TW202012654A - Manufacturing method for hot-dip galvanized steel sheet, and manufacturing method for alloyed hot-dip galvanized steel sheet - Google Patents
Manufacturing method for hot-dip galvanized steel sheet, and manufacturing method for alloyed hot-dip galvanized steel sheet Download PDFInfo
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Abstract
Description
本揭示係有關熔融鍍鋅鋼板之製造方法及合金化熔融鍍鋅鋼板之製造方法。The present disclosure relates to a method for manufacturing hot-dip galvanized steel sheet and a method for manufacturing alloyed hot-dip galvanized steel sheet.
熔融鍍鋅鋼板(以下亦稱為GI)及合金化熔融鍍鋅鋼板(以下亦稱為GA)係藉由如下製造方法製造。首先,準備成為熔融鍍鋅處理之對象的鋼板(母材鋼板)。母材鋼板可為熱軋鋼板,亦可為冷軋鋼板。將所準備之母材鋼板(上述之熱軋鋼板或冷軋鋼板)浸漬於熔融鍍鋅浴中,實施熔融鍍鋅處理,製造熔融鍍鋅鋼板。製造合金化熔融鍍鋅鋼板時,進而將熔融鍍鋅鋼板於合金化爐內進行熱處理,而製造合金化熔融鍍鋅鋼板。The hot-dip galvanized steel sheet (hereinafter also referred to as GI) and the alloyed hot-dip galvanized steel sheet (hereinafter also referred to as GA) are manufactured by the following manufacturing method. First, a steel sheet (base material steel sheet) to be subjected to hot-dip galvanizing treatment is prepared. The base material steel plate may be a hot rolled steel plate or a cold rolled steel plate. The prepared base material steel sheet (the above-mentioned hot-rolled steel sheet or cold-rolled steel sheet) is immersed in a hot-dip galvanizing bath, and hot-dip galvanizing treatment is performed to manufacture a hot-dip galvanized steel sheet. When manufacturing an alloyed hot-dip galvanized steel sheet, the hot-dip galvanized steel sheet is further heat-treated in an alloying furnace to manufacture an alloyed hot-dip galvanized steel sheet.
熔融鍍鋅鋼板及合金化熔融鍍鋅鋼板之製造步驟中實施之熔融鍍鋅處理之細節如下。熔融鍍鋅處理所用之熔融鍍鋅設備具備收納熔融鍍鋅浴之熔融鋅鍋、配置於熔融鍍鋅浴中之沉降輥、及氣體吹掃裝置。The details of the hot-dip galvanizing treatment performed in the manufacturing steps of the hot-dip galvanized steel sheet and the alloyed hot-dip galvanized steel sheet are as follows. The hot-dip galvanizing equipment used in the hot-dip galvanizing process includes a molten zinc pot that houses the hot-dip galvanizing bath, a settling roller disposed in the hot-dip galvanizing bath, and a gas purge device.
熔融鍍鋅處理中,例如將經燒鈍處理之鋼板浸漬於熔融鍍鋅浴。接著,藉由配置於熔融鍍鋅浴中之沉降輥,將鋼板之行進方向轉變為向上方,將鋼板自熔融鍍鋅浴拉起。對於拉起且向上方行進之鋼板,自氣體吹掃裝置對鋼板表面吹附吹掃氣體。噴出氣體刮除剩餘之熔融鋅,調整鋼板表面之鍍敷附著量。藉由以上方法,實施熔融鍍鋅處理。又,製造合金化熔融鍍鋅鋼板時,進而將鍍敷附著量經調整之鋼板裝入合金化爐中實施合金化處理。In the hot-dip galvanizing process, for example, the steel plate subjected to the passivation treatment is immersed in a hot-dip galvanizing bath. Next, by using a settling roller arranged in the hot-dip galvanizing bath, the traveling direction of the steel plate is turned upward, and the steel plate is pulled up from the hot-dip galvanizing bath. For a steel plate that is pulled up and travels upward, a purge gas is blown onto the surface of the steel plate from the gas purge device. The sprayed gas scrapes off the remaining molten zinc to adjust the amount of plating adhesion on the surface of the steel plate. By the above method, hot galvanizing treatment is performed. In addition, when manufacturing an alloyed hot-dip galvanized steel sheet, the steel sheet in which the amount of plating adhesion is adjusted is further charged into an alloying furnace to perform alloying treatment.
因此,上述之熔融鍍鋅處理中,自浸漬於熔融鍍鋅浴中之鋼板溶出Fe至熔融鍍鋅浴中。自鋼板溶出至熔融鍍鋅浴中之Fe與存在於熔融鍍鋅浴中之Al或Zn反應時,形成稱為碎渣之金屬間化合物。碎渣中存在有浮渣(top dross)與底渣(bottom dross)。浮渣係比重較熔融鍍鋅浴輕之金屬間化合物,浮於熔融鍍鋅浴之液面上之碎渣。底渣係比重較熔融鍍鋅浴重之金屬間化合物,堆積於熔融鋅鍋之底部之碎渣。Therefore, in the above hot-dip galvanizing treatment, Fe is eluted from the steel sheet immersed in the hot-dip galvanizing bath to the hot-dip galvanizing bath. When Fe eluted from the steel sheet into the hot-dip galvanizing bath reacts with Al or Zn present in the hot-dip galvanizing bath, an intermetallic compound called slag is formed. There are top dross and bottom dross in the broken slag. Scum is an intermetallic compound with a lighter specific gravity than the hot-dip galvanizing bath. It is a broken dross floating on the liquid surface of the hot-dip galvanizing bath. The bottom slag is the intermetallic compound whose specific gravity is heavier than that of the hot-dip galvanizing bath, and is accumulated in the bottom of the molten zinc pot.
熔融鍍鋅處理中,因熔融鍍鋅浴中之鋼板行進而發生伴隨流。所謂伴隨流意指伴隨鋼板行進,於熔融鍍鋅浴中發生流動。如上述,浮渣由於浮於熔融鍍鋅浴之液面上,故不太受到伴隨流之影響。相對於此,底渣堆積於熔融鋅鍋之底部。因此,會有因伴隨流而自堆積之熔融鋅鍋底揚起之情況。該情況下,底渣浮游於熔融鍍鋅浴中。此種浮游底渣有附著於熔融鍍鋅處理中之鋼板表面之情況。In the hot dip galvanizing process, accompanying flow occurs as the steel sheet in the hot dip galvanizing bath proceeds. The accompanying flow means that as the steel sheet travels, it flows in the hot-dip galvanizing bath. As mentioned above, the scum floats on the liquid surface of the hot-dip galvanizing bath, so it is less affected by the accompanying flow. In contrast, bottom slag accumulates at the bottom of the molten zinc pot. Therefore, there is a case where the bottom of the molten zinc pot that has accumulated due to the flow rises. In this case, the bottom dross floats in the hot-dip galvanizing bath. Such floating bottom slag may adhere to the surface of the steel plate during the hot-dip galvanizing process.
附著於鋼板表面之底渣於合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板表面有成為點狀缺陷之情況。此等底渣起因之表面缺陷於本說明書中稱為「碎渣缺陷」。碎渣缺陷會使合金化熔融鍍鋅鋼板及熔融鍍鋅鋼板之外觀降低,或耐腐蝕性降低。因此,較好為可抑制碎渣缺陷發生。The bottom slag adhering to the surface of the steel sheet may become point defects on the surface of the alloyed hot-dip galvanized steel sheet or the hot-dip galvanized steel sheet. The surface defects caused by these bottom slags are called "debris defects" in this manual. Debris defects will reduce the appearance of alloyed galvanized steel sheets and galvanized steel sheets, or reduce corrosion resistance. Therefore, it is preferable to suppress the occurrence of chipping defects.
抑制碎渣缺陷發生之技術已提案於日本特開平11-350096號公報(專利文獻1)及日本特開平11-350097號公報(專利文獻2)。Techniques for suppressing the occurrence of chipping defects have been proposed in Japanese Patent Laid-Open No. 11-350096 (Patent Document 1) and Japanese Patent Laid-Open No. 11-350097 (Patent Document 2).
專利文獻1中,於合金化熔融鍍鋅鋼板之製造方法中,熔融鋅浴溫度設為T(℃),以Cz=-0.015×T+0.76所定義之邊界Al濃度設為Cz (wt%)。該情況下,熔融鍍鋅溫度T保持於435~500℃之範圍內,並且浴中Al濃度保持於Cz±0.01wt%之範圍內。專利文獻1中,於δ1
相與ζ相之邊界實施熔融鍍鋅處理。專利文獻2中,於合金化熔融鍍鋅鋼板之製造方法中,浴中Al濃度保持於0.15±0.01wt%之範圍內。專利文獻2中,於浮渣與δ1
相之邊界實施熔融鍍鋅處理。
[先前技術文獻]
[專利文獻]In
[專利文獻1] 日本特開平11-350096號公報 [專利文獻2] 日本特開平11-350097號公報 [非專利文獻][Patent Document 1] Japanese Patent Laid-Open No. 11-350096 [Patent Document 2] Japanese Patent Laid-Open No. 11-350097 [Non-patent literature]
[非專利文獻1] Practical Applications of Phase Diagrams in Continuous Galvanizing, Nai-Yong Tang, Journal of Phase Equilibria and Diffusion Vol. 27, No. 5, 2006[Non-Patent Literature 1] Practical Applications of Phase Diagrams in Continuous Galvanizing, Nai-Yong Tang, Journal of Phase Equilibria and Diffusion Vol. 27, No. 5, 2006
[發明欲解決之課題][Problem to be solved by invention]
如專利文獻1及2所記載,可知熔融鍍鋅浴中之Al濃度較高時,碎渣大多並非底渣,而是浮渣。浮渣浮於熔融鍍鋅浴液面。因此,自熔融鍍鋅浴去除浮渣比自熔融鍍鋅浴去除底渣更容易。因此,以往之熔融鍍鋅處理,有時採用提高熔融鍍鋅浴中之Al含量,使熔融鍍鋅浴中之碎渣作為浮渣浮於熔融鍍鋅浴液面並去除,而抑制碎渣缺陷發生之方法。如此,生成浮渣作為碎渣之操作於本說明書中稱為浮渣操作。As described in
藉由浮渣操作,可抑制碎渣缺陷。然而,提高熔融鍍鋅浴中之Al濃度時,合金化處理中之熔融鍍鋅層變得不容易合金化。因此,為了促進合金化,尤其較好為抑制熔融鍍鋅液中之Al濃度。實施浮渣操作時,熔融鍍鋅浴中之Al濃度也總是變高。By the operation of scum, the defects of broken slag can be suppressed. However, when the Al concentration in the hot-dip galvanizing bath is increased, the hot-dip galvanized layer in the alloying process becomes difficult to alloy. Therefore, in order to promote alloying, it is particularly preferable to suppress the Al concentration in the hot-dip galvanizing bath. When the scumming operation is carried out, the Al concentration in the hot-dip galvanizing bath also always becomes high.
抑制熔融鍍鋅浴中之Al濃度,生成底渣作為碎渣之操作於本說明書稱為底渣操作。底渣操作之情況,為了抑制熔融鍍鋅浴中之游離Al濃度,可促進合金化。然而,底渣操作之情況,要求可抑制因底渣生成所致之碎渣缺陷之方法。The operation of suppressing the Al concentration in the hot-dip galvanizing bath and generating bottom slag as broken slag is called bottom slag operation in this specification. In the case of bottom slag operation, in order to suppress the free Al concentration in the hot-dip galvanizing bath, alloying can be promoted. However, the bottom slag operation requires a method that can suppress chipping defects caused by bottom slag formation.
本發明之目的係提供於熔融鍍鋅處理中即使生成底渣,亦可抑制碎渣缺陷發生的熔融鍍鋅鋼板及合金化熔融鍍鋅鋼板之製造方法。 [用以解決課題之手段]An object of the present invention is to provide a method for producing a hot-dip galvanized steel sheet and an alloyed hot-dip galvanized steel sheet that can suppress the occurrence of chipping defects even if a bottom dross is generated in the hot-dip galvanizing process. [Means to solve the problem]
本揭示之熔融鍍鋅鋼板之製造方法具備下述步驟: 以滿足式(1)之方式調整熔融鍍鋅浴中之游離Al濃度CAl (質量%)及浴溫T(℃),於前述熔融鍍鋅浴中生成粒徑為300μm以上之粗大底渣之粗大底渣生成步驟,及 將前述粗大底渣生成步驟後之前述熔融鍍鋅浴之前述游離Al濃度CAl 及前述浴溫T調整為滿足式(2),使用前述游離Al濃度CAl 及前述浴溫T滿足式(2)之前述熔融鍍鋅浴,實施熔融鍍鋅處理,於鋼板形成熔融鍍鋅層之熔融鍍鋅處理步驟, The manufacturing method of the hot-dip galvanized steel sheet of the present disclosure includes the following steps: The free Al concentration C Al (mass %) and the bath temperature T (°C) in the hot-dip galvanizing bath are adjusted in a manner that satisfies the formula (1) to melt A coarse bottom slag generation step for generating a coarse bottom slag having a particle diameter of 300 μm or more in the galvanizing bath, and adjusting the free Al concentration C Al and the bath temperature T of the molten galvanizing bath after the coarse bottom slag generation step to Satisfying formula (2), using the above-mentioned free Al concentration C Al and the above bath temperature T satisfying the above-mentioned hot-dip galvanizing bath, performing hot-dip galvanizing treatment, forming a hot-dip galvanizing layer on the steel sheet, a hot-dip galvanizing treatment step,
本揭示之合金化熔融鍍鋅鋼板之製造方法具備下述步驟: 實施上述熔融鍍鋅鋼板之製造方法,製造熔融鍍鋅鋼板之步驟,及 對前述熔融鍍鋅鋼板實施合金化處理之合金化處理步驟。 [發明效果]The manufacturing method of the alloyed hot-dip galvanized steel sheet of the present disclosure includes the following steps: Implementing the above method of manufacturing the hot-dip galvanized steel sheet, the steps of manufacturing the hot-dip galvanized steel sheet, and The alloying step of alloying the aforementioned hot-dip galvanized steel sheet. [Effect of the invention]
本揭示之熔融鍍鋅鋼板之製造方法及合金化熔融鍍鋅鋼板之製造方法於熔融鍍鋅處理中即使生成底渣,亦可抑制碎渣缺陷發生。The manufacturing method of the hot-dip galvanized steel sheet and the manufacturing method of the alloyed hot-dip galvanized steel sheet of the present disclosure can suppress the occurrence of chipping defects even if a bottom dross is generated in the hot-dip galvanizing process.
