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JPH0615926B2 - Method for reburning combustion ash containing unburned matter - Google Patents
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JPH0615926B2 - Method for reburning combustion ash containing unburned matter - Google Patents

Method for reburning combustion ash containing unburned matter

Info

Publication number
JPH0615926B2
JPH0615926B2 JP61082332A JP8233286A JPH0615926B2 JP H0615926 B2 JPH0615926 B2 JP H0615926B2 JP 61082332 A JP61082332 A JP 61082332A JP 8233286 A JP8233286 A JP 8233286A JP H0615926 B2 JPH0615926 B2 JP H0615926B2
Authority
JP
Japan
Prior art keywords
ash
combustion
fuel
fine powder
collected
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
JP61082332A
Other languages
Japanese (ja)
Other versions
JPS62238917A (en
Inventor
有彦 空田
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 JP61082332A priority Critical patent/JPH0615926B2/en
Publication of JPS62238917A publication Critical patent/JPS62238917A/en
Publication of JPH0615926B2 publication Critical patent/JPH0615926B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 産業上の利用分野 本発明は、石炭、石油コークス等の固体燃料を使用する
ボイラに於ける未燃分の抑制による燃焼効率向上のため
の未燃分を含む燃焼灰の再燃焼方法に関するものであ
る。
TECHNICAL FIELD The present invention relates to combustion ash containing unburned matter for improving combustion efficiency by suppressing unburned matter in a boiler using a solid fuel such as coal and petroleum coke. The present invention relates to a method of reburning.

従来の技術 近時、石油の供給不安定、値上がり等により石油代替燃
料として、石炭、石油コークス等の固体燃料が多く使用
されるようになって来た。
2. Description of the Related Art Recently, solid fuels such as coal and petroleum coke have been widely used as alternative fuels to petroleum due to unstable supply of petroleum and rising prices.

しかし、石炭、石油コークスは重油などの液体燃料と比
べて揮発分がすくないため燃焼性が悪く、ボイラ燃料と
してその多くは微粉砕して使用される。それでも未燃分
は数%〜十数%に達するため、燃焼効率が低下する。
However, coal and petroleum coke have less volatile components than liquid fuels such as heavy oil and thus have poor combustibility, and most of them are finely pulverized and used as boiler fuel. Even so, the unburned content reaches several percent to several tens of percent, so that the combustion efficiency decreases.

これを防止するため、従来もホッパ等で捕集する灰を炉
内へ回収する方法が採られていたが、その回収熱量は僅
かであった。
In order to prevent this, a method of collecting ash collected in a hopper or the like into the furnace has been conventionally used, but the amount of recovered heat was small.

すなわち、第2図は、従来の未燃分を含む燃焼灰の再燃
焼方法を採用しているボイラの系統図であり、1は火
炉、2は燃料供給口、3はアッシュホッパ、4はストー
カ、5は節炭器、6なホッパ、7は通風機、8は電気集
塵器、9は誘引通風機、10は煙突である。
That is, FIG. 2 is a system diagram of a boiler that employs a conventional method for reburning combustion ash containing unburned matter, where 1 is a furnace, 2 is a fuel supply port, 3 is an ash hopper, and 4 is a stoker. 5 is a economizer, 6 is a hopper, 7 is a fan, 8 is an electric dust collector, 9 is a draft fan, and 10 is a chimney.

このような系統のボイラにおいて、従来は、燃料供給口
2から供給された燃料が火炉1で燃焼し、発生した燃料
ガスは、火炉1内を上方に流れ、過熱器(図示せず)や
節炭器5部分に順次流入し、蒸気・水等との熱交換を行
った後電気集塵器8で除塵され、誘引通風機9を経て煙
突10から大気中へ放出されていた。
In the boiler of such a system, conventionally, the fuel supplied from the fuel supply port 2 is burned in the furnace 1, and the generated fuel gas flows upward in the furnace 1 to generate a superheater (not shown) or a node. It successively flowed into the charcoal vessel 5 part, where it exchanged heat with steam, water, etc., and was then dust-removed by the electrostatic precipitator 8 and was discharged from the chimney 10 into the atmosphere via the induced draft fan 9.

