JPH04259352A - Steel excellent in hydrogen-induced cracking resistance and its manufacture - Google Patents

Steel excellent in hydrogen-induced cracking resistance and its manufacture

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Publication number
JPH04259352A
JPH04259352A JP2112491A JP2112491A JPH04259352A JP H04259352 A JPH04259352 A JP H04259352A JP 2112491 A JP2112491 A JP 2112491A JP 2112491 A JP2112491 A JP 2112491A JP H04259352 A JPH04259352 A JP H04259352A
Authority
JP
Japan
Prior art keywords
steel
hydrogen
less
refining
induced cracking
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2112491A
Other languages
Japanese (ja)
Inventor
Yoshikatsu Furuno
好克 古野
Shinji Kuriyama
栗山 伸二
Hiromi Nakamura
博巳 中村
Hitoshi Kobayashi
日登志 小林
Takeshi Matsuzaki
健 松崎
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP2112491A priority Critical patent/JPH04259352A/en
Publication of JPH04259352A publication Critical patent/JPH04259352A/en
Pending legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To manufacture a steel excellent in hydrogen-induced cracking by subjecting molten iron to preliminary dephosphorizing and desulfurizing, thereafter performing steel refining in a converter, furthermore subjecting it to desulfurizing and refining in a ladle and degassing treatment and thereafter blowing Ca therein. CONSTITUTION:Blast furnace molten iron is subjected to preliminary dephosphorizing and desulfurizing treatment to reduce the content of P and S in the molten iron to <0.015% and <0.004%. Next, this molten iron is subjected to desulfurizing and refining in a converter into molten steel, is thereafter charged to a ladle and is freed of mixed slag to prevent the return of phosphorus from the slag. Then, desulfurizing and refining are performed by arc heating and atmospheric regulation to regulate the content of S to <0.0008%, and is successively subjected to degassing and refining to <0.00015% H2 and <0.000% N2 by an RH type vacuum degassing apparatus or the like, in which Ca-Si is blown by Ar, etc., within 3min in the ratio of 0.05 to 0.10kg in terms of Ca per one ton molten steel. The steel contg., by weight, 0.02 to 0.05% C, 0.01 to 0.05% Si, 0.60 to 2.00% Mn, 0.01 to 0.10% Al, <0.001% S and 0.0005 to 0.002% Ca and excellent in hydrogen induced cracking resistance can be manufactured.

Description

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

【0001】0001

【産業上の利用分野】本発明は耐水素割れ性の優れた鋼
の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing steel with excellent hydrogen cracking resistance.

【0002】0002

【従来の技術と課題】近年、石油消費量の増加に伴う油
田の開発とパイプラインの敷設が多く計画されているが
、このような場合において、その石油や天然ガス等のパ
イプ輸送や貯蔵タンクなどはそれらに含有される硫化水
素と水との共存条件にあって鋼表面が著しく腐食される
。すなわち上記したような条件下における腐食によって
発生した水素は鋼中に侵入し、延伸されたMnS など
の硫化物系介在物の周辺に凝集して内圧を高める結果、
板厚方向に平行な水素誘起割れを生じ、場合によっては
板厚方向に貫通して鋼材を破壊する。今までの研究によ
ると、水素誘起割れは、環境から腐食にともなって鋼中
に侵入した水素が非金属介在物物と地鉄の境界に集まり
、そのガス圧によって生じるものであり、非金属介在物
のうち介在物先端の形状効果(切欠き効果)による応力
集中が生じ易いMnSの量および展延度と強い相関があ
り、伸長したMnSが少ない程、割れ感受生は低下する
[Prior Art and Problems] In recent years, many plans have been made to develop oil fields and lay pipelines due to the increase in oil consumption. When the hydrogen sulfide contained in these steels coexists with water, the steel surface is severely corroded. In other words, hydrogen generated by corrosion under the above conditions invades the steel and aggregates around the drawn sulfide inclusions such as MnS, increasing the internal pressure.
Hydrogen-induced cracks occur parallel to the plate thickness direction, and in some cases, they penetrate through the plate thickness direction and destroy the steel material. According to research to date, hydrogen-induced cracking occurs when hydrogen that has entered the steel from the environment due to corrosion collects at the boundary between nonmetallic inclusions and the steel base, and is caused by the gas pressure. There is a strong correlation with the amount and degree of spreading of MnS, which tends to cause stress concentration due to the shape effect (notch effect) at the tip of inclusions, and the less elongated MnS there is, the lower the susceptibility to cracking becomes.

