JPH046247A - Steel for waste incineration furnace boiler - Google Patents
Steel for waste incineration furnace boilerInfo
- Publication number
- JPH046247A JPH046247A JP10714690A JP10714690A JPH046247A JP H046247 A JPH046247 A JP H046247A JP 10714690 A JP10714690 A JP 10714690A JP 10714690 A JP10714690 A JP 10714690A JP H046247 A JPH046247 A JP H046247A
- Authority
- JP
- Japan
- Prior art keywords
- steel
- corrosion
- boiler
- waste incineration
- less
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、蒸気温度400℃まで使用可能な、ごみ焼却
炉ボイラ用鋼に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a steel for waste incinerator boilers that can be used at steam temperatures up to 400°C.
都市ごみ焼却炉では、燃焼によって生じる排熱をエネル
ギー源として有効利用するために、排熱ボイラを設置し
、発電を行う例が多くなってきている。発電ボイラの熱
効率は、蒸気条件が高温高圧になるほど向上することは
自明であるが、例えば「火力発電」昭和45年第21巻
第5号489頁で公知のごとく、ごみ焼却炉では、ごみ
中に多く含まれる塩化ビニル等の燃焼によって、腐食性
の高いHαガスが高濃度に発生し、さらに塩化物系の低
融点共晶化合物が管に付着するため、蒸気温度が300
℃を越えると、著しく腐食が加速され、腐食を避けるた
め、やむなく蒸気条件を300°C以下に抑えて低効率
操業をしているのが現状である。しかしながらエネルギ
ーの有効利用の観点から、ごみ発電の高温高圧化は強く
望まれている課題である。In order to effectively utilize the exhaust heat generated by combustion as an energy source, municipal waste incinerators are increasingly equipped with exhaust heat boilers to generate electricity. It is obvious that the thermal efficiency of a power generation boiler improves as the steam conditions become higher temperature and higher pressure. Due to the combustion of vinyl chloride, etc., which is contained in large amounts in
If the temperature exceeds 300°C, corrosion will be significantly accelerated, and in order to avoid corrosion, the current situation is that steam conditions must be kept below 300°C to operate at low efficiency. However, from the perspective of effective energy use, increasing the temperature and pressure of waste power generation is strongly desired.
塩化水素ガス、溶融塩酸塩環境では、Crが蒸気圧の高
い塩化物を形成するため、ステンレス鋼等の従来からの
耐食合金では十分な耐食効果が得られない、また、Ni
は比較的この環境では有効であるが、含有量を増すと高
価となる欠点があり、現状ではごみ焼却ボイラにはCr
−Mo系低合金鋼が使用されている。In hydrogen chloride gas and molten hydrochloride environments, Cr forms chlorides with high vapor pressure, so conventional corrosion-resistant alloys such as stainless steel cannot provide sufficient corrosion resistance.
Although Cr is relatively effective in this environment, it has the disadvantage of becoming expensive as the content increases, and currently waste incineration boilers do not use Cr.
-Mo based low alloy steel is used.
本発明は、現状の蒸気温度400℃まで使用可能でかつ
安価な、ごみ焼却炉ボイラ用鋼を提供することを目的と
する。An object of the present invention is to provide a steel for a waste incinerator boiler that can be used up to the current steam temperature of 400° C. and is inexpensive.
本発明は上記課題を解決すべく研究を行った結果、蒸気
温度400℃までは、Cr塩化物の揮発が腐食を律速す
るため、Crの添加は有害であり、10%以下に抑える
必要があることが判明し、さらにこの条件の下で、Si
を0.5%以上含有しかつオーステナイト相とすること
により塩化水素ガス、溶融塩酸塩による高温耐食性が著
しく向上するという知見が得られたことにより完成され
たものであり、その要旨とするところは、重量%にてC
:0.02〜0.1%、St:0.5〜5%、Mn:5
%以下、Cr:5〜10%、Ni:5〜30%、Mo:
0.5〜3%を含有するか、さらに
(1)N : 0.05〜0.4%、 Cu: 0.2
〜0.5%の1種以上、
(2)Nb : 0.05〜2%、Ti:0.02〜0
.5%の1種以上
のうちの両項目またはいずれかを含有するかし、残部が
Feおよび不可避的不純物からなることを特徴とするご
み焼却炉ボイラ用鋼にある。As a result of research conducted to solve the above problems, the present invention found that when the steam temperature is up to 400°C, the volatilization of Cr chloride limits the rate of corrosion, so the addition of Cr is harmful and needs to be kept below 10%. It was found that under these conditions, Si
It was completed based on the finding that high-temperature corrosion resistance by hydrogen chloride gas and molten hydrochloride is significantly improved by containing 0.5% or more and forming an austenite phase. , C in weight%
: 0.02-0.1%, St: 0.5-5%, Mn: 5
% or less, Cr: 5-10%, Ni: 5-30%, Mo:
(1) N: 0.05-0.4%, Cu: 0.2
-0.5% of one or more types, (2) Nb: 0.05-2%, Ti: 0.02-0
.. A steel for a waste incinerator boiler is characterized in that the steel contains 5% of one or more of the two or more items, and the balance is Fe and inevitable impurities.
