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JP2008261033A - Method for producing grain-oriented silicon steel sheet and its continuous decarburizing / nitriding annealing equipment - Google Patents

Method for producing grain-oriented silicon steel sheet and its continuous decarburizing / nitriding annealing equipment Download PDF

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JP2008261033A
JP2008261033A JP2007105914A JP2007105914A JP2008261033A JP 2008261033 A JP2008261033 A JP 2008261033A JP 2007105914 A JP2007105914 A JP 2007105914A JP 2007105914 A JP2007105914 A JP 2007105914A JP 2008261033 A JP2008261033 A JP 2008261033A
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Shigenobu Koga
重信 古賀
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Nippon Steel Corp
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Abstract

【課題】雰囲気ガスを安価に供給するとともに、皮膜性能および磁性の高位安定化を図ることのできる方向性珪素鋼板の製造方法及びその連続脱炭・窒化焼鈍設備を提供する。
【解決手段】Siを2.0〜4.8%含む所定厚の冷延鋼板に、脱炭工程を含む一次再結晶焼鈍及び窒化焼鈍を行い、焼鈍分離材を塗布して仕上焼鈍を施す方向性珪素鋼板の製造方法及びその製造設備において、窒化焼鈍を行う窒化帯または窒化帯の前後の雰囲気仕切り内から雰囲気ガスを回収・脱水し、H2、不活性ガスを主成分とし、NH3を1vol%(ドライガス換算)未満含む再生雰囲気ガスを生産し、供給後の窒化帯雰囲気がH2濃度:25vol%(ドライガス換算)以上、NH3:0.1〜10vol%(ドライガス換算)、露点:10℃以下、残部不活性ガスになるように、再生雰囲気ガスに、不活性ガス、NH3、H20を加えて成分調整してから窒化帯に供給することを特徴とする。
【選択図】図1
The present invention provides a method for producing a grain-oriented silicon steel sheet capable of supplying atmospheric gas at low cost and achieving high film stability and high magnetic stability, and a continuous decarburizing / nitriding annealing equipment thereof.
A direction in which a cold-rolled steel sheet having a predetermined thickness containing Si of 2.0 to 4.8% is subjected to primary recrystallization annealing and nitriding annealing including a decarburizing step, and an annealing separator is applied to perform finish annealing. In the manufacturing method and manufacturing equipment for the heat-resistant silicon steel sheet, the atmospheric gas is recovered and dehydrated from the nitriding zone where the nitridation annealing is performed or from the atmosphere partition before and after the nitriding zone, and the NH 3 is mainly composed of H 2 and inert gas. Regenerative atmosphere gas containing less than 1 vol% (in terms of dry gas) is produced, and the nitriding zone atmosphere after supply is H 2 concentration: 25 vol% (in terms of dry gas) or more, NH 3 : 0.1 to 10 vol% (in terms of dry gas) The dew point is 10 ° C. or less, and the inert gas, NH 3 , H 2 0 are added to the regeneration atmosphere gas so as to be the inert gas, and the components are adjusted before being supplied to the nitriding zone.
[Selection] Figure 1

Description

本発明は、鉄損が極めて低い方向性珪素鋼板の製造方法および方向性珪素鋼板の連続脱炭・窒化焼鈍設備に関するものである。   The present invention relates to a method for manufacturing a grain-oriented silicon steel sheet with extremely low iron loss and a continuous decarburization / nitriding annealing facility for grain-oriented silicon steel sheets.

方向性珪素鋼板は、電気機器の磁気鉄心として多用され、エネルギーロスを少なくする鋼板自体の改善はもとより、鋼板の製造の安定性改善、製造コスト低減等が繰り返し研究されてきた。脱炭工程を含む一次再結晶焼鈍を行う脱炭焼鈍工程や窒化焼鈍工程も、例外ではなかった。   Oriented silicon steel plates are frequently used as magnetic iron cores in electrical equipment, and have been repeatedly studied not only for improving the steel plates themselves to reduce energy loss, but also for improving the stability of manufacturing steel plates and reducing manufacturing costs. The decarburization annealing process and the nitriding annealing process in which the primary recrystallization annealing including the decarburization process is performed were no exception.

脱炭・窒化焼鈍工程の主たる目的は、熱延工程でのγ相域確保等の理由で、鋼板に含まれている炭素(通常、5×10-2質量%程度)を、最終製品で磁性が時効劣化しない領域(15質量ppm未満)まで脱炭し、次いで、鋼板表面に適正な酸素付与を行って、FeおよびSi酸化物を形成させた後、鋼板に適正な窒素付与を行い、その後、次工程の仕上焼鈍で、表面に塗布したMgOを反応させてグラス皮膜を形成するとともに、2次再結晶させる前準備として、最適な結晶粒サイズに一次再結晶させることである。 The main purpose of the decarburizing / nitriding annealing process is to secure carbon (usually about 5 × 10 −2 mass%) contained in the steel sheet in the final product for reasons such as securing the γ-phase region in the hot rolling process. Is decarburized to a region where aging does not deteriorate (less than 15 ppm by mass), then, after applying appropriate oxygen to the steel sheet surface to form Fe and Si oxides, applying appropriate nitrogen to the steel sheet, In the next annealing process, MgO applied to the surface is reacted to form a glass film, and as a preparation for secondary recrystallization, primary recrystallization is performed to an optimum crystal grain size.

従来、この方向性珪素鋼板の脱炭焼鈍工程は連続焼鈍炉で行われ、炉内で鋼板が連続的に脱炭され、鋼板表面に酸素が付与されるとともに、雰囲気ガスも連続的に還元され、炉外に放散燃焼されていた。また、窒化焼鈍工程は、炉内で鋼板が連続的に窒化され、鋼板に窒素が付与されるとともに、雰囲気ガスも、連続的に、NH3分解および還元され、炉外に放散燃焼されていた。 Conventionally, the decarburization annealing process of the grain-oriented silicon steel sheet is performed in a continuous annealing furnace, the steel sheet is continuously decarburized in the furnace, oxygen is given to the steel sheet surface, and the atmospheric gas is also continuously reduced. It was burned out of the furnace. Further, in the nitriding annealing process, the steel sheet was continuously nitrided in the furnace, nitrogen was imparted to the steel sheet, and the atmospheric gas was continuously decomposed and reduced with NH 3 and diffused and burned out of the furnace. .

