JPS63169411A - Fluidized bed boiler - Google Patents
Fluidized bed boilerInfo
- Publication number
- JPS63169411A JPS63169411A JP61310143A JP31014386A JPS63169411A JP S63169411 A JPS63169411 A JP S63169411A JP 61310143 A JP61310143 A JP 61310143A JP 31014386 A JP31014386 A JP 31014386A JP S63169411 A JPS63169411 A JP S63169411A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- fuel
- crusher
- lime
- desulfurization
- 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
Landscapes
- Solid-Fuel Combustion (AREA)
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
、 本発明は砂が流動する流動燃焼室内へ石炭を供給し
て燃焼させ、伝熱管内の水を加熱して蒸気を発生させる
とともに、燃焼後のガスを脱硫剤で脱硫して外部へ排出
する流動床ボイラに関するものである。[Detailed description of the invention] [Industrial application field] The present invention supplies coal into a fluidized combustion chamber in which sand flows, burns it, heats the water in the heat transfer tube, generates steam, and burns the coal. This relates to a fluidized bed boiler that desulfurizes the remaining gas using a desulfurizing agent and discharges it to the outside.
近年、燃焼効率が高くて廃ガス公害が少ないボイラとし
て流動床ボイラが開発されている。この種の流動床ボイ
ラは、ボイラ本体内に下段から順に隔成された貯蔵室、
燃焼室、脱硫窓の3室を備えており、貯蔵室から燃焼室
へ送られて常時所定量だけ燃焼室内に蓄えられた砂を空
気の吹き込みによって流動させ、燃焼室へ供給される石
炭を砂とともに流動させながら燃焼させるものであって
、燃焼室の伝熱管内を通過する水がこの燃焼ガスで加熱
されることによって蒸気が発生する。そして燃焼ガスは
脱硫室で石灰石などの脱硫剤で脱硫されて排気されると
ともに、脱硫室では未燃カーボンが捕獲されて燃焼する
。In recent years, fluidized bed boilers have been developed as boilers with high combustion efficiency and low waste gas pollution. This type of fluidized bed boiler has storage chambers separated from the bottom in order from the bottom of the boiler body.
It is equipped with three chambers: a combustion chamber and a desulfurization window, and the sand that is sent from the storage chamber to the combustion chamber and always stored in the combustion chamber in a predetermined amount is fluidized by blowing air, and the coal supplied to the combustion chamber is converted into sand. Steam is generated by heating the water passing through the heat transfer tubes of the combustion chamber with the combustion gas. The combustion gas is then desulfurized using a desulfurizing agent such as limestone in the desulfurization chamber and exhausted, and unburned carbon is captured and burned in the desulfurization chamber.
しかしながら、従来の流動床ボイラにおいては、脱硫に
使用された廃脱硫剤を排出口から排出して廃棄していた
ので、新たな石灰石の供給量が多く、材料消費面におい
て必ずしも満足すべきものでなかった。However, in conventional fluidized bed boilers, the waste desulfurization agent used for desulfurization is discharged from the outlet and disposed of, which requires a large supply of new limestone, which is not always satisfactory in terms of material consumption. Ta.
このような問題点を解決するために本発明では廃脱硫剤
の排出口に粉砕機を接続するとともに、この粉砕機の石
灰石排出管および別の燃料供給管が接続された成形押出
機とボイラ本体の燃料室とを還元管で接続した。また、
別発明では上記粉砕機にH,0供給管を接続し、粉砕機
とボイラ本体の脱硫室との間を還元管で接続した。In order to solve these problems, in the present invention, a crusher is connected to the waste desulfurization agent discharge port, and a molding extruder and boiler main body are connected to the limestone discharge pipe of the crusher and another fuel supply pipe. The fuel chamber was connected with a reduction pipe. Also,
In another invention, an H,0 supply pipe was connected to the pulverizer, and a reduction pipe was connected between the pulverizer and the desulfurization chamber of the boiler body.