[關於碎渣缺陷產生要因][Regarding the causes of slag defects]
本發明人等首先針對實施底渣操作時,成為碎渣缺陷要因之碎渣進行檢討。碎渣缺陷係以熔融鍍鋅處理中生成之碎渣為發生要因。以往之研究中已報導,作為熔融鍍鋅處理中發生之碎渣存在如下種類。 (A) 浮渣 (B) δ1 相碎渣 (C) Γ1 相碎渣 (D) ζ相碎渣The inventors first reviewed the dross that became the cause of dross defects when the bottom dross operation was performed. The slag defects are caused by the slag generated during the hot-dip galvanizing process. It has been reported in previous studies that the following types of slag generated during the hot dip galvanizing process exist. (A) Scum (B) δ 1 phase crushed slag (C) Γ 1 phase crushed slag (D) ζ phase crushed slag
浮渣如前述比重輕於熔融鍍鋅浴。因此,浮渣容易浮於熔融鍍鋅浴液面。浮渣之化學組成,以質量%計,係由45%之Al與38%之Fe及17%之Zn所成。浮渣由於浮於熔融鍍鋅浴液面,故容易自熔融鍍鋅浴去除。因此,浮渣操作之情況,藉由去除浮渣,可有效抑制碎渣缺陷。The scum is lighter than the hot-dip galvanizing bath as mentioned above. Therefore, scum is likely to float on the surface of the hot-dip galvanizing bath. The chemical composition of the scum, in terms of mass %, is composed of 45% Al, 38% Fe and 17% Zn. Since the scum floats on the liquid surface of the hot-dip galvanizing bath, it is easily removed from the hot-dip galvanizing bath. Therefore, the scum operation can be effectively suppressed by removing scum.
另一方面,δ1 相碎渣、Γ1 相碎渣及ζ相碎渣稱為底渣。底渣比重重於熔融鍍鋅浴。因此,底渣容易堆積於儲存熔融鍍鋅浴之熔融鍍鋅鍋之底部。實施底渣操作時,該等底渣成為缺陷要因時,以往之研究中才會被考慮。On the other hand, δ 1 phase slag, Γ 1 phase slag and ζ phase slag are called bottom slag. The bottom slag is heavier than the hot-dip galvanizing bath. Therefore, the bottom slag is easy to accumulate on the bottom of the hot-dip galvanizing pot that stores the hot-dip galvanizing bath. When carrying out the bottom slag operation, when such bottom slag becomes the cause of defects, it will be considered in previous studies.
此處,δ1 相碎渣之結晶構造為六方晶。δ1 相碎渣之化學組成,以質量%計,係由1%以下之Al、9%以上之Fe及90%以上之Zn所成。Γ1 相碎渣之結晶構造為面心立方晶。Γ1 相碎渣之化學組成,以質量%計,係由20%之Fe及80%左右之Zn所成。ζ相之結晶構造為單斜晶。ζ相之化學組成,以質量%計,係由1%以下之Al、6%左右之Fe及94%左右之Zn所成。Here, the crystal structure of the delta 1 phase slag is hexagonal. The chemical composition of δ 1 phase slag, in mass%, is composed of less than 1% Al, more than 9% Fe and more than 90% Zn. The crystal structure of Γ 1 phase slag is face-centered cubic crystal. The chemical composition of Γ 1 phase slag, in mass%, is composed of 20% Fe and about 80% Zn. The crystal structure of the ζ phase is monoclinic. The chemical composition of the ζ phase, in mass%, is composed of less than 1% Al, about 6% Fe, and about 94% Zn.
以往之研究中,存在多數報導例報導底渣中,碎渣缺陷之主要原因為δ1
相碎渣。上述專利文獻1及2中,亦認為δ1
相碎渣為碎渣缺陷之要因之一。因此,本發明人等最初亦認為δ1
相碎渣係碎渣缺陷之主要要因,而進行調查及研究。然而,熔融鍍鋅處理中抑制δ1
相碎渣時,依然有於熔融鍍鋅鋼板及合金化熔融鍍鋅鋼板之表面發生碎渣缺陷之情況。In previous studies, there are many reported cases of bottom slag, the main reason for the slag defect is δ 1 phase slag. In the above-mentioned
因此,本發明人等認為會不會碎渣缺陷之發生要因並非δ1 相碎渣,而是其他碎渣。因此,本發明人等使用發生碎渣缺陷之合金化熔融鍍鋅鋼板實施底渣操作,針對碎渣缺陷部分之組成及結晶構造,重新進行分析。本發明人等進一步針對底渣操作中熔融鍍鋅浴中發生之碎渣種類亦重新進行分析。其結果,本發明人針對碎渣缺陷,獲得與以往研究結果不同之如下見解。Therefore, the inventors believe that the cause of the occurrence of the slag defect is not δ 1 phase slag but other slag. Therefore, the present inventors used the alloyed hot-dip galvanized steel sheet with slag defects to perform the bottom slag operation, and re-analyzed the composition and crystal structure of the slag defects. The present inventors further analyzed the type of slag that occurred in the hot-dip galvanizing bath during the bottom slag operation. As a result, the present inventors have obtained the following insights that are different from the results of previous researches on the slag defects.
首先,使用EPMA(Electron Probe Micro Analyzer:電子束微分析儀)分析合金化熔融鍍鋅鋼板表面之碎渣缺陷部分之化學組成。再者,使用TEM (Transmission Electron Microscope:透過型電子顯微鏡)解析碎渣部分之結晶構造。其結果,碎渣缺陷部分之化學組成以質量%計,由2%之Al、8%之Fe及90%之Zn所成,結晶構造為面心立方晶。First, EPMA (Electron Probe Micro Analyzer: Electron Beam Micro Analyzer) was used to analyze the chemical composition of the slag defect portion on the surface of the alloyed galvanized steel sheet. In addition, the TEM (Transmission Electron Microscope) is used to analyze the crystal structure of the slag portion. As a result, the chemical composition of the defective part of the slag is 2% of Al, 8% of Fe and 90% of Zn, and the crystal structure is a face-centered cubic crystal.
以往被認為係碎渣缺陷之主要原因之δ1 相碎渣的化學組成(以質量%計,係1%以下之Al、9%以上之Fe及90%以上之Zn)與上述碎渣缺陷部分的化學組成類似。然而,δ1 相碎渣的結晶構造為六方晶,並非於碎渣缺陷部分所特定出之面心立方晶。因此,本發明人等認為以往被認為係碎渣缺陷之主要原因之δ1 相碎渣實際上並非碎渣缺陷之主要原因。In the past, the chemical composition of δ 1 phase slag (mainly 1% or less Al, 9% or more Fe, and 90% or more Zn), which is considered to be the main cause of slag defects, and the above slag defect parts The chemical composition is similar. However, the crystal structure of the delta 1 phase slag is hexagonal crystal, not a face-centered cubic crystal specified in the slag defect part. Therefore, the inventors believe that the δ 1 phase slag, which was considered to be the main cause of slag defects, is not actually the main cause of the slag defects.
因此,本發明人等進行成為碎渣缺陷原因之碎渣的特定。上述之底渣(B)~(D)之碎渣中,關於Γ1 相碎渣,結晶構造雖係與碎渣缺陷部分相同的面心立方晶,但化學組成(以質量%計,係20%之Fe及80%之Zn)與碎渣缺陷部分之化學組成大為不同。關於ζ相碎渣,化學組成(以質量%計,係1%以下之Al、6%左右之Fe及94%左右之Zn)與碎渣缺陷部分之化學組成不同,而且結晶構造(單斜晶)亦與碎渣缺陷部分之結晶構造(面心立方晶)不同。Therefore, the present inventors specified the slag which is the cause of slag defects. Among the above-mentioned bottom slags (B) to (D), the Γ 1 phase slag has a crystal structure with the same face-centered cubic crystal as the defective part of the slag, but its chemical composition (in mass% is 20 % Fe and 80% Zn) are very different from the chemical composition of the broken slag defects. Regarding the ζ-phase slag, the chemical composition (in terms of mass%, less than 1% of Al, about 6% of Fe, and about 94% of Zn) is different from the chemical composition of the defective part of the slag, and the crystal structure (monoclinic ) Is also different from the crystal structure (face-centered cubic crystal) of the defective part of the slag.
基於以上檢討結果,本發明人等認為碎渣缺陷並非起因於上述之(B)~(D)之碎渣者。因此,本發明人等認為碎渣缺陷會不會是起因於上述(B)~(D)以外之其他種類之底渣者。Based on the results of the above review, the inventors believe that the slag defects are not caused by the slag from (B) to (D) above. Therefore, the inventors believe that the slag defects may be caused by other types of bottom slag than (B) to (D).
因此,本發明人等進一步進行熔融鍍鋅浴中之底渣分析。底渣之分析係使用上述EPMA及TEM。其結果,本發明人等探究出熔融鍍鋅浴中生成之底渣係以Γ2 相碎渣存在。Therefore, the present inventors further performed bottom slag analysis in the hot-dip galvanizing bath. For the analysis of bottom slag, the aforementioned EPMA and TEM were used. As a result, the present inventors investigated that the bottom slag generated in the hot-dip galvanizing bath exists as Γ 2 phase crushed slag.
Γ2 相碎渣之化學組成,以質量%計,係由2%之Al、8%之Fe及90%之Zn所成,與上述解析之碎渣缺陷部分之化學組成一致。再者,Γ2 相碎渣之結晶構造為面心立方晶,與碎渣缺陷之結晶構造一致。因此,本發明人等認為Γ2 相碎渣會不會是碎渣缺陷之主要原因。而且,由於Γ2 相碎渣之比重大於熔融鍍鋅浴的比重,故Γ2 相碎渣相當於可堆積於熔融鋅鍋底部之底渣。The chemical composition of the Γ 2 phase slag, in mass%, is composed of 2% Al, 8% Fe, and 90% Zn, which is consistent with the chemical composition of the slag defect part analyzed above. Furthermore, the crystal structure of the Γ 2 phase slag is a face-centered cubic crystal, which is consistent with the crystal structure of the slag defect. Therefore, the present inventors considered whether the Γ 2 phase slag is the main cause of slag defects. Moreover, since the proportion of Γ 2 phase crushed slag is greater than that of the molten galvanizing bath, the Γ 2 phase crushed slag is equivalent to bottom slag that can accumulate on the bottom of the molten zinc pot.
本發明人等進一步針對Γ2 相碎渣及其他(B)~(D)之碎渣進行調查。其結果判知碎渣缺陷係起因於硬質碎渣,軟質碎渣不易形成碎渣缺陷。本發明人等進一步檢討之結果,判知上述(B)~(D)之碎渣及Γ2 相碎渣中,Γ2 相碎渣為最硬質的碎渣。The inventors further investigated Γ 2 phase slag and other (B) to (D) slag. As a result, it was found that the slag defects were caused by hard slag, and soft slag was not easy to form slag defects. As a result of further review by the present inventors, it was determined that among the above-mentioned crushed slags (B) to (D) and the Γ 2 phase crushed slag, the Γ 2 phase crushed slag is the hardest crushed slag.
基於以上檢討結果,本發明人等認為實施熔融鍍鋅處理之合金化熔融鍍鋅鋼板及熔融鍍鋅鋼板的表面發生之碎渣缺陷的主要原因並非δ1 相碎渣,而是Γ2 相碎渣。進而,本發明人等獲得之見解為對底渣所分類之碎渣,雖為Γ2 相碎渣、δ1 相碎渣、ζ相碎渣及Γ1 相碎渣之任一者,但於熔融鍍鋅浴中,Γ1 相碎渣幾乎不存在。Based on the results of the above review, the present inventors believe that the main cause of the slag defects on the surface of the alloyed hot-dip galvanized steel sheet and the hot-dip galvanized steel sheet subjected to hot-dip galvanizing treatment is not δ 1 phase slag, but Γ 2 phase slag Slag. Furthermore, the inventors obtained the insight that the broken slag classified into bottom slag is any of Γ 2 phase slag, δ 1 phase slag, ζ phase slag, and Γ 1 phase slag, but In the hot dip galvanizing bath, Γ 1 phase slag is almost absent.
因此,本發明人等進一步針對抑制熔融鍍鋅浴中游離Al濃度,實施底渣操作時之碎渣缺陷進行檢討。因鋼板朝熔融鍍鋅浴之通板所發生之伴隨流會將堆積於熔融鋅鍋底部之底渣的一部分揚起。因此揚起的底渣附著於鋼板。該情況下,可能發生碎渣缺陷。Therefore, the present inventors further reviewed the slag defects when performing the bottom slag operation to suppress the free Al concentration in the hot-dip galvanizing bath. A part of the bottom slag that accumulates on the bottom of the molten zinc pot due to the accompanying flow that occurs when the steel plate passes through the molten galvanizing bath. Therefore, the raised bottom slag adheres to the steel plate. In this case, slag defects may occur.
本文中,本發明人等著眼於底渣尺寸進行檢討。其結果,本發明人等獲得如下見解。將粒徑未達100μm之底渣定義為微細底渣。微細底渣有因伴隨流而於熔融鍍鋅浴中自熔融鋅鍋底部揚起之可能性。然而,假使微細底渣揚起並附著於鋼板,由於底渣尺寸較小,因此亦不易成為碎渣缺陷。另一方面,將粒徑超過300μm之底渣定義為粗大底渣。粗大底渣之質量較重。因此,粗大底渣不易因伴隨流而揚起,不易附著於鋼板。以上調查之結果,本發明人等發現成為碎渣缺陷要因之底渣為粒徑100~300μm之底渣(以下亦稱為中型底渣)。In this article, the inventors waited for the review of the bottom slag size. As a result, the inventors obtained the following findings. The bottom slag with a particle size of less than 100 μm is defined as a fine bottom slag. The fine bottom slag may rise from the bottom of the molten zinc pot in the molten zinc plating bath due to the accompanying flow. However, even if the fine bottom slag is raised and attached to the steel plate, the size of the bottom slag is small, so it is not likely to become a slag defect. On the other hand, bottom dross with a particle size exceeding 300 μm is defined as coarse bottom dross. The quality of coarse bottom slag is heavier. Therefore, the coarse bottom slag is less likely to be lifted by the accompanying flow, and is less likely to adhere to the steel plate. As a result of the above investigation, the present inventors have found that the bottom slag that causes the slag defect is a bottom slag having a particle size of 100 to 300 μm (hereinafter also referred to as a medium-sized bottom slag).
因此,本發明人等認為於實施底渣操作時,於實施熔融鍍鋅處理之期間中(以下亦稱為運轉期間中),若能抑制中型底渣之生成,亦可有效抑制碎渣缺陷。Therefore, the present inventors believe that when the bottom slag operation is carried out, during the period during which the hot-dip galvanizing treatment is performed (hereinafter also referred to as during the operation period), if the generation of medium-sized bottom slag can be suppressed, the slag defects can also be effectively suppressed.
本發明人等首先為了抑制中型底渣之生成,而著眼於各底渣之成長速度。上述(B)~(D)之底渣及Γ2 相碎渣中,Γ2 相碎渣生長最快,δ1 相碎渣最慢。因此,Γ2 相碎渣比δ1 相碎渣更快成長,於遠比δ1 相碎渣更早之階段,Γ2 相碎渣之粒徑已超過100μm。相對於此,δ1 相碎渣之生長速度顯著比Γ2 相碎渣慢。因此,即使δ1 相碎渣核成長,δ1 相碎渣亦不易比Γ2 相更早期成長。因此認為於實施熔融鍍鋅處理步驟之期間(運轉期間),相較於Γ2 相碎渣之生長區域,於δ1 相之生長區域實施熔融鍍鋅處理較佳。The inventors first focused on the growth rate of each bottom slag in order to suppress the formation of medium-sized bottom slag. Among the above bottom slags (B) to (D) and Γ 2 phase crushed slag, Γ 2 phase crushed slag grows fastest, and δ 1 phase crushed slag is the slowest. Thus, Γ 2 δ 1 phase ratio of the slag phase grow faster slag, the slag in an earlier phase than the δ 1 phase, the particle size of the slag phase Γ 2 exceeds 100μm. In contrast, the growth rate of δ 1 phase slag is significantly slower than that of Γ 2 phase slag. Therefore, even if the δ 1 phase slag core grows, the δ 1 phase slag does not easily grow earlier than the Γ 2 phase. Therefore, it is considered that it is better to perform the hot-dip galvanizing treatment on the growth area of the δ 1 phase than the growth area of the Γ 2 phase slag during the hot-dip galvanizing treatment step (operation period).
