Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP6911235B2 - Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine - Google Patents
[go: Go Back, main page]

JP6911235B2 - Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine - Google Patents

Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine Download PDF

Info

Publication number
JP6911235B2
JP6911235B2 JP2017073331A JP2017073331A JP6911235B2 JP 6911235 B2 JP6911235 B2 JP 6911235B2 JP 2017073331 A JP2017073331 A JP 2017073331A JP 2017073331 A JP2017073331 A JP 2017073331A JP 6911235 B2 JP6911235 B2 JP 6911235B2
Authority
JP
Japan
Prior art keywords
nitrogen gas
blast furnace
rotating shaft
gas supply
casing
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.)
Active
Application number
JP2017073331A
Other languages
Japanese (ja)
Other versions
JP2018173070A (en
Inventor
修一郎 小野
修一郎 小野
克巳 山名
克巳 山名
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.)
Mitsui E&S Machinery Co Ltd
Original Assignee
Mitsui E&S Machinery Co 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 Mitsui E&S Machinery Co Ltd filed Critical Mitsui E&S Machinery Co Ltd
Priority to JP2017073331A priority Critical patent/JP6911235B2/en
Publication of JP2018173070A publication Critical patent/JP2018173070A/en
Application granted granted Critical
Publication of JP6911235B2 publication Critical patent/JP6911235B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Sealing Using Fluids, Sealing Without Contact, And Removal Of Oil (AREA)
  • Turbine Rotor Nozzle Sealing (AREA)

Description

本発明は、高炉ガスにより回転駆動される炉頂圧回収タービンの回転軸の腐食防止装置に関する。 The present invention relates to a corrosion prevention device for a rotating shaft of a furnace top pressure recovery turbine that is rotationally driven by blast furnace gas.

高炉プラントの排ガス路にタービンを設置して発電等に利用する炉頂圧回収タービン発電設備は、製鉄所の高炉で発生する高炉ガスの持つ圧力エネルギをタービンによって電力として回収すると共に、高炉の炉頂圧制御を行なうものであり、近年、製鉄所の省エネルギ化を図り、環境保全に貢献するための極めて重要な設備となっている。 The top pressure recovery turbine power generation equipment, which is used for power generation by installing a turbine in the exhaust gas path of the blast furnace plant, recovers the pressure energy of the blast furnace gas generated in the blast furnace of the steelworks as electric power by the turbine, and also recovers the pressure energy of the blast furnace. It controls the top pressure, and in recent years, it has become an extremely important facility for saving energy in steelworks and contributing to environmental conservation.

この炉頂圧回収タービン発電設備には湿式と乾式があり、湿式の炉頂圧回収タービン発電設備は、高炉から出た高炉ガスを湿式除塵装置で水洗浄した後に、発電機駆動用の炉頂圧回収タービンに導くものである。他方、乾式の炉頂圧回収タービン発電設備においては、高炉ガスが乾式除塵装置により水洗浄されることなく除塵されるため、高炉ガスの温度が低下せず、回収電力が湿式に比べて25〜45%高くなり、電力の回収を効率的に行なうことができる。 There are two types of top pressure recovery turbine power generation equipment, wet and dry. In the wet top pressure recovery turbine power generation equipment, the blast furnace gas emitted from the blast furnace is washed with water using a wet dust remover, and then the top of the furnace is used to drive the generator. It leads to a pressure recovery turbine. On the other hand, in the dry furnace top pressure recovery turbine power generation facility, the blast furnace gas is removed without being washed with water by the dry dust remover, so that the temperature of the blast furnace gas does not decrease and the recovered power is 25 to 25 to that of the wet type. It is 45% higher, and power can be recovered efficiently.

いずれの方式の炉頂圧回収タービン発電設備においても、発電用タービンを回転駆動させるための燃料を必要としないため、CO2 削減と省エネルギ効果が極めて高く、現在、国内製鉄所のほとんどの高炉には、湿式又は乾式の炉頂圧回収タービン発電設備が設置されている。 Both types of turbine top pressure recovery turbine power generation equipment do not require fuel to drive the turbine for power generation, so CO2 reduction and energy saving effects are extremely high. Currently, most blast furnaces in domestic steelworks are used. Is equipped with wet or dry furnace top pressure recovery turbine power generation equipment.

しかしながら、上述の湿式の炉頂圧回収タービン発電設備においては、高炉ガスが湿式除塵装置で水洗浄される結果、高炉ガスが蒸気を飽和状態まで含むと共に、湿式除塵装置において除塵する過程で、例えばCl、SO4 等の腐食成分がダスト洗浄後の除塵水に溶解し、この除塵水の一部はミストとして排ガスに同伴してタービン内に流入する。他方、乾式の炉頂圧回収タービン発電設備においては、排ガス中に含まれる腐食成分は除去されないまま、タービンで発生する凝縮ミスト中に高い濃度で溶融される。 However, in the above-mentioned wet top pressure recovery turbine power generation equipment, as a result of washing the blast furnace gas with water by the wet dust remover, the blast furnace gas contains steam to a saturated state, and in the process of removing dust by the wet dust remover, for example. Corrosive components such as Cl and SO4 dissolve in the dust-removed water after dust cleaning, and a part of this dust-removed water flows into the turbine as mist along with the exhaust gas. On the other hand, in a dry-type furnace top pressure recovery turbine power generation facility, the corrosive components contained in the exhaust gas are not removed and are melted at a high concentration in the condensed mist generated in the turbine.

したがって、湿式、乾式の炉頂圧回収タービンのいずれの発電設備においても、これらミスト中に含まれるCl、SO4 等の腐食成分により、回転軸、ダービン翼、ケーシング等に接触して、これらを腐食させるという問題がある。 Therefore, in both wet and dry furnace top pressure recovery turbine power generation equipment, the corrosive components such as Cl and SO4 contained in these mists come into contact with the rotating shaft, Durbin blades, casing, etc. and corrode them. There is a problem of letting it.

このミスト中に含まれるCl、SO4 等の腐食成分により、回転軸、ダービン翼、ケーシング等が腐食するという問題に対しては、従来は、付着したダストや腐食成分を水洗浄等により除去する方法、回転軸については防食塗装を施すなどの方法により対処してきた(例えば、特許文献1〜4参照)。 To solve the problem that the rotating shaft, darbin blade, casing, etc. are corroded by the corrosive components such as Cl and SO4 contained in this mist, the conventional method is to remove the adhering dust and corrosive components by washing with water or the like. , The rotating shaft has been dealt with by a method such as applying anticorrosion coating (see, for example, Patent Documents 1 to 4).

特開平07−011974号公報Japanese Unexamined Patent Publication No. 07-011974 特開平07−011973号公報Japanese Unexamined Patent Publication No. 07-011973 特開2014−080872号公報Japanese Unexamined Patent Publication No. 2014-080872 特開2007−315364号公報Japanese Unexamined Patent Publication No. 2007-315364

しかしながら、回転軸に関しては、上述の従来の防食塗装だけでは、防食塗装自体の剥離や劣化等から、回転軸が直接腐食成分を含むミストに曝される可能性がある。また、排ガス中のダストによる摩耗によってもこの防食塗装の被膜の寿命が短くなり、腐食成分を含むミストに曝される可能性が高まる。 However, with respect to the rotating shaft, the above-mentioned conventional anticorrosive coating alone may cause the rotating shaft to be directly exposed to mist containing a corrosive component due to peeling or deterioration of the anticorrosive coating itself. In addition, wear due to dust in the exhaust gas also shortens the life of the anticorrosive coating film, increasing the possibility of exposure to mist containing corrosive components.

このように、使用時間の経過とともに回転軸が直接腐食成分を含むミストに曝されるようになると、その一部、特に回転軸のドラム部の前後端部が腐食する一方、回転軸には動翼によって常時大きな遠心応力が作用していることから、腐食しているドラム部の端部を起因として、回転軸に応力腐食割れが発生する可能性が考えられないわけではない、という問題がある。 In this way, when the rotating shaft is directly exposed to mist containing corrosive components with the passage of use time, a part of the rotating shaft, particularly the front and rear ends of the drum portion of the rotating shaft, corrodes while the rotating shaft moves. Since a large centrifugal stress is constantly applied by the blade, there is a problem that stress corrosion cracking may occur on the rotating shaft due to the end of the corroded drum part. ..