燃焼ガスの脱硫に使用されたのち排出口から排出され九
廃脱硫剤は、粉砕機で粉砕されると、外郭を形成する石
膏が割れて中の石灰が露出し、これを成形押出機に供給
して別に供給した産業廃棄物や未燃灰1石灰等の燃料と
混ぜて練ったのち押出すと、゛ベレット状になって押出
されるので、これを燃焼室へ還元すると、燃料として燃
焼するとともに、脱硫作用もする。また前記粉砕機へH
2Oを供給しながら廃脱硫剤を粉砕すると、水酸化力y
シウムとなって排出されるので、とれを脱硫室1a内し
て脱硫に使用する。After being used to desulfurize the combustion gas, the Kuwase desulfurizing agent is discharged from the exhaust port and is crushed in a crusher. When the plaster that forms the outer shell cracks and the lime inside is exposed, this is fed to the molding extruder. When mixed with separately supplied fuel such as industrial waste and unburned ash 1 lime, kneaded and extruded, it is extruded into a pellet shape, which is then returned to the combustion chamber and burned as fuel. At the same time, it also has a desulfurizing effect. Also, to the crusher
When the waste desulfurization agent is crushed while supplying 2O, the hydration power y
Since it is discharged as sium, the residue is placed in the desulfurization chamber 1a and used for desulfurization.
第1図は本発明に係る流動床ボイラの実施例を示す縦断
面図である。図において流動床ボイラの本体1は、図示
しない複数個の水冷管が埋設された水冷壁2で4方を囲
まれて直方船の箱状に形成されており、その内部には、
3段の水冷管3入り仕切板4,5.6によって下段から
順に空気室7゜貯蔵室8.燃焼室9.脱硫室10が隔成
されている。空気室7と貯蔵室8とには、図示しない送
風装置に接続された送気管11.12がそれぞれ係入さ
れていて空気が吹込まれておplまた、燃焼室9には、
図示しない石炭供給ホッパとの間を乾燥機と粉砕機とを
介して接続された空気輸送式の石炭供給管13が係入さ
れていて石炭が供給されている。さらに、脱硫室10に
は、図示しない石灰石供給ホッパとの間を粉砕機を介し
て接続された空気輸送式の石灰石輸送管14が係入され
ていて脱硫室1a内に常時所定量の石灰石15が蓄えら
れるように供給されている。16は燃焼室9内を千鳥状
に往復するように彎曲して架設された伝熱バイブであっ
て、その一端に連結された送気管1Tは循環ポンプに接
続されておシ、また他端に連結された供給管18は、蒸
気使用設備に接続されている。なお、本実施例に訃いて
は、送気管1Tと供給管18との途中を接続するバイパ
スが設けられていて別に設けた排熱利用ボイラの伝熱チ
ューブとなっている。19は各仕切板4,5.6に複数
個ずつ設けられ、吹込まれた空気を均一に分配しながら
順次上方の室へと吹き上げるディストリビュータである
。FIG. 1 is a longitudinal sectional view showing an embodiment of a fluidized bed boiler according to the present invention. In the figure, the main body 1 of the fluidized bed boiler is surrounded on four sides by water-cooled walls 2 in which a plurality of water-cooled pipes (not shown) are buried, and is shaped like a box of a rectangular ship.
Partition plates 4, 5.6 containing 3 water-cooled pipes in three stages form an air chamber 7° and a storage chamber 8. Combustion chamber9. A desulfurization chamber 10 is separated. Air pipes 11 and 12 connected to an air blower (not shown) are inserted into the air chamber 7 and the storage chamber 8, respectively, and air is blown into the combustion chamber 9.
A pneumatic coal supply pipe 13 connected to a coal supply hopper (not shown) via a dryer and a crusher is connected to supply coal. Furthermore, a pneumatic limestone transport pipe 14 connected to a limestone supply hopper (not shown) via a crusher is inserted into the desulfurization chamber 10, so that a predetermined amount of limestone 15 is always kept in the desulfurization chamber 1a. is supplied so that it can be stored. Reference numeral 16 denotes a heat transfer vibrator installed in a curved manner so as to reciprocate in a staggered manner within the combustion chamber 9, and an air supply pipe 1T connected to one end of the vibrator 16 is connected to a circulation pump, and a The connected supply pipe 18 is connected to steam-using equipment. In addition, in this embodiment, a bypass is provided to connect the air supply pipe 1T and the supply pipe 18 in the middle, and serves as a heat transfer tube of a separately provided waste heat utilization boiler. A plurality of distributors 19 are provided on each of the partition plates 4, 5, and 6, and are used to uniformly distribute the blown air and sequentially blow it up into the upper chambers.
