among the two arrows indicating the roll position indicates the position of the roll in the furnace.
この図4からわかるように、前者の無酸化炉を酸化条件で用いて酸化する場合(通常酸化時)には、酸化皮膜は徐々に成長するため、酸化膜厚が厚くなりつつある時点や、酸化膜厚が厚くなった時点で酸化膜が炉内にあるロールに接触する。一方、後者の酸化帯で急速酸化させる場合(急速酸化時)には、酸化速度が速いために、ロールとの接触が無く酸化膜を成長させることが可能になる。このため、後者の場合は酸化膜がはがれ難くなると考えられる。即ち、後者の場合には、無酸化炉で無酸化状態で(鋼板を酸化させることなく、あるいは、ほとんど酸化させることなく)鋼板の温度を上げておくことにより、酸化帯で急激に酸化させて酸化膜厚が急速に厚くなるので、酸化膜厚が形成される前や、酸化膜厚が僅かに形成された(極めて薄い)時点では炉の中央のロールの手前(左)のロールと接触することはあっても、酸化帯で酸化膜厚が厚くなりつつある時点や、酸化膜厚が厚くなった時点ではロールとの接触が少ない。このため、酸化膜のはがれが発生しにくくなると考えられる。また、還元炉入り口にはロールがあり、鋼板はロールと接触し酸化皮膜ははがれる恐れがある。いずれにしても、後者(図3に示すもの)の場合は、急速酸化により酸化膜厚を厚くすることが可能であり、ロールとの接触回数が減る。このため、ロールによる酸化膜のはがれやロールにはがれた酸化膜が付着することによるおし傷の発生頻度を低下させることが可能であると考えられる。 As can be seen from FIG. 4, when oxidizing using the former non-oxidizing furnace under oxidizing conditions (normally during oxidation), the oxide film grows gradually, so that the oxide film thickness is becoming thicker, When the oxide film thickness increases, the oxide film comes into contact with the roll in the furnace. On the other hand, when rapid oxidation is performed in the latter oxidation zone (during rapid oxidation), since the oxidation rate is fast, it is possible to grow an oxide film without contact with the roll. For this reason, in the latter case, it is considered that the oxide film is difficult to peel off. That is, in the latter case, the temperature of the steel plate is raised in the non-oxidizing state in a non-oxidizing furnace (without oxidizing or hardly oxidizing the steel plate), thereby rapidly oxidizing in the oxidation zone. Since the oxide film thickness increases rapidly, it comes into contact with the roll in front of the center roll (left) before the oxide film is formed or when the oxide film is slightly formed (very thin). However, there is little contact with the roll when the oxide film thickness is increasing in the oxidation zone or when the oxide film thickness is increased. For this reason, it is considered that peeling of the oxide film hardly occurs. Moreover, there is a roll at the entrance of the reduction furnace, and the steel sheet may come into contact with the roll and the oxide film may be peeled off. In any case, in the latter case (shown in FIG. 3), the oxide film thickness can be increased by rapid oxidation, and the number of contact with the roll is reduced. For this reason, it is considered possible to reduce the frequency of occurrence of scratches due to the peeling of the oxide film due to the roll and the adhesion of the oxide film peeled off to the roll.
上記図2に示す設備は水平ラインのライン構成のものである。ここで、垂直ラインのライン構成のものを図1に示す。この図1に示す垂直ラインの場合は、ロールでの板の曲率が大きいため、上記図2に示す水平ラインの場合よりも、酸化膜のはがれが起りやすいと考えられる。 The equipment shown in FIG. 2 has a horizontal line configuration. Here, a vertical line configuration is shown in FIG. In the case of the vertical line shown in FIG. 1, since the curvature of the plate at the roll is large, it is considered that the oxide film peels more easily than in the case of the horizontal line shown in FIG.
前述のように、Si含有量が多いSi含有鋼板の場合は、酸化条件ではFeが酸化し難く、還元ではSiの濃化が激しくなるため、酸化還元法での酸化により形成する酸化膜厚を厚くする必要があり、この傾向と酸化膜厚を厚くする必要性は特にSi含有量:1.8 質量%以上のSi含有鋼板の場合に顕著である。本発明に係る溶融亜鉛めっき方法は、前述のように、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、酸化還元法での酸化により形成する酸化膜の膜厚を厚くすることができる。故に、本発明に係る溶融亜鉛めっき方法は、特にSi含有量:1.8 質量%以上のSi含有鋼板の場合に用いて有用で価値がある。 As described above, in the case of a Si-containing steel sheet with a high Si content, Fe is difficult to oxidize under oxidizing conditions, and Si concentration is intense during reduction. It is necessary to increase the thickness, and this tendency and the necessity to increase the oxide film thickness are particularly remarkable in the case of a Si-containing steel sheet having a Si content of 1.8% by mass or more . As described above, the hot dip galvanizing method according to the present invention increases the thickness of the oxide film formed by oxidation in the oxidation-reduction method without reducing the line speed, without increasing the furnace length of the oxidation furnace. can do. Therefore, the hot dip galvanizing method according to the present invention is useful and valuable particularly in the case of a Si-containing steel sheet having a Si content of 1.8% by mass or more .