図3に、従来の連続脱炭・窒化焼鈍設備の一例を示す。炉2は、加熱・均熱帯3、還元帯4、窒化帯5、冷却帯6、および、それらの処理帯間の雰囲気仕切り7〜9から構成されている。   FIG. 3 shows an example of conventional continuous decarburization / nitriding annealing equipment. The furnace 2 includes a heating / soaking zone 3, a reduction zone 4, a nitriding zone 5, a cooling zone 6, and atmosphere partitions 7 to 9 between these treatment zones.

加熱・均熱帯3の雰囲気ガスは、加熱・均熱帯3の後方の雰囲気ガス供給管20Aより供給され、鋼板1と対向しながら、大半は、炉2の前部に流れ、雰囲気ガス排出管11Aより放散燃焼されるが、一部は、炉入口から放散されるとともに、雰囲気仕切り7へ流出する。   The atmosphere gas in the heating / soaking zone 3 is supplied from the atmosphere gas supply pipe 20A behind the heating / soaking zone 3, and most of the atmosphere gas flows to the front of the furnace 2 while facing the steel plate 1, and the atmosphere gas discharge pipe 11A. Although more dissipated and burned, a part of it is dissipated from the furnace inlet and flows out to the atmosphere partition 7.

還元帯4の雰囲気ガスは、雰囲気ガス供給管20Bより供給され、雰囲気ガス排出管11Bより放散燃焼されるとともに、前後の雰囲気仕切り7、8へ流出する。窒化帯5の雰囲気ガスは、雰囲気ガス供給管20Cより供給され、雰囲気ガス排出管11Cより放散燃焼されるとともに、前後の雰囲気仕切り8、9へ流出する。   The atmosphere gas in the reduction zone 4 is supplied from the atmosphere gas supply pipe 20B, diffused and burned from the atmosphere gas discharge pipe 11B, and flows out to the front and rear atmosphere partitions 7 and 8. The atmosphere gas in the nitriding zone 5 is supplied from the atmosphere gas supply pipe 20C, diffused and combusted from the atmosphere gas discharge pipe 11C, and flows out to the front and rear atmosphere partitions 8 and 9.

冷却帯6の雰囲気ガスは、雰囲気ガス供給管20Dより供給され、前部の雰囲気仕切り9に流出するとともに、炉出口より放散される。   The atmosphere gas in the cooling zone 6 is supplied from the atmosphere gas supply pipe 20D, flows out to the atmosphere partition 9 at the front, and is dissipated from the furnace outlet.

また、各雰囲気仕切り7〜9からは、雰囲気ガス排出管11E〜Gを通して、雰囲気ガスが放散燃焼している。なお、各雰囲気仕切りの炉圧は、前後の処理帯より一定値だけ低くなるよう設定され、これを維持するよう、各雰囲気ガス排出管11A〜C、E〜Gから雰囲気ガスが放散燃焼されている。   In addition, atmospheric gas is diffused and burned from the atmospheric partitions 7 to 9 through the atmospheric gas discharge pipes 11E to 11G. In addition, the furnace pressure of each atmosphere partition is set to be lower by a certain value than the preceding and following processing zones, and the atmosphere gas is diffused and burned from each atmosphere gas discharge pipe 11A to 11C, EG to maintain this. Yes.

特許文献1には、連続脱炭・窒化焼鈍設備からガス回収することが開示されている。この場合、窒化炉およびその前後炉から回収された雰囲気ガスは、全量、NH3分解装置を通して残留NH3を分解し、さらに、雰囲気ガス生成装置で精製後、連続脱炭・窒化焼鈍設備に還流される。 Patent Document 1 discloses gas recovery from a continuous decarburization / nitridation annealing facility. In this case, the entire atmospheric gas recovered from the nitriding furnace and its front and rear furnaces is decomposed into residual NH 3 through an NH 3 decomposition device, and further refined with an atmospheric gas generator, and then returned to a continuous decarburization / nitriding annealing facility. Is done.

特開平10−212527号公報JP-A-10-212527

図3に示す従来の方向性珪素鋼板の脱炭・窒化焼鈍工程では、使用された雰囲気ガスは炉外に放散燃焼されるので、高い雰囲気コストを余儀なくされている。雰囲気コスト削減のため、雰囲気ガス量の低減化が試みられたが、しばしば、窒化不良、または、磁性不良を招くとともに、これらの不良改善に、多大の時間と費用を費やさざるを得なかった。   In the conventional decarburization / nitridation annealing process of the directional silicon steel sheet shown in FIG. 3, the atmosphere gas used is diffused and burned out of the furnace, which necessitates a high atmosphere cost. In order to reduce the atmospheric cost, attempts have been made to reduce the amount of atmospheric gas. However, it often causes nitriding defects or magnetic defects, and much time and cost must be spent on improving these defects.

特許文献1で開示されている連続脱炭・窒化焼鈍設備は、窒化炉およびその前後炉から回収された雰囲気ガスが、全量、NH3分解装置を通り、残留NH3が熱分解された後、さらに、雰囲気ガス生成装置で精製され、連続脱炭・窒化焼鈍設備に雰囲気ガスが還流されるような大規模設備である。 In the continuous decarburization / nitridation annealing facility disclosed in Patent Document 1, all of the atmospheric gas recovered from the nitriding furnace and its front and rear furnaces passes through the NH 3 decomposition apparatus, and the residual NH 3 is thermally decomposed. Furthermore, it is a large-scale facility that is refined by an atmospheric gas generator and the atmospheric gas is refluxed to a continuous decarburization / nitridation annealing facility.

すなわち、特許文献1開示の連続脱炭・窒化焼鈍設備は、ガス回収・精製に必要な設備が巨大となり、設備費も非常に高価となり、巨大な熱処理設備にしか適用が困難なものである。   That is, the continuous decarburization / nitridation annealing facility disclosed in Patent Document 1 requires a large amount of equipment necessary for gas recovery and refining, and the equipment cost is very high, making it difficult to apply only to a large heat treatment equipment.

