JP2020139232A - Manufacturing method and facility of surface-treatment metal strip - Google Patents

Manufacturing method and facility of surface-treatment metal strip Download PDF

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JP2020139232A
JP2020139232A JP2020030265A JP2020030265A JP2020139232A JP 2020139232 A JP2020139232 A JP 2020139232A JP 2020030265 A JP2020030265 A JP 2020030265A JP 2020030265 A JP2020030265 A JP 2020030265A JP 2020139232 A JP2020139232 A JP 2020139232A
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decompression chamber
metal band
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treatment liquid
decompression
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JP6992828B2 (en
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広和 杉原
Hirokazu Sugihara
広和 杉原
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JFE Steel Corp
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Abstract

To provide a manufacturing method of a surface-treatment metal strip capable of executing inexpensively a process including dehydration after application of surface-treatment liquid.SOLUTION: A manufacturing method of a surface-treatment metal strip in a continuous line has a surface treatment step for applying surface-treatment liquid x onto the surface of the metal strip, and a drying step for drying the surface-treatment liquid x applied onto the metal strip surface in the surface treatment step. In the drying step, the metal strip is passed through a decompression chamber A decompressed below atmospheric pressure, preferably, to a vapor pressure or lower of a solvent of the surface-treatment liquid, to thereby evaporate the solvent of the surface-treatment liquid x adhering onto the metal strip surface in the decompression chamber A.SELECTED DRAWING: Figure 1

Description

本発明は、表面処理金属帯の製造方法及び設備、詳細には金属帯に塗布した表面処理液の乾燥方法に特徴を有する表面処理金属帯の製造方法及び設備に関するものであり、特に、亜鉛めっき鋼板や溶融亜鉛めっき鋼板にクロメートフリー表面処理を施して表面処理亜鉛めっき鋼板を製造する場合に好適な製造技術である。 The present invention relates to a method and equipment for producing a surface-treated metal band, specifically, a method and equipment for producing a surface-treated metal band characterized by a method for drying a surface-treated liquid applied to the metal band, and in particular, galvanizing. This is a manufacturing technique suitable for producing a surface-treated galvanized steel sheet by subjecting a steel sheet or a hot-dip galvanized steel sheet to a chromate-free surface treatment.

従来、鋼帯などの金属材料(以下、鋼帯を例に説明する)の表面に耐食性、耐熱性、耐指紋性、塗装性などの特性を付与するための表面処理法として、クロメート処理が広く行われてきた。しかし、近年、クロメート処理は環境負荷が大きいという理由から、クロメートを用いないクロメートフリー表面処理の開発が行われている。 Conventionally, chromate treatment has been widely used as a surface treatment method for imparting properties such as corrosion resistance, heat resistance, fingerprint resistance, and paintability to the surface of a metal material such as a steel strip (hereinafter, a steel strip will be described as an example). It has been done. However, in recent years, chromate-free surface treatments that do not use chromate have been developed because chromate treatment has a large environmental load.

乾燥後膜厚が同じ場合、クロメートフリー表面処理皮膜は、クロメート処理皮膜に比べて耐食性などの必要特性が低下するため、クロメートフリー表面処理では、より厚い皮膜を形成する必要がある。厚い皮膜を形成するには、(i)処理液の塗布量を多くして塗布膜厚を厚くする、(ii)処理液の固形分濃度を高くする、という方法がある。しかし、前者の方法では、乾燥に必要な熱量が多くなるため製造コストが増大する。一方、後者の方法では、ロールコーターなど、ロールを用いた塗装をする際に皮膜欠陥の発生リスクが高くなる。
また、従来では塗料(表面処理液)の溶媒として有機溶剤が使用されることも多かったが、近年では、環境負荷低減のために溶媒を水系にする傾向が強くなっている。
When the film thickness after drying is the same, the chromate-free surface treatment film has lower required properties such as corrosion resistance than the chromate-treated film, so that it is necessary to form a thicker film in the chromate-free surface treatment. To form a thick film, there are methods of (i) increasing the coating amount of the treatment liquid to increase the coating film thickness, and (ii) increasing the solid content concentration of the treatment liquid. However, in the former method, the amount of heat required for drying increases, so that the manufacturing cost increases. On the other hand, in the latter method, the risk of film defects increases when painting with a roll such as a roll coater.
Further, in the past, an organic solvent was often used as a solvent for paints (surface treatment liquids), but in recent years, there has been a strong tendency to use an aqueous solvent in order to reduce the environmental load.

以下、鋼帯に水性塗料(水系表面処理液)を塗装する場合を例に、従来行われている塗膜の乾燥焼付方法とその課題について説明する。
連続ラインにおいて鋼帯に水性塗料を塗装する場合、ロールコーターなどの連続塗装装置で鋼帯に水性塗料を塗装して塗膜を形成し、続いて乾燥焼付装置により塗膜を乾燥焼付けする。従来使用されている乾燥焼付装置には、熱風加熱炉、誘導加熱炉、赤外線加熱炉などがあり、また、これらの加熱炉を組み合わせたものも用いられている。
例えば、特許文献1には、熱風加熱炉と誘導加熱炉からなる乾燥焼付装置を用いた塗装鋼板の焼付け方法として、前段の熱風加熱炉において塗膜の1次乾燥を行い、後段の誘導加熱炉において塗膜の最終乾燥と焼付を行う方法が開示されている。
Hereinafter, a conventional method for drying and baking a coating film and its problems will be described by taking as an example a case where a water-based paint (water-based surface treatment liquid) is applied to a steel strip.
When the water-based paint is applied to the steel strip in the continuous line, the water-based paint is applied to the steel strip with a continuous coating device such as a roll coater to form a coating film, and then the coating film is dried and baked by a drying baking device. Conventionally used drying and baking apparatus include a hot air heating furnace, an induction heating furnace, an infrared heating furnace, and the like, and a combination of these heating furnaces is also used.
For example, in Patent Document 1, as a method of baking a coated steel sheet using a drying baking apparatus including a hot air heating furnace and an induction heating furnace, the coating film is first dried in the hot air heating furnace in the first stage, and the induction heating furnace in the latter stage. Discloses a method for final drying and baking of a coating film.

特開昭63−190681号公報JP-A-63-190681

誘導加熱炉は、鋼帯を誘導加熱することで塗膜を乾燥焼付けするものであり、鋼帯を高温に加熱することにより、塗膜の乾燥焼付け速度を高めている。また、熱風加熱炉などの他の加熱炉でも、乾燥焼付け過程で鋼帯はある程度の高温状態になる。
鋼帯の塗装ラインでは、最終工程でオペレータによる塗膜の検査が行われるため、その検査のために鋼帯は常温近くまで冷却される必要がある。塗膜の乾燥焼付け後の冷却方法としては、水冷却は塗膜が劣化する問題があるため、通常、ガス冷却や圧縮空気による空冷が行われるが、このような冷却にもエネルギーコストが余計にかかる。また、膜厚が厚い場合、蒸発させなければならない水分量が多くなり、乾燥に必要なエネルギーが大きくなるという課題もある。
In the induction heating furnace, the coating film is dried and baked by inducing heating the steel strip, and the drying and baking rate of the coating film is increased by heating the steel strip to a high temperature. Further, in other heating furnaces such as a hot air heating furnace, the steel strip becomes a high temperature state to some extent during the drying and baking process.
In the steel strip coating line, the coating film is inspected by the operator in the final process, so the steel strip needs to be cooled to near room temperature for the inspection. As a cooling method after drying and baking the coating film, water cooling has a problem of deterioration of the coating film, so gas cooling or air cooling with compressed air is usually performed, but such cooling also requires extra energy cost. It takes. Further, when the film thickness is thick, the amount of water that must be evaporated increases, and there is also a problem that the energy required for drying increases.

本発明は、上記課題に鑑みなされたものであって、その目的は、表面処理液塗布後の乾燥を含めた工程を低コストで実施することができる表面処理金属帯の製造方法を提供することにある。 The present invention has been made in view of the above problems, and an object of the present invention is to provide a method for producing a surface-treated metal band, which can carry out a process including drying after applying a surface-treating liquid at low cost. It is in.

本発明者は、上記課題を解決するために検討を重ねた結果、連続ラインにおいて金属帯表面に塗布された表面処理液を乾燥させる方法として、金属帯を大気圧未満、好ましくは表面処理液の溶媒の蒸気圧以下に減圧された減圧室に導入し、この減圧室において表面処理液の溶媒を揮発させることにより表面処理液を乾燥させるという新たな方法を創案した。
すなわち、上記課題を解決するための本発明の要旨は以下のとおりである。
As a result of repeated studies to solve the above problems, the present inventor, as a method for drying the surface treatment liquid applied to the surface of the metal band in a continuous line, applies a metal band below atmospheric pressure, preferably a surface treatment liquid. A new method was devised in which the surface treatment liquid was dried by introducing it into a decompression chamber whose pressure was reduced below the vapor pressure of the solvent and volatilizing the solvent of the surface treatment liquid in this decompression chamber.
That is, the gist of the present invention for solving the above problems is as follows.

[1]連続ラインにおける表面処理金属帯の製造方法であって、
金属帯の表面に表面処理液(x)を塗布する表面処理工程と、
該表面処理工程で金属帯表面に塗布された表面処理液(x)を乾燥させる乾燥工程を有し、
該乾燥工程では、金属帯を大気圧未満に減圧された減圧室(A)を通過させ、該減圧室(A)において、金属帯表面に付着した表面処理液(x)の溶媒を揮発させることを特徴とする表面処理金属帯の製造方法。
[2]上記[1]の製造方法において、減圧室(A)が表面処理液(x)の溶媒の蒸気圧以下(但し、溶媒が蒸気圧が異なる2種以上の液体からなる場合には、蒸気圧が低い方の液体の蒸気圧以下)に減圧されていることを特徴とする表面処理金属帯の製造方法。
[3]上記[2]の製造方法において、表面処理液(x)の溶媒の主成分が水であり、減圧室(A)が605Pa以上101kPa以下に減圧されていることを特徴とする表面処理金属帯の製造方法。
[1] A method for manufacturing a surface-treated metal band in a continuous line.
The surface treatment process of applying the surface treatment liquid (x) to the surface of the metal band,
The surface treatment step includes a drying step of drying the surface treatment liquid (x) applied to the surface of the metal strip.
In the drying step, the metal band is passed through a decompression chamber (A) decompressed to less than atmospheric pressure, and the solvent of the surface treatment liquid (x) adhering to the surface of the metal band is volatilized in the decompression chamber (A). A method for producing a surface-treated metal strip, which comprises.
[2] In the production method of the above [1], when the pressure reducing chamber (A) is equal to or lower than the vapor pressure of the vapor pressure of the surface treatment liquid (x) (however, when the solvent consists of two or more liquids having different vapor pressures), A method for producing a surface-treated metal band, characterized in that the vapor pressure is reduced to the vapor pressure of the liquid having the lower vapor pressure or less).
[3] In the production method of the above [2], the main component of the solvent of the surface treatment liquid (x) is water, and the pressure reducing chamber (A) is reduced to 605 Pa or more and 101 kPa or less. Manufacturing method of metal strip.