【0003】したがって、過酷な油田腐食環境で使用さ
れる鋼材は、S含有量を低下させて水素誘起割れの発生
起点となる硫化物系介在物を減少させ、さらにCaを添
加して非金属介在物の形状を制御して水素誘起割れ感受
性を低下させることが行われている。
Therefore, steel materials used in the harsh corrosive environment of oil fields are made by reducing the S content to reduce sulfide-based inclusions, which are the starting point for hydrogen-induced cracking, and by adding Ca to reduce non-metallic inclusions. Controlling the shape of objects has been attempted to reduce susceptibility to hydrogen-induced cracking.

【0004】耐水素割れ性の優れた鋼材の製造方法とし
て、特許公報、昭57−14747に開示されているよ
うに、 S  を0.0020wt% 未満、  Ca
  を0.002wt%以上、0.0050wt% 未
満含むようにCaワイヤーにより溶鋼にCaを添加して
いる。
[0004] As a method for producing steel materials with excellent hydrogen cracking resistance, as disclosed in Japanese Patent Publication No. 57-14747, less than 0.0020 wt% of S and less than 0.0020 wt% of Ca are used.
Ca is added to the molten steel using a Ca wire so that it contains 0.002 wt% or more and less than 0.0050 wt%.

【0005】しかしながら、この方法ではCa添加の歩
留りは高々18%であり、過剰なCa分は酸化物を形成
し、その一部は介在物として鋼材中に止まる。このため
、近年の高強度で耐水素誘起割れ性に優れた鋼材の仕様
の厳格化にともない、安定して前記仕様を満足する高品
質の鋼材を製造することが困難であった。
However, in this method, the yield of Ca addition is at most 18%, and excess Ca forms oxides, some of which remain in the steel material as inclusions. For this reason, as the specifications for steel materials with high strength and excellent hydrogen-induced cracking resistance have become stricter in recent years, it has been difficult to manufacture high-quality steel materials that stably satisfy the specifications.

【0006】本発明はかかる事情に鑑みてなされたもの
で、高強度で、かつ耐水素誘起割れ性の優れた鋼材およ
びその製造方法を提供しようとするものである。
The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a steel material having high strength and excellent resistance to hydrogen-induced cracking, and a method for manufacturing the same.

【0007】[0007]

【課題を解決するための手段、作用】第1の発明による
耐水素誘起割れ性のすぐれた鋼材は、 C;0.02 
〜0.05t%、Si:0.01〜0.05wt% 、
Mn:0.60〜2.00wt% およびAl:0.0
1〜0.10wt% を含有し、硫化水素を含む環境下
で使用される鋼材において、0.001wt%に満たな
い量に低減したSと0.002 〜0.005wt%の
Caを含み、残部は不純物を含めて実質的にFeよりな
ることを特徴とする。
[Means and effects for solving the problem] The steel material with excellent hydrogen-induced cracking resistance according to the first invention has a C; 0.02.
~0.05t%, Si:0.01~0.05wt%,
Mn: 0.60-2.00wt% and Al: 0.0
In steel materials containing 1 to 0.10 wt% and used in environments containing hydrogen sulfide, it contains S reduced to less than 0.001 wt% and Ca of 0.002 to 0.005 wt%, with the balance is characterized in that it consists essentially of Fe including impurities.