因此,本發明人等針對熔融鍍鋅浴之溫度T(℃)、熔融鍍鋅浴之游離Al濃度CAl (質量%)與生成之碎渣狀態進一步進行調查及檢討。其結果,本發明人等作成圖1所示之熔融鍍鋅浴中之碎渣準安定狀態圖。以下針對圖1加以說明。Therefore, the inventors further investigated and reviewed the temperature T (° C.) of the hot-dip galvanizing bath, the free Al concentration C Al (mass %) of the hot-dip galvanizing bath, and the state of the generated slag. As a result, the present inventors prepared a quasi-stable state diagram of slag in the hot-dip galvanizing bath shown in FIG. 1. The following describes FIG. 1.
圖1之縱軸表示熔融鍍鋅浴之游離Al濃度CAl (質量%)。本文中,本說明書中所謂「熔融鍍鋅浴之游離Al濃度CAl 」意指熔融鍍鋅浴中熔融之游離Al濃度(質量%)。亦即,本說明書中,所謂「熔融鍍鋅浴之游離Al濃度CAl 」意指碎渣(浮渣及底渣)中所含之Al含量除外,於熔融鍍鋅浴中熔融(亦即液相中)之游離Al濃度(質量%)。圖1之橫軸表示熔融鍍鋅浴中之浴溫T(℃)。The vertical axis of FIG. 1 represents the free Al concentration C Al (mass %) of the hot-dip galvanizing bath. Herein, the "free Al concentration C Al "of the hot dip galvanizing bath in this specification means the free Al concentration (mass %) melted in the hot dip galvanizing bath. That is, in this specification, the so-called "free Al concentration C Al of the hot-dip galvanizing bath" means that the Al content contained in the slag (scum and bottom slag) is not included, and is melted in the hot-dip galvanizing bath (that is, liquid Phase) free Al concentration (mass%). The horizontal axis of Fig. 1 represents the bath temperature T (°C) in the hot-dip galvanizing bath.
參考圖1,於圖1所示之游離Al濃度CAl
範圍與浴溫T(℃)中,熔融鍍鋅浴中存在生成浮渣之區域1A(以下稱為浮渣生成區域1A)、生成Γ2
相碎渣之區域2(以下稱為Γ2
相生成區域2)、及生成δ1
相碎渣之區域3(以下稱為δ1
相生成區域3)。Referring to FIG. 1, in the range of free Al concentration C Al shown in FIG. 1 and bath temperature T (° C.), there is a region 1A (hereinafter referred to as a scum generation region 1A) where dross is generated in the hot-dip galvanizing bath, and Γ is generated
浮渣生成區域1A與Γ2
相生成區域2由變態線F12
區分。浮渣生成區域1A與δ1
相生成區域3由變態線F13
區分。Γ2
相生成區域2與δ1
相生成區域3由變態線F23
區分。The scum generation region 1A and the Γ 2
例如浴溫T為440℃,游離Al濃度CAl
為0.135 %之熔融鍍鋅浴中生成Γ2
相碎渣。假定於該熔融鍍鋅浴之游離Al濃度CAl
仍維持為0.135%,而將浴溫T自440℃上升至470℃之情況。該情況下,熔融鍍鋅浴之狀態自Γ2
相生成區域2超過變態線F23
,移至δ1
相生成區域3。因此,熔融鍍鋅浴中之Γ2
相碎渣進行相變態成為δ1
相碎渣。又,假定浴溫T為440℃,且游離Al濃度CAl
為0.135%之熔融鍍鋅浴中之游離Al濃度CAl
提高至0.140%之情況。該情況下,熔融鍍鋅浴之狀態自Γ2
相生成區域2超過變態線F12
,移至浮渣生成區域1A。因此,熔融鍍鋅浴中之Γ2
相碎渣進行相變態成為浮渣。For example, a Γ 2 phase slag is generated in a hot-dip galvanizing bath with a bath temperature T of 440°C and a free Al concentration of C Al of 0.135%. Assuming that the free Al concentration C Al in the hot-dip galvanizing bath is still maintained at 0.135%, and the bath temperature T is increased from 440°C to 470°C. In this case, the state of the hot dip galvanizing bath moves from the Γ 2
本發明人等進而發現圖1所示之準安定狀態圖之Γ2
相生成區域2中,存在有區分Γ2
核生成區域21與Γ2
粒成長區域22之邊界線F2122
。本發明人等進而發現圖1所示之準安定狀態圖之δ1
相生成區域3中,存在有區分δ1
核生成區域31與δ1
粒成長區域32之邊界線F3132
。以下,針對此點進行說明。The inventors further found that in the Γ 2
Γ2
相生成區域2中,Γ2
核生成區域21比Γ2
粒成長區域22更位於邊界線F2122
之低溫側。Γ2
核生成區域21與Γ2
粒成長區域22相比,促進熔融鍍鋅浴中Γ2
相碎渣之核生成。亦即,促進微細Γ2
相碎渣之生成。另一方面,Γ2
粒成長區域22與Γ2
核生成區域21相比,促進熔融鍍鋅浴中已存在之Γ2
相之成長(粒成長)。In the Γ 2
同樣,於δ1
相生成區域3中,δ1
核生成區域31比δ1
粒成長區域32更位於邊界線F3132
之高溫側。δ1
核生成區域31與δ1
粒成長區域32相比,促進熔融鍍鋅浴中δ1
相碎渣之核生成。亦即,促進微細δ1
相碎渣之生成。另一方面,δ1
粒成長區域32與δ1
核生成區域31相比,促進熔融鍍鋅浴中已存在之δ1
相之成長(粒成長)。Similarly, in the δ 1
準安定狀態圖中之變態線F23 可藉下述式(A)定義。 再者,邊界線F2122 可藉下述式(B)定義。 再者,邊界線F3132 可藉下述式(C)定義。 此處,式(A)~式(C)中之「CAl 」係代入熔融鍍鋅浴中之游離Al濃度CAl (質量%)。The abnormal line F 23 in the quasi-stability state diagram can be defined by the following formula (A). Furthermore, the boundary line F 2122 can be defined by the following formula (B). Furthermore, the boundary line F 3132 can be defined by the following formula (C). Here, “C Al ”in formulas (A) to (C) is the free Al concentration C Al (mass %) substituted into the hot-dip galvanizing bath.
本發明人等基於圖1之準安定狀態圖,針對可抑制碎渣缺陷之熔融鍍鋅處理方法進行檢討。如上述,碎渣缺陷起因於粒徑100~未達300μm之中型底渣。於實施熔融鍍鋅處理之期間中(運轉期間中),為了抑制中型底渣之生成,只要將熔融鍍鋅浴之狀態成為如圖1中δ1 核生成區域31般調整熔融鍍鋅浴中游離Al濃度CAl 及浴溫T即可。δ1 核生成區域31中雖促進δ1 相碎渣之核生成,但抑制進δ1 相碎渣之成長。再者,如上述,底渣中,δ1 相碎渣之成長速度最慢。因此,若將運轉期間中之熔融鍍鋅浴作成δ1 核生成區域31,則可抑制底渣(此處為δ1 相碎渣)成長為中型底渣。Based on the quasi-stabilized state diagram of FIG. 1, the inventors of the present invention reviewed the hot-dip galvanizing treatment method that can suppress slag defects. As mentioned above, the slag defects are caused by medium-sized bottom slag with a particle size of 100 to less than 300 μm. During processing in the embodiment of the hot-dip galvanized (during the operation), to suppress the formation of bottom dross of medium, as long as the state of the hot-dip galvanizing bath of FIG. 31 become the molten galvanizing bath adjusted as free [delta] 1 1 nucleation region Al concentration C Al and bath temperature T are sufficient. [delta] 1 nucleation region 31, although promoting the nucleation of the slag phase [delta] 1, [delta] but inhibited the growth phase into the slag. Furthermore, as mentioned above, among the bottom slag, the growth rate of δ 1 phase crushed slag is the slowest. Therefore, if the hot-dip galvanizing bath during the operation is made into the δ 1 nucleus generation region 31, the growth of the bottom slag (here, the δ 1 phase crushed slag) can be suppressed to a medium-sized bottom slag.
然而,運轉期間中之熔融鍍鋅浴即使於δ1 核生成區域31維持,若熔融鍍鋅處理之實施期間(運轉期間)為長期間,則微細δ1 相碎渣亦某程度成長。因此,僅將運轉期間中之熔融鍍鋅浴設為δ1 核生成區域31,若運轉期間為長期間,則有生成中型底渣之可能性。However, even if the hot-dip galvanizing bath during the operation period is maintained in the δ 1 nucleus generation region 31, if the execution period (operation period) of the hot-dip galvanizing treatment is a long period, fine δ 1 phase slag will grow to some extent. Therefore, only the hot-dip galvanizing bath during the operation period is set as the δ 1 nucleus generation region 31. If the operation period is a long period, there is a possibility that medium-sized bottom dross is generated.
熔融鍍鋅浴中的中型底渣增加時,若實施自熔融鋅鍋去除底渣之作業(以下稱為底渣去除步驟),則可抑制碎渣缺陷之發生。然而,實施底渣去除步驟時,必須停止熔融鍍鋅處理,停止連續熔融鍍鋅產線設備。如此停止熔融鍍鋅處理之狀態,於本說明書中稱為「停機」。採用上述之底渣去除步驟時,底渣去除步驟之頻度若變高,則生產效率降低。When the medium-sized bottom slag in the hot-dip galvanizing bath is increased, if the bottom slag is removed from the molten zinc pot (hereinafter referred to as bottom slag removal step), the occurrence of chipping defects can be suppressed. However, when the bottom dross removal step is carried out, it is necessary to stop the hot-dip galvanizing process and stop the continuous hot-dip galvanizing production line equipment. The state where the hot-dip galvanizing treatment is stopped in this way is called "stop" in this manual. When the above-mentioned bottom slag removal step is adopted, if the frequency of the bottom slag removal step becomes higher, the production efficiency decreases.
因此,本發明人等針對以底渣操作實施熔融鍍鋅處理之情況下,抑制底渣去除步驟之頻度而可充分抑止碎渣缺陷之方法進一步檢討。其結果,本發明人等發現於熔融鍍鋅浴中,刻意預先含有粒徑300μm以上之粗大底渣後,於δ1 核生成區域31實施熔融鍍鋅處理,而於長期間內可抑制中型底渣之生成。以下針對該點進行說明。Therefore, the present inventors further reviewed a method for suppressing the frequency of the bottom dross removal step and sufficiently suppressing the dross defects when the hot galvanizing treatment is performed by the bottom slag operation. As a result, the present inventors found that in a hot-dip galvanizing bath, after intentionally containing coarse bottom slag with a particle size of 300 μm or more in advance, hot-dip galvanizing treatment is performed in the δ 1 nucleus generation region 31, and the medium-sized bottom can be suppressed for a long period of time Slag generation. This point will be described below.
底渣處於某程度大小時,因奧斯瓦爾得成長而成長。所謂奧斯瓦爾得成長係於母相中(本說明書中為液相之Zn)存在粒徑不同之同種金屬粒子時,粒徑較小之金屬粒子收縮或消滅,粒徑較大之金屬粒子進一步成長至粗大之現象。When the bottom slag is at a certain size, Osvald grows and grows. The so-called Osvaldian growth is that when the same type of metal particles with different particle sizes exist in the parent phase (Zn in the liquid phase in this specification), the metal particles with smaller particle sizes shrink or disappear, and the metal particles with larger particle sizes further The phenomenon of growing to coarseness.
本實施形態中,實施熔融鍍鋅處理之前的熔融鍍鋅浴中預先含有粒徑為300μm以上之粗大底渣。而且,使用含有粗大底渣之熔融鍍鋅浴,於δ1 核生成區域31實施熔融鍍鋅處理。該情況,於熔融鍍鋅處理之實施期間中,雖核生成δ1 相碎渣,但核生成之δ1 相碎渣收縮或消滅,被粗大底渣(該情況為粗大δ1 相碎渣)吸收。亦即,使用預先含有粗大底渣之熔融鍍鋅浴時,微細δ1 相碎渣藉由奧斯瓦爾德成長,而被粗大底渣(粗大δ1 相碎渣)吸收。粗大底渣進而成長,亦使粗大底渣質量增大,故不易因伴隨流而揚起。該方法之情況下,即使熔融鍍鋅處理之實施期間變長,亦可抑制微細δ1 相碎渣之生成。因此,進一步抑制中型底渣之生成。其結果,即使運轉期間為長期間,亦可抑制發生碎渣缺陷。In the present embodiment, the hot-dip galvanizing bath before the hot-dip galvanizing treatment contains a coarse bottom slag having a particle diameter of 300 μm or more in advance. Then, a hot-dip galvanizing bath containing coarse bottom dross is used to perform hot-dip galvanizing treatment on the delta 1 nucleus generation area 31. In this case, during the implementation of the hot-dip galvanizing process, although the nucleus generated δ 1 phase slag, the nucleated δ 1 phase slag shrank or disappeared, and it was coarse bottom slag (in this case, the coarse δ 1 phase slag) absorb. That is, when a hot-dip galvanizing bath containing a coarse bottom slag is used in advance, the fine δ 1 phase crushed slag grows by Oswald and is absorbed by the coarse bottom slag (coarse δ 1 phase crushed slag). The growth of the coarse bottom slag also increases the quality of the coarse bottom slag, so it is not easy to rise due to the accompanying flow. In the case of this method, even if the implementation period of the hot-dip galvanizing treatment becomes longer, the generation of fine δ 1 phase slag can be suppressed. Therefore, the formation of medium-sized bottom slag is further suppressed. As a result, even if the operation period is a long period, the occurrence of chipping defects can be suppressed.
簡言之,本實施形態中,預先於熔融鍍鋅浴中含有粗大底渣後,於δ1 核生成區域31實施熔融鍍鋅處理。該情況,藉由奧斯瓦爾德成長而使粗大底渣進一步成長,而不僅抑制微細底渣(微細δ1 相碎渣)的成長亦抑制生成。其結果可有效抑制成為碎渣缺陷要因之中型底渣之生成。In short, in this embodiment, after the coarse bottom slag is contained in the hot-dip galvanizing bath in advance, the hot-dip galvanizing treatment is performed in the δ 1 core generation region 31. In this case, the coarse bottom slag is further grown by the growth of Oswald, which not only suppresses the growth of fine bottom slag (fine δ 1 phase crushed slag) but also suppresses the generation. As a result, it is possible to effectively suppress the formation of medium-sized bottom slag which is the cause of chipping defects.