そして、貯蔵室8内には、1.6w程度の径を有する流
動媒体としての砂20が蓄えられており、また、燃焼室
9内にも同じ砂20が、前記供給される石炭の下層に蓄
えられている。21.22は貯蔵室8と燃焼室9とを連
通してそれぞれ設けられた砂20用のアッパカマ−とダ
ウンカマーでありて、手動またはセンナによるレベル検
出等によりて砂20を両室8,9間で往復させ、燃焼室
9内における砂20の量を常時一定に保持するように構
成されている。−万、脱硫室10の上端部には燃焼ガス
を排出する排出口23が設けられてシシ、ダクトにより
前記排熱利用ボイラを経て煙突にf&絖されている。Sand 20 as a fluid medium having a diameter of about 1.6W is stored in the storage chamber 8, and the same sand 20 is also stored in the combustion chamber 9 in the lower layer of the supplied coal. It is stored. Reference numerals 21 and 22 denote an upper comer and a downcomer for the sand 20, which are provided in communication with the storage chamber 8 and the combustion chamber 9, and the sand 20 is transferred to both chambers 8 and 9 by manual or level detection using a senna, etc. The sand 20 is moved back and forth between the combustion chambers 9 and 20 to keep the amount of sand 20 in the combustion chamber 9 constant at all times. - An exhaust port 23 for discharging the combustion gas is provided at the upper end of the desulfurization chamber 10, and the exhaust gas is passed through the exhaust heat utilization boiler to the chimney via a duct.
さらに脱硫室10の水冷壁2に設けた買通孔には、流入
口24aを石灰石15の上層に係入させた廃石灰石用の
抜き出し筒24aが挿通されて7ランク部を水冷壁2の
外面に固定されてi?り、脱硫により変質して上層部に
集まった石灰石15が抜き出し筒24内ヘオーバフロー
して排出されるよりに構成されている。したがって、流
入口24bは常に石灰石150表面に開口している。そ
して、抜き出し筒24から排出される廃石灰石の内部は
、生石灰(Cab)であって外郭を石IF (Cano
e)でくるまれている。25は本本1側にブラケット2
6を介して支持された例えばハンマクラツシャ等の粉砕
機であって、これには抜き出し筒24の排出口24bが
7ランジ接続されておシ、排出口24bから機内へ排出
される廃石灰石を粉砕して石1t (CBSO*)を割
シ、内部の生石灰(Cab)を露出させるように構成さ
れている。2Tは粉砕機25との間を石灰石排出管28
で接続された2軸式の成形押出機であって、これには、
産業廃棄物としての廃プラスティックや石灰石、未燃灰
9石炭などの燃料を供給する燃料供給管29が接続され
ており、両管28.29から供給された生石灰(Cab
)と燃料とを混練しペレット状にして押出すように構成
されている。この成形押出機2Tの押出口と燃焼室9と
は、還元管30で接続されており、成形押出機2Tから
排出された生石灰(Cab)と燃料との混線物が燃焼室
9へ還元されて燃焼するとともに、燃焼ガスの脱硫が行
われる。Furthermore, a waste limestone extraction tube 24a whose inlet 24a is inserted into the upper layer of the limestone 15 is inserted into the through hole provided in the water-cooled wall 2 of the desulfurization chamber 10, and the 7th rank part is inserted into the outer surface of the water-cooled wall 2. Fixed to i? The limestone 15 which has changed in quality due to desulfurization and has gathered in the upper layer overflows into the extraction tube 24 and is discharged. Therefore, the inlet 24b is always open to the surface of the limestone 150. The inside of the waste limestone discharged from the extraction tube 24 is quicklime (Cab), and the outer shell is made of stone IF (Cab).
e) It is wrapped in 25 is the bracket 2 on the book 1 side.