本発明の実施例および比較例を以下説明する。なお、本発明はこの実施例に限定されるものではなく、本発明の趣旨に適合し得る範囲で適当に変更を加えて実施することも可能であり、それらはいずれも本発明の技術的範囲に含まれる。 Examples of the present invention and comparative examples will be described below. The present invention is not limited to this embodiment, and can be implemented with appropriate modifications within a range that can be adapted to the gist of the present invention, all of which are within the technical scope of the present invention. include.
〔例1〕
予熱室、無酸化帯、酸化帯、還元帯をこの順に有する焼鈍ラインと、溶融亜鉛浴槽およびエアワイピング手段を有する溶融亜鉛めっき装置と、鋼板移送のためのロールとを有する溶融亜鉛めっき設備であって、水平ラインのものを用い、下記のようにして溶融亜鉛めっき鋼板を得た。
[Example 1]
A hot dip galvanizing facility having an annealing line having a preheating chamber, a non-oxidation zone, an oxidation zone, and a reduction zone in this order, a hot dip galvanizing apparatus having a hot dip galvanizing bath and air wiping means, and a roll for transferring steel plates. Using a horizontal line, a hot dip galvanized steel sheet was obtained as follows.
C:0.1 質量%、Si:1.8 質量%、Mn:1.5 質量%、残部がFeおよび不可避的不純物からなる鋼成分を有する高張力鋼板を、予熱室で400 ℃に予熱した後、無酸化炉で700 ℃まで加熱する。この後、酸化炉で、鋼板に対して火炎を照射するバーナを用いて鋼板を850 ℃まで加熱する。このとき、バーナの燃焼空気での空気比は、1.2 である。これにより、鋼板表面に酸化膜を成長させて形成する。この酸化膜成長速度は560Å/sであり、形成された酸化膜の厚みは5600Åである。 C: 0.1% by mass, Si: 1.8% by mass, Mn: 1.5% by mass, a high-tensile steel plate having a steel component consisting of Fe and inevitable impurities in the balance is preheated to 400 ° C. in a preheating chamber, Heat to 700 ° C. Thereafter, the steel plate is heated to 850 ° C. using a burner that irradiates the steel plate with flame in an oxidation furnace. At this time, the air ratio in the burner combustion air is 1.2. Thereby, an oxide film is grown and formed on the steel plate surface. The growth rate of the oxide film is 560 s / s, and the thickness of the formed oxide film is 5600 Å.
上記酸化皮膜を形成した鋼板を水素雰囲気(空気および水素の混合ガスで、該ガス中の水素濃度:15体積%である雰囲気)の還元炉に投入し、この還元炉で酸化皮膜を還元する処理をした後、溶融亜鉛浴中を通して溶融亜鉛めっきし、次いでエアワイピングでめっき量を50g/m2に調整し、溶融亜鉛めっき鋼板を得た(No.1)。なお、上記還元炉に入ってくる鋼板の温度は850 ℃である。還元炉の炉温は900 ℃である。 The steel sheet on which the oxide film has been formed is put into a reduction furnace in a hydrogen atmosphere (air mixture of air and hydrogen, and the hydrogen concentration in the gas is 15% by volume), and the oxide film is reduced in this reduction furnace Then, hot dip galvanizing was performed through a hot dip galvanizing bath, and then the plating amount was adjusted to 50 g / m 2 by air wiping to obtain a hot dip galvanized steel sheet (No. 1). The temperature of the steel sheet entering the reduction furnace is 850 ° C. The furnace temperature of the reduction furnace is 900 ° C.
上記のことからわかるように、鋼板を無酸化炉で高温まで加熱しておき、この後、酸化炉でバーナによる火炎照射等により更に高温に加熱すると、酸化膜成長速度を非常に大きくすることができる。 As can be seen from the above, heating the steel sheet to a high temperature in a non-oxidizing furnace and then heating it further to a higher temperature by means of flame irradiation with a burner in an oxidizing furnace can greatly increase the oxide film growth rate. it can.
