JP3119003B2 - Dust supply system for fluidized bed waste incinerator - Google Patents

Dust supply system for fluidized bed waste incinerator

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Publication number
JP3119003B2
JP3119003B2 JP04340622A JP34062292A JP3119003B2 JP 3119003 B2 JP3119003 B2 JP 3119003B2 JP 04340622 A JP04340622 A JP 04340622A JP 34062292 A JP34062292 A JP 34062292A JP 3119003 B2 JP3119003 B2 JP 3119003B2
Authority
JP
Japan
Prior art keywords
waste
hopper
incinerator
supply
screw
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 - Fee Related
Application number
JP04340622A
Other languages
Japanese (ja)
Other versions
JPH06193844A (en
Inventor
幹夫 茂木
真 三樹
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP04340622A priority Critical patent/JP3119003B2/en
Publication of JPH06193844A publication Critical patent/JPH06193844A/en
Application granted granted Critical
Publication of JP3119003B2 publication Critical patent/JP3119003B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、流動床式廃棄物焼却炉
の給塵装置に係り、特にシール性を保ちながら連続的か
つ定量的に廃棄物を焼却炉に供給することが可能な流動
床式廃棄物焼却炉の給塵装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust supply system for a fluidized bed waste incinerator, and more particularly to a fluid supply system capable of continuously and quantitatively supplying waste to an incinerator while maintaining sealing performance. The present invention relates to a dust supply device for a floor type waste incinerator.

【0002】[0002]

【従来の技術】一般に、流動床式廃棄物焼却炉の給塵装
置は、給塵ダクトを介して該焼却炉に廃棄物を供給して
いる。この給塵装置は、焼却炉内の排ガスが給塵ダクト
を通じて逆流したり、余剰空気が流入するのを防ぐため
に、内部をシールする必要がある。また、上記焼却炉に
は定量的かつ連続的に廃棄物を供給してやる必要があ
る。従って、上記給塵装置は、ホッパ内に廃棄物を溜め
て、スクリューコンベヤにて廃棄物をダクトへ送り出し
ながらマテリアルシールする構造が一般に用いられてい
る。
2. Description of the Related Art Generally, a dust supply device of a fluidized bed type waste incinerator supplies waste to the incinerator through a dust supply duct. It is necessary to seal the inside of this dust supply device in order to prevent the exhaust gas in the incinerator from flowing backward through the dust supply duct and to prevent excess air from flowing in. Further, it is necessary to supply the above incinerator with waste quantitatively and continuously. Therefore, the dust supply apparatus generally has a structure in which waste is accumulated in a hopper, and a material is sealed while sending the waste to a duct by a screw conveyor.

【0003】以下に従来の流動床式廃棄物焼却炉の給塵
装置について添付図面に基づき詳述する。
[0003] Hereinafter, a dust supply device for a conventional fluidized bed waste incinerator will be described in detail with reference to the accompanying drawings.

【0004】図3は、流動床式廃棄物焼却炉の給塵装置
1の構造を示すものである。図3に示すように、給塵装
置1は、該焼却炉に供給する廃棄物14を収容するホッ
パ3と、そのホッパ3の下部から上記焼却炉の給塵ダク
ト2の取入口4に延びると共にその取入口4に接続され
るトラフ5と、トラフ5内に収容されホッパ3内の廃棄
物14を上記取入口4に搬送するスクリュー6からなっ
ている。このトラフ5内には、スクリュー6がその先端
部を給塵ダクト2の取入口4に臨ませて収容されてい
る。またトラフ5の上流側である後端は外壁7が接合さ
れて塞がれている。この外壁7の中央部には壁を貫通し
て軸受け9が設けられており、スクリュー6の回転軸8
はこの軸受け9に支持されている。また、トラフ5の外
部には駆動部(図示せず)が設けられており、この回転
軸8が回転されることによりスクリュー6の周囲のもの
を飲み込んでスクリューの先端まで搬送するスクリュー
コンベヤを形成している。
FIG. 3 shows the structure of a dust supply device 1 for a fluidized bed waste incinerator. As shown in FIG. 3, the dust supply device 1 includes a hopper 3 containing waste 14 to be supplied to the incinerator, and extends from a lower portion of the hopper 3 to an intake 4 of a dust supply duct 2 of the incinerator. A trough 5 is connected to the inlet 4, and a screw 6 is accommodated in the trough 5 and transports the waste 14 in the hopper 3 to the inlet 4. A screw 6 is accommodated in the trough 5 with its tip facing the intake 4 of the dust supply duct 2. The rear end on the upstream side of the trough 5 is closed by joining the outer wall 7. A bearing 9 is provided in the center of the outer wall 7 so as to penetrate the wall, and a rotating shaft 8 of the screw 6 is provided.
Are supported by the bearing 9. A drive unit (not shown) is provided outside the trough 5, and the rotation shaft 8 is rotated to form a screw conveyor that swallows the surroundings of the screw 6 and conveys it to the tip of the screw. doing.

