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JPS5914684B2 - Powdered fuel combustion equipment - Google Patents
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JPS5914684B2 - Powdered fuel combustion equipment - Google Patents

Powdered fuel combustion equipment

Info

Publication number
JPS5914684B2
JPS5914684B2 JP11435880A JP11435880A JPS5914684B2 JP S5914684 B2 JPS5914684 B2 JP S5914684B2 JP 11435880 A JP11435880 A JP 11435880A JP 11435880 A JP11435880 A JP 11435880A JP S5914684 B2 JPS5914684 B2 JP S5914684B2
Authority
JP
Japan
Prior art keywords
fuel
combustion
primary
powdered
powdered fuel
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
Application number
JP11435880A
Other languages
Japanese (ja)
Other versions
JPS5737606A (en
Inventor
善利 関口
昇 沖上
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.)
Kanadevia Corp
Original Assignee
Hitachi Shipbuilding and Engineering Co 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 Hitachi Shipbuilding and Engineering Co Ltd filed Critical Hitachi Shipbuilding and Engineering Co Ltd
Priority to JP11435880A priority Critical patent/JPS5914684B2/en
Publication of JPS5737606A publication Critical patent/JPS5737606A/en
Publication of JPS5914684B2 publication Critical patent/JPS5914684B2/en
Expired legal-status Critical Current

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  • Combustion Of Fluid Fuel (AREA)

Description

【発明の詳細な説明】 本発明は粉体燃料燃焼装置に関する。[Detailed description of the invention] The present invention relates to a powdered fuel combustion device.

微粉炭等粉砕した固体燃料を燃料に使用するボイラー、
ガロ熱炉等の燃焼装置においては、通常固体燃料中にか
なりのN分が含まれ、燃焼によって発生する窒素酸化物
の濃度は非常に高く、かつ水噴射、排ガス再循環法、燃
料濃淡燃焼法、空気2段燃焼法等でその発生を効果的に
抑制することは困難であり、現在環も有効な燃焼法は3
段燃焼法である。
Boilers that use pulverized solid fuel such as pulverized coal as fuel;
In combustion equipment such as garrothermal furnaces, the solid fuel usually contains a considerable amount of N, and the concentration of nitrogen oxides generated by combustion is extremely high. However, it is difficult to effectively suppress its occurrence using air two-stage combustion methods, etc., and currently there are three effective combustion methods.
This is a staged combustion method.

これは1次燃料と1次空気で低空気比の1次燃焼を行な
わせ、その周辺から2次燃料のみを1次燃焼排ガス中に
残在する酸素を消費するに必要な量より過剰に供給して
2次燃焼域が還元性雰囲気となるようになし、この領域
で1次燃焼域で発生したNOxをN2 に還元させた後
、さらにその外周部又は後流から2次空気を供給して3
次燃焼域を形成し、ここでCO2C02H20等の還元
性物質を完全に無公害のCO2,C20にする燃焼方法
である。
This allows primary combustion to occur at a low air ratio using primary fuel and primary air, and supplies only secondary fuel from the surrounding area in excess of the amount required to consume the oxygen remaining in the primary combustion exhaust gas. After the NOx generated in the primary combustion area is reduced to N2 in this area, secondary air is supplied from the outer periphery or downstream of the secondary combustion area. 3
This is a combustion method in which a secondary combustion zone is formed, where reducing substances such as CO2C02H20 are converted into completely pollution-free CO2 and C20.

この際、燃料が粉体、特にその粒径が粗い場合は、供給
された2次燃料の分解ガス化が急速に行なわれず、かつ
その濃度も均一にならないため、NOxの還元が効果的
に行なわれない。
At this time, if the fuel is powder, especially if its particle size is coarse, the supplied secondary fuel will not be decomposed and gasified rapidly and its concentration will not be uniform, making it difficult to effectively reduce NOx. Not possible.

まだ未燃カーボンも残り易く、燃焼効率の低下が起るな
どの問題があった。
There was a problem that unburned carbon still remained easily, resulting in a decrease in combustion efficiency.

本発明はこれらの欠点を解消したもので、固体燃料にお
いても液体燃料と同様に燃焼効率を低下させることなく
大巾なNOx抑制を可能にした粉体燃料燃焼装置を提供
するものである。
The present invention eliminates these drawbacks and provides a powdered fuel combustion device that can significantly suppress NOx even when using solid fuel without reducing the combustion efficiency in the same way as when using liquid fuel.

以下本発明の一実施例を図面に基づいて説明する。An embodiment of the present invention will be described below based on the drawings.