【0008】第2の発明による耐水素誘起割れ性のすぐ
れた鋼材を製造する方法は、溶銑予備処理により、溶銑
中の P  を0.015wt%以下、 S  を0.
004wt%以下とし、転炉精錬で脱炭した溶鋼を取鍋
精錬により S  を0.0008wt% 以下として
、脱ガス処理により H  を0.0001wt% 以
下とした後、溶鋼にCaを添加することを特徴とする。
[0008] A method for manufacturing a steel material with excellent hydrogen-induced cracking resistance according to the second invention is to reduce the P content to 0.015 wt% or less and the S content to 0.015 wt% or less in the hot metal by pre-treating the hot metal.
004 wt% or less, S is reduced to 0.0008 wt% or less by ladle refining of molten steel decarburized by converter refining, H is reduced to 0.0001 wt% or less by degassing treatment, and then Ca is added to the molten steel. Features.

【0009】この場合、Ca純分で0.05〜0.10
kg/tonをCaSi合金の粉体により、3 分以内
でArガスとともに、取鍋内の溶鋼に上吹きランスを通
して、溶鋼にCaを添加することが望ましい。
In this case, the pure Ca content is 0.05 to 0.10
It is desirable to add Ca to the molten steel by passing kg/ton of CaSi alloy powder into the molten steel in a ladle through a top blowing lance together with Ar gas within 3 minutes.

【0010】0010

【実施例】本実施例の製造プロセスは次の通りである。 先ず高炉から出銑された溶銑を鋳床脱珪により Si 
≦0.10wt% とした後、溶銑脱硫装置で S  
≦0.004wt%、次いで、溶銑脱燐装置により P
  ≦0.015wt%とする。この溶銑予備処理を行
った溶銑を細管集合体よりなる底吹きノズルより不活性
ガスを吹き込む上下吹き転炉に装入して脱炭、脱燐を行
い、 P  ≦0.010 wt% , C  ≦0.
040wt%として取鍋に装入したあと、復燐防止のた
め真空除滓装置で除滓する。前記除滓の終わった溶鋼を
アーク加熱および雰囲気調整の機能をもつ取鍋精錬装置
で脱硫、脱酸を行い、 S  ≦0.0008wt% 
、T O ≦0.0030wt% とする。 次いで、RH脱ガス装置で脱水素、脱窒を行って、 H
  ≦0.00010wt%、  N ≦ 0.004
0wt%とする。脱ガス処理の後、不活性ガスとともに
粉体を溶鋼中に吹き込むパウダーインジェクション装置
で、CaSiを吹き込き込み、溶鋼中にCaを添加する
。Caの添加は、Ca純分で0.04〜0.10kg/
tonを流量2000〜3000Nl/minのArガ
スをキャリアガスとして溶鋼中に吹き込む。Caの添加
量が0.04kg/ton未満であると、MnS の形
態制御が不充分で、0.10kg/tonを超えるとC
a系の硫酸化物が増加する。
[Example] The manufacturing process of this example is as follows. First, the hot metal tapped from the blast furnace is desiliconized in the cast bed to remove Si.
After setting the concentration to ≦0.10wt%, S
≦0.004wt%, then P by hot metal dephosphorization equipment
≦0.015wt%. The hot metal that has been subjected to this hot metal pretreatment is charged into a top-bottom blowing converter in which inert gas is blown through a bottom-blowing nozzle made of a collection of thin tubes, and decarburization and dephosphorization are performed. P ≦0.010 wt%, C ≦ 0.
After charging the sample into a ladle at 0.40 wt%, the sludge is removed using a vacuum sludge remover to prevent rephosphorization. The molten steel after the slag removal is desulfurized and deoxidized in a ladle refining device with arc heating and atmosphere adjustment functions, and S ≦0.0008wt%.
, T O ≦0.0030wt%. Next, dehydrogenation and denitrification are performed in an RH degassing device, and H
≦0.00010wt%, N≦0.004
It is set to 0wt%. After the degassing treatment, CaSi is injected into the molten steel using a powder injection device that injects powder together with an inert gas into the molten steel. Addition of Ca is 0.04 to 0.10 kg/ pure Ca.
ton of Ar gas is blown into the molten steel as a carrier gas at a flow rate of 2000 to 3000 Nl/min. If the amount of Ca added is less than 0.04 kg/ton, the morphology control of MnS will be insufficient, and if it exceeds 0.10 kg/ton, the amount of Ca added will be insufficient.
A-based sulfates increase.

