JP3402962B2 - Fluidized bed equipment - Google Patents

Fluidized bed equipment

Info

Publication number
JP3402962B2
JP3402962B2 JP28817896A JP28817896A JP3402962B2 JP 3402962 B2 JP3402962 B2 JP 3402962B2 JP 28817896 A JP28817896 A JP 28817896A JP 28817896 A JP28817896 A JP 28817896A JP 3402962 B2 JP3402962 B2 JP 3402962B2
Authority
JP
Japan
Prior art keywords
fluidized bed
ash
fluidized
cooling
gas
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
JP28817896A
Other languages
Japanese (ja)
Other versions
JPH10132213A (en
Inventor
武志 鈴木
智規 小山
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP28817896A priority Critical patent/JP3402962B2/en
Publication of JPH10132213A publication Critical patent/JPH10132213A/en
Application granted granted Critical
Publication of JP3402962B2 publication Critical patent/JP3402962B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Crucibles And Fluidized-Bed Furnaces (AREA)

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、流動床ボイラ、ガ
ス化炉などの流動床装置に関する。 【0002】 【従来の技術】図2は流動床ボイラ、ガス化炉など従来
の流動床装置の説明図である。図において、符号01は
流動床容器、03は流動床の目皿、04は流動床灰の抜
出し管、06は流動床灰の冷却用コイル、08は冷却さ
れた流動床灰の抜出し管である。流動媒体中の流動床灰
は抜出し管04内を通って流動床容器01外へ排出され
るが、この流動床灰は800℃程度と高温のために冷却
する必要があり、冷却用コイル06などを設置して冷却
を行っている。 【0003】 【発明が解決しようとする課題】上記のように、従来の
流動床装置においては流動床灰を冷却するために流動床
容器01の下流に冷却用コイル06などを設置してお
り、このために流動床の設備が複雑化するとともに、冷
却用コイル06の磨耗が生じるなどの不具合がある。 【0004】 【課題を解決するための手段】本発明に係る流動床装置
は上記課題の解決を目的にしており、流動床容器内の第
1の目皿上第1の流動床を有し同第1の流動床で生成
される流動床灰を抜出し管を介して下方へ排出する流動
床装置において、上記流動床容器内の上記抜出し管の下
流に設置され上記抜出し管を介して排出される流動床灰
を受ける第2の目皿と、上記流動床容器に設けられ同第
2の目皿の下方へガスを供給して同第2の目皿上の流動
床灰を冷却するガス投入管とを備え、同第2の目皿上に
流動床灰冷却用の第2の流動床を形成し、上記ガス投入
管から供給され上記第2の流動床を通過したガスを上記
第1の目皿を通して上記第1の流動床の流動に用いるよ
うに構成してなることを特徴とする。このように、本流
動床装置においては流動床容器内の第1の目皿上の第1
流動床の抜出し管の下流に第2の目皿を設置しガス投
入管により第2の目皿の下方からガスを供給することに
より流動床容器内の第1の流動床下方に流動床灰冷却用
第2の流動床が形成されており、流動床灰を冷却する
ための特別な冷却装置を必要とせず、また第2の流動床
での流動床灰冷却用のガスと第1の流動床における流動
媒体の流動用に用いるガスとを共用することにより大量
の冷却用ガスを必要とせず、また流動床灰の冷却と同時
第1の流動床における流動媒体を流動化するガスが予
熱される。 【0005】 【発明の実施の形態】図1は本発明の実施の一形態に係
る流動床装置の説明図である。図において、本実施の形
態に係る流動床装置は流動床ボイラ、ガス化炉など流動
床反応器内で生成される流動床灰の冷却を必要とする流
動床装置で、図における符号1は流動床容器、3は第1
流動床の第1の目皿、11は流動床灰冷却用の第2の
流動床の第2の目皿、4は流動床灰の抜出し管、9は流
動床灰冷却用のガス投入管である。流動媒体中の流動床
灰は抜出し管4内を通って下方へ排出されるが、この流
動床灰は800℃程度と高温のために冷却する必要があ
り、本流動床装置においては図に示すように第1の流動
床の第1の目皿3の下部に流動床灰冷却用の第2 目皿
11を設置するとともに、この第2の目皿11の下方か
ら流動床灰冷却用のガスを投入して流動床容器1内に流
動床灰冷却用の第2の流動床を形成している。 【0006】このように、本流動床装置においては流動
床容器1内に第1の流動床の第1の目皿3と流動床灰冷
却用の第2の流動床の第2の目皿11とが設置されてい
る。第1の流動床の第1の目皿3上の流動床灰は、抜出
し管4から下部の流動床灰冷却用の第2の流動床に入
る。流動床灰冷却用のガスは、ガス投入管9から流動床
容器1内下部へ投入されて流動床灰冷却用の第2の流動
床の第2の目皿11を通り、流動床灰冷却用の第2の
動床の流動床灰層を通過しながら流動床灰を冷却する。
このため、ガス投入管9から流動床容器1内へ投入され
たガスが暖まり、予熱された状態で第1の流動床の第1
目皿3を通って上方の流動媒体へ供給される。 【0007】従来の流動床装置においては流動床灰を冷
却するために流動床容器の下流に冷却用コイルなどを設
置しており、このために流動床の設備が複雑化するとと
もに、冷却用コイルの磨耗が生じるなどの不具合がある
が、本流動床装置においては流動床容器1内の第1の
動床の抜出し管の下流に流動床灰の冷却を行う別の第2
流動床を設置して流動床灰冷却用のガスに第1の流動
床の流動媒体の流動に用いるガスを利用しており、流動
床灰冷却のために特に別の冷却装置を必要とせず、また
流動床灰冷却用のガスは第1の流動床で流動媒体の流動
に用いるガスを利用することにより大量の流動床灰冷却
用のガスを必要とせず、また流動床灰を冷却すると同時
に流動用ガスを予熱することができるなど、装置ならび
に運転用のコストが低減される。 【0008】 【発明の効果】本発明に係る流動床装置は前記のように
構成されており、流動床灰を冷却するための特別な冷却
装置を必要とせず、また流動床灰冷却用のガスと第1の
流動床における流動媒体の流動用に用いるガスとを共用
することにより大量の冷却用ガスを必要とせず、また流
動床灰の冷却と同時に第1の流動床における流動媒体を
流動化するガスが予熱されるので、流動床装置および流
動床装置の運転に要するコストの削減が可能になる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fluidized bed apparatus such as a fluidized bed boiler and a gasification furnace. FIG. 2 is an explanatory view of a conventional fluidized-bed apparatus such as a fluidized-bed boiler and a gasifier. In the figure, reference numeral 01 denotes a fluidized bed container, 03 denotes a fluidized bed plate, 04 denotes a fluidized bed ash extraction tube, 06 denotes a fluidized bed ash cooling coil, and 08 denotes a cooled fluidized bed ash extraction tube. . The fluidized bed ash in the fluidized medium is discharged to the outside of the fluidized bed container 01 through the extraction pipe 04, but the fluidized bed ash needs to be cooled because of its high temperature of about 800 ° C. Is installed for cooling. [0003] As described above, in the conventional fluidized bed apparatus , a cooling coil 06 or the like is installed downstream of the fluidized bed vessel 01 for cooling fluidized bed ash. This complicates the equipment of the fluidized bed, and causes problems such as abrasion of the cooling coil 06. [0004] A fluidized-bed apparatus according to the present invention has an object to solve the above-mentioned problems, and has the following features .
Oite fluidized bed apparatus for discharging downwardly through the first having a fluidized bed the first fluidized bed ash extraction tube produced in a fluidized bed on the first perforated plate, of the fluidized bed vessel A second tray installed downstream of the extraction pipe and receiving fluidized bed ash discharged through the extraction pipe; and a second tray provided in the fluidized bed container.
Supply gas to the lower part of the second plate and flow it over the second plate