【0005】また、トラフ5の両天縁10、11には、
先端側から順に先端側天井12及びホッパ3及び根元側
天井13が接合され、両天縁10、11間はホッパ部で
吹き抜けになりそれ以外で気密な天井を有している。
[0005] In addition, the two ridges 10, 11 of the trough 5 have
The top side ceiling 12, the hopper 3 and the base side ceiling 13 are joined in order from the top side, and the space between the two top edges 10, 11 is blow-by at the hopper portion, and otherwise has an airtight ceiling.

【0006】このように構成された従来の流動床式廃棄
物焼却炉の給塵装置は、以下の様にしてマテリアルシー
ル性を有することができる。まず廃棄物14がホッパ3
上部のシュートに投下され、ホッパ3及びトラフ5内に
蓄積される。こうしてホッパ3内に蓄積された廃棄物1
4の上面レベル15が所定の高さに維持されると、ホッ
パ3下部からスクリュー6により取り込まれて先端側天
井12の下へ搬送されて程良く圧縮された廃棄物14の
抵抗により、ガスは通行不能になり、マテリアルシール
性が維持される。
[0006] The conventional dust feeder for a fluidized bed waste incinerator thus configured can have a material sealing property as follows. First, waste 14 is hopper 3
It is dropped on the upper chute and accumulated in the hopper 3 and the trough 5. The waste 1 thus accumulated in the hopper 3
When the upper surface level 15 of the hopper 4 is maintained at a predetermined height, the gas is taken in by the screw 6 from the lower part of the hopper 3, conveyed to the lower part of the front end side ceiling 12, and is compressed by a moderately compressed waste 14. It becomes impassable and the material sealability is maintained.

【0007】[0007]

【発明が解決しようとする課題】しかしながら、上述の
ような従来の流動床式廃棄物焼却炉の給塵装置1では、
ホッパ3内に堆積した廃棄物14の上面レベル15を高
くすると、スクリューにかかる廃棄物荷重が増加して、
より圧縮されて飲み込まれマテリアルシール性はよくな
るが、スクリュー6により搬送される廃棄物14が、先
端側天井12とホッパ3の接合部である喉部を通過する
ときに上方からの荷重がなくなり再膨張するため、喉部
及び先端側天井12に押し付けられて大きな摩擦抵抗を
受け、このとき廃棄物14は圧縮と圧縮限界条件での解
放による膨張を繰り返すようになり、喉部から取入口4
までの廃棄物14は粗密状態で移動され、定量供給性が
保てなくなるという問題があった。従って定量供給性を
保つには上面レベル15を下げて膨張による影響を減ら
すことが必要だが、あまり下げ過ぎると先端側天井12
の下へ搬送されて圧縮された廃棄物14は上部で粗とな
り、マテリアルシール性が保てなくなるという問題があ
った。このため、上面レベル15の調整が難しく、定量
供給性とマテリアルシール性の双方を良好に維持するこ
とは難しかった。従って、従来の流動床式廃棄物焼却炉
の給塵装置1はマテリアルシール性及び廃棄物の定量供
給性が不安定であり、それらを向上させることが課題で
あった。
However, in the above-described conventional dust feeder 1 for a fluidized bed waste incinerator,
When the upper surface level 15 of the waste 14 accumulated in the hopper 3 is increased, the waste load on the screw increases,
Although the material is more compressed and swallowed, the material sealing property is improved, but when the waste 14 conveyed by the screw 6 passes through the throat, which is the junction between the tip-side ceiling 12 and the hopper 3, there is no load from above and the waste 14 Because of expansion, it is pressed against the throat and the top side ceiling 12 and receives a large frictional resistance. At this time, the waste 14 repeats compression and expansion due to release under the compression limit condition.
There is a problem that the waste 14 is moved in a coarse and dense state, and the quantitative supply cannot be maintained. Therefore, it is necessary to lower the upper surface level 15 to reduce the influence of the expansion in order to maintain the quantitative supply property.
There is a problem that the waste 14 conveyed below and compressed becomes coarse in the upper part, and the material sealing property cannot be maintained. Therefore, it is difficult to adjust the upper surface level 15, and it has been difficult to maintain both the quantitative supply property and the material sealing property. Therefore, the conventional dust feeder 1 for a fluidized-bed waste incinerator has an unstable material sealing property and a quantitative supply property of waste, and it has been a problem to improve them.

【0008】そこで、本発明の目的は、上記課題を解決
し、マテリアルシール性を保ったまま廃棄物の定量供給
性を良好に保てる流動床式廃棄物焼却炉の給塵装置を提
供することにある。
Accordingly, an object of the present invention is to solve the above problems and to provide a dust supply apparatus for a fluidized bed waste incinerator which can maintain a good quantitative supply of waste while maintaining a material sealing property. is there.