【0011】次ぎにこの溶鋼を垂直曲げ型連鋳機に鋳込
んでスラブとし、プレートミルで圧延した後、UOEミ
ルで造管する。
[0011] Next, this molten steel is cast into a vertical bending type continuous casting machine to form a slab, which is rolled in a plate mill and then pipe-formed in a UOE mill.

【0012】近年、耐水素誘起割れ(耐HIC)性に対
する需要家の仕様が厳しくなっているが、その1例とし
て、API規格のX65,X60に対するHICの仕様
を表1に示す。
[0012] In recent years, customer specifications for hydrogen-induced cracking (HIC) resistance have become stricter. Table 1 shows, as an example, HIC specifications for X65 and X60 of the API standard.

【0013】[0013]

【表1】[Table 1]

【0014】表1に示したCLR(Crack Len
gth Ratio),CSR(Crack Sens
itivity Ratio) 、CTR(Crack
 Thickness Ratio) は鋼材の耐水素
割れ性の試験に関する測定法を示すもので、ASTMに
規定されてあるものである。この測定法を簡単に説明す
ると、上記のようにして造管されたラインパイプから試
料を切出して、この試料をASTM 01−77で規定
されたいわゆるNACE溶液、すなわち(5% NaC
l + 0.5% CH3COOH + H2S飽和、
pH 3.5〜3.8 )の溶液に96時間浸漬したあ
と、発生した割れを顕微鏡で 3 x 20mm の面
積について観察する。観察された割れについて、CLR
は割れの長さ、CTRは複数の割れが板厚方向に層状に
なっいるときの厚さ、CSRは前記の割れの長さと厚さ
との積、をそれぞれ観測した断面積で除した値を%で示
したものである。また、表1には降伏強度(Ys,kg
/mm2) 、引張り強度(Ts,kg/mm2) も
合わせて示してあるが、従来の低グレードのAPI 規
格製品に比較して強度が高いにもかかわらず、SLR、
SCR、STR 等の割れに対する仕様は緩和されてお
らず、表1に示す仕様は実質的に厳しいものとなってい
る。従来の製造方法においては、X60については仕様
を充分満足していたが、X65については表1の仕様を
満足せず、製品不良となるものが約13.6% に達し
ており、この不良率を下げることが強く望まれていた。
CLR (Crack Len) shown in Table 1
gth Ratio), CSR (Crack Sens.
CTR (Crack
Thickness Ratio indicates a measurement method for testing the hydrogen cracking resistance of steel materials, and is specified by ASTM. To briefly explain this measurement method, a sample is cut out from the line pipe made as described above, and the sample is mixed with a so-called NACE solution specified by ASTM 01-77, that is, (5% NaC
l + 0.5% CH3COOH + H2S saturation,
After immersion in a solution with a pH of 3.5 to 3.8 for 96 hours, the cracks that have occurred are observed under a microscope over an area of 3 x 20 mm. Regarding the observed cracks, CLR
is the crack length, CTR is the thickness when multiple cracks are layered in the plate thickness direction, and CSR is the product of the crack length and thickness divided by the observed cross-sectional area as %. This is shown in . Table 1 also shows the yield strength (Ys, kg
/mm2) and tensile strength (Ts, kg/mm2) are also shown, but although the strength is higher than that of conventional low-grade API standard products, SLR,
The specifications for cracks such as SCR and STR have not been relaxed, and the specifications shown in Table 1 are actually strict. In the conventional manufacturing method, the X60 fully satisfies the specifications, but the X65 does not meet the specifications in Table 1, resulting in approximately 13.6% of products being defective, and this defective rate is It was strongly desired to lower the