そこで、本発明は、上述した従来の脱炭・窒化焼鈍工程が持っている課題に鑑み、大小すべての熱処理設備において、雰囲気ガスを安価に供給することができるとともに、高位に品質が安定した製品を供給することができる方向性珪素鋼板の製造方法および方向性珪素鋼板の連続脱炭・窒化焼鈍設備を提供することを目的とする。   Therefore, in view of the problems of the above-described conventional decarburization / nitridation annealing process, the present invention can supply atmospheric gas at a low price in both large and small heat treatment facilities and has a high quality stable product. It aims at providing the manufacturing method of the grain-oriented silicon steel plate which can supply, and the continuous decarburization and nitriding annealing equipment of a grain-oriented silicon steel plate.

本発明の要旨は、以下の(1)〜(4)の通りである。   The gist of the present invention is as follows (1) to (4).

(1) Si:2.0〜4.8質量%、インヒビタ成分を含み、残部鉄および不可避的不純物からなる珪素鋼板の熱延鋼帯を、焼鈍するかまたは焼鈍することなく、その後、1回または中間焼鈍を含む2回以上の冷間圧延を行って所定の板厚とし、次いで、脱炭工程を含む一次再結晶焼鈍および窒化焼鈍を行い、さらに、焼鈍分離材を塗布して仕上焼鈍を施す、方向性珪素鋼板の製造方法において、
(i)前記脱炭工程を含む一次再結晶焼鈍および窒化焼鈍を行う際、窒化焼鈍を行う窒化帯または窒化帯の前後の雰囲気仕切り内から炉の雰囲気ガスを回収して脱水し、H2、不活性ガスを主成分とし、NH3を1vol%(ドライガス換算)未満含む再生雰囲気ガスを生産し、
(ii)該再生雰囲気ガスを供給した後の窒化帯の雰囲気が、H2濃度:25vol%(ドライガス換算)以上、NH3:0.1〜10vol%(ドライガス換算)、露点:10℃以下、残部不活性ガスになるように、前記再生雰囲気ガスに不活性ガス、NH3、H20を加えて成分調整してから、窒化帯に供給する
ことを特徴とする方向性珪素鋼板の製造方法。
(1) Si: 2.0 to 4.8% by mass, including an inhibitor component, the hot-rolled steel strip of a silicon steel plate composed of the remaining iron and inevitable impurities is annealed or annealed once thereafter. Or, cold rolling at least twice including intermediate annealing is performed to a predetermined thickness, then primary recrystallization annealing and nitriding annealing including decarburization process are performed, and further, annealing separator is applied to finish annealing. In a method for producing a grain-oriented silicon steel sheet,
(I) When performing primary recrystallization annealing and nitriding annealing including the decarburization step, the atmosphere gas in the furnace is recovered from the nitriding zone where the nitriding annealing is performed or the atmosphere partition before and after the nitriding zone, and dehydrated, H 2 , Producing a regenerative atmosphere gas containing an inert gas as a main component and containing NH 3 in an amount of less than 1 vol% (in terms of dry gas),
(Ii) The atmosphere of the nitriding zone after supplying the regeneration atmosphere gas is H 2 concentration: 25 vol% (in terms of dry gas) or more, NH 3 : 0.1 to 10 vol% (in terms of dry gas), dew point: 10 ° C. Hereinafter, the directional silicon steel sheet is supplied to the nitriding zone after adjusting the components by adding an inert gas, NH 3 , H 2 0 to the regeneration atmosphere gas so that the remaining inert gas becomes an inert gas. Production method.

(2) 前記窒化帯に供給した後の残余の再生雰囲気ガスを、NH3熱分解・精整した後、H2含有ガス、不活性ガスおよびH2Oを加えて成分調整し、窒化帯を除く1個以上の処理帯に供給することを特徴とする上記(1)に記載の方向性珪素鋼板の製造方法。 (2) After the remaining regeneration atmosphere gas supplied to the nitriding zone is thermally decomposed and refined with NH 3 , H 2 -containing gas, inert gas and H 2 O are added to adjust the components, The method for producing a grain-oriented silicon steel sheet according to the above (1), wherein the steel sheet is supplied to one or more treatment zones except for the above.

(3) 方向性珪素鋼板の連続脱炭・窒化焼鈍設備において、窒化焼鈍を行う窒化帯または窒化帯前後の雰囲気仕切り内から回収した使用済み雰囲気ガスを脱水し、NH3を1vol%(ドライガス換算)未満含む再生雰囲気ガスを生産する脱水装置を配設するとともに、再生雰囲気ガスにNH3、不活性ガスおよびH2Oを加えて成分調整する窒化帯向けの雰囲気ガス成分調整装置を配設したことを特徴とする方向性珪素鋼板の連続脱炭・窒化焼鈍設備。 (3) In a continuous decarburization / nitridation annealing facility for grain-oriented silicon steel sheets, used atmosphere gas recovered from the nitriding zone for nitriding annealing or the atmosphere partition before and after the nitriding zone is dehydrated, and NH 3 is 1 vol% (dry gas In addition to a dehydration device that produces a regeneration atmosphere gas containing less than the equivalent), an atmosphere gas component adjustment device for the nitriding zone that adjusts the composition by adding NH 3 , inert gas and H 2 O to the regeneration atmosphere gas A continuous decarburization and nitridation annealing facility for grain oriented silicon steel sheets.

(4) 前記窒化帯に供給した後の残余の再生雰囲気ガス中のNH3を熱分解・精整するNH3熱分解・精整装置を配設し、熱分解・精製後にH2含有ガス、不活性ガスおよびH2Oを加えて成分調整する窒化帯を除く1個以上の処理帯向けの雰囲気ガス成分調整装置を配設したことを特徴とする上記(3)に記載の方向性珪素鋼板の連続脱炭・窒化焼鈍設備。 (4) An NH 3 thermal decomposition / refining device for thermally decomposing / refining NH 3 in the remaining regeneration atmosphere gas after being supplied to the nitriding zone is provided, and an H 2 -containing gas after thermal decomposition / refining, The grain oriented silicon steel sheet according to (3) above, wherein an atmosphere gas component adjusting device for one or more treatment zones excluding the nitriding zone for adjusting the components by adding an inert gas and H 2 O is provided. Continuous decarburization and nitriding annealing equipment.