A crusher, such as a hammer crusher, supported through a shaft 6, to which the discharge port 24b of the extraction cylinder 24 is connected with a 7 flange, is used to crush waste limestone discharged into the machine from the discharge port 24b. It is constructed so that 1 ton of stone (CBSO*) is broken open to expose the quicklime (Cab) inside. 2T is a limestone discharge pipe 28 between the crusher 25
A twin-screw molding extruder connected by
A fuel supply pipe 29 is connected to supply fuel such as industrial waste such as waste plastic, limestone, and unburned ash9 coal.
) and fuel are kneaded into pellets and extruded. The extrusion port of the molding extruder 2T and the combustion chamber 9 are connected by a reduction pipe 30, and the mixture of quicklime (Cab) and fuel discharged from the molding extruder 2T is returned to the combustion chamber 9. Along with combustion, the combustion gas is desulfurized.
以上のように構成された流動床ボイラの動作を説明する
。燃焼室9内に蓄えられた砂21の上層へ石炭を供給し
、空気室Tと貯蔵室8とへ空気を送ったのち、バーナ等
で予熱した石炭に点火すると、燃焼用空気の供給によっ
て石炭が燃焼し、この燃焼は、ディストリビュータ19
からの吹き上げ空気で砂21と石炭とが流動することに
よシ促進され、効率よく燃焼する。この燃焼によって伝
熱チューブ16内の水が加熱されて蒸気が発生し、蒸気
使用設備へ供給される。−万、燃焼ガスはディストリビ
ュータ19t−経て脱硫室1Gに入り、硫黄分を除去さ
れ無害のガスとなって排出口23−から排出されるとと
もに、脱硫N1G内では未燃カーボンが捕捉されて燃焼
する。排出口23から排出された燃焼ガスは、別に設け
たボイラを通過するときに供給管18から蒸気使用設備
へ向う蒸気を昇温させたのち、煙突から排出される。The operation of the fluidized bed boiler configured as above will be explained. After supplying coal to the upper layer of sand 21 stored in the combustion chamber 9 and sending air to the air chamber T and the storage chamber 8, when the coal preheated with a burner etc. is ignited, the coal is heated by the supply of combustion air. is combusted, and this combustion is caused by the distributor 19
The sand 21 and coal are fluidized by the air blown up from the combustion chamber, promoting efficient combustion. This combustion heats the water in the heat transfer tube 16 to generate steam, which is supplied to steam-using equipment. -10,000, the combustion gas enters the desulfurization chamber 1G via the distributor 19t-, the sulfur content is removed, it becomes a harmless gas, and is discharged from the exhaust port 23-, while unburned carbon is captured and burned in the desulfurization N1G. . The combustion gas discharged from the exhaust port 23 heats the steam headed from the supply pipe 18 to the steam usage equipment when passing through a separately provided boiler, and then is discharged from the chimney.
また、脱硫室10内の石灰石15のうち、脱硫によシ変
質し流入口24aよりも高くなるように上層へ集まった
廃石灰石15は、流入口24aからオーバ70−し、抜
き出し筒24′f、経て粉砕機25へ排出される。この
廃石灰石は粉砕機25で粉砕されることにより外郭の石
育(CBSO4)が割れて内部の生石灰(Cab)が露
出し、石灰石排出管28を通って成形押出機2Tに供給
される。このとき成れら生石灰(CaO)と燃料とが混
練され押出口からベレット状となって押出される。押出
された生石灰(Cab)と燃料との混線物は、還元管3
0を通って燃焼室9へ還元され、燃料は燃焼し生石灰は
燃焼ガスの脱硫に使用される。Furthermore, among the limestone 15 in the desulfurization chamber 10, the waste limestone 15 that has changed in quality due to desulfurization and has gathered in an upper layer so as to be higher than the inlet 24a flows over the inlet 70- from the inlet 24a and reaches the extraction tube 24'f. , and then discharged to the crusher 25. This waste limestone is crushed by the crusher 25, thereby cracking the outer stone wall (CBSO4) and exposing the internal quicklime (Cab), which is then supplied to the molding extruder 2T through the limestone discharge pipe 28. At this time, the quicklime (CaO) and fuel are kneaded and extruded from the extrusion port in the form of a pellet. The mixture of extruded quicklime (Cab) and fuel is removed from the reduction pipe 3.
