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JP5353033B2 - Corrosion prevention method for exhaust gas cooler - Google Patents

Corrosion prevention method for exhaust gas cooler Download PDF

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JP5353033B2
JP5353033B2 JP2008065476A JP2008065476A JP5353033B2 JP 5353033 B2 JP5353033 B2 JP 5353033B2 JP 2008065476 A JP2008065476 A JP 2008065476A JP 2008065476 A JP2008065476 A JP 2008065476A JP 5353033 B2 JP5353033 B2 JP 5353033B2
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exhaust gas
gas cooler
vacuum degassing
horizontal
exhaust
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JP2009221508A (en
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和道 ▲吉▼田
敏之 和田
不二哉 野上
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Nippon Steel Corp
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Nippon Steel and Sumitomo Metal Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for preventing the corrosion of an exhaust gas cooler by which the corrosion of an exhaust gas cooler part is prevented by reducing NOx concentration incorporated in the exhaust gas at the preheating time with a simple structure, thereby reducing the maintenance cost of the exhaust gas cooler and extending the service life. <P>SOLUTION: An exhaust gas duct 12 is constituted of; a first horizontal part 12a whose one end is connected to the upper part of a vacuum-degassing vessel 10; an inclining part 12b whose one end is connected to another end of the first horizontal part 12a and which inclines in slanting lower part; and a second horizontal part 12c whose one end is connected to another end of the inclining part 12b and whose another end is connected to the exhaust gas cooler 11. A connection part between the first horizontal part 12a and the inclining part 12b is made to be a first bending part P1 having the bending angle &alpha;1 to the horizontal surface, and the connecting part of the inclining part 12b and the second horizontal part 12c, is made into a second bending part P2 having the bending angle &alpha;2 to the horizontal surface. Level difference D of the bending, is made to be &ge;1.0 and &lt;4.0 times of the inner diameter of the first horizontal part 12a, and the bending angles &alpha;1, &alpha;2, are defined as &lt;45&deg;. <P>COPYRIGHT: (C)2010,JPO&amp;INPIT

Description

本発明は、真空脱ガス処理において、真空脱ガス槽の予熱を行う際に発生する排ガス中に含まれるNOxに起因する排ガスクーラーの腐食を防止する方法に関する。 The present invention relates to a method for preventing corrosion of an exhaust gas cooler caused by NOx contained in exhaust gas generated when preheating a vacuum degassing tank in vacuum degassing treatment.

転炉において一次精錬が終了した溶鋼は、脱炭のため、又は水素や窒素などの溶存ガスの除去を目的として、真空脱ガス処理装置を用いて脱ガス処理が行われる。脱ガス処理では、真空脱ガス槽の下部(浸漬管)を取鍋内の溶鋼に浸漬させた後、真空脱ガス槽内が真空状態となるように真空脱ガス槽内のエアを吸引することにより、溶鋼が真空脱ガス槽内に吸い上げられ、溶鋼中のガス成分が真空脱ガス槽内に放出される。 The molten steel that has undergone primary refining in the converter is degassed using a vacuum degassing apparatus for decarburization or for the purpose of removing dissolved gases such as hydrogen and nitrogen. In the degassing treatment, after the lower part (immersion tube) of the vacuum degassing tank is immersed in the molten steel in the pan, the air in the vacuum degassing tank is sucked so that the vacuum degassing tank is in a vacuum state. Thus, the molten steel is sucked into the vacuum degassing tank, and the gas components in the molten steel are released into the vacuum degassing tank.

真空脱ガス槽は、溶鋼の脱ガス処理時には、溶鋼から受ける熱により高温となるが、待機時には温度が急激に低下する。真空脱ガス槽の温度が低下した状態で次の溶鋼を脱ガス処理した場合、スプラッシュや地金の付着が著しく、操業が阻害される原因となる。そのため、次の溶鋼の脱ガス処理に備えて、バーナー等の加熱手段を用いて真空脱ガス槽の予熱が行われる。 The vacuum degassing tank has a high temperature due to heat received from the molten steel at the time of degassing the molten steel, but the temperature rapidly decreases during standby. When the next molten steel is degassed in a state where the temperature of the vacuum degassing tank is lowered, the adhesion of the splash and the metal is remarkable, which causes the operation to be hindered. Therefore, in preparation for the next degassing treatment of molten steel, the vacuum degassing tank is preheated using a heating means such as a burner.

真空脱ガス槽の予熱に関連する技術として、特許文献1には、真空脱ガス槽から排ガスを排ガスクーラーに導くための排ガスダクトの真空脱ガス槽直近位置に遮断弁を設けたことを特徴とする真空脱ガス槽の保温装置の発明が開示されている。 As a technique related to preheating of the vacuum degassing tank, Patent Document 1 is characterized in that a shut-off valve is provided in the position immediately adjacent to the vacuum degassing tank of the exhaust gas duct for guiding the exhaust gas from the vacuum degassing tank to the exhaust gas cooler. An invention of a heat retaining device for a vacuum degassing tank is disclosed.