[4]上記[1]〜[3]のいずれかの製造方法において、減圧室(A)は、主減圧室(a)と、その入側及び出側にそれぞれ付設された予備減圧室(b1),(b2)とを有し、金属帯を、大気圧未満に減圧された両予備減圧室(b1),(b2)を通じて主減圧室(a)を通過させることを特徴とする表面処理金属帯の製造方法。
[5]上記[1]〜[4]のいずれかの製造方法において、減圧室(A)の入側にロールコーターを設け、該ロールコーターにより金属帯表面に表面処理液(x)を塗布することを特徴とする表面処理金属帯の製造方法。
[6]上記[1]〜[5]のいずれかの製造方法において、減圧室(A)の内部、減圧室(A)の入側直前の位置、減圧室(A)の出側直後の位置のうちの少なくとも1箇所に加熱装置を設け、該加熱装置により金属帯を加熱することを特徴とする表面処理金属帯の製造方法。
[7]上記[1]〜[6]のいずれかの製造方法において、減圧室(A)の内部、減圧室(A)の入側直前の位置、減圧室(A)の出側直後の位置のうちの少なくとも1箇所に制振装置を設け、該制振装置により金属帯の振動を抑制することを特徴とする表面処理金属帯の製造方法。
[4] In any of the manufacturing methods [1] to [3] above, the decompression chamber (A) is the main decompression chamber (a) and the preliminary decompression chambers (b) provided on the inlet and outlet sides thereof, respectively. It has 1 ) and (b 2 ), and is characterized by passing the metal band through the main decompression chamber (a) through both preliminary decompression chambers (b 1 ) and (b 2 ) decompressed below atmospheric pressure. A method for manufacturing a surface-treated metal band.
[5] In any of the above-mentioned production methods [1] to [4], a roll coater is provided on the entrance side of the decompression chamber (A), and the surface treatment liquid (x) is applied to the surface of the metal band by the roll coater. A method for producing a surface-treated metal band.
[6] In any of the above [1] to [5] manufacturing methods, the inside of the decompression chamber (A), the position immediately before the entry side of the decompression chamber (A), and the position immediately after the exit side of the decompression chamber (A). A method for producing a surface-treated metal band, which comprises providing a heating device at at least one of the heating devices and heating the metal band by the heating device.
[7] In any of the manufacturing methods [1] to [6] above, the inside of the decompression chamber (A), the position immediately before the entry side of the decompression chamber (A), and the position immediately after the exit side of the decompression chamber (A). A method for producing a surface-treated metal band, which comprises providing a vibration damping device at at least one of the vibration damping devices and suppressing the vibration of the metal band by the vibration damping device.

[8]上記[4]の製造方法において、減圧室(A)の入側にロールコーターを設け、該ロールコーターにより金属帯表面に表面処理液(x)を塗布し、且つ主減圧室(a)の出側に付設された予備減圧室(b2)内に制振装置を設け、該制振装置により金属帯の振動を抑制することを特徴とする表面処理金属帯の製造方法。
[9]上記[5]又は[8]の製造方法において、ロールコーターを構成する上下1対の塗布ロールが、金属帯を拘束しつつ減圧室(A)の入口方向に送り出すことにより、金属帯を減圧室(A)内に水平通板するように案内することを特徴とする表面処理金属帯の製造方法。
[10]上記[7]又は[8]の製造方法において、制振装置は、抑えロール、非接触式の電磁式制振装置の中から選ばれる1種以上であることを特徴とする表面処理金属帯の製造方法。
[11]上記[4]又は[8]の製造方法において、主減圧室(a)の入側に付設された予備減圧室(b1)内に加熱装置を設け、該加熱装置により金属帯を加熱することを特徴とする表面処理金属帯の製造方法。
[12]上記[6]又は[11]の製造方法において、加熱装置で金属帯を加熱することにより、表面処理液(x)の溶媒の蒸気圧を調整することを特徴とする表面処理金属帯の製造方法。
[13]上記[1]〜[12]のいずれかの製造方法において、減圧室(A)を通過する際の金属帯の温度に応じて、減圧室(A)内の圧力を制御することを特徴とする表面処理金属帯の製造方法。
[8] In the manufacturing method of the above [4], a roll coater is provided on the entrance side of the decompression chamber (A), the surface treatment liquid (x) is applied to the surface of the metal band by the roll coater, and the main decompression chamber (a) is used. A method for manufacturing a surface-treated metal band, which comprises providing a vibration damping device in a preliminary decompression chamber (b 2 ) attached to the exit side of the metal band and suppressing the vibration of the metal band by the vibration damping device.
[9] In the manufacturing method of the above [5] or [8], a pair of upper and lower coating rolls constituting the roll coater are sent out toward the inlet of the decompression chamber (A) while restraining the metal band, thereby causing the metal band. A method for producing a surface-treated metal strip, which comprises guiding the metal strip to be horizontally passed through the decompression chamber (A).
[10] In the manufacturing method of the above [7] or [8], the vibration damping device is one or more selected from a suppression roll and a non-contact electromagnetic vibration damping device. Manufacturing method of metal strip.
[11] In the manufacturing method of [4] or [8] above, a heating device is provided in the preliminary decompression chamber (b 1 ) provided on the entrance side of the main decompression chamber (a), and the metal band is formed by the heating device. A method for producing a surface-treated metal strip, which comprises heating.
[12] In the production method of [6] or [11] above, the surface-treated metal strip is characterized in that the vapor pressure of the solvent of the surface-treating liquid (x) is adjusted by heating the metal strip with a heating device. Manufacturing method.
[13] In any of the production methods [1] to [12] above, controlling the pressure in the decompression chamber (A) according to the temperature of the metal band when passing through the decompression chamber (A). A method for producing a characteristic surface-treated metal band.

[14]連続ラインによる表面処理金属帯の製造設備であって、
金属帯の表面に表面処理液(x)を塗布する表面処理設備と、
該表面処理設備で金属帯表面に塗布された表面処理液(x)を乾燥させる乾燥設備を有し、
該乾燥設備は金属帯を通過させる減圧室(A)を有し、該減圧室(A)において、金属帯表面に付着した表面処理液(x)の溶媒を揮発させるようにしたことを特徴とする表面処理金属帯の製造設備。
[15]上記[14]の製造設備において、減圧室(A)は、主減圧室(a)と、その入側及び出側にそれぞれ付設された予備減圧室(b1),(b2)とを有し、金属帯を両予備減圧室(b1),(b2)を通じて主減圧室(a)を通過させるようにしたことを特徴とする表面処理金属帯の製造設備。
[14] A facility for manufacturing surface-treated metal strips using a continuous line.
Surface treatment equipment that applies surface treatment liquid (x) to the surface of the metal strip,
The surface treatment facility has a drying facility for drying the surface treatment liquid (x) applied to the surface of the metal strip.
The drying facility has a decompression chamber (A) through which the metal band passes, and the decompression chamber (A) is characterized in that the solvent of the surface treatment liquid (x) adhering to the surface of the metal band is volatilized. Surface-treated metal strip manufacturing equipment.
[15] In the manufacturing equipment of [14] above, the decompression chamber (A) is the main decompression chamber (a) and the preliminary decompression chambers (b 1 ) and (b 2 ) attached to the inlet and outlet sides thereof, respectively. A surface-treated metal band manufacturing facility characterized in that the metal band is allowed to pass through the main decompression chamber (a) through both preliminary decompression chambers (b 1 ) and (b 2 ).

本発明によれば、連続ラインにおいて金属帯表面に塗布された表面処理液を、金属帯を高温に加熱することなく乾燥させることができる。このため乾燥後の冷却工程が不要となり、表面処理金属帯の製造コストを低減することができる。 According to the present invention, the surface treatment liquid applied to the surface of the metal band in the continuous line can be dried without heating the metal band to a high temperature. Therefore, the cooling step after drying becomes unnecessary, and the manufacturing cost of the surface-treated metal band can be reduced.

本発明の製造方法と製造設備の一実施形態を模式的に示す説明図Explanatory drawing which shows typically one Embodiment of the manufacturing method and manufacturing equipment of this invention. 本発明の製造方法と製造設備の他の実施形態を模式的に示す説明図Explanatory drawing which shows typically the manufacturing method of this invention and other embodiment of manufacturing equipment 本発明の実施形態において、鋼帯制振用の抑えロールを利用したロールシール機構の一例を示す説明図Explanatory drawing which shows an example of the roll seal mechanism using the holding roll for vibration damping of a steel strip in embodiment of this invention

本発明は、連続ラインにおける表面処理金属帯の製造方法であって、金属帯の表面に表面処理液xを塗布する表面処理工程と、この表面処理工程で金属帯表面に塗布された表面処理液xを乾燥させる乾燥工程を有し、この乾燥工程では、金属帯を大気圧未満、好ましくは表面処理液の溶媒の蒸気圧以下に減圧された減圧室Aを通過させ、この減圧室Aにおいて、金属帯表面に付着した表面処理液xの溶媒を揮発させるものである。以下、金属帯が鋼帯である場合を例に説明するが、本発明は鋼帯以外の種々の金属帯の表面処理に適用することができる。 The present invention is a method for producing a surface-treated metal band in a continuous line, which comprises a surface treatment step of applying a surface treatment liquid x to the surface of the metal band and a surface treatment liquid applied to the surface of the metal band in this surface treatment step. It has a drying step of drying x, in which the metal band is passed through a decompression chamber A decompressed below atmospheric pressure, preferably below the vapor pressure of the solvent of the surface treatment solution, and in this decompression chamber A, It volatilizes the solvent of the surface treatment liquid x adhering to the surface of the metal band. Hereinafter, the case where the metal strip is a steel strip will be described as an example, but the present invention can be applied to the surface treatment of various metal strips other than the steel strip.

一般に、液体状態の物質が大気圧未満の減圧下、特に蒸気圧以下の減圧下に置かれると、液体状態でいることが難しくなり、気化が促進される。表面処理液xの溶媒が水の場合、水の蒸気圧は100℃で約101kPa、20℃で約2kPaになる。表面処理液xの溶媒である水は、その蒸気圧を超える圧力であっても大気圧未満の減圧下であれば気化が進行し、表面処理液xを乾燥させることができるが、例えば、鋼帯の温度が20℃であれば、その表面に付着した表面処理液xの溶媒の温度も概ね20℃になるため、蒸気圧以下である2kPa以下の減圧下に置くことにより、乾燥をより促進させることができる。 In general, when a substance in a liquid state is placed under a reduced pressure below atmospheric pressure, particularly under a reduced pressure below a vapor pressure, it becomes difficult to be in a liquid state and vaporization is promoted. When the solvent of the surface treatment liquid x is water, the vapor pressure of water is about 101 kPa at 100 ° C. and about 2 kPa at 20 ° C. Water, which is the solvent of the surface treatment liquid x, vaporizes even if the pressure exceeds the vapor pressure under a reduced pressure of less than atmospheric pressure, and the surface treatment liquid x can be dried. If the temperature of the band is 20 ° C., the temperature of the solvent of the surface treatment liquid x adhering to the surface is also approximately 20 ° C. Therefore, drying is further promoted by placing the band under a reduced pressure of 2 kPa or less, which is the vapor pressure or less. Can be made to.