以下に成分の限定理由について説明する。 The reasons for limiting the ingredients will be explained below.
Cは塩化水素、溶融塩酸塩による耐食性に害を及ぼすも
のであり、できるだけ少ない方が望ましいが、高温での
強度確保に必要であり、また、オーステナイト相の安定
化にも有効であるため、各特性を損なわない範囲として
、上限を0.1%、下限を0.02%とした。C is harmful to corrosion resistance due to hydrogen chloride and molten hydrochloride, and it is desirable to reduce it as much as possible, but since it is necessary to ensure strength at high temperatures and is also effective in stabilizing the austenite phase, each The upper limit was set to 0.1% and the lower limit was set to 0.02% as a range that does not impair the characteristics.
Siは塩化水素、溶融塩酸塩環境における耐食性確保に
きわめて有効な元素である。しかし5%を越えて含有さ
せると加工性、溶接性の劣化を招き、0.5%未満では
十分な耐食効果が得られないため、上限を5%、下限を
0.5%とした。Si is an extremely effective element for ensuring corrosion resistance in hydrogen chloride and molten hydrochloride environments. However, if the content exceeds 5%, workability and weldability will deteriorate, and if it is less than 0.5%, a sufficient corrosion resistance effect cannot be obtained, so the upper limit was set at 5% and the lower limit was set at 0.5%.
Mnはオーステナイト相形成に寄与する元素であるが、
過度の添加は溶製上、熱間加工上のトラブルを生ずるた
め、上限を5%とした。Mn is an element that contributes to austenite phase formation,
Excessive addition causes problems in melting and hot processing, so the upper limit was set at 5%.
Crは一般の高温酸化、高温腐食特性向上には有効であ
るが、蒸気温度400°Cまでの条件では、塩化水素、
溶融塩酸塩環境においてはCr塩化物の揮発が腐食を律
速するため、むしろ有害であり、なるべく低い方が望ま
しく、10%以下とする。しかし、ボイラ停止時の結露
による耐塩酸露点腐食性や、ボイラ鋼管内面の耐水蒸気
酸化性を確保するために、5%以上の添加は必須である
。このため、上限を10%、下限を5%とした。Cr is effective for general high-temperature oxidation and improving high-temperature corrosion properties, but at steam temperatures up to 400°C, hydrogen chloride,
In a molten hydrochloride environment, the volatilization of Cr chloride is rate-limiting for corrosion and is rather harmful, so it is desirable to keep it as low as possible, and it is set at 10% or less. However, in order to ensure resistance to hydrochloric acid dew point corrosion due to dew condensation when the boiler is stopped and resistance to steam oxidation on the inner surface of the boiler steel pipes, addition of 5% or more is essential. Therefore, the upper limit was set to 10% and the lower limit was set to 5%.
Niは塩化水素、溶融塩酸塩環境における耐食性向上に
好ましく、オーステナイト相形成のためにも必要な成分
である。上述のCr、 Si量に応じてオーステナイト
相安定に必要な量が決定されるため、5%以上の添加が
必要である。一方、Ni量の上昇とともに鋼材価格も上
昇するが、30%を越えると価格に見合うだけの特性の
向上が得られない。Ni is preferable for improving corrosion resistance in a hydrogen chloride or molten hydrochloride environment, and is also a necessary component for forming an austenite phase. Since the amount necessary for stabilizing the austenite phase is determined depending on the above-mentioned amounts of Cr and Si, it is necessary to add 5% or more. On the other hand, as the Ni content increases, the price of steel material also increases, but if it exceeds 30%, the properties cannot be improved enough to justify the price.