本発明によれば、雰囲気ガスを安価に供給することができるとともに、極めて安定して、方向性珪素鋼板を製造することが可能となる。   According to the present invention, an atmospheric gas can be supplied at a low cost, and a grain-oriented silicon steel sheet can be manufactured extremely stably.

雰囲気ガスの炉内でのガス濃度を詳細に調査したところ、窒化帯では、主に、NH3が分解して、H2とN2に変わり、一部H2が、鋼板の地鉄の酸化物を還元して、H2Oが若干増加することが判明した。なお、還元帯の雰囲気の露点は、窒化帯の露点より低くないのが一般的である。 When the gas concentration in the furnace of the atmospheric gas was investigated in detail, in the nitriding zone, NH 3 was mainly decomposed and changed to H 2 and N 2 , and part of the H 2 was oxidized of the steel plate. The product was reduced and H 2 O was found to increase slightly. Note that the dew point of the reducing zone atmosphere is generally not lower than the dew point of the nitriding zone.

これらのH2、N2、H2O、NH3の内で、窒化帯での使用の障害となるガス成分は、残留H2Oのみである。また、加熱・均熱帯での使用の障害となるガス成分は、NH3のみであり、また、加熱・均熱帯および窒化帯以外の処理帯での使用の障害となるガス成分は、NH3、H2Oのみである。その他の雰囲気ガス成分は、使用済み雰囲気ガスの各組成の濃度を分析し、不足分を補充することで、再使用可能である。 Of these H 2 , N 2 , H 2 O, and NH 3 , the only gas component that hinders use in the nitriding zone is residual H 2 O. The gas component as a failure of use in heating and soaking zone is, NH 3 is only, also a gas component as a failure of use in heating and soaking zone and treatment zone other than the nitride band, NH 3, Only H 2 O. Other atmospheric gas components can be reused by analyzing the concentration of each composition of the used atmospheric gas and replenishing the shortage.

図1に、本発明の連続脱炭・窒化焼鈍設備の一例を示す。炉2は、加熱・均熱帯3、還元帯4、窒化帯5、冷却帯6、および、それらの処理帯間の雰囲気仕切り7〜9から構成されている。   FIG. 1 shows an example of the continuous decarburizing / nitriding annealing equipment of the present invention. The furnace 2 includes a heating / soaking zone 3, a reduction zone 4, a nitriding zone 5, a cooling zone 6, and atmosphere partitions 7 to 9 between these treatment zones.

加熱・均熱帯3の後方の雰囲気ガス供給管20Aから炉内に供給された雰囲気ガスは、鋼板1と対向して進行し、大半は、炉の前部に至り、雰囲気ガス排出管11Aから炉外に排出されるが、一部は、炉入口から放散されるとともに、雰囲気仕切り7へ流出する。なお、雰囲気ガスが炉の前部に流れるにつれ、H2Oが消費されて減少するとともに、COxが増加する。 The atmospheric gas supplied into the furnace from the atmospheric gas supply pipe 20A at the rear of the heating / soaking zone 3 proceeds in opposition to the steel plate 1, most of which reaches the front of the furnace and is supplied from the atmospheric gas discharge pipe 11A to the furnace. Although it is discharged outside, a part of it is diffused from the furnace inlet and flows out to the atmosphere partition 7. Note that as the atmospheric gas flows to the front of the furnace, H 2 O is consumed and reduced, and CO x increases.

還元帯4の雰囲気ガスは、雰囲気ガス供給管20Bより供給され、雰囲気ガス排出管11Bより排出されるとともに、前後の雰囲気仕切り7、8へ流出する。窒化帯5に雰囲気ガス供給管20Cから供給される雰囲気ガスは、雰囲気ガス排出管11Cから炉外に排出されるとともに、前後の雰囲気仕切り8、9へ流出する。   The atmosphere gas in the reduction zone 4 is supplied from the atmosphere gas supply pipe 20B, discharged from the atmosphere gas discharge pipe 11B, and flows out to the front and rear atmosphere partitions 7 and 8. The atmospheric gas supplied from the atmospheric gas supply pipe 20C to the nitriding zone 5 is discharged out of the furnace from the atmospheric gas discharge pipe 11C and flows out to the front and rear atmospheric partitions 8 and 9.

冷却帯6の雰囲気ガスは、雰囲気ガス供給管20Dより供給され、前部の雰囲気仕切り9に流出するとともに、炉出口より放散される。また、各雰囲気仕切り7〜9からは、雰囲気ガス排出管11E〜Gを通して、雰囲気ガスが排出される。各雰囲気仕切りの炉圧は、前後の処理帯より一定値だけ低くなるよう設定され、これを維持するよう、各雰囲気ガス排出管11A〜C、E〜Gから雰囲気ガスが排出される。   The atmosphere gas in the cooling zone 6 is supplied from the atmosphere gas supply pipe 20D, flows out to the atmosphere partition 9 at the front, and is dissipated from the furnace outlet. Moreover, atmospheric gas is discharged | emitted from each atmospheric partition 7-9 through atmospheric gas discharge pipe 11E-G. The furnace pressure of each atmosphere partition is set to be lower than the front and rear treatment zones by a certain value, and the atmosphere gas is discharged from each atmosphere gas discharge pipe 11A-C, EG to maintain this.

なお、窒化帯では、鋼帯の表面が若干還元され、それに伴い、雰囲気中のH2濃度は、若干減少するが、ごく微量であり、酸化ポテンシアル{P(H2O)/P(H2)}に影響を与えるほどではない。 In the nitriding zone, the surface of the steel strip is slightly reduced, and accordingly, the H 2 concentration in the atmosphere is slightly reduced, but is very small, and the oxidation potential {P (H 2 O) / P (H 2 )}.