また、特許文献2には、槽本体の上部に排気管が接続され、槽本体の下部に浸漬管が取り付けられた真空脱ガス槽において、排気管の下部内壁が槽本体から遠ざかるにつれて低く大きくなるように傾斜させる技術が開示されている。 Further, in Patent Document 2, in a vacuum degassing tank in which an exhaust pipe is connected to the upper part of the tank body and a dip pipe is attached to the lower part of the tank body, the lower inner wall of the exhaust pipe becomes lower and larger as it moves away from the tank body. Thus, a technique for inclining is disclosed.

特公平6−89395号公報Japanese Patent Publication No. 6-89395 特開2004−68060号公報JP 2004-68060 A

しかしながら、特許文献1に記載された保温装置では、排ガスダクトに遮断弁を取り付ける必要があるため、予熱時に熱により遮断弁が損傷しやすく、遮断弁のメンテナンス費用が嵩む問題がある。また、予熱時の排ガスが、高熱下で損傷した遮断弁からリークして排ガスダクト内に進入し、排ガスクーラーの腐食を招く原因となるという問題がある。
一方、特許文献2に記載された真空脱ガス槽の場合、輻射熱で加熱される排気管の面積が大きくなるため、排気管を構成する耐火物が損傷して排気管の寿命が低下するという問題がある。また、排気管の構造が複雑となるので、製造コストが高くなる。加えて、排気管に流入するスプラッシュが傾斜面を流下して下部に堆積するので、堆積した地金の除去に手間が掛かるという問題もある。
However, in the heat retaining device described in Patent Document 1, since it is necessary to attach a shut-off valve to the exhaust gas duct, there is a problem that the shut-off valve is easily damaged by heat during preheating and the maintenance cost of the shut-off valve increases. Further, there is a problem that the exhaust gas during preheating leaks from the shut-off valve damaged under high heat and enters the exhaust gas duct, causing corrosion of the exhaust gas cooler.
On the other hand, in the case of the vacuum degassing tank described in Patent Document 2, since the area of the exhaust pipe heated by radiant heat increases, the refractory constituting the exhaust pipe is damaged and the life of the exhaust pipe is reduced. There is. Further, since the structure of the exhaust pipe becomes complicated, the manufacturing cost increases. In addition, since the splash flowing into the exhaust pipe flows down the inclined surface and accumulates in the lower part, there is a problem that it takes time to remove the accumulated metal.

そこで、上記問題を解決するため、真空脱ガス槽と排ガスクーラーとを水平の排気ダクトで連結した真空脱ガス処理装置が提案されている。図7に、水平の排気ダクトを有する真空脱ガス処理装置の模式図を示す。真空脱ガス槽10の上蓋を貫通して挿入されたバーナー16で真空脱ガス槽10を燃焼予熱すると、燃焼によって生成された排ガスは、排気ダクト72内に吸引されて部分流れCを形成し、この部分流れCは、排気ダクト72の上面に沿って排ガスクーラー11まで流れていき、排ガスクーラー11で冷やされて排気ダクト72の下面を流れて戻る大きな循環流を形成する。
なお、排ガスクーラー11内には、冷却水が循環する冷媒配管15が配設されており、冷媒配管15の表面に発生した結露は、排ガスクーラー11の下端部に接続されたドレン13を介してシールポット14に排水される。
In order to solve the above problem, a vacuum degassing apparatus in which a vacuum degassing tank and an exhaust gas cooler are connected by a horizontal exhaust duct has been proposed. FIG. 7 shows a schematic diagram of a vacuum degassing apparatus having a horizontal exhaust duct. When the vacuum degassing tank 10 is preheated by the burner 16 inserted through the upper lid of the vacuum degassing tank 10, the exhaust gas generated by the combustion is sucked into the exhaust duct 72 to form a partial flow C, This partial flow C flows along the upper surface of the exhaust duct 72 to the exhaust gas cooler 11, is cooled by the exhaust gas cooler 11, and forms a large circulating flow that flows back through the lower surface of the exhaust duct 72.
In addition, a refrigerant pipe 15 through which cooling water circulates is disposed in the exhaust gas cooler 11, and dew condensation generated on the surface of the refrigerant pipe 15 passes through a drain 13 connected to the lower end of the exhaust gas cooler 11. It is drained into the seal pot 14.