And a gas inlet pipe for cooling the floor ash.
Forming a second fluidized bed for cooling the fluidized bed ash,
The gas supplied from the pipe and passing through the second fluidized bed is
It is used for the flow of the first fluidized bed through the first dish.
It is characterized by comprising . Thus, in the fluidized bed apparatus, the first plate on the first dish in the fluidized bed container
A second tray is installed downstream of the fluidized bed withdrawal pipe, and gas is supplied from below the second tray by a gas inlet pipe, so that the fluidized bed ash falls below the first fluidized bed in the fluidized bed vessel. the second fluidized bed for cooling is formed, without requiring any special cooling device for cooling the fluidized bed ash, and the second fluidized bed
A large amount of cooling gas is not required by sharing the gas for cooling the fluidized bed ash in the first step with the gas used for flowing the fluidized medium in the first fluidized bed, and the first gas is cooled simultaneously with the cooling of the fluidized bed ash . The gas that fluidizes the fluidizing medium in the fluidized bed of the preheater is preheated. FIG. 1 is an explanatory view of a fluidized bed apparatus according to an embodiment of the present invention. In the figure, a fluidized bed apparatus according to the present embodiment is a fluidized bed apparatus which requires cooling of a fluidized bed ash generated in a fluidized bed reactor such as a fluidized bed boiler and a gasification furnace. Floor container, 3 is first
A first dish of a fluidized bed of the second, 11 for a second fluidized bed ash cooling
The second plate 4 of the fluidized bed is a pipe for extracting the fluidized bed ash, and 9 is a gas inlet pipe for cooling the fluidized bed ash. Although fluidized bed ashes in the fluidized medium is discharged downward through the extraction tube 4, the fluidized bed ash must be cooled because of high temperature and about 800 ° C., shown in FIG. In this fluidized bed apparatus we established a first flow first second perforated plate 11 of the fluidized bed ash cooling the bottom of the perforated plate 3 of the bed as, for fluidized bed ash cooled below the second perforated plate 11 A second fluidized bed for fluidized bed ash cooling is formed in the fluidized bed container 1 by introducing gas. As described above, in the present fluidized bed apparatus , the first dish 3 of the first fluidized bed and the second dish 11 of the second fluidized bed for cooling the ash in the fluidized bed vessel 1 are provided . And is installed. The fluidized bed ash on the first dish 3 of the first fluidized bed enters the lower fluidized bed ash cooling second fluidized bed from the withdrawal pipe 4. The gas for cooling the fluidized-bed ash is introduced into the lower part of the fluidized-bed container 1 from the gas inlet pipe 9 and the second fluid for cooling the fluidized-bed ash is supplied.
The fluidized bed ash is cooled through the second bed 11 of the bed and through the fluidized bed ash layer of the second fluidized bed for cooling the fluidized bed ash.
For this reason, the gas introduced into the fluidized bed container 1 from the gas introduction pipe 9 is warmed, and the first fluidized bed of the first fluidized bed is preheated .
It is supplied to the upper fluidized medium through the perforated plate 3. In the conventional fluidized bed apparatus , a cooling coil or the like is installed downstream of the fluidized bed vessel in order to cool the fluidized bed ash. wear but there is a problem such as occurs, the fluidized bed in the device a second alternative for cooling the fluidized bed ash downstream withdrawal tube of the first flow <br/> fluidized bed in the fluidized bed vessel 1
And the gas used for fluidizing the fluidized medium of the first fluidized bed is used as the gas for cooling the fluidized bed ash, and a separate cooling device is not particularly required for cooling the fluidized bed ash. The gas for cooling the fluidized-bed ash does not require a large amount of gas for cooling the fluidized-bed ash by utilizing the gas used for flowing the fluidized medium in the first fluidized bed. Equipment and operating costs are reduced, such as the ability to preheat the flowing gas. [0008] The fluidized bed apparatus according to the present invention is constructed as described above, does not require a special cooling device for cooling the fluidized bed ash, and has a gas for cooling the fluidized bed ash. If without requiring a large amount of cooling gas by sharing the gas used for the flow of the first <br/> fluidized in a fluidized bed medium, also flow in the first fluidized bed at the same time cooling of the fluidized bed ash Since the gas for fluidizing the medium is preheated, the cost required for operating the fluidized bed apparatus and the fluidized bed apparatus can be reduced.