一方、排出管11Fから排出される雰囲気ガスは、NH3を含有するとともに、その露点は、一般的には、窒化帯の露点より高い。また、排出管11Gから排出される雰囲気ガスは、NH3を含有し、その露点は、一般的には、窒化帯の露点より低い。 On the other hand, the atmospheric gas discharged from the discharge pipe 11F contains NH 3 and its dew point is generally higher than the dew point of the nitriding zone. Further, the atmospheric gas discharged from the discharge pipe 11G contains NH 3 , and its dew point is generally lower than the dew point of the nitriding zone.

上記3系統の雰囲気ガス排出管11C、F、Gから排出されるNH3含有ガスは、集合された後、フィルタ21で、炉からの飛散物が除去され、脱水装置22に導かれ、H2Oが除去される。 After the NH 3 -containing gas discharged from the three atmospheric gas discharge pipes 11C, F, and G is collected, the scattered matter from the furnace is removed by the filter 21 and guided to the dehydrating device 22, and H 2 O is removed.

脱水に、特に難しい条件はなく、H2Oが除去され、窒化帯の雰囲気の露点より低ければよく、吸着方式でも、その他の方式でもよい。例えば、吸着方式の場合では、吸着剤としては、アルカリに反応しないものであれば、特に特定されるものではない。また、冷却方式の脱水装置でもかまわない。窒化帯の雰囲気の露点より、回収雰囲気温度を冷却してやればよい。また、圧力を上げる方法をとることで、回収雰囲気ガスの冷却温度を低減することも可能である。 There is no particularly difficult condition for dehydration, and it is sufficient that H 2 O is removed and the dew point of the nitriding zone atmosphere is lower, and an adsorption method or other methods may be used. For example, in the case of the adsorption method, the adsorbent is not particularly specified as long as it does not react with alkali. Also, a cooling type dehydrator may be used. The recovered atmosphere temperature may be cooled from the dew point of the nitriding zone atmosphere. Further, the cooling temperature of the recovered atmospheric gas can be reduced by taking a method of increasing the pressure.

脱水装置22で脱水された再生雰囲気ガスは、ガス分析装置26でガス成分の濃度が分析され、雰囲気ガス成分調整装置19Cで、不足するNH3、H2O、および、必要に応じ不活性ガスが補充され、窒化帯5に供給される。また、余剰の再生ガスは、放散・燃焼される。なお、上記回路中には、雰囲気ガス循環装置13が配設され、雰囲気ガスの循環・脱水に必要な駆動力を付与している。 The regeneration atmosphere gas dehydrated by the dehydrator 22 is analyzed for the concentration of gas components by the gas analyzer 26, and the lacking NH 3 , H 2 O and, if necessary, inert gas by the atmosphere gas component adjuster 19C. Is replenished and supplied to the nitriding zone 5. Excess regeneration gas is diffused and burned. In the circuit, an atmospheric gas circulation device 13 is provided to apply a driving force necessary for the circulation and dehydration of the atmospheric gas.

本発明に使用するフィルタは、ステンレス等の非酸化性の金属を微細繊維としたものを織物とし、さらに、焼結して作られた素材を襞をもたせて加工したフィルタが、高温でも安全であることから、好ましいが、耐熱性とフィルタ能力のあるものであれば、他の構造のものでも支障はない。   The filter used in the present invention is made of a non-oxidizing metal such as stainless steel made of fine fibers, and a filter made by sintering a material made by sintering with a wrinkle is safe even at high temperatures. For this reason, it is preferable, but other structures can be used as long as they have heat resistance and filter ability.

本発明に係る方向性珪素鋼板は、Si:2.0〜4.8質量%、さらに、方向性珪素鋼板製造に必要なインヒビタ成分を含み、残部Feおよび不可避的不純物からなるものである。その他の成分は、特に規定しない。   The grain-oriented silicon steel sheet according to the present invention comprises Si: 2.0 to 4.8% by mass, and further contains an inhibitor component necessary for producing the grain-oriented silicon steel sheet, and is composed of the remaining Fe and inevitable impurities. Other components are not particularly defined.

Siは、電気抵抗を高め鉄損を下げるうえで重要であるが、その含有量が4.8質量%超では、冷間圧延時に、割れが発生し易くなる。一方、2.0質量%未満では、電気抵抗が低く、鉄損を下げるうえで問題がある。   Si is important for increasing electric resistance and lowering iron loss, but if its content exceeds 4.8% by mass, cracking is likely to occur during cold rolling. On the other hand, if it is less than 2.0% by mass, the electrical resistance is low, and there is a problem in reducing iron loss.

インヒビタ成分としては、Mn、S、Al、N、Se、Sn、B、Bi、Nb、Ti、P、がある。   Inhibitor components include Mn, S, Al, N, Se, Sn, B, Bi, Nb, Ti, and P.

Si:2.0〜4.8質量%、および、方向性珪素鋼板の製造に必要なインヒビタ成分を含み、残部Feおよび不可避的不純物からなる溶鋼を、通常の工程で、例えば、連続鋳造して、熱延鋼板または熱延鋼帯とする。この熱延鋼板または熱延鋼帯に、750〜1200℃の温度域で30秒〜30分間、磁束密度向上のための焼鈍を施し、または、施さず、次いで、これらの熱延鋼板または熱延鋼帯を冷間圧延する。   Si: 2.0 to 4.8% by mass, and a molten steel containing an inhibitor component necessary for the production of the grain-oriented silicon steel sheet, and the balance Fe and unavoidable impurities are continuously cast in a normal process, for example, , Hot-rolled steel sheet or hot-rolled steel strip. This hot-rolled steel sheet or hot-rolled steel strip is subjected to annealing for improving the magnetic flux density in a temperature range of 750 to 1200 ° C. for 30 seconds to 30 minutes or not, and then these hot-rolled steel sheet or hot-rolled steel strip Cold-roll the steel strip.

冷間圧延は、最終冷間圧延率50%以上、望ましくは、特開2003−3215号公報に開示されているように、80%以上とする。冷間圧延後の材料を、連続脱炭・窒化焼鈍設備に入れる。   The cold rolling is performed at a final cold rolling rate of 50% or more, desirably 80% or more as disclosed in Japanese Patent Application Laid-Open No. 2003-3215. The material after cold rolling is put into a continuous decarburizing / nitriding annealing facility.