この一方、図3に示すように、ドラム部の前後に配設されるケーシング100,101と回転軸102との間をそれぞれ気密にするために、軸封用窒素ガスによる与圧が行われて、内部への高炉ガスの進入が防止されるようになっている炉頂圧回収タービンがある。 On the other hand, as shown in FIG. 3, pressurization with a shaft sealing nitrogen gas is performed in order to make the casings 100 and 101 arranged in front of and behind the drum portion and the rotating shaft 102 airtight, respectively. , There is a top pressure recovery turbine that is designed to prevent the ingress of blast furnace gas into the interior.

しかしながら、このケーシング100,101と回転軸102との間に軸封用窒素ガスを供給して内部への高炉ガスの進入を防止するだけでは、この軸封用窒素ガスの高炉ガス路への出口となるポケット部103,104において、この窒素ガスの圧力や流れを仔細に制御することは困難であり、高炉ガスがポケット部103,104内へ進入することを防止することはできない。このため、従来の軸封用窒素ガスだけでは、ドラム部102aの前端部105及び後端部106が高炉ガスによって腐食することを防止することはできない。 However, if the shaft sealing nitrogen gas is simply supplied between the casings 100 and 101 and the rotating shaft 102 to prevent the blast furnace gas from entering the inside, the shaft sealing nitrogen gas is discharged to the blast furnace gas path. It is difficult to finely control the pressure and flow of the nitrogen gas in the pocket portions 103 and 104, and it is not possible to prevent the blast furnace gas from entering the pocket portions 103 and 104. Therefore, it is not possible to prevent the front end portion 105 and the rear end portion 106 of the drum portion 102a from being corroded by the blast furnace gas only with the conventional nitrogen gas for shaft sealing.

これに対して、ケーシング100,101と回転軸102との間に供給する軸封用窒素ガスの圧力を増圧し、あるいは供給量を増量するという方法も考えられるが、この軸封用窒素ガスの増圧、増量だけでは、供給しなければならない窒素ガスが多量になるにも拘わらず、高炉ガス路への出口となるポケット部103,104内の窒素ガスの圧力や流れを仔細に制御することは同様に困難であり、高炉ガスのポケット部103,104内への進入を防止することはできない。 On the other hand, a method of increasing the pressure of the shaft sealing nitrogen gas supplied between the casings 100 and 101 and the rotating shaft 102 or increasing the supply amount is also conceivable. Finely controlling the pressure and flow of the nitrogen gas in the pockets 103 and 104, which are the outlets to the blast furnace gas path, even though the amount of nitrogen gas that must be supplied increases only by increasing the pressure and volume. Is similarly difficult, and it is not possible to prevent the blast furnace gas from entering the pocket portions 103 and 104.

本発明はこのような問題を解決するためになされたもので、ポケット部内に露出する回転軸のドラム部の、特に端部近傍の高炉ガスによる腐食が防止されて、炉頂圧回収タービンの回転軸の応力腐食割れの可能性を大幅に低下させることができる、炉頂圧回収タービンの回転軸構造を提供することを課題とする。 The present invention has been made to solve such a problem, and corrosion of the drum portion of the rotating shaft exposed in the pocket portion due to the blast furnace gas, particularly near the end portion, is prevented, and the rotation of the top pressure recovery turbine is prevented. An object of the present invention is to provide a rotary shaft structure of a furnace top pressure recovery turbine capable of significantly reducing the possibility of stress corrosion cracking of the shaft.

上述の課題を解決するために、本発明が採用する手段は、炉頂圧回収タービン発電設備に使用されて高炉から供給される高炉ガスにより回転駆動される炉頂圧回収タービンの回転軸の腐食防止装置であって、小径の軸部と大径のドラム部とを有する回転軸と、ドラム部に取り付けられて高炉ガスにより回転軸を回転駆動させる動翼と、ドラム部の軸方向端部の外側に全周にわたって環状に延びる一定幅の隙間である開口部を介して配設されて、高炉ガス路の内側部を形成するケーシングと、開口部の内部に、かつドラム部の軸方向端部とケーシングの軸方向端部との間に形成された拡大空洞からなるポケット部と、ケーシングの内部を通ってポケット部又はポケット部の近傍に開口する吐出口と、高圧の窒素ガスを吐出口へ供給する窒素ガス供給路と、高圧の窒素ガスを窒素ガス供給路へ供給する窒素ガス供給機構とを備えたことにある。 In order to solve the above-mentioned problems, the means adopted by the present invention is corrosion of the rotating shaft of the blast furnace top pressure recovery turbine, which is used in the furnace top pressure recovery turbine power generation facility and is rotationally driven by the blast furnace gas supplied from the blast furnace. A preventive device, a rotating shaft having a small-diameter shaft portion and a large-diameter drum portion, a moving blade attached to the drum portion to rotationally drive the rotating shaft by blast furnace gas, and an axial end portion of the drum portion. A casing that is disposed on the outside through an opening that is a gap of a constant width extending in an annular shape over the entire circumference to form an inner portion of the blast furnace gas path, and an axial end portion of the drum portion inside the opening. A pocket portion composed of an enlarged cavity formed between the blast furnace and the axial end portion of the blast furnace, a discharge port that passes through the inside of the casing and opens in the vicinity of the pocket portion or the pocket portion, and a blast furnace gas to the discharge port. It is equipped with a nitrogen gas supply path for supplying and a nitrogen gas supply mechanism for supplying high-pressure nitrogen gas to the nitrogen gas supply path.

上述の炉頂圧回収タービンの回転軸の腐食防止装置において、回転軸のドラム部とケーシングとの間の周方向に環状に延びる一定幅の隙間である開口部の、その内部に形成された拡大空洞からなるポケット部には、ケーシングの内部を通ってポケット部又はこのポケ
ット部の近傍に開口する吐出口から高圧の窒素ガスが供給されるから、この高圧の窒素ガスにより、高炉ガスがポケット部内に進入することが禁止されると共に、たとえ高炉ガスがポケット部内に進入したとしても直ちに窒素置換が行われ、進入した高炉ガスはこのポケット部から高炉ガス路へ排出される。
In the above-mentioned corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine, an enlargement formed inside the opening, which is a gap having a constant width extending in a circumferential direction between the drum portion of the rotary shaft and the casing. Since high-pressure nitrogen gas is supplied to the hollow pocket portion from the discharge port that passes through the inside of the casing and opens in the pocket portion or in the vicinity of the pocket portion, the high-pressure nitrogen gas causes the blast furnace gas to enter the pocket portion. Even if the blast furnace gas enters the pocket, nitrogen substitution is immediately performed, and the blast furnace gas that has entered is discharged from the pocket to the blast furnace gas passage.

したがって、ポケット部内に露出する回転軸のドラム部の、特に端部近傍の高炉ガスによる腐食が防止される。このため、回転軸の応力腐食割れの可能性を大幅に低下させることができる。 Therefore, corrosion of the drum portion of the rotating shaft exposed in the pocket portion, particularly by the blast furnace gas near the end portion, is prevented. Therefore, the possibility of stress corrosion cracking of the rotating shaft can be significantly reduced.

上記炉頂圧回収タービンの回転軸の腐食防止装置において、吐出口から吐出される高圧の窒素ガスは、動翼を通過する高炉ガスよりもその圧力が高いことが望ましい。 In the corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine, it is desirable that the high-pressure nitrogen gas discharged from the discharge port has a higher pressure than the blast furnace gas passing through the rotor blades.

