JP2002340313A - Purging method for intermediate hopper in inserting apparatus of waste melting furnace - Google Patents
Purging method for intermediate hopper in inserting apparatus of waste melting furnaceInfo
- Publication number
- JP2002340313A JP2002340313A JP2001147551A JP2001147551A JP2002340313A JP 2002340313 A JP2002340313 A JP 2002340313A JP 2001147551 A JP2001147551 A JP 2001147551A JP 2001147551 A JP2001147551 A JP 2001147551A JP 2002340313 A JP2002340313 A JP 2002340313A
- Authority
- JP
- Japan
- Prior art keywords
- intermediate hopper
- furnace
- gas
- inert gas
- waste
- 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.)
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- Furnace Charging Or Discharging (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、一般廃棄物、産業
廃棄物等の廃棄物を熱分解溶融処理する廃棄物溶融炉の
装入装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for charging a waste melting furnace for thermally decomposing and melting waste such as general waste and industrial waste.
【0002】[0002]
【従来の技術】一般廃棄物、産業廃棄物等の廃棄物の処
理方法として、廃棄物をシャフト炉式の廃棄物溶融炉に
装入し、廃棄物を乾燥、予熱、熱分解、燃焼、溶融し、
スラグやメタルとして取り出す熱分解溶融処理方法が知
られている。2. Description of the Related Art As a method of treating general waste and industrial waste, waste is charged into a shaft furnace type waste melting furnace, and the waste is dried, preheated, pyrolyzed, burned, and melted. And
There is known a thermal decomposition / melting method for extracting slag or metal.
【0003】廃棄物処理炉の装入装置としては、ごみピ
ット等からごみクレーンにより搬送された廃棄物が装入
される時、炉内で発生した熱分解ガスをシールするため
に、上部シールダンパと下部シールダンパを設けてい
る。二重ダンパに囲まれた空間である中間ホッパには、
炉内の可燃性ガスが炉外へ漏出すること、炉外の大気が
炉内へ侵入することを防ぐために不活性ガスが供給され
る。廃棄物処理炉の装入装置への不活性ガスの供給につ
いては、例えば、本出願人の出願に係る特開2000−
310411号に開示されている。[0003] As a charging device for a waste treatment furnace, an upper seal damper is used to seal pyrolysis gas generated in the furnace when waste conveyed by a waste crane from a waste pit or the like is loaded. And a lower seal damper. The intermediate hopper, a space surrounded by double dampers,
An inert gas is supplied to prevent the flammable gas inside the furnace from leaking out of the furnace and to prevent the atmosphere outside the furnace from entering the furnace. The supply of the inert gas to the charging device of the waste treatment furnace is described in, for example, Japanese Patent Application Laid-Open No. 2000-2000 filed by the present applicant.
No. 3,104,411.
【0004】図2は従来の廃棄物処理炉の装入装置を示
す図である。FIG. 2 is a view showing a conventional charging apparatus for a waste treatment furnace.
【0005】図2(a)において、廃棄物は投入ホッパ
1から中間ホッパ2に装入し、廃棄物溶融炉3で乾燥、
熱分解、燃焼、溶融する。廃棄物は溶融炉3の上部に設
けられた中間ホッパ2に一時貯留し、上部シールダンパ
10、下部シールダンパ11が設けられた中間ホッパ2
に不活性ガスや蒸気もしくは燃焼排ガスをパージするこ
とで、炉内ガスの大気への流出を防止及び大気の炉内へ
の侵入を防止ししている。[0005] In FIG. 2 (a), waste is charged from an input hopper 1 into an intermediate hopper 2, and dried in a waste melting furnace 3.
Pyrolyzes, burns, melts. The waste is temporarily stored in an intermediate hopper 2 provided at an upper part of the melting furnace 3, and the intermediate hopper 2 provided with an upper seal damper 10 and a lower seal damper 11 is provided.
By purging inert gas, steam, or combustion exhaust gas, the outflow of the gas in the furnace to the atmosphere and the intrusion of the atmosphere into the furnace are prevented.