【0015】この不良率低減を目的として種々検討を行
ったが、その1つとして発生した割れの内部または近傍
をEPMA(Electron Micro Prob
e Analyzer) 分析した。そのー例を図1に
示す。図1によれば、観察された介在物は Ca−Al
系硫酸化物であることが判明した。耐水素誘起割れ鋼に
ついて、Ca添加によりMnS の形態制御が重要であ
ることはよく知られているが、過剰のCa挙動について
も充分検討を行う必要がある。形態制御に対して必要以
上の添加は上記のCa系の硫酸化物を生じ、割れ発生を
増加させる要因となる。
[0015] Various studies have been conducted for the purpose of reducing the defective rate, and one of them is to use EPMA (Electron Micro Prob
e Analyzer). An example is shown in Figure 1. According to Figure 1, the observed inclusions are Ca-Al
It turned out to be a type sulfate. It is well known that controlling the morphology of MnS by adding Ca is important for hydrogen-induced cracking resistant steel, but it is also necessary to thoroughly study the behavior of excessive Ca. Addition of more than necessary for morphology control produces the above-mentioned Ca-based sulfides, which increases the occurrence of cracks.

【0016】この点に注目して、添加するCaの歩留り
について検討した。この結果を図2に示す。図2は、上
述のプロセスにより、脱ガスの後にパウダーインジェク
ションによって行う CaSi 合金の添加量(kg/
ch)と Ca の濃度、Caの歩留りとの関係を示す
。ここで使用した CaSi 合金はCa;30wt%
、Si;60wt%、残部Feの粉末である。したがっ
て、上記 CaSi 合金の添加量(kg/ch) は
本実施例では溶鋼は235ton/ch で、これにC
aの歩留りを考慮してCa純分の添加量kg/ch が
容易に求められる。図2に示されているように、CaS
i添加量の低減によりCaの添加歩留りは向上し、製品
中 Ca は、CaSi合金添加量を40kg/ch 
まで低減しても、16〜20ppm とすることができ
る。また、Ca歩留りは30% と向上するので、過剰
な酸化物、硫化物は大幅に低減する。また、製品中 S
  を8ppm以下とすることにより、Ca/S  は
2以上を確保することができる。したがって、  福味
、他、鉄と鋼,69(1983)S214 に示されて
いる通り、Ca/S  が2以上あればMnS の形態
制御も可能である。上記に示したように、耐HIC鋼の
製造においてはCa歩留りを向上させ、Caロス分とし
て生成するCaの硫酸化物(Oxysulfide)の
低減を図る必要があることが分かる。表2に S  が
10ppm 以下の場合についても、Ca添加の効果が
明らかであることを示す。
[0016] Focusing on this point, the yield of added Ca was studied. The results are shown in FIG. Figure 2 shows the amount of CaSi alloy added (kg/
ch), the concentration of Ca, and the yield of Ca. The CaSi alloy used here contains Ca; 30wt%
, Si; 60 wt%, balance Fe powder. Therefore, in this example, the addition amount (kg/ch) of the CaSi alloy is 235 ton/ch for the molten steel, and
Considering the yield of a, the added amount of pure Ca (kg/ch) can be easily determined. As shown in Figure 2, CaS
The addition yield of Ca is improved by reducing the amount of i added, and the amount of Ca in the product is reduced to 40 kg/ch.
Even if it is reduced to 16 to 20 ppm. Furthermore, since the Ca yield is improved to 30%, excess oxides and sulfides are significantly reduced. In addition, S in the product
By setting Ca/S to 8 ppm or less, it is possible to ensure Ca/S of 2 or more. Therefore, as shown in Fukumi et al., Tetsu-to-Hagane, 69 (1983) S214, it is possible to control the morphology of MnS if Ca/S is 2 or more. As shown above, it is understood that in the production of HIC-resistant steel, it is necessary to improve the Ca yield and reduce Ca sulfide (Oxysulfide) generated as Ca loss. Table 2 shows that the effect of Ca addition is clear even when S is 10 ppm or less.

