JPS5817397B2 - Scrap preheating equipment - Google Patents
Scrap preheating equipmentInfo
- Publication number
- JPS5817397B2 JPS5817397B2 JP55058061A JP5806180A JPS5817397B2 JP S5817397 B2 JPS5817397 B2 JP S5817397B2 JP 55058061 A JP55058061 A JP 55058061A JP 5806180 A JP5806180 A JP 5806180A JP S5817397 B2 JPS5817397 B2 JP S5817397B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- air
- scrap
- temperature
- 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.)
- Expired
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Incineration Of Waste (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Furnace Details (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Description
【発明の詳細な説明】
本発明はスクラップを原料として供給するようにした溶
解炉におけるスクラップ原料の予熱設備に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to equipment for preheating scrap raw material in a melting furnace which supplies scrap as raw material.
溶解炉にスクラップを原料として供給する際、溶解炉の
排ガスを利用してスクラップを予熱すること(こより溶
解炉操業の省エネルギー化を図ることが考えられている
。When supplying scrap as raw material to a melting furnace, the waste gas from the melting furnace is used to preheat the scrap (this is thought to be a way to save energy in the operation of the melting furnace).
しかし従来のスクラップ予熱設備は、溶解炉からの排ガ
スを単純に予熱器内のスクラップに通気させて加熱を行
うようにしているため、加熱によって排ガス温度が低下
し、従ってスクラップ内に含まれる油脂分等の可燃成分
、プラスチック等の分解による臭気成分が燃焼及び加熱
分解されることなく大気に排出されて著しく環境を悪化
させる問題を生じていた。However, with conventional scrap preheating equipment, the exhaust gas from the melting furnace is simply vented through the scrap in the preheater to heat it, so heating lowers the exhaust gas temperature, which reduces the amount of oil and fat contained in the scrap. combustible components such as plastics, etc., and odor components resulting from the decomposition of plastics, etc., are emitted into the atmosphere without being burned or thermally decomposed, resulting in a problem that significantly deteriorates the environment.
又斯かる予備設備にあっては、エルボシール部等の空気
漏入部から吸引される空気により排ガス温度を低下させ
てしまうので、排カス利用を阻害する一因ともなってい
た。In addition, in such preliminary equipment, the exhaust gas temperature is lowered by the air sucked through the air leakage portion such as the elbow seal portion, which has also been a factor in inhibiting the utilization of the exhaust gas.
本発明は前記実情fこ鑑みなしたもので、溶解炉と、該
溶解炉からの排ガスの燃焼を行わしめる燃焼炉と、前記
溶解炉と燃焼炉との間の配管中に備えたエルボシール部
と、前記燃焼炉からのガスによってスクラップの予熱を
行う予熱器と、該予熱器からの予熱後のガス中に含有す
る可燃成分の燃焼及び臭気成分の分解を行う分解炉と、
前記燃焼炉からのガスを分岐して導き高温の種火を形成
するよう前記分解炉に設けたパイロットバーナと、前記
分解炉からの高温ガスによって送風機からの空気を加熱
せしめる空気加熱器と、該空気加熱器からの加熱空気を
前記エルボシール部tこ導く加熱空気配管、とを備えた
ことを特徴とするスクラップ予熱設備に係るものである
。The present invention has been made in view of the above-mentioned actual situation, and includes a melting furnace, a combustion furnace for combusting exhaust gas from the melting furnace, and an elbow seal portion provided in the piping between the melting furnace and the combustion furnace. a preheater that preheats scrap with gas from the combustion furnace; a cracking furnace that burns combustible components and decomposes odor components contained in the preheated gas from the preheater;
a pilot burner provided in the cracking furnace to branch and guide gas from the combustion furnace to form a high-temperature pilot flame; an air heater that heats air from a blower with the high-temperature gas from the cracking furnace; The present invention relates to a scrap preheating equipment characterized by comprising: a heated air pipe that guides heated air from an air heater to the elbow seal portion t.
以下図面を参照しつつ本発明の詳細な説明する。The present invention will be described in detail below with reference to the drawings.