【0006】また、図2(b)装入装置では、廃棄物溶
融炉3の炉頂部に中間ホッパ2が設けられ、中間ホッパ
2の上端開口部に上端開口部を開閉する上部シールダン
パ10が設けられ、廃棄物処理炉内に通じる下端開口部
には、下端開口部を開閉する下部シールダンパ11が設
けられ、中間ホッパ内には、中間ホッパ内に装入された
廃棄物を溶融炉内に装入するとともに、中間ホッパと廃
棄物溶融炉内をシールする掻き出しダンパ12が回動自
在に設けられている。In the charging device shown in FIG. 2B, an intermediate hopper 2 is provided at the top of the waste melting furnace 3, and an upper seal damper 10 for opening and closing the upper end opening is provided at the upper end opening of the intermediate hopper 2. A lower seal damper 11 that opens and closes the lower end opening is provided at a lower end opening communicating with the waste treatment furnace, and the waste loaded in the intermediate hopper is placed in the melting furnace in the intermediate hopper. , And a scraping damper 12 for sealing the inside of the intermediate hopper and the waste melting furnace is rotatably provided.
【0007】[0007]
【発明が解決しようとする課題】従来の装入装置では、
不活性ガスを供給するために不活性ガス供給装置を設け
たり、廃棄物処理炉内で発生する排ガスを配管したりし
ている。そのため、不活性ガスを供給するための膨大な
設備費とランニングコストがかかっていた。In the conventional charging device,
An inert gas supply device is provided to supply the inert gas, and exhaust gas generated in the waste treatment furnace is piped. Therefore, a huge facility cost and a running cost for supplying the inert gas are required.
【0008】また、中間ホッパ内に侵入する、CO、N
2、蒸気、H2などの混合ガスである炉内ガスとパージ
する不活性ガスの密度差によって循環流が形成されて、
効率良く中間ホッパ内のガスを追い出すことができなか
った。[0008] Further, CO, N invading the intermediate hopper.
2. A circulating flow is formed by the density difference between the furnace gas, which is a mixed gas such as steam and H 2, and the inert gas to be purged,
The gas in the intermediate hopper could not be efficiently expelled.
【0009】そこで、本発明は、二重ダンパに囲まれた
中間ホッパ内のガスのパージに必要な不活性ガスの使用
量をできるだけ減らすとともに、循環流の発生を抑えて
効率よく中間ホッパ内のガスを追い出し、且つ不活性ガ
ス供給装置の設備を小型化、ランニングコストを低減さ
せることを目的とする。Therefore, the present invention reduces the amount of inert gas required for purging the gas in the intermediate hopper surrounded by the double damper as much as possible, and suppresses the generation of a circulating flow to efficiently reduce the amount of inert gas in the intermediate hopper. It is an object of the present invention to expel gas, reduce the size of equipment of an inert gas supply device, and reduce running costs.
【0010】[0010]
【課題を解決するための手段】本発明の廃棄物溶融炉の
中間ホッパのパージ方法は、廃棄物処理炉の炉頂部に中
間ホッパが設けられ、中間ホッパの上端開口部に上端開
口部を開閉する上部シールダンパが設けられ、廃棄物処
理炉内に通じる下端開口部には、下端開口部を開閉する
下部シールダンパが設けられ、中間ホッパ内の炉内ガス
を不活性ガスでパージする方法において、不活性ガスを
昇温させて不活性ガスの密度を少なくとも中間ホッパ内
の炉内ガスの密度に近似させて中間ホッパの上部からパ
ージすることを特徴とする。According to the method of purging an intermediate hopper of a waste melting furnace according to the present invention, an intermediate hopper is provided at a furnace top of a waste treatment furnace, and an upper end opening is opened and closed at an upper end opening of the intermediate hopper. An upper seal damper is provided, and a lower seal damper that opens and closes a lower end opening is provided at a lower end opening communicating with the waste treatment furnace, and a method of purging furnace gas in an intermediate hopper with an inert gas. The temperature of the inert gas is increased to make the density of the inert gas at least approximate to the density of the gas in the furnace in the intermediate hopper, and the inert gas is purged from above the intermediate hopper.
【0011】[0011]
【発明の実施の形態】本発明は、N2などの不活性ガス
を廃棄物処理炉内で発生させる蒸気による熱交換器や電
気ヒータ等により昇温させて中間ホッパ内のガスの密度
に少なくとも近似させて供給する。なお、中間ホッパの
上部からパージすることで中間ホッパ内のガスの効果的
なパージを実現することができる。また、中間ホッパ内
に廃棄物を掻き出すダンパ(掻き出しダンパと称す)を
有する設備においては、掻き出しダンパからパージして
もよい。DETAILED DESCRIPTION OF THE INVENTION The present invention is at least warmed by the heat exchanger and an electric heater or the like with steam for generating inert gas in waste treatment furnace such as N 2 to a density of gas in the intermediate hopper Supply by approximation. In addition, by purging from the upper part of the intermediate hopper, effective purging of the gas in the intermediate hopper can be realized. Further, in a facility having a damper for scraping waste in the intermediate hopper (referred to as a scraping damper), the purge may be performed from the scraping damper.