0 and is returned to the combustion chamber 9, where the fuel is combusted and the quicklime is used to desulfurize the combustion gas.
なお、上記燃料供給管29から成形押出!!!27に供
給される新燃料としては、廃ガス中の未燃灰を利用する
ことができる。すなわち、排出管23と図示しないボイ
ラとの間に集塵機を設けて未燃分の多い灰を取出し、こ
れを底形押出機27に供給して石灰石とともに燃焼室へ
還元し、新たな石灰に合流させて燃焼させれば、未燃分
を有効に燃焼させることができる。In addition, molding extrusion is performed from the fuel supply pipe 29! ! ! As the new fuel supplied to No. 27, unburned ash in the waste gas can be used. That is, a dust collector is provided between the discharge pipe 23 and a boiler (not shown) to extract ash with a large amount of unburned content, which is supplied to the bottom extruder 27 and returned to the combustion chamber together with limestone, where it is combined with new lime. If the fuel is allowed to combust, the unburned matter can be effectively combusted.
第2因は別発明に係る流動床ボイラの実施例を示す縦断
面図で6ってこれを同図に基づいて説明する。ボイラ本
体と抜き出し筒ならびに粉砕機の構成はWc1図に示す
流動床ボイラと同溝成であるから、これと同符号を付し
てその構成と動作との説明を省略する。粉砕機25には
蒸気または温水などのH2Oを供給する&O供給管31
が接続されており、粉砕機25の生石灰排出口とボ゛イ
ラ本体の脱硫室10側とは、還元管32で接続されてい
る。The second factor is a vertical cross-sectional view showing an embodiment of a fluidized bed boiler according to another invention, and this will be explained based on the same figure. Since the configurations of the boiler main body, extraction tube, and crusher are the same as those of the fluidized bed boiler shown in Figure Wc1, the same reference numerals will be given to them, and the explanation of their configuration and operation will be omitted. An &O supply pipe 31 supplies H2O such as steam or hot water to the crusher 25.
The quicklime discharge port of the crusher 25 and the desulfurization chamber 10 side of the boiler body are connected by a reduction pipe 32.
このように構成されていることにより流入口24からオ
ーバ7 a−して粉砕機25へ供給された廃石灰石は、
H2O供給管31から供給される蒸気。With this configuration, the waste limestone supplied from the inlet 24 to the crusher 25 is
Steam supplied from the H2O supply pipe 31.
温水などのH2Oを加えられながら粉砕され、外郭の石
育(C,SO4)が割れて内部の生石灰(Cab)が露
出する。この結果C,OとH2Oとが反応し水酸化カル
シクム(CB(OH)m)となって排出される。排出さ
れた水酸化カルシクム(Ca (OH) 鴬)は還元管
32を通って脱硫室10へ還元され、脱硫剤として燃焼
ガスの脱硫に使用される。It is crushed while adding H2O such as hot water, and the outer stone (C, SO4) cracks and the quicklime (Cab) inside is exposed. As a result, C, O, and H2O react to form calcium hydroxide (CB(OH)m), which is discharged. The discharged calcium hydroxide (Ca(OH)) is reduced to the desulfurization chamber 10 through the reduction pipe 32, and is used as a desulfurization agent for desulfurization of the combustion gas.
なお1.前記各実施例では、粉砕機25を抜き出し筒2
4の排出口24bに直結してボイラ本体に直接取付けた
例を示したが、粉砕!!25をボイラ本体とは別体で設
け、抜き出し筒24から排出された廃石灰石をいったん
タンク等に蓄えてから所要量ずつ粉砕機25に供給して
粉砕を行なうようにしてもよい。また、実施例のように
ボイラ′7g:体に直続した粉砕機25と成形押出!!