このように、吐出口から吐出される高圧の窒素ガスは、動翼を通過する高炉ガスよりもその圧力が高いから、この高圧の窒素ガスにより、高炉ガスがポケット部内に進入することがより確実に禁止されると共に、たとえ高炉ガスがポケット部内に進入したとしても直ちに窒素置換が行われ、進入した高炉ガスはこのポケット部から高炉ガス路へより速やかに排出される。 In this way, the high-pressure nitrogen gas discharged from the discharge port has a higher pressure than the blast furnace gas passing through the moving blades, so that the high-pressure nitrogen gas makes it more certain that the blast furnace gas enters the pocket portion. Even if the blast furnace gas enters the pocket, nitrogen substitution is immediately performed, and the blast furnace gas that has entered is discharged from the pocket to the blast furnace gas passage more quickly.

したがって、ポケット部内に露出する回転軸のドラム部の後端部近傍の高炉ガスによる腐食がさらに防止される。このため、回転軸の応力腐食割れの可能性をさらに低下させることができる。 Therefore, corrosion by the blast furnace gas near the rear end of the drum portion of the rotating shaft exposed in the pocket portion is further prevented. Therefore, the possibility of stress corrosion cracking of the rotating shaft can be further reduced.

上記炉頂圧回収タービンの回転軸の腐食防止装置において、上述の窒素ガス供給路は、ケーシングの周方向の複数箇所に配設されていることが望ましい。 In the corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine, it is desirable that the above-mentioned nitrogen gas supply paths are arranged at a plurality of locations in the circumferential direction of the casing.

このように、窒素ガス供給路をケーシングの周方向の複数箇所に配設することにより、窒素ガス供給路からポケット部内への高圧の窒素ガスの吐出がケーシングの周方向に均一に行われ、高炉ガスがポケット部内に進入することがより確実に禁止される。したがって、回転軸の応力腐食割れの可能性を一段と低下させることができる。 By arranging the nitrogen gas supply paths at a plurality of locations in the circumferential direction of the casing in this way, high-pressure nitrogen gas is uniformly discharged from the nitrogen gas supply path into the pocket portion in the circumferential direction of the casing, and the blast furnace Gas is more reliably prohibited from entering the pocket. Therefore, the possibility of stress corrosion cracking of the rotating shaft can be further reduced.

上記炉頂圧回収タービンの回転軸の腐食防止装置において、上述の窒素ガス供給路は、ケーシング内に配設された周方向に延びる空洞部を介して窒素ガス供給機構から吐出口まで連通していることが望ましい。 In the corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine, the nitrogen gas supply path communicates from the nitrogen gas supply mechanism to the discharge port through a cavity extending in the circumferential direction arranged in the casing. It is desirable to be there.

このように、窒素ガス供給路が、ケーシング内に配設された周方向に延びる空洞部を介して窒素ガス供給機構から窒素ガス供給路の吐出口まで連通しているから、高圧の窒素ガスが一旦この周方向に連続する空洞部を通ることにより、圧力の均一化や脈動の防止が図られる。 In this way, since the nitrogen gas supply path communicates from the nitrogen gas supply mechanism to the discharge port of the nitrogen gas supply path through the cavity extending in the circumferential direction arranged in the casing, high-pressure nitrogen gas is released. By passing through this cavity that is continuous in the circumferential direction, pressure can be made uniform and pulsation can be prevented.

上記炉頂圧回収タービンの回転軸の腐食防止装置において、上述のケーシングと回転軸との間は、窒素ガス供給路とは別路で上記窒素ガス供給機構から供給された軸封用窒素ガスにより与圧されて内部への高炉ガスの進入が禁止されることが望ましい。 In the corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine, the shaft sealing nitrogen gas supplied from the nitrogen gas supply mechanism in a separate path from the nitrogen gas supply path between the casing and the rotary shaft is used. It is desirable that pressure be applied to prevent the entry of blast furnace gas into the interior.

このように、ケーシングと回転軸との間を気密にするための与圧を窒素ガス供給路とは別路で、上述の高圧の窒素ガスと同じ窒素ガス供給機構から供給される軸封用窒素ガスによって行うことにより、窒素ガス供給機構全体を簡素化することができる。 In this way, the pressure applied to make the space between the casing and the rotating shaft airtight is different from the nitrogen gas supply path, and the shaft sealing nitrogen is supplied from the same nitrogen gas supply mechanism as the high-pressure nitrogen gas described above. By using gas, the entire nitrogen gas supply mechanism can be simplified.

本発明の炉頂圧回収タービンの回転軸の腐食防止装置は、炉頂圧回収タービン発電設備に使用されて高炉から供給される高炉ガスにより回転駆動される炉頂圧回収タービンの回
転軸の腐食防止装置であって、小径の軸部と大径のドラム部とを有する回転軸と、ドラム部に取り付けられて高炉ガスにより回転軸を回転駆動させる動翼と、ドラム部の軸方向端部の外側に全周にわたって環状に延びる一定幅の隙間である開口部を介して配設されて高炉ガス路の内側部を形成するケーシングと、開口部の内部に、かつドラム部の軸方向端部とケーシングの軸方向端部との間に形成された拡大空洞からなるポケット部と、ケーシングの内部を通ってポケット部又はポケット部の近傍に開口する吐出口と、高圧の窒素ガスを吐出口へ供給する窒素ガス供給路と、高圧の窒素ガスを窒素ガス供給路へ供給する窒素ガス供給機構とを備える。
The corrosion prevention device for the rotary shaft of the top pressure recovery turbine of the present invention is used in the top pressure recovery turbine power generation equipment and is rotationally driven by the blast furnace gas supplied from the blast furnace. Corrosion of the rotary shaft of the top pressure recovery turbine. A preventive device, a rotating shaft having a small-diameter shaft portion and a large-diameter drum portion, a moving blade attached to the drum portion and rotationally driving the rotating shaft by blast furnace gas, and an axial end portion of the drum portion. A casing that is disposed on the outside through an opening that is a gap of a constant width extending in an annular shape over the entire circumference to form an inner portion of the blast furnace gas passage, and an axial end portion of the drum portion inside the opening. A pocket portion consisting of an enlarged cavity formed between the axial end portion of the casing, a discharge port that passes through the inside of the casing and opens in the vicinity of the pocket portion or the pocket portion, and a blast furnace gas is supplied to the discharge port. It is provided with a turbine gas supply path and a blast furnace gas supply mechanism for supplying high-pressure blast furnace gas to the turbine gas supply path.

したがって、ポケット部内に露出する回転軸のドラム部の、特に端部近傍の高炉ガスによる腐食が防止されて、炉頂圧回収タービンの回転軸の応力腐食割れの可能性を大幅に低下させることができる、という優れた効果を奏する。 Therefore, corrosion of the drum portion of the rotating shaft exposed in the pocket portion, especially by the blast furnace gas near the end portion, can be prevented, and the possibility of stress corrosion cracking of the rotating shaft of the rotating shaft of the furnace top pressure recovery turbine can be significantly reduced. It has the excellent effect of being able to do it.

本発明に係る炉頂圧回収タービンの回転軸の腐食防止装置を示す部分断面図である。It is a partial cross-sectional view which shows the corrosion prevention device of the rotary shaft of the furnace top pressure recovery turbine which concerns on this invention. 図1の炉頂圧回収タービンへ高圧窒素ガスを供給するための窒素ガス供給機構を示す模式図である。It is a schematic diagram which shows the nitrogen gas supply mechanism for supplying high pressure nitrogen gas to the furnace top pressure recovery turbine of FIG. 従来の炉頂圧回収タービンの回転軸の腐食防止装置を示す部分断面図である。It is a partial cross-sectional view which shows the corrosion prevention device of the rotary shaft of the conventional furnace top pressure recovery turbine.

本発明に係る炉頂圧回収タービンの回転軸の腐食防止装置を実施するための形態を、図1及び図2を参照して詳細に説明する。 A mode for implementing the corrosion prevention device for the rotary shaft of the furnace top pressure recovery turbine according to the present invention will be described in detail with reference to FIGS. 1 and 2.