如以上,本實施形態之熔融鍍鋅鋼板之製造方法意指以刻意於熔融鍍鋅浴中包含於過去認為應去除之對象的粗大底渣之狀態進行熔融鍍鋅處理,係基於與以往全然不同之技術思想而完成者。具體而言,本實施形態之熔融鍍鋅鋼板之製造方法係如下。As described above, the manufacturing method of the hot-dip galvanized steel sheet of the present embodiment means that the hot-dip galvanizing treatment is carried out in a state where the coarse bottom slag contained in the hot-dip galvanizing bath is included in the object that should be removed in the past, and it is based on a completely different from the past The technical thought is completed. Specifically, the manufacturing method of the hot dip galvanized steel sheet of this embodiment is as follows.
[1]一種熔融鍍鋅鋼板之製造方法,其具備下述步驟: 以滿足式(1)之方式調整熔融鍍鋅浴中之游離Al濃度CAl 及浴溫T,於前述熔融鍍鋅浴中生成粒徑為300μm以上之粗大底渣之粗大底渣生成步驟,及 將前述粗大底渣生成步驟後之前述熔融鍍鋅浴之前述游離Al濃度CAl 及前述浴溫T調整為滿足式(2),使用前述游離Al濃度CAl 及前述浴溫T滿足式(2)之前述熔融鍍鋅浴,實施熔融鍍鋅處理,於鋼板形成熔融鍍鋅層之熔融鍍鋅處理步驟, [1] A method for manufacturing a hot-dip galvanized steel sheet, comprising the following steps: adjusting the free Al concentration in the hot-dip galvanizing bath C Al and the bath temperature T in a manner satisfying the formula (1) in the aforementioned hot-dip galvanizing bath A coarse bottom slag generation step that generates a coarse bottom slag having a particle size of 300 μm or more, and the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath after the coarse bottom slag generation step are adjusted to satisfy equation (2) ), using the above-mentioned free Al concentration C Al and the above bath temperature T satisfying the above-mentioned hot-dip galvanizing bath of formula (2), performing hot-dip galvanizing treatment, forming a hot-dip galvanizing layer on the steel sheet, a hot-dip galvanizing treatment step,
[2]之熔融鍍鋅鋼板之製造方法係[1]記載之熔融鍍鋅鋼板之製造方法,其中於停止實施前述熔融鍍鋅處理步驟之停機時,對前述熔融鍍鋅處理步驟後之前述熔融鍍鋅浴實施前述粗大底渣生成步驟。[2] The method of manufacturing the hot-dip galvanized steel sheet is the method of manufacturing the hot-dip galvanized steel sheet described in [1], wherein when the shutdown of the hot-dip galvanizing treatment step is stopped, the melting after the hot-dip galvanizing treatment step is performed. The galvanizing bath performs the aforementioned coarse bottom slag generation step.
[3]之熔融鍍鋅鋼板之製造方法係[1]或[2]記載之熔融鍍鋅鋼板之製造方法,其中於前述熔融鍍鋅處理步驟,使前述粗大底渣生成步驟後之前述熔融鍍鋅浴之前述浴溫T上升,作成滿足式(2)之前述熔融鍍鋅浴。[3] The method of manufacturing a hot-dip galvanized steel sheet is the method of manufacturing a hot-dip galvanized steel sheet according to [1] or [2], wherein in the hot-dip galvanizing treatment step, the hot-dip plating after the coarse bottom dross generating step The aforementioned bath temperature T of the zinc bath is increased to prepare the aforementioned hot-dip galvanizing bath satisfying the formula (2).
[4]之熔融鍍鋅鋼板之製造方法係[3]記載之熔融鍍鋅鋼板之製造方法,其中進而交替重複實施前述粗大底渣生成步驟及前述熔融鍍鋅處理步驟, 於前述熔融鍍鋅處理步驟後,實施前述粗大底渣生成步驟時,於前述粗大底渣步驟,使前述熔融鍍鋅處理步驟後之前述熔融鍍鋅浴之前述浴溫T下降,作成滿足式(1)之前述熔融鍍鋅浴。[4] The method of manufacturing the hot-dip galvanized steel sheet is the method of manufacturing the hot-dip galvanized steel sheet described in [3], wherein the coarse bottom slag generation step and the hot-dip galvanizing treatment step are alternately repeated. After the hot galvanizing treatment step, when performing the coarse bottom slag generation step, in the coarse bottom slag step, the bath temperature T of the hot galvanizing bath after the hot galvanizing treatment step is reduced to satisfy the formula ( 1) The aforementioned hot-dip galvanizing bath.
[5]之熔融鍍鋅鋼板之製造方法係[1]~[4]中任一項記載之熔融鍍鋅鋼板之製造方法,其中前述粗大底渣生成步驟及前述熔融鍍鋅處理步驟之前述熔融鍍鋅浴中之前述游離Al濃度CAl 為0.125質量%以上。[5] The manufacturing method of the hot-dip galvanized steel sheet is the manufacturing method of the hot-dip galvanized steel sheet according to any one of [1] to [4], wherein the melting of the coarse bottom slag generation step and the hot-dip galvanizing treatment step The aforementioned free Al concentration C Al in the galvanizing bath is 0.125% by mass or more.
[6]之熔融鍍鋅鋼板之製造方法係[5]記載之熔融鍍鋅鋼板之製造方法,其中前述粗大底渣生成步驟及前述熔融鍍鋅處理步驟之前述熔融鍍鋅浴中之前述游離Al濃度CAl 為0.138質量%以下。[6] The method for manufacturing hot-dip galvanized steel sheet is the method for manufacturing hot-dip galvanized steel sheet according to [5], wherein the free Al in the hot-dip galvanizing bath in the coarse bottom slag generation step and the hot-dip galvanizing treatment step The concentration C Al is 0.138% by mass or less.
[7]之熔融鍍鋅鋼板之製造方法係[1]~[6]中任一項記載之熔融鍍鋅鋼板之製造方法,其中進而於實施前述粗大底渣生成步驟之前,具備將前述熔融鍍鋅浴中之前述粗大底渣之至少一部分去除之底渣去除步驟。[7] The method for manufacturing hot-dip galvanized steel sheet is the method for manufacturing hot-dip galvanized steel sheet as described in any one of [1] to [6], further comprising performing the above-mentioned hot-dip plating The bottom slag removing step of removing at least a part of the aforementioned coarse bottom slag in the zinc bath.
[8]之合金化熔融鍍鋅鋼板之製造方法,係具備下述步驟: 實施如[1]至[7]中任一項記載之前述熔融鍍鋅鋼板之製造方法,製造前述熔融鍍鋅鋼板之步驟,及 對前述熔融鍍鋅鋼板實施合金化處理之合金化處理步驟。[8] The manufacturing method of alloyed hot-dip galvanized steel sheet includes the following steps: Implementing the method of manufacturing the aforementioned hot-dip galvanized steel sheet as described in any one of [1] to [7], the steps of manufacturing the aforementioned hot-dip galvanized steel sheet, and The alloying step of alloying the aforementioned hot-dip galvanized steel sheet.
以下邊參考所附圖式邊針對本發明之較佳實施形態詳細說明。The preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
[熔融鍍鋅產線設備之構成]
圖2顯示熔融鍍鋅鋼板及合金化熔融鍍鋅鋼板之製造中所用之熔融鍍鋅產線設備之全體構成之一例的功能方塊圖。參考圖2,熔融鍍鋅產線設備1具備燒鈍爐20、熔融鍍鋅設備10及調質壓延機(平整機)35。[Composition of equipment for hot-dip galvanizing line]
FIG. 2 is a functional block diagram showing an example of the overall configuration of a hot-dip galvanized steel sheet and an alloyed hot-dip galvanized steel sheet used in the manufacture of hot-dip galvanized steel production lines. Referring to FIG. 2, the hot-dip galvanizing
燒鈍爐20包含未圖示之1或複數個加熱帶及配置於加熱帶下游之1或複數個冷卻帶。於燒鈍爐20,將鋼板供給至燒鈍爐20之加熱帶,對鋼板實施燒鈍。經燒鈍之鋼板以冷卻帶予以冷卻,搬送至熔融鍍鋅設備10。熔融鍍鋅設備10配置於燒鈍爐20之下游。於熔融鍍鋅設備10,對鋼板實施熔融鍍鋅處理,製造合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板。調質壓延機35配置於熔融鍍鋅設備10之下游。於調質壓延機35,對於在熔融鍍鋅設備10中製造之合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板,根據需要進行輕壓力下,調整合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板之表面。The
[關於熔融鍍鋅設備10]
圖3係圖1中之熔融鍍鋅設備10之側視圖。參考圖3,熔融鍍鋅設備10具備例如熔融鋅鍋101、沉降輥107、支撐輥113、氣體吹掃裝置109及合金化爐111。[About hot-dip galvanizing equipment 10]
FIG. 3 is a side view of the hot-
設於熔融鍍鋅設備10前段之燒鈍爐20係內部維持於還原性環境。於燒鈍爐20,加熱所連續搬送之鋼板S。藉由燒鈍爐20加熱鋼板S,使鋼板S表面活化,調整鋼板S之機械性質。相當於燒鈍爐20之輸出側之燒鈍爐20之下游端部具有配置翻轉輥30之空間。燒鈍爐20之下游端部連接於噴嘴部105之上游端部。噴嘴部105之下游端部浸漬於熔融鍍鋅浴103中。噴嘴部105之內部與大氣環境遮斷,維持於還原性環境。The
藉由翻轉輥30將搬送方向改變為向下之鋼板S通過噴嘴部105,朝儲存於熔融鋅鍋101中之熔融鍍鋅浴103中連續浸漬。於熔融鋅鍋101之內部配置沉降輥107。沉降輥107具有與鋼板S之寬度方向平行之旋轉軸。沉降輥107之軸向寬度大於鋼板S之寬度。沉降輥107與鋼板S接觸將鋼板S之行進方向轉換至熔融鍍鋅設備10之上方。The steel plate S whose conveying direction is changed downward by the reversing
支撐輥113係習知構件。支撐輥113係於熔融鍍鋅浴103中,配置於較沉降輥107更上方。支撐輥113具備一對輥。支撐輥113之一對輥具有與鋼板S之寬度方向平行之旋轉軸。支撐輥113挾住藉由沉降輥107將行進方向轉換為上方之鋼板S,而支撐向上方搬送之鋼板S。The
氣體吹掃裝置109配置於較沉降輥107及支撐輥113更上方,且較熔融鍍鋅浴103之液面更上方。氣體吹掃裝置109具備一對氣體噴射裝置。一對氣體噴射裝置具有相互對抗之氣體噴射噴嘴。熔融鍍鋅處理時,鋼板S通過氣體吹掃裝置109之一對氣體噴射噴嘴之間。此時,一對氣體噴射噴嘴與鋼板S表面對向。氣體吹掃裝置109對於自熔融鍍鋅浴103拉起之鋼板S兩表面吹附氣體。藉此,氣體吹掃裝置109將附著於鋼板S之兩表面之熔融鍍鋅浴之一部分刮落,調整鋼板S表面之熔融鍍鋅附著量。The
合金化爐111配置於氣體吹掃裝置109之上方。合金化爐111使通過氣體吹掃裝置109而向上方搬送之鋼板S通過內部,對於鋼板S實施合金化處理。合金化爐111依自鋼板S之輸入側朝向輸出側之順序,包含加熱帶、保熱帶、冷卻帶。加熱帶以使鋼板S之溫度(板溫)略為均一之方式進行加熱。保熱帶保持鋼板S之板溫。此時,使形成於鋼板S表面之熔融鍍鋅層合金化而成為合金化熔融鍍鋅層。冷卻帶將形成有合金化熔融鍍鋅層之鋼板S冷卻。如以上,合金化爐111使用加熱帶、保熱帶、冷卻帶,實施合金化處理。又,合金化爐111於製造合金化熔融鍍鋅鋼板時,實施上述合金化處理。另一方面,製造熔融鍍鋅鋼板時,合金化爐111未實施合金化處理。該情況下,鋼板S通過未作動之合金化爐111內。此處,所謂未作動意指例如以合金化爐111配置於產線上直接停止電源之狀態(未啟動之狀態)。通過合金化爐111之鋼板S藉由頂輥40搬送至下一步驟。The alloying
製造熔融鍍鋅鋼板時,如圖4所示,合金化爐111亦可移動至離線。該情況下,鋼板S並未通過合金化爐111,而藉由頂輥40搬送至下一步驟。When manufacturing a hot-dip galvanized steel sheet, as shown in FIG. 4, the alloying
又,熔融鍍鋅設備10係熔融鍍鋅鋼板專用設備之情況下,如圖5所示,熔融鍍鋅設備10亦可不具備合金化爐111。In addition, when the hot-
[關於熔融鍍鋅產線設備之其他構成例]
熔融鍍鋅產線設備1並未限定於圖2之構成。例如對熔融鍍鋅處理前之鋼板實施預鍍Ni處理,於鋼板上形成Ni層之情況,如圖6所示,於燒鈍爐20與熔融鍍鋅設備10之間,亦可配置預鍍Ni設備45。預鍍Ni設備45具備儲存鍍Ni浴之鍍Ni單元。預鍍Ni處理係藉由電鍍法實施。又,圖2及圖6之熔融鍍鋅產線設備1具備燒鈍爐20及調質壓延機35。然而,熔融鍍鋅產線設備1亦可不具備燒鈍爐20。又,熔融鍍鋅產線設備1亦可不具備調質壓延機35。熔融鍍鋅產線設備1只要至少具備熔融鍍鋅設備10即可。燒鈍爐20及調質壓延機35只要根據需要配置即可。又,熔融鍍鋅產線設備1亦可於較熔融鍍鋅設備10更上游具備用以酸洗鋼板之酸洗設備,亦可具備燒鈍爐20及酸洗設備以外之其他設備。熔融鍍鋅產線設備1亦可進而於較熔融鍍鋅設備10更下游具備調質壓延機35以外之其他設備。[About other configuration examples of hot-dip galvanizing production line equipment]
The hot-
[關於本實施形態之熔融鍍鋅鋼板之製造方法]
[關於所利用之熔融鍍鋅產線中之設備]
本實施形態之熔融鍍鋅處理方法係使用熔融鍍鋅產線設備1。熔融鍍鋅產線設備1具有例如圖2或圖6所示之構成。本實施形態之熔融鍍鋅處理方法所用之熔融鍍鋅產線設備1,如上述可為圖2或圖6所示之設備,亦可為於圖2或圖6所示之設備中進而追加其他構成者。又,如上述,熔融鍍鋅產線設備1亦可不具備燒鈍爐20。又,熔融鍍鋅產線設備1亦可不具備調質壓延機35。熔融鍍鋅產線設備1只要至少具備熔融鍍鋅設備10即可。亦可使用與圖2或圖6不同構成之習知熔融鍍鋅產線設備1。[About the manufacturing method of the hot dip galvanized steel sheet of this embodiment]
[About the equipment used in the hot-dip galvanizing line]
The hot dip galvanizing treatment method of this embodiment uses the hot dip galvanizing
[關於成為熔融鍍鋅處理對象之鋼板] 本實施形態之熔融鍍鋅處理方法所用之鋼板(母材鋼板)之鋼種及尺寸(板厚、板寬等)並未特別限定。鋼板係對應於所製造之合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板所要求之各機械性質(例如拉伸強度、加工性等),利用適用於合金化熔融鍍鋅鋼板或熔融鍍鋅鋼板之習知鋼板即可。汽車外板所用之鋼板亦可利用作為熔融鍍鋅處理對象之鋼板。成為本實施形態之熔融鍍鋅處理對象之鋼板(母材鋼板)可為熱軋鋼板,亦可為冷軋鋼板。[About steel sheets subject to hot dip galvanizing] The steel type and size (plate thickness, plate width, etc.) of the steel plate (base material steel plate) used in the hot dip galvanizing treatment method of this embodiment are not particularly limited. The steel sheet corresponds to the required mechanical properties (such as tensile strength, workability, etc.) of the alloyed hot-dip galvanized steel sheet or hot-dip galvanized steel sheet, and is suitable for alloyed hot-dip galvanized steel sheet or hot-dip galvanized steel sheet. Knowing the steel plate is enough. The steel plate used for the automobile outer plate can also be used as the steel plate subject to the hot-dip galvanizing treatment. The steel sheet (base metal steel sheet) to be subjected to the hot-dip galvanizing treatment of the present embodiment may be a hot-rolled steel sheet or a cold-rolled steel sheet.