【0009】[0009]

【課題を解決するための手段】上記目的を達成するため
に本発明は、流動床式廃棄物焼却炉に供給する廃棄物を
収容するホッパと、該ホッパの下部から上記焼却炉の給
塵ダクトの取入口に延びると共にその取入口に接続され
るトラフと、該トラフ内に収容され上記ホッパ内の廃棄
物を上記取入口に搬送するスクリューとを備えた流動床
式廃棄物焼却炉の給塵装置において、上記取入口に接続
される先端側トラフ天井の下部に定量供給部を形成し、
その先端側トラフ天井とホッパとを接続する喉部にスク
リュー根元側に斜め下方もしくは垂直に延びたシールプ
レートを設けて区画しスクリュー根元側上部に飲込み部
を形成し上記先端側トラフ天井を上記シールプレートの
下端より高くしたものである。
In order to achieve the above object, the present invention provides a hopper for storing waste to be supplied to a fluidized bed type waste incinerator, and a dust supply duct for the incinerator from a lower portion of the hopper. Dust supply of a fluidized bed waste incinerator, comprising: a trough extending to and connected to the intake of the fluid bed, and a screw accommodated in the trough and transporting waste in the hopper to the intake. In the apparatus, a fixed-quantity supply unit is formed at a lower portion of a top trough ceiling connected to the intake,
In the throat connecting the tip-side trough ceiling and the hopper, a seal plate that extends diagonally downward or vertically is provided at the screw root side to partition and form a swallowing part at the screw root side upper part, and the tip-side trough ceiling is This is higher than the lower end of the seal plate.

【0010】[0010]

【作用】上記構成によれば、廃棄物は、ホッパ内でシー
ルプレート下端よりも高いレベルまで蓄積された後飲込
み部を通してトラフ内に搬送され、シールプレート下端
を通過後、上方からの圧縮がなくなるため膨張するが、
先端側トラフ部の天井がシールプレート下端よりも十分
高く膨張空間が形成されているため、天井から摩擦抵抗
を受けることなくスムーズに搬送されることになり、廃
棄物の定量供給性が良くなる。また、ホッパ内でシ−ル
プレート下端よりも直ぐ上程度に廃棄物の上面レベルを
保ちさえすれば、廃棄物がシールプレート下端の下に圧
縮されて定量供給部に入るところでガスは通行不能にな
り、マテリアルシール性を確保できるので、マテリアル
シール性が安定する。従って、マテリアルシール性及び
廃棄物の定量供給性を同時に良く保つことができる。
According to the above construction, the waste is accumulated in the hopper to a higher level than the lower end of the seal plate, and then conveyed into the trough through the swallowing section. After passing through the lower end of the seal plate, the waste is compressed from above. Because it disappears, it expands,
Since the expansion space is formed at the ceiling of the trough on the distal end side sufficiently higher than the lower end of the seal plate, it is smoothly transported without receiving frictional resistance from the ceiling, and the quantitative supply of waste is improved. Also, as long as the upper surface level of the waste is maintained just above the lower end of the seal plate in the hopper, the gas is impassable when the waste is compressed under the lower end of the seal plate and enters the quantitative supply section. Therefore, the material sealing property can be ensured, so that the material sealing property is stabilized. Therefore, the material sealing property and the quantitative supply property of the waste can be simultaneously kept good.

【0011】[0011]

【実施例】以下、本発明の実施例を添付図面に基づいて
詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the accompanying drawings.

【0012】図1は、本発明による流動床式廃棄物焼却
炉の給塵装置16の一実施例を示す断面図である。該焼
却炉(図示せず)の給塵ダクト2の取入口4には、トラ
フ17の先端が気密に接続されている。このトラフ17
は略水平な台36に設けた支持材18にて水平に支持さ
れている。またトラフ17内には、トラフ後端側外部に
設けた駆動部により駆動されるスクリュー19が、根元
側の回転軸20を軸受け21にて支持され先端を取入口
4に臨ませて水平に設けられており、トラフ17はこの
スクリュー19を収めるのに充分な深さを有している。
トラフ17の天縁部22,23には、根元側ではホッパ
24が吹き抜け状に接続され、それより先端側は天井2
5が接合されている。この先端側の天井25はスクリュ
ー19上面より十分高く形成され、定量供給部Bを形成
している。先端側の天井25とホッパ24は喉部26を
形成して接続されている。その喉部26には、シールプ
レート27がスクリュー根元側に斜め下方若しくは垂直
に延びる向きで上端を気密に接続されて設けられ、スク
リュー根元側上部に飲込み部Aを形成している。詳しく
説明すると後述する廃棄物の飲込み量と供給量のバラン
ス及びマテリアルシールとの関係から斜め下方垂直まで
実際の施設毎に適切な角度に設定する。
FIG. 1 is a sectional view showing an embodiment of a dust supply device 16 of a fluidized bed waste incinerator according to the present invention. The tip of a trough 17 is airtightly connected to the intake 4 of the dust supply duct 2 of the incinerator (not shown). This trough 17
Are horizontally supported by a support member 18 provided on a substantially horizontal base 36. In the trough 17, a screw 19 driven by a drive unit provided outside the rear end of the trough is provided horizontally with the rotation shaft 20 on the base side supported by the bearing 21 and the tip facing the inlet 4. The trough 17 has a sufficient depth to accommodate the screw 19.
A hopper 24 is connected to the top edges 22 and 23 of the trough 17 at the base side in a blow-by manner, and the tip end side of the hopper 24 is connected to the ceiling 2.
5 are joined. The ceiling 25 on the distal end side is formed sufficiently higher than the upper surface of the screw 19 to form a fixed supply section B. The ceiling 25 on the tip side and the hopper 24 are connected by forming a throat 26. In the throat portion 26, a seal plate 27 is provided with the upper end airtightly connected to the screw root side in a direction extending obliquely downward or vertically, and a swallowing portion A is formed at the upper portion of the screw root side. More specifically, an appropriate angle is set for each actual facility from the relationship between the amount of waste and the amount of supply of waste, which will be described later, and from the relationship with the material seal to the diagonally downward and vertical directions.