【0012】図1は本発明を実施するための廃棄物溶融
設備の全体図である。FIG. 1 is an overall view of a waste melting facility for carrying out the present invention.
【0013】廃棄物溶融炉3には、廃棄物、副資材であ
るコークス、石灰石を炉上部の投入ホッパ1から上部シ
ールダンパ10及び下部シールダンパ11を備えた中間
ホッパ2に装入し、廃棄物溶融炉3で乾燥、熱分解、燃
焼、溶融する。炉内からの可燃分は、熱分解ガスとして
炉上部のダクトから排出され、燃焼室4で燃焼後、ボイ
ラ5、タービン発電機などの付帯設備により熱及び電気
エネルギーとして利用される。その後、排ガスは、ガス
冷却器で冷却され、集じん装置6を経た後、誘引送風機
により煙突7から放出する。In the waste melting furnace 3, waste, coke and limestone as auxiliary materials are charged from the charging hopper 1 at the upper part of the furnace into the intermediate hopper 2 provided with the upper seal damper 10 and the lower seal damper 11, and discarded. It is dried, thermally decomposed, burned and melted in the material melting furnace 3. The combustibles from the furnace are exhausted from a duct at the upper part of the furnace as pyrolysis gas, burned in a combustion chamber 4, and then used as heat and electric energy by auxiliary equipment such as a boiler 5 and a turbine generator. Thereafter, the exhaust gas is cooled by a gas cooler, passes through a dust collecting device 6, and is discharged from a chimney 7 by an induced blower.
【0014】廃棄物溶融炉の下部には空気と酸素を混合
した酸素富化空気を吹き込む送風羽口が設けられ、灰分
はスラグ及びメタルとして出滓口から取り出す。送風羽
口から吹き込んだ酸素富化空気は炉内のコークス及び熱
分解で発生したチャーを燃焼させ、その燃焼熱は炉内に
装入された廃棄物の乾燥、熱分解、及び不燃物の溶融に
利用される。[0014] At the lower part of the waste melting furnace, there is provided a blowing tuyere for blowing oxygen-enriched air, which is a mixture of air and oxygen, and ash is taken out of the slag outlet as slag and metal. The oxygen-enriched air blown from the tuyere burns the coke in the furnace and the char generated by pyrolysis, and the heat of combustion is used to dry the waste loaded in the furnace, pyrolyze it, and melt incombustibles. Used for
【0015】装入装置の中間ホッパ2に吹き込む不活性
ガスとして、例えば窒素発生装置8で発生させた窒素を
ボイラ4で発生させた加圧蒸気(たとえば、約200
℃)を利用する熱交換器9で加熱し、中間ホッパ2に形
成された吹込口13より中間ホッパ2に吹き込む。な
お、吹込口13は、上部シールダンパ10の下面に形成
してもよい。不活性ガスは、加熱させてそのガス密度を
炉内ガスのそれに近似させる。膨張効果を期待して更に
昇温し、不活性ガス密度が炉内ガス密度より小さくなっ
ても不活性ガスは中間ホッパ2の上方に停滞しようとす
るためパージ効果は期待される。As the inert gas blown into the intermediate hopper 2 of the charging apparatus, for example, nitrogen generated by the nitrogen generator 8 is pressurized steam generated by the boiler 4 (for example, about 200
(° C.) and is blown into the intermediate hopper 2 from a blowing port 13 formed in the intermediate hopper 2. The air inlet 13 may be formed on the lower surface of the upper seal damper 10. The inert gas is heated to bring its gas density close to that of the furnace gas. Even if the temperature is further increased in anticipation of the expansion effect and the inert gas density becomes smaller than the gas density in the furnace, the inert gas tends to stagnate above the intermediate hopper 2, so that a purging effect is expected.