[關於熔融鍍鋅浴] 熔融鍍鋅浴之主成分為Zn。熔融鍍鋅浴除了Zn以外,進而含有Al。亦即,本實施形態之熔融鍍鋅處理方法所利用之熔融鍍鋅浴係含有特定濃度之Al,其餘部分係由Zn及雜質所成之鍍液。雜質例如為Fe。熔融鍍鋅浴若含有特定濃度之Al,則可抑制浴中之Fe與Zn之過度反應。其結果,可抑制浸漬於熔融鍍鋅浴之鋼板與Zn之不均一合金反應之進行。[About hot-dip galvanizing bath] The main component of the hot dip galvanizing bath is Zn. The hot dip galvanizing bath contains Al in addition to Zn. That is, the hot-dip galvanizing bath used in the hot-dip galvanizing method of this embodiment contains a specific concentration of Al, and the rest is a plating solution made of Zn and impurities. The impurity is Fe, for example. If the hot-dip galvanizing bath contains Al at a specific concentration, the excessive reaction of Fe and Zn in the bath can be suppressed. As a result, it is possible to suppress the reaction of the non-uniform alloy of the steel sheet immersed in the hot-dip galvanizing bath and Zn.
如圖1所示,游離Al濃度CAl 之較佳下限為0.125%。游離Al濃度CAl 若為0.125質量%以上,則於合金化處理中,可抑制熔融鍍鋅層之合金化過度進行。因此,可抑制因過度合金化所致之合金化熔融鍍鋅層之脆化。其結果,提高合金化熔融鍍鋅層對鋼板之密著性。游離Al濃度CAl 之進而較佳下限為0.127%,又更佳為0.129%,再更佳為0.130%。As shown in Figure 1, the preferred lower limit of the free Al concentration C Al is 0.125%. If the free Al concentration C Al is 0.125% by mass or more, the alloying treatment can suppress excessive alloying of the hot-dip galvanized layer. Therefore, the embrittlement of the alloyed hot-dip galvanized layer due to over-alloying can be suppressed. As a result, the adhesion of the alloyed hot-dip galvanized layer to the steel sheet is improved. The further preferred lower limit of the free Al concentration C Al is 0.127%, more preferably 0.129%, and even more preferably 0.130%.
游離Al濃度CAl 之較佳上限為0.138質量%以下。該情況下,進而有效實施合金化,充分形成合金化熔融鍍鋅層。游離Al濃度CAl 之進而較佳上限為0.137%,又更佳為0.136%,再更佳為0.135%。The preferable upper limit of the free Al concentration C Al is 0.138% by mass or less. In this case, alloying is further effectively performed to fully form an alloyed hot-dip galvanized layer. The further preferred upper limit of the free Al concentration C Al is 0.137%, more preferably 0.136%, and even more preferably 0.135%.
熔融鍍鋅浴103中之游離Fe濃度並未特別限定。游離Fe濃度例如以質量%計,為0.020~0.060%。熔融鍍鋅浴103中之Fe可為自鋼板S溶出者,亦可為因其他理由而於熔融鍍鋅浴103中含有者。熔融鍍鋅浴103亦可含有Fe以外之其他雜質。此處所謂雜質意指因原料其他要因而混入之成分,而容許為對本實施形態之製造方法不會造成不良影響之範圍者。The free Fe concentration in the hot
[熔融鍍鋅浴103中之游離Al濃度及游離Fe濃度之測定方法]
熔融鍍鋅浴103中之游離Al濃度及游離Fe濃度之決定方法並未特別限定。例如基於感應耦合電漿(ICP:Inductively Coupled Plasma)發光分光分析法所得之Al濃度及Fe濃度,求出游離Al濃度CAl
(質量%)及游離Fe濃度(質量%)。[Measurement method of free Al concentration and free Fe concentration in the hot-dip galvanizing bath 103] The method of determining the free Al concentration and free Fe concentration in the hot-
具體而言,自熔融鍍鋅浴103採取樣本。將樣本急冷而固化。使用經固化之樣本,藉由ICP發光分光分析法獲得Al濃度及Fe濃度。藉由ICP發光分光分析法獲得之Al濃度不僅為熔融鍍鋅浴中之游離Al濃度,亦包含碎渣中之Al濃度。亦即,藉由ICP發光分光分析法獲得之Al濃度係所謂之總Al濃度。同樣地藉由上述ICP發光分光分析法獲得之Fe濃度不僅為熔融鍍鋅浴中之游離Fe濃度,亦包含碎渣中之Fe濃度。亦即,藉由ICP發光分光分析法所得之Fe濃度係所謂之總Fe濃度。因此,所得總Al濃度及總Fe濃度係使用周知之Zn-Fe-Al三元系狀態圖,決定游離Al濃度CAl
及游離Fe濃度。Specifically, a sample is taken from the hot-
游離Al濃度CAl
及游離Fe濃度之決定方法如下。準備於採取樣本時之浴溫T下之Zn-Fe-Al三元系狀態圖。如上述,Zn-Fe-Al三元系狀態圖係周知,亦揭示於非專利文獻1中之圖2及圖3。又,非專利文獻1係熔融鍍鋅浴之研究者及開發者間之著名論文。Zn-Fe-Al三元系狀態圖中,自藉由ICP發光分光分析法所得之總Al濃度及總Fe濃度所特定出之點進行作圖。接著,自所作圖之點於Zn-Fe-Al三元系狀態圖之液相線中畫出連結線(共軛線)。液相線與連結線之交點的Al濃度定義為游離Al濃度CAl
,液相線與連結線之交點的Fe濃度定義為游離Fe濃度。The method of determining the free Al concentration C Al and free Fe concentration is as follows. Prepare a state diagram of the Zn-Fe-Al ternary system at the bath temperature T at the time the sample is taken. As described above, the state diagram of the Zn-Fe-Al ternary system is well known and is also disclosed in FIGS. 2 and 3 of
藉由上述方法,可求出熔融鍍鋅浴中之游離Al濃度CAl 及熔融鍍鋅浴中之游離Fe濃度。又,熔融鍍鋅浴之化學組成中,游離Al濃度CAl 及游離Fe濃度以外之其餘部分可視為Zn。By the above method, the free Al concentration C Al in the hot-dip galvanizing bath and the free Fe concentration in the hot-dip galvanizing bath can be determined. In addition, in the chemical composition of the hot-dip galvanizing bath, the rest other than the free Al concentration C Al and the free Fe concentration can be regarded as Zn.
[關於本實施形態之熔融鍍鋅鋼板之製造方法] 本實施形態之熔融鍍鋅鋼板之製造方法包含粗大底渣生成步驟(S1)及熔融鍍鋅處理步驟(S2)。以下針對各步驟進行說明。[About the manufacturing method of the hot dip galvanized steel sheet of this embodiment] The manufacturing method of the hot dip galvanized steel sheet of this embodiment includes a coarse bottom slag generation step (S1) and a hot dip galvanizing treatment step (S2). The following describes each step.
[粗大底渣生成步驟(S1)] 粗大底渣生成步驟(S1)係於未實施熔融鍍鋅處理之期間實施。亦即,粗大底渣生成步驟(S1)係例如鋼板不通過熔融鍍鋅設備,於使熔融鍍鋅產線設備停止之期間(停機時間)實施。[Procedure for generating coarse bottom slag (S1)] The coarse bottom slag generation step (S1) is carried out while the hot-dip galvanizing treatment is not performed. That is, the coarse bottom dross generation step (S1) is implemented, for example, while the steel sheet does not pass through the hot-dip galvanizing equipment, while the hot-dip galvanizing production line equipment is stopped (downtime).
粗大底渣生成步驟(S1)中,以滿足式(1)之方式調整熔融鍍鋅浴中之游離Al濃度CAl
及浴溫T,於熔融鍍鋅浴中生成粒徑300μm以上之粗大底渣。
其中,式(1)中之「CAl
」係代入熔融鍍鋅浴103中之游離Al濃度CAl
(質量%)。In the step of generating coarse bottom dross (S1), the free Al concentration C Al and the bath temperature T in the hot-dip galvanizing bath are adjusted in such a way as to satisfy the formula (1), and a coarse bottom dross with a particle size of 300 μm or more is generated in the hot-dip galvanizing bath . Among them, “C Al ”in formula (1) is the free Al concentration C Al (mass %) substituted into the hot-
式(1)中之「466.15×CAl +385.14」相當於上述式(B)。亦即,466.15×CAl +385.14相當於圖1中邊界線F2122 。式(1)中之「577.24×CAl +382.49」相當於式(A)。亦即,577.24×CAl +382.49相當於圖1中變態線F23 。因此,式(1)意指圖1中之Γ2 粒成長區域22。"466.15×C Al +385.14" in formula (1) corresponds to the above formula (B). That is, 466.15×C Al +385.14 corresponds to the boundary line F 2122 in FIG. 1. "577.24×C Al +382.49" in equation (1) corresponds to equation (A). That is, 577.24×C Al +382.49 corresponds to the abnormal line F 23 in FIG. 1. Therefore, formula (1) means the Γ 2 grain growth region 22 in FIG. 1.
粗大底渣生成步驟(S1)中,調整熔融鍍鋅浴中之游離Al濃度CAl
及浴溫T,將熔融鍍鋅浴103之狀態保持於Γ2
粒成長區域22。此時,熔融鍍鋅浴103中生成之底渣為Γ2
相碎渣。如上述,Γ2
相碎渣於底渣中成長速度最快。再者,Γ2
粒成長區域22與Γ2
核生成區域21比較,更促進Γ2
相碎渣成長。因此,粗大底渣生成步驟(S1)中,粒徑為300μm以上之粗大底渣可於比較短期間生成。In the coarse bottom slag generation step (S1), the free Al concentration C Al in the hot-dip galvanizing bath and the bath temperature T are adjusted to maintain the state of the hot-
粗大底渣成長步驟中,以滿足式(1)之方式維持熔融鍍鋅浴103之期間並未特別限定。只要可生成粒徑為300μm以上之粗大底渣即可。又,若將不存在底渣而新建浴之熔融鍍鋅浴103於滿足式(1)之條件至少維持30天,則可確認生成粒徑為300μm以上之Γ2
相碎渣。因此,於粗大底渣成長步驟中,較好以滿足式(1)之方式將熔融鍍鋅浴103至少維持30天。進而較好於粗大底渣成長步驟中,以滿足式(1)之方式將熔融鍍鋅浴103至少維持60天,進而較好至少維持90天。In the step of growing the coarse bottom dross, the period during which the hot-
又,本說明書中,底渣粒徑係如下定義。參考圖7,於各底渣100中,將底渣100與母相200之界面(意即碎渣外周)150之任意2點予以連結之線段LS中,最大之線段LS定義為「粒徑」。粒徑可對於觀察視野之照片圖像使用圖像處理而求出。又,本說明書中,針對最長徑未達20μm之碎渣,由於對碎渣缺陷幾無影響,故設為對象外。In this specification, the bottom slag particle size is defined as follows. Referring to FIG. 7, in each
[熔融鍍鋅處理步驟(S2)]
熔融鍍鋅處理步驟(S2)係使用粗大底渣生成步驟(S1)後之熔融鍍鋅浴103,對鋼板實施熔融鍍鋅處理。具體而言,將鋼板通入於含粗大底渣之熔融鍍鋅浴103。此時,於鋼板表面形成熔融鍍鋅層。[Process of hot-dip galvanizing (S2)]
The hot-dip galvanizing treatment step (S2) uses the hot-
熔融鍍鋅處理步驟(S2)中,實施熔融鍍鋅處理之期間中(亦即運轉期間中),以滿足式(2)之方式調整熔融鍍鋅浴中之游離Al濃度CAl
及浴溫T。
其中,式(2)中之「CAl
」係代入熔融鍍鋅浴103中之游離Al濃度CAl
(質量%)。In the hot-dip galvanizing treatment step (S2), during the hot-dip galvanizing process (that is, during the operation period), the free Al concentration C Al and the bath temperature T in the hot-dip galvanizing bath are adjusted in a manner that satisfies formula (2) . Among them, “C Al ”in formula (2) is the free Al concentration C Al (mass %) substituted into the hot-
式(2)中之「390.91×CAl +414.20」相當於上述式(C)。亦即,390.91×CAl +414.20相當於圖1中邊界線F3132 。"390.91×C Al +414.20" in the formula (2) corresponds to the above formula (C). That is, 390.91×C Al +414.20 corresponds to the boundary line F 3132 in FIG. 1.
簡言之,於熔融鍍鋅處理步驟(S2),使粗大底渣生成步驟(S1)後之熔融鍍鋅浴103之浴溫T上升,將熔融鍍鋅浴103之狀態自Γ2
粒成長區域22移行至δ1
相核生成區域31。接著,將熔融鍍鋅浴103之狀態於δ1
相核生成區域31予以保持。此時,熔融鍍鋅浴103中之粗大底渣自Γ2
相相變態至δ1
相。相變態時,粗大底渣之一部分或全部並未溶解。亦即,自粗大底渣生成步驟(S1)移行至熔融鍍鋅處理步驟(S2)時,堆積於熔融鋅鍋101底部之粗大底渣,其粒徑及形狀並無太大變化,自Γ2
相相變態至δ1
相。In short, in the hot-dip galvanizing treatment step (S2), the bath temperature T of the hot-
如上述,於熔融鍍鋅處理步驟(S2),使熔融鍍鋅浴103之浴溫T上升,將熔融鍍鋅浴103之狀態自Γ2
粒成長區域22移行至δ1
核生成區域31。接著,將熔融鍍鋅浴103之狀態於δ1
核生成區域31予以保持。此時,於熔融鋅鍋101底部存在有自Γ2
相變態至δ1
相之粗大底渣。亦即於熔融鍍鋅處理步驟(S2),使用含粗大底渣之熔融鍍鋅浴103,實施熔融鍍鋅處理。As described above, in the hot-dip galvanizing treatment step (S2), the bath temperature T of the hot-
於熔融鍍鋅處理步驟(S2),實施熔融鍍鋅處理之期間中(亦即運轉期間中),熔融鍍鋅浴103之狀態為δ1
核生成區域31。因此,熔融鍍鋅處理步驟中,於熔融鍍鋅浴103中生成微細δ1
相碎渣。然而,於熔融鋅鍋101底部存在有粗大底渣。因此,藉由奧斯瓦爾德成長,微細δ1
相碎渣收縮或消滅,粗大底渣成長。亦即,於熔融鍍鋅處理步驟(S2),利用粗大底渣之奧斯瓦爾德成長,抑制微細底渣(微細δ1
相碎渣)之生成及成長。該情況下,微細δ1
相碎渣進一步減小,粗大底渣進一步變大。其結果,可抑制粒徑為100~300μm之中型底渣(δ1
相碎渣)之生成。又,熔融鍍鋅處理步驟(S2)之實施期間,粗大底渣進一步成長。然而,因粗大底渣之質量增大,故不易伴隨伴隨流而於熔融鍍鋅浴103中揚起。因此,粗大底渣附著於鋼板之可能性極低。In the hot-dip galvanizing process step (S2), during the hot-dip galvanizing process (that is, during the operation period), the state of the hot-
如此,於熔融鍍鋅處理步驟(S2),熔融鍍鋅處理中,即使生成微細底渣(δ1 相碎渣),藉由利用粗大底渣之奧斯瓦爾德成長,而有效抑制微細底渣成長為中型底渣。因此,可抑制於熔融鍍鋅鋼板或合金化熔融鍍鋅鋼板形成碎渣缺陷。In this way, in the hot-dip galvanizing treatment step (S2), even in the hot-dip galvanizing process, even if a fine bottom slag (δ 1 phase crushed slag) is generated, the fine bottom slag is effectively suppressed by using the Oswald growth of the coarse bottom slag Growing into a medium-sized bottom slag. Therefore, it is possible to suppress the formation of slag defects in the hot-dip galvanized steel sheet or the alloyed hot-dip galvanized steel sheet.
