JPS582507A - Burning method of solid - Google Patents

Burning method of solid

Info

Publication number
JPS582507A
JPS582507A JP10173681A JP10173681A JPS582507A JP S582507 A JPS582507 A JP S582507A JP 10173681 A JP10173681 A JP 10173681A JP 10173681 A JP10173681 A JP 10173681A JP S582507 A JPS582507 A JP S582507A
Authority
JP
Japan
Prior art keywords
solids
solid
furnace
combustion
combustion furnace
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.)
Granted
Application number
JP10173681A
Other languages
Japanese (ja)
Other versions
JPS6246763B2 (en
Inventor
Seiichi Takahashi
清一 高橋
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 JP10173681A priority Critical patent/JPS582507A/en
Publication of JPS582507A publication Critical patent/JPS582507A/en
Publication of JPS6246763B2 publication Critical patent/JPS6246763B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B7/00Combustion techniques; Other solid-fuel combustion apparatus

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Fuel Combustion (AREA)

Abstract

PURPOSE:To obtain burning method of solid, through which fuel is burnt effectively even if powderly wolid is mingled with it, by pelletizing the unburnt solid contained in an exhaust gas, and burning in a combustion furnace. CONSTITUTION:Massive solid in a solid fuel is supplied into a combustion furnace 1 through a fuel supply device 2. On the other hand, powderly solid is sent to a pelletizing device 7 through a transportation means 10. The unburnt solid within exhaust gas from the combustion furnace 1 is collected by an unburnt solid collector 4, and sent to the pelletizing device 7 through the transportation means 5. In the pelletizing device 7 the mixture of the solid and the powdery solid are made into a pellet form which is sent to the combustion furnace 1. Thus, even if a large quantity of the powdery solid is contained in the fuel it is used as fuel and its combustion efficiency is improved, too.

Description

【発明の詳細な説明】 本発明は、燃焼炉9例えばストーカ焚き燃焼炉等で石炭
、木片、ピッチ、プラスチック等の固形物を燃焼させる
固形物燃焼方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solid material combustion method for burning solid materials such as coal, wood chips, pitch, and plastics in a combustion furnace 9, such as a stoker-fired combustion furnace.

従来の燃焼方法を第1図に示す態様例に基づいて説明す
る。・ 燃焼炉01には塊′状固彫物、粉状固形物を燃焼炉O1
内に供給する燃料供給装置02が設けられ、燃焼炉01
の排ガス出口に設けられたダクト03の途中には未燃固
形物捕集装置04が設けられて−る。未燃固形物捕集装
置04の未燃固形物出口には、未燃固形物を燃゛焼炉0
1”内に導゛〈輸送手段05が連結されている。又、燃
焼炉O1は、燃焼炉O1に燃焼用空気を供給するための
送風機06と連通している。
A conventional combustion method will be explained based on the embodiment shown in FIG. - In the combustion furnace 01, solid carved pieces and powdered solids are placed in the combustion furnace 01.
A fuel supply device 02 is provided to supply fuel into the combustion furnace 01.
An unburnt solids collection device 04 is provided in the middle of a duct 03 provided at the exhaust gas outlet of the engine. At the unburned solids outlet of the unburned solids collection device 04, the unburned solids are transferred to the combustion furnace 0.
The combustion furnace O1 is connected to a blower 06 for supplying combustion air to the combustion furnace O1.

燃焼炉O1内に燃料供給装置02から塊状固形物を供給
し、送風機06を介して供給される空気によって固形物
を燃焼させる。ダクト03内を流れる排ガス中に含まれ
る灰と未燃固形物は未燃固形物捕集装置04で分離し、
灰は炉外へ排失し、未燃固形物は再び輸送手段0.5を
介して燃焼炉01内に供給され再燃焼する。
A lumpy solid is supplied into the combustion furnace O1 from a fuel supply device 02, and the solid is combusted by air supplied via a blower 06. Ash and unburned solids contained in the exhaust gas flowing in the duct 03 are separated by an unburnt solids collector 04,
The ash is discharged to the outside of the furnace, and the unburned solids are again supplied into the combustion furnace 01 via the transportation means 0.5 and re-burned.