上記循環流の形成過程について、図8に示す熱流速解析結果に基づいて説明する。バーナー16によって加熱された排ガスC1は、排気ダクト72内で上昇し、排気ダクト72の上面に衝突する。排気ダクト72の上面に衝突した排ガスC1の一部C2は分岐して、排気ダクト72の上面に沿って排ガスクーラー11まで流れていく。排ガスクーラー11内に流れ込んだ排ガスC3は、冷却されて下降し、真空脱ガス槽10へ戻る流れC4となる。 The formation process of the circulating flow will be described based on the thermal flow rate analysis result shown in FIG. The exhaust gas C 1 heated by the burner 16 rises in the exhaust duct 72 and collides with the upper surface of the exhaust duct 72. A part C2 of the exhaust gas C1 colliding with the upper surface of the exhaust duct 72 is branched and flows to the exhaust gas cooler 11 along the upper surface of the exhaust duct 72. The exhaust gas C3 that has flowed into the exhaust gas cooler 11 is cooled and descends, and becomes a flow C4 that returns to the vacuum degassing tank 10.

燃焼予熱では、真空脱ガス槽10内に吸い込まれた空気中の酸素と窒素が化学反応を起こし、NOxが生成される。排ガスが循環流となった場合、燃焼予熱に伴う空気の吸込量が増加するため、生成されるNOxも増大し、排ガス中のNOx濃度が極端に高くなる。排ガス中のNOxは、排ガスクーラー11内で発生した結露に溶解してpH度の低い硝酸水溶液となり、排ガスクーラー11、ドレン13、及びシールポット14からなる排ガスクーラー部を急激に腐食する。 In the combustion preheating, oxygen and nitrogen in the air sucked into the vacuum degassing tank 10 cause a chemical reaction, and NOx is generated. When the exhaust gas becomes a circulating flow, the amount of air sucked with combustion preheating increases, so the generated NOx also increases, and the NOx concentration in the exhaust gas becomes extremely high. The NOx in the exhaust gas dissolves in the dew condensation generated in the exhaust gas cooler 11 to become a nitric acid aqueous solution having a low pH, and abruptly corrodes the exhaust gas cooler portion including the exhaust gas cooler 11, the drain 13, and the seal pot 14.

本発明はかかる事情に鑑みてなされたもので、簡単な構造で、予熱時の排ガスに含まれるNOx濃度を低減して排ガスクーラー部の腐食を防止し、以て排ガスクーラー部の保全費用の削減及び長寿命化を図る排ガスクーラーの腐食防止方法を提供することを目的とする。 The present invention has been made in view of such circumstances, and with a simple structure, the NOx concentration contained in the exhaust gas during preheating is reduced to prevent corrosion of the exhaust gas cooler, thereby reducing the maintenance cost of the exhaust gas cooler. And it aims at providing the corrosion prevention method of the exhaust gas cooler which aims at lifetime extension.

上記目的を達成するため、本発明は、真空脱ガス槽と排ガスクーラーとを排気ダクトで連結した真空脱ガス処理装置において、前記真空脱ガス槽の予熱時に発生する排ガス中に含まれるNOxに起因する前記排ガスクーラーの腐食を防止する方法であって、前記排気ダクトに2箇所以上4箇所以下の屈曲部を設け、少なくとも一部の前記屈曲部の高さを、該屈曲部より前記真空脱ガス槽側に位置する屈曲部より下方、及び/又は、該屈曲部より前記排ガスクーラー側に位置する屈曲部より上方とすることを特徴としている。 In order to achieve the above object, the present invention is based on NOx contained in exhaust gas generated during preheating of the vacuum degassing tank in a vacuum degassing treatment apparatus in which a vacuum degassing tank and an exhaust gas cooler are connected by an exhaust duct. A method for preventing corrosion of the exhaust gas cooler, wherein the exhaust duct is provided with two or more bent portions at four or less portions, and at least a part of the bent portions has a height from the bent portion by the vacuum degassing. It is characterized by being below the bent part located on the tank side and / or above the bent part located on the exhaust gas cooler side from the bent part.

本発明では、真空脱ガス槽と排ガスクーラーとを連結する排気ダクトを、下向き方向に2箇所以上4箇所以下屈曲させる(一部の屈曲部間が水平であっても良い。)ことにより、後述するように、排気ダクトの上面に沿って排ガスクーラーに向かう排ガスの流れを屈曲部で断ち切ることができる。加えて、循環流が形成されにくくなることにより、燃焼予熱に伴う空気の吸込量が減少し、NOxの発生量が低下する。その結果、排ガス中のNOx濃度が大幅に低減され、排ガスクーラー部の腐食を防止することができる。 In the present invention, the exhaust duct connecting the vacuum degassing tank and the exhaust gas cooler is bent in the downward direction at 2 or more and 4 or less (a part of the bent portions may be horizontal) to be described later. As described above, the flow of the exhaust gas toward the exhaust gas cooler along the upper surface of the exhaust duct can be cut off at the bent portion. In addition, since it becomes difficult to form a circulating flow, the amount of air sucked with combustion preheating decreases, and the amount of NOx generated decreases. As a result, the NOx concentration in the exhaust gas is greatly reduced, and corrosion of the exhaust gas cooler can be prevented.