図面は本発明の概略を示すフローシートであり、溶解炉
、例えば電気炉1に電気炉1からの排ガス(通常830
〜850℃程度)中のCOを完全に燃焼させて爆発等の
危険性を無くすよう設計され且つプレダスタ−としての
機能を充分備えた燃焼炉2をエルボ3及び排ガス管4を
介し接続し、該燃焼炉2には、燃焼炉2からの予熱用ガ
スによってスクラップを予熱するための予熱器5を予熱
用ガス配管6を介し接続し、該予熱器5には、予熱によ
って温度が低下しく300〜500’C程度)且つスク
ラップ中に含まれる油分及びプラスチック等Eこより生
じた可燃成分や臭気成分を含有した予熱後ガスを加熱処
理するための分解炉7を予熱後ガス配管8を介し接続す
る。The drawing is a flow sheet showing the outline of the present invention, in which exhaust gas (usually 830
A combustion furnace 2, which is designed to completely combust the CO in the atmosphere (approximately 850°C to 850°C) and eliminate the risk of explosion, and is fully equipped with the function of a pre-duster, is connected via an elbow 3 and an exhaust gas pipe 4. A preheater 5 for preheating the scrap with preheating gas from the combustion furnace 2 is connected to the combustion furnace 2 via a preheating gas pipe 6. A decomposition furnace 7 is connected via a preheated gas pipe 8 to heat-treat the preheated gas containing combustible components and odor components generated from oil, plastic, etc. contained in the scrap.
分解炉7にはその上部に種火として作用するパイロット
バーナ9を備える。The decomposition furnace 7 is equipped with a pilot burner 9 at its upper part, which acts as a pilot flame.
パイロットバーナ9は、灯油、酸素を供給する燃料導入
部10と、空気予熱器11を備えて予熱した空気を供給
する燃焼空気導入部12と、前記予熱用ガス配管6の一
部を分岐して供給する高温ガス導入部13とを備えて前
記分解炉7内に柱状火炎を形成させ、前記予熱器5から
の予熱後ガスを直接接触させるようにし然も分解炉γ内
温度を750℃程度以上に珠持てきるようにしている。The pilot burner 9 has a fuel introduction section 10 that supplies kerosene and oxygen, a combustion air introduction section 12 that is equipped with an air preheater 11 and supplies preheated air, and a part of the preheating gas pipe 6 branched off. A columnar flame is formed in the decomposition furnace 7 by supplying a high-temperature gas introduction part 13, and the preheated gas from the preheater 5 is brought into direct contact with the decomposition furnace γ, and the temperature inside the decomposition furnace γ is kept at about 750° C. or more. I try to hold as many beads as possible.
前記分解炉7をこは配管14を介し空気加熱器15を接
続して分解炉7(こて加熱されたガスと送風器16から
送給された空気とを熱交換できるようにし、更瘉こ熱回
収されたガスを集塵器保護のためのガスクーラー17、
集塵器1B、コントロールダンパー19、排風機20を
順次介して煙突21から大気に排出し得るよう配管構成
する。The decomposition furnace 7 is connected to an air heater 15 via piping 14 to enable heat exchange between the gas heated by the trowel and the air supplied from the blower 16. a gas cooler 17 for protecting the heat-recovered gas from a dust collector;
The piping is configured so that it can be discharged to the atmosphere from a chimney 21 via a dust collector 1B, a control damper 19, and an exhaust fan 20 in this order.
又、前記エルボ3部にフード3′を設けると共に該フー
ド3′に前記空気加熱器15からの加熱空気配管22を
接続し、加熱空気をエルボ3部に送給することによりエ
ルボ3の空気漏入部から外部の空気(冷風)を吸引させ
ないようにする。Furthermore, a hood 3' is provided on the elbow 3, and the heated air pipe 22 from the air heater 15 is connected to the hood 3' to supply heated air to the elbow 3, thereby eliminating air leakage in the elbow 3. Prevent outside air (cold air) from being sucked in from the entrance.
尚、図中23.24は予熱器5へ導入するガス量とパイ
ロットバーナ9へ導入するガス量とを調節して分解炉7
1にてスクラップ排気の可燃成分の燃焼、臭気成分の分
解に必要な温度を確保するためのダンパーである。In addition, 23 and 24 in the figure are used to control the decomposition furnace 7 by adjusting the amount of gas introduced into the preheater 5 and the amount of gas introduced into the pilot burner 9.
1 is a damper for ensuring the temperature necessary for burning the combustible components of the scrap exhaust and decomposing the odor components.