表面処理工程において、鋼帯に表面処理液xを塗布する方法は特に制限はなく、例えば、ロールコーターやバーコーターによる塗布、浸漬、スプレー塗布など任意の方法を適用できるが、表面処理工程で表面処理液xが塗布された鋼帯を、他の部材と接触させることなく乾燥工程が行われる減圧室A内に安定して導くには、後述するようにロールコーターを用いるのが有利であるので、ロールコーターによる塗布が特に好ましい。
鋼帯に塗布される表面処理液xの種類や組成も特に制限はなく、通常用いられているものを用いることができる。表面処理液xの溶媒は、水、有機溶媒、水と有機溶剤の混合溶媒のいずれでもよいが、一般には水を主成分とする溶媒(水のみからなる溶媒を含む。)が用いられる場合(すなわち水系の表面処理液x)が多い。ここで、溶媒の主成分である水に対して有機溶媒を混合する場合、有機溶媒の割合は溶媒全体で10質量%程度を上限とすることが好ましい。水系の表面処理液xとしては、例えば、シランカップリング剤や界面活性剤などを含有する水溶液が挙げられる。
In the surface treatment step, the method of applying the surface treatment liquid x to the steel strip is not particularly limited, and any method such as coating with a roll coater or a bar coater, dipping, or spray coating can be applied. In order to stably guide the steel strip coated with the treatment liquid x into the decompression chamber A in which the drying process is performed without contacting with other members, it is advantageous to use a roll coater as described later. , Coating with a roll coater is particularly preferable.
The type and composition of the surface treatment liquid x applied to the steel strip are not particularly limited, and a commonly used one can be used. The solvent of the surface treatment liquid x may be water, an organic solvent, or a mixed solvent of water and an organic solvent, but in general, a solvent containing water as a main component (including a solvent consisting only of water) is used (including a solvent consisting only of water). That is, there are many aqueous surface treatment liquids x). Here, when the organic solvent is mixed with water which is the main component of the solvent, the ratio of the organic solvent is preferably up to about 10% by mass in the whole solvent. Examples of the aqueous surface treatment liquid x include an aqueous solution containing a silane coupling agent, a surfactant, and the like.

表面処理工程において表面に表面処理液xが塗布された鋼帯を大気圧未満、好ましくは表面処理液xの溶媒の蒸気圧以下(より好ましくは表面処理液の溶媒の蒸気圧未満)に減圧された減圧室Aに導入し、この減圧室Aにおいて、鋼帯表面に付着した表面処理液xの溶媒を揮発させる乾燥工程が行われる。ここで、減圧室A内を表面処理液xの溶媒の蒸気圧以下(より好ましくは表面処理液xの溶媒の蒸気圧未満)に減圧した方が、より乾燥を促進できる。表面処理液xの溶媒の蒸気圧は、例えば、表面処理液xが塗布されて減圧室Aに導入される直前又は導入された直後の鋼板の温度を測定し、通常、この鋼板温度≒表面処理液x温度であることから、この鋼板温度に基づき求めることができる。
なお、減圧室Aが表面処理液xの溶媒の蒸気圧以下に減圧される場合であって、溶媒が蒸気圧が異なる2種以上の液体からなる場合(例えば、溶媒が水と有機溶媒の混合溶媒である場合)には、蒸気圧が低い方の液体の蒸気圧以下に減圧されることが好ましい。
減圧室A内を減圧するために、真空ポンプなどを用いて室内の排気が行われる。
In the surface treatment step, the steel strip coated with the surface treatment liquid x is reduced to less than atmospheric pressure, preferably less than the vapor pressure of the solvent of the surface treatment liquid x (more preferably less than the vapor pressure of the solvent of the surface treatment liquid). A drying step is performed in which the solvent is introduced into the decompression chamber A and the solvent of the surface treatment liquid x adhering to the surface of the steel strip is volatilized. Here, it is better to reduce the pressure in the decompression chamber A to the vapor pressure of the solvent of the surface treatment liquid x or less (more preferably less than the vapor pressure of the solvent of the surface treatment liquid x) to further promote the drying. For the vapor pressure of the solvent of the surface treatment liquid x, for example, the temperature of the steel sheet immediately before or immediately after the surface treatment liquid x is applied and introduced into the decompression chamber A is measured, and usually this steel plate temperature ≈ surface treatment. Since it is the liquid x temperature, it can be obtained based on this steel sheet temperature.
When the decompression chamber A is depressurized below the vapor pressure of the solvent of the surface treatment liquid x, and the solvent is composed of two or more liquids having different vapor pressures (for example, the solvent is a mixture of water and an organic solvent). In the case of a solvent), it is preferable that the vapor pressure is reduced to the vapor pressure of the liquid having the lower vapor pressure or less.
In order to decompress the inside of the decompression chamber A, the inside of the chamber is exhausted by using a vacuum pump or the like.

この減圧室A内での乾燥工程では、表面に表面処理液xが付着した鋼帯は、少なくとも表面処理皮膜成分が搬送ロールに付着しない程度に乾燥され、この状態で減圧室Aを出てライン下流側に送られる。減圧室Aを出た直後の表面処理鋼帯の表面処理皮膜は、製品のレベルまでは乾燥し切れていない場合もあるが、通常の連続ラインでは、減圧室Aの下流側にルーパーなどの長大なラインがあるので、そのライン下流側に搬送される過程でさらに乾燥(自然乾燥)が進み、製品レベルの所望の表面処理皮膜が得られる。したがって、乾燥工程以降において表面処理皮膜の焼付処理(加熱処理)を行う必要はない。
なお、表面処理皮膜の付着量(乾燥後の付着量)は、皮膜の種類によって異なり、一律には規定できないが、例えば、実施例に示したような成分を含有する皮膜の場合には、耐食性の確保の点から0.2〜1.0g/m程度とすることが好ましい。付着量が0.2g/m未満では耐食性が不足する場合があり、一方、1.0g/mを超えると皮膜が部分的に剥離するおそれがある。
In the drying step in the decompression chamber A, the steel strip having the surface treatment liquid x adhered to the surface is dried to the extent that at least the surface treatment film component does not adhere to the transport roll, and in this state, the steel strip leaves the decompression chamber A and is lined up. It is sent to the downstream side. The surface-treated film of the surface-treated steel strip immediately after leaving the decompression chamber A may not be completely dried to the product level, but in a normal continuous line, a looper or the like is long on the downstream side of the decompression chamber A. Since there is a line, drying (natural drying) proceeds further in the process of being transported to the downstream side of the line, and a desired surface treatment film at the product level can be obtained. Therefore, it is not necessary to perform the baking treatment (heat treatment) of the surface treatment film after the drying step.
The amount of adhesion of the surface-treated film (the amount of adhesion after drying) differs depending on the type of film and cannot be uniformly specified. For example, in the case of a film containing a component as shown in Examples, corrosion resistance From the viewpoint of ensuring the above, it is preferably about 0.2 to 1.0 g / m 2 . If the adhesion amount is less than 0.2 g / m 2 , the corrosion resistance may be insufficient, while if it exceeds 1.0 g / m 2 , the film may be partially peeled off.

本発明法は、減圧室Aでの乾燥工程だけで必要とされる表面処理液xの乾燥を行うことができるので、乾燥工程では鋼帯が高温とならず、このため乾燥後の冷却工程が基本的に不要となり、その分、製造コストを低減することができる。
加えて、本発明法では、従来法のように誘導加熱炉で塗膜の乾燥焼付けを行う場合における以下のような問題についても、基本的に回避することができる。すなわち、塗膜の乾燥焼付けに使用されている誘導加熱炉では、通板する鋼帯を取り囲むように誘導加熱コイルが配設されている。この誘導加熱炉で塗膜を乾燥焼付けすると水蒸気が発生するが、誘導加熱コイルはその内部で循環している冷却水によって冷却されているので、誘導加熱炉内で発生した水蒸気が誘導加熱コイルに結露し、凝集した水滴が塗装鋼帯面に滴下付着し、塗装鋼帯の品質を損なうという問題がある。特に厚い塗膜を乾燥焼付けする場合、蒸発水分量が多くなって結露が生じやすくなるため、塗装鋼帯に水滴が落下し、表面品質の低下を招くリスクが増大する。したがって、特許文献1のように熱風加熱炉と誘導加熱炉を併用する乾燥焼付け方法も同様の課題がある。本発明法では、このような表面処理液の乾燥に伴う水蒸気の結露による問題が基本的に生じないので、厚い塗膜を形成する場合でも、優れた表面品質の表面処理金属帯を安定して製造することができる。
In the method of the present invention, the surface treatment liquid x required only in the drying step in the decompression chamber A can be dried, so that the steel strip does not become hot in the drying step, and therefore the cooling step after drying is performed. It is basically unnecessary, and the manufacturing cost can be reduced accordingly.
In addition, in the method of the present invention, the following problems in the case of drying and baking the coating film in the induction heating furnace as in the conventional method can be basically avoided. That is, in the induction heating furnace used for drying and baking the coating film, the induction heating coil is arranged so as to surround the steel strip through which the plate is passed. When the coating film is dried and baked in this induction heating furnace, steam is generated, but since the induction heating coil is cooled by the cooling water circulating inside the induction heating coil, the steam generated in the induction heating furnace becomes the induction heating coil. There is a problem that dew condensation and agglomerated water droplets drip and adhere to the surface of the coated steel strip, impairing the quality of the coated steel strip. In particular, when a thick coating film is dried and baked, the amount of evaporated water increases and dew condensation is likely to occur, which increases the risk of water droplets falling on the coated steel strip and causing deterioration of surface quality. Therefore, the drying and baking method in which the hot air heating furnace and the induction heating furnace are used in combination as in Patent Document 1 also has the same problem. In the method of the present invention, since the problem due to dew condensation of water vapor due to the drying of such a surface treatment liquid basically does not occur, a surface treatment metal band having excellent surface quality can be stably formed even when a thick coating film is formed. Can be manufactured.

図1は、本発明の製造方法と製造設備の一実施形態を模式的に示したものである。
本実施形態では、連続ラインにおいて鋼帯Sに張力を付与するための上流側及び下流側ブライドルロール2a,2b間に、上流側からロールコーター1と減圧室Aが順に設けられている。
減圧室Aは、鋼帯Sが通過する入口4と出口5を有するとともに、真空ポンプ3が接続され、この真空ポンプ3で減圧室A内の空気が排気され、減圧されるようになっている。通常、真空ポンプ3としては、少なくとも高圧用ポンプと低圧用ポンプを併用し、これらを減圧の程度に応じて使い分けることが経済的であり、本実施形態でも、真空ポンプ3として高圧用ポンプ30(例えば、油回転ポンプなど)と低圧用ポンプ31(例えば、メカニカルブースターポンプなど)を設け、適宜使い分けるようにしている。
FIG. 1 schematically shows an embodiment of the manufacturing method and manufacturing equipment of the present invention.
In the present embodiment, the roll coater 1 and the decompression chamber A are sequentially provided from the upstream side between the upstream side and the downstream side bridle rolls 2a and 2b for applying tension to the steel strip S in the continuous line.
The decompression chamber A has an inlet 4 and an outlet 5 through which the steel strip S passes, and a vacuum pump 3 is connected. The vacuum pump 3 exhausts the air in the decompression chamber A to reduce the pressure. .. Normally, it is economical to use at least a high-pressure pump and a low-pressure pump in combination as the vacuum pump 3, and use these properly according to the degree of decompression. Also in this embodiment, the high-pressure pump 30 (as the vacuum pump 3) For example, an oil rotary pump or the like) and a low-pressure pump 31 (for example, a mechanical booster pump or the like) are provided and used properly.