〔例2〕
酸化炉でのバーナによる火炎照射に際し、バーナの燃焼空気に水蒸気を燃焼空気量に対して10体積%の流量で投入し、この点を除き例1の場合と同様の方法により溶融亜鉛めっき鋼板を得た(No.2)。この酸化炉での酸化による酸化膜成長速度は770Å/sであり、この酸化により形成された酸化膜の厚みは7700Åである。
[Example 2]
In the flame irradiation by the burner in the oxidation furnace, steam is introduced into the burner combustion air at a flow rate of 10% by volume with respect to the amount of combustion air. Except for this point, the hot dip galvanized steel sheet is prepared in the same manner as in Example 1. Obtained (No. 2). The oxide film growth rate by oxidation in this oxidation furnace is 770 Å / s, and the thickness of the oxide film formed by this oxidation is 7700 Å.
〔例3〕
酸化炉でのバーナによる火炎照射に際し、バーナの燃焼空気に酸素を燃焼空気量に対して5体積%の流量で投入し、この点を除き例1の場合と同様の方法により溶融亜鉛めっき鋼板を得た(No.3)。この酸化炉での酸化による酸化膜成長速度は620Å/sであり、この酸化により形成された酸化膜の厚みは6200Åである。
[Example 3]
When irradiating the flame with the burner in the oxidation furnace, oxygen was introduced into the burner combustion air at a flow rate of 5% by volume with respect to the amount of combustion air. Except for this point, the hot dip galvanized steel sheet was prepared in the same manner as in Example 1. Obtained (No. 3). The oxide film growth rate by oxidation in this oxidation furnace is 620 Å / s, and the thickness of the oxide film formed by this oxidation is 6200 Å.
〔例4〕
酸化炉でのバーナによる火炎照射に際し、バーナの燃焼空気に酸素を5体積%の流量で投入すると共に水蒸気を10体積%の流量で投入し、この点を除き例1の場合と同様の方法により溶融亜鉛めっき鋼板を得た(No.4)。この酸化炉での酸化による酸化膜成長速度は850Å/sであり、この酸化により形成された酸化膜の厚みは8500Åである。
[Example 4]
When igniting the flame with the burner in the oxidation furnace, oxygen was introduced into the burner combustion air at a flow rate of 5% by volume and water vapor was introduced at a flow rate of 10% by volume. A hot dip galvanized steel sheet was obtained (No. 4). The oxide film growth rate by oxidation in this oxidation furnace is 850 Å / s, and the thickness of the oxide film formed by this oxidation is 8500 Å.
〔例5〕
無酸化炉では600 ℃まで加熱し、酸化炉では750 ℃まで加熱した。酸化炉でのバーナによる火炎照射に際し、バーナの燃焼空気に酸素を5体積%の流量で投入すると共に水蒸気を10体積%の流量で投入した。これらの点を除き、例1の場合と同様の方法により溶融亜鉛めっき鋼板を得た(No.5)。この酸化炉での酸化による酸化膜成長速度は180Å/sであり、この酸化により形成された酸化膜の厚みは1800Åである。なお、還元炉に入ってくる鋼板の温度は750 ℃である。この還元炉の炉温は、800 ℃である(例1の場合と異なる)。
[Example 5]
The non-oxidizing furnace was heated to 600 ° C, and the oxidizing furnace was heated to 750 ° C. During the flame irradiation by the burner in the oxidation furnace, oxygen was introduced into the combustion air of the burner at a flow rate of 5% by volume and water vapor was introduced at a flow rate of 10% by volume. Except for these points, a hot-dip galvanized steel sheet was obtained by the same method as in Example 1 (No. 5). The oxide film growth rate by oxidation in this oxidation furnace is 180 Å / s, and the thickness of the oxide film formed by this oxidation is 1800 Å. The temperature of the steel sheet entering the reduction furnace is 750 ° C. The furnace temperature of this reduction furnace is 800 ° C. (different from the case of Example 1).
〔例6〕
例1の場合と同様の鋼板を予熱室で400 ℃に予熱した後、無酸化炉で700 ℃まで加熱する。この後、酸化炉でバーナにより鋼板に火炎照射するのではなく、雰囲気酸化という方法により、鋼板を850 ℃まで加熱する。これにより、鋼板表面に酸化膜を成長させて形成する。この酸化膜成長速度は50Å/sであり、形成された酸化膜の厚みは500Åである。
[Example 6]
A steel plate similar to that in Example 1 is preheated to 400 ° C in a preheating chamber, and then heated to 700 ° C in a non-oxidizing furnace. Thereafter, the steel sheet is heated to 850 ° C. by a method called atmospheric oxidation, instead of irradiating the steel sheet with a flame in an oxidation furnace. Thereby, an oxide film is grown and formed on the steel plate surface. The growth rate of the oxide film is 50 Å / s, and the thickness of the formed oxide film is 500 Å.
