JPH09119606A - Blast furnace gas mixed firing coal fired boiler - Google Patents

Blast furnace gas mixed firing coal fired boiler

Info

Publication number
JPH09119606A
JPH09119606A JP27889195A JP27889195A JPH09119606A JP H09119606 A JPH09119606 A JP H09119606A JP 27889195 A JP27889195 A JP 27889195A JP 27889195 A JP27889195 A JP 27889195A JP H09119606 A JPH09119606 A JP H09119606A
Authority
JP
Japan
Prior art keywords
blast furnace
furnace gas
compartment
coal
pulverized coal
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
JP27889195A
Other languages
Japanese (ja)
Other versions
JP3073434B2 (en
Inventor
Yuzo Taguchi
雄三 田口
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 JP07278891A priority Critical patent/JP3073434B2/en
Publication of JPH09119606A publication Critical patent/JPH09119606A/en
Application granted granted Critical
Publication of JP3073434B2 publication Critical patent/JP3073434B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To improve a boiler efficiency, increase the safetiness of flue instruments and reduce the generating amount of NOx by a method wherein a blast furnace gas compartment is arranged between the thick mixture compartment of pulverized coal. and the thin mixture compartment of the same while respective compartments are provided with downward angles. SOLUTION: In a lower coal/blast furnace gas combination stage 13, an AUX compartment 18, charging auxiliary combustion air, a thin mixture compartment 17, low in the concentration of pulverized cloal, a blast furnace gas compartment 16 and a thick mixture compartment 15, high in the concentration of pulverized coal, are arranged sequentially from the lowr part. On the other hand, an arrangement in an upper coal/blast furnace gas combination stage 11 is reversed to the arrangement in the lowr stage. Respective compartments of the coal/blast furnace gas combination stages 11, 13 are installed so as to have downward angles to elongate the staying period of time of respective fuels and air in a furnace 2. According to this method, the generating amount of NOx can be restrained in a low degree.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、事業用・自家発発
電設備の高炉ガス混焼石炭(微粉炭)焚きボイラ、特に
その燃焼装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a blast furnace gas co-firing coal (pulverized coal) -fired boiler for a business / in-house power generation facility, and more particularly to a combustion device thereof.

【0002】[0002]

【従来の技術】従来、ボイラの燃料として高炉ガスを用
いる場合、重油や天然ガスと混焼するケースがほとんど
であったが、近年は高炉ガスと石炭(微粉炭燃焼)の混
焼ボイラも計画されるようになった。
2. Description of the Related Art Conventionally, when blast furnace gas was used as a fuel for a boiler, it was mostly co-firing with heavy oil or natural gas, but in recent years, a co-firing boiler of blast furnace gas and coal (pulverized coal combustion) is also planned. It became so.

【0003】従来の重油(あるいは天然ガス)と高炉ガ
スとの混焼においては、高炉ガスの主成分であるCOの
分解を効果的にするために、図3に示すように高炉ガス
用のコンパートメントは、バーナ風箱の最下部に配置さ
れるものが、ほとんどであった。
In the conventional co-firing of heavy oil (or natural gas) and blast furnace gas, in order to effectively decompose CO, which is the main component of the blast furnace gas, a compartment for the blast furnace gas is provided as shown in FIG. Most were placed at the bottom of the burner box.

【0004】一方、NOx 発生を抑制する石炭焚(微粉
炭燃焼)ボイラにおいては、図4に示すような配置とな
っている。すなわち、低NOx 化のために1つの石炭コ
ンパートメントが微粉炭濃度の高い濃混合気コンパート
メントと微粉炭濃度の低い淡混合気コンパートメントの
2つのブロックに分割され、更にその2つのブロックの
間には、濃混合気の燃焼火炎と淡混合気の火炎を分割す
るために、セパレートコンパートメントが設けられて、
高さの比較的高い風箱を構成していた。
On the other hand, a coal-fired (pulverized coal combustion) boiler which suppresses the generation of NO x is arranged as shown in FIG. That is, in order to reduce NO x , one coal compartment is divided into two blocks, a dense air-fuel mixture compartment with a high pulverized coal concentration and a light air-fuel mixture compartment with a low pulverized coal concentration, and between the two blocks. , A separate compartment is provided to divide the rich mixture combustion flame and the light mixture flame.
It consisted of a relatively tall wind box.

【0005】[0005]

【発明が解決しようとする課題】高炉ガスは火炎の燃焼
温度が低いので、燃焼の完結に必要な炉内滞留時間を長
くとらねばならない。ところが高炉ガスの場合、その燃
料の組成上、燃料の発熱量あたりの排ガス発生量が多い
ので炉内の空塔速度が速くなり、重油、天然ガス、石炭
等の専焼に比べて、炉内の滞留時間がかえって短くな
る。そのため高炉ガスと石炭(微粉炭)との混焼ボイラ
においては、炉内の滞留時間が短くなる分、灰中未然分
が増大し、ボイラ効率の点からも煙道機器(空気予熱
器、集塵器、脱硫装置、脱硝装置等)の安全性の点から
も問題が生じる。
Since the blast furnace gas has a low flame combustion temperature, the residence time in the furnace required for completion of combustion must be long. However, in the case of blast furnace gas, due to the composition of the fuel, the amount of exhaust gas generated per calorific value of the fuel is large, so the superficial velocity in the furnace becomes faster, and compared with the case of mono-fuel combustion of heavy oil, natural gas, coal, etc. The residence time is rather shortened. Therefore, in a mixed-fired boiler of blast furnace gas and coal (pulverized coal), the amount of ash in the ash increases as the residence time in the furnace shortens, and from the viewpoint of boiler efficiency, flue equipment (air preheater, dust collector) There is also a problem in terms of the safety of the reactor, desulfurization equipment, denitration equipment, etc.

【0006】すなわち、石炭(微粉炭)・高炉ガス混焼
ボイラにおいて、高炉ガスコンパートメントを最下段に
配置し、空気比1.0以上で完全燃焼させる場合、発熱
量あたりの発生ガス量が非常に多くなるので、上段の石
炭(微粉炭)燃焼部の空塔速度が速くなって微粉炭燃焼
自体を阻害し、その結果として火炉内で微粉炭の不燃物
つまり灰中未燃分が増大する。
That is, in a coal (pulverized coal) / blast furnace gas co-firing boiler, when the blast furnace gas compartment is arranged at the lowest stage and complete combustion is performed at an air ratio of 1.0 or more, the amount of gas generated per calorific value is very large. Therefore, the superficial velocity of the upper part of the coal (pulverized coal) combusting section is increased to inhibit the combustion of the pulverized coal itself, and as a result, the incombustible material of the pulverized coal, that is, the unburned matter in the ash is increased in the furnace.

【0007】この現象を抑制するための燃焼方法として
は、最下段の高炉ガスコンパートメント部の空気比を下
げ、火炉下部からのガスの巻き上げを抑制する方法をと
らざるを得ない。しかしながら、高炉ガス自体の自燃性
が他の燃料に比べて悪いので、大幅に空気比を下げるこ
とは失火抑止の観点から望ましくない。
As a combustion method for suppressing this phenomenon, it is unavoidable to reduce the air ratio in the lowermost blast furnace gas compartment to suppress the gas from being blown up from the lower part of the furnace. However, since the self-combustibility of blast furnace gas itself is worse than that of other fuels, it is not desirable to greatly reduce the air ratio from the viewpoint of suppressing misfire.

【0008】[0008]

【課題を解決するための手段】本発明者は、前記従来の
課題を解決するために、微粉炭と空気との混合気および
高炉ガスをボイラ火炉に投入して燃焼させる高炉ガス混
焼石炭焚きボイラにおいて、微粉炭濃度の高い濃混合気
を投入するコンパートメントと微粉炭濃度の低い淡混合
気を投入するコンパートメントとの間に高炉ガスを投入
するコンパートメントを配置するとともに、各コンパー
トメントを下向きに傾斜させたことを特徴とする高炉ガ
ス混焼石炭焚きボイラを提案するものである。
In order to solve the above-mentioned conventional problems, the present inventor has introduced a blast-furnace gas co-firing coal-fired boiler in which a mixture of pulverized coal and air and blast furnace gas are put into a boiler furnace and burned. In the above, a compartment for introducing blast furnace gas was placed between a compartment for introducing a rich mixture with a high pulverized coal concentration and a compartment for introducing a light mixture with a low pulverized coal concentration, and each compartment was inclined downward. This is to propose a blast furnace gas co-firing coal-fired boiler characterized by the above.

【0009】本発明によれば、従来の微粉炭焚きバーナ
において濃混合気コンパートメントと淡混合気コンパー
トメントの間に配置されていたセパレートコンパートメ
ントの部分に高炉ガスコンパートメントを設けたので、
以下の作用が生じる。
According to the present invention, the blast furnace gas compartment is provided in the part of the separate compartment which is disposed between the rich air-fuel mixture compartment and the light air-fuel mixture compartment in the conventional pulverized coal burning burner.
The following effects occur.

【0010】1) 従来最下段に配置されていた高炉ガ
スコンパートメントが、通常複数組設けられる微粉炭投
入コンパートメントのそれぞれに分割配置されるので、
バーナ下部からの排ガスの吹き上げが低減され、灰中未
燃分の発生が抑制される。
1) Since the blast furnace gas compartment, which was conventionally arranged at the bottom, is divided and arranged in each of the pulverized coal charging compartments, which are usually provided in plural sets,
The blowing up of exhaust gas from the lower part of the burner is reduced, and the generation of unburned matter in ash is suppressed.

【0011】2) 石炭(微粉炭)の火炎によって、本
来失火しやすい高炉ガスの保炎が確実に行なわれる。
2) The flame of coal (pulverized coal) reliably holds flame of blast furnace gas which is likely to misfire.

【0012】3) 石炭バーナ自体は濃混合気炎,淡混
合気を形成する低NOx バーナとなっており、NOx
発生が抑制される。
3) The coal burner itself is a low NO x burner that forms a rich air-fuel mixture and a light air-fuel mixture, and the generation of NO x is suppressed.

【0013】本発明ではまた、各コンパートメントを下
向きに傾斜させるので、火炎が下向きになり、炉内の滞
留時間が長くなる。
The present invention also tilts each compartment downward so that the flame is downward and the residence time in the furnace is long.

【0014】[0014]

【発明の実施の形態】図1は本発明の実施の一形態に係
る高炉ガス混焼石炭焚きボイラを示す縦断面図、図2は
図1中の主バーナ(1)の風箱配置を示す正面図および
一部側面図である。
1 is a vertical cross-sectional view showing a blast furnace gas co-firing coal-fired boiler according to an embodiment of the present invention, and FIG. 2 is a front view showing a wind box arrangement of a main burner (1) in FIG. It is a figure and a partial side view.

【0015】まず図1において、本実施形態の高炉ガス
混焼石炭焚きボイラは、火炉(2)の側面に主バーナ
(1)が、上部に過熱器(3)や再熱器(4)等が、そ
れぞれ配置されていて、後部煙道(7)内に節炭器等の
熱交換器(5)が設置されている。主バーナ(1)で投
入された燃料は火炉(2)内で燃焼し、排ガスとなって
後部煙道(7)および排ガスダクト(6)を経て外部へ
放出される。
First, referring to FIG. 1, in the blast furnace gas co-firing coal-fired boiler of this embodiment, a main burner (1) is provided on a side surface of a furnace (2), and a superheater (3), a reheater (4), etc. are provided at an upper portion. A heat exchanger (5) such as a economizer is installed in each rear flue (7). The fuel injected in the main burner (1) burns in the furnace (2) and becomes exhaust gas, which is discharged to the outside through the rear flue (7) and the exhaust gas duct (6).

【0016】次に上記主バーナ(1)の一例を図2によ
り説明する。この主バーナ(1)は下から順にLFA段
(14)、下部石炭・高炉ガスコンビネーション段(1
3)、重油段(12)、上部石炭・高炉ガスコンビネー
ション段(11)およびOFA段(10)の配置となっ
ている。中央部に重油段(12)が配されているのは、
初期起動時に点火燃焼してボイラ火炉の暖気と石炭(微
粉炭)の着火を行なうためであり、他の点火・着火手段
があればなくてもよいものであって、石炭および高炉ガ
スの燃焼時は停止している。
Next, an example of the main burner (1) will be described with reference to FIG. This main burner (1) consists of the LFA stage (14), the lower coal / blast furnace gas combination stage (1
3), heavy oil stage (12), upper coal / blast furnace gas combination stage (11) and OFA stage (10). The heavy oil stage (12) is arranged in the center,
This is to ignite and burn the boiler furnace and ignite coal (pulverized coal) at the time of initial startup, and it is not necessary to have other ignition / ignition means, and when burning coal and blast furnace gas. Has stopped.

【0017】下部石炭・高炉ガスコンビネーション段
(13)には、下から順に補助の燃焼用空気を投入する
AUXコンパートメント(18)、微粉炭濃度の低い淡
混合気コンパートメント(17)、高炉ガスコンパート
メント(16)および微粉炭濃度の高い濃混合気コンパ
ートメント(15)が配置されている。また上部石炭・