【0016】ガスは、温度により体積が膨張し、密度が
下がる。表1は、炉内ガス(CO、N2、CO2、H2
O、H2、CH4等を主成分とする混合ガス)の温度と
密度と、中間ホッパに吹き込むN2温度のガス密度との
関係を示すものである。The gas expands in volume depending on the temperature and decreases in density. Table 1 shows the furnace gases (CO, N 2 , CO 2 , H 2
It shows the relationship between the temperature and density of a mixed gas containing O, H 2 , CH 4 and the like as main components) and the gas density at the N 2 temperature blown into the intermediate hopper.
【0017】[0017]
【表1】 表1から、例えば、炉内ガス温度が80℃の場合、N2
温度を146℃にすれば、同じガス密度になることが分
かる。従って、中間ホッパ内の炉内ガス温度に対応して
パージガスを加熱することにより、密度を近似させるこ
とができる。[Table 1] From Table 1, for example, when the furnace gas temperature is 80 ° C., N 2
It can be seen that the same gas density is obtained when the temperature is set to 146 ° C. Therefore, the density can be approximated by heating the purge gas in accordance with the gas temperature in the furnace in the intermediate hopper.
【0018】したがって、供給する不活性ガスを昇温す
ることにより、不活性ガスの体積を膨張させ、不活性ガ
ス供給装置から供給ガス量を減らすことができ、また、
密度差による循環流の形成を抑制することができる。な
お、その際、不活性ガスの密度が炉内ガスの密度以下に
なっても前述したようにパージ効果は期待できる。Therefore, by raising the temperature of the inert gas to be supplied, the volume of the inert gas can be expanded, and the amount of gas supplied from the inert gas supply device can be reduced.
The formation of a circulating flow due to the density difference can be suppressed. At this time, even if the density of the inert gas becomes lower than the density of the gas in the furnace, the purging effect can be expected as described above.
【0019】[0019]
【発明の効果】本発明は、不活性ガスを昇温することに
よって不活性ガス供給装置から供給する不活性ガス量を
大きく低減することができ、供給する量が減ることによ
り供給するガス装置の小型化による設備費低減とランニ
ングコストの低減を図ることができる。また、中間ホッ
パ内の炉内ガス温度に対応してパージガスを加熱するこ
とにより、密度を近似させ、中間ホッパ上部からパージ
することにより密度差による循環流の形成を抑制して、
効率良く中間ホッパ内のガスを追い出すことができる。According to the present invention, the amount of inert gas supplied from the inert gas supply device can be greatly reduced by raising the temperature of the inert gas. It is possible to reduce equipment costs and running costs by downsizing. In addition, by heating the purge gas in accordance with the gas temperature in the furnace in the intermediate hopper, the density is approximated, and purging from the upper part of the intermediate hopper suppresses the formation of a circulating flow due to the density difference,
The gas in the intermediate hopper can be efficiently expelled.
【図1】本発明を実施するための廃棄物溶融設備の全体
図である。FIG. 1 is an overall view of a waste melting facility for carrying out the present invention.
【図2】従来の廃棄物処理炉の装入装置を示す図であ
る。FIG. 2 is a diagram showing a conventional charging apparatus for a waste treatment furnace.
1:投入ホッパ 2:中間ホッパ 3:溶融炉 4:燃焼室 5:ボイラ 6:集じん装置 7:煙突 8:窒素発生装置 9:熱交換器 10:上部シールダンパ 11:下部シールダンパ 12:掻き出しダンパ 13:パージ吹込口 1: Input hopper 2: Intermediate hopper 3: Melting furnace 4: Combustion chamber 5: Boiler 6: Dust collector 7: Chimney 8: Nitrogen generator 9: Heat exchanger 10: Upper seal damper 11: Lower seal damper 12: Scavenging Damper 13: Purge inlet
─────────────────────────────────────────────────────
────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成13年6月18日(2001.6.1
8)[Submission date] June 18, 2001 (2001.6.1)
8)
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】特許請求の範囲[Correction target item name] Claims
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【特許請求の範囲】[Claims]
【手続補正2】[Procedure amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0006[Correction target item name] 0006
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0006】また、図2(b)装入装置では、廃棄物溶
融炉3の炉頂部に中間ホッパ2が設けられ、中間ホッパ
2の上端開口部に上端開口部を開閉する上部シールダン
パ10が設けられ、廃棄物処理炉内に通じる下端開口部
には、下端開口部を開閉する下部シールダンパ11が設
けられ、中間ホッパ内には、中間ホッパ内に装入された
廃棄物を溶融炉内に装入する掻き出しダンパ12が回動