従来の方法では1回収した未燃固形物を燃焼炉01に戻
しても1.完全に燃焼し切らず、未燃分として系外に持
ち去られ廃棄処理に手間を要していた。又燃料供給装置
02から燃焼炉01内へ供給される塊状固形物中にも多
量の粉状固形物が含まれており、塊状固形物と粉状固形
物の混在によって塊状固形物のみの場合よシ燃焼しK<
<送風機06の動力を大きくする例があった。そのため
粉状固形物を前□処理段階で分離してから塊状固形物の
みを燃料とすることも行李数回にわたり、未燃固形物捕
集装置04と燃焼炉010間を循環する必要があるため
、未燃固形物捕集装置04の容量を大きくしたり循環系
の目づまりや摩耗の対策を講じていた。
In the conventional method, even if the recovered unburned solids are returned to the combustion furnace 01, 1. It was not completely combusted and was carried out of the system as unburned matter, requiring time and effort to dispose of it. Furthermore, the lumpy solids supplied from the fuel supply device 02 into the combustion furnace 01 also contain a large amount of powdery solids, and due to the mixture of lumpy solids and powdery solids, the amount of powdery solids is higher than in the case of only lumpy solids. It burns and K<
<There was an example of increasing the power of the blower 06. For this reason, it is necessary to separate the powdery solids in the pre-processing stage and then use only the lumpy solids as fuel, which requires several trips and circulation between the unburned solids collector 04 and the combustion furnace 010. Measures were taken to prevent clogging and abrasion of the circulation system, such as increasing the capacity of the unburned solids collector 04.

そこで本発明は、固形物燃料及び燃焼炉から排出される
未燃分を効率よく、かつ安定して燃焼させるための固定
物燃焼方法を提供することを目的と、してなiれたもの
であり1本1発明は。
SUMMARY OF THE INVENTION Therefore, the present invention has been made with the object of providing a method for burning solid materials to efficiently and stably burn solid fuel and unburned matter discharged from a combustion furnace. There is one invention per book.

燃焼炉内に固鯵物を供給して燃焼させるとともに、炉外
に排出される排ガス中の未燃固形物を回収した後炉内へ
供給して再燃焼させる固形物燃焼方法において、前記固
形物を塊状固形物と粉状固形物とに分離して前記塊状固
形物を炉内レット化し炉内へ供給して燃焼させることを
特徴とする固形物燃焼方法を提供している。
In a solid matter combustion method, in which a hard mackerel is supplied into a combustion furnace and combusted, and unburned solid matter in exhaust gas discharged outside the furnace is recovered and then supplied into the furnace and re-burned, the solid matter is The present invention provides a solid matter combustion method, which comprises separating solid matter into lumpy solids and powdery solids, turning the lumpy solids into pellets in a furnace, and feeding the pellets into the furnace for combustion.

本発明が提供する方法によれば、排ガス中の未燃固形物
と粉状固形物とをペリ1.ト化して燃焼炉内で燃焼させ
るので、未燃固形物が炉外へ未燃焼の11排失されない
ので燃焼効率が良く・粉状固形物の減少に伴ない燃焼が
安定化し1機器の容量アップも不用で、燃料中に粉状固
形物が混在していても効率よく燃郷でき、燃料が完全燃
焼するので、系内の多数回の循環が不用・となり、系内
の目づまりや摩耗のトラブルも少なく灰のみが廃棄物と
して排出されるので廃棄処理が簡単となり、燃料中に多
量の粉状固形物が含まれていても燃料として使え各種燃
料が使用できるようになる、等の利点が得られる。  
 ・さらに本発明は、燃焼炉内に固形物を供給して燃焼
させるとと也に、炉外に排出される排ガ′中の未燃固形
物を豐収した後炉内゛供給して再燃焼させる固形物、l
&焼、方法において、爆〜へ蒐前記固形物を塊状固形物
と粉状固形物とに分離して前記塊状固形物を炉内に供給
して燃焼さ、せるとともに、前記未燃固形物を回収した
後。
According to the method provided by the present invention, unburned solids and powdered solids in exhaust gas are removed from the periphery 1. Since the unburned solids are combusted in the combustion furnace, the combustion efficiency is improved because unburned solids are not discharged outside the furnace, and combustion is stabilized due to the reduction of powdery solids, increasing the capacity of the equipment. Even if powdery solids are mixed in the fuel, it can be burned efficiently and the fuel is completely combusted, eliminating the need for multiple circulations within the system and reducing clogging and abrasion within the system. There are fewer troubles and only the ash is discharged as waste, making disposal easier, and even if the fuel contains a large amount of powdery solids, it can be used as fuel, and various other fuels can be used. can get.
・Furthermore, the present invention provides that when solids are fed into the combustion furnace and combusted, unburned solids in the exhaust gas discharged outside the furnace are collected and then fed back into the furnace for regeneration. solids to be burned, l
In the burning method, the solid matter is separated into lumpy solids and powdery solids, and the lumpy solids are fed into a furnace to be burned, and the unburnt solids are removed. After collecting.