また、本発明に係る排ガスクーラーの腐食防止方法では、前記真空脱ガス槽に最も近い位置にある前記屈曲部と前記排ガスクーラーに最も近い位置にある前記屈曲部との間の鉛直距離を、前記排気ダクトの内法幅の1.0倍以上且つ4.0倍未満とすることを好適とする。
真空脱ガス槽に最も近い位置にある屈曲部と排ガスクーラーに最も近い位置にある屈曲部との間の鉛直距離(以下、「屈曲段差」と呼ぶ。)が排気ダクトの内法幅の1.0倍未満の場合は、排ガスクーラーの方向に部分的に流れる排ガスが循環流を形成しやすくなるため好ましくない。一方、屈曲段差が排気ダクトの内法幅の4.0倍以上の場合は、排気抵抗が増大して真空精錬に支障を来すおそれがある。
In the exhaust gas cooler corrosion prevention method according to the present invention, the vertical distance between the bent portion located closest to the vacuum degassing tank and the bent portion located closest to the exhaust gas cooler, The inner width of the exhaust duct is preferably 1.0 times or more and less than 4.0 times.
The vertical distance between the bent portion closest to the vacuum degassing tank and the bent portion closest to the exhaust gas cooler (hereinafter referred to as “bent step”) is 1. If it is less than 0 times, the exhaust gas partially flowing in the direction of the exhaust gas cooler is liable to form a circulation flow, which is not preferable. On the other hand, when the bending step is 4.0 times or more the internal width of the exhaust duct, the exhaust resistance may increase and hinder vacuum refining.

本発明では、真空脱ガス槽と排ガスクーラーとを連結する排気ダクトを、下向き方向に2箇所以上4箇所以下屈曲させることにより、排ガス中のNOx濃度を大幅に低減させることができる。その結果、排ガスクーラー部の腐食が防止され、以て排ガスクーラー部の保全費用の削減及び長寿命化を図ることができる。 In the present invention, the NOx concentration in the exhaust gas can be greatly reduced by bending the exhaust duct connecting the vacuum degassing tank and the exhaust gas cooler in the downward direction at 2 or more and 4 or less . As a result, corrosion of the exhaust gas cooler part is prevented, so that the maintenance cost of the exhaust gas cooler part can be reduced and the life can be extended.

続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態につき説明し、本発明の理解に供する。 Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.

図1に、本発明の一実施の形態に係る排ガスクーラーの腐食防止方法を適用する真空脱ガス処理装置を構成する排気ダクトの模式図を示す。
排気ダクト12は、真空脱ガス槽10の上部に一端が接続される第一の水平部12aと、第一の水平部12aの他端に一端が接続され、斜め下方に傾斜する傾斜部12bと、傾斜部12bの他端に一端が接続され、他端が排ガスクーラー11に接続される第二の水平部12cとから構成されている。
FIG. 1 shows a schematic diagram of an exhaust duct constituting a vacuum degassing apparatus to which a method for preventing corrosion of an exhaust gas cooler according to an embodiment of the present invention is applied.
The exhaust duct 12 includes a first horizontal portion 12a having one end connected to the upper portion of the vacuum degassing tank 10, and an inclined portion 12b having one end connected to the other end of the first horizontal portion 12a and inclined obliquely downward. The second end of the inclined portion 12b is connected to the other end of the inclined portion 12b, and the other end of the inclined portion 12b is connected to the exhaust gas cooler 11.

第一の水平部12aと傾斜部12bとの接続部は、水平面に対する屈曲角α1を有する第一の屈曲部P1とされ、傾斜部12bと第二の水平部12cとの接続部は、水平面に対する屈曲角α2を有する第二の屈曲部P2とされている。即ち、第二の屈曲部P2は、第二の屈曲部P2より真空脱ガス槽10側に位置する第一の屈曲部P1より下方に位置し、第一の屈曲部P1は、第一の屈曲部P1より排ガスクーラー11側に位置する第二の屈曲部P2より上方に位置する。 The connecting portion between the first horizontal portion 12a and the inclined portion 12b is a first bent portion P1 having a bending angle α1 with respect to the horizontal plane, and the connecting portion between the inclined portion 12b and the second horizontal portion 12c is relative to the horizontal plane. The second bent portion P2 has a bent angle α2. That is, the second bent portion P2 is positioned below the first bent portion P1 located on the vacuum degassing tank 10 side from the second bent portion P2, and the first bent portion P1 is the first bent portion P1. It is located above the second bent part P2 located on the exhaust gas cooler 11 side from the part P1.