前記構成において、電気炉1から管4を介して排出され
燃焼炉21こて燃焼された予熱用ガスは、配管6を介し
予熱器5に導入されて該予熱器5内のスクラップを予熱
する。In the above configuration, the preheating gas discharged from the electric furnace 1 via the pipe 4 and burned in the combustion furnace 21 is introduced into the preheater 5 via the pipe 6 to preheat the scrap in the preheater 5.
この予熱により予熱後ガスは低温となり且つスクラップ
中に混入している油分等による可燃成分及びプラスナッ
ク等による臭気成分を含んだまま、配管8を介し分解炉
Tに導かれる。Due to this preheating, the preheated gas has a low temperature and is guided to the cracking furnace T through the pipe 8 while containing combustible components such as oil and odor components such as plastic snacks mixed in the scrap.
分解炉7に導入されたガスは、それが含有している可燃
成分を分解炉T内に形成されている高温の柱状火炎1こ
直接接触することにより効果的に燃焼せしめられ、且つ
臭気の原因となる硫化メチル、メチルアミン、アンモニ
ア、アセトアルデヒド等の臭気成分を750°C程度以
上に保たれている分解炉7内温度によって高温加熱分解
されて無臭の物質に変化せしめられる。The gas introduced into the cracking furnace 7 is effectively combusted by directly contacting the combustible components it contains with the high-temperature columnar flame formed in the cracking furnace T, and eliminates the cause of odor. Odor components such as methyl sulfide, methylamine, ammonia, and acetaldehyde are decomposed by high-temperature heating in the decomposition furnace 7, which is maintained at a temperature of about 750° C. or higher, and converted into odorless substances.
この時、分解炉7内温度を800℃以上とすることが好
ましい。At this time, it is preferable that the temperature inside the decomposition furnace 7 is 800° C. or higher.
分解炉7において燃焼、分解を終了したガスは配管14
を介し空気加熱器15に導入され、該空気加熱器15内
をこおいて送風機16から送給された空気を熱交換によ
って加熱昇温せしめる。The gas that has been burned and decomposed in the decomposition furnace 7 is transferred to the pipe 14.
The air is introduced into the air heater 15 through the air heater 15, and the air passed through the air heater 15 and sent from the blower 16 is heated and heated by heat exchange.
この加熱空気は加熱空気配管22によりエルボ3部のフ
ード3′に導かれ、エルボ3の空気漏入部から吸引され
る冷風を遮断すると共に、加熱空気自体が吸引されるよ
う作用する。This heated air is guided by the heated air pipe 22 to the hood 3' of the elbow 3, which acts to block the cold air drawn from the air leakage part of the elbow 3 and to draw the heated air itself.
尚、この加熱空気の供給量の調整は、送風機16の圧力
調節(コントロー )L/ タフ バー 19の使用を
含む)とフード3′の調節によって行う。The amount of heated air to be supplied is adjusted by adjusting the pressure of the blower 16 (including the use of a controller L/tough bar 19) and adjusting the hood 3'.
このようにして空気漏入部から加熱空気が吸引されるの
で、スクラップ予熱用ガス温度の低下を防止し侍て、即
ち予熱ガス温度を昇温せしめてスクラップの予熱効果を
向上させることができる。Since the heated air is sucked through the air leakage portion in this way, it is possible to prevent the temperature of the scrap preheating gas from decreasing, that is, to increase the temperature of the preheating gas, thereby improving the effect of preheating the scrap.
従って配管8を介して分解炉7に導入される予熱後ガス
の温度も高められるので、前記燃料導入部10からの供
給燃料量の減少、燃焼空気量の減少とそれに伴う空気予
熱器11及び図示しないフ狛ワーの小型化、及び分解炉
7内温度の上昇による燃焼、分解機能の向上を図ること
ができる。Therefore, the temperature of the preheated gas introduced into the cracking furnace 7 via the pipe 8 is also increased, so that the amount of fuel supplied from the fuel introduction section 10 is reduced, the amount of combustion air is reduced, and the air preheater 11 and the air preheater 11 (not shown) are accordingly reduced. The combustion and decomposition functions can be improved by reducing the size of the furnace and increasing the temperature inside the decomposition furnace 7.
更に予熱用ガス配管6の一部を分岐してパイロットバー
ナ9に導いていることにより、パイロットバーナ9に高
温の種火を形成することができ、分解炉7内の燃焼、昇
温を効果的に行うことができる。Furthermore, by branching a part of the preheating gas pipe 6 and leading it to the pilot burner 9, a high-temperature pilot flame can be formed in the pilot burner 9, thereby effectively increasing the combustion and temperature inside the cracking furnace 7. can be done.