図1は、一例としての、炉頂圧回収タービン発電設備の高炉プラントの排ガス路に設置されて発電等を行なう、炉頂圧回収タービン1の主要部を示す部分断面図である。炉頂圧回収タービンの発電設備においては、高炉から供給された高炉ガスが、様々な機器を介してこの炉頂圧回収タービン1に導かれてこれを回転駆動させる。 FIG. 1 is a partial cross-sectional view showing a main part of a top pressure recovery turbine 1 installed in an exhaust gas path of a blast furnace plant of a top pressure recovery turbine power generation facility as an example to generate power. In the power generation equipment of the top pressure recovery turbine, the blast furnace gas supplied from the blast furnace is guided to the top pressure recovery turbine 1 via various devices and driven to rotate.

炉頂圧回収タービン1の回転軸10によって発電機を回転駆動させることにより、発電が行なわれる。回転軸10は、前方及び後方でベアリング等により軸支される軸部10bと、軸部10bよりも大径に形成されるドラム部10aとを有し、このドラム部10aには、クリスマスツリ型の取付部を介して、例えば2段の第1段動翼(初段動翼)11と第2段動翼(最終段動翼)12が取り付けられる。 Power is generated by rotationally driving the generator by the rotating shaft 10 of the furnace top pressure recovery turbine 1. The rotating shaft 10 has a shaft portion 10b that is pivotally supported by bearings or the like at the front and rear, and a drum portion 10a that is formed to have a diameter larger than that of the shaft portion 10b. The drum portion 10a has a Christmas tree type. For example, a two-stage first-stage rotor blade (first-stage rotor blade) 11 and a second-stage rotor blade (final-stage rotor blade) 12 are attached via the mounting portion of the above.

つまり、この炉頂圧回収タービン1の回転軸10には、2段(複数段)の動翼11、12が配設され、各段の動翼11、12は、周方向に複数枚がそれぞれ取り付けられて増速翼列を形成し、動翼11、12を通過して断熱膨張する高炉ガスの作用を受けて回転軸10を回転駆動させる。 That is, two stages (plurality of stages) of moving blades 11 and 12 are arranged on the rotary shaft 10 of the furnace top pressure recovery turbine 1, and a plurality of blades 11 and 12 of each stage are arranged in the circumferential direction. It is attached to form a speed-increasing blade row, and the rotating shaft 10 is rotationally driven by the action of blast furnace gas that passes through the moving blades 11 and 12 and adiabatically expands.

符号13は、回転軸10のドラム部10aに取り付けられた第1段動翼(初段動翼)11の、プラットフォーム11aの前端部よりもさらに前方に延出された前方延出部、符号14は、回転軸10のドラム部10aに取り付けられた第2段動翼(最終段動翼)12の、プラットフォーム12aの後端部よりもさらに後方に延出された後方延出部を示す。 すなわち、炉頂圧回収タービン1の回転軸10は、従来の炉頂圧回収タービンの回転軸よりも、ドラム部10aの高炉ガスの流路に接する部分が前方延出部13及び後方延出部14の分だけ前後方向に延長されている。 Reference numeral 13 is a forward extension portion of the first stage rotor blade (first stage rotor blade) 11 attached to the drum portion 10a of the rotating shaft 10, which is further forward than the front end portion of the platform 11a. , The rear extension portion of the second stage rotor blade (final stage rotor blade) 12 attached to the drum portion 10a of the rotating shaft 10 is further extended rearward from the rear end portion of the platform 12a. That is, in the rotary shaft 10 of the furnace top pressure recovery turbine 1, the portion of the drum portion 10a in contact with the blast furnace gas flow path is the front extension portion 13 and the rear extension portion, as compared with the rotation shaft of the conventional furnace top pressure recovery turbine. It is extended in the front-back direction by 14 minutes.

回転軸10とは別体に形成されて、前方延出部13の外周部に取り付けられてこの外周
部を覆う保護部材15と、同様に回転軸10とは別体に形成されて、後方延出部14の外周部に取り付けられてこの外周部を覆う保護部材16とが配設される。これらの保護部材15,16は、それぞれ周方向に分割形成された複数個の保護部材ピースからなる。
A protective member 15 that is formed separately from the rotating shaft 10 and is attached to the outer peripheral portion of the front extending portion 13 to cover the outer peripheral portion, and similarly formed separately from the rotating shaft 10 and extends backward. A protective member 16 that is attached to the outer peripheral portion of the protruding portion 14 and covers the outer peripheral portion is arranged. Each of these protective members 15 and 16 is composed of a plurality of protective member pieces formed separately in the circumferential direction.

このように、回転軸10のドラム部10aは、第1段動翼11よりも前方に延出された前方延出部13、及び第2段動翼12よりも後方に延出された後方延出部14をそれぞれ有するから、特に高炉ガスによる腐食が発生しやすいドラム部10aの前方延出部13の前端部(軸方向端部)18、及び後方延出部14の後端部(軸方向端部)19が、動翼11,12から離れた位置に配置されることにより、動翼11,12から受ける遠心応力の応力値が低下する。したがって、特にドラム部10aの前及び後端部18,19の腐食等を原因とする、回転軸10の応力腐食割れの可能性を低下させることができる。 As described above, the drum portion 10a of the rotating shaft 10 extends forward from the first stage rotor blade 11 and extends rearward from the second stage rotor blade 12. Since each of the protrusions 14 is provided, the front end (axial end) 18 of the front extension 13 of the drum portion 10a, which is particularly prone to corrosion due to blast furnace gas, and the rear end (axial direction) of the rear extension 14 By arranging the end portion) 19 at a position away from the moving blades 11 and 12, the stress value of the centrifugal stress received from the moving blades 11 and 12 is reduced. Therefore, the possibility of stress corrosion cracking of the rotating shaft 10 due to corrosion of the front and rear end portions 18 and 19 of the drum portion 10a can be reduced.

また、回転軸10は、前方延出部13の外周部と後方延出部14の外周部に取り付けられて、これら外周部を覆う保護部材15,16が取り付けられる。したがって、前方延出部13及び後方延出部14の外周部が腐食成分を含むミストに直接曝されることが防止され、これによっても回転軸10の応力腐食割れの可能性を低下させる。 Further, the rotating shaft 10 is attached to the outer peripheral portion of the front extending portion 13 and the outer peripheral portion of the rear extending portion 14, and the protective members 15 and 16 covering these outer peripheral portions are attached. Therefore, it is possible to prevent the outer peripheral portions of the front extending portion 13 and the rear extending portion 14 from being directly exposed to the mist containing the corrosive component, which also reduces the possibility of stress corrosion cracking of the rotating shaft 10.

上述の保護部材15,16と同様の保護部材17が、第1段動翼11と第2段動翼12の間の回転軸10のドラム部10aの外周部にも取り付けられる。この保護部材17も、周方向に分割形成された複数個の保護部材体からなる。したがって、これまで高炉ガスに直接曝されていた2段の動翼11,12の間の回転軸10のドラム部10aの外周部を、高炉ガスから保護することができ、回転軸10の応力腐食割れの可能性をさらに低下させる。 A protective member 17 similar to the protective members 15 and 16 described above is also attached to the outer peripheral portion of the drum portion 10a of the rotating shaft 10 between the first-stage rotor blade 11 and the second-stage rotor blade 12. The protective member 17 is also composed of a plurality of protective member bodies divided and formed in the circumferential direction. Therefore, the outer peripheral portion of the drum portion 10a of the rotating shaft 10 between the two-stage rotor blades 11 and 12, which has been directly exposed to the blast furnace gas, can be protected from the blast furnace gas, and stress corrosion of the rotating shaft 10 can be achieved. Further reduce the possibility of cracking.

入口ケーシング20が、ドラム部10aの前方延出部13の前端部18よりも前方に、一定幅の隙間を設けて配設されて、その外側にある中央ケーシング30との間で高炉ガス路2を形成する。入口ケーシング20は、高炉ガス路2の内側部3を形成する。高炉ガス路2の外側部を形成する中央ケーシング30のさらに外側には、図示しない外側ケーシングが設けられている。 The inlet casing 20 is arranged in front of the front end portion 18 of the front extending portion 13 of the drum portion 10a with a gap of a certain width provided, and the blast furnace gas passage 2 is provided between the inlet casing 20 and the central casing 30 on the outside thereof. To form. The inlet casing 20 forms the inner portion 3 of the blast furnace gas passage 2. An outer casing (not shown) is provided on the outer side of the central casing 30 forming the outer portion of the blast furnace gas passage 2.