まず、鋼板温度800〜850℃で脱炭焼鈍を行う。この時、炉に供給する雰囲気ガスの組成は、H2:25vol%(ドライガス換算)以上、望ましくは、75vol%(ドライガス換算)、露点:50〜75℃、残部不活性ガスとする。 First, decarburization annealing is performed at a steel plate temperature of 800 to 850 ° C. At this time, the composition of the atmospheric gas supplied to the furnace is H 2 : 25 vol% (in terms of dry gas) or more, preferably 75 vol% (in terms of dry gas), dew point: 50 to 75 ° C., and the balance inert gas.

次に、鋼板温度:800〜850℃で還元焼鈍を行う。炉に供給する雰囲気ガスの組成は、H2:25vol%(ドライガス換算)以上、望ましくは、75vol%(ドライガス換算)、露点:45℃以下、残部不活性ガスとする。 Next, reduction annealing is performed at a steel plate temperature of 800 to 850 ° C. The composition of the atmospheric gas supplied to the furnace is H 2 : 25 vol% (in terms of dry gas) or more, preferably 75 vol% (in terms of dry gas), dew point: 45 ° C. or less, and the remaining inert gas.

次いで、鋼板温度:700〜800℃で窒化焼鈍を行う。窒化帯の雰囲気は、NH3:0.1〜10vol%(ドライガス換算)、H2:25vol%(ドライガス換算)以上、望ましくは、65vol%(ドライガス換算)超、露点:10℃以下、残部不活性ガスの雰囲気とする。 Next, nitriding annealing is performed at a steel plate temperature of 700 to 800 ° C. The atmosphere of the nitriding zone is NH 3 : 0.1 to 10 vol% (in terms of dry gas), H 2 : 25 vol% (in terms of dry gas) or more, preferably over 65 vol% (in terms of dry gas), dew point: 10 ° C. or less The atmosphere of the remaining inert gas is used.

図2に、本発明の連続脱炭・窒化焼鈍設備の別の一例を示す。図1との違いは、窒化帯5に供給した残余の雰囲気ガスを放散燃焼させることなく、NH3分解・精整装置23で残存NH3を熱分解・精製し、分析装置27で雰囲気ガス成分を分析し、雰囲気成分調整装置19A、19Bで、不足するH2源ガス、不活性ガスおよびH2Oを調整し、加熱・均熱帯3および還元帯4に供給していることである。 FIG. 2 shows another example of the continuous decarburizing / nitriding annealing equipment of the present invention. The difference from FIG. 1 is that residual NH 3 supplied to the nitriding zone 5 is not diffused and burned, and the remaining NH 3 is thermally decomposed and purified by the NH 3 decomposition / refining device 23, and the atmospheric gas components are analyzed by the analyzer 27. The deficient H 2 source gas, inert gas and H 2 O are adjusted by the atmospheric component adjusting devices 19A and 19B and supplied to the heating / soaking zone 3 and the reduction zone 4.

この例では、窒化帯、または、窒化帯の前後の雰囲気仕切りから流出するNH3を含む雰囲気ガスは、全て、回収・再使用されており、環境汚染の危惧は解消されている。 In this example, all of the nitriding zone or the atmospheric gas containing NH 3 flowing out from the atmosphere partition before and after the nitriding zone has been recovered and reused, thereby eliminating the fear of environmental pollution.

こうして脱炭し、さらに、窒化した鋼板または鋼帯を、MgOを主成分とする焼鈍分離材を塗布して、仕上焼鈍炉に入れ、920〜1150℃に到達後、5時間以上保持して2次再結晶し、その後、純化のため1200℃まで昇温し、この温度に10時間以上保持する。仕上焼鈍終了後、必要に応じて磁区細分化処理を含む張力コーティングを行う。   The steel sheet or steel strip thus decarburized and further coated with an annealing separator mainly composed of MgO is put into a finish annealing furnace, and after reaching 920 to 1150 ° C., it is held for 5 hours or more and 2 Next, recrystallization is performed, and then the temperature is raised to 1200 ° C. for purification, and this temperature is maintained for 10 hours or more. After finish annealing, tension coating including magnetic domain refinement is performed as necessary.

Si:3.2質量%、酸可溶性Al:0.029質量%、N:0.065質量%、Mn:0.12質量%、S:0.008質量%、C:0.05質量%を含み、残部Feおよび不可避的不純物からなる珪素鋼板の熱延鋼帯を、1100℃で2分間焼鈍した後、冷延し、0.23mm厚とした。   Si: 3.2% by mass, acid-soluble Al: 0.029% by mass, N: 0.065% by mass, Mn: 0.12% by mass, S: 0.008% by mass, C: 0.05% by mass In addition, the hot-rolled steel strip of the silicon steel plate including the remaining Fe and inevitable impurities was annealed at 1100 ° C. for 2 minutes and then cold-rolled to a thickness of 0.23 mm.

本発明例1では、窒素帯に、当初、アンモニア分解ガス(H2:75vol%、N2:25vol%、いずれもドライガス換算):200m3/hr、NH3:100m3/hrを、露点0℃として、ガス供給管から炉へ補給した。窒化帯および前後の雰囲気仕切りから雰囲気ガスを回収し、脱水装置で回収雰囲気ガスを冷却し、脱水し、露点0℃とした後、再び、NH3を加え調整後、窒素帯に循環させた。 In Example 1 of the present invention, ammonia decomposing gas (H 2 : 75 vol%, N 2 : 25 vol%, both in terms of dry gas): 200 m 3 / hr, NH 3 : 100 m 3 / hr at the beginning of the dew point in the nitrogen band The furnace was replenished from the gas supply pipe at 0 ° C. The atmosphere gas was recovered from the nitriding zone and the front and rear atmosphere partitions, and the recovered atmosphere gas was cooled and dehydrated with a dehydrator, dehydrated to 0 ° C., adjusted again with NH 3, and then circulated through the nitrogen zone.