前記粉状固形物と混合してペレット化し、その−後炉内
又は排ガスの熱で餉記ベレ□ットを乾燥し炉内へ供給し
て燃焼させることを特徴とする固形物燃焼方法を提供し
ており1本発明方−によれば、さらに廃熱を利用しそペ
レットを乾燥させるので、十分な強度のペレットが得ら
れ、循環系のトラブルがより減少するという利点がある
Provided is a solid matter combustion method characterized in that the pelletized pellets are mixed with the powdered solid matter, and then the pellets are dried in a furnace or with the heat of exhaust gas, and then fed into a furnace and burned. According to the method of the present invention, the waste heat is further used to dry the perilla pellets, which has the advantage that pellets with sufficient strength can be obtained and troubles in the circulation system can be further reduced.

次に本発明を第2図に示す第1の実施の態様例に基づい
て具体的に説′興する。
Next, the present invention will be specifically explained based on a first embodiment shown in FIG.

燃焼炉1には、塊状固形物を燃焼炉1内に供給する燃料
供給装置2が設けられ、燃焼炉lの排ガス出口に連結さ
れたダクト3の途中には未燃固形物捕集装置4が設けら
れている。未燃固形物捕集装置4の未燃固形物排出口に
は未燃固形物をペレット製造装置7内に導く輸送手段5
が設けられている。。固形物を塊・状固形物と粉状固形
物とに分け′・る分級器8、には、塊状・固形物排出口
から塊状固形物を燃料供給装置2に導く輸送手段9が設
けられ、又、さらに分級器8には粉状固形物をペレット
化製造装置7に導く輸送手段lOが設けられている。ペ
レット化製造装置7には、ベレットを燃焼炉l内に導く
輸送手段11が設けられている。又9さらに燃焼炉1は
、燃焼炉1内に燃焼用空気を供給するだめの送風機6と
連通している。なお、ペレット化製造装置7は、適、当
な水分で粉体物をペレット化するものである。
The combustion furnace 1 is provided with a fuel supply device 2 that supplies lumpy solids into the combustion furnace 1, and an unburned solids collection device 4 is installed in the middle of a duct 3 connected to the exhaust gas outlet of the combustion furnace 1. It is provided. At the unburned solids discharge port of the unburned solids collection device 4, there is a transportation means 5 for guiding the unburned solids into the pellet manufacturing device 7.
is provided. . A classifier 8 for separating solids into lump-like solids and powder-like solids is provided with a transportation means 9 for guiding the lump-like solids from a lump-solid discharge port to the fuel supply device 2, Furthermore, the classifier 8 is provided with a transport means 10 for guiding the powdery solids to the pelletizing production device 7. The pelletizing production device 7 is provided with a transport means 11 that guides the pellets into the combustion furnace 1. Furthermore, the combustion furnace 1 is in communication with a blower 6 for supplying combustion air into the combustion furnace 1. Incidentally, the pelletizing production device 7 is used to pelletize the powdered material using appropriate moisture.

固形物燃料中の塊状固形物は1分級器8で粉状固形物と
分離され輸送手段9を介して燃料供給装置2に送られ、
燃・料供給装置2により燃焼炉lへ供給する。一方粉状
固形物は輸送手段10を介してペレット製造装置7へ送
られる。燃焼、炉lからの排ガス中の未燃固形物は未燃
固形物捕集装置4で捕集され1.輸送手段5によりペレ
ット製造装置7へ送られる。
The lumpy solids in the solid fuel are separated from the powdered solids by a classifier 8 and sent to the fuel supply device 2 via a transportation means 9.
The fuel is supplied to the combustion furnace l by the fuel supply device 2. On the other hand, the powdered solids are sent to the pellet manufacturing device 7 via the transportation means 10. Unburned solids in the exhaust gas from the combustion furnace 1 are collected by an unburned solids collector 4.1. The pellets are sent to the pellet manufacturing device 7 by the transportation means 5.