ロールコーター1は、それ自体は従来から使用されているものでよいが、本実施形態では、減圧室Aの入側に近接して設置されており、このロールコーター1が鋼帯Sを減圧室A内で水平に通板させるための案内手段の役目も果すようにしている。すなわち、減圧室Aの入口4の前面において、ロールコーター1を構成する上下1対の塗布ロール12が鋼帯Sを拘束しつつ入口4方向に送り出すことにより、表面処理液xが塗布された鋼帯Sを、他の部材(例えば、減圧室Aの入口4や出口5などの部材)と接触させることなく、減圧室A内で安定して水平に通板させることができるようにしている。このためロールコーター1は、減圧室Aの入側にできるだけ近接して設置されることが好ましく、特にロールコーター1の最下流側位置(塗布ロール12の出側)と減圧室Aの入口4との距離が1m以下となるように設置されることが好ましい。 The roll coater 1 itself may be one that has been used conventionally, but in the present embodiment, the roll coater 1 is installed close to the entrance side of the decompression chamber A, and the roll coater 1 puts the steel strip S in the decompression chamber. It also serves as a guide for passing the board horizontally in A. That is, on the front surface of the inlet 4 of the decompression chamber A, a pair of upper and lower coating rolls 12 constituting the roll coater 1 restrain the steel strip S and send it out in the direction of the inlet 4, so that the steel coated with the surface treatment liquid x. The band S can be stably and horizontally passed through the decompression chamber A without coming into contact with other members (for example, members such as the inlet 4 and the outlet 5 of the decompression chamber A). Therefore, the roll coater 1 is preferably installed as close as possible to the entrance side of the decompression chamber A, and in particular, the most downstream position of the roll coater 1 (outside of the coating roll 12) and the inlet 4 of the decompression chamber A. It is preferable that the distance is 1 m or less.

また、図示しないが、鋼帯Sが振動して他の部材(例えば、減圧室Aの入口4や出口5などの部材)と接触することをより確実に防止するため、減圧室Aの内部、減圧室Aの入側直前(好ましくは減圧室Aの入口4の上流側1m以内)の位置、減圧室Aの出側直後(好ましくは減圧室Aの出口5の下流側1m以内)の位置のうちの少なくとも1箇所に制振装置を設け、この制振装置により鋼帯Sの振動を抑制することが好ましい。この制振装置としては、例えば、抑えロール、非接触式の電磁式制振装置(電磁サポート装置)などが挙げられ、これらの1種以上を用いることができる。
抑えロールとしては、例えば、鋼帯Sを上下ロールで挟んで拘束する公知のロール装置などを用いることができる。また、非接触式の電磁式制振装置としては、鋼帯通板ラインの両側に配置された電磁石から鋼帯Sに磁力(引力又は斥力)を及ぼすことにより鋼帯Sを制振する公知の電磁式制振装置などを用いることができる。
Further, although not shown, in order to more reliably prevent the steel strip S from vibrating and coming into contact with other members (for example, members such as the inlet 4 and the outlet 5 of the decompression chamber A), the inside of the decompression chamber A, Immediately before the entrance side of the decompression chamber A (preferably within 1 m upstream of the inlet 4 of the decompression chamber A) and immediately after the exit side of the decompression chamber A (preferably within 1 m downstream of the outlet 5 of the decompression chamber A). It is preferable to provide a vibration damping device at at least one of them and suppress the vibration of the steel strip S by this vibration damping device. Examples of the vibration damping device include a suppression roll, a non-contact electromagnetic vibration damping device (electromagnetic support device), and one or more of these can be used.
As the holding roll, for example, a known roll device for restraining the steel strip S by sandwiching it between upper and lower rolls can be used. Further, as a non-contact electromagnetic vibration damping device, there is a known known vibration damping device for damping a steel strip S by applying a magnetic force (attractive force or repulsive force) to the steel strip S from electromagnets arranged on both sides of the steel strip passing plate line. An electromagnetic vibration damping device or the like can be used.

また、表面処理液xによっては、所定の温度に加熱しないと皮膜成分と鋼帯が反応しないため十分な皮膜特性が得られない場合があるため、図示しないが、減圧室Aの内部、減圧室Aの入側直前(好ましくは減圧室Aの入口4の上流側1m以内)の位置、減圧室Aの出側直後(好ましくは減圧室Aの出口5の下流側1m以内)の位置のうちの少なくとも1箇所に加熱装置を設け、この加熱装置で鋼帯(表面処理液x)を加熱できるようにしてもよい。加熱装置の種類は特に制限はないが、加熱温度の制御性などの観点から誘導加熱装置が特に好ましい。また、上記のように減圧室A内(室内の入口4に近い位置)や減圧室Aの入側直前に加熱装置を設け、この加熱装置で鋼帯S(表面処理液x)を加熱することにより、表面処理液xの溶媒の蒸気圧を調整することができ、これにより減圧室Aの減圧の程度を軽減することも可能である。
なお、減圧室A内に設置された誘導加熱装置で鋼帯を加熱しても、発生した水蒸気は真空ポンプ3で吸引されて排気されるため、誘導加熱装置に結露を生じるおそれはない。
Further, depending on the surface treatment liquid x, sufficient film characteristics may not be obtained because the film component and the steel strip do not react unless heated to a predetermined temperature. Therefore, although not shown, the inside of the decompression chamber A and the decompression chamber Of the positions immediately before the entrance side of A (preferably within 1 m on the upstream side of the inlet 4 of the decompression chamber A) and immediately after the exit side of the decompression chamber A (preferably within 1 m on the downstream side of the outlet 5 of the decompression chamber A). A heating device may be provided at at least one place so that the steel strip (surface treatment liquid x) can be heated by this heating device. The type of the heating device is not particularly limited, but the induction heating device is particularly preferable from the viewpoint of controllability of the heating temperature. Further, as described above, a heating device is provided in the decompression chamber A (position close to the inlet 4 of the chamber) or immediately before the entrance side of the decompression chamber A, and the steel strip S (surface treatment liquid x) is heated by this heating device. Therefore, the vapor pressure of the solvent of the surface treatment liquid x can be adjusted, and thereby the degree of decompression in the decompression chamber A can be reduced.
Even if the steel strip is heated by the induction heating device installed in the decompression chamber A, the generated water vapor is sucked by the vacuum pump 3 and exhausted, so that there is no possibility of dew condensation on the induction heating device.

減圧室Aの入口4と出口5は、通常、スリット状の開口部で構成される。これらの開口部は、空気の流入をなるべく少なくするために、通板する鋼帯Sとの隙間が小さい方が好ましいが、鋼帯Sとの隙間が小さすぎると鋼帯Sが接触する恐れがある。このため減圧室Aの入口4と出口5には、必要に応じて、空気の流入を抑えるための適当なシール機構を設けることができる。このシール機構には、例えば、ロールシールやエアシール(エアカーテン)などの公知のシール機構を用いることができる。
また、鋼帯Sの板幅に応じて入口4と出口5の幅を変更できるようにするため、減圧室Aの入口4と出口5には、それらの幅方向の一部を塞ぐことができる可動式のマスクを付設することが好ましい。
The inlet 4 and outlet 5 of the decompression chamber A are usually composed of slit-shaped openings. In order to minimize the inflow of air, it is preferable that these openings have a small gap with the steel strip S through which the plate passes, but if the gap with the steel strip S is too small, the steel strip S may come into contact with the steel strip S. is there. Therefore, an appropriate sealing mechanism for suppressing the inflow of air can be provided at the inlet 4 and the outlet 5 of the decompression chamber A, if necessary. For this sealing mechanism, for example, a known sealing mechanism such as a roll seal or an air seal (air curtain) can be used.
Further, in order to make it possible to change the widths of the inlet 4 and the outlet 5 according to the plate width of the steel strip S, the inlet 4 and the outlet 5 of the decompression chamber A can be partially closed in the width direction. It is preferable to attach a movable mask.

図1の実施形態では、減圧室A内が真空ポンプ3により大気圧未満、好ましくは表面処理液xの溶媒の蒸気圧以下(より好ましくは表面処理液xの溶媒の蒸気圧未満)に減圧される。
ロールコーター1により鋼帯Sの表面に表面処理液xが塗布され(表面処理工程)、この表面処理液xが塗布された鋼帯Sは直ちに減圧室Aに導入され、減圧室Aを通過する過程で表面処理液xの乾燥がなされる(乾燥工程)。
In the embodiment of FIG. 1, the inside of the decompression chamber A is depressurized by the vacuum pump 3 to less than the atmospheric pressure, preferably less than the vapor pressure of the solvent of the surface treatment liquid x (more preferably less than the vapor pressure of the solvent of the surface treatment liquid x). To.
The surface treatment liquid x is applied to the surface of the steel strip S by the roll coater 1 (surface treatment step), and the steel strip S coated with the surface treatment liquid x is immediately introduced into the decompression chamber A and passes through the decompression chamber A. The surface treatment liquid x is dried in the process (drying step).

減圧室A内を表面処理液xの溶媒の蒸気圧以下に減圧する場合、例えば、減圧室Aの入側で鋼帯S(表面処理液x)の温度を放射温度計などで測定し、この測定温度に基づいて表面処理液xの溶媒の蒸気圧を求め、減圧室A内の圧力を制御するようにしてもよい。また、減圧室A内や減圧室Aの入側直前で加熱装置により鋼帯S(表面処理液x)を加熱する場合には、この加熱後の鋼帯S(表面処理液x)の温度を放射温度計などで測定し、この測定温度に基づいて表面処理液xの溶媒の蒸気圧を求め、減圧室A内の圧力を制御するようにしてもよい。
本実施形態では、鋼帯Sが減圧室Aの入口4や出口5などで部材と接触しないようにするため、ロールコーター1を減圧室Aの入側に近接して設置しているが、さらに必要に応じて、ブライドルロール2a,2b間の鋼帯張力を増加させたり、上述したような制振装置を設置して鋼帯Sの振動を抑制してもよい。
When the inside of the decompression chamber A is depressurized below the vapor pressure of the solvent of the surface treatment liquid x, for example, the temperature of the steel strip S (surface treatment liquid x) is measured on the entrance side of the decompression chamber A with a radiation thermometer or the like. The vapor pressure of the solvent of the surface treatment liquid x may be obtained based on the measurement temperature, and the pressure in the decompression chamber A may be controlled. Further, when the steel strip S (surface treatment liquid x) is heated by the heating device in the decompression chamber A or immediately before the entry side of the decompression chamber A, the temperature of the steel strip S (surface treatment liquid x) after heating is changed. It is also possible to measure with a radiation thermometer or the like, obtain the vapor pressure of the solvent of the surface treatment liquid x based on the measured temperature, and control the pressure in the decompression chamber A.
In the present embodiment, the roll coater 1 is installed close to the entrance side of the decompression chamber A in order to prevent the steel strip S from coming into contact with the members at the inlet 4 and the outlet 5 of the decompression chamber A. If necessary, the tension of the steel strip between the bridle rolls 2a and 2b may be increased, or the vibration damping device as described above may be installed to suppress the vibration of the steel strip S.

また、図1の実施形態のように単体の減圧室のみで減圧を行うと、減圧室Aの入口4と出口5の隙間から空気を吸引するため、圧力を必要なレベルまで低下させるために排気能力が高い高価な真空ポンプが必要になる。そこで、主たる減圧室の前後に予備室を設けることで、主たる減圧室と外部との気圧差を小さくし、主たる減圧室への外部からの空気吸引が抑制されるようにすることが好ましい。
図2は、そのような形態の本発明の製造方法と製造設備の一実施形態を模式的に示している。
Further, when decompression is performed only in the single decompression chamber as in the embodiment of FIG. 1, air is sucked from the gap between the inlet 4 and the outlet 5 of the decompression chamber A, so that the pressure is exhausted in order to reduce the pressure to a required level. An expensive vacuum pump with high capacity is required. Therefore, it is preferable to provide spare chambers before and after the main decompression chamber to reduce the pressure difference between the main decompression chamber and the outside so that air suction from the outside to the main decompression chamber is suppressed.
FIG. 2 schematically shows an embodiment of the manufacturing method and manufacturing equipment of the present invention in such a form.