このため、上限を30%、下限を5%とした。Therefore, the upper limit was set to 30% and the lower limit was set to 5%.
Moは高温での耐食性には効果がないが、ボイラ停止時
の結露によって生ずる塩酸露点腐食を防止するために必
要な成分であり、その目的のためには0.5%以上の添
加が必要である。しかし、オーステナイト相を安定化す
るという面から3%を上限とした。Although Mo has no effect on corrosion resistance at high temperatures, it is a necessary component to prevent hydrochloric acid dew point corrosion caused by dew condensation when the boiler is stopped, and for that purpose it is necessary to add 0.5% or more. be. However, in order to stabilize the austenite phase, the upper limit was set at 3%.
本発明ではこのほかに下記の成分も添加してよい。In the present invention, the following components may also be added.
Nは高温強度の向上、オーステナイト相形成に有効な元
素であり、Cr、 Siの量により、必要に応じて添加
されるものであって、その効果を得るためには0.05
%以上の添加が必要である。しかし、0.4%鰯の添加
は、鋼中に気泡を発生させるとともに、窒化物の形成が
著しくなり、靭性劣化を招くため、上限を0.4%、下
限を0.05%とした。N is an element effective in improving high-temperature strength and forming an austenite phase, and is added as necessary depending on the amount of Cr and Si.
It is necessary to add more than %. However, the addition of 0.4% sardine generates bubbles in the steel, and the formation of nitrides becomes significant, leading to deterioration of toughness, so the upper limit was set to 0.4% and the lower limit was set to 0.05%.
Nb 、 Tiは、特に高温強度が要求される場合に添
加されるものであり、その効果を得るためにはNbは0
.05%以上、Tiは0.02%以上必要である。Nb and Ti are added when high-temperature strength is required, and in order to obtain this effect, Nb is added to 0.
.. 0.05% or more, and Ti is required to be 0.02% or more.
しかし、Nb、 Tiがそれぞれ2%、0.5%を越え
ると、それらの炭化物、窒化物の生成量が過剰となり、
逆に強度低下をもたらす。従って、Nb添加量は0.0
5〜2%、Ti添加量は0.02〜0.5%とした。However, when Nb and Ti exceed 2% and 0.5%, respectively, the amount of carbides and nitrides produced becomes excessive.
On the contrary, it causes a decrease in strength. Therefore, the amount of Nb added is 0.0
The amount of Ti added was 0.02 to 0.5%.
Cuはオーステナイト相形成に有効な元素である。Cu is an element effective in forming an austenite phase.
また、耐酸性を向上させる効果もあり、特に塩酸露点腐
食等の低温での耐食性が要求される場合に062〜0.
5%添加する。下限を0.2%にしたのは、これ未満で
は十分な効果が得られないからであり、また、上限を0
.5%としたのは、0.5%を越えて添加すると熱間加
工性が著しく損なわれるからである。It also has the effect of improving acid resistance, especially when corrosion resistance at low temperatures such as hydrochloric acid dew point corrosion is required.
Add 5%. The reason why the lower limit was set to 0.2% is that sufficient effects cannot be obtained with less than this, and the upper limit was set to 0.2%.
.. The reason why it is set at 5% is that if it is added in excess of 0.5%, hot workability will be significantly impaired.
本発明は、蒸気条件400°Cまで使用可能な、ごみ焼
却ボイラ用過熱器官として開発、発明された鋼である。The present invention is a steel developed and invented as a superheating device for waste incineration boilers that can be used under steam conditions up to 400°C.