【図面の簡単な説明】 【図1】図1は本発明の実施の一形態に係る流動床装置
の断面図である。 【図2】図2は従来の流動床装置の断面図である。 【符号の説明】 1 流動床容器 3 第1の目皿 4 抜出し管 9 ガス投入管 11 第2の目皿
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a sectional view of a fluidized bed apparatus according to one embodiment of the present invention. FIG. 2 is a sectional view of a conventional fluidized bed apparatus . [Description of Signs] 1 Fluidized bed container 3 First perforated plate 4 Extraction tube 9 Gas inlet tube 11 Second perforated plate

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) F23C 10/24 F27B 15/16 F23G 5/30 B01J 8/24 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) F23C 10/24 F27B 15/16 F23G 5/30 B01J 8/24

Claims (1)

(57)【特許請求の範囲】 【請求項1】 流動床容器内の第1の目皿上第1の
動床を有し同第1の流動床で生成される流動床灰を抜出
し管を介して下方へ排出する流動床装置において、上記
流動床容器内の上記抜出し管の下流に設置され上記抜出
し管を介して排出される流動床灰を受ける第2の目皿
と、上記流動床容器に設けられ同第2の目皿の下方へガ
スを供給して同第2の目皿上の流動床灰を冷却するガス
投入管とを備え、同第2の目皿上に流動床灰冷却用の第
2の流動床を形成し、上記ガス投入管から供給され上記
第2の流動床を通過したガスを上記第1の目皿を通して
上記第1の流動床の流動に用いるように構成してなる
とを特徴とする流動床装置。
(57) Patent Claims 1. A flow generated by the first perforated plate has a first flow <br/> fluidized bed on the same first fluidized bed in the fluidized bed vessel In a fluidized bed apparatus for discharging bed ash downward through a discharge pipe, a second tray installed downstream of the discharge pipe in the fluidized bed container and receiving the fluidized bed ash discharged through the discharge pipe And a gas inlet pipe provided in the fluidized-bed container for supplying gas below the second dish to cool fluidized-bed ash on the second dish. On top of the fluidized bed ash for cooling
2 to form the fluidized bed,
The gas that has passed through the second fluidized bed is passed through the first pan.
A fluidized bed apparatus configured to be used for the fluidization of the first fluidized bed.
JP28817896A 1996-10-30 1996-10-30 Fluidized bed equipment Expired - Fee Related JP3402962B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28817896A JP3402962B2 (en) 1996-10-30 1996-10-30 Fluidized bed equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28817896A JP3402962B2 (en) 1996-10-30 1996-10-30 Fluidized bed equipment

Publications (2)

Publication Number Publication Date
JPH10132213A JPH10132213A (en) 1998-05-22
JP3402962B2 true JP3402962B2 (en) 2003-05-06

Family

ID=17726829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28817896A Expired - Fee Related JP3402962B2 (en) 1996-10-30 1996-10-30 Fluidized bed equipment

Country Status (1)

Country Link
JP (1) JP3402962B2 (en)

Also Published As

Publication number Publication date
JPH10132213A (en) 1998-05-22

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