図2の実施形態は、連続ラインにおいて鋼帯Sに張力を付与するための上流側及び下流側ブライドルロール2a,2b間に、上流側からロールコーター1と減圧室Aが順に設けられている点は図1と同様であるが、減圧室Aを、主減圧室aとその入側及び出側にそれぞれ付設された予備減圧室b1,b2で構成し、鋼帯Sを、大気圧未満に減圧された両予備減圧室b1,b2を通じて主減圧室aを通過させるようにしている。ここで、主減圧室aでは、図1の実施形態の減圧室Aと同様に、表面処理液xの乾燥が行われ、予備減圧室b1,b2は、主減圧室aと外部との気圧差を小さくし、主減圧室aへの外部からの空気吸引を抑制する役目をする。 In the embodiment of FIG. 2, the roll coater 1 and the decompression chamber A are sequentially provided from the upstream side between the upstream side and downstream side bridle rolls 2a and 2b for applying tension to the steel strip S in the continuous line. Is the same as in FIG. 1, but the decompression chamber A is composed of the main decompression chamber a and the preliminary decompression chambers b 1 and b 2 provided on the entry side and the exit side thereof, respectively, and the steel strip S is less than the atmospheric pressure. The main decompression chamber a is passed through both pre-decompression chambers b 1 and b 2 which have been decompressed. Here, in the main decompression chamber a, the surface treatment liquid x is dried as in the decompression chamber A of the embodiment of FIG. 1, and the preliminary decompression chambers b 1 and b 2 are the main decompression chamber a and the outside. It reduces the pressure difference and suppresses the suction of air from the outside to the main decompression chamber a.

主減圧室aと予備減圧室b1,b2には、それぞれ真空ポンプ3a,3b1,3b2が接続され、これら真空ポンプ3a,3b1,3b2で主減圧室aと予備減圧室b1,b2内の空気が排気され、減圧されるようになっている。本実施形態でも、真空ポンプ3として高圧用ポンプ30(例えば、油回転ポンプなど)と低圧用ポンプ31(例えば、メカニカルブースターポンプなど)を設け、適宜使い分けるようにしている。
なお、予備減圧室による効果をさらに高めるために、予備減圧室b1と予備減圧室b2を、それぞれライン方向で隣接する複数の予備減圧室で構成し、各予備減圧室を真空ポンプで減圧するようにしてもよい。
Vacuum pumps 3a, 3b 1 , and 3b 2 are connected to the main decompression chamber a and the preliminary decompression chambers b 1 and b 2 , respectively, and these vacuum pumps 3a, 3b 1 , and 3b 2 connect the main decompression chamber a and the preliminary decompression chamber b. The air in 1 and b 2 is exhausted and decompressed. Also in this embodiment, a high pressure pump 30 (for example, an oil rotary pump) and a low pressure pump 31 (for example, a mechanical booster pump) are provided as the vacuum pump 3, and they are used properly.
In order to further enhance the effect of the preliminary decompression chamber, the preliminary decompression chamber b 1 and the preliminary decompression chamber b 2 are composed of a plurality of preliminary decompression chambers adjacent to each other in the line direction, and each preliminary decompression chamber is decompressed by a vacuum pump. You may try to do so.

予備減圧室b1の入口6、予備減圧室b2の出口7、予備減圧室b1と主減圧室a間の出入口8、主減圧室aと予備減圧室b2間の出入口9は、通常、スリット状の開口部で構成される。これらの開口部は、空気の流入をなるべく少なくするために、通板する鋼帯Sとの隙間が小さい方が好ましいが、鋼帯Sとの隙間が小さすぎると鋼帯Sが接触する恐れがある。このため予備減圧室b1の入口6、予備減圧室b2の出口7、予備減圧室b1と主減圧室a間の出入口8、主減圧室aと予備減圧室b2間の出入口9には、必要に応じて、空気の流入を抑えるための適当なシール機構を設けることができる。このシール機構としては、ロールシール(例えば図3参照)やエアシール(エアカーテン)などの公知のシール機構を適用できる。 Inlet 6 of the preliminary vacuum chamber b 1, the outlet 7 of the preliminary vacuum chamber b 2, the preliminary vacuum chamber b 1 and doorway 8 between the main vacuum chamber a, the main vacuum chamber a and the preliminary vacuum chamber b 2 between inlet and outlet 9 of generally , Consists of a slit-shaped opening. In order to minimize the inflow of air, it is preferable that these openings have a small gap with the steel strip S through which the plate passes, but if the gap with the steel strip S is too small, the steel strip S may come into contact with the steel strip S. is there. Thus the inlet 6 of the preliminary vacuum chamber b 1, the outlet 7 of the preliminary vacuum chamber b 2, the preliminary vacuum chamber b 1 and doorway 8 between the main vacuum chamber a, the entrance 9 between the main vacuum chamber a and the preliminary vacuum chamber b 2 Can be provided with an appropriate sealing mechanism for suppressing the inflow of air, if necessary. As this sealing mechanism, a known sealing mechanism such as a roll seal (see, for example, FIG. 3) or an air seal (air curtain) can be applied.

図1の実施形態と同様、本実施形態でも、ロールコーター1は、減圧室A(予備減圧室b1)の入側に近接して設置されており、このロールコーター1が鋼帯Sを減圧室A内で水平に通板させるための案内手段の役目も果すようにしている。これにより表面処理液xが塗布された鋼帯Sを、他の部材(例えば、予備減圧室b1の入口6、予備減圧室b2の出口7、予備減圧室b1と主減圧室a間の出入口8、主減圧室aと予備減圧室b2間の出入口9などの部材)と接触させることなく、減圧室A内で安定して水平に通板させることができるようにしている。この実施形態でも、ロールコーター1は、減圧室A(予備減圧室b1)の入側にできるだけ近接して設置されることが好ましく、特にロールコーター1の最下流側位置(塗布ロール12の出側)と予備減圧室b1の入口6との距離が1m以下となるように設置されることが好ましい。 Similar to the embodiment of FIG. 1, in this embodiment as well, the roll coater 1 is installed close to the entrance side of the decompression chamber A (preliminary decompression chamber b 1 ), and the roll coater 1 decompresses the steel strip S. It also serves as a guide for allowing the board to pass horizontally in room A. Thus the steel strip S surface treatment solution x is applied, the other member (e.g., the inlet 6 of the preliminary vacuum chamber b 1, the outlet 7 of the preliminary vacuum chamber b 2, the preliminary vacuum chamber b 1 and between the main vacuum chamber a The plate can be passed through the decompression chamber A in a stable and horizontal manner without contacting the doorway 8 and the doorway 9 between the main decompression chamber a and the preliminary decompression chamber b 2 ). Also in this embodiment, the roll coater 1 is preferably installed as close as possible to the entry side of the decompression chamber A (preliminary decompression chamber b 1 ), and in particular, the most downstream position of the roll coater 1 (the exit of the coating roll 12). It is preferable that the distance between the side) and the inlet 6 of the preliminary decompression chamber b 1 is 1 m or less.

また、図1の実施形態と同様に、図2の実施形態のような減圧室の構造でも、減圧室A(主減圧室a、予備減圧室b1、予備減圧室b2のうちの少なくとも1つ)の内部、減圧室Aの入側直前(好ましくは予備減圧室b1の入口6の上流側1m以内)の位置、減圧室Aの出側直後(好ましくは予備減圧室b2の出口7の下流側1m以内)の位置のうちの少なくとも1箇所に制振装置や加熱装置を設けることができ、それらを設ける意義や制振装置の詳細などは、図1の実施形態で述べた通りであるが、本実施形態では、主減圧室aの入側に付設された予備減圧室b1内に誘導加熱装置などの加熱装置10を設け、この加熱装置10により鋼帯Sを加熱できるようにするとともに、主減圧室aの出側に付設された予備減圧室b2内に制振装置である抑えロール11を設け、この抑えロール11により鋼帯Sの振動を抑制するようにしている。なお、制振装置には、非接触式の電磁式制振装置などを用いてもよい。 Further, similarly to the embodiment of FIG. 1, in the structure of the decompression chamber as in the embodiment of FIG. 2, at least one of the decompression chamber A (main decompression chamber a, preliminary decompression chamber b 1 , and preliminary decompression chamber b 2) is used. Inside, just before the entrance side of the decompression chamber A (preferably within 1 m upstream of the inlet 6 of the preliminary decompression chamber b 1 ), immediately after the exit side of the decompression chamber A (preferably the outlet 7 of the preliminary decompression chamber b 2 ). A vibration damping device and a heating device can be provided at least one of the positions (within 1 m on the downstream side of the), and the significance of providing them and the details of the vibration damping device are as described in the embodiment of FIG. However, in the present embodiment, a heating device 10 such as an induction heating device is provided in the preliminary decompression chamber b 1 provided on the entrance side of the main decompression chamber a so that the steel strip S can be heated by the heating device 10. At the same time, a restraining roll 11 which is a vibration damping device is provided in the preliminary decompression chamber b 2 provided on the exit side of the main decompression chamber a, and the restraining roll 11 suppresses the vibration of the steel strip S. As the vibration damping device, a non-contact electromagnetic vibration damping device or the like may be used.

図2の実施形態では、減圧室Aの主減圧室a内が真空ポンプ3aにより大気圧未満、好ましくは表面処理液xの溶媒の蒸気圧以下(より好ましくは表面処理液xの溶媒の蒸気圧未満)に減圧されるとともに、予備減圧室b1,b2内も真空ポンプ3b1,3b2により大気圧未満に減圧される。ここで、主減圧室aと予備減圧室b1,b2の減圧状態としては、予備減圧室b1,b2の圧力が主減圧室aの圧力よりも高くなるようにすることが好ましい。
ロールコーター1により鋼帯Sの表面に表面処理液xが塗布され(表面処理工程)、この表面処理液xが塗布された鋼帯Sは直ちに減圧室Aに導入され、減圧室A(主減圧室a)を通過する過程で表面処理液xの乾燥がなされる(乾燥工程)。その際、予備減圧室b1,b2が外部との気圧差を緩衝する領域となるため、主減圧室aへの外部からの空気吸引が抑えられ、このため排気能力が高い高価な真空ポンプを用いなくても主減圧室aの減圧を比較的容易に行うことができる。
In the embodiment of FIG. 2, the inside of the main decompression chamber a of the decompression chamber A is less than the atmospheric pressure by the vacuum pump 3a, preferably equal to or less than the vapor pressure of the solvent of the surface treatment liquid x (more preferably, the vapor pressure of the solvent of the surface treatment liquid x). The pressure is reduced to less than atmospheric pressure, and the pressure inside the preliminary decompression chambers b 1 and b 2 is also reduced to less than atmospheric pressure by the vacuum pumps 3 b 1 and 3 b 2 . Here, as the decompression state of the main decompression chambers a and the preliminary decompression chambers b 1 and b 2 , it is preferable that the pressures of the preliminary decompression chambers b 1 and b 2 are higher than the pressure of the main decompression chambers a.
The surface treatment liquid x is applied to the surface of the steel strip S by the roll coater 1 (surface treatment step), and the steel strip S coated with the surface treatment liquid x is immediately introduced into the decompression chamber A to reduce the pressure chamber A (main decompression chamber A). The surface treatment liquid x is dried in the process of passing through the chamber a) (drying step). At that time, since the preliminary decompression chambers b 1 and b 2 are regions that buffer the pressure difference with the outside, air suction from the outside to the main decompression chamber a is suppressed, and therefore an expensive vacuum pump with high exhaust capacity. The decompression of the main decompression chamber a can be performed relatively easily without using the above.