【0013】スクリュー19の形状は、飲込み部に先細
のテーパー状シャフト部28を有し、定量供給部にテー
パー状シャフト部28の先端の径と略同一の径の定径シ
ャフト部29を有し、スクリュー羽根30のスクリュー
ピッチは飲込み部では荒く定量供給部では細かくなって
いる。しかし上述の如く定量供給部の定径シャフト部2
9の直径を飲込み部のテーパー状シャフト部28の最小
直径に形成して飲込み部より定量供給部が搬送容量が大
となることが可能である。
The shape of the screw 19 has a tapered tapered shaft portion 28 at the swallowing portion, and a constant diameter shaft portion 29 having a diameter substantially the same as the diameter of the tip of the tapered shaft portion 28 at the fixed amount supply portion. However, the screw pitch of the screw blade 30 is rough in the swallowing section and fine in the quantitative supply section. However, as described above, the fixed diameter shaft section 2 of the fixed amount supply section
The diameter of 9 can be formed to be the minimum diameter of the tapered shaft portion 28 of the swallowing section, so that the fixed-volume supply section can have a larger transfer capacity than the swallowing section.

【0014】また、シールプレート27の直上のホッパ
24内に、そのシールプレート27上に常時廃棄物14
が溜まっていることを検出する固定式レベルセンサー3
1が設けられ、また、スクリュー19の根元部側上方の
ホッパ24内に、廃棄物14のレベルを一定に制御する
可動式レベルセンサー32が縦長の取り付け枠内でスラ
イド式に上下位置調整可能に設けられている。また、ホ
ッパ24の上部には、可動式の廃棄物落下調整用プレー
ト33を有するシュート34が設けてある。またこのシ
ュート34の入口には、廃棄物を搬入してシュート34
内に落下する搬入コンベヤ35が設けられている。
In the hopper 24 immediately above the seal plate 27, the waste 14
Fixed level sensor 3 that detects that there is accumulation
A movable level sensor 32 for controlling the level of the waste 14 at a constant level is provided in a hopper 24 above the root side of the screw 19 so that the vertical position can be adjusted in a sliding manner within a vertically long mounting frame. Is provided. A chute 34 having a movable waste drop adjusting plate 33 is provided on the upper part of the hopper 24. At the entrance of the chute 34, waste is carried in and the chute 34 is introduced.
A carry-in conveyor 35 that falls into the inside is provided.

【0015】次に、本実施例の作用について述べる。Next, the operation of this embodiment will be described.

【0016】本実施例の流動床式廃棄物焼却炉の給塵装
置16によれば、廃棄物14は、搬入コンベヤ35によ
り搬入されシュート34内に落下し、可動式の廃棄物落
下調整用プレート33に落下場所をほぼ一定に調整さ
れ、落下してホッパ24内でシールプレート27下端よ
りも高いレベルまで蓄積されて荷重により圧縮されて飲
込み部を通してトラフ17内を搬送され、定量供給部に
送られる。廃棄物14はシールプレート27下端を通過
後、上方からの荷重がなくなるため膨張するが、先端側
の天井25がシールプレート27下端よりも十分高いの
で、天井25から摩擦抵抗を受けることなくスムーズに
搬送されることになる。従って廃棄物14の定量供給性
が良くなる。また、シ−ルプレート27下端よりも直ぐ
上程度に廃棄物の上面レベル15を保ちさえすれば、廃
棄物14が定量供給部に入る前にシールプレート27下
端の下に圧縮されて高密度になるところでガスは通行不
能になりマテリアルシール性を確保できる。従ってマテ
リアルシール性を保ったまま廃棄物の定量供給性を良好
に保つことができる。
According to the dust feeder 16 of the fluidized bed waste incinerator of the present embodiment, the waste 14 is carried in by the carry-in conveyor 35 and falls into the chute 34, and the movable waste fall adjustment plate 33, the drop location is adjusted to be substantially constant, the drop is dropped, accumulated to a level higher than the lower end of the seal plate 27 in the hopper 24, compressed by the load, conveyed through the swallowing section through the trough 17, and sent to the fixed quantity supply section. Sent. The waste 14 expands after passing through the lower end of the seal plate 27 because there is no load from above. However, since the ceiling 25 on the tip side is sufficiently higher than the lower end of the seal plate 27, the waste 14 smoothly receives no frictional resistance from the ceiling 25. It will be transported. Therefore, the quantitative supply of the waste 14 is improved. Further, if the upper surface level 15 of the waste is maintained just above the lower end of the seal plate 27, the waste 14 is compressed under the lower end of the seal plate 27 before entering the fixed amount supply portion, and the density is increased. At that point, the gas cannot pass, and the material sealing property can be secured. Therefore, it is possible to maintain good quantitative supply of waste while maintaining the material sealing property.