この入口ケーシング20の後端部(軸方向端部)22と回転軸10のドラム部10aの前端部18との間に、一定幅の隙間であって全周にわたり環状に延びる前方開口部26が形成される。この前方開口部26の内部には、内円筒状の入口ケーシング20に沿って周方向に全周にわたり環状に延びると共に、例えば軸方向に拡大されてなる、拡大空洞からなる前方ポケット部24が配設される。前方開口部26は、上述の高炉ガス路2に一定幅の隙間を設けて開口している。 Between the rear end portion (axial end portion) 22 of the inlet casing 20 and the front end portion 18 of the drum portion 10a of the rotating shaft 10, a front opening 26 having a constant width and extending in an annular shape over the entire circumference is provided. It is formed. Inside the front opening 26, a front pocket portion 24 formed of an enlarged cavity, which extends in an annular shape in the circumferential direction along the inner cylindrical inlet casing 20 and is expanded in the axial direction, for example, is arranged. Will be set up. The front opening 26 is opened by providing a gap of a certain width in the above-mentioned blast furnace gas passage 2.

前方窒素ガス供給路32が、入口ケーシング20の内部を通って前方ポケット部24に開口し、吐出口34を形成する。後に詳述するように、この吐出口34から第1段動翼11の入口近傍を通過する高炉ガスよりも高圧の窒素ガスが、前方ポケット部24内へ直接吐出される。なお、吐出口34は、高圧の窒素ガスが前方ポケット部24内へ有効に吐出できるものであれば、必ずしも前方ポケット部24に開口するものに限定されるものではなく、前方ポケット部24の近傍に開口するものであってもよい。 The front nitrogen gas supply path 32 passes through the inside of the inlet casing 20 and opens into the front pocket portion 24 to form a discharge port 34. As will be described in detail later, nitrogen gas having a pressure higher than that of the blast furnace gas passing near the inlet of the first stage rotor blade 11 is directly discharged from the discharge port 34 into the front pocket portion 24. The discharge port 34 is not necessarily limited to the one that opens into the front pocket portion 24 as long as the high-pressure nitrogen gas can be effectively discharged into the front pocket portion 24, and the discharge port 34 is in the vicinity of the front pocket portion 24. It may open to.

同様に、出口ケーシング21が、回転軸10の後端部19よりも後方に全周にわたり環状に延びる一定幅の隙間を設けて配設されて、中央ケーシング30との間で高炉ガス路2を形成する。出口ケーシング21は、入口ケーシング20と同様に、高炉ガス路2の内側部4を形成する。出口ケーシング21は、図示しない複数の翼形支柱(ストラットともいう)により中央ケーシング30に支持されている。 Similarly, the outlet casing 21 is arranged behind the rear end portion 19 of the rotating shaft 10 with a gap having a constant width extending in an annular shape over the entire circumference, and a blast furnace gas passage 2 is provided between the outlet casing 21 and the central casing 30. Form. The outlet casing 21 forms the inner portion 4 of the blast furnace gas passage 2 in the same manner as the inlet casing 20. The outlet casing 21 is supported by the central casing 30 by a plurality of airfoil-shaped struts (also referred to as struts) (not shown).

出口ケーシング21の前端部(軸方向端部)23と、回転軸10のドラム部10aの後端部19との間に、一定幅の隙間であって全周にわたり環状に延びる後方開口部27が形成される。この後方開口部27の内部には、内円筒状の出口ケーシング21に沿って周方向に全周にわたり環状に延びると共に、周方向に環状に延びると共に、例えば軸方向に拡大されてなる拡大空洞からなる後方ポケット部25が配設される。後方開口部27は、上述の高炉ガス路2に一定幅の隙間を設けて開口している。 A rear opening 27 having a constant width and extending in an annular shape over the entire circumference is provided between the front end (axial end) 23 of the outlet casing 21 and the rear end 19 of the drum portion 10a of the rotating shaft 10. It is formed. Inside the rear opening 27, an enlarged cavity extending in the circumferential direction along the inner cylindrical outlet casing 21 in an annular shape, extending in an annular direction in the circumferential direction, and expanding in the axial direction, for example, The rear pocket portion 25 is arranged. The rear opening 27 is opened by providing a gap of a certain width in the above-mentioned blast furnace gas passage 2.

後方窒素ガス供給路33が、出口ケーシング21の内部を通って後方ポケット部25に開口し、吐出口35を形成する。後に詳述するように、この吐出口35から、第2段動翼12の出口近傍を通過する高炉ガスよりも高圧の窒素ガスが、後方ポケット部25内へ直接吐出される。なお、吐出口35は、上述の高圧の窒素ガスが後方ポケット部25内へ有効に吐出できるものであれば、必ずしも後方ポケット部25に開口するものに限定されるものではなく、後方ポケット部25の近傍に開口するものであってもよい。 The rear nitrogen gas supply path 33 passes through the inside of the outlet casing 21 and opens into the rear pocket portion 25 to form a discharge port 35. As will be described in detail later, nitrogen gas having a pressure higher than that of the blast furnace gas passing near the outlet of the second stage rotor blade 12 is directly discharged into the rear pocket portion 25 from the discharge port 35. The discharge port 35 is not necessarily limited to the one that opens into the rear pocket portion 25 as long as the above-mentioned high-pressure nitrogen gas can be effectively discharged into the rear pocket portion 25. It may open in the vicinity of.

上述の前方窒素ガス供給路32及びその吐出口34は、入口ケーシング20の周方向の3箇所(複数箇所)に配設されている。同様に、後方窒素ガス供給路33及びその吐出口35は、出口ケーシング21の周方向の2箇所(複数箇所)に配設されている。上述の前方及び後方ポケット部24,25は、たとえ粉塵等を含む高炉ガスが前方及び後方開口部26,27を通して回転軸10とケーシング20,21との間に進入したとしても、粉塵等がこのポケット部24,25内に滞留ないし付着して、ポケット部24,25よりもさらに内部へ進入しないようにしたものである。 The above-mentioned front nitrogen gas supply passage 32 and its discharge port 34 are arranged at three locations (plural locations) in the circumferential direction of the inlet casing 20. Similarly, the rear nitrogen gas supply passage 33 and its discharge port 35 are arranged at two locations (plural locations) in the circumferential direction of the outlet casing 21. In the above-mentioned front and rear pocket portions 24 and 25, even if the blast furnace gas containing dust and the like enters between the rotating shaft 10 and the casings 20 and 21 through the front and rear openings 26 and 27, the dust and the like enter the front and rear pocket portions 24 and 25. It stays or adheres to the pockets 24 and 25 so as not to enter the inside further than the pockets 24 and 25.

図2に示すように、窒素ガス供給機構40は次のように構成される。窒素ガス供給路42は、窒素ガス供給源41から圧力調節弁43を通った後に前方窒素ガス供給路44と後方窒素ガス供給路45とに分岐される。前方窒素ガス供給路44は、流量調整弁47、圧力調節弁48を通って、さらに2路に分岐される。この2路に分岐して窒素ガス供給機構40を出た前方窒素ガス供給路44は、中央ケーシング30内にそれぞれ入る。 As shown in FIG. 2, the nitrogen gas supply mechanism 40 is configured as follows. The nitrogen gas supply path 42 is branched into a front nitrogen gas supply path 44 and a rear nitrogen gas supply path 45 after passing through the pressure control valve 43 from the nitrogen gas supply source 41. The forward nitrogen gas supply path 44 is further branched into two paths through the flow rate regulating valve 47 and the pressure regulating valve 48. The front nitrogen gas supply passages 44, which are branched into the two passages and exit the nitrogen gas supply mechanism 40, enter the central casing 30, respectively.