本実施形態では、鋼帯Sが予備減圧室b1の入口6、予備減圧室b2の出口7、予備減圧室b1と主減圧室a間の出入口8、主減圧室aと予備減圧室b2間の出入口9などで部材と接触しないようにするため、ロールコーター1を減圧室Aの入側に近接して設置するとともに、予備減圧室b2内に制振装置(抑えロール11)を設けており、これにより鋼帯Sが減圧室A内の部材と接触することが適切に防止されるが、さらに必要に応じて、ブライドルロール2a,2b間の鋼帯張力を増加させるなどの対応を採ってもよい。 In the present embodiment, the inlet 6 of the steel strip S is pre-decompression chamber b 1, the outlet 7 of the preliminary vacuum chamber b 2, the preliminary vacuum chamber b 1 and doorway 8 between the main vacuum chamber a, the main vacuum chamber a and the preliminary vacuum chamber A roll coater 1 is installed close to the entrance side of the decompression chamber A and a vibration damping device (suppressing roll 11) is installed in the preliminary decompression chamber b 2 so as not to come into contact with members at the entrance 9 between b 2 and the like. Is provided so that the steel strip S can be appropriately prevented from coming into contact with the members in the decompression chamber A, but if necessary, the steel strip tension between the bridle rolls 2a and 2b can be increased. You may take action.

また、予備減圧室b1内に設けられた加熱装置10で鋼帯S(表面処理液x)を加熱することにより、所定の皮膜特性を得るために加熱が必要な表面処理液xの場合にも適切に対応することができる。さらに、加熱装置10で鋼帯S(表面処理液x)を加熱することにより、表面処理液xの溶媒の温度をコントロールすることでその蒸気圧を調整することができ、これにより減圧室Aの減圧の程度を軽減することも可能である。
主減圧室a内を表面処理液xの溶媒の蒸気圧以下に減圧する場合、例えば、予備減圧室b1内で鋼帯S(表面処理液x)の温度を放射温度計などで測定し、この測定温度と蒸気圧曲線に基づいて表面処理液xの溶媒の蒸気圧を求め、減圧室A内の圧力を制御するようにしてもよい。また、予備減圧室b1内の加熱装置10により鋼帯Sを加熱する場合には、この加熱後の鋼帯S(表面処理液x)の温度を放射温度計などで測定し、この測定温度と蒸気圧曲線に基づいて表面処理液xの溶媒の蒸気圧を求め、減圧室A内の圧力を制御するようにしてもよい。
Further, in the case of the surface treatment liquid x that needs to be heated in order to obtain a predetermined film characteristic by heating the steel strip S (surface treatment liquid x) with the heating device 10 provided in the preliminary decompression chamber b 1 . Can also be dealt with appropriately. Further, by heating the steel strip S (surface treatment liquid x) with the heating device 10, the vapor pressure thereof can be adjusted by controlling the temperature of the solvent of the surface treatment liquid x, whereby the pressure reducing chamber A can be adjusted. It is also possible to reduce the degree of decompression.
When the inside of the main decompression chamber a is depressurized below the vapor pressure of the solvent of the surface treatment liquid x, for example, the temperature of the steel strip S (surface treatment liquid x) is measured in the preliminary decompression chamber b 1 with a radiation thermometer or the like. The vapor pressure of the solvent of the surface treatment liquid x may be obtained based on the measured temperature and the vapor pressure curve, and the pressure in the decompression chamber A may be controlled. When the steel strip S is heated by the heating device 10 in the preliminary decompression chamber b 1 , the temperature of the steel strip S (surface treatment liquid x) after heating is measured with a radiation thermometer or the like, and the measured temperature is measured. And the vapor pressure of the solvent of the surface treatment liquid x may be obtained based on the vapor pressure curve, and the pressure in the decompression chamber A may be controlled.

本発明では、減圧室Aの出口などにおいて、鋼帯制振用の抑えロールを利用してロールシール機構を構成することができる。図3は、そのロールシール機構の一例を示しており、減圧室Aの出口に抑えロール11(制振装置)を組み込み、この抑えロール11でロールシール機構13を構成したものである。出口を構成する減圧室A側の部材は、抑えロール11との隙間をできるだけ小さくし、場合によっては適当な摺動部材を介して抑えロール11と接触させてもよい。このような抑えロール11を利用したロールシール機構は、例えば、図1の出口5、図2の出口7、出入口9などに適用できる。 In the present invention, at the outlet of the decompression chamber A or the like, a roll seal mechanism can be configured by using a holding roll for damping a steel strip. FIG. 3 shows an example of the roll sealing mechanism, in which a holding roll 11 (vibration damping device) is incorporated at the outlet of the decompression chamber A, and the holding roll 11 constitutes the roll sealing mechanism 13. The member on the decompression chamber A side constituting the outlet may have a small gap with the holding roll 11 as much as possible, and may be brought into contact with the holding roll 11 via an appropriate sliding member in some cases. Such a roll sealing mechanism using the holding roll 11 can be applied to, for example, the outlet 5 of FIG. 1, the outlet 7 of FIG. 2, the entrance / exit 9, and the like.

さきに述べたように本発明法は、減圧室Aでの乾燥工程だけで必要とされる表面処理液xの乾燥を行うことができるので、乾燥工程では鋼帯が高温とならず、このため乾燥後の冷却工程が基本的に不要となる。ただし、場合によっては、熱風加熱や誘導加熱などのような公知の乾燥方法と組み合わせて用いることもでき、例えば、熱風加熱(前段)+本発明法(後段)、本発明法(前段)+誘導加熱(後段)などの実施形態を採ることもできる。また、皮膜の種類によっては、成膜反応や硬化反応を促進するために、必要に応じて紫外線照射工程を設け、本発明法と組み合わせて実施してもよい。 As described above, in the method of the present invention, the surface treatment liquid x required only in the drying step in the decompression chamber A can be dried, so that the steel strip does not become hot in the drying step. The cooling process after drying is basically unnecessary. However, in some cases, it can be used in combination with a known drying method such as hot air heating or induction heating. For example, hot air heating (first stage) + the method of the present invention (second stage), the method of the present invention (first stage) + induction It is also possible to adopt an embodiment such as heating (second stage). Further, depending on the type of film, in order to promote the film forming reaction and the curing reaction, an ultraviolet irradiation step may be provided as necessary and carried out in combination with the method of the present invention.

減圧室で表面処理液の乾燥を行う場合、減圧室内を真空に近い状態(例えば100Pa程度)まで減圧するには減圧室と外部との隙間をなくすことが重要であるが、本発明法は連続ラインで行われるため、金属帯が減圧室Aを通過するための隙間が必ず生じる。このような隙間がある減圧室A内を真空に近い状態まで減圧するには、大規模な設備と真空ポンプによる大量の気体の排出が必要となり、莫大な費用を要する。
一般的な表面処理液xは溶媒の主成分が水であり、水の蒸気圧は0℃で605Pa、100℃で101kPaである。本発明法では、減圧室Aは水の蒸気圧以下まで減圧することができれば十分であるため、表面処理液xの溶媒の主成分が水の場合、減圧室Aは605Pa以上101kPa以下に減圧されていればよく、それよりも低い圧力(例えば100Pa程度)まで減圧しないことが、真空設備(真空ポンプを含む減圧用設備)の設備コストの観点から好ましい。また、減圧室Aで必要とされる減圧の程度は水の蒸気圧で決まり、水の蒸気圧は加熱装置で金属帯温度を調整することにより制御できることから、真空設備と加熱装置の両方の費用のバランスを取りながら乾燥設備を設計することにより、設備コストを抑えることも可能である。
When the surface treatment liquid is dried in the decompression chamber, it is important to eliminate the gap between the decompression chamber and the outside in order to reduce the pressure in the decompression chamber to a state close to vacuum (for example, about 100 Pa), but the method of the present invention is continuous. Since it is performed on the line, there is always a gap for the metal band to pass through the decompression chamber A. In order to depressurize the inside of the decompression chamber A having such a gap to a state close to vacuum, it is necessary to discharge a large amount of gas by a large-scale facility and a vacuum pump, which requires a huge cost.
The main component of the solvent of the general surface treatment liquid x is water, and the vapor pressure of water is 605 Pa at 0 ° C. and 101 kPa at 100 ° C. In the method of the present invention, it is sufficient that the decompression chamber A can be depressurized to the vapor pressure or less of water. Therefore, when the main component of the solvent of the surface treatment liquid x is water, the decompression chamber A is depressurized to 605 Pa or more and 101 kPa or less. From the viewpoint of equipment cost of vacuum equipment (decompression equipment including a vacuum pump), it is preferable not to reduce the pressure to a pressure lower than that (for example, about 100 Pa). In addition, the degree of decompression required in the decompression chamber A is determined by the vapor pressure of water, and the vapor pressure of water can be controlled by adjusting the metal band temperature with a heating device, so the cost of both the vacuum equipment and the heating device It is also possible to reduce the equipment cost by designing the drying equipment while balancing the above.

溶融亜鉛めっき鋼板(GI)を被処理金属帯(以下「鋼帯」という)とし、これにクロメートフリー表面処理を施して表面処理鋼帯を製造した。
発明例では、図2に示すような設備において、鋼帯の表面にロールコーター1で表面処理液を塗布した後、減圧室Aで表面処理液を乾燥させた。比較例1、2では、従来法にしたがい鋼帯の表面にロールコーターで表面処理液を塗布した後、誘導加熱炉で表面処理液を乾燥させた。また、比較例3では、図2に示すような設備において減圧室A内の圧力を敢えて大気圧よりも高くし、表面処理液が塗布された鋼帯を通過させた。
A hot-dip galvanized steel sheet (GI) was used as a metal strip to be treated (hereinafter referred to as "steel strip"), and a chromate-free surface treatment was applied to the metal strip to produce a surface-treated steel strip.
In the example of the invention, in the equipment as shown in FIG. 2, the surface treatment liquid was applied to the surface of the steel strip with the roll coater 1, and then the surface treatment liquid was dried in the decompression chamber A. In Comparative Examples 1 and 2, the surface treatment liquid was applied to the surface of the steel strip according to the conventional method with a roll coater, and then the surface treatment liquid was dried in an induction heating furnace. Further, in Comparative Example 3, in the equipment as shown in FIG. 2, the pressure in the decompression chamber A was intentionally made higher than the atmospheric pressure, and the steel strip coated with the surface treatment liquid was passed.