第1表Nα1〜32に示す、請求項1〜4のいずれかの
組成を有する鋼それぞれ20kgを真空誘導加熱炉を用
いて溶解した。これを熱間圧延にて板厚10mmの板に
し、1150°Cで601n加熱後急冷した後、15
X 25 X 41の試験片を作製した。従来材には、
第1表に示す化学成分のJIS規格5TBA24゜5U
S304を用いた。腐食試験は、第1図に示すように、
KCj、 NaC1を等モルづつ混合した合成灰中に試
験片を浸漬し、0.2%Hα+30%H20+5%O2
+ba!、 H2の混合ガス気流中で500℃×24h
r加熱することにより行った。500℃は蒸気温度40
0°Cの場合に、管外表面として考えられる温度である
。腐食試験結果の評価は、脱スケール後の腐食減量で行
った。腐食試験結果を第1表に併せて示す。従来材の腐
食量が25+sg/d以上であるのに対し、本発明鋼の
腐食量は20s+g/cr1以下と、はるかに高い耐食
性を示している。このように本発明鋼は塩化水素ガス、
溶融塩酸塩環境で極めて高い耐食性を示すことが明かと
なった。20 kg of each steel having a composition according to any one of Claims 1 to 4 shown in Table 1 Nα1 to Nα1 to Nα32 was melted using a vacuum induction heating furnace. This was hot rolled into a plate with a thickness of 10 mm, heated at 1150°C for 601n, then rapidly cooled,
A test piece measuring 25 x 41 was prepared. Conventional materials include
JIS standard 5TBA24゜5U of chemical components shown in Table 1
S304 was used. The corrosion test is as shown in Figure 1.
The test piece was immersed in synthetic ash mixed with equal moles of KCj and NaCl, and 0.2% Hα + 30% H20 + 5% O2
+ba! , 500℃×24h in a mixed gas flow of H2
This was done by heating. 500℃ is steam temperature 40
In the case of 0°C, this is the temperature considered as the outer surface of the tube. The corrosion test results were evaluated based on the corrosion weight loss after descaling. The corrosion test results are also shown in Table 1. While the amount of corrosion of the conventional material is 25+sg/d or more, the amount of corrosion of the steel of the present invention is less than 20s+g/cr1, showing much higher corrosion resistance. In this way, the steel of the present invention can contain hydrogen chloride gas,
It has been revealed that it exhibits extremely high corrosion resistance in a molten hydrochloride environment.
さらに、第1表に示した本発明鋼については、高温強度
、時効後靭性、加工性、溶接性についても、ボイラ用鋼
として十分な値が得られた。Furthermore, for the steels of the present invention shown in Table 1, sufficient values were obtained for high temperature strength, toughness after aging, workability, and weldability as steels for boilers.
本発明によれば、400℃までの蒸気温度で使用される
ごみ焼却ボイラの過熱器官等に対して、塩化水素ガス、
溶融塩酸塩による耐食性の優れた材料を提供することが
可能になり、産業の発展に寄与するところ極めて大なる
ものがある。According to the present invention, hydrogen chloride gas,
It has become possible to provide a material with excellent corrosion resistance due to molten hydrochloride, which will greatly contribute to the development of industry.
第1図は腐食試験の方法を説明する模式図である。符号
1は試験片、符号2は合成法、符号3は石英皿、符号4
は加熱炉、符号5は腐食ガスを示す。FIG. 1 is a schematic diagram illustrating the corrosion test method. Code 1 is the test piece, code 2 is the synthesis method, code 3 is the quartz dish, code 4
5 indicates a heating furnace, and 5 indicates a corrosive gas.
Claims (4)
とを特徴とするごみ焼却炉ボイラ用鋼。(1) In weight% C: 0.02-0.1% Si: 0.5-5% Mn: 5% or less Cr: 5-10% Ni: 5-30% Mo: 0.5-3% A steel for a waste incinerator boiler, characterized in that the remainder consists of Fe and unavoidable impurities.
不純物からなることを特徴とするごみ焼却炉ボイラ用鋼
。(2) In weight% C: 0.02-0.1% Si: 0.5-5% Mn: 5% or less Cr: 5-10% Ni: 5-30% Mo: 0.5-3% Garbage characterized by further containing one or two of Cu: 0.2-0.5% N: 0.05-0.4%, with the remainder consisting of Fe and inevitable impurities. Steel for incinerator boilers.
不純物からなることを特徴とするごみ焼却炉ボイラ用鋼
。(3) In weight% C: 0.02-0.1% Si: 0.5-5% Mn: 5% or less Cr: 5-10% Ni: 5-30% Mo: 0.5-3% In addition to Nb: 0.05-2% Ti: 0.02-0.5% A garbage incinerator characterized in that it further contains one or two of the following, with the remainder consisting of Fe and inevitable impurities. Steel for boilers.