27との間にタンク等を設け、粉砕機25で粉砕して得
た生石灰fシュートやコンベア等でこのタンクへ供給し
て蓄えたのち、所要量ずつ成形押出機2Tへ送シ込んで
もよい。Note 1. In each of the above embodiments, the crusher 25 is extracted and the cylinder 2 is removed.
An example was shown in which it was directly connected to the discharge port 24b of No. 4 and attached directly to the boiler body, but it was crushed! ! 25 may be provided separately from the boiler main body, and after the waste limestone discharged from the extraction tube 24 is stored in a tank or the like, the required amount is supplied to the crusher 25 for crushing. In addition, as in the example, boiler '7g: crusher 25 directly connected to the body and extrusion molding! !
A tank or the like may be provided between the pulverizer 25 and the quicklime 27, and the quicklime obtained by pulverizing it in the pulverizer 25 may be supplied to this tank using a chute, a conveyor, etc., stored therein, and then sent in the required amount to the molding extruder 2T.
さらに、前記各実施例では脱硫剤として石灰石を例示し
たが例えばドロマイトなど他の脱硫剤でもよい。Further, in each of the above embodiments, limestone is used as an example of the desulfurizing agent, but other desulfurizing agents such as dolomite may also be used.
以上の説明により明らかなよりに、本発明によれば流動
床ボイラにシいて、廃脱硫剤の排出口に粉砕機を接続す
るとともに、この粉砕機の石灰石排出管と別の燃料管と
が接続された成形押出機とボイラ本体の燃焼室とを還元
管で接続し、新燃料が添加された廃石灰石を燃焼管へ還
元して燃焼と脱硫とを行わせるように構成したことによ
り、廃石灰石が有効に利用され、石灰石の供給量を減少
させることができる。また別発明によれば、廃脱硫剤の
排出口に粉砕機を接続するとともに、この粉砕機にH2
Oの供給管を接続してこの粉砕機とボイラ本体の脱硫室
とを還元管で接続し、廃石灰石を迅速な反応で水酸化カ
ルシウムにして脱硫室へ還元し脱硫を行わせるよ5に溝
底したことにより、廃石灰石が有効に利用され、新丸な
石灰石の供給量を減少させることができて資源の節減が
計れる。As is clear from the above explanation, according to the present invention, in a fluidized bed boiler, a pulverizer is connected to the waste desulfurization agent outlet, and the limestone discharge pipe of the pulverizer is connected to another fuel pipe. By connecting the molding extruder and the combustion chamber of the boiler body with a reduction pipe, waste limestone with new fuel added is returned to the combustion pipe to perform combustion and desulfurization. can be effectively utilized and the amount of limestone supplied can be reduced. According to another invention, a crusher is connected to the outlet of the waste desulfurization agent, and H2
Connect the O supply pipe and connect this pulverizer to the desulfurization chamber of the boiler main body with a reduction pipe, and use a quick reaction to turn waste limestone into calcium hydroxide and return it to the desulfurization chamber to perform desulfurization. By draining the limestone, waste limestone can be used effectively and the supply of fresh limestone can be reduced, leading to resource savings.
第1図は特許請求の範囲第1項記載の発明に係る流動床
ボイラの実施例を示す縦断面図、第2、特許請求の範囲
第2項記載の発明に係る流動床ボイラの縦断面図である
。
1・・・・本体、2・・・・水冷壁、9・・・−燃焼室
、10・・Φ・脱硫室、1411・・Φ石灰石輸送管、
15・・・・石灰石、23・・・・排出口、24・・・
・抜き出し筒、24a・・・・流入口、24b・・・・
流出口、25・拳・争粉砕機、27・・・―成形押出機
、28・・・・石灰石排出管、29・・e・燃料供給管
、3Qees−還元管、31・・・・H2O供給管、3
2・・拳・還元管。FIG. 1 is a longitudinal cross-sectional view showing an embodiment of the fluidized bed boiler according to the invention set forth in claim 1, and FIG. 2 is a longitudinal cross-sectional view of the fluidized bed boiler according to the invention set forth in claim 2. It is. 1...Main body, 2...Water cooling wall, 9...-combustion chamber, 10...Φ desulfurization chamber, 1411...Φ limestone transport pipe,
15...limestone, 23...outlet, 24...