表面処理液は、3−グリシドキシプロピルトリメトキシシラン、有機ケイ素化合物、Zrフルオロ化合物、リン酸、オキシ硫酸バナジウム、ポリエチレンオキサイドを含む薬液を所定の固形分濃度になるように純水で希釈したものを用いた。この表面処理液は、粘度10mPas、表面張力40mN/m、比重1であった。
本実施例では、以下のようにして、乾燥工程完了直後の表面処理皮膜の乾燥状態と鋼帯温度を調べるとともに、製造された表面処理鋼帯の耐食性、耐黒変性、外観の評価を行った。なお、乾燥後の皮膜付着量は、表面処理鋼帯から切り出した試験片を試料として重量法で校正した蛍光X線分析により測定した。それらの結果を、製造条件ととともに表1に示す。
The surface treatment solution was a chemical solution containing 3-glycidoxypropyltrimethoxysilane, an organosilicon compound, a Zrfluoro compound, phosphoric acid, vanadium oxysulfate, and polyethylene oxide diluted with pure water to a predetermined solid content concentration. I used the one. This surface treatment liquid had a viscosity of 10 mPas, a surface tension of 40 mN / m, and a specific gravity of 1.
In this example, the dry state and steel strip temperature of the surface-treated film immediately after the completion of the drying process were investigated, and the corrosion resistance, blackening resistance, and appearance of the manufactured surface-treated steel strip were evaluated as follows. .. The amount of film adhered after drying was measured by fluorescent X-ray analysis calibrated by a gravimetric method using a test piece cut out from a surface-treated steel strip as a sample. The results are shown in Table 1 together with the manufacturing conditions.

(1)乾燥工程完了直後の塗膜の乾燥状態の評価
検査台において乾燥工程完了直後の表面処理鋼帯(1コイル分)の表面状態を目視で観察することで塗膜の乾燥状態を評価した。すなわち、表面処理液が十分に乾燥する前に表面処理鋼帯が予備減圧室b2内の抑えロール11(比較例1,2を実施した設備では誘導加熱炉の出側に設けた抑えロール)に接触した結果、皮膜に「かすれ」が生じたか否かを目視で判定した。乾燥の良否は表面処理鋼帯の搬送速度の影響もあることから、表面処理鋼帯の搬送速度により判定基準を下記のように細分化した。
◎:搬送速度150mpm以上であっても「かすれ」が生じなかったもの
○:搬送速度125mpm以上であっても150mpm未満であれば「かすれ」が生じなかったもの
●:搬送速度100mpm以上であっても125mpm未満であれば「かすれ」が生じなかったもの
△:搬送速度75mpm以上であっても100mpm未満であれば「かすれ」が生じなかったもの
▲:搬送速度50mpm以上であっても75mpm未満であれば「かすれ」が生じなかったもの
×:搬送速度50mpm未満であっても「かすれ」が生じたもの
(1) Evaluation of the dry state of the coating film immediately after the completion of the drying process The dry state of the coating film was evaluated by visually observing the surface condition of the surface-treated steel strip (for one coil) immediately after the completion of the drying process on the inspection table. .. That is, before the surface treatment liquid is sufficiently dried, the surface treatment steel strip is formed in the holding roll 11 in the preliminary decompression chamber b 2 (in the equipment in which Comparative Examples 1 and 2 were carried out, the holding roll provided on the outlet side of the induction heating furnace). As a result of contact with the film, it was visually determined whether or not "blurring" occurred in the film. Since the quality of drying is also affected by the transport speed of the surface-treated steel strip, the judgment criteria were subdivided as follows according to the transport speed of the surface-treated steel strip.
⊚: No “blurring” occurred even when the transport speed was 150 mpm or more ○: No “blurring” occurred when the transport speed was 125 mpm or more but less than 150 mmp ●: The transport speed was 100 mpm or more If it is less than 125 mpm, "blurring" does not occur. Δ: Even if the transport speed is 75 mmp or more, "blurring" does not occur if it is less than 100 mmp. ▲: Even if the transport speed is 50 mmp or more, it is less than 75 mmp. If there is, "blurring" did not occur ×: “blurring” occurred even if the transport speed was less than 50 mpm

(2)乾燥工程完了直後の鋼帯温度の評価
検査台において乾燥工程完了直後の表面処理鋼帯(1コイル分)の温度を放射温度計で測定した。なお、乾燥工程完了直後の表面処理鋼帯から試験片を切り出して熱電対で温度を測定し、この測定値との比較により放射率の校正を実施した。測定された乾燥工程完了直後の鋼帯温度が60℃未満を合格(○)、60℃以上を不合格(×)とした。
(3)外観の評価
表面処理鋼帯(1コイル分)の外観については、皮膜欠陥(上述した皮膜の「かすれ」や他の皮膜欠陥)の有無を目視で確認し、いずれの鋼帯搬送速度であっても皮膜欠陥が確認された場合を不合格(×)、少なくとも一部範囲の鋼帯搬送速度では皮膜欠陥が確認されなかった場合を合格(○)とした。
また、表面処理鋼帯が乾燥設備を通過する間に同設備の構成部材(抑えロール11を除く)に接触して皮膜に「こすれ」が生じていないかどうかも調べた。
(2) Evaluation of steel strip temperature immediately after the completion of the drying process The temperature of the surface-treated steel strip (for one coil) immediately after the completion of the drying process was measured with a radiation thermometer on the inspection table. A test piece was cut out from the surface-treated steel strip immediately after the completion of the drying process, the temperature was measured with a thermocouple, and the emissivity was calibrated by comparison with the measured value. A steel strip temperature of less than 60 ° C. immediately after the measured drying process was completed was regarded as acceptable (◯), and a steel strip temperature of 60 ° C. or higher was regarded as rejected (x).
(3) Appearance evaluation Regarding the appearance of the surface-treated steel strip (for one coil), visually check for the presence or absence of film defects (the above-mentioned "smearing" of the film and other film defects), and which steel strip transfer speed is used. Even so, the case where the film defect was confirmed was regarded as a failure (x), and the case where the film defect was not confirmed at least in a part of the steel strip transport speed was regarded as a pass (◯).
It was also examined whether or not the film was "rubbed" by contacting the constituent members (excluding the holding roll 11) of the surface-treated steel strip while passing through the drying equipment.

(4)耐食性の評価
表面処理鋼帯から切り出した試験片に対してJIS Z2371に準拠した塩水噴霧試験を24時間実施し、錆発生面積率を測定した。錆発生面積率が10%未満の場合を合格(○)とし、10%以上の場合を不合格(×)とした。
(5)耐黒変性の評価
表面処理鋼帯から切り出した試験片(サイズ50×150mm)を80℃、98%RHの恒温槽に24時間保持し、この保持前後の試験片の色調を分光色彩計で測定し、Lab表色系のL値の差(ΔL)で評価した。その判定基準は以下のとおりである。
○:ΔL≧−3
△:−3>ΔL≧−5
×:ΔL<−5
なお、乾燥工程前の鋼帯温度は、予備減圧室b1内の加熱装置10(誘導加熱装置)の下流側に設置した放射温度計を用いて測定した。
(4) Evaluation of corrosion resistance A salt spray test conforming to JIS Z2371 was carried out for 24 hours on the test piece cut out from the surface-treated steel strip, and the rust generation area ratio was measured. When the rust area ratio was less than 10%, it was evaluated as acceptable (◯), and when it was 10% or more, it was evaluated as rejected (x).
(5) Evaluation of blackening resistance A test piece (size 50 x 150 mm) cut out from a surface-treated steel strip was held in a constant temperature bath at 80 ° C. and 98% RH for 24 hours, and the color tone of the test piece before and after this holding was spectrally colored. It was measured with a meter and evaluated by the difference (ΔL) in the L value of the Lab color system. The judgment criteria are as follows.
◯: ΔL ≧ -3
Δ: -3> ΔL ≧ -5
X: ΔL <-5
The temperature of the steel strip before the drying step was measured using a radiation thermometer installed on the downstream side of the heating device 10 (induction heating device) in the preliminary decompression chamber b 1 .

Figure 2020139232
Figure 2020139232

表1において、発明例1〜4,10は、減圧室A(主減圧室a)の圧力を大気圧未満であって、かつ表面処理液の溶媒の蒸気圧よりも高い圧力に設定した。なお、発明例10では、ロールコーター1の入側位置において冷却液で鋼帯を0℃に冷却し、ロールコーター1で塗布された表面処理液が0℃となるようにした。発明例5は、減圧室A(主減圧室a)の圧力を表面処理液の溶媒の蒸気圧以下の圧力に設定した。発明例1〜5,10では、予備減圧室b1内に設置した加熱装置10(誘導加熱装置)は使用しなかった。また、発明例6〜8では、予備減圧室b1内に設置した加熱装置10を使用して鋼帯を加熱することで表面処理液の溶媒の蒸気圧を高め、減圧室の圧力をその蒸気圧以下となるように設定した。このため加熱装置10で加熱された直後の鋼帯の温度の測定結果を基に表面処理液の溶媒の蒸気圧を求め、この蒸気圧以下になるように減圧室の圧力を制御した。また、発明例9では、発明例5と同等の乾燥条件としたが、制振装置である抑えロール11を使用しなかった。 In Table 1, in Invention Examples 1 to 4 and 10, the pressure in the decompression chamber A (main decompression chamber a) was set to a pressure lower than the atmospheric pressure and higher than the vapor pressure of the solvent of the surface treatment liquid. In Invention Example 10, the steel strip was cooled to 0 ° C. with a coolant at the entry side position of the roll coater 1 so that the surface treatment liquid applied by the roll coater 1 became 0 ° C. In Invention Example 5, the pressure in the decompression chamber A (main decompression chamber a) was set to a pressure equal to or lower than the vapor pressure of the solvent of the surface treatment liquid. In Invention Examples 1 to 5 and 10, the heating device 10 (induction heating device) installed in the preliminary decompression chamber b 1 was not used. Further, in Invention Examples 6 to 8, the vapor pressure of the solvent of the surface treatment liquid is increased by heating the steel strip using the heating device 10 installed in the preliminary decompression chamber b 1 , and the pressure of the decompression chamber is changed to the vapor. It was set to be below the pressure. Therefore, the vapor pressure of the solvent of the surface treatment liquid was determined based on the measurement result of the temperature of the steel strip immediately after being heated by the heating device 10, and the pressure in the decompression chamber was controlled so as to be equal to or lower than this vapor pressure. Further, in Invention Example 9, the drying conditions were the same as those in Invention Example 5, but the suppression roll 11, which is a vibration damping device, was not used.

比較例1、2では、製造された表面処理鋼帯は耐食性、外観等の特性を満足したが、検査台において温度が60℃以上あり、安全上、オペレータによる検査を実施できなかった。
比較例2では、皮膜付着量が多く、これに伴い乾燥工程での蒸発水分量も多いため、蒸発した水蒸気が誘導加熱炉内で結露し、水滴が鋼帯上に落下し、製造された表面処理鋼帯は外観不良となった。
比較例3では乾燥不良となり、それに伴い製造された表面処理鋼帯は皮膜特性や外観も劣位であった。
In Comparative Examples 1 and 2, the produced surface-treated steel strip satisfied the characteristics such as corrosion resistance and appearance, but the temperature was 60 ° C. or higher on the inspection table, and the inspection by the operator could not be performed for safety reasons.
In Comparative Example 2, since the amount of film adhered is large and the amount of water evaporated in the drying step is also large, the evaporated water vapor condenses in the induction heating furnace, and water droplets fall on the steel strip to produce the surface. The treated steel strip had a poor appearance.
In Comparative Example 3, the drying was poor, and the surface-treated steel strip produced accordingly was inferior in film characteristics and appearance.