上記酸化皮膜の形成の後、例1の場合と同様の方法により還元処理、溶融亜鉛めっき、エアワイピングによるめっき量の調整をし、溶融亜鉛めっき鋼板を得た(No.6)。 After the formation of the oxide film, the amount of plating by reduction treatment, hot dip galvanizing, and air wiping was adjusted in the same manner as in Example 1 to obtain a hot dip galvanized steel sheet (No. 6).
〔例7〕
例1の場合と同様の鋼板を予熱室で400 ℃に予熱した後、無酸化炉を酸化で運転し、700 ℃まで加熱する。ただし、この無酸化炉のバーナ空気比は1.2 であるという雰囲気とした。このため、上記無酸化炉での加熱の際、鋼板は酸化されて酸化膜が形成される。この酸化膜の膜厚は、2000Åである。この酸化膜成長速度は100Å/sである。
[Example 7]
A steel plate similar to that in Example 1 is preheated to 400 ° C. in a preheating chamber, and then a non-oxidizing furnace is operated by oxidation and heated to 700 ° C. However, the atmosphere was such that the burner air ratio of this non-oxidizing furnace was 1.2. For this reason, when heating in the non-oxidizing furnace, the steel sheet is oxidized to form an oxide film. The thickness of this oxide film is 2000 mm. The oxide film growth rate is 100 Å / s.
この後、例1の場合と同様の方法により、酸化炉での850 ℃までの加熱、還元処理、溶融亜鉛めっき、エアワイピングによるめっき量の調整をし、溶融亜鉛めっき鋼板を得た(No.7)。 Thereafter, in the same manner as in Example 1, heating up to 850 ° C. in an oxidation furnace, reduction treatment, hot dip galvanizing, and adjustment of the plating amount by air wiping were performed to obtain a hot dip galvanized steel sheet (No. 7).
このとき、酸化炉での酸化による酸化膜成長速度は180Å/sであり、この酸化で形成された酸化膜の厚みは1800Åである。 At this time, the growth rate of the oxide film by oxidation in the oxidation furnace is 180 Å / s, and the thickness of the oxide film formed by this oxidation is 1800 Å.
上記無酸化炉で形成された酸化膜の厚みと酸化炉で形成された酸化膜の厚みを合計すると、3800Åである。酸化還元法によるめっき性の向上の点からは、この合計厚みが重要である。上記無酸化炉および酸化炉での酸化膜成長速度は、130Å/sである。ロールとの接触による酸化膜のはがれの防止の点からは、かかる酸化膜のはがれに対し、この無酸化炉および酸化炉での酸化膜成長速度も影響するが、比較的酸化膜が厚いときに問題となるので、酸化炉での酸化膜成長速度の方が重要である。 The sum of the thickness of the oxide film formed in the non-oxidation furnace and the thickness of the oxide film formed in the oxidation furnace is 3800 mm. This total thickness is important from the viewpoint of improving the plating property by the oxidation-reduction method. The oxide film growth rate in the non-oxidation furnace and the oxidation furnace is 130 Å / s. From the standpoint of preventing peeling of the oxide film due to contact with the roll, this oxide film peeling also affects the oxide film growth rate in this non-oxidation furnace and oxidation furnace, but when the oxide film is relatively thick Since it becomes a problem, the oxide film growth rate in the oxidation furnace is more important.
〔結果〕
このようにして得られた溶融亜鉛めっき鋼板について、めっきの特性を調べた。その結果を表1に示す。
〔result〕
The galvanized steel sheet thus obtained was examined for plating characteristics. The results are shown in Table 1.
No.1〜4 の場合、酸化膜成長速度が560〜850Å/sであり、形成された酸化膜の厚みが5600〜8500Åであって厚い。このため、めっき外観が良好な亜鉛めっき鋼板を得られた。 In the case of Nos. 1 to 4, the oxide film growth rate is 560 to 850 Å / s, and the thickness of the formed oxide film is 5600 to 8500 Å, which is thick. For this reason, the galvanized steel plate with a favorable plating external appearance was obtained.