又前記パイロットバーナ9をこ高温ガス導入部13を介
して導入している高温ガスは、予熱用ガスがスクラップ
を予熱するのに必要な量販上に発生するのでこの余剰分
を利用するようをこしている。Furthermore, the high temperature gas introduced into the pilot burner 9 through the high temperature gas introduction section 13 is generated during mass sales when the preheating gas is necessary for preheating the scrap, so it is recommended to use this surplus. ing.
前記空気加熱器15にて熱を回収された後のガスは、ガ
スクーラー1Tにより集塵器18に支障を来さない温度
まで冷却された後、集塵器18にテ集塵せしめられ、コ
ントロールダンパー19によりその吸引力を調整されつ
つ排風機20(こて吸引され、煙突21より大気に排出
される。After the heat has been recovered by the air heater 15, the gas is cooled by the gas cooler 1T to a temperature that does not cause any trouble to the dust collector 18, and then collected by the dust collector 18 and then controlled. While the suction force is adjusted by the damper 19, the air is sucked in by the exhaust fan 20 (trowel) and discharged into the atmosphere from the chimney 21.
ところで、排風機20による吸引を、従来は電気炉1排
ガス量のioo%増し程度で引っ張るようにしていたた
めに、電気炉1内に不要な過剰空気を吸引してしまい、
そのため過大なエネルギー損失を生じているが、本発明
においては漏入空気の量が従来の半分以下【こなるよう
前述の如くコントロールダンパー19を調節して予熱用
ガスの温度を高め、且つエルボ3部に加熱空気を供給す
ることにより、予熱回路全体のガス温度を高めることが
でき、従ってスクラップの昇温を容易且つ短時間に行う
ことができると共に、分解炉7の機能の向上を図ること
ができ、全体としての熱回収効果を向上させることがで
きる。By the way, conventionally, the suction by the exhaust fan 20 was increased by about ioo% of the amount of exhaust gas in the electric furnace 1, which resulted in unnecessary excessive air being sucked into the electric furnace 1.
This results in excessive energy loss, but in the present invention, the amount of leaked air is less than half of the conventional amount. By supplying heated air to the preheating section, the gas temperature of the entire preheating circuit can be raised, and therefore the temperature of the scrap can be easily and quickly raised, and the functionality of the cracking furnace 7 can be improved. This can improve the overall heat recovery effect.
尚、本発明は前記実施例においてはエルボ3の空気漏入
部に対し加熱空気を供給できるよう加熱空気配管22と
フード3′を設けたが、図において仮想線で示す如く、
電気炉1の空気漏入部に対しフード1′を又予熱器5の
空気漏入部に対しフード5′を夫々必要に応じて設け、
且つ加熱空気配管22からの分岐管22′、21′によ
り夫々加熱空気を供給するようにすれば、スクラップの
予熱効果を更に向上させることができる。Incidentally, in the above embodiment of the present invention, a heated air pipe 22 and a hood 3' were provided so as to supply heated air to the air leakage part of the elbow 3, but as shown by the imaginary line in the figure,
A hood 1' is provided for the air leakage part of the electric furnace 1, and a hood 5' is provided for the air leakage part of the preheater 5, as necessary.
In addition, by supplying heated air through branch pipes 22' and 21' from the heated air pipe 22, the preheating effect of the scrap can be further improved.
尚又、本発明はスクラップの予熱を行う種々の装置に適
用できること、その他本発明の要旨を逸脱しない限り種
々変更を加え得ることは勿論である。Furthermore, it goes without saying that the present invention can be applied to various devices for preheating scrap, and that various other changes can be made without departing from the gist of the present invention.
如上のように本発明によれば、
(i) スクラップの予熱によってガス中に生じる可
燃成分の燃焼及び臭気成分の分解を分解炉にて効果的を
こ行わしめることができるので、排ガスによる公害問題
の発生を防止でき、且つスクラップの利用範囲を拡大し
て廃棄物処理、省資源に寄与し得る。As described above, according to the present invention, (i) The combustion of combustible components and the decomposition of odor components generated in the gas by preheating the scrap can be effectively carried out in the cracking furnace, thereby solving the problem of pollution caused by exhaust gas. It is possible to prevent the occurrence of waste, and expand the range of scrap usage, contributing to waste treatment and resource conservation.