そして、ホッパ6で捕集された灰は、通風機7から空気
輸送管11を介して送られてくる空気流によって火炉1
内へ吹き込まれて、再度燃焼に供されていた。尚、電気
集塵器8で捕集された灰は、系外へ排出して捨てられて
いた。
Then, the ash collected by the hopper 6 is supplied to the furnace 1 by the air flow sent from the fan 7 via the air transport pipe 11.
It was blown into the interior and was burned again. The ash collected by the electrostatic precipitator 8 was discharged to the outside of the system and discarded.

発明が解決しようとする問題点 上記のホッパ6から回収される灰の量は、全体の5%程
度であり、この中に含まれる未燃分の回収熱量は全体の
約0.2%程度にしかならない。従って、大部分の未燃
分は単に捨てられているだけであった。
Problems to be Solved by the Invention The amount of ash recovered from the hopper 6 is about 5% of the total amount, and the amount of unburned heat contained in the ash is about 0.2% of the total amount. It only happens. Therefore, most of the unburned matter was simply discarded.

灰分の少い固体燃料を燃焼させる場合、集塵器で捕集す
る灰の発熱量は未だ数千Kcal/Kgを有するものがあり、
これを回収せずに捨てるのはエネルギー的にもロスであ
る。
When burning solid fuel with low ash content, the heat value of the ash collected by the dust collector may still be several thousand Kcal / Kg.
It is an energy loss to discard this without collecting it.

又、未燃分が多いと多量の捕集灰量となるため、これの
処理に要する費用が公害面の関係もあり多大となる。
In addition, since a large amount of unburned ash results in a large amount of collected ash, the cost required for the treatment of the collected ash is large due to pollution.

これらは固体燃料使用の場合の一番のデメリットであ
る。
These are the biggest disadvantages when using solid fuel.

問題点を解決するための手段 本発明は、上記の問題点を解決するために、固体燃料を
粉砕して微粉にしたものを火炉へ供給して燃焼させる燃
焼装置において、燃焼排ガス中の燃焼灰を集塵し、その
燃焼灰の一部を前記微粉に混入し、前記燃焼灰中に含ま
れるFe,Mg系元素の触媒作用を利用して前記微粉の燃焼
促進を計ると共に、燃焼灰を再燃焼させるようにしたも
のである。
Means for Solving the Problems In order to solve the above problems, the present invention relates to a combustion apparatus in which solid fuel is pulverized into fine powder and is supplied to a furnace for combustion, and combustion ash in combustion exhaust gas is used. Is collected, and a part of the combustion ash is mixed with the fine powder, and the combustion promotion of the fine powder is measured by utilizing the catalytic action of Fe and Mg-based elements contained in the combustion ash and regenerating the combustion ash. It is designed to burn.

作用 微粉燃料を燃焼させる場合、その燃焼排ガス中に含まれ
る未燃分は、固体燃料の固定炭素の燃焼時間が不足して
発生するもので、また、捕集される灰の粒度は、燃料の
粒度とほゞ同じ位である。従って燃料排ガス中の灰を捕
集して微粉燃料に混入して再燃焼させると、燃焼時間が
多くとれるために、未燃分が減じ、かつ灰に含まれてい
るFe,Mg系元素が燃焼促進剤として作用するので、燃料
の燃焼効果が活性化し、未燃分を大幅に減じてエネルギ
のロスを最小限におさえることができる。
Action When combusting pulverized fuel, the unburned matter contained in the combustion exhaust gas is generated due to insufficient combustion time of the fixed carbon of the solid fuel, and the particle size of the collected ash depends on the fuel. It is about the same as the grain size. Therefore, when the ash in the fuel exhaust gas is collected, mixed with the fine powder fuel and re-burned, the unburned content is reduced because the combustion time is long and the Fe and Mg-based elements contained in the ash are burned. Acting as a promoter, the combustion effect of the fuel is activated, the unburned content is greatly reduced, and the energy loss can be minimized.

実施例 以下本発明の一実施例を第1図を参照して詳細に説明す
る。なお、第1図において、第2図と同一部分には同一
符号を附してあるので、その部分の説明は省略する。
Embodiment One embodiment of the present invention will be described in detail below with reference to FIG. In FIG. 1, the same parts as those in FIG. 2 are designated by the same reference numerals, and the description thereof will be omitted.