2路に分岐された前方窒素ガス供給路44は、入口ケーシング20内に配設された周方向に延びる前方空洞部(空洞部)36に入る。この前方空洞部36は、入口ケーシング20内に環状に形成されている。前方窒素ガス供給路44は、前方空洞部36の出口で3路に分岐された後、図1に示す前方窒素ガス供給路44の吐出口34まで連通している。 The front nitrogen gas supply path 44 branched into two paths enters the front cavity portion (cavity portion) 36 arranged in the inlet casing 20 and extending in the circumferential direction. The front cavity portion 36 is formed in an annular shape in the inlet casing 20. The front nitrogen gas supply path 44 is branched into three paths at the outlet of the front cavity 36, and then communicates with the discharge port 34 of the front nitrogen gas supply path 44 shown in FIG.

このように、前方窒素ガス供給路44が、入口ケーシング20内に配設された周方向に延びる前方空洞部36を介して、窒素ガス供給機構40から前方窒素ガス供給路44の吐出口34まで連通しているから、高圧の窒素ガスが一旦この周方向に延びる前方空洞部36を通ることにより、高圧の窒素ガスの脈動の防止や圧力の均一化が図られる。 In this way, the front nitrogen gas supply path 44 extends from the nitrogen gas supply mechanism 40 to the discharge port 34 of the front nitrogen gas supply path 44 via the front cavity portion 36 arranged in the inlet casing 20 in the circumferential direction. Since the high-pressure nitrogen gas is communicated with each other, the high-pressure nitrogen gas once passes through the front cavity portion 36 extending in the circumferential direction, thereby preventing the pulsation of the high-pressure nitrogen gas and making the pressure uniform.

他方、後方窒素ガス供給路45は、流量調整弁50、圧力調節弁51を通って2路に分岐される。この2路に分岐して窒素ガス供給機構40を出た後方窒素ガス供給路45は、出口ケーシング21内に入る。その後、後方窒素ガス供給路45は、出口ケーシング21の内部配管内を通り、図1に示す後方窒素ガス供給路45の吐出口35まで連通している。 On the other hand, the rear nitrogen gas supply path 45 is branched into two paths through the flow rate regulating valve 50 and the pressure regulating valve 51. The rear nitrogen gas supply path 45, which is branched into these two paths and exits the nitrogen gas supply mechanism 40, enters the outlet casing 21. After that, the rear nitrogen gas supply path 45 passes through the internal pipe of the outlet casing 21 and communicates with the discharge port 35 of the rear nitrogen gas supply path 45 shown in FIG.

窒素ガス供給機構40の窒素ガス供給源41から圧力調節弁43によって圧力調整された後、高圧の窒素ガスは、分岐した前方窒素ガス供給路44を通り、流量調節弁47によって、前方ポケット部24を通って高炉ガス路2へ排出される後述の軸封用窒素ガスの、例えば0.7〜1.0倍の質量流量になるように流量調整される。 After the pressure is adjusted by the pressure control valve 43 from the nitrogen gas supply source 41 of the nitrogen gas supply mechanism 40, the high-pressure nitrogen gas passes through the branched front nitrogen gas supply path 44 and is passed through the branched front nitrogen gas supply path 44 by the flow rate control valve 47 to the front pocket portion 24. The flow rate is adjusted so as to have a mass flow rate of, for example, 0.7 to 1.0 times that of the shaft-sealing nitrogen gas to be discharged to the blast furnace gas passage 2 through the gas passage 2.

続く圧力調節弁48により、吐出口34において第1段動翼11の入口近傍の高炉ガス
路2を通る高炉ガスに対して、例えば0.2〜0.5kgf/cm2 だけ高い圧力になるように調整され、さらに入口ケーシング20内に配設された前方空洞部36を通って、図1に示す前方窒素ガス供給路44の吐出口34から、前方ポケット部24内へ直接吐出される。
The subsequent pressure control valve 48 increases the pressure at the discharge port 34 by, for example, 0.2 to 0.5 kgf / cm2, with respect to the blast furnace gas passing through the blast furnace gas passage 2 near the inlet of the first stage moving blade 11. The gas is directly discharged into the front pocket portion 24 from the discharge port 34 of the front nitrogen gas supply path 44 shown in FIG. 1 through the front cavity portion 36 which is adjusted and further arranged in the inlet casing 20.

このため、この前方ポケット部24内へ直接吐出された高圧の窒素ガスにより、高炉ガスが前方ポケット部24内に進入することが禁止されると共に、たとえ高炉ガスの一部が進入したとしても直ちに窒素置換が行われて、高炉ガスは前方ポケット部24から高炉ガス路2へ速やかに排出される。したがって、前方ポケット部24内に露出する、ドラム部10aの前端部18の近傍の高炉ガスによる腐食が防止される。このため、回転軸10の応力腐食割れの可能性が大幅に低下する。 Therefore, the high-pressure nitrogen gas directly discharged into the front pocket portion 24 prohibits the blast furnace gas from entering the front pocket portion 24, and even if a part of the blast furnace gas enters the front pocket portion 24 immediately. Nitrogen substitution is performed, and the blast furnace gas is rapidly discharged from the front pocket portion 24 to the blast furnace gas passage 2. Therefore, corrosion by the blast furnace gas in the vicinity of the front end portion 18 of the drum portion 10a exposed in the front pocket portion 24 is prevented. Therefore, the possibility of stress corrosion cracking of the rotating shaft 10 is greatly reduced.

同様に、窒素ガス供給機構40の窒素ガス供給源41から圧力調節弁43によって圧力調整された後、高圧の窒素ガスは、分岐した後方窒素ガス供給路45を通り、流量調節弁50によって、後方ポケット部25を通って高炉ガス路2に排出される後述の軸封用窒素ガスの、例えば0.7〜1.0倍の質量流量になるように流量調整される。 Similarly, after the pressure is adjusted by the pressure control valve 43 from the nitrogen gas supply source 41 of the nitrogen gas supply mechanism 40, the high-pressure nitrogen gas passes through the branched rear nitrogen gas supply path 45 and is rearward by the flow rate control valve 50. The flow rate is adjusted so that the mass flow rate of the shaft-sealing nitrogen gas, which will be described later, discharged to the blast furnace gas passage 2 through the pocket portion 25 is, for example, 0.7 to 1.0 times.

続く圧力調節弁51により、吐出口35において第2段動翼12の出口近傍の高炉ガス路2を通る高炉ガスに対して、例えば0.2〜0.5kgf/cm2 だけ高い圧力になるように調整され、出口ケーシング21内を通って図1に示す後方窒素ガス供給路45の吐出口35から後方ポケット部25内へ直接吐出される。 The subsequent pressure control valve 51 increases the pressure at the discharge port 35 by, for example, 0.2 to 0.5 kgf / cm2, with respect to the blast furnace gas passing through the blast furnace gas passage 2 near the outlet of the second stage moving blade 12. After being adjusted, the gas is directly discharged from the discharge port 35 of the rear nitrogen gas supply path 45 shown in FIG. 1 into the rear pocket portion 25 through the outlet casing 21.

このため、後方ポケット部25内へ直接吐出された高圧の窒素ガスにより、高炉ガスが後方ポケット部25内に進入することが禁止されると共に、たとえ高炉ガスが進入したとしても直ちに窒素置換が行われ、高炉ガスは後方ポケット部25から高炉ガス路2へ速やかに排出される。したがって、後方ポケット部25内に露出する、ドラム部10aの後端部19の近傍の高炉ガスによる腐食が防止される。このため、回転軸10の応力腐食割れの可能性が大幅に低下する。 Therefore, the high-pressure nitrogen gas discharged directly into the rear pocket portion 25 prohibits the blast furnace gas from entering the rear pocket portion 25, and even if the blast furnace gas enters, nitrogen substitution is performed immediately. The blast furnace gas is quickly discharged from the rear pocket portion 25 into the blast furnace gas passage 2. Therefore, corrosion by the blast furnace gas in the vicinity of the rear end portion 19 of the drum portion 10a exposed in the rear pocket portion 25 is prevented. Therefore, the possibility of stress corrosion cracking of the rotating shaft 10 is greatly reduced.