【0017】また搬入コンベヤ35により搬入されシュ
ート34内に落下する廃棄物14の落下状態を可動式の
廃棄物落下調整用プレート33で一定に調整することに
より、飲込み部の廃棄物上面レベルをスクリュー19の
テーパー上面に平行に若しくはややスクリュー19の根
元側に偏重させるように調整し廃棄物14の密度の一定
化をはかり、スクリュー19による飲み込み量が安定す
るようにできるので定量供給性がよくなる。
Further, the falling state of the waste 14 which is carried in by the carry-in conveyor 35 and falls into the chute 34 is adjusted to be constant by the movable waste fall adjusting plate 33, so that the upper surface level of the waste in the swallowing section is adjusted. The density of the waste 14 is adjusted by adjusting the weight to be parallel to the tapered upper surface of the screw 19 or slightly toward the root of the screw 19, and the amount of the swallowed by the screw 19 can be stabilized, so that the quantitative supply is improved. .

【0018】また、スクリュー19は、飲込み部に先細
のテーパー状シャフト部28を有しているので、根元側
だけでなく飲込み部全面から廃棄物14を飲込むことが
でき、また、定量供給部にテーパー状シャフト部28先
端の径と略同一の径の定径シャフト部29を有し、スク
リュー羽根30が、その飲込み部よりも定量供給部で小
さくなるピッチを有して且つ飲込み部より定量供給部で
搬送容量が大であるように形成してあるので、飲込み部
は大きなピッチにより廃棄物を飲み込みやすくなり、し
かもその飲込み量が定量供給部で再膨張しても搬送能力
以内に収まるため廃棄物の定量供給性が安定する。ま
た、定量供給部ではピッチが小さいことにより廃棄物の
連続供給性が向上する。
Further, since the screw 19 has the tapered tapered shaft portion 28 at the swallowing portion, the waste 14 can be swallowed not only from the root side but also from the entire swallowing portion. The supply section has a constant diameter shaft section 29 having substantially the same diameter as the diameter of the tip of the tapered shaft section 28, and the screw blade 30 has a pitch smaller than that of the swallowing section in the fixed supply section and has a smaller pitch. The swallowing unit is formed so that the transport capacity is larger than the swallowing unit, so that the swallowing unit can easily swallow the waste due to the large pitch. Because it is within the transport capacity, the quantitative supply of waste is stable. In the fixed-quantity supply unit, the small pitch improves continuous supply of waste.

【0019】また、シールプレート27の直上のホッパ
24に、そのシールプレート27の下端より上に常時廃
棄物14が溜まっていることを検出する固定式レベルセ
ンサー31が設けられているので、シール性確保を確認
する情報が得られる。また定量供給部内の廃棄物の上面
レベルがこのセンサー以下のレベルに下がったら廃棄物
切れの事前警報アラームを出したり無条件で廃棄物供給
を行わせたりする信号を出すようにもできる。またこの
固定式レベルセンサー31は以下に述べるように可動式
レベルセンサーを最適な位置に設定するために使用され
る。
The hopper 24 immediately above the seal plate 27 is provided with a fixed level sensor 31 for constantly detecting that the waste 14 is accumulated above the lower end of the seal plate 27, so that the sealing performance is improved. Information to confirm the security is obtained. Further, when the upper surface level of the waste in the fixed amount supply unit falls to a level below this sensor, it is possible to output a signal for giving a pre-warning alarm of waste exhaustion or for performing waste supply unconditionally. The fixed level sensor 31 is used for setting the movable level sensor at an optimum position as described below.

【0020】また、スクリュー19の根元部側上部のホ
ッパ24に廃棄物のレベルを一定に制御する可動式レベ
ルセンサー32が設けられているので、搬入コンベヤ3
5をインバータ制御もしくはタイマー制御することによ
り、従来は運転中変動していた飲込み部の廃棄物の上面
レベル15を運転中一定のレベルに保つことができ、飲
込み廃棄物の密度が一定化し、従って飲込み量が一定す
るので廃棄物の定量供給性が向上する。また可動式レベ
ルセンサー32を取り付け枠内でスライド式に任意に上
下位置調整をして、上述したように一定に保たれる上面
レベル15が最適レベルになるように容易に設定調整で
きるので、廃棄物の定量供給性を最適化でき、また運転
性も良くなる。これについて図2を用い、給塵装置16
の運転の実際に即して以下に詳しく説明する。
Since a movable level sensor 32 for controlling the level of waste is provided in the hopper 24 on the upper side of the screw 19 at the root side, the carry-in conveyor 3 is provided.
5 by inverter control or timer control, the upper level 15 of the waste in the swallowing unit, which has conventionally fluctuated during operation, can be maintained at a constant level during operation, and the density of the swallowed waste is reduced. Therefore, since the amount of swallow is constant, the quantitative supply of waste is improved. In addition, the movable level sensor 32 can be slidably adjusted up and down in the mounting frame to easily set and adjust the upper surface level 15 kept constant as described above to an optimum level. Quantitative supply of materials can be optimized and operability can be improved. In this regard, referring to FIG.
The operation will be described in detail below.