これに対して、発明例1〜10では、検査台温度が60℃未満(40℃以下)でオペレータ検査に問題がなく、製造された表面処理鋼帯は耐食性、外観等の特性を満足していた。特に、減圧室の圧力を表面処理液の溶媒の蒸気圧未満にした発明例5〜9は、皮膜の乾燥状態が特に良好であった。
また、発明例9は、制振装置である抑えロール11を使用しなかったために、表面処理鋼帯が乾燥設備を通過する間に同設備の構成部材(抑えロール11を除く)に接触して皮膜の「こすれ」が生じ、この皮膜欠陥が100コイル中1〜5本程度の割合で観察された。これに対して、制振装置である抑えロール11を使用した発明例1〜8,10では、そのような皮膜欠陥は観察されなかった。
また、合金化溶融亜鉛めっき鋼板(GA)を被処理金属帯とし、これにクロメートフリー表面処理を施して表面処理鋼帯を製造し、上記と同様の評価を行ったところ、本発明条件を満足することにより優れた耐食性及び外観性を有する表面処理鋼帯が得られた。
On the other hand, in Invention Examples 1 to 10, the inspection table temperature is less than 60 ° C. (40 ° C. or lower), there is no problem in the operator inspection, and the manufactured surface-treated steel strip satisfies the characteristics such as corrosion resistance and appearance. It was. In particular, in Invention Examples 5 to 9 in which the pressure in the decompression chamber was set to less than the vapor pressure of the solvent of the surface treatment liquid, the dry state of the film was particularly good.
Further, in Invention Example 9, since the suppression roll 11 which is a vibration damping device was not used, the surface-treated steel strip came into contact with the constituent members (excluding the suppression roll 11) of the equipment while passing through the drying equipment. “Rubbing” of the film occurred, and this film defect was observed at a ratio of about 1 to 5 out of 100 coils. On the other hand, in Invention Examples 1 to 8 and 10 using the damping roll 11 which is a vibration damping device, such a film defect was not observed.
Further, an alloyed hot-dip galvanized steel sheet (GA) was used as a metal strip to be treated, and a chromate-free surface treatment was applied to the metal strip to produce a surface-treated steel strip, and the same evaluation as above was performed. As a result, the conditions of the present invention were satisfied. By doing so, a surface-treated steel strip having excellent corrosion resistance and appearance was obtained.

A 減圧室
a 主減圧室
b1,b2 予備減圧室
1 ロールコーター
2a,2b ブライドルロール
3,3a,3b1,3b2 真空ポンプ
4 入口
5 出口
6 入口
7 出口
8,9 出入口
10 加熱装置
11 抑えロール
12 塗布ロール
13 ロールシール機構
30 高圧用ポンプ
31 低圧用ポンプ
S 鋼帯
A decompression chamber
a Main decompression chamber
b 1 , b 2 Preliminary decompression chamber 1 Roll coater 2a, 2b Bridle roll 3, 3a, 3b 1 , 3b 2 Vacuum pump 4 Inlet 5 Outlet 6 Inlet 7 Outlet 8, 9 Inlet 10 Heating device 11 Suppressing roll 12 Coating roll 13 Roll Seal mechanism 30 High-pressure pump 31 Low-pressure pump S Steel strip

Claims (15)

連続ラインにおける表面処理金属帯の製造方法であって、
金属帯の表面に表面処理液(x)を塗布する表面処理工程と、
該表面処理工程で金属帯表面に塗布された表面処理液(x)を乾燥させる乾燥工程を有し、
該乾燥工程では、金属帯を大気圧未満に減圧された減圧室(A)を通過させ、該減圧室(A)において、金属帯表面に付着した表面処理液(x)の溶媒を揮発させることを特徴とする表面処理金属帯の製造方法。
A method for manufacturing a surface-treated metal strip on a continuous line.
The surface treatment process of applying the surface treatment liquid (x) to the surface of the metal band,
The surface treatment step includes a drying step of drying the surface treatment liquid (x) applied to the surface of the metal strip.
In the drying step, the metal band is passed through a decompression chamber (A) decompressed to less than atmospheric pressure, and the solvent of the surface treatment liquid (x) adhering to the surface of the metal band is volatilized in the decompression chamber (A). A method for producing a surface-treated metal strip, which comprises.
減圧室(A)が表面処理液(x)の溶媒の蒸気圧以下(但し、溶媒が蒸気圧が異なる2種以上の液体からなる場合には、蒸気圧が低い方の液体の蒸気圧以下)に減圧されていることを特徴とする請求項1に記載の表面処理金属帯の製造方法。 The decompression chamber (A) is below the vapor pressure of the solvent of the surface treatment liquid (x) (however, when the solvent consists of two or more liquids with different vapor pressures, the vapor pressure of the liquid with the lower vapor pressure or less) The method for producing a surface-treated metal band according to claim 1, wherein the vapor pressure is reduced to 1. 表面処理液(x)の溶媒の主成分が水であり、減圧室(A)が605Pa以上101kPa以下に減圧されていることを特徴とする請求項2に記載の表面処理金属帯の製造方法。 The method for producing a surface-treated metal band according to claim 2, wherein the main component of the solvent of the surface-treating liquid (x) is water, and the pressure reducing chamber (A) is reduced to 605 Pa or more and 101 kPa or less. 減圧室(A)は、主減圧室(a)と、その入側及び出側にそれぞれ付設された予備減圧室(b1),(b2)とを有し、金属帯を、大気圧未満に減圧された両予備減圧室(b1),(b2)を通じて主減圧室(a)を通過させることを特徴とする請求項1〜3のいずれかに記載の表面処理金属帯の製造方法。 The decompression chamber (A) has a main decompression chamber (a) and preliminary decompression chambers (b 1 ) and (b 2 ) attached to its entry side and exit side, respectively, and the metal band is less than atmospheric pressure. The method for producing a surface-treated metal band according to any one of claims 1 to 3, wherein the main decompression chamber (a) is passed through both the preliminary decompression chambers (b 1 ) and (b 2 ). .. 減圧室(A)の入側にロールコーターを設け、該ロールコーターにより金属帯表面に表面処理液(x)を塗布することを特徴とする請求項1〜4のいずれかに記載の表面処理金属帯の製造方法。 The surface-treated metal according to any one of claims 1 to 4, wherein a roll coater is provided on the entrance side of the decompression chamber (A), and the surface treatment liquid (x) is applied to the surface of the metal band by the roll coater. How to make an obi. 減圧室(A)の内部、減圧室(A)の入側直前の位置、減圧室(A)の出側直後の位置のうちの少なくとも1箇所に加熱装置を設け、該加熱装置により金属帯を加熱することを特徴とする請求項1〜5のいずれかに記載の表面処理金属帯の製造方法。 A heating device is provided at least one of the inside of the decompression chamber (A), the position immediately before the entrance side of the decompression chamber (A), and the position immediately after the exit side of the decompression chamber (A), and the metal band is formed by the heating device. The method for producing a surface-treated metal band according to any one of claims 1 to 5, wherein the surface-treated metal band is heated. 減圧室(A)の内部、減圧室(A)の入側直前の位置、減圧室(A)の出側直後の位置のうちの少なくとも1箇所に制振装置を設け、該制振装置により金属帯の振動を抑制することを特徴とする請求項1〜6のいずれかに記載の表面処理金属帯の製造方法。 A vibration damping device is provided at least one of the inside of the decompression chamber (A), the position immediately before the entrance side of the decompression chamber (A), and the position immediately after the exit side of the decompression chamber (A), and the metal is provided by the vibration damping device. The method for producing a surface-treated metal band according to any one of claims 1 to 6, wherein the vibration of the band is suppressed. 減圧室(A)の入側にロールコーターを設け、該ロールコーターにより金属帯表面に表面処理液(x)を塗布し、且つ主減圧室(a)の出側に付設された予備減圧室(b2)内に制振装置を設け、該制振装置により金属帯の振動を抑制することを特徴とする請求項4に記載の表面処理金属帯の製造方法。 A roll coater is provided on the entrance side of the decompression chamber (A), the surface treatment liquid (x) is applied to the surface of the metal band by the roll coater, and a preliminary decompression chamber (a) provided on the exit side of the main decompression chamber (a). b 2 ) The method for producing a surface-treated metal band according to claim 4, wherein a vibration damping device is provided in the vibration damping device, and the vibration of the metal band is suppressed by the vibration damping device. ロールコーターを構成する上下1対の塗布ロールが、金属帯を拘束しつつ減圧室(A)の入口方向に送り出すことにより、金属帯を減圧室(A)内に水平通板するように案内することを特徴とする請求項5又は8に記載の表面処理金属帯の製造方法。 A pair of upper and lower coating rolls constituting the roll coater guides the metal band to pass horizontally into the decompression chamber (A) by sending the metal band toward the inlet of the decompression chamber (A) while restraining the metal band. The method for producing a surface-treated metal band according to claim 5 or 8, characterized in that. 制振装置は、抑えロール、非接触式の電磁式制振装置の中から選ばれる1種以上であることを特徴とする請求項7又は8に記載の表面処理金属帯の製造方法。 The method for manufacturing a surface-treated metal band according to claim 7 or 8, wherein the vibration damping device is one or more selected from a suppression roll and a non-contact electromagnetic vibration damping device. 主減圧室(a)の入側に付設された予備減圧室(b1)内に加熱装置を設け、該加熱装置により金属帯を加熱することを特徴とする請求項4又は8に記載の表面処理金属帯の製造方法。 The surface according to claim 4 or 8, wherein a heating device is provided in a preliminary decompression chamber (b 1 ) provided on the entrance side of the main decompression chamber (a), and the metal band is heated by the heating device. A method for manufacturing a treated metal band. 加熱装置で金属帯を加熱することにより、表面処理液(x)の溶媒の蒸気圧を調整することを特徴とする請求項6又は11に記載の表面処理金属帯の製造方法。 The method for producing a surface-treated metal band according to claim 6 or 11, wherein the vapor pressure of the solvent of the surface-treated liquid (x) is adjusted by heating the metal band with a heating device. 減圧室(A)を通過する際の金属帯の温度に応じて、減圧室(A)内の圧力を制御することを特徴とする請求項1〜12のいずれかに記載の表面処理金属帯の製造方法。 The surface-treated metal band according to any one of claims 1 to 12, wherein the pressure in the decompression chamber (A) is controlled according to the temperature of the metal band when passing through the decompression chamber (A). Production method. 連続ラインによる表面処理金属帯の製造設備であって、
金属帯の表面に表面処理液(x)を塗布する表面処理設備と、
該表面処理設備で金属帯表面に塗布された表面処理液(x)を乾燥させる乾燥設備を有し、
該乾燥設備は金属帯を通過させる減圧室(A)を有し、該減圧室(A)において、金属帯表面に付着した表面処理液(x)の溶媒を揮発させるようにしたことを特徴とする表面処理金属帯の製造設備。
It is a manufacturing facility for surface-treated metal strips using a continuous line.
Surface treatment equipment that applies surface treatment liquid (x) to the surface of the metal strip,
The surface treatment facility has a drying facility for drying the surface treatment liquid (x) applied to the surface of the metal strip.
The drying facility has a decompression chamber (A) through which the metal band passes, and the decompression chamber (A) is characterized in that the solvent of the surface treatment liquid (x) adhering to the surface of the metal band is volatilized. Surface-treated metal strip manufacturing equipment.
減圧室(A)は、主減圧室(a)と、その入側及び出側にそれぞれ付設された予備減圧室(b1),(b2)とを有し、金属帯を両予備減圧室(b1),(b2)を通じて主減圧室(a)を通過させるようにしたことを特徴とする請求項14に記載の表面処理金属帯の製造設備。 The decompression chamber (A) has a main decompression chamber (a) and preliminary decompression chambers (b 1 ) and (b 2 ) attached to its entry side and exit side, respectively, and has both preliminary decompression chambers with metal bands. The equipment for manufacturing a surface-treated metal band according to claim 14, wherein the main decompression chamber (a) is passed through (b 1 ) and (b 2 ).
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