なお、ポケット部24,25へ供給される高圧窒素ガスの上記流量及び圧力に関する上限値及び下限値は、供給する高圧窒素ガス量との関係等で、高炉ガスのポケット部24,25への進入禁止と、一旦進入した高炉ガスのポケット部24,25からの排出とを最も効果的に行うことができる範囲を例示したものであり、ポケット部24,25へ供給する高圧窒素ガスの流量及び圧力は、必ずしも上記範囲に限定されるものではない。必要に応じて適宜に調整される。 The upper and lower limits of the flow rate and pressure of the high-pressure nitrogen gas supplied to the pockets 24 and 25 are related to the amount of high-pressure nitrogen gas to be supplied, and the blast furnace gas enters the pockets 24 and 25. It exemplifies the range in which the prohibition and the discharge of the blast furnace gas once entered from the pockets 24 and 25 can be performed most effectively, and the flow rate and pressure of the high-pressure nitrogen gas supplied to the pockets 24 and 25. Is not necessarily limited to the above range. It will be adjusted as needed.

一方、窒素ガス供給機構40の窒素ガス供給源41から分岐する、図2に破線で示す別路の窒素ガス供給路52が、回転軸10の軸部10bと入口ケーシング20との間、及び回転軸10の軸部10bと出口ケーシング21との間をそれぞれ気密にするための、軸封用窒素ガスを供給する。 On the other hand, another nitrogen gas supply path 52, which is branched from the nitrogen gas supply source 41 of the nitrogen gas supply mechanism 40 and is shown by a broken line in FIG. 2, rotates between the shaft portion 10b of the rotating shaft 10 and the inlet casing 20. Nitrogen gas for sealing the shaft is supplied to make the space between the shaft portion 10b of the shaft 10 and the outlet casing 21 airtight.

この軸封用窒素ガスは、図2に示すように、回転軸10の軸部10bと入口ケーシング20との間、及び回転軸10の軸部10bと出口ケーシング21との間をそれぞれ通って、最終的には上述の前方及び後方ポケット部24,25内へ排出される。前方及び後方ポケット部24,25内では、上述の窒素置換用の高圧の窒素ガスと混合されて、高炉ガス路2へそれぞれ排出される。 As shown in FIG. 2, the shaft sealing nitrogen gas passes between the shaft portion 10b of the rotating shaft 10 and the inlet casing 20, and between the shaft portion 10b of the rotating shaft 10 and the outlet casing 21, respectively. Finally, it is discharged into the above-mentioned front and rear pocket portions 24 and 25. In the front and rear pocket portions 24 and 25, they are mixed with the above-mentioned high-pressure nitrogen gas for nitrogen replacement and discharged to the blast furnace gas passage 2, respectively.

この軸封用窒素ガスにより、たとえわずかな量の高炉ガスが前方ポケット部24や後方ポケット部25に進入したとしても、回転軸10の軸部10bと入口ケーシング20との間の内部や回転軸10の軸部10bと出口ケーシング21との間の内部へ、高炉ガスがさ
らに進入することが阻止される。
Due to this shaft sealing nitrogen gas, even if a small amount of blast furnace gas enters the front pocket portion 24 or the rear pocket portion 25, the inside or the rotating shaft between the shaft portion 10b of the rotating shaft 10 and the inlet casing 20 Further entry of blast furnace gas into the interior between the shaft portion 10b of 10 and the outlet casing 21 is prevented.

したがって、回転軸10、入口ケーシング20、出口ケーシング21の内部腐食は確実に防止される。この軸封用窒素ガスも、上述の窒素ガス供給機構40から供給される。このため、炉頂圧回収タービン1の窒素ガス供給機構全体を極めて簡素化することができる。 Therefore, internal corrosion of the rotating shaft 10, the inlet casing 20, and the outlet casing 21 is reliably prevented. This nitrogen gas for shaft sealing is also supplied from the nitrogen gas supply mechanism 40 described above. Therefore, the entire nitrogen gas supply mechanism of the furnace top pressure recovery turbine 1 can be extremely simplified.

また、上述の窒素ガス供給路44,45は、入口及び出口ケーシング20,21の周方向の複数箇所に配設されているから、窒素ガス供給機構40からの前方及び後方ポケット部24,25内への高圧の窒素ガスの吐出が、入口及び出口ケーシング20,21の周方向に均一に行われ、高炉ガスが前方及び後方ポケット部24,25内に進入することが確実に防止される。したがって、回転軸の応力腐食割れの可能性を一段と低下させることができる。 Further, since the above-mentioned nitrogen gas supply passages 44 and 45 are arranged at a plurality of locations in the circumferential direction of the inlet and outlet casings 20 and 21, the front and rear pocket portions 24 and 25 from the nitrogen gas supply mechanism 40 are included. The high-pressure nitrogen gas is uniformly discharged to the inlet and outlet casings 20 and 21 in the circumferential direction, and the blast furnace gas is surely prevented from entering the front and rear pocket portions 24 and 25. Therefore, the possibility of stress corrosion cracking of the rotating shaft can be further reduced.

なお、上述の炉頂圧回収タービンの腐食防止装置は一例にすぎず、本発明の趣旨に基づいて種々の変形が可能であり、それらを本発明の範囲から除外するものではない。 The above-mentioned corrosion prevention device for the furnace top pressure recovery turbine is only an example, and various modifications can be made based on the gist of the present invention, and these are not excluded from the scope of the present invention.

1 炉頂圧回収タービン
2 高炉ガス路
3,4 内側部
10 回転軸
10a ドラム部
10b 軸部
11 第1段動翼(初段動翼)
11a プラットフォーム
12 第2段動翼(最終段動翼)
12a プラットフォーム
13 前方延出部
14 後方延出部
15,16,17 保護部材
18 前端部(軸方向端部)
19 後端部(軸方向端部)
20 入口ケーシング
21 出口ケーシング
22 後端部(軸方向端部)
23 前端部(軸方向端部)
24 前方ポケット部
25 後方ポケット部
26 前方開口部
27 後方開口部
30 中央ケーシング
32 前方窒素ガス供給路
33 後方窒素ガス供給路
34,35 吐出口
36 前方空洞部(空洞部)
40 窒素ガス供給機構
41 窒素ガス供給源
42 窒素ガス供給路
43 圧力調節弁
44 前方窒素ガス供給路
45 後方窒素ガス供給路
47 流量調整弁
48 圧力調節弁
50 流量調整弁
51 圧力調節弁
52 窒素ガス供給路
100,101 ケーシング
102 回転軸
102a ドラム部
103,104 ポケット部
105 前端部
106 後端部
1 Furnace top pressure recovery turbine 2 Blast furnace gas passage 3, 4 Inner part 10 Rotating shaft 10a Drum part 10b Shaft part 11 First stage rotor blade (first stage rotor blade)
11a Platform 12 Second stage rotor blade (final stage rotor blade)
12a Platform 13 Front extension 14 Rear extension 15, 16, 17 Protective member 18 Front end (axial end)
19 Rear end (axial end)
20 Inlet casing 21 Outlet casing 22 Rear end (axial end)
23 Front end (axial end)
24 Front pocket 25 Rear pocket 26 Front opening 27 Rear opening 30 Central casing 32 Front nitrogen gas supply path 33 Rear nitrogen gas supply path 34, 35 Discharge port 36 Front cavity (cavity)
40 Nitrogen gas supply mechanism 41 Nitrogen gas supply source 42 Nitrogen gas supply path 43 Pressure control valve 44 Front nitrogen gas supply path 45 Rear nitrogen gas supply path 47 Flow control valve 48 Pressure control valve 50 Flow control valve 51 Pressure control valve 52 Nitrogen gas Supply path 100, 101 Casing 102 Rotating shaft 102a Drum part 103, 104 Pocket part 105 Front end part 106 Rear end part