【0017】[0017]

【表2】[Table 2]

【0018】表2はA〜Dの4つの水準について行った
もので、A,Bは Sが10ppm 以下の本実施例で
、C,Dは比較例として,CaSi添加を除いて本実施
例であるA,Bと同様に上述のプロセスに従って製造し
たものを試料としてある。A,BはCaSi合金の添加
量は0.05kg/tonである。この表に示されてい
る通り、A,BではCLRは最大で7%で、充分、表1
の耐HICの仕様を満足する。 これに対してCa添加を行わないC,DについてはCL
Rが最小で26%,最大で33%に達しており、上記表
1の仕様を満足しない。したがって、極低硫化処理( 
S ≦8ppm) だけでは介在物としてのMnS が
割れの起点となることを示している。
[0018] Table 2 shows the results for four levels A to D. A and B are for this example in which S is 10 ppm or less, and C and D are comparative examples for this example except for the addition of CaSi. Similar to certain A and B, the samples were manufactured according to the above-mentioned process. In A and B, the amount of CaSi alloy added is 0.05 kg/ton. As shown in this table, the maximum CLR for A and B is 7%, which is sufficient.
Satisfies HIC resistance specifications. On the other hand, for C and D without Ca addition, CL
R reaches 26% at the minimum and 33% at the maximum, which does not satisfy the specifications in Table 1 above. Therefore, ultra-low sulfidation treatment (
S ≦8 ppm) alone indicates that MnS as an inclusion becomes the starting point of cracking.

【0019】表3に実操業で製造したX65グレードの
鋼材の成分分析値を10個の異なる試料についていずれ
も重量比で示してある。これらはいずれも表1の仕様を
満足するものである。任意元素であるCu,Ni,V,
Nb,Ti は製造される鋼の性質に一層の改善をを与
えるため必要に応じて添加するものである。これらの添
加元素は耐水素誘起割れ性を損なわない程度に適性な範
囲で、1種または2種以上入れることができる。
Table 3 shows the component analysis values of X65 grade steel produced in actual operation for 10 different samples, all expressed as weight ratios. All of these satisfy the specifications in Table 1. Arbitrary elements Cu, Ni, V,
Nb and Ti are added as necessary to further improve the properties of the manufactured steel. One or more of these additive elements can be added within an appropriate range without impairing the hydrogen-induced cracking resistance.

【0020】[0020]

【表3】[Table 3]

【0021】次に本発明の耐水素誘起割れ性の優れた鋼
材の成分の限定理由について説明する。 C:0.01wt% 未満では必要強度が得られず、0
.05wt% を超えると鋼の靱性や溶接性に好ましく
ない影響が現れるので、0.02〜 0.05wt%と
した。 Si:脱酸上必要な元素であるが、0.01wt% 未
満では脱酸効果がなく、0.50wt% を超えると靱
性劣化のおそれがあるので、0.01〜0.50wt%
 とした。 Mn:0.60wt% に、満たないと強度面の要請が
満たされ難く、一方2.00wt% をこえると靱性お
よび溶接性に悪影響を及ぼすので、0.60〜2.00
wt% とした。 Al:脱酸上必要な元素であるが、0.01wt% に
満たないと脱酸効果が事実上生じない反面、0.10w
t% を超えると結晶粒の粗大化を促進し材質を劣化さ
せるので、0.01〜0.10wt% とした。 S:0.001 wt% をこえると割れの起点となる
MnS の形態制御をを効果的に行うことができないの
で、0.001 wt% 以下とした。 Ca:0.0005wt% 未満ではMnS の形態制
御を充分行うことができず、0.002 wt% 以上
ではCa系の硫酸化物の生成を効果的に低減することが
できないので、0.0005〜0.002 wt% と
した。
Next, the reasons for limiting the components of the steel material having excellent hydrogen-induced cracking resistance according to the present invention will be explained. C: If it is less than 0.01wt%, the required strength cannot be obtained, and 0.
.. If it exceeds 0.05 wt%, unfavorable effects will appear on the toughness and weldability of the steel, so the content was set at 0.02 to 0.05 wt%. Si: An element necessary for deoxidation, but if it is less than 0.01 wt%, there is no deoxidizing effect, and if it exceeds 0.50 wt%, there is a risk of deterioration of toughness, so Si: 0.01 to 0.50 wt%.
And so. Mn: If it is less than 0.60 wt%, it will be difficult to meet the strength requirements, while if it exceeds 2.00 wt%, it will have a negative effect on toughness and weldability.
It was set as wt%. Al: is an element necessary for deoxidation, but if it is less than 0.01wt%, the deoxidation effect will not actually occur, but at 0.10w
If it exceeds t%, it promotes coarsening of crystal grains and deteriorates the material quality, so it is set at 0.01 to 0.10wt%. S: If it exceeds 0.001 wt%, it is not possible to effectively control the morphology of MnS, which becomes the starting point of cracks, so the content was set to 0.001 wt% or less. Ca: If it is less than 0.0005 wt%, the morphology of MnS cannot be controlled sufficiently, and if it is more than 0.002 wt%, the production of Ca-based sulfates cannot be effectively reduced. It was set as .002 wt%.