【0021】上述した様に、従来の構成の給塵装置にお
いては、ホッパ内の廃棄物上面レベルがあるレベルまで
高くなると喉部を通過して膨張した廃棄物が先端側天井
(この天井レベルを図2中にPで示した)から受ける摩
擦抵抗のため定量供給性が満たされなくなり始めてい
た。本発明による給塵装置16においても、飲込み部の
廃棄物の上面レベルを上げていくと定量供給部の廃棄物
の上面レベルは上がっていく。しかし本発明による給塵
装置16によれば、この定量供給部側の廃棄物の上面レ
ベルがPに達し始めるような飲込み部の廃棄物の上面レ
ベルAiで運転しても、先端側トラフ天井25はPより
十分高いので、定量供給部側で膨張した廃棄物の上面レ
ベルAoより十分高く、従って廃棄物に摩擦抵抗を与え
ることがないため、その点で定量供給性を悪化させるこ
とがなく、従来の給塵装置に比べ定量供給性が向上して
いる。
As described above, in the conventional dust supply apparatus, when the level of the upper surface of the waste in the hopper rises to a certain level, the waste expanded through the throat portion is moved to the ceiling on the front end side (the ceiling level is reduced). (Indicated by P in FIG. 2), the quantitative feedability began to be unsatisfactory due to the frictional resistance received. Also in the dust supply device 16 according to the present invention, when the upper surface level of the waste in the drinking section is increased, the upper surface level of the waste in the fixed amount supply section is also increased. However, according to the dust supply device 16 according to the present invention, even if the dust supply device 16 is operated at the upper surface level Ai of the waste in the swallowing unit such that the upper surface level of the waste in the fixed amount supply unit starts to reach P, the trough ceiling on the distal end side is used. Since 25 is sufficiently higher than P, it is sufficiently higher than the upper surface level Ao of the waste expanded on the quantitative supply section side, and therefore does not give frictional resistance to the waste, so that the quantitative supply is not deteriorated at that point. In addition, the quantitative feedability is improved as compared with the conventional dust supply device.

【0022】ところで、この給塵装置16を本格的に運
転する際、飲込み部の廃棄物の上面レベルを一定レベル
に制御して運転するほうが廃棄物の密度が一定化し飲込
み量が一定となるので定量供給性のために望ましいが、
その一定レベルを上述のレベルAiにして運転すること
が最適であるとは限らない。なぜなら飲込み部の廃棄物
の上面レベルを上述のレベルAiにして運転した場合、
定量供給部で膨張した廃棄物がスクリュー19の搬送能
力以上に膨張するため飲込み量と定量供給部の能力のバ
ランスがくずれ定量供給性が悪化するケースがあるから
である。従って、給塵装置16は、本格的に運転される
際は、実際の施設ごとのばらつきや廃棄物の特性を鑑
み、給塵装置16の飲込み部側の廃棄物の上面レベルを
以下に述べるようなBiレベル以下で一定に制御して運
転される。即ち、Biレベル以上となるとスクリュー先
端部で廃棄物がスクリュー羽根30の上端を越えるよう
な状態となり、飲込み量が多過ぎてバランスが取れなく
なるからである。
By the way, when the dust supply device 16 is operated in full scale, it is better to control the upper surface level of the waste in the swallowing section to a constant level so that the density of the waste is constant and the swallowing amount is constant. Is desirable for quantitative supply,
It is not always optimal to drive the vehicle at the fixed level Ai described above. Because, when the upper level of the waste in the swallowing section is driven to the level Ai described above,
This is because the waste swollen in the fixed-amount supply unit expands beyond the carrying capacity of the screw 19, so that the balance between the swallowing amount and the capacity of the fixed-amount supply unit may be lost, and the fixed-amount supply property may be deteriorated. Therefore, when the dust supply device 16 is operated in full scale, the top level of the waste at the swallowing unit side of the dust supply device 16 will be described below in consideration of actual facility-specific variations and waste characteristics. The operation is performed with a constant control at a Bi level or lower. That is, when the level is equal to or higher than the Bi level, the waste comes to exceed the upper end of the screw blade 30 at the tip of the screw, so that the swallowing amount is too large and the balance cannot be obtained.