Claims (4)

炉頂圧回収タービン発電設備に使用されて高炉から供給される高炉ガスにより回転駆動される炉頂圧回収タービン(1)の回転軸の腐食防止装置であって、小径の軸部(10b)と大径のドラム部(10a)とを有する回転軸(10)と、前記ドラム部に取り付けられて前記高炉ガスにより前記回転軸を回転駆動させる動翼(11,12)と、前記ドラム部の軸方向端部(18,19)の外側に全周にわたって環状に延びる一定幅の隙間である開口部(26,27)を介して配設されて高炉ガス路(2)の内側部(3,4)を形成するケーシング(20,21)と、前記開口部の内部に、かつ前記ドラム部の前記軸方向端部と前記ケーシングの軸方向端部(22,23)との間に形成された拡大空洞からなるポケット部(24,25)と、前記ケーシングの内部を通って前記ポケット部又は前記ポケット部の近傍に開口する吐出口(34,35)と、前記動翼を通過する前記高炉ガスよりも圧力が高い窒素ガスを前記吐出口へ供給する窒素ガス供給路(44,45)と、前記窒素ガスを前記窒素ガス供給路へ供給する窒素ガス供給機構(40)とを備えたことを特徴とする炉頂圧回収タービンの回転軸の腐食防止装置。 Top pressure recovery turbine A corrosion prevention device for the rotating shaft of the top pressure recovery turbine (1), which is used in power generation equipment and is rotationally driven by blast furnace gas supplied from the blast furnace, and has a small diameter shaft (10b). A rotating shaft (10) having a large-diameter drum portion (10a), a moving blade (11, 12) attached to the drum portion and rotationally driving the rotating shaft by the blast furnace gas, and a shaft of the drum portion. The inner part (3,4) of the blast furnace gas passage (2) is arranged through an opening (26,27) which is a gap having a constant width extending in a ring shape over the entire circumference on the outer side of the directional end (18, 19). ), And an enlargement formed inside the opening and between the axial end of the drum and the axial end of the casing (22, 23). From the hollow pocket portion (24, 25), the discharge port (34, 35) that passes through the inside of the casing and opens in the vicinity of the pocket portion or the pocket portion, and the blast furnace gas that passes through the turbine blade. It is also characterized by having a nitrogen gas supply path (44, 45) for supplying high-pressure nitrogen gas to the discharge port and a nitrogen gas supply mechanism (40) for supplying the nitrogen gas to the nitrogen gas supply path. A device for preventing corrosion of the rotating shaft of the furnace top pressure recovery turbine. 前記窒素ガス供給路(44,45)は、前記ケーシング(20,21)内において周方向の複数箇所に配設されていることを特徴とする請求項1に記載の炉頂圧回収タービンの回転軸の腐食防止装置。 The rotation of the furnace top pressure recovery turbine according to claim 1, wherein the nitrogen gas supply passages (44, 45) are arranged at a plurality of locations in the circumferential direction in the casing (20, 21). Shaft corrosion protection device. 前記ケーシング(20)内の前記周方向の複数箇所に配設された前記窒素ガス供給路(44)は、前記ケーシング内に配設された周方向に延びる空洞部(36)を介して前記吐出口(34)まで連通していることを特徴とする請求項に記載の炉頂圧回収タービンの回転軸の腐食防止装置。 The nitrogen gas supply paths (44) arranged at a plurality of locations in the circumferential direction in the casing (20) are discharged through the cavity portions (36) arranged in the casing in the circumferential direction. The corrosion prevention device for a rotary shaft of a furnace top pressure recovery turbine according to claim 2 , wherein the turbine communicates with the outlet (34). 前記ケーシング(20,21)と前記回転軸(10)との間は、前記窒素ガス供給路(44,45)とは別路で前記窒素ガス供給機構(40)から供給された軸封用窒素ガスにより与圧にされて内部への前記高炉ガスの進入が禁止されることを特徴とする請求項1ないし3のいずれかに記載の炉頂圧回収タービンの回転軸の腐食防止装置。
The shaft sealing nitrogen supplied from the nitrogen gas supply mechanism (40) is separated from the nitrogen gas supply path (44, 45) between the casing (20, 21) and the rotating shaft (10). The corrosion prevention device for a rotary shaft of a furnace top pressure recovery turbine according to any one of claims 1 to 3, wherein the blast furnace gas is pressurized by gas to prevent the blast furnace gas from entering the inside.
JP2017073331A 2017-04-01 2017-04-01 Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine Active JP6911235B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2017073331A JP6911235B2 (en) 2017-04-01 2017-04-01 Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2017073331A JP6911235B2 (en) 2017-04-01 2017-04-01 Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine

Publications (2)

Publication Number Publication Date
JP2018173070A JP2018173070A (en) 2018-11-08
JP6911235B2 true JP6911235B2 (en) 2021-07-28

Family

ID=64108543

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2017073331A Active JP6911235B2 (en) 2017-04-01 2017-04-01 Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine

Country Status (1)

Country Link
JP (1) JP6911235B2 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5446904U (en) * 1977-09-09 1979-03-31
JPS58154833U (en) * 1982-04-10 1983-10-17 三井造船株式会社 Stator vane shaft sealing device for top pressure recovery turbine
JP3316424B2 (en) * 1997-07-02 2002-08-19 三菱重工業株式会社 gas turbine
JP5734052B2 (en) * 2011-03-30 2015-06-10 三菱重工業株式会社 Rotary shaft seal structure

Also Published As

Publication number Publication date
JP2018173070A (en) 2018-11-08

Similar Documents

Publication Publication Date Title
US10352249B2 (en) Gas turbine power generation equipment, and device and method for drying gas turbine cooling air system
JP5416712B2 (en) Turbine and method for cleaning turbine stator blades in operating condition
CN105736481B (en) Dust Extraction Devices for Gas Turbine Engines
US7922825B2 (en) Extraneous matter removing system for turbine
CN101818664B (en) Rotor chamber cover member having aperture for dirt separation and related turbine
US20170362955A1 (en) Piping system cleaning method, piping system, and steam turbine plant
JP6911235B2 (en) Corrosion prevention device for the rotating shaft of the furnace top pressure recovery turbine
JP5324034B2 (en) Shaft sealing structure for transmission expander or transmission compressor, and transmission expander or transmission compressor having shaft sealing structure
US11333043B2 (en) Steam turbine plant
US11691246B2 (en) Methods for cleaning flow path components of power systems and sump purge kits
US10352196B2 (en) Gas turbine operation method and operation control device
US9816391B2 (en) Compressor wash system with spheroids
JP6416382B2 (en) Steam turbine and method of operating steam turbine
KR102120499B1 (en) Cleaning device of an exhaust gas turbine
US6242819B1 (en) Gas expansion turbine for low power output
JP6211367B2 (en) Supercharger cleaning device, supercharger provided with the same, internal combustion engine provided therewith, and supercharger cleaning method
JP6855659B2 (en) Rotating shaft structure of top pressure recovery turbine
JP2012140901A (en) Condensate type steam turbine, and method of remodeling the same
US20140126998A1 (en) Compressor Bellmouth with a Wash Door
JP2000240470A (en) Gas turbine equipment
TW202417731A (en) Steam turbine and modification method thereof
JP2014084744A (en) Dust adhesion prevention device for stator blade of furnace top pressure recovery turbine
WO2024135490A1 (en) Rust prevention method for gas turbine and gas turbine equipment capable of executing same
JPH07269372A (en) Gas turbine fuel supply system
JP2024527794A5 (en)

Legal Events

Date Code Title Description
A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20180612

A625 Written request for application examination (by other person)

Free format text: JAPANESE INTERMEDIATE CODE: A625

Effective date: 20200304

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20201224

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20210112

A601 Written request for extension of time

Free format text: JAPANESE INTERMEDIATE CODE: A601

Effective date: 20210308

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20210422

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20210608

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20210608

R150 Certificate of patent or registration of utility model

Ref document number: 6911235

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250