ここで、屈曲角α1、α2は、45度未満とされる。屈曲角α1、α2が45度以上になると、排気抵抗が増大し、真空脱ガス処理に時間を要することになる。
また、真空脱ガス槽10に最も近い位置にある屈曲部P1と排ガスクーラー11に最も近い位置にある屈曲部P2との間の鉛直距離である屈曲段差Dは、第一の水平部12aの内径の1.0倍以上、好ましくは1.5倍以上、且つ4.0倍未満とされる。
Here, the bending angles α1 and α2 are less than 45 degrees. When the bending angles α1 and α2 are 45 degrees or more, the exhaust resistance increases and it takes time for the vacuum degassing process.
Further, the bending step D, which is the vertical distance between the bent portion P1 located closest to the vacuum degassing tank 10 and the bent portion P2 located closest to the exhaust gas cooler 11, is an inner diameter of the first horizontal portion 12a. 1.0 times or more, preferably 1.5 times or more and less than 4.0 times.

なお、第一の水平部12aの一端から排ガスクーラー11中央部までの水平距離Hは、6m〜20mが好ましい。距離Hが6m未満であると、排ガスクーラー11の方向に部分的に流れる排ガスが排ガスクーラー11まで到達し、排ガスクーラー11の腐食を招くことになる。一方、距離Hが20mを超えると、排気抵抗が増大し、真空脱ガス処理に時間を要することになる。 In addition, as for the horizontal distance H from the end of the 1st horizontal part 12a to the exhaust gas cooler 11 center part, 6-20 m is preferable. If the distance H is less than 6 m, the exhaust gas partially flowing in the direction of the exhaust gas cooler 11 reaches the exhaust gas cooler 11 and causes corrosion of the exhaust gas cooler 11. On the other hand, if the distance H exceeds 20 m, the exhaust resistance increases and it takes time for the vacuum degassing process.

ここで、本発明による排ガスクーラーの腐食防止メカニズムについて説明する。
図2は、熱流速解析によって得られた、図1の形状を有する排気ダクト12内の排ガスの流れを示した模式図である。バーナーによって加熱された排ガスG1は、第一の水平部12a内で上昇し、傾斜部12bの上面に衝突する。傾斜部12bの上面に衝突した排ガスG1の大部分は、第一の水平部12aの上面に沿って真空脱ガス槽10に戻る部分流れとなり、排ガスG1の一部G2が分岐して傾斜部12bの上面に沿って下方に流れる。分岐した流れG2は、冷却されて下降し、傾斜部12bの下面に衝突する。傾斜部12bの下面に衝突した排ガスG3の大部分は、傾斜部12bの下面に沿って真空脱ガス槽10に戻る部分流れとなり、排ガスG3の一部G4が分岐して第二の水平部12cの方向に流れていく。
Here, the corrosion prevention mechanism of the exhaust gas cooler according to the present invention will be described.
FIG. 2 is a schematic diagram showing the flow of exhaust gas in the exhaust duct 12 having the shape shown in FIG. The exhaust gas G1 heated by the burner rises in the first horizontal portion 12a and collides with the upper surface of the inclined portion 12b. Most of the exhaust gas G1 that has collided with the upper surface of the inclined portion 12b becomes a partial flow that returns to the vacuum degassing tank 10 along the upper surface of the first horizontal portion 12a, and a part G2 of the exhaust gas G1 branches to form the inclined portion 12b. It flows downward along the upper surface of. The branched flow G2 is cooled and descends and collides with the lower surface of the inclined portion 12b. Most of the exhaust gas G3 colliding with the lower surface of the inclined portion 12b becomes a partial flow returning to the vacuum degassing tank 10 along the lower surface of the inclined portion 12b, and a part G4 of the exhaust gas G3 is branched to form the second horizontal portion 12c. It flows in the direction of.

このように、本実施の形態の方法において、排気ダクト12は、排ガスの大部分が排ガスクーラー11に達する前に、真空脱ガス槽10に戻る部分流れG1、G3となり、循環流が形成されにくくなる。このため、燃焼予熱に伴う空気の吸込量が減少し、NOxの発生量が低下する。その結果、排ガスクーラー11内のNOxが大幅に低減され、排ガスクーラー部の腐食を防止することができる。 Thus, in the method of the present embodiment, the exhaust duct 12 becomes the partial flows G1 and G3 that return to the vacuum degassing tank 10 before most of the exhaust gas reaches the exhaust gas cooler 11, and a circulation flow is not easily formed. Become. For this reason, the amount of air suction accompanying combustion preheating decreases, and the amount of NOx generated decreases. As a result, NOx in the exhaust gas cooler 11 is significantly reduced, and corrosion of the exhaust gas cooler portion can be prevented.