ペレット製造装置7では、適当な水分で未燃固形物と粉
体固形物とを混合してペレット化しベレットは、輸送手
段11により燃焼炉1に送られ、燃焼炉内でペレット化
した状態で燃焼する。排ガス中の未燃固形物と、燃料か
ら分離された粉状固形物とを特殊なバインダーを用いず
適当な水分のみでペレットにして燃焼炉l内で燃焼させ
るので、ペレット化に高い費用を要せず未燃固形物が燃
焼炉1外へ未燃焼のtま排失されないので燃焼効率が良
く、粉状固形物の減少に伴ない燃焼が安定化し2機器の
容量アップも不用で燃料中に粉状固形物が混在していて
も効率よく燃焼でき、燃料が完全燃焼するので、系内の
多数回の微開が不要となり、系内の目づまりや摩耗のト
ラブルも少なく灰のみが廃棄物として排出されるので廃
棄処理が従来より簡単となシ、そして燃料中に多量の粉
状固形物が含まれていても燃料として使え各種燃料が使
用できるようになる。
In the pellet production device 7, unburnt solids and powder solids are mixed with appropriate moisture and pelletized, and the pellets are sent to the combustion furnace 1 by means of transportation 11, and burned in the pelletized state in the combustion furnace. do. The unburned solids in the exhaust gas and the powdered solids separated from the fuel are made into pellets using only an appropriate amount of moisture without using a special binder and are burned in a combustion furnace, which requires high costs for pelletizing. The combustion efficiency is good because the unburned solids are not discharged outside the combustion furnace 1 until unburned, and the combustion is stabilized as the powdery solids are reduced, and there is no need to increase the capacity of 2 devices. Even if powdery solids are mixed in, it can be efficiently combusted, and the fuel is completely combusted, so there is no need to open the system multiple times, and there are fewer clogging and abrasion problems in the system, and the only waste is ash. This makes disposal easier than before, and even if the fuel contains a large amount of powdery solids, it can be used as fuel, making it possible to use a variety of fuels.

次に本発明を第3図に示す第2の実施態様例に基づいて
説明する。
Next, the present invention will be explained based on a second embodiment shown in FIG.

本例の装置は、第1の実施態様例の装置のペレット化製
造装置7にダクト3を流れる排ガスの1部を導入し、排
ガスの熱でペレットを乾燥させるペレット乾燥装置12
を設けたもので。
The apparatus of this example introduces a part of the exhaust gas flowing through the duct 3 into the pelletizing production apparatus 7 of the apparatus of the first embodiment, and a pellet drying apparatus 12 that dries the pellets with the heat of the exhaust gas.
It has been set up.

その他は第1の実施態様例の装置と同じであり。The rest is the same as the device of the first embodiment.

ここでは−造の説明は省略する。The explanation of the construction will be omitted here.

固形状の燃料中の塊状固形物は分iN8で粉状固形物と
分離し、燃料供給装置2で燃焼炉1へ供給する。一方粉
状固形物はペレット製造装置7へ送る。燃焼の排ガス中
に含まれる未燃固形物は、未燃固形物捕集装置4で分離
され、ペレット製造装置7へ送られる。ペレット製造装
置7へ送られた未燃固形物には、燃焼灰が多量に混入す
るため、特種なバインダーを混合しなくても適量の水分
があれば容易にペレット化する。このペレットは、排ガ
スの余熱を利用したベレット乾燥装置稔で十分な強度ま
で固化し。
The lumpy solids in the solid fuel are separated from the powdered solids in a minute iN8, and are supplied to the combustion furnace 1 by the fuel supply device 2. On the other hand, the powdered solids are sent to the pellet manufacturing device 7. Unburned solids contained in the combustion exhaust gas are separated by an unburned solids collector 4 and sent to a pellet manufacturing device 7. Since a large amount of combustion ash is mixed in the unburned solids sent to the pellet production device 7, it can be easily pelletized without mixing a special binder as long as there is an appropriate amount of moisture. These pellets are solidified to sufficient strength using a pellet dryer that uses residual heat from exhaust gas.

ベレット燃料として燃焼炉lへ送られて、そこで燃焼す
る。
It is sent as pellet fuel to the combustion furnace I, where it is burned.

従って本例によれば、未燃損失の減少と廃棄物処理の省
力化ができ、粉状固形物の減少に伴なう燃焼の安定化が
可能で、排ガスの余熱を利用するので簡単な装置で十分
な強度のベレット殻製作でき、循環系のトラブルも減少
する。
Therefore, according to this example, it is possible to reduce unburned loss and save labor in waste treatment, stabilize combustion due to the reduction of powdery solids, and use the residual heat of exhaust gas, so it is possible to use a simple device. It is possible to produce a pellet shell with sufficient strength, and problems with the circulatory system are also reduced.

さらに次に1本発明を第4図に示す第3の実施の態様例
に基づいて説明する。
Next, one aspect of the present invention will be explained based on a third embodiment shown in FIG.