於上述熔融鍍鋅處理步驟(S2),即使長期間實施熔融鍍鋅處理,亦可有效抑制中型底渣之生成。因此,亦可不實施底渣去除步驟,且即使於實施底渣去除步驟之情況,亦可抑制實施之頻度。亦即,可抑制使熔融鍍鋅設備10停止之頻度(停機頻度)。因此,亦可提高生產效率。In the above hot-dip galvanizing treatment step (S2), even if hot-dip galvanizing treatment is performed for a long period of time, the formation of medium-sized bottom dross can be effectively suppressed. Therefore, the bottom dross removal step may not be performed, and even if the bottom dross removal step is performed, the frequency of implementation may be suppressed. That is, the frequency (stop frequency) of stopping the hot-
[粗大底渣生成步驟(S1)之實施時期]
本實施形態中,建浴新的熔融鍍鋅浴103時,於實施熔融鍍鋅處理步驟(S2)之前,實施粗大底渣生成步驟(S1)。[Implementation time of coarse bottom slag generation step (S1)]
In the present embodiment, when a new hot-
另一方面,長期間實施熔融鍍鋅處理步驟(S2)時,堆積於熔融鋅鍋101底部之粗大底渣過度成長,粗大底渣之堆積量變過多。該情況下,亦可自熔融鍍鋅設備10取出熔融鋅鍋101,實施粗大底渣去除步驟。於底渣去除步驟,去除熔融鍍鋅浴103中粗大底渣之至少一部分或全部。底渣去除方法只要藉習知方法實施即可。底渣去除步驟中例如將以吊車垂吊下之吊桶浸漬於熔融鋅鍋101內,以吊桶掏取底渣。隨後,自熔融鋅鍋101拉起吊桶,將以吊桶掏取之底渣取出至熔融鋅鍋101之外部。且,於熔融鋅鍋101內投入Al,藉由將底渣浮渣化,亦可去除底渣。On the other hand, when the hot-dip galvanizing step (S2) is performed for a long period of time, the coarse bottom slag deposited on the bottom of the
對於堆積於熔融鋅鍋101底部之底渣經去除之熔融鍍鋅浴103,實施粗大底渣生成步驟(S1)。藉此,於經浴調整之熔融鍍鋅浴103中,再度生成粗大底渣。接著,將包含粗大底渣且經浴調整之熔融鍍鋅浴103再度設置於熔融鍍鋅設備10中。隨後,實施熔融鍍鋅處理步驟(S2)。簡言之,粗大底渣生成步驟(S1)與熔融鍍鋅處理步驟(S2)係重複實施複數次。The
[熔融鍍鋅浴103之游離Al濃度CAl
及浴溫T之調整方法]
上述粗大底渣生成步驟(S1)及熔融鍍鋅處理步驟(S2)之熔融鍍鋅浴103之游離Al濃度CAl
及浴溫T之調整只要藉習知方法實施即可。[Free molten galvanizing bath of 103 C and adjusting the bath temperature T Al of the Al concentration Method] The coarse bottom dross formation step (S1) and hot dip galvanization step (S2) of the free molten galvanizing bath of
例如,熔融鍍鋅浴中之游離Al濃度CAl 係藉由於熔融鍍鋅浴中添加Al而調整。Al之添加例如係藉由將Al錠塊浸漬於熔融鍍鋅浴中而進行。Al之添加亦可藉由將Al錠塊浸漬於熔融鍍鋅浴以外之其他方法進行。藉由將Al錠塊浸漬於熔融鍍鋅浴而於熔融鍍鋅浴中添加Al之情況,以可抑制熔融鍍鋅浴之溫度急速變化之浸漬速度,將Al錠塊浸漬於熔融鍍鋅浴中。熔融鍍鋅浴中之游離Al濃度CAl 之調整方法不限定於上述方法。熔融鍍鋅浴中之游離Al濃度CAl 之調整方法宜為習知方法。For example, the free Al concentration C Al in the hot dip galvanizing bath is adjusted by adding Al to the hot dip galvanizing bath. The addition of Al is performed, for example, by immersing the Al ingot in the hot-dip galvanizing bath. The addition of Al can also be performed by immersing the Al ingot in a method other than the hot-dip galvanizing bath. By immersing the Al ingot in the hot-dip galvanizing bath and adding Al to the hot-dip galvanizing bath, the Al ingot is immersed in the hot-dip galvanizing bath at an immersion rate that can suppress the rapid change in temperature of the hot-dip galvanizing bath . The method of adjusting the free Al concentration C Al in the hot-dip galvanizing bath is not limited to the above method. The method for adjusting the free Al concentration C Al in the hot-dip galvanizing bath is preferably a conventional method.
又,熔融鍍鋅浴103之浴溫T係使用熔融鋅鍋101中設置之加熱裝置而調整。加熱裝置例如為高頻感應加熱裝置。In addition, the bath temperature T of the hot-
自粗大底渣生成步驟(S1)移行至熔融鍍鋅處理步驟(S2)之情況,僅藉由使熔融鍍鋅浴103之浴溫變化,即可容易地自滿足式(1)之熔融鍍鋅浴103移行至滿足式(2)之熔融鍍鋅浴103。具體而言,參考圖1,於粗大底渣生成步驟(S1),熔融鍍鋅浴103之狀態(游離Al濃度CAl
及浴溫T)成為Γ2
粒成長區域22之範圍內。此處,自粗大底渣生成步驟(S1)移行至熔融鍍鋅處理步驟(S2)之情況,若使浴溫T上升,則熔融鍍鋅浴103之狀態容易自Γ2
粒成長區域移行至δ1
核生成區域。亦即,僅藉由變更浴溫T,可容易地自滿足式(1)之熔融鍍鋅浴103變更至滿足式(2)之熔融鍍鋅浴103。When transitioning from the coarse bottom slag generation step (S1) to the hot-dip galvanizing treatment step (S2), only by changing the bath temperature of the hot-
又,本實施形態中,粗大底渣生成步驟(S1)與熔融鍍鋅處理步驟(S2)亦可交替重複實施。於熔融鍍鋅處理步驟(S2)後實施粗大底渣生成步驟(S1)時,於粗大底渣生成步驟(S1),若將熔融鍍鋅處理步驟(S1)後之熔融鍍鋅浴103之浴溫T降低,則可自滿足式(2)之熔融鍍鋅浴103作成滿足式(1)之熔融鍍鋅浴103。In addition, in this embodiment, the coarse bottom slag generation step (S1) and the hot-dip galvanizing treatment step (S2) may be alternately repeated. When the coarse bottom dross generation step (S1) is carried out after the hot galvanizing step (S2), if the
簡言之,本實施形態之熔融鍍鋅鋼板之製造方法,僅藉變更浴溫T,熔融鍍鋅浴103可容易地切換為滿足式(1)之狀態或滿足式(2)之狀態。因此,本實施形態中,藉由使浴溫T上升或下降,而可極容易地進行粗大底渣生成步驟(S1)與熔融鍍鋅處理步驟(S2)之切換。In short, in the method of manufacturing the hot-dip galvanized steel sheet of the present embodiment, only by changing the bath temperature T, the hot-
如以上,本實施形態中,實施粗大底渣生成步驟(S1)與熔融鍍鋅處理步驟(S2),而於鋼板表面上形成熔融鍍鋅層,製造熔融鍍鋅鋼板。As described above, in the present embodiment, the coarse bottom slag generation step (S1) and the hot-dip galvanizing treatment step (S2) are performed to form a hot-dip galvanized layer on the surface of the steel sheet to manufacture a hot-dip galvanized steel sheet.
本實施形態中,於熔融鍍鋅處理步驟(S2)中,不易生成成為碎渣缺陷要因之中型底渣。其結果,可抑制於熔融鍍鋅鋼板生成碎渣缺陷。再者,可抑制使熔融鍍鋅設備10停止之頻度(停機頻度),可於長期間內實施熔融鍍鋅處理步驟(S2)。In the present embodiment, in the hot-dip galvanizing treatment step (S2), it is difficult to generate a medium-sized bottom dross which is the cause of dross defects. As a result, the generation of slag defects in the hot-dip galvanized steel sheet can be suppressed. Furthermore, the frequency (stop frequency) of stopping the hot-
再者,停機時,熔融鍍鋅浴103進行浴調整後,於實施熔融鍍鋅處理步驟(S2)之前,實施粗大底渣生成步驟(S1)。藉此,於停機後再次實施熔融鍍鋅處理步驟(S2)時,預先含有粗大底渣之熔融鍍鋅浴103可利用於熔融鍍鋅處理步驟(S2)。Furthermore, during shutdown, after the hot-
[合金化熔融鍍鋅鋼板之製造方法] 上述本實施形態之熔融鍍鋅鋼板之製造方法可適用於合金化熔融鍍鋅鋼板之製造方法。[Manufacturing method of alloyed galvanized steel sheet] The manufacturing method of the hot-dip galvanized steel sheet of the present embodiment described above can be applied to the manufacturing method of the alloyed hot-dip galvanized steel sheet.
本實施形態之合金化熔融鍍鋅鋼板之製造方法具備製造熔融鍍鋅鋼板之步驟及合金化處理步驟。製造熔融鍍鋅鋼板之步驟中,實施上述之熔融鍍鋅鋼板之製造方法。合金化處理步驟中,對於藉由製造熔融鍍鋅鋼板之步驟所製造之熔融鍍鋅鋼板,使用圖3所示之合金化爐111實施合金化處理。合金化處理方法只要應用習知方法即已足夠。藉由以上製造步驟,可製造合金化熔融鍍鋅鋼板。The manufacturing method of the alloyed hot-dip galvanized steel sheet of this embodiment includes the steps of manufacturing the hot-dip galvanized steel sheet and the alloying treatment step. In the step of manufacturing the hot-dip galvanized steel sheet, the above-mentioned manufacturing method of the hot-dip galvanized steel sheet is carried out. In the alloying step, the alloying
以上,針對本實施形態之熔融鍍鋅鋼板之製造方法及合金化熔融鍍鋅鋼板之製造方法詳細說明。本實施形態係使用預先含有粗大底渣之熔融鍍鋅浴103,於δ1
核生成區域31中,實施熔融鍍鋅處理步驟(S2)。因此,實施熔融鍍鋅處理之期間中(亦即運轉期間中),利用熔融鍍鋅浴103中之粗大底渣之奧斯瓦爾德成長,可有效抑制微細底渣之生成及成長。其結果,於實施熔融鍍鋅處理步驟之期間,可抑制成為碎渣缺陷要因之中型底渣之生成,可抑制熔融鍍鋅鋼板及合金化熔融鍍鋅鋼板之碎渣缺陷。In the above, the manufacturing method of the hot dip galvanized steel sheet of this embodiment and the manufacturing method of the alloyed hot dip galvanized steel sheet were demonstrated in detail. In this embodiment, a hot-
再者,通常於底渣操作之情況下,堆積於熔融鋅鍋101底部之底渣之堆積量若增加,則堆積之中型底渣會因伴隨流而揚起,容易發生碎渣缺陷。然而,本實施形態之情況下,於熔融鋅鍋101底部堆積粗大底渣。粗大底渣其粒徑為300μm以上,因其質量而不易因伴隨流而揚起。因此,粗大底渣不易成為碎渣缺陷之要因。因此,可減少熔融鋅鍋101內之底渣去除步驟之實施頻度。其結果,可減低熔融鍍鋅設備10之停止頻度(停機頻度),使生產性提高。
[實施例]In addition, usually in the case of bottom slag operation, if the amount of bottom slag deposited on the bottom of the
邊顯示本發明例及比較例,針對本實施形態之熔融鍍鋅鋼板之製造方法具體說明。又,以下所示之實施例畢竟只是本實施形態之熔融鍍鋅鋼板之製造方法之一例。因此,本實施形態之熔融鍍鋅鋼板之製造方法並非限定於以下實施例者。While showing examples of the present invention and comparative examples, the method for manufacturing the hot-dip galvanized steel sheet of the present embodiment will be specifically described. In addition, the embodiment shown below is only one example of the method of manufacturing the hot-dip galvanized steel sheet of this embodiment. Therefore, the manufacturing method of the hot-dip galvanized steel sheet of this embodiment is not limited to the following examples.
[實施例1] [考慮粗大底渣生成步驟之試驗] 準備模擬實機之實驗的熔融鍍鋅浴。邊將熔融鍍鋅浴中之游離Al濃度CAl 維持於0.135%,浴溫T維持於455℃,邊保持10天(240小時)。亦即,熔融鍍鋅浴於Γ2 粒成長區域22保持10天。又,此時之熔融鍍鋅浴中之游離Fe濃度為0.026%。保持10天後,以如下方法調查熔融鍍鋅浴中之底渣形態(相及粒徑)。[Example 1] [Experiment considering the step of generating coarse bottom slag] Prepare a hot-dip galvanizing bath that simulates the experiment of a real machine. The free Al concentration C Al in the hot-dip galvanizing bath was maintained at 0.135% and the bath temperature T was maintained at 455°C for 10 days (240 hours). That is, the hot dip galvanizing bath is maintained in the Γ 2 grain growth region 22 for 10 days. At this time, the free Fe concentration in the hot-dip galvanizing bath was 0.026%. After holding for 10 days, the shape (phase and particle size) of the bottom slag in the hot-dip galvanizing bath was investigated as follows.
