JPS6246763B2 - - Google Patents
Info
- Publication number
- JPS6246763B2 JPS6246763B2 JP10173681A JP10173681A JPS6246763B2 JP S6246763 B2 JPS6246763 B2 JP S6246763B2 JP 10173681 A JP10173681 A JP 10173681A JP 10173681 A JP10173681 A JP 10173681A JP S6246763 B2 JPS6246763 B2 JP S6246763B2
- Authority
- JP
- Japan
- Prior art keywords
- solids
- combustion furnace
- solid matter
- combustion
- unburned
- 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
Links
- 239000007787 solid Substances 0.000 claims description 107
- 238000002485 combustion reaction Methods 0.000 claims description 62
- 239000008188 pellet Substances 0.000 claims description 32
- 238000005453 pelletization Methods 0.000 claims description 11
- 238000009841 combustion method Methods 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 8
- 239000000446 fuel Substances 0.000 description 21
- 239000007789 gas Substances 0.000 description 14
- 238000004519 manufacturing process Methods 0.000 description 14
- 230000004087 circulation Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000011343 solid material Substances 0.000 description 3
- 239000004449 solid propellant Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000005299 abrasion Methods 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23B—METHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
- F23B7/00—Combustion 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)
Description
【発明の詳細な説明】
本発明は、燃焼炉、例えばストーカ焚き燃焼炉
等で石炭、木片、ピツチ、プラスチツク等の固形
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 plastic in a combustion furnace, 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。 A conventional combustion method will be explained based on the embodiment shown in FIG.
燃焼炉01には塊状固形物、粉状固形物を燃焼
炉01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
れている。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01内に導く輸送
手段05が連結されている。又、燃焼炉01は、
燃焼炉01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。 The combustion furnace 01 is equipped with a fuel supply device 02 that supplies lumpy solids and powdered solids into the combustion furnace 01, and a duct 03 provided at the exhaust gas outlet of the combustion furnace 01 has a duct 03 for capturing unburned solids. A collection device 04 is provided. A transportation means 05 that guides the unburned solids into the combustion furnace 01 is connected to the unburned solids outlet of the unburned solids collection device 04 . In addition, the combustion furnace 01 is
It communicates with a blower 06 for supplying combustion air to the combustion furnace 01.
燃焼炉01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
によつ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、灰は炉外へ排出し、
未燃固形物は再び輸送手段05を介して燃焼炉0
1内に供給され再燃焼する。 A lumpy solid is supplied into a combustion furnace 01 from a fuel supply device 02, and the solid is combusted by air supplied through a blower 06. The ash and unburned solids contained in the exhaust gas flowing through the duct 03 are separated by the unburnt solids collector 04, and the ash is discharged outside the furnace.
The unburned solids are transferred again to the combustion furnace 0 via the transportation means 05.
1 and re-burned.
従来の方法では、回収した未燃固形物を燃焼炉
01に戻しても、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つ
て塊状固形物のみの場合より燃焼しにくく送風機
06の動力を大きくする例があつた。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なわれている。また燃
料が燃えつきるまでには多数回にわたり、未燃固
形物補集装置04と燃焼炉01の間を循環する必
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 were returned to the combustion furnace 01, they were not completely burned and were carried out of the system as unburned substances, requiring time and effort for disposal. 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, only the lumpy solids are contained. There was an example in which the power of the blower 06 was increased to make combustion more difficult. Therefore, it is also practiced to separate the powdery solids in a pretreatment stage and then use only the lumpy solids as fuel. In addition, since the fuel needs to be circulated between the unburned solids collector 04 and the combustion furnace 01 many times before it is burned out, the capacity of the unburned solids collector 04 may be increased or the circulation system Measures were taken to prevent clogging and wear.
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
としてなされたものであり、本発明は、燃焼炉内
に固形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前
記燃焼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前記燃焼炉内に
供給して燃焼させるとともに、前記未燃焼固形物
を回収した後、前記粉状固形物と混合してペレツ
ト化し前記燃焼炉内へ供給して前記塊状固形物と
共に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。 SUMMARY OF THE INVENTION Therefore, the present invention has been made for the purpose of providing a method for burning solid substances efficiently and stably to burn solid fuel and unburned matter discharged from a combustion furnace. , a solid matter combustion method in which solid matter 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 combustion furnace and re-burned; Separating the solids into lumpy solids and powdery solids, supplying the lumpy solids into the combustion furnace and burning them, and collecting the unburned solids and mixing them with the powdery solids. The solid matter combustion method is characterized in that the solid matter is pelletized and then fed into the combustion furnace to be burned together with the agglomerated solid matter.