本例は、第′3図に示す第2の実施態様例におけるベレ
ット乾燥装置12を燃焼炉1内に配置し・″″″ト化製
造“と″″″ト乾燥装置12とを輸送手段11で連結し
、ペレット化製造装置7かム送られてきたペレ・トをペ
レ・ト乾燥装置12、□内で、燃焼炉1内の熱を利用し
て乾燥し9.乾燥後のペレットをストーカ等の炉底の燃
焼床へ供給するものである。
In this example, the pellet drying device 12 in the second embodiment shown in FIG. 9. The pellets sent through the pelletizing production device 7 are dried in the pellet drying device 12, using the heat in the combustion furnace 1. It is supplied to the combustion bed at the bottom of the hearth.

本例の作用効果については、第2の実施態様例と#1ぼ
同一の作用効果(奏するので、ここではその説明を省略
する。
The effects of this example are almost the same as those of the second embodiment, so the explanation thereof will be omitted here.

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

第1図は従来の固形物燃焼方法を実施する装置のフロー
チャート図、第2図ないし第4図は夫々は本発明の第1
ないし第3の実施のi機側のフローチャート図下ある。 01、l・・・燃焼炉、02,2・・・燃料供給装置。 04.4・・・未燃固形物捕集装置、06,6・・・送
風機、7・・・ペレット乾燥装置、8・・・分級器。 12・・・ペレット乾燥装置。 N4図
FIG. 1 is a flowchart of an apparatus for carrying out a conventional solid matter combustion method, and FIGS.
The flowchart on the i-machine side of the third implementation is shown below. 01, l... Combustion furnace, 02,2... Fuel supply device. 04.4...Unburnt solids collection device, 06,6...Blower, 7...Pellet drying device, 8...Classifier. 12... Pellet drying device. N4 diagram

Claims (1)

【特許請求の範囲】 +11  燃焼炉内に固形物を供給して燃焼させるとと
ヤもに、炉外に排出される排ガス中の未燃固形物を“回
収した後炉内へ需給して再燃焼させる固形物燃焼方法に
おいて、前記固形物を塊゛ 状面彫物と粉状固形物とに
分離して前記塊状i彫物1%・炉内に供給して燃焼させ
るとともに。 前記未燃固形物を回収した後、前記粉状固形物と混合し
てペレット化し炉内へ供給して燃・焼させることを特徴
とする固形物燃焼方法。 (2)  燃焼炉内KIi形物彫物給して燃焼させると
ともに、炉外に排出される排ガス中の未燃固形物を回収
した後炉内へ供給して再燃・焼させる固形物燃焼、方法
において、前記固形物を塊状固形物、と粉状II形彫物
に分離して、前記塊状固形物を炉内に供給して燃焼させ
るととも°に、前記未燃固形物を回収した後前記粉状固
形物と混合してペレット化し、その後炉内又は排ガスの
熱で前記ペレットを乾燥し炉内へ供給して燃焼させるこ
とを特徴とする固形物燃焼方法。
[Claims] +11 When solids are supplied into the combustion furnace and combusted, the unburned solids in the exhaust gas discharged outside the furnace are “recovered and then supplied and supplied to the furnace for reuse.” In the solid matter combustion method, the solid matter is separated into a lump-like surface carved material and a powdered solid material, and the solid material is fed into the lump-shaped carved material 1% furnace and burned.The unburned solid material is A solid matter combustion method characterized in that, after being collected, the solid matter is mixed with the powdered solid matter, pelletized, and fed into a furnace for combustion. (2) KIi shaped sculptures are fed into the combustion furnace and burned. In addition, in a solid combustion method in which unburned solids in the exhaust gas discharged outside the furnace are collected and then supplied into the furnace for reburning and burning, the solids are converted into lump solids and powdered II shape carvings. The lumpy solids are fed into the furnace and burned, and the unburnt solids are collected and mixed with the powdery solids to pelletize them, and then stored in the furnace or in the exhaust gas. A solid matter combustion method characterized by drying the pellets with heat and supplying the pellets into a furnace for combustion.
JP10173681A 1981-06-30 1981-06-30 Burning method of solid Granted JPS582507A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10173681A JPS582507A (en) 1981-06-30 1981-06-30 Burning method of solid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10173681A JPS582507A (en) 1981-06-30 1981-06-30 Burning method of solid

Publications (2)

Publication Number Publication Date
JPS582507A true JPS582507A (en) 1983-01-08
JPS6246763B2 JPS6246763B2 (en) 1987-10-05

Family

ID=14308533

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10173681A Granted JPS582507A (en) 1981-06-30 1981-06-30 Burning method of solid

Country Status (1)

Country Link
JP (1) JPS582507A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03104951U (en) * 1990-11-09 1991-10-30

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03104951U (en) * 1990-11-09 1991-10-30
JPH055637Y2 (en) * 1990-11-09 1993-02-15

Also Published As

Publication number Publication date
JPS6246763B2 (en) 1987-10-05

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