【0022】[0022]

【発明の効果】本発明によば、溶銑予備処理により脱硫
、脱燐を行い、転炉精錬、取鍋精錬、脱ガス処理を経て
Ca添加を行うので、極低硫化によりCaの添加量を低
減し、かつ歩留りを向上することができ、過剰なCaに
よる硫酸化物を低減して耐水素誘起われ性を向上するこ
とができる。
According to the present invention, desulfurization and dephosphorization are performed through hot metal pretreatment, and Ca addition is performed through converter refining, ladle refining, and degassing treatment, so the amount of Ca added can be reduced by extremely low sulfidation. It is possible to reduce the amount of Ca and improve the yield, and it is possible to reduce sulfates caused by excess Ca and improve resistance to hydrogen-induced fragility.

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

【図1】EPMA分析によるX線のエネルギーと強度と
の関係を示すグラフ図である。
FIG. 1 is a graph showing the relationship between X-ray energy and intensity according to EPMA analysis.

【図2】CaSi 合金の添加量(kg/ch) と、
 Ca の濃度およびCaの歩留りとの関係を示すグラ
フ図である。
[Figure 2] Addition amount (kg/ch) of CaSi alloy and
FIG. 2 is a graph diagram showing the relationship between the concentration of Ca and the yield of Ca.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】  C;0.02 〜0.05t%、Si
:0.01〜0.05wt% 、Mn:0.60〜2.
00wt%およびAl:0.01〜0.10wt% を
含有し、硫化水素を含む環境下で使用される鋼材におい
て、0.001wt%に満たない量に低減したSと0.
002 〜0.005wt%のCaを含み、残部は不純
物を含めて実質的にFeよりなることを特徴とする耐水
素誘起割れ性のすぐれた鋼材。
Claim 1: C; 0.02 to 0.05t%, Si
:0.01~0.05wt%, Mn:0.60~2.
00 wt% and Al: 0.01 to 0.10 wt% and used in an environment containing hydrogen sulfide, S and 0.00 wt% are reduced to less than 0.001 wt%.
A steel material having excellent resistance to hydrogen-induced cracking, characterized in that it contains 0.02 to 0.005 wt% of Ca, and the remainder, including impurities, consists essentially of Fe.
【請求項2】  溶銑予備処理により、溶銑中の P 
 を0.015wt%以下、 S  を0.004wt
%以下とし、転炉精錬で脱炭した溶鋼を取鍋精錬により
 S  を0.0008wt% 以下として、脱ガス処
理により H  を0.00015wt%以下、 N 
 を0.0050wt% 以下とした後、溶鋼にCaを
添加することを特徴とする耐水素誘起割れ性の優れた鋼
材を製造する方法。
[Claim 2] P in hot metal is reduced by hot metal pretreatment.
0.015wt% or less, S 0.004wt
% or less, S is reduced to 0.0008 wt% or less by ladle refining of molten steel decarburized by converter refining, H is reduced to 0.00015 wt% or less by degassing treatment, N is reduced to 0.00015 wt% or less, and N
A method for producing a steel material with excellent hydrogen-induced cracking resistance, which comprises adding Ca to molten steel after reducing the content of the steel to 0.0050 wt% or less.
【請求項3】  Ca純分で0.05〜0.10kg/
tonをCaSi合金の粉体により、3 分以内でAr
ガスとともに、取鍋内の溶鋼に上吹きランスを通して、
溶鋼にCaを添加することを特徴とする請求項2の耐水
素誘起割れ性の優れた鋼材を製造する方法。
[Claim 3] Ca pure content: 0.05 to 0.10 kg/
ton by CaSi alloy powder within 3 minutes.
Pass the gas through the top blowing lance through the molten steel in the ladle,
3. The method for producing a steel material with excellent hydrogen-induced cracking resistance according to claim 2, characterized in that Ca is added to the molten steel.
JP2112491A 1991-02-14 1991-02-14 Steel excellent in hydrogen-induced cracking resistance and its manufacture Pending JPH04259352A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2112491A JPH04259352A (en) 1991-02-14 1991-02-14 Steel excellent in hydrogen-induced cracking resistance and its manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2112491A JPH04259352A (en) 1991-02-14 1991-02-14 Steel excellent in hydrogen-induced cracking resistance and its manufacture