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レツト化して燃焼炉
内で燃焼させるので、未燃固形物が炉外へ未燃焼
のま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、機器の容量
アツプも不用で、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。 According to the method provided by the present invention, unburned solids and powdered solids in the exhaust gas are pelletized and burned in the combustion furnace, so that the unburned solids are not discharged outside the furnace unburned. As a result, combustion efficiency is high, combustion is stabilized due to the reduction of powdery solids, there is no need to increase the capacity of equipment, even if powdery solids are mixed in the fuel, it can be combusted efficiently, and the fuel is completely combusted. This eliminates the need for multiple circulations within the system, reduces clogging and abrasion problems within the system, and only ash is discharged as waste, simplifying disposal. Even if it contains, it can be used as a fuel and has the advantage of being able to use various fuels.
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前記燃焼炉内へ供給し
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
塊状固形物を前記燃焼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ツト化し、その後前記燃
焼炉内又は排ガスの熱で前記ペレツトを乾燥し前
記燃焼炉内へ供給して前記塊状固形物と共に燃焼
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、本発明方法によれば、さらに廃熱を利用
してペレツトを乾燥させるので、十分な強度のペ
レツトが得られ、循環系のトラブルがより減少す
るという利点がある。 Furthermore, the present invention provides solid combustion in which solids are supplied into a combustion furnace and combusted, and unburned solids in exhaust gas discharged outside the furnace are recovered and then supplied into the combustion furnace and re-burned. In the method, the solids are separated into lumpy solids and powdery solids, the lumpy solids are fed into the combustion furnace and burned, and after recovering the unburned solids, the powdery Provided is a solid matter combustion method, characterized in that the pellets are mixed with solid matter and pelletized, and then the pellets are dried in the combustion furnace or with the heat of exhaust gas, and the pellets are fed into the combustion furnace and burned together with the lumpy solid matter. According to the method of the present invention, waste heat is further used to dry the pellets, so that pellets with sufficient strength can be obtained, and problems 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明する。 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1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
物補集装置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
ツト製造装置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ツ
ト化製造装置7に導く輸送手段10が設けられて
いる。ペレツト化製造装置7には、ペレツトを燃
焼炉1内に導く輸送手段11が設けられている。
又、さらに燃焼炉1は、燃焼炉1内に燃焼用空気
を供給するための送風機6と連通している。な
お、ペレツト化製造装置7は、適当な水分で粉体
物をペレツ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. A transport means 5 for guiding the unburned solids into the pellet manufacturing apparatus 7 is provided at the unburned solids discharge port of the unburned solids collection device 4. The classifier 8 that separates the solids into lumpy solids and powdered solids is provided with a transportation means 9 that guides the lumpy solids from the lumpy solids outlet to the fuel supply device 2. A transport means 10 is provided for guiding the powdery solids to the pelletizing production device 7. The pelletizing production apparatus 7 is provided with a transport means 11 for guiding the pellets into the combustion furnace 1.
Further, 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 for pelletizing the powdered material with appropriate moisture.
固形物燃料中の塊状固形物は、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1へ
供給する。一方粉状固形物は輸送手段10を介し
てペレツト化製造装置7へ送られる。燃焼炉1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、輸送手段5によりペレツト製造装
置7へ送られる。 The lumpy solids in the solid fuel are separated from powder solids by a classifier 8 and sent to a fuel supply device 2 via a transportation means 9, and then supplied to a combustion furnace 1 by the fuel supply device 2. On the other hand, the powdered solid material is sent to the pelletizing production device 7 via the transportation means 10. Unburned solids in the exhaust gas from the combustion furnace 1 are collected by an unburnt solids collector 4 and sent to a pellet manufacturing device 7 by a transportation means 5.
ペレツト製造装置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ツト化し、ペ
レツトは、輸送手段11により燃焼炉1に送ら
れ、燃焼炉内でペレツ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
分のみでペレツトにして燃焼炉1内で燃焼させる
ので、ペレツト化に高い費用を要せず未燃固形物
が燃焼炉1外へ未燃焼のまま排失されないので燃
焼交率が良く、粉状固形物の減少に伴ない燃焼が
安定化し、機器の容量アツ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、系内の多数回の循間が不
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り、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 manufacturing device 7, unburnt solids and powder solids are mixed with appropriate moisture and pelletized. The pellets are sent to the combustion furnace 1 by means of transportation 11, and are pelletized in the combustion furnace. Burn.
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 the combustion furnace 1, so pelletizing requires high costs. Since the unburned solids are not discharged unburned outside the combustion furnace 1, the combustion exchange rate is good, the combustion is stabilized as the powdery solids are reduced, and there is no need to increase the capacity of equipment, and there is no need to increase the capacity of the equipment. Even if powdery solids are mixed in, it can be efficiently combusted, and the fuel is completely combusted, eliminating the need for multiple circulations in the system, reducing clogging and abrasion problems in the system, and leaving only ash as waste. 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
ツト化製造装置7にダクト3を流れる排ガスの1
部を導入し、排ガスの熱でペレツトを乾燥させる
ペレツト乾燥装置12を設けたもので、その他は
第1の実施態様例の装置と同じであり、ここでは
構造の説明は省略する。 The apparatus of the present embodiment is configured such that one part of the exhaust gas flowing through the duct 3 is supplied to the pelletizing production apparatus 7 of the apparatus of the first embodiment.