自熔融鍍鋅浴之深度中央位置且寬度中央位置,且長度中央位置之區域採取300g試料。採取之試料經急冷並固化。自經固化之試料採取測量樣本。以距急冷之面0.5mm之量研磨測量樣本。測量之樣本表面中,經研磨表面作為觀察面。觀察面中任意5視野以200倍光學顯微鏡觀察。各視野之面積為250μm×250μm。各視野中,可藉由對比度容易區別母相(Zn)與碎渣。據此,測定各視野之碎渣。A sample of 300g was taken from the area at the center of the depth of the hot dip galvanizing bath and at the center of the width and at the center of the length. The sample taken was quenched and solidified. Measurement samples are taken from the cured samples. Grind the measurement sample by 0.5 mm from the quenched surface. Among the measured sample surfaces, the polished surface serves as the observation surface. Any 5 fields in the observation surface were observed with a 200x optical microscope. The area of each field of view is 250 μm×250 μm. In each field of view, the parent phase (Zn) and slag can be easily distinguished by contrast. Based on this, the debris in each field of view was measured.
各視野之碎渣相以如下方法特定。各碎渣之化學組成使用EPMA分析。進而,各碎渣之結晶構造使用TEM予以解析。其結果,5個視野之任一碎渣的化學組成以質量%計,均由2%之Al與8%之Fe、與90%之Zn所成,結晶構造為面心立方晶。因此,熔融鍍鋅浴中之碎渣被特定為Γ2 相碎渣。據此,各視野之Γ2 相碎渣之粒徑以上述方法特定。其結果,5個視野中全部Γ2 相碎渣之平均粒徑均為100μm以上。圖8(A)之照片圖像係實施例1之掃描型電子顯微鏡所得之圖像之一例。圖中記載為「Γ2」之粒子為Γ2 相碎渣。又,圖像中之亮度越高,意指Al濃度越高(參考圖8右之Al(%))。The slag phase in each field of view is specified as follows. The chemical composition of each slag was analyzed using EPMA. Furthermore, the crystal structure of each crushed slag was analyzed using TEM. As a result, the chemical composition of any of the slags in the five fields of view is composed of 2% of Al, 8% of Fe, and 90% of Zn in mass%, and the crystal structure is a face-centered cubic crystal. Therefore, the dross in the hot dip galvanizing bath is designated as Γ 2 phase dross. Accordingly, the particle size of the Γ 2 phase slag in each field of view is specified by the method described above. As a result, the average particle size of all Γ 2 phase slag in all five fields of view was 100 μm or more. The photographic image of FIG. 8(A) is an example of an image obtained by the scanning electron microscope of Example 1. The particles described as "Γ2" in the figure are Γ 2 phase slag. Also, the higher the brightness in the image, the higher the Al concentration (refer to Al(%) on the right of FIG. 8).
藉由以上試驗,邊將建浴之熔融鍍鋅浴中之游離Al濃度CAl 維持於0.135%,浴溫T維持於455℃,邊保持10天時,熔融鍍鋅浴中形成粒徑為100μm以上之Γ2 相碎渣。又,邊將建浴之熔融鍍鋅浴中之游離Al濃度CAl 維持於0.135%,浴溫T維持於455℃,邊保持90天之結果,5個視野之Γ2 相碎渣均成為300μm以上。Through the above test, while maintaining the free Al concentration C Al in the hot-dip galvanizing bath of the built-up bath at 0.135% and the bath temperature T at 455°C, while maintaining it for 10 days, the particle size in the hot-dip galvanizing bath was 100 μm The above Γ 2 phase slag. Furthermore, while maintaining the free Al concentration C Al in the hot-dip galvanizing bath of the built-up bath at 0.135% and the bath temperature T at 455°C, the results were maintained for 90 days while the Γ 2 phase slag in all five fields of vision became 300 μm the above.
[實施例2] [假定熔融鍍鋅處理步驟之試驗] 其次,與實施例1同樣,準備實驗用之熔融鍍鋅浴。邊將熔融鍍鋅浴中之游離Al濃度CAl 維持於0.135%,浴溫T維持於470℃,邊保持10天(240小時)。亦即,熔融鍍鋅浴於δ1 核生成區域31保持10天。又,保持10天後,以如下方法調查熔融鍍鋅浴中之底渣形態(相及粒徑)。藉由與實施例1同樣之方法,調查熔融鍍鋅浴中之底渣形態(相及粒徑)。圖8(B)之照片圖像係實施例2之掃描型電子顯微鏡所得之圖像之一例。圖中之箭頭表示之「δ1」係δ1 相碎渣。[Example 2] [Test assuming hot-dip galvanizing treatment step] Next, as in Example 1, a hot-dip galvanizing bath for the experiment was prepared. The free Al concentration C Al in the hot-dip galvanizing bath was maintained at 0.135% and the bath temperature T was maintained at 470°C for 10 days (240 hours). That is, the hot-dip galvanizing bath is maintained in the δ 1 nucleation zone 31 for 10 days. Furthermore, after holding for 10 days, the form (phase and particle size) of the bottom slag in the hot-dip galvanizing bath was investigated as follows. By the same method as in Example 1, the bottom slag form (phase and particle size) in the hot-dip galvanizing bath was investigated. The photographic image of FIG. 8(B) is an example of an image obtained by the scanning electron microscope of Example 2. The "δ1" indicated by the arrow in the figure is the delta 1 phase slag.
亦如圖8所示,5個視野之任一碎渣的化學組成以質量%計,均由1%以下之Al與9%以上之Fe、與90%以上之Zn所成,結晶構造為面心立方晶。因此,實施例2之熔融鍍鋅浴中之碎渣被認定為δ1 相碎渣。以上述方法測定δ1 相碎渣之粒徑。其結果,5個視野中全部δ1 相碎渣之粒徑均遠小於100μm。又5個視野中,未確認到粒徑為100μm以上之Γ2 相碎渣。As also shown in Fig. 8, the chemical composition of any slag in the five fields of view, in terms of mass%, is composed of 1% or less of Al, 9% or more of Fe, and 90% or more of Zn, and the crystal structure is plane Heart cubic crystal. Therefore, the slag in the hot-dip galvanizing bath of Example 2 was regarded as δ 1 phase slag. The particle size of the δ 1 phase slag was measured by the above method. As a result, the particle diameters of all δ 1 phase slags in the five fields of view were much smaller than 100 μm. In five more fields of view, no Γ 2 phase slag having a particle size of 100 μm or more was confirmed.
以上實施例1及實施例2之試驗結果顯示與自圖1之準安定狀態圖所預測之碎渣像相當一致。因此,可知藉由適當調整熔融鍍鋅浴之游離Al濃度CAl (質量%)及浴溫T(℃),可調整底渣粒徑。The test results of Example 1 and Example 2 above show that they are quite consistent with the slag image predicted from the quasi-stability state diagram of FIG. 1. Therefore, it can be seen that by appropriately adjusting the free Al concentration C Al (mass %) of the hot-dip galvanizing bath and the bath temperature T (°C), the bottom slag particle size can be adjusted.
[實施例3] 基於上述實施例1及實施例2,使用實機之連續熔融鍍鋅設備,以如下方法製造合金化熔融鍍鋅鋼板。[Example 3] Based on the above-mentioned Example 1 and Example 2, the continuous molten galvanizing equipment of a real machine was used and the alloyed molten galvanized steel sheet was manufactured as follows.
各試驗編號中,停機期間中,熔融鍍鋅浴之游離Al濃度CAl (質量%)及浴溫T(℃)係保持為如表1之「停機時」欄之「Al濃度CAl 」欄及「浴溫T」欄所示。保持時間設為30天。In each test number, during the shutdown period, the free Al concentration C Al (mass %) and the bath temperature T (°C) of the hot-dip galvanizing bath are maintained as shown in the "Al concentration C Al "column of the "Shutdown" column of Table 1 And "Bath temperature T" column. The holding time is set to 30 days.
經過停機期間後,實施熔融鍍鋅處理步驟。熔融鍍鋅處理步驟之期間中,熔融鍍鋅浴之游離Al濃度CAl (質量%)及浴溫T(℃)係保持為如表1之「運轉時」欄所示。保持時間設為5天。保持期間中之鋼板通入量係與各試驗條件相同。又,對於熔融鍍鋅處理後之鋼板實施周知之合金化處理。各試驗編號所用之鋼板種類相同。又,合金化處理之條件於各試驗編號為相同。藉由以上步驟,製造各試驗編號之合金化熔融鍍鋅鋼板。After the shutdown period, the hot-dip galvanizing process is implemented. During the process of the hot-dip galvanizing process, the free Al concentration C Al (mass %) and bath temperature T (°C) of the hot-dip galvanizing bath are maintained as shown in the "Operation" column of Table 1. The hold time is set to 5 days. The steel plate flux during the holding period is the same as each test condition. In addition, the steel sheet after the hot-dip galvanizing treatment is subjected to a well-known alloying treatment. The types of steel plates used for each test number are the same. In addition, the conditions of alloying treatment are the same in each test number. Through the above steps, the alloyed hot-dip galvanized steel sheets of each test number were manufactured.
又,以上述方法經時測定各試驗編號之游離Al濃度CAl ,調整熔融鍍鋅浴之游離A1濃度CAl 。In addition, the free Al concentration C Al of each test number was measured over time by the above method, and the free A1 concentration C Al of the hot-dip galvanizing bath was adjusted.
於保持期間之最後2小時之間實施熔融鍍鋅處理之合金化熔融鍍鋅鋼板之表面以目視觀察,藉由如下評價指標,評價碎渣缺陷。The surface of the alloyed hot-dip galvanized steel sheet subjected to hot-dip galvanizing treatment during the last 2 hours of the holding period was visually observed, and the slag defects were evaluated by the following evaluation indexes.
具體而言,合金化熔融鍍鋅鋼板之合金化熔融鍍鋅層表面中,自任意寬度中央位置採取樣本。所採取之樣本的合金化熔融鍍鋅層表面中,將1m×1m之矩形區域設為1視野,將任意10個視野作為測定對象。各視野中,藉由目視,觀察粒徑100μm以上之碎渣。粒徑為100μm以上之碎渣附著於合金化熔融鍍鋅層時,認定為碎渣缺陷。以10個視野進行特定。計算碎渣缺陷之總個數。基於碎渣缺陷總個數與10個視野之總面積(10m2 ),求出碎渣缺陷之每單位面積之個數(個/10m2 )。又,目視中,針對粒徑是否為100μm以上難以判別之碎渣,使用100倍光學顯微鏡判別。Specifically, on the surface of the alloyed hot-dip galvanized steel sheet, samples are taken from the center of any width. On the surface of the alloyed hot-dip galvanized layer of the sample taken, a rectangular area of 1 m×1 m was set as 1 field of view, and any 10 fields of view were taken as the measurement object. In each field of view, visually observe debris with a particle size of 100 μm or more. When the slag having a particle diameter of 100 μm or more adheres to the alloyed hot-dip galvanized layer, it is regarded as a slag defect. Specify with 10 fields of view. Calculate the total number of slag defects. Based on the total number of slag defects and the total area of 10 fields of view (10m 2 ), the number of slag defects per unit area (pieces/10m 2 ) is determined. In addition, in the visual observation, it is judged by using a 100-fold optical microscope to determine whether the particle size is 100 μm or more and it is difficult to distinguish the slag.
碎渣缺陷評價之基準如下。 評價A:碎渣缺陷之每單位面積之個數為0個~1個/10m2 。 評價B:碎渣缺陷之每單位面積之個數為1~10個/10m2 。 評價C:碎渣缺陷之每單位面積之個數為11個/10m2 以上。The criteria for the evaluation of chipping defects are as follows. Evaluation A: The number of chipping defects per unit area is 0 to 1/10m 2 . Evaluation B: The number of broken slag defects per unit area is 1 to 10/10m 2 . Evaluation C: The number of chipping defects per unit area is 11 pieces/10m 2 or more.
[評價結果] 評價結果示於表1。 [Evaluation Results] The evaluation results are shown in Table 1.
又,表1中之「F2122 」欄中,表示對應之試驗編號的F2122 值。「F23 」欄中,表示對應之試驗編號的F23 值。「F3132 」欄中,表示對應之試驗編號的F3132 值。表1中之「停機時」欄中之「區域」欄中,表示停機期間之各試驗編號之熔融鍍鋅浴之狀態。例如,試驗編號1之情況下,停機期間之熔融鍍鋅浴狀態表示Γ2 粒成長區域。同樣表1中之「運轉時」欄中之「區域」欄中,表示運轉期間之各試驗編號之熔融鍍鋅浴之狀態。例如,試驗編號1之情況下,運轉期間之熔融鍍鋅浴狀態表示δ1 粒成長區域。In addition, the "F 2122 "column in Table 1 shows the F 2122 value of the corresponding test number. The "F 23 "column shows the F 23 value of the corresponding test number. The "F 3132 "column shows the F 3132 value of the corresponding test number. The "Area" column in the "At Shutdown" column in Table 1 indicates the state of the hot-dip galvanizing bath for each test number during shutdown. For example, in the case of Test No. 1, the state of the hot-dip galvanizing bath during shutdown indicates the growth area of Γ 2 grains. Similarly, the "Area" column in the "Operation" column in Table 1 indicates the state of the hot-dip galvanizing bath for each test number during operation. For example, in the case of Test No. 1, the state of the hot-dip galvanizing bath during operation indicates a growth area of δ 1 grain.
參考表1於試驗編號3~6、13~16、24~26、33~35,停機期間中,熔融鍍鋅浴之游離Al濃度CAl
及浴溫T滿足式(1)。亦即,熔融鍍鋅浴狀態為Γ2
粒成長區域。再者,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl
及浴溫T滿足式(2)。亦即,熔融鍍鋅浴狀態為δ1
核生成區域。因此,所製造之合金化熔融鍍鋅鋼板中未觀察到碎渣缺陷,可有效抑制碎渣缺陷(評價A)。Refer to Table 1 in the
另一方面,試驗編號1及2中,於運轉期間中,熔融鍍鋅浴之游離Al濃度CAl
及浴溫T未滿足式(2)。具體而言,運轉期間中,熔融鍍鋅浴狀態並非δ1
核生成區域,而是δ1
粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。On the other hand, in the
試驗編號7中,停機期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(1),熔融鍍鋅浴狀態為δ1 粒成長區域。再者,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 7, during the shutdown period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy equation (1), and the state of the hot-dip galvanizing bath was δ 1 grain growth area. In addition, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath do not satisfy the formula (2), and the state of the hot-dip galvanizing bath is δ 1 grain growth region. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號10中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為Γ2 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 10, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy the formula (2), and the state of the hot-dip galvanizing bath was a growth region of 2 grains. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號11中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為Γ2 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 11, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy the formula (2), and the state of the hot-dip galvanizing bath was a growth region of 2 grains. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號12中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 12, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy the formula (2), and the state of the hot-dip galvanizing bath was δ 1 grain growth region. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號17中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 17, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy equation (2), and the state of the hot-dip galvanizing bath was δ 1 grain growth region. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號18及19中,停機期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(1),熔融鍍鋅浴狀態為δ1 核生成區域。因此,所製造之合金化熔融鍍鋅鋼板中雖確認到碎渣缺陷但較少(評價B)。In Test Nos. 18 and 19, during the shutdown period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy Equation (1), and the state of the hot-dip galvanizing bath was δ 1 nucleus generation area. Therefore, although dross defects were confirmed in the produced alloyed hot-dip galvanized steel sheet (evaluation B).
試驗編號20~22中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl
及浴溫T未滿足式(2),熔融鍍鋅浴狀態為Γ2
粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In the
試驗編號23中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中雖確認到碎渣缺陷但較少(評價B)。In Test No. 23, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy equation (2), and the state of the hot-dip galvanizing bath was δ 1 grain growth region. Therefore, although dross defects were confirmed in the produced alloyed hot-dip galvanized steel sheet (evaluation B).