Publications (1)

Publication Number Publication Date
JPH04259352A true JPH04259352A (en) 1992-09-14

Family

ID=12046140

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2112491A Pending JPH04259352A (en) 1991-02-14 1991-02-14 Steel excellent in hydrogen-induced cracking resistance and its manufacture

Country Status (1)

Country Link
JP (1) JPH04259352A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10176240A (en) * 1996-12-13 1998-06-30 Nippon Steel Corp H-section steel for tunnel support and method of manufacturing the same
JP2000087127A (en) * 1998-09-04 2000-03-28 Sumitomo Metal Ind Ltd Method for producing highly clean HIC steel
KR100916098B1 (en) * 2002-12-24 2009-09-08 주식회사 포스코 Steel refining method for manufacturing calcium-containing pipe
KR100949724B1 (en) * 2002-12-12 2010-03-25 주식회사 포스코 Hydrogen Reduction Molten Steel Refining Method of Low Sulfur Used Carbon Steel
WO2010093057A1 (en) * 2009-02-12 2010-08-19 新日本製鐵株式会社 High-strength steel sheet and high-strength steel pipe having excellent hydrogen-induced cracking resistance for use in line pipe
CN114134393A (en) * 2021-12-14 2022-03-04 芜湖新兴铸管有限责任公司 Method for producing high-quality 38CrMoAl steel by converter-refining furnace-RH furnace-round billet continuous casting machine

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10176240A (en) * 1996-12-13 1998-06-30 Nippon Steel Corp H-section steel for tunnel support and method of manufacturing the same
JP2000087127A (en) * 1998-09-04 2000-03-28 Sumitomo Metal Ind Ltd Method for producing highly clean HIC steel
KR100949724B1 (en) * 2002-12-12 2010-03-25 주식회사 포스코 Hydrogen Reduction Molten Steel Refining Method of Low Sulfur Used Carbon Steel
KR100916098B1 (en) * 2002-12-24 2009-09-08 주식회사 포스코 Steel refining method for manufacturing calcium-containing pipe
WO2010093057A1 (en) * 2009-02-12 2010-08-19 新日本製鐵株式会社 High-strength steel sheet and high-strength steel pipe having excellent hydrogen-induced cracking resistance for use in line pipe
JP2010209460A (en) * 2009-02-12 2010-09-24 Nippon Steel Corp High-strength steel sheet and high-strength steel pipe having excellent hydrogen-induced cracking resistance for use in line pipe
CN114134393A (en) * 2021-12-14 2022-03-04 芜湖新兴铸管有限责任公司 Method for producing high-quality 38CrMoAl steel by converter-refining furnace-RH furnace-round billet continuous casting machine
CN114134393B (en) * 2021-12-14 2022-06-07 芜湖新兴铸管有限责任公司 Method for producing high-quality 38CrMoAl steel by converter-refining furnace-RH furnace-round billet continuous casting machine

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