第1図において、12は燃料ホッパ、13は石炭、コー
クス等の固体燃料を粉砕して微粉化するミル、14は微
粉粉管、15はバグフィルタ、16はビン、17は混合
微粉管、18は灰輸送管、19はアッシュビン、20、2
1、22は夫々通風機である。
In FIG. 1, 12 is a fuel hopper, 13 is a mill for crushing solid fuel such as coal or coke into fine powder, 14 is a fine powder tube, 15 is a bag filter, 16 is a bottle, 17 is a mixed fine powder tube, 18 Is an ash transport pipe, 19 is an ash bottle, 20, 2
Reference numerals 1 and 22 are ventilation fans, respectively.

バーナ2から、ミル13で粉砕された微粉燃料が火炉1
へ投入されて燃焼させられる。そして、燃焼によって生
じた排ガスは電気集塵器8へ導入され、排ガス中の固形
分が集塵されて、固形分の除かれた排ガスが、誘引通風
機9を経て煙突10から大気中へ排出される。
Fine fuel pulverized by the mill 13 from the burner 2 is the furnace 1
It is thrown in and burned. Then, the exhaust gas generated by the combustion is introduced into the electrostatic precipitator 8, the solid content in the exhaust gas is collected, and the exhaust gas from which the solid content is removed is discharged from the chimney 10 to the atmosphere via the induced draft fan 9. To be done.

一方、電気集塵器8で集められた固形分は、未燃分を含
む灰であり、微粉燃料と同程度の粒度のものである。そ
こで、この灰を通風機22により、灰輸送管18を通し
て微粉管14へ合流させ、ミル13から送られて来る微
粉燃料と混合する。この灰と微粉燃料の混合粉体はバグ
フィルタ15出口の通風機21で吸引され、ビン16に
貯えられる。そして、ビン16に貯えられた灰と微粉燃
料の混合粉体は、1次通風機20で押し出され、混合微
粉管17を通してバーナ2へ供給されて燃焼に供され
る。
On the other hand, the solid content collected by the electrostatic precipitator 8 is ash containing unburned content, and has a particle size similar to that of the pulverized fuel. Then, this ash is merged with the fine powder pipe 14 through the ash transport pipe 18 by the blower 22 and mixed with the fine powder fuel sent from the mill 13. The mixed powder of ash and fine fuel is sucked by the fan 21 at the outlet of the bag filter 15 and stored in the bottle 16. Then, the mixed powder of ash and fine fuel stored in the bottle 16 is extruded by the primary air blower 20 and supplied to the burner 2 through the mixed fine powder tube 17 for combustion.

なお、微粉燃料に混合させる灰の量は、電気集塵器8で
捕集した灰の全部又は一部であってよく、そのため、灰
をアッシュビン19へブリードさせることができるよう
になっている。また、電気集塵器8で捕集された灰の全
量を循環させると、ボイラ1内の灰量が漸次増加するこ
とになるので、これを防止するためにも間欠的にブリー
ドすることが好ましく、連続的に混合する場合には20
%程度の灰をアッシュビン19へブリードさせるのが好
ましい。
The amount of ash to be mixed with the pulverized fuel may be all or part of the ash collected by the electrostatic precipitator 8, so that the ash can be made to bleed into the ash bin 19. . Further, if the entire amount of ash collected by the electrostatic precipitator 8 is circulated, the amount of ash in the boiler 1 will gradually increase, so it is preferable to intermittently bleed in order to prevent this. , 20 for continuous mixing
% Ash is preferably allowed to bleed into the ash bin 19.