自在に設けられている。In the charging device shown in FIG. 2 (b), an intermediate hopper 2 is provided at the top of the waste melting furnace 3, and an upper seal damper 10 is provided at the upper end opening of the intermediate hopper 2 to open and close the upper end opening. A lower seal damper 11 that opens and closes a lower end opening is provided at a lower end opening communicating with the waste treatment furnace, and a waste loaded in the intermediate hopper is disposed in the melting furnace in the intermediate hopper. the take can out damper 12 you charged is rotatably provided on.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F27D 17/00 101 F27D 17/00 101Z (72)発明者 戸高 光正 北九州市戸畑区大字中原46−59 日鐵プラ ント設計株式会社内 (72)発明者 山田 政史 北九州市戸畑区大字中原46−59 日鐵プラ ント設計株式会社内 Fターム(参考) 3K065 AA16 AB03 AC01 BA06 EA04 EA06 EA25 EA48 JA05 JA18 4K055 AA00 BA03 MA00 4K056 AA05 BA01 CA20 DA31 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme court ゛ (Reference) F27D 17/00 101 F27D 17/00 101Z (72) Inventor Mitsumasa Todaka 46-59, Nakahara, Tobata-ku, Kitakyushu-shi (72) Inventor Masafumi Yamada 46-59 Ohara Nakahara, Tobata-ku, Kitakyushu Nippon Steel Plant Design Co., Ltd.F-term (reference) MA00 4K056 AA05 BA01 CA20 DA31
Claims (3)
けられ、中間ホッパの上端開口部に上端開口部を開閉す
る上部シールダンパが設けられ、廃棄物処理炉内に通じ
る下端開口部には、下端開口部を開閉する下部シールダ
ンパが設けられ、中間ホッパ内の炉内ガスを不活性ガス
でパージする方法において、不活性ガスを昇温させて不
活性ガスの密度を少なくとも中間ホッパ内の炉内ガスの
密度に近似させて中間ホッパの上部からパージすること
を特徴とする、廃棄物溶融炉の挿入装置における中間ホ
ッパのパージ方法。An intermediate hopper is provided at the furnace top of the waste treatment furnace, and an upper seal damper for opening and closing the upper end opening is provided at an upper end opening of the intermediate hopper. Is provided with a lower seal damper for opening and closing the lower end opening, and in a method of purging the furnace gas in the intermediate hopper with the inert gas, the inert gas is heated to reduce the density of the inert gas at least in the intermediate hopper. Purging from the upper part of the intermediate hopper by approximating the density of the gas in the furnace.
から不活性ガスをパージすることを特徴とする請求項1
記載の廃棄物溶融炉の挿入装置における中間ホッパのパ
ージ方法。2. An inert gas is purged from a scraping damper disposed in an intermediate hopper.
A method for purging an intermediate hopper in an insertion device of a waste melting furnace as described in the above.
発生させた加圧蒸気を利用する熱交換器で不活性ガスを
昇温させることを特徴とする請求項1又は2記載の廃棄
物溶融炉の挿入装置における中間ホッパのパージ方法。3. The waste according to claim 1, wherein the temperature of the inert gas is raised by a heat exchanger using pressurized steam generated in a boiler of an exhaust gas treatment system of the waste treatment furnace. A method for purging an intermediate hopper in an insertion device of a melting furnace.
Priority Applications (1)
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JP2001147551A JP2002340313A (en) | 2001-05-17 | 2001-05-17 | Purging method for intermediate hopper in inserting apparatus of waste melting furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001147551A JP2002340313A (en) | 2001-05-17 | 2001-05-17 | Purging method for intermediate hopper in inserting apparatus of waste melting furnace |
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Publication Number | Publication Date |
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JP2002340313A true JP2002340313A (en) | 2002-11-27 |
Family
ID=18993021
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103866134A (en) * | 2013-09-12 | 2014-06-18 | 湖南水口山有色金属集团有限公司 | Fuming furnace and coal supply pipeline thereof |
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2001
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103866134A (en) * | 2013-09-12 | 2014-06-18 | 湖南水口山有色金属集团有限公司 | Fuming furnace and coal supply pipeline thereof |
CN103866134B (en) * | 2013-09-12 | 2016-08-17 | 湖南水口山有色金属集团有限公司 | Fuming furnace and coal supply pipeline thereof |
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