・Extraction cylinder, 24a...Inflow port, 24b...
Outlet, 25.Fist/war crusher, 27..-forming extruder, 28..limestone discharge pipe, 29..e. fuel supply pipe, 3Qees-reduction pipe, 31..H2O supply tube, 3
2. Fist/reduction tube.
Claims (2)
剤を粉砕して外郭の石膏から石灰を露出させる粉砕機を
接続するとともに、この粉砕機の石灰排出管および別に
設けた燃料供給管が接続されこれら両管からの石灰と燃
料とを混練して押出す成形押出機を設けてその押出口と
ボイラ本体内の燃焼室とを還元管で連結したことを特徴
とする流動床ボイラ。(1) A pulverizer that crushes the waste desulfurizing agent to be discharged and exposes lime from the outer plaster is connected to the exhaust port of the waste desulfurizing agent, and a lime discharge pipe of this pulverizer and a separate fuel supply are connected. A fluidized bed boiler characterized in that a molding extruder is provided in which pipes are connected and lime and fuel from both pipes are kneaded and extruded, and the extrusion outlet and the combustion chamber in the boiler body are connected by a reduction pipe. .
剤を粉砕して外郭の石膏から石灰を露出させる粉砕機を
接続するとともに、この粉砕機にH_2Oの供給管を接
続し、かつこの粉砕機とボイラ本体の脱硫室とを還元管
で連結したことを特徴とする流動床ボイラ。(2) A pulverizer that crushes the waste desulfurizing agent to be discharged to expose lime from the outer plaster is connected to the waste desulfurizing agent outlet, and a H_2O supply pipe is connected to this pulverizer, and A fluidized bed boiler characterized in that this crusher and a desulfurization chamber of the boiler body are connected through a reduction pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61310143A JPS63169411A (en) | 1986-12-29 | 1986-12-29 | Fluidized bed boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61310143A JPS63169411A (en) | 1986-12-29 | 1986-12-29 | Fluidized bed boiler |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63169411A true JPS63169411A (en) | 1988-07-13 |
Family
ID=18001683
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61310143A Pending JPS63169411A (en) | 1986-12-29 | 1986-12-29 | Fluidized bed boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63169411A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5577605A (en) * | 1978-12-08 | 1980-06-11 | Mitsubishi Heavy Ind Ltd | Fluidized bed type combustion apparatus |
| JPS5664207A (en) * | 1979-10-29 | 1981-06-01 | Babcock Hitachi Kk | Fluidized bed furnace having desulfurizing agent supplying system |
| JPS5819612A (en) * | 1981-07-28 | 1983-02-04 | Babcock Hitachi Kk | Fluidized bed combustion device |
| JPS58150417A (en) * | 1982-03-03 | 1983-09-07 | Sumitomo Heavy Ind Ltd | Desulfurization of waste gas |
| JPS6118422A (en) * | 1984-07-05 | 1986-01-27 | Kawasaki Heavy Ind Ltd | Desulfurization agent/fly ash granulation supply method in fluidized bed boiler |
-
1986
- 1986-12-29 JP JP61310143A patent/JPS63169411A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5577605A (en) * | 1978-12-08 | 1980-06-11 | Mitsubishi Heavy Ind Ltd | Fluidized bed type combustion apparatus |
| JPS5664207A (en) * | 1979-10-29 | 1981-06-01 | Babcock Hitachi Kk | Fluidized bed furnace having desulfurizing agent supplying system |
| JPS5819612A (en) * | 1981-07-28 | 1983-02-04 | Babcock Hitachi Kk | Fluidized bed combustion device |
| JPS58150417A (en) * | 1982-03-03 | 1983-09-07 | Sumitomo Heavy Ind Ltd | Desulfurization of waste gas |
| JPS6118422A (en) * | 1984-07-05 | 1986-01-27 | Kawasaki Heavy Ind Ltd | Desulfurization agent/fly ash granulation supply method in fluidized bed boiler |
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