発明の効果 以上詳述したように、本発明によれば、固体燃料を粉砕
して微粉したものを火炉へ供給して燃焼させる燃焼装置
において、燃焼排ガス中の燃焼灰を集塵し、その燃焼灰
の一部を前記微分に混入し、前記燃焼灰中に含まれるF
e,Mg系元素の触媒作用を利用して前記微粉の燃焼促進
を計ると共に、燃焼灰を再燃焼させるようにしたので、
未燃分の大幅に減少させ、燃焼効率の向上に大きく寄与
することができる。電気集塵器では99%の灰の捕集が
可能であり、上流のホッパに溜る5%程度の量の灰を差
引いても90%以上の灰を捕集して再燃焼させるので、
回収熱量が大幅に向上することがわかる。また、電気集
塵器から取り出す灰の量も減少することとなり、その灰
の処理やそれにかかる費用も軽減させるという効率も得
られる。
Effects of the Invention As described in detail above, according to the present invention, in a combustion device that pulverizes and pulverizes solid fuel and supplies it to a furnace for combustion, the combustion ash in the flue gas is collected and burned. Part of the ash is mixed with the derivative, and F contained in the combustion ash
Since the combustion of the fine powder was promoted and the combustion ash was recombusted by utilizing the catalytic action of e and Mg-based elements,
It is possible to greatly reduce the unburned content and greatly contribute to the improvement of combustion efficiency. The electric dust collector can collect 99% of ash, and even if you subtract 5% of ash accumulated in the upstream hopper, 90% or more of ash is collected and reburned.
It can be seen that the amount of heat recovered is greatly improved. In addition, the amount of ash taken out from the electrostatic precipitator will be reduced, and the efficiency of processing the ash and reducing the cost thereof can be obtained.

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

第1図は本発明を実施するボイラの一例を示す系統図、
第2図は従来の燃焼灰の再燃焼方法を実施するボイラの
系統図である。 1……火炉、2……バーナ、8……電気集塵器、13…
…ミル、14……微粉管、17……混合微粉管、18…
…灰輸送管、19……アッシュビン。
FIG. 1 is a system diagram showing an example of a boiler for carrying out the present invention,
FIG. 2 is a system diagram of a boiler that implements a conventional method for reburning combustion ash. 1 ... Furnace, 2 ... Burner, 8 ... Electrostatic precipitator, 13 ...
… Mill, 14… Fine powder tube, 17… Mixed fine powder tube, 18…
… Ash transport tube, 19… Ash bin.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】固体燃料を粉砕して微粉にしたものを火炉
へ供給して燃焼させる燃焼装置において、燃焼排ガス中
の燃焼灰を集塵し、その燃焼灰の一部を前記微粉に混入
し、前記燃焼灰中に含まれるFe,Mg系元素の触媒作用を
利用して前記微粉の燃焼促進を計ると共に、燃焼灰を再
燃焼させるようにしたことを特徴とする、未燃分を含む
燃焼灰の再燃焼方法。
1. A combustor in which solid fuel is pulverized into fine powder and supplied to a furnace for combustion, and the combustion ash in combustion exhaust gas is collected, and a part of the combustion ash is mixed with the fine powder. Fe, Mg contained in the combustion ash, utilizing the catalytic action of the Mg-based elements to promote the combustion of the fine powder, the combustion ash is reburned, combustion containing unburned content, How to reburn ash.
JP61082332A 1986-04-11 1986-04-11 Method for reburning combustion ash containing unburned matter Expired - Fee Related JPH0615926B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61082332A JPH0615926B2 (en) 1986-04-11 1986-04-11 Method for reburning combustion ash containing unburned matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61082332A JPH0615926B2 (en) 1986-04-11 1986-04-11 Method for reburning combustion ash containing unburned matter

Publications (2)

Publication Number Publication Date
JPS62238917A JPS62238917A (en) 1987-10-19
JPH0615926B2 true JPH0615926B2 (en) 1994-03-02

Family

ID=13771604

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61082332A Expired - Fee Related JPH0615926B2 (en) 1986-04-11 1986-04-11 Method for reburning combustion ash containing unburned matter

Country Status (1)

Country Link
JP (1) JPH0615926B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS509617U (en) * 1973-05-23 1975-01-31
JPS5661515A (en) * 1979-10-23 1981-05-27 Babcock Hitachi Kk Treating device of uncombusted carbon
JPS6146806A (en) * 1984-08-11 1986-03-07 Kawasaki Heavy Ind Ltd Burning method of oil coke

Also Published As

Publication number Publication date
JPS62238917A (en) 1987-10-19

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