第1図において、1は燃焼炉、2は炉壁に設けられた1
次燃料ノズル、3は該1次燃料ノズル2の周囲から1次
空気aを供給する1次空気口、4は1次燃焼域に後流か
ら2次燃料dを供給して2次燃焼域を形成する2次燃料
ノズル、5は2次燃焼域に後流から2次空気すを供給し
て3次燃焼域を形成する2次空気口である。
In Fig. 1, 1 is a combustion furnace, and 2 is a 1 installed on the furnace wall.
A primary fuel nozzle, 3 is a primary air port that supplies primary air a from around the primary fuel nozzle 2, and 4 is a primary combustion area that supplies secondary fuel d from the wake to the secondary combustion area. The secondary fuel nozzle 5 formed is a secondary air port that supplies secondary air from the wake to the secondary combustion area to form a tertiary combustion area.

6は粗粒ホッパーで、固体燃料の粗粒がブロワ−7を通
して1次燃料Cとして1次燃料ノズル2に供給される。
Reference numeral 6 denotes a coarse particle hopper, through which coarse particles of solid fuel are supplied as primary fuel C to the primary fuel nozzle 2 through a blower 7.

8は細粒ホッパーで、固体燃料の細粒がブロワ−9を通
して2次燃料dとして2次燃料ノズル4に供給される。
Reference numeral 8 denotes a fine grain hopper, through which solid fuel fine grains are supplied to the secondary fuel nozzle 4 as secondary fuel d through a blower 9.

次にその動作について説明する。Next, its operation will be explained.

固体燃料としては例えば平均粒径80μmのものを用い
、これを例えば分級点60μmで分割し、分級点以下の
ものを細粒固体燃料として細粒ホッパー8に貯留し、分
級点を越えるものを粗粒固体燃料として粗粒ホッパー6
に貯留し、それぞれの供給量が50%となるようにブロ
ワ−9および7を介して2次燃料ノズル4および1次燃
料ノズル2に送り、燃焼条件として燃焼量を300kg
/h、に維持した。
For example, solid fuel with an average particle diameter of 80 μm is used, and this is divided at a classification point of 60 μm, and those below the classification point are stored in the fine hopper 8 as fine solid fuel, and those exceeding the classification point are coarsely divided. Coarse hopper 6 as granular solid fuel
The fuel is stored in the tank and sent to the secondary fuel nozzle 4 and the primary fuel nozzle 2 via blowers 9 and 7 so that each supply amount is 50%, and the combustion condition is that the combustion amount is 300 kg.
/h.

また1次空気としては、全燃料を燃焼するに必要な空気
量の0.3倍を供給した。
Further, as primary air, 0.3 times the amount of air required to burn all the fuel was supplied.

燃焼はまず粗粒の1次燃料と1次空気で低空気比の1次
燃焼を行なわせ、その後流から細粒の2次燃料を1次燃
焼排ガス中に残存する酸素を消費するに必要な量より過
剰な状態になるように供給して2次燃焼域を還元性雰囲
気となし、1次燃焼域で発生したNOxをこの2次燃焼
域でN2に還元させた後、さらにその後流から2次空気
を供給して3次燃焼域を形成し、ここで還元性物質を完
全に無公害の物質に燃焼させた。
Combustion begins with primary combustion of coarse-grained primary fuel and primary air at a low air ratio, followed by fine-grained secondary fuel that is necessary to consume the oxygen remaining in the primary combustion exhaust gas. After the NOx generated in the primary combustion zone is reduced to N2 in the secondary combustion zone, NOx is supplied in excess of the amount to create a reducing atmosphere in the secondary combustion zone. Secondary air was supplied to form a tertiary combustion zone, where the reducing substances were combusted into completely non-polluting substances.

この場合、2次燃料は細粒であるだめ、2次燃料の分解
ガス化が急速に行なわれ、その濃度も均一になり、NO
xの還元が効果的に行なわれた。
In this case, since the secondary fuel is fine particles, the secondary fuel is rapidly decomposed and gasified, its concentration becomes uniform, and NO
The reduction of x was effectively carried out.

すなわち第1表に示すように、固体燃料が分級されなか
った場合、NOxは180ppmであったのに対し、上
記のように分級した場合は150ppmに低下し、窒素
酸化物の濃度は小さくなった。
In other words, as shown in Table 1, when the solid fuel was not classified, NOx was 180 ppm, but when it was classified as described above, it decreased to 150 ppm, and the concentration of nitrogen oxides became small. .

第2図は別の実施例を示す。FIG. 2 shows another embodiment.