試驗編號27中,停機期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(1),熔融鍍鋅浴狀態為δ1 粒成長區域。再者,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In Test No. 27, during the shutdown period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy equation (1), and the state of the hot-dip galvanizing bath was δ 1 grain growth area. In addition, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath do not satisfy the formula (2), and the state of the hot-dip galvanizing bath is δ 1 grain growth region. Therefore, dross defects were confirmed in the produced alloyed galvanized steel sheet (evaluation C).
試驗編號28中,停機期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(1),熔融鍍鋅浴狀態為δ1 核生成區域。因此,所製造之合金化熔融鍍鋅鋼板中雖確認到碎渣缺陷但較少(評價B)。In Test No. 28, during the shutdown period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy the formula (1), and the state of the hot-dip galvanizing bath was δ 1 nucleus generation area. Therefore, although dross defects were confirmed in the produced alloyed hot-dip galvanized steel sheet (evaluation B).
試驗編號30及31中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl
及浴溫T未滿足式(2),熔融鍍鋅浴狀態為Γ2
粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價C)。In the
試驗編號32中,運轉期間中,熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(2),熔融鍍鋅浴狀態為δ1 粒成長區域。因此,所製造之合金化熔融鍍鋅鋼板中確認到碎渣缺陷(評價B)。In Test No. 32, during the operation period, the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath did not satisfy Equation (2), and the state of the hot-dip galvanizing bath was δ 1 grain growth region. Therefore, dross defects were confirmed in the produced alloyed hot-dip galvanized steel sheet (Evaluation B).
試驗編號8、9及29中,停機期間中及運轉期間中,浴溫為一定且為470℃以上。該等試驗編號中,停機期間中之熔融鍍鋅浴之游離Al濃度CAl 及浴溫T雖未滿足式(1),但所製造之合金化熔融鍍鋅鋼板並未確認到碎渣缺陷(評價A)。另一方面,如上述,試驗編號18、19及28中,由於浴溫為470℃以上而為一定,停機期間中之熔融鍍鋅浴之游離Al濃度CAl 及浴溫T未滿足式(1),故所製造之合金化熔融鍍鋅鋼板中雖確認到碎渣缺陷但較少(評價B)。因此,認為為了更安定地抑制碎渣缺陷,停機期間中之熔融鍍鋅浴之游離Al濃度CAl 及浴溫T滿足式(1),且運轉期間中熔融鍍鋅浴之游離Al濃度CAl 及浴溫T滿足式(2)為有效。In Test Nos. 8, 9 and 29, during the shutdown period and during the operation period, the bath temperature was constant and above 470°C. In these test numbers, although the free Al concentration C Al and the bath temperature T of the hot-dip galvanizing bath during the shutdown period did not satisfy the formula (1), the alloyed hot-dip galvanized steel sheet produced did not confirm slag defects (evaluation A). On the other hand, as mentioned above, in test numbers 18, 19, and 28, the bath temperature is constant at 470°C or higher. The free Al concentration C Al and bath temperature T of the hot-dip galvanizing bath during the shutdown period do not satisfy equation (1) ), so there are few slag defects in the alloyed hot-dip galvanized steel sheet (Evaluation B). Therefore, in order to suppress the slag defects more stably, the free Al concentration C Al and bath temperature T of the hot-dip galvanizing bath during the shutdown period satisfy the formula (1), and the free Al concentration C Al of the hot-dip galvanizing bath during the operation period And the bath temperature T satisfies formula (2) is effective.
[實施例4] 藉以下方法調查實施例3之試驗編號4(停機期間中為Γ2 粒成長區域,運轉期間中為δ1 核生成區域)、試驗編號11(停機期間中及運轉期間中均為Γ2 粒成長區域),及試驗編號18(停機期間中及運轉期間中均為δ1 核生成區域)之熔融鍍鋅浴中之碎渣尺寸及個數。[Example 4] The test number 4 (Γ 2 grain growth area during shutdown and δ 1 nucleus generation area during operation) and test number 11 (both during shutdown and during operation) were investigated by the following method It is the Γ 2 grain growth area), and the size and number of slag in the hot-dip galvanizing bath of test number 18 (delta 1 nucleus generation area during shutdown and during operation).
自試驗編號4、試驗編號11、試驗編號18之運轉期間結束後之各熔融鍍鋅浴之長度中央位置,且寬度中央位置且距熔融鍍鋅浴之液面300mm深之位置之區域,採取樣本(液相)。又,距熔融鍍鋅浴之液面300mm深之位置相當於將熔融鍍鋅浴深度假定為D(mm)時,自液面向深度方向D/10附近之位置。Samples are taken from the area at the center of the length of each hot-dip galvanizing bath after the operation period of test number 4, test number 11, and test number 18, and at the center of the width and at a depth of 300 mm from the liquid surface of the hot-dip galvanizing bath. (Liquid phase). In addition, a
使用銅製鑄模將採取之樣本急冷,固化為矩形狀。經固化之樣本表面之一定義為觀察面。將觀察面鏡面研磨。經鏡面研磨之觀察面中,將任意之20mm×20mm之範圍特定為視野面。使用雷射顯微鏡,測定視野面中所含之底渣粒徑及個數。具體而言,將20mm×20mm之視野面分割為100個2mm×2mm之微細區域。以光學顯微鏡觀察各微細區域,生成照片圖像(光學像)。於微細區域之照片圖像中,母相(Zn)與底渣之對比度不同。因此,以適當閾值對微細區域之照片圖像實施2值化處理,如圖7所示,明確出母相200與底渣100之界面150。特定出微細區域中之底渣100,藉由圖像處理求出所特定出之各底渣100之最大長度LS。所求出之最大長度定義為所對應之底渣100之粒徑(μm)。特定出所有微細區域中之底渣,且求出所特定出之底渣粒徑。接著,將所有微細區域中之底渣按特定粒徑範圍依階級分級。接著,求出每各階級之底渣個數。將每階級之底渣個數予以柱狀圖化。The sample taken is quenched with a copper mold and solidified into a rectangular shape. One of the cured sample surfaces is defined as the observation surface. Polish the observation mirror. Among the observation surfaces polished by mirror surface, an arbitrary range of 20 mm×20 mm is designated as the field of view. Using a laser microscope, measure the particle size and number of bottom slag contained in the field of view. Specifically, the field of view of 20 mm×20 mm is divided into 100 fine areas of 2 mm×2 mm. Observe each fine area with an optical microscope to generate a photo image (optical image). In the photo image of the fine area, the contrast between the parent phase (Zn) and the bottom slag is different. Therefore, by performing a binarization process on the photo image of the fine area with an appropriate threshold value, as shown in FIG. 7, the
又,上述之樣本採取位置位於較堆積於熔融鋅浴101底部之粗大底渣更上方。因此,所採取之樣本中,並未包含堆積於熔融鋅鍋101底部之粗大底渣。In addition, the sampling position mentioned above is located above the coarse bottom slag deposited on the bottom of the
基於測定之粒徑與底渣個數,作成圖9所示之柱狀圖。Based on the measured particle size and the number of bottom slag, a histogram as shown in FIG. 9 is prepared.
[評價結果] 參考圖9,對本發明例之試驗編號4(停機期間中為Γ2 粒成長區域,運轉期間中為δ1 核生成區域)與其他試驗編號11及18比較,視野面中之底渣總數最少。試驗編號4中,認為係作用如下機制。藉由於停機期間中實施粗大底渣生成步驟,而生成粗大底渣。接著,使用包含粗大底渣之熔融鍍鋅浴,於運轉期間中,進行熔融鍍鋅處理之結果,因奧斯瓦爾德成長,抑制了微細δ1 相碎渣之生成及成長。因此,粒徑為100μm~未達300μm之底渣個數最少,底渣總數亦最少。其結果,認為未確認到底渣缺陷。[Evaluation Results] Referring to FIG. 9, the test number 4 (Γ 2 grain growth area during shutdown and δ 1 nucleus generation area during operation) of the present invention is compared with other test numbers 11 and 18, and the bottom in the field of view The total amount of slag is the least. In Test No. 4, it is considered that the system acts as the following mechanism. The coarse bottom slag is generated by the step of generating the coarse bottom slag during the shutdown period. Next, a hot-dip galvanizing bath containing coarse bottom dross was used, and as a result of hot-dip galvanizing treatment during operation, the formation and growth of fine δ 1 phase dross was suppressed due to the growth of Oswald. Therefore, the number of bottom slag with a particle size of 100 μm to less than 300 μm is the smallest, and the total number of bottom slag is also the smallest. As a result, it is considered that slag defects were not confirmed.
另一方面,試驗編號11(停機期間中及運轉期間中均為Γ2 粒成長區域)與試驗編號4及試驗編號18比較,粒徑為100μm~未達300μm之底渣最多。由於粒徑為100μm~未達300μm之底渣較多,故預測於試驗編號11中碎渣缺陷較多。On the other hand, compared with the test number 4 and the test number 18, the test number 11 (both the Γ 2 grain growth area during the shutdown period and the operation period) has the most bottom slag having a particle size of 100 μm to less than 300 μm. Since there are many bottom slags with a particle size of 100 μm to less than 300 μm, it is predicted that there are many slag defects in Test No. 11.
試驗編號18(停機期間中及運轉期間中均為δ1 核生成區域)與試驗編號4比較,粒徑為100μm~未達300μm之底渣較多。尤其粒徑為100μm~未達150μm之底渣個數較多。因此,與試驗編號4比較,可預測碎渣缺陷較多。於試驗編號18中,由於未存在粗大底渣,故運轉期間中,無法充分抑制因粗大底渣之奧斯瓦爾德成長所致之微細δ1 相碎渣之生成及成長,其結果,認為粒徑為100μm~未達150μm之底渣個數變多。Compared with test number 4 in test number 18 (both δ 1 nucleus generation areas during shutdown and during operation), there are many bottom slags with a particle size of 100 μm to less than 300 μm. In particular, there are many bottom slags with a particle size of 100 μm to less than 150 μm. Therefore, compared with the test number 4, it can be predicted that there are many slag defects. In Test No. 18, since there was no coarse bottom slag, the generation and growth of fine δ 1 phase slag due to the Oswald growth of the coarse bottom slag could not be sufficiently suppressed during the operation period. The number of bottom slag whose diameter is from 100μm to less than 150μm becomes more.
[實施例5] 基於上述實驗結果,於1年內重複下述步驟:於連續熔融鍍鋅設備之停機期間中實施30~40天之粗大底渣生成步驟,隨後,使用含粗大底渣之熔融鍍鋅浴,實施30~40天之熔融鍍鋅處理步驟。此時,以使於粗大底渣生成步驟之熔融鍍鋅浴滿足式(1),於熔融鍍鋅處理步驟之熔融鍍鋅浴滿足式(2)之方式,將浴溫T上升或降低予以調整。其結果,於1年內重複30~40天之停機期間與30~40天之運轉期間,與於停機期間及運轉期間中,游離Al濃度CAl 為0.130%而為一定,浴溫為455℃而為一定進行操作之情況比較,底渣去除步驟的實施頻度可減低至1/3。[Example 5] Based on the above experimental results, the following steps are repeated within 1 year: during the shutdown period of the continuous molten galvanizing equipment, a step of generating a large bottom slag is carried out for 30 to 40 days, and then, the melt containing the large bottom slag is used Galvanizing bath, carry out 30 to 40 days of hot-dip galvanizing process. At this time, the bath temperature T is adjusted to increase or decrease in such a manner that the hot-dip galvanizing bath in the coarse bottom dross generation step satisfies formula (1) and the hot-dip galvanizing bath in the hot galvanizing process step satisfies formula (2). . As a result, the 30-40 day shutdown period and 30-40 day operation period are repeated within 1 year, and during the shutdown period and operation period, the free Al concentration C Al is constant at 0.130% and the bath temperature is 455°C For comparison of certain operations, the frequency of the bottom slag removal step can be reduced to 1/3.
以上,說明本發明之實施形態。然而,上述實施形態不過係用以實施本發明之例示。因此,本發明並非限定於上述實施形態,在不脫離其主旨之範圍內,可適當變更上述實施形態而實施。The embodiment of the present invention has been described above. However, the above-mentioned embodiments are merely examples for implementing the present invention. Therefore, the present invention is not limited to the above-mentioned embodiment, and can be implemented by appropriately changing the above-mentioned embodiment without departing from the scope of the gist.
1:熔融鍍鋅產線設備 10:熔融鍍鋅設備 20:燒鈍爐 30:翻轉輥 35:調質壓延機 40:頂輥 45:預鍍Ni設備 100:底渣 101:熔融鋅鍋 103:熔融鍍鋅浴 105:噴嘴部 107:沉降輥 109:氣體吹掃裝置 111:合金化爐 113:支撐輥 150:界面 200:母相 S:鋼板1: Hot-dip galvanizing production line equipment 10: Hot-dip galvanizing equipment 20: Burning furnace 30: flip roller 35: Tempering and Calendering Machine 40: Top roller 45: Pre-plated Ni equipment 100: bottom slag 101: molten zinc pot 103: Hot-dip galvanizing bath 105: nozzle part 107: Settling roller 109: Gas purge device 111: Alloying furnace 113: Support roller 150: Interface 200: mother phase S: Steel plate
圖1係熔融鍍鋅浴之碎渣生成相針對浴溫T(℃)及游離Al濃度CAl
予以整理之準安定狀態圖。
圖2係顯示合金化熔融鍍鋅鋼板及熔融鍍鋅鋼板之製造中所用之熔融鍍鋅產線設備之全體構成的功能方塊圖。
圖3係圖2中熔融鍍鋅設備之側視圖。
圖4係與圖3不同構成之熔融鍍鋅設備之側視圖。
圖5係與圖3及圖4不同構成之熔融鍍鋅設備之側視圖。
圖6係顯示與圖2不同構成之熔融鍍鋅產線設備之全體構成的功能方塊圖。
圖7係用以說明底渣粒徑之測定方法之示意圖。
圖8係顯示實施例1及2中建浴10天後之熔融鍍鋅浴中生成之底渣形態之顯微鏡照片。
圖9係針對實施例5之各製造條件下之碎渣粒徑與個數之關係加以顯示之圖表。Fig. 1 is a quasi-stabilized state diagram of the slag generation phase of the hot-dip galvanizing bath for the bath temperature T (°C) and the free Al concentration C Al . FIG. 2 is a functional block diagram showing the overall configuration of a hot-dip galvanized steel sheet and a hot-dip galvanized steel sheet used in the manufacture of a hot-dip galvanized steel sheet. Fig. 3 is a side view of the hot-dip galvanizing equipment in Fig. 2. FIG. 4 is a side view of a hot dip galvanizing equipment with a different structure from FIG. 3. Fig. 5 is a side view of a hot-dip galvanizing equipment with a different structure from Fig. 3 and Fig. 4. FIG. 6 is a functional block diagram showing the overall configuration of a hot-dip galvanizing production line with a configuration different from FIG. 2. FIG. 7 is a schematic diagram for explaining the measurement method of the bottom slag particle size. 8 is a microscope photograph showing the shape of the bottom slag formed in the hot-
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