それに伴い、アンモニア分解ガスの供給を漸減し、最終的には、零とした。なお、加熱・均熱帯には、アンモニア分解ガス(H2:75vol%、N2:25vol%、いずれもドライガス換算)を、露点69℃として、ガス供給管から供給した。また、還元帯には、アンモニア分解ガス(H2:75vol%、N2:25vol%、いずれもドライガス換算)を、露点35℃として、ガス供給管から供給した。 Along with this, the supply of ammonia decomposition gas was gradually reduced to zero. For heating and soaking, ammonia decomposition gas (H 2 : 75 vol%, N 2 : 25 vol%, both in terms of dry gas) was supplied from a gas supply pipe with a dew point of 69 ° C. Further, ammonia decomposition gas (H 2 : 75 vol%, N 2 : 25 vol%, both in terms of dry gas) was supplied to the reduction zone from the gas supply pipe with a dew point of 35 ° C.

そのなかで鋼板を通板し、鋼板温度830℃で2分間焼鈍するとともに、還元帯で鋼板表面の処理を行い、最後に2次再結晶を安定させるために、アンモニア雰囲気中で窒化処理を行い、鋼板の窒素量の目標を200質量ppmとし、インヒビタを強化した後、アンモニア分解ガス雰囲気で冷却した。   In this process, a steel plate is passed through, annealed at a steel plate temperature of 830 ° C. for 2 minutes, treated with a reduction zone, and finally subjected to nitriding treatment in an ammonia atmosphere to stabilize secondary recrystallization. The target of the nitrogen amount of the steel sheet was set to 200 mass ppm, the inhibitor was strengthened, and then cooled in an ammonia decomposition gas atmosphere.

本発明例2では、回収し、脱水した雰囲気ガスを窒化帯に供給した後の残余のガスを、NH3分解・精製し、再利用した。雰囲気条件は、本発明例1と同じである。 In Example 2 of the present invention, the remaining gas after supplying the recovered and dehydrated atmospheric gas to the nitriding zone was decomposed and purified by NH 3 and reused. The atmospheric conditions are the same as those of Example 1 of the present invention.

比較例11、12では、窒化帯にガス供給管から、各々、アンモニア分解ガス(H2:75vol%、N2:25vol%、いずれもドライガス換算):100、150m3/hrおよびNH3:70、60m3/hrを、露点0℃として、供給し、鋼板の窒素量の目標を200質量ppmとした。加熱・均熱帯、還元帯への雰囲気供給は、本発明例と同じである。 In Comparative Examples 11 and 12, from the gas supply pipe to the nitriding zone, ammonia decomposition gas (H 2 : 75 vol%, N 2 : 25 vol%, both in terms of dry gas): 100, 150 m 3 / hr and NH 3 : 70 and 60 m 3 / hr were supplied at a dew point of 0 ° C., and the target of the amount of nitrogen in the steel sheet was 200 mass ppm. Heating, soaking, and atmosphere supply to the reduction zone are the same as in the example of the present invention.

その後、本発明例、比較例ともに、MgOを主成分とする焼鈍分離材を塗布し、高温焼鈍した。高温焼鈍では、1100℃まで、10vol%N2−90vol%H2雰囲気で、150℃/hrの昇温速度を保ちながら昇温し、1100℃到達後、その温度で、10時間保持した。 Thereafter, in both the inventive examples and the comparative examples, an annealing separator mainly composed of MgO was applied and subjected to high temperature annealing. In the high temperature annealing, the temperature was increased to 1100 ° C. in a 10 vol% N 2 -90 vol% H 2 atmosphere while maintaining a temperature increase rate of 150 ° C./hr, and after reaching 1100 ° C., the temperature was maintained for 10 hours.

その後、100vol%H2雰囲気とし、さらに、1200℃まで昇温し、この温度に10時間保持した。仕上焼鈍終了後、リン酸−クロム酸系の張力コーティング処理を行った。得られた特性および皮膜状況は表1の通りである。 Thereafter, the atmosphere was 100 vol% H 2 , the temperature was further raised to 1200 ° C., and the temperature was maintained for 10 hours. After finishing annealing, phosphoric acid-chromic acid type tension coating treatment was performed. Table 1 shows the obtained characteristics and coating conditions.

Figure 2008261033
Figure 2008261033

表1から明らかなように、本発明例では、雰囲気ガスを安価に、供給できるとともに、磁性および皮膜を含めて、製品品質が高位のレベルで安定した。   As is apparent from Table 1, in the present invention example, the atmospheric gas can be supplied at a low cost, and the product quality including the magnetism and the film is stabilized at a high level.

本発明の連続脱炭・窒化焼鈍設備の一例を示す図である。It is a figure which shows an example of the continuous decarburization and nitridation annealing equipment of this invention. 本発明の連続脱炭・窒化焼鈍設備の他の一例を示す図である。It is a figure which shows another example of the continuous decarburization and nitridation annealing equipment of this invention. 従来の連続脱炭・窒化焼鈍設備の一例を示す図である。It is a figure which shows an example of the conventional continuous decarburization and nitridation annealing equipment.

符号の説明Explanation of symbols

1 鋼帯
2 炉
3 加熱・均熱帯
4 還元帯
5 窒化帯
6 冷却帯
7〜9 雰囲気仕切り
11A〜C、E〜G 雰囲気ガス排出管
12C、F 雰囲気ガス排出管バルブ
13 雰囲気ガス循環装置
18A〜B 回収雰囲気ガス供給管バルブ
19A〜C 雰囲気ガス成分調整装置
20A〜D 雰囲気ガス供給管
21 フィルタ
22 脱水装置
23 NH3熱分解・精整装置
26、27 ガス分析装置
33 H2源ガス供給管
34A〜D H2源ガス供給管バルブ
35 H2O源ガス供給管
36A、B H2O源ガス供給管バルブ
37 NH3ガス供給管
38 NH3ガス供給管バルブ
X 鋼板均熱温度到達点
DESCRIPTION OF SYMBOLS 1 Steel strip 2 Furnace 3 Heating and soaking zone 4 Reduction zone 5 Nitriding zone 6 Cooling zone 7-9 Atmosphere partition 11A-C, E-G Atmospheric gas exhaust pipe 12C, F Atmospheric gas exhaust pipe valve 13 Atmospheric gas circulation device 18A- B Recovery atmospheric gas supply pipe valve 19A to C Atmospheric gas component adjustment apparatus 20A to D Atmospheric gas supply pipe 21 Filter 22 Dehydration apparatus 23 NH 3 pyrolysis and refining apparatus 26, 27 Gas analyzer 33 H 2 source gas supply pipe 34A ˜DH 2 source gas supply pipe valve 35 H 2 O source gas supply pipe 36A, B H 2 O source gas supply pipe valve 37 NH 3 gas supply pipe 38 NH 3 gas supply pipe valve X Steel plate soaking temperature reaching point