【0023】まず、図2にも示したように、飲込み部の
廃棄物の上面レベルが固定式センサー31よりも低いレ
ベルDにある状態では、飲込み荷重が小さく定量供給性
が確保できなくなりまたシール性が低下する危険が大き
いので、運転に適さない。従って飲込み部の廃棄物の上
面レベルは最低でも固定式レベルセンサー31の高さを
有してなければならない。この固定式レベルセンサー3
1を通りしかも飲込み量とバランスが保たれ定量供給性
が実用上確保できるレベルを、可動式レベルセンサーを
用いて試運転することにより実測し、実用上の上限をB
iと決めることができる。さらに、変動を考慮して可動
式レベルセンサー32をスライド式に高さ調整してBi
より僅かに下のCiの高さに設定してやれば、常に飲込
み量と供給量のバランスが保たれ、定量供給性が確保で
きる。その高さCiに可動式レベルセンサー32を保
ち、このセンサー32からの信号でインバーター方式も
しくはタイマー方式(NOT Hレベルn秒で運転、H
レベルで停止)で搬入コンベヤ35を制御することによ
り、飲込み部の廃棄物の上面レベルを最適レベルCiに
一定に制御することができる。
First, as shown in FIG. 2, when the upper surface level of the waste in the swallowing section is at a level D lower than that of the fixed sensor 31, the swallowing load is so small that the quantitative supply cannot be ensured. Further, since there is a great risk that the sealing property is reduced, it is not suitable for driving. Therefore, the upper surface level of the waste in the swallowing section must have at least the height of the fixed level sensor 31. This fixed level sensor 3
1 and the level that can be practically secured with the balance with the swallowing amount and the quantitative supply is actually measured by trial running using a movable level sensor.
i can be determined. Further, the height of the movable level sensor 32 is adjusted in a sliding manner in consideration of the fluctuation, and Bi
If the height is set slightly lower than the height of Ci, the balance between the swallowing amount and the supply amount is always maintained, and the quantitative supply property can be secured. The movable level sensor 32 is maintained at the height Ci, and an inverter type or a timer type (NOT H level n seconds operation, H
By controlling the carry-in conveyor 35 at the level (stop at the level), it is possible to control the upper surface level of the waste in the swallowing unit to be the optimum level Ci.

【0024】なお、ホッパ24内のスクリュー19は、
一連だけではなく並列に二連以上の多連式に配設しても
よい。
The screw 19 in the hopper 24 is
It may be arranged not only in a series but also in multiples of two or more in parallel.

【0025】[0025]

【発明の効果】以上要するに本発明によれば、流動床式
廃棄物焼却炉に対して、シール性を保ったまま、廃棄物
を連続的且つ定量的に供給することが可能になる。
In summary, according to the present invention, it is possible to continuously and quantitatively supply waste to a fluidized bed waste incinerator while maintaining the sealing property.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施例を示す断面図である。FIG. 1 is a sectional view showing an embodiment of the present invention.

【図2】図1の実施例における廃棄物のレベルを示す説
明図である。
FIG. 2 is an explanatory diagram showing a waste level in the embodiment of FIG. 1;

【図3】従来の流動床式廃棄物焼却炉の給塵装置を示す
図である。
FIG. 3 is a diagram showing a dust supply device of a conventional fluidized bed waste incinerator.

【符号の説明】[Explanation of symbols]

2 給塵ダクト 4 取入口 14 廃棄物 16 給塵装置 17 トラフ 19 スクリュー 24 ホッパ 25 先端側トラフ天井 26 喉部 27 シールプレート 28 テーパー状シャフト 29 定径シャフト 30 スクリュー羽根 31 固定式レベルセンサー 32 可動式レベルセンサー 33 廃棄物落下調整用プレート 34 シュート A 飲込み部 B 定量供給部 2 Dust Supply Duct 4 Inlet 14 Waste 16 Dust Supply Device 17 Trough 19 Screw 24 Hopper 25 Tip Trough Ceiling 26 Throat 27 Seal Plate 28 Tapered Shaft 29 Constant Diameter Shaft 30 Screw Blade 31 Fixed Level Sensor 32 Movable Level sensor 33 Waste drop adjustment plate 34 Chute A Drinking part B Quantitative supply part

フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23G 5/30 F23G 5/44 F23K 3/16 302 B65G 65/46 Continuation of the front page (58) Field surveyed (Int.Cl. 7 , DB name) F23G 5/30 F23G 5/44 F23K 3/16 302 B65G 65/46