図3は、熱流速解析によって得られた、排ガスクーラー内におけるNOxとOの濃度変化を示したグラフである。同図より、水平排気ダクトの場合、10分経過後から排ガスクーラー内のNOx濃度が急激に増加することがわかる。また、これに伴い、O濃度も増加している。一方、本発明に係る排気ダクトでは、排ガスクーラー内のNOx濃度は殆ど増加せず、非常に低い値であることがわかる。また、燃焼効率が高いため、O濃度も非常に低い値となっている。 FIG. 3 is a graph showing changes in the concentrations of NOx and O 2 in the exhaust gas cooler obtained by heat flow rate analysis. From the figure, it can be seen that in the case of a horizontal exhaust duct, the NOx concentration in the exhaust gas cooler increases rapidly after 10 minutes. Along with this, the O 2 concentration also increases. On the other hand, in the exhaust duct according to the present invention, it can be seen that the NOx concentration in the exhaust gas cooler hardly increases and is a very low value. Moreover, since the combustion efficiency is high, the O 2 concentration is also a very low value.

次に、本発明のその他の実施の形態に係る排ガスクーラーの腐食防止方法を適用する真空脱ガス処理装置を構成する排気ダクトについて説明する。
図4(A)、(B)は、屈曲部が3箇所の場合、図4(C)〜(E)は、屈曲部が4箇所の場合をそれぞれ示している。
図4(A)、(D)の排気ダクト22、52は、第一の水平部22a、52aと第二の水平部22c、52cとの間の傾斜部22b、52bが下方に凸とされ、図4(B)、(E)排気ダクト32、62は、第一の水平部32a、62aと第二の水平部32c、62cとの間の傾斜部32b、62bが上方に凸とされている。また、図4(C)の排気ダクト42は、第一の水平部42aと第二の水平部42cとの間の傾斜部42bの中間部が水平とされている。
Next, an exhaust duct constituting a vacuum degassing apparatus to which the corrosion prevention method for an exhaust gas cooler according to another embodiment of the present invention is applied will be described.
4A and 4B show the case where there are three bent portions, and FIGS. 4C to 4E show the case where there are four bent portions, respectively.
In the exhaust ducts 22 and 52 shown in FIGS. 4A and 4D, the inclined portions 22b and 52b between the first horizontal portions 22a and 52a and the second horizontal portions 22c and 52c are projected downward. In the exhaust ducts 32 and 62 in FIGS. 4B and 4E, the inclined portions 32b and 62b between the first horizontal portions 32a and 62a and the second horizontal portions 32c and 62c are convex upward. Yes. Further, in the exhaust duct 42 of FIG. 4C, the intermediate portion of the inclined portion 42b between the first horizontal portion 42a and the second horizontal portion 42c is horizontal.

屈曲部P1、P2、P3、P4における屈曲角α1、α2、α3、α4は、45度未満とされ、真空脱ガス槽10に最も近い位置にある屈曲部P1と排ガスクーラー11に最も近い位置にある屈曲部P3、P4との間の鉛直距離である屈曲段差Dは、第一の水平部22a、32a、42a、52a、62aの内径の1.0倍以上且つ4.0倍未満である。
なお、屈曲部が4箇所を超えると、真空脱ガス処理における排気抵抗が増大して精錬に支障が生じるので、4箇所以内が望ましい。
The bending angles α1, α2, α3, and α4 at the bent portions P1, P2, P3, and P4 are less than 45 degrees, and are positioned closest to the bent portion P1 and the exhaust gas cooler 11 that are closest to the vacuum degassing tank 10. A bending step D, which is a vertical distance between certain bending portions P3 and P4, is 1.0 times or more and less than 4.0 times the inner diameter of the first horizontal portions 22a, 32a, 42a, 52a, and 62a.
In addition, since the exhaust resistance in a vacuum degassing process will increase and a refinement will be hindered when a bending part exceeds four places, within four places are desirable.

以上、本発明の実施の形態について説明してきたが、本発明は何ら上記した実施の形態に記載の構成に限定されるものではなく、特許請求の範囲に記載されている事項の範囲内で考えられるその他の実施の形態や変形例も含むものである。例えば、上記の実施の形態では、排気ダクトの断面は円形を想定しているが、矩形としてもよい。 Although the embodiments of the present invention have been described above, the present invention is not limited to the configurations described in the above-described embodiments, and is considered within the scope of the matters described in the claims. Other embodiments and modifications are also included. For example, in the above embodiment, the cross section of the exhaust duct is assumed to be circular, but may be rectangular.