10は燃料ホッパーで、例えば平均粒径80μmの全固
体燃料が貯留され、ブロワ−11を介して分級機12に
送られ、ここで例えば分級点60μmを境にして分割さ
れ、細粒は2次燃料として2次燃料ノズル4へ、組粒は
1次燃料として1次燃料ノズル2へ供給される。
Reference numeral 10 denotes a fuel hopper, in which all solid fuel with an average particle size of 80 μm, for example, is stored and sent via a blower 11 to a classifier 12, where it is divided at, for example, a classification point of 60 μm, and fine particles are separated into secondary particles. The aggregate particles are supplied to the secondary fuel nozzle 4 as fuel, and the aggregate particles are supplied to the primary fuel nozzle 2 as primary fuel.

以上本発明によれば、供給される2次燃料の分解ガス化
が急速に行なわれ、かつその濃度も均一になり、NOx
の還元が効果的に行なわれて窒素酸化物の濃度を低減さ
せることができるとともに、燃焼効率も向上できる利点
を有し、工業的価値は極めて高い。
As described above, according to the present invention, the supplied secondary fuel is rapidly decomposed and gasified, and its concentration becomes uniform, resulting in NOx
It has the advantage of being able to effectively reduce the concentration of nitrogen oxides and improve combustion efficiency, and has extremely high industrial value.

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

第1図は本発明の一実施例を示す全体構成図、第2図は
別の実施例を示す要部構成図である。 2・・・1次燃料ノズル、3・・・1次空気口、4・・
・2次燃料ノズル、5・・・2次空気口、6・・・粗粒
ホッパー、8・・・細粒ホッパー、12・・・分級機。
FIG. 1 is an overall block diagram showing one embodiment of the present invention, and FIG. 2 is a main part block diagram showing another embodiment. 2...Primary fuel nozzle, 3...Primary air port, 4...
-Secondary fuel nozzle, 5...Secondary air port, 6...Coarse grain hopper, 8...Fine grain hopper, 12...Classifier.

Claims (1)

【特許請求の範囲】 1 粉体燃料を1次および2次燃料に分割供給し、燃焼
用空気を1次および2次空気に分割供給して3段燃焼を
行なう粉体燃料燃焼装置において粉体燃料を分級し、微
細粒径のものを2次燃料に、粗粒径のものを1次燃料に
使用するようにしたことを特徴とする粉体燃料燃焼装置
。 2 粉体燃料供給配管途中に設けた分級機により粉体燃
料を分割供給することを特徴とする特許請求の範囲第1
項記載の粉体燃料燃焼装置。
[Claims] 1. In a powdered fuel combustion device that performs three-stage combustion by supplying powdered fuel dividedly into primary and secondary fuel and dividingly supplying combustion air into primary and secondary air, A pulverized fuel combustion device characterized in that fuel is classified so that fine particle size fuel is used as secondary fuel and coarse particle size fuel is used as primary fuel. 2. Claim 1 characterized in that the powdered fuel is dividedly supplied by a classifier installed in the middle of the powdered fuel supply pipe.
Powdered fuel combustion device as described in section.
JP11435880A 1980-08-19 1980-08-19 Powdered fuel combustion equipment Expired JPS5914684B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11435880A JPS5914684B2 (en) 1980-08-19 1980-08-19 Powdered fuel combustion equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11435880A JPS5914684B2 (en) 1980-08-19 1980-08-19 Powdered fuel combustion equipment

Publications (2)

Publication Number Publication Date
JPS5737606A JPS5737606A (en) 1982-03-02
JPS5914684B2 true JPS5914684B2 (en) 1984-04-05

Family

ID=14635719

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11435880A Expired JPS5914684B2 (en) 1980-08-19 1980-08-19 Powdered fuel combustion equipment

Country Status (1)

Country Link
JP (1) JPS5914684B2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5837408A (en) * 1981-08-28 1983-03-04 Kawasaki Heavy Ind Ltd Pulverized coal combustion method
JPS5949409A (en) * 1982-09-11 1984-03-22 Babcock Hitachi Kk Boiler device
JPS5974409A (en) * 1982-10-22 1984-04-26 Babcock Hitachi Kk Powdered coal combustion device
JPS602119U (en) * 1983-06-15 1985-01-09 バブコツク日立株式会社 Pulverized coal mixed coal/mixed combustion combustion equipment
JPS60174409A (en) * 1984-02-20 1985-09-07 Hitachi Zosen Corp Low ΝOx combustion method for pulverized coal
JPS60185004A (en) * 1984-02-29 1985-09-20 Hitachi Zosen Corp Three-stage combustion device
JPS60233403A (en) * 1984-05-07 1985-11-20 Hitachi Zosen Corp Three-stage combustion device
JPS60245907A (en) * 1984-05-21 1985-12-05 Hitachi Zosen Corp Three-stage burner
DE60238470D1 (en) 2001-02-27 2011-01-13 Yantai Longyuan Power Tech Co PLASMA IGNITOR WITH COMPOSITE CATHODE

Also Published As

Publication number Publication date
JPS5737606A (en) 1982-03-02

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