No.5の場合、酸化膜成長速度が180Å/sと低く、形成された酸化膜の厚みが1800Åと薄い。このため、点状の不めっきが発生し、良好な亜鉛めっき鋼板は得られなかった。 In the case of No. 5, the oxide film growth rate is as low as 180 Å / s, and the thickness of the formed oxide film is as thin as 1800 Å. For this reason, dot-like non-plating generate | occur | produced and the favorable galvanized steel plate was not obtained.
No.6の場合、酸化膜成長速度が50Å/sと低く、形成された酸化膜の厚みが500Åと薄い。このため、点状の不めっきが発生し、良好な亜鉛めっき鋼板は得られなかった。 In the case of No. 6, the oxide film growth rate is as low as 50 cm / s, and the thickness of the formed oxide film is as thin as 500 mm. For this reason, dot-like non-plating generate | occur | produced and the favorable galvanized steel plate was not obtained.
No.7の場合、酸化炉での酸化膜成長速度が130Å/sと低く、形成された酸化膜の厚みが3800Åと薄い。このため、点状の不めっきが発生し、良好な亜鉛めっき鋼板は得られなかった。 In the case of No. 7, the oxide film growth rate in the oxidation furnace is as low as 130 Å / s, and the thickness of the formed oxide film is as thin as 3800 Å. For this reason, dot-like non-plating generate | occur | produced and the favorable galvanized steel plate was not obtained.
本発明に係る溶融亜鉛めっき方法によれば、Si含有量:1.8 質量%以上のSi含有鋼板を酸化還元法により酸化還元した後、溶融亜鉛めっきするに際し、ラインスピードを低下させることなく、酸化炉の炉長を長くすることなく、前記酸化還元法での酸化により形成する酸化膜の膜厚を厚くすることができるので、Si含有量:1.8 質量%以上のSi含有鋼板を基材として不めっきのない亜鉛めっき鋼板あるいは合金化溶融亜鉛めっき鋼板を製造しようとする際に好適に用いることができる。 According to the hot dip galvanizing method of the present invention, the Si content: 1.8% by mass or more of the Si-containing steel plate is oxidized and reduced by the oxidation-reduction method, and then hot-dip galvanized without reducing the line speed. Since the thickness of the oxide film formed by oxidation by the oxidation-reduction method can be increased without lengthening the furnace length of Si , the Si content: 1.8% by mass or more of the Si-containing steel plate as a base material is not plated. When it is going to manufacture a galvanized steel plate without alloy or a galvannealed steel plate, it can use suitably .
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| CN2011102093331A CN102260842B (en) | 2004-12-21 | 2005-12-21 | Method and facility for hot dip zinc plating |
| US11/722,410 US8216695B2 (en) | 2004-12-21 | 2005-12-21 | Method and facility for hot dip zinc plating |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP4701852B2 (en) * | 2005-06-16 | 2011-06-15 | Jfeスチール株式会社 | Method for producing hot-dip galvanized steel sheet |
| EP2010690B1 (en) * | 2006-04-26 | 2010-02-24 | ThyssenKrupp Steel Europe AG | Hot dip coating process for a steel plate product made of high strengthheavy-duty steel |
| JP4563347B2 (en) * | 2006-06-21 | 2010-10-13 | 株式会社神戸製鋼所 | Steel plate pretreatment method in hot dip galvanizing annealing furnace |
| EP2009127A1 (en) * | 2007-06-29 | 2008-12-31 | ArcelorMittal France | Process for manufacturing a galvanized or a galvannealed steel sheet by DFF regulation |
| KR101079472B1 (en) * | 2008-12-23 | 2011-11-03 | 주식회사 포스코 | Method for Manufacturing High Manganese Hot Dip Galvanizing Steel Sheet with Superior Surface Property |
| JP5863464B2 (en) * | 2012-01-11 | 2016-02-16 | 株式会社神戸製鋼所 | Annealing furnace of hot dip galvanizing equipment and operation method in the annealing furnace |
| JP7148438B2 (en) * | 2018-03-05 | 2022-10-05 | 株式会社神戸製鋼所 | Oxide film thickness measurement method |
| CN112143992A (en) * | 2020-10-23 | 2020-12-29 | 杭州创力科技服务有限公司 | Temperature-variable oxidation-reduction integrated pretreatment process and treatment device thereof |
| WO2024014372A1 (en) * | 2022-07-12 | 2024-01-18 | Jfeスチール株式会社 | Method for heating steel plate, method for producing plated steel plate, direct-fired heating furnace, and continuous hot-dip galvanizing equipment |
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| CN101057004A (en) | 2007-10-17 |
| JP2006176806A (en) | 2006-07-06 |
| CN101057004B (en) | 2012-07-04 |
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