排気ダクトの屈曲部の数と屈曲段差Dをパラメータとして、排ガスクーラー内のNOx濃度について試験を実施した。試験条件及び試験結果を表1に示す。表1中の屈曲段差Dは排気ダクトの内径に対する比であり、腐食指数は従来例の腐食面積に対する比である。
また、その際の排気ダクト(屈曲部が2箇所の場合)の寸法を図5に、屈曲段差Dと腐食指数との関係を示す試験結果のグラフを図6に示す。
Using the number of bent portions of the exhaust duct and the bent step D as parameters, a test was conducted on the NOx concentration in the exhaust gas cooler. Table 1 shows the test conditions and test results. The bending step D in Table 1 is the ratio to the inner diameter of the exhaust duct, and the corrosion index is the ratio to the corrosion area of the conventional example.
In addition, FIG. 5 shows the dimensions of the exhaust duct (when there are two bent portions) at that time, and FIG. 6 shows a graph of test results showing the relationship between the bent step D and the corrosion index.

Figure 0005353033
Figure 0005353033

表1より以下のことがわかる。
従来例の水平ダクトの場合は、排ガスクーラーに達する大きな循環流が形成されているため、連続的にNOxが発生し、腐食が進行する。これに対して、屈曲部を2箇所設けた本発明の実施例1〜5は、従来例に比べて腐食指数が低くなっている。一方、屈曲部を1箇所設けた比較例1は、屈曲部を設けたことにより排ガスクーラーに達する大きな循環流は形成されないが、排ガスクーラーが排気ダクトより下に位置する構造となるため、排ガスクーラーにダストが堆積するという問題がある。また、屈曲部を5箇所設けた比較例2は、屈曲部を多く設けることで腐食指数は非常に低くなるが、排気ダクト内の圧損(排気抵抗)が大きくなり真空脱ガス処理時間が長くなるという問題がある。
Table 1 shows the following.
In the case of the horizontal duct of the conventional example, since a large circulation flow reaching the exhaust gas cooler is formed, NOx is continuously generated and corrosion proceeds. On the other hand, Examples 1 to 5 of the present invention in which two bent portions are provided have a lower corrosion index than the conventional example. On the other hand, in Comparative Example 1 in which one bent portion is provided, a large circulation flow reaching the exhaust gas cooler is not formed by providing the bent portion, but the exhaust gas cooler has a structure located below the exhaust duct. There is a problem that dust accumulates. Further, in Comparative Example 2 in which five bent portions are provided, the corrosion index becomes very low by providing a large number of bent portions, but the pressure loss (exhaust resistance) in the exhaust duct increases and the vacuum degassing treatment time increases. There is a problem.

実施例同士を比較した場合、図6から明らかなように、屈曲段差Dが大きくなるほど腐食指数が低くなっていることがわかる。また、実施例については、屈曲段差Dと腐食指数との相関関係(図6)がある。
屈曲段差Dが排気ダクトの内径の0.5倍である実施例4は、排ガスクーラーの方向に部分的に流れる排ガスが循環流を形成しやすくなるため、他の実施例に比べて腐食指数が高くなっている。実施例1、2、3、5では、排気ダクトに十分な屈曲段差Dを確保しているため、排ガスクーラーに達する大きな循環流が形成されず、排気ダクト内のNOx量も少なく、排ガスクーラーの腐食は殆ど発生しない。但し、実施例5は、屈曲段差Dが排気ダクトの内径の4.0倍であるため、排気ダクトの圧損が大きく、真空脱ガス処理時間が長くなる。
When the examples are compared with each other, as is apparent from FIG. 6, it can be seen that the corrosion index decreases as the bending step D increases. Moreover, about an Example, there exists correlation (FIG. 6) with the bending level | step difference D and a corrosion index.
In Example 4 in which the bending step D is 0.5 times the inner diameter of the exhaust duct, the exhaust gas that partially flows in the direction of the exhaust gas cooler easily forms a circulation flow, and therefore has a corrosion index as compared with other examples. It is high. In Examples 1, 2, 3, and 5, since a sufficient bending step D is secured in the exhaust duct, a large circulation flow reaching the exhaust gas cooler is not formed, the amount of NOx in the exhaust duct is small, and the exhaust gas cooler Little corrosion occurs. However, in Example 5, since the bending step D is 4.0 times the inner diameter of the exhaust duct, the pressure loss of the exhaust duct is large, and the vacuum degassing processing time becomes long.