Claims (4)

Si:2.0〜4.8質量%、インヒビタ成分を含み、残部鉄および不可避的不純物からなる珪素鋼板の熱延鋼帯を、焼鈍するかまたは焼鈍することなく、その後、1回または中間焼鈍を含む2回以上の冷間圧延を行って所定の板厚とし、次いで、脱炭工程を含む一次再結晶焼鈍および窒化焼鈍を行い、さらに、焼鈍分離材を塗布して仕上焼鈍を施す方向性珪素鋼板の製造方法において、
(i)前記脱炭工程を含む一次再結晶焼鈍および窒化焼鈍を行う際、窒化焼鈍を行う窒化帯または窒化帯の前後の雰囲気仕切り内から炉の雰囲気ガスを回収して脱水し、H2、不活性ガスを主成分とし、NH3を1vol%(ドライガス換算)未満含む再生雰囲気ガスを生産し、
(ii)該再生雰囲気ガスを供給した後の窒化帯の雰囲気が、H2濃度:25vol%(ドライガス換算)以上、NH3:0.1〜10vol%(ドライガス換算)、露点:10℃以下、残部不活性ガスの雰囲気になるように、前記再生雰囲気ガスに、不活性ガス、NH3、H20を加えて成分調整してから、窒化帯に供給する
ことを特徴とする方向性珪素鋼板の製造方法。
Si: 2.0 to 4.8% by mass, including an inhibitor component, the hot-rolled steel strip of the silicon steel plate composed of the remaining iron and unavoidable impurities is annealed or annealed once or thereafter without annealing. The directionality which performs cold rolling of 2 times or more including, and makes it a predetermined plate thickness, then performs primary recrystallization annealing and nitriding annealing including a decarburization step, and further performs finish annealing by applying an annealing separator In the method for producing a silicon steel plate,
(I) When performing primary recrystallization annealing and nitriding annealing including the decarburization step, the atmosphere gas in the furnace is recovered from the nitriding zone where the nitriding annealing is performed or the atmosphere partition before and after the nitriding zone, and dehydrated, H 2 , Producing a regenerative atmosphere gas containing an inert gas as a main component and containing NH 3 in an amount of less than 1 vol% (in terms of dry gas),
(Ii) The atmosphere of the nitriding zone after supplying the regeneration atmosphere gas is H 2 concentration: 25 vol% (in terms of dry gas) or more, NH 3 : 0.1 to 10 vol% (in terms of dry gas), dew point: 10 ° C. In the following, a directionality is characterized in that an inert gas, NH 3 , and H 2 O are added to the regeneration atmosphere gas to adjust the components so that the remaining inert gas atmosphere is provided, and then supplied to the nitriding zone. A method for producing a silicon steel sheet.
前記窒化帯に供給した後の残余の再生雰囲気ガスを、NH3熱分解・精整した後、H2含有ガス、不活性ガスおよびH2Oを加えて成分調整し、窒化帯を除く1個以上の処理帯に供給することを特徴とする請求項1に記載の方向性珪素鋼板の製造方法。 The remaining regeneration atmosphere gas supplied to the nitriding zone is thermally decomposed and refined with NH 3 , then H 2 -containing gas, inert gas and H 2 O are added to adjust the components, and the nitriding zone is removed. The method for producing a grain-oriented silicon steel sheet according to claim 1, wherein the steel sheet is supplied to the treatment zone. 方向性珪素鋼板の連続脱炭・窒化焼鈍設備において、窒化焼鈍を行う窒化帯または窒化帯前後の雰囲気仕切り内から回収した使用済み雰囲気ガスを脱水し、NH3を1vol%(ドライガス換算)未満含む再生雰囲気ガスを生産する脱水装置を配設するとともに、再生雰囲気ガスにNH3、不活性ガスおよびH2Oを加えて成分調整する窒化帯向けの雰囲気ガス成分調整装置を配設したことを特徴とする方向性珪素鋼板の連続脱炭・窒化焼鈍設備。 In continuous decarburization / nitridation annealing equipment for grain-oriented silicon steel sheets, used atmosphere gas recovered from the nitriding zone for nitriding annealing or the atmosphere partition before and after the nitriding zone is dehydrated, and NH 3 is less than 1 vol% (in terms of dry gas) And a dehydrating device for producing a regenerating atmosphere gas including an atmosphere gas component adjusting device for a nitriding zone for adjusting components by adding NH 3 , an inert gas and H 2 O to the regenerating atmosphere gas. A feature of continuous decarburization and nitriding annealing equipment for directional silicon steel sheets. 前記窒化帯に供給した後の残余の再生雰囲気ガス中のNH3を熱分解・精整するNH3熱分解・精整装置を配設し、熱分解・精製後にH2含有ガス、不活性ガスおよびH2Oを加えて成分調整する窒化帯を除く1個以上の処理帯向けの雰囲気ガス成分調整装置を配設したことを特徴とする請求項3に記載の方向性珪素鋼板の連続脱炭・窒化焼鈍設備。 Wherein the NH 3 in the residual regeneration atmospheric gas after supplying the nitriding zone disposed the NH 3 Pyrolysis and finishing line equipment for thermal decomposition and finishing line, H 2 containing gas after the pyrolysis and purification, an inert gas 4. The continuous decarburization of grain-oriented silicon steel sheet according to claim 3, further comprising an atmosphere gas component adjusting device for one or more treatment zones excluding a nitriding zone for adjusting components by adding H 2 O. 5.・ Nitride annealing equipment.
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