The apparatus is equipped with a pellet drying apparatus 12 for drying the pellets using the heat of exhaust gas.
固形状の燃料中の塊状固形物は分級器8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ツト製造装置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、ペレツト製造
装置7へ送られる。ペレツト製造装置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ツト化する。このペレツト
は、排ガスの余熱を利用したペレツト乾燥装置1
2で十分な強度まで固化し、ペレツト燃料として
燃焼炉1へ送られて、そこで燃焼する。 The lumpy solids in the solid fuel are separated from powdery solids by a classifier 8, and are supplied to the combustion furnace 1 by a fuel supply device 2. On the other hand, the powdered solids are sent to the pellet manufacturing device 7. Unburnt solids contained in combustion exhaust gas are
The solids are separated by the unburned solids collector 4 and sent to the pellet manufacturing device 7. Since a large amount of combustion ash is mixed into the unburned solids sent to the pellet manufacturing device 7, it can be easily pelletized as long as there is an appropriate amount of moisture without mixing a special binder. These pellets are dried in a pellet drying device 1 that uses residual heat from exhaust gas.
2, it is solidified to sufficient strength and sent as pellet fuel to the combustion furnace 1, where it is burned.
従つて本例によれば、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ペレツトが製作で
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 losses and save labor in waste treatment, stabilize combustion due to the reduction of powdery solids, and use the residual heat of exhaust gas, making it possible to The device can produce pellets with sufficient strength, reducing problems with the circulation system.
さらに次に、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, 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
るペレツト乾燥装置12を燃焼炉1内に配置し、
ペレツト化製造7とペレツト乾燥装置12とを輸
送手段11で連結し、ペレツト化製造装置7から
送られてきたペレツトをペレツト乾燥装置12内
で、燃焼炉1内の熱を利用して乾燥し、乾燥後の
ペレツ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. 3 is placed inside the combustion furnace 1,
The pelletizing production device 7 and the pellet drying device 12 are connected by a transportation means 11, and the pellets sent from the pelletizing production device 7 are dried in the pellet drying device 12 using the heat in the combustion furnace 1. The dried pellets are fed to the combustion bed at the bottom of the furnace, such as a stoker.
本例の作用効果については、第2の実施態様例
とほぼ同一の作用効果を奏するので、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.
第1図は従来の固形物燃焼方法を実施する装置
のフローチヤート図、第2図ないし第4図は夫々
は本発明の第1ないし第3の実施の態様例のフロ
ーチヤート図である。
01,1……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……ペレツト化製造装置、8……
分級器、12……ペレツト乾燥装置。
FIG. 1 is a flowchart of an apparatus for carrying out a conventional solid matter combustion method, and FIGS. 2 to 4 are flowcharts of first to third embodiments of the present invention, respectively. 01,1... Combustion furnace, 02,2... Fuel supply device, 04,4... Unburnt solids collection device, 06,6
...Blower, 7...Pelletization manufacturing equipment, 8...
Classifier, 12... pellet drying device.
Claims (1)
もに、炉外に排出される排ガス中の未燃固形物を
回収した後前記燃焼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前
記燃焼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
てペレツト化し前記燃焼炉内へ供給して前記塊状
固形物と共に燃焼させることを特徴とする固形物
燃焼方法。 2 燃焼炉内に固形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
回収した後前記燃焼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
前記燃焼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
してペレツト化し、その後前記燃焼炉内又は排ガ
スの熱で前記ペレツトを乾燥し前記燃焼炉内へ供
給して前記塊状固形物と共に燃焼させることを特
徴とする固形物燃焼方法。[Scope of Claims] 1. Solids are supplied into a combustion furnace and burned, and after recovering unburned solids from exhaust gas discharged outside the furnace, solids are supplied into the combustion furnace and re-burned. In the solid matter combustion method, the solid matter is separated into lumpy solid matter and powdery solid matter, and the lumpy solid matter is fed into the combustion furnace and burned, and the unburned solid matter is recovered, and then the powdery solid matter is collected. A solid matter combustion method, which comprises mixing the pellets with solid matter, supplying the pellets to the combustion furnace, and burning the pellets together with the lumpy solid matter. 2. A solid matter combustion method in which solid matter 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 combustion furnace and re-burned. Separating the solids into lumpy solids and powdery solids, feeding the lumpy solids into the combustion furnace and burning them, and collecting the unburned solids and mixing them with the powdery solids. A solid matter combustion method comprising: pelletizing the pellets, then drying the pellets in the combustion furnace or using the heat of exhaust gas, and supplying the pellets to the combustion furnace where they are combusted together with the lumpy solids.
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 JPS582507A (en) | 1983-01-08 |
JPS6246763B2 true 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) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH055637Y2 (en) * | 1990-11-09 | 1993-02-15 |
-
1981
- 1981-06-30 JP JP10173681A patent/JPS582507A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS582507A (en) | 1983-01-08 |
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