本発明の一実施の形態に係る排ガスクーラーの腐食防止方法を適用する真空脱ガス処理装置を構成する排気ダクトの模式図である。It is a schematic diagram of the exhaust duct which comprises the vacuum degassing processing apparatus to which the corrosion prevention method of the exhaust gas cooler which concerns on one embodiment of this invention is applied. 同排気ダクト内における排ガスの流れを説明するための模式図である。It is a schematic diagram for demonstrating the flow of the waste gas in the same exhaust duct. 排ガスクーラー内におけるNOxとOの濃度変化を示したグラフである。Is a graph showing the change in concentration of NOx and O 2 in the exhaust gas in the cooler. (A)〜(E)はそれぞれ本発明のその他の実施の形態に係る排ガスクーラーの腐食防止方法を適用する真空脱ガス処理装置を構成する排気ダクトの模式図である。(A)-(E) are the schematic diagrams of the exhaust duct which comprises the vacuum degassing processing apparatus to which the corrosion prevention method of the exhaust gas cooler which concerns on other embodiment of this invention is applied, respectively. 試験に用いた排気ダクトの模式図である。It is a schematic diagram of the exhaust duct used for the test. 屈曲段差Dと腐食指数との関係を示す試験結果のグラフである。It is a graph of the test result which shows the relationship between the bending level | step difference D and a corrosion index. 排ガスクーラーの腐食メカニズムを説明するための模式図である。It is a schematic diagram for demonstrating the corrosion mechanism of an exhaust gas cooler. 水平の排気ダクト内における排ガスの流れを説明するための模式図である。It is a schematic diagram for demonstrating the flow of the waste gas in a horizontal exhaust duct.

符号の説明Explanation of symbols

10:真空脱ガス槽、11:排ガスクーラー、12:排気ダクト、12a:第一の水平部、12b:傾斜部、12c:第二の水平部、13:ドレン、14:シールポット、15:冷媒配管、16:バーナー、22:排気ダクト、22a:第一の水平部、22b:傾斜部、22c:第二の水平部、32:排気ダクト、32a:第一の水平部、32b:傾斜部、32c:第二の水平部、42:排気ダクト、42a:第一の水平部、42b:傾斜部、42c:第二の水平部、52:排気ダクト、52a:第一の水平部、52b:傾斜部、52c:第二の水平部、62:排気ダクト、62a:第一の水平部、62b:傾斜部、62c:第二の水平部、72:排気ダクト、D:屈曲段差、P1:第一の屈曲部(屈曲部)、P2:第二の屈曲部(屈曲部)、P3、P4:屈曲部、α1、α2、α3、α4:屈曲角 10: vacuum degassing tank, 11: exhaust gas cooler, 12: exhaust duct, 12a: first horizontal part, 12b: inclined part, 12c: second horizontal part, 13: drain, 14: seal pot, 15: refrigerant Piping, 16: burner, 22: exhaust duct, 22a: first horizontal portion, 22b: inclined portion, 22c: second horizontal portion, 32: exhaust duct, 32a: first horizontal portion, 32b: inclined portion, 32c: second horizontal portion, 42: exhaust duct, 42a: first horizontal portion, 42b: inclined portion, 42c: second horizontal portion, 52: exhaust duct, 52a: first horizontal portion, 52b: inclined Part, 52c: second horizontal part, 62: exhaust duct, 62a: first horizontal part, 62b: inclined part, 62c: second horizontal part, 72: exhaust duct, D: bending step, P1: first Bending part (bending part), P2: second bending part (bending part) P3, P4: bent portion, α1, α2, α3, α4: bending angle

Claims (2)

真空脱ガス槽と排ガスクーラーとを排気ダクトで連結した真空脱ガス処理装置において、前記真空脱ガス槽の予熱時に発生する排ガス中に含まれるNOxに起因する前記排ガスクーラーの腐食を防止する方法であって、
前記排気ダクトに2箇所以上4箇所以下の屈曲部を設け、少なくとも一部の前記屈曲部の高さを、該屈曲部より前記真空脱ガス槽側に位置する屈曲部より下方、及び/又は、該屈曲部より前記排ガスクーラー側に位置する屈曲部より上方とすることを特徴とする排ガスクーラーの腐食防止方法。
In a vacuum degassing apparatus in which a vacuum degassing tank and an exhaust gas cooler are connected by an exhaust duct, the exhaust gas cooler is prevented from corroding due to NOx contained in the exhaust gas generated during preheating of the vacuum degassing tank. There,
The exhaust duct is provided with 2 to 4 bent portions, and the height of at least a portion of the bent portion is lower than the bent portion located on the vacuum degassing tank side from the bent portion, and / or A method for preventing corrosion of an exhaust gas cooler, characterized by being located above the bent portion located on the exhaust gas cooler side from the bent portion.
請求項1記載の排ガスクーラーの腐食防止方法において、前記真空脱ガス槽に最も近い位置にある前記屈曲部と前記排ガスクーラーに最も近い位置にある前記屈曲部との間の鉛直距離を、前記排気ダクトの内法幅の1.0倍以上且つ4.0倍未満とすることを特徴とする排ガスクーラーの腐食防止方法。 The corrosion prevention method for an exhaust gas cooler according to claim 1, wherein a vertical distance between the bent portion closest to the vacuum degassing tank and the bent portion closest to the exhaust gas cooler is defined as the exhaust gas. A method for preventing corrosion of an exhaust gas cooler, wherein the inner width of the duct is 1.0 times or more and less than 4.0 times.
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