(II)分解炉からの排気の利用(こよる空気加熱器を
設けると共に該空気加熱器からの加熱空気をエルボ部に
導入できるようQこしたので、従来の如き冷風吸引によ
る溶解炉排ガス温度の低下を防止でき、従って予熱効果
を向上できると共に分解炉の高温度維持を図れて燃焼、
分解効果を向上させることができる。(II) Use of exhaust gas from the cracking furnace Therefore, it is possible to improve the preheating effect, maintain the high temperature of the cracking furnace, and improve combustion.
The decomposition effect can be improved.
(曲 分解炉内に燃焼炉からの高温ガスを導入するよう
にしたので、分解炉内温度を上昇して分解炉の機能の向
上を図ることができる。(Since high-temperature gas from the combustion furnace is introduced into the cracking furnace, the temperature inside the cracking furnace can be increased and the functionality of the cracking furnace can be improved.
eV) 新規、既存を問わず類似の技術分野に容易に
適用して実施することができる。eV) Can be easily applied and implemented in similar technical fields, whether new or existing.
等の優れた効果を発揮する。Demonstrates excellent effects such as
図面は本発明の実施例を示すフローシートである。
1・・・・・・電気炉、2・・・・・・燃焼炉、3・・
・・・・エルボ、5・・・・・・予熱器、7・・・・・
・分解炉、9・・・・・・パイロットバーナ、13・・
・・・・高温ガス導入部、15・・・・・・空気加熱室
、16・・・・・・送風機、22・・・・・・加熱空気
配管。The drawing is a flow sheet showing an embodiment of the invention. 1... Electric furnace, 2... Combustion furnace, 3...
...Elbow, 5...Preheater, 7...
・Decomposition furnace, 9...Pilot burner, 13...
...High temperature gas introduction section, 15...Air heating chamber, 16...Blower, 22...Heating air piping.
Claims (1)
る燃焼炉と、前記溶解炉と燃焼炉との間の配管中に備え
たエルボシール部と、前記燃焼炉からのガスによってス
クラップの予熱を行う予熱器と、該予熱器からの予熱後
のガス中に含有する可燃成分の燃焼及び臭気成分の分解
を行う分解炉と前記燃焼炉からのガスを分岐して導き高
温の種火を形成するよう前記分解炉fこ設けたパイロッ
トバーナと、前記分解炉からの高温ガスによって送風機
からの空気を加熱せしめる空気加熱器と、該空気加熱器
からの加熱空気を前記エルボシール部に導く加熱空気配
管、とを備えたこ吉を特徴とするスクラップ予熱設備。1. A melting furnace, a combustion furnace that burns exhaust gas from the melting furnace, an elbow seal provided in the piping between the melting furnace and the combustion furnace, and a preheating of scrap with the gas from the combustion furnace. a decomposition furnace that burns combustible components and decomposes odor components contained in the preheated gas from the preheater; and a decomposition furnace that branches and guides the gas from the combustion furnace to form a high-temperature pilot flame. a pilot burner installed in the decomposition furnace f, an air heater that heats air from the blower with high-temperature gas from the decomposition furnace, and heated air that guides the heated air from the air heater to the elbow seal portion. Scrap preheating equipment featuring Kokichi, equipped with piping, and.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55058061A JPS5817397B2 (en) | 1980-05-01 | 1980-05-01 | Scrap preheating equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55058061A JPS5817397B2 (en) | 1980-05-01 | 1980-05-01 | Scrap preheating equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56155379A JPS56155379A (en) | 1981-12-01 |
JPS5817397B2 true JPS5817397B2 (en) | 1983-04-06 |
Family
ID=13073387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55058061A Expired JPS5817397B2 (en) | 1980-05-01 | 1980-05-01 | Scrap preheating equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5817397B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58158490A (en) * | 1982-03-16 | 1983-09-20 | 大同特殊鋼株式会社 | Method of preheating scrap |
JPS60162179A (en) * | 1984-02-01 | 1985-08-23 | 日立造船株式会社 | Method of controlling inner pressure of electric furnace |
JP4723880B2 (en) * | 2005-03-07 | 2011-07-13 | 株式会社東芝 | Radio wave induction device |
-
1980
- 1980-05-01 JP JP55058061A patent/JPS5817397B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS56155379A (en) | 1981-12-01 |
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