不純物からなることを特徴とするごみ焼却炉ボイラ用鋼
。(4) In weight% C: 0.02-0.1% Si: 0.5-5% Mn: 5% or less Cr: 5-10% Ni: 5-30% Mo: 0.5-3% In addition, one or two of Cu: 0.2-0.5% N: 0.05-0.4% and Nb: 0.05-2% Ti: 0.02-0.5% A steel for a waste incinerator boiler, characterized in that it contains one or two of the following, with the remainder consisting of Fe and inevitable impurities.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10714690A JPH046247A (en) | 1990-04-23 | 1990-04-23 | Steel for waste incineration furnace boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10714690A JPH046247A (en) | 1990-04-23 | 1990-04-23 | Steel for waste incineration furnace boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH046247A true JPH046247A (en) | 1992-01-10 |
Family
ID=14451682
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10714690A Pending JPH046247A (en) | 1990-04-23 | 1990-04-23 | Steel for waste incineration furnace boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH046247A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62264528A (en) * | 1986-03-10 | 1987-11-17 | エルレツク アンデユストリ | Compensation type thermostat apparatus |
| EP0798395A3 (en) * | 1996-03-28 | 1997-12-03 | Kabushiki Kaisha Toshiba | Heat insulating alloy steel and die casting machine parts |
| WO2001025143A1 (en) * | 1999-10-06 | 2001-04-12 | Norsk Hydro Asa | METHOD AND APPARATUS FOR SYNTHESIS OF HCl |
| WO2004031419A1 (en) * | 2002-10-01 | 2004-04-15 | Magotteaux International S.A. | Graphite and nitrogen-free cast alloys |
| US7442264B2 (en) * | 2003-02-27 | 2008-10-28 | Institute Francais Du Petrole | Method of using low alloy anticoking steels with an increased silicon and manganese content in refining and petrochemicals applications |
| WO2012131236A1 (en) * | 2011-03-31 | 2012-10-04 | Mersen France Py Sas | Facility and reactor for directly synthesizing hydrochloric acid from hydrogen and chlorine with heat recovery |
| US8970085B2 (en) | 2011-04-01 | 2015-03-03 | Denso Corporation | Rotor for electric rotating machine and method of manufacturing the same |
-
1990
- 1990-04-23 JP JP10714690A patent/JPH046247A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62264528A (en) * | 1986-03-10 | 1987-11-17 | エルレツク アンデユストリ | Compensation type thermostat apparatus |
| EP0798395A3 (en) * | 1996-03-28 | 1997-12-03 | Kabushiki Kaisha Toshiba | Heat insulating alloy steel and die casting machine parts |
| WO2001025143A1 (en) * | 1999-10-06 | 2001-04-12 | Norsk Hydro Asa | METHOD AND APPARATUS FOR SYNTHESIS OF HCl |
| WO2004031419A1 (en) * | 2002-10-01 | 2004-04-15 | Magotteaux International S.A. | Graphite and nitrogen-free cast alloys |
| US7442264B2 (en) * | 2003-02-27 | 2008-10-28 | Institute Francais Du Petrole | Method of using low alloy anticoking steels with an increased silicon and manganese content in refining and petrochemicals applications |
| WO2012131236A1 (en) * | 2011-03-31 | 2012-10-04 | Mersen France Py Sas | Facility and reactor for directly synthesizing hydrochloric acid from hydrogen and chlorine with heat recovery |
| FR2973365A1 (en) * | 2011-03-31 | 2012-10-05 | Mersen France Py Sas | INSTALLATION AND REACTOR FOR THE DIRECT SYNTHESIS OF HYDROCHLORIC ACID FROM HYDROGEN AND CHLORINE WITH HEAT RECOVERY |
| AU2012236012B2 (en) * | 2011-03-31 | 2015-08-20 | Mersen France Py Sas | Facility and reactor for directly synthesizing hydrochloric acid from hydrogen and chlorine with heat recovery |
| US9415364B2 (en) | 2011-03-31 | 2016-08-16 | Mersen France Py Sas | Facility and reactor for directly synthesizing hydrochloric acid from hydrogen and chlorine with heat recovery |
| US8970085B2 (en) | 2011-04-01 | 2015-03-03 | Denso Corporation | Rotor for electric rotating machine and method of manufacturing the same |
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