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 流動床式廃棄物焼却炉に供給する廃棄物
を収容するホッパと、該ホッパの下部から上記焼却炉の
給塵ダクトの取入口に延びると共にその取入口に接続さ
れるトラフと、該トラフ内に収容され上記ホッパ内の廃
棄物を上記取入口に搬送するスクリューとを備えた流動
床式廃棄物焼却炉の給塵装置において、上記取入口に接
続される先端側トラフ天井の下部に定量供給部を形成
し、その先端側トラフ天井とホッパとを接続する喉部に
スクリュー根元側に斜め下方もしくは垂直に延びたシー
ルプレートを設けて区画し、スクリュー根元側上部に飲
込み部を形成し上記先端側トラフ天井を上記シールプレ
ートの下端より高くしたことを特徴とする流動床式廃棄
物焼却炉の給塵装置。
1. A hopper containing waste to be supplied to a fluidized-bed waste incinerator, and a trough extending from a lower portion of the hopper to an intake of a dust supply duct of the incinerator and connected to the intake. A screw that is accommodated in the trough and conveys the waste in the hopper to the inlet, and a dust feeder for a fluidized-bed waste incinerator, A fixed-quantity supply unit is formed in the lower part, and a seal plate extending diagonally downward or vertically is provided at the throat connecting the ceiling of the trough and the hopper on the tip side, and a swallowing unit is provided at the upper part of the screw base. A dust feeder for a fluidized bed type waste incinerator, wherein the top of the trough ceiling is higher than the lower end of the seal plate.
【請求項2】上記シールプレートの直上のホッパに、そ
のシールプレート上に常時廃棄物が溜まっていることを
検出する固定式レベルセンサーを有し、スクリューの根
元部側上部のホッパに、廃棄物のレベルを制御する上下
位置調整可能な可動式レベルセンサーを有することを特
徴とする請求項1記載の流動床式廃棄物焼却炉の給塵装
置。
2. A hopper immediately above the seal plate, having a fixed level sensor for detecting that waste is constantly accumulated on the seal plate, 2. The dust supply device for a fluidized bed waste incinerator according to claim 1, further comprising a movable level sensor capable of adjusting a vertical position of the incinerator.
【請求項3】上記スクリューが、飲込み部に先細のテー
パー状シャフト部を有し、定量供給部にテーパー状シャ
フト部先端の径と略同一の径の定径シャフト部を有し、
スクリュー羽根が、その飲込み部よりも定量供給部で小
さくなるピッチを有して飲込み部より定量供給部で搬送
容量が大であることを特徴とする請求項1記載の流動床
式廃棄物焼却炉の給塵装置。
3. The screw has a tapered tapered shaft portion at the swallowing portion, and a constant diameter shaft portion having a diameter substantially the same as the diameter of the tapered shaft portion tip at the fixed amount supply portion,
The fluidized bed waste according to claim 1, wherein the screw blade has a pitch that is smaller in the fixed supply section than in the swallowing section, and has a larger transport capacity in the fixed supply section than in the swallow section. Dust supply device for incinerator.
【請求項4】ホッパ上部のシュート内に可動式の廃棄物
落下調整用プレートを設けたことを特徴とする請求項1
記載の流動床式廃棄物焼却炉の給塵装置。
4. A movable waste drop adjusting plate is provided in a chute at an upper portion of the hopper.
A dust supply device for a fluidized bed waste incinerator according to the above.
JP04340622A 1992-12-21 1992-12-21 Dust supply system for fluidized bed waste incinerator Expired - Fee Related JP3119003B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04340622A JP3119003B2 (en) 1992-12-21 1992-12-21 Dust supply system for fluidized bed waste incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04340622A JP3119003B2 (en) 1992-12-21 1992-12-21 Dust supply system for fluidized bed waste incinerator

Publications (2)

Publication Number Publication Date
JPH06193844A JPH06193844A (en) 1994-07-15
JP3119003B2 true JP3119003B2 (en) 2000-12-18

Family

ID=18338740

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04340622A Expired - Fee Related JP3119003B2 (en) 1992-12-21 1992-12-21 Dust supply system for fluidized bed waste incinerator

Country Status (1)

Country Link
JP (1) JP3119003B2 (en)

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Publication number Priority date Publication date Assignee Title
US6268443B1 (en) 1994-09-06 2001-07-31 Chisso Corporation Process for producing a solid catalyst component for olefin polymerization and a process for producing an olefin polymer
US6300415B1 (en) 1995-11-24 2001-10-09 Chisso Corporation Propylene composition, process for preparing the same, polypropylene composition, and molded articles
US6319991B1 (en) 1997-05-22 2001-11-20 Chisso Corporation Propylene polymer blends, processes of producing the same and polypropylene resin compositions
US6323286B1 (en) 1998-08-18 2001-11-27 Chisso Corporation Polypropylene composition
JP2014516653A (en) * 2011-05-04 2014-07-17 ファースト ディフェンス ホールディングス エルエルシー Nasal filter structure
KR101426335B1 (en) * 2013-11-13 2014-08-07 지에스플라텍 주식회사 Apparatus for inserting material of gasification melting furnace and gasification melting furnace system with the same

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JP2008303013A (en) * 2007-06-06 2008-12-18 Babcock Hitachi Kk Screw type waste feeder
KR200482733Y1 (en) * 2016-02-01 2017-02-27 에너원 주식회사 Device for supplying solid refuge fuel constantly in a combustion apparatus

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6268443B1 (en) 1994-09-06 2001-07-31 Chisso Corporation Process for producing a solid catalyst component for olefin polymerization and a process for producing an olefin polymer
US6300415B1 (en) 1995-11-24 2001-10-09 Chisso Corporation Propylene composition, process for preparing the same, polypropylene composition, and molded articles
US6319991B1 (en) 1997-05-22 2001-11-20 Chisso Corporation Propylene polymer blends, processes of producing the same and polypropylene resin compositions
US6323286B1 (en) 1998-08-18 2001-11-27 Chisso Corporation Polypropylene composition
JP2014516653A (en) * 2011-05-04 2014-07-17 ファースト ディフェンス ホールディングス エルエルシー Nasal filter structure
KR101426335B1 (en) * 2013-11-13 2014-08-07 지에스플라텍 주식회사 Apparatus for inserting material of gasification melting furnace and gasification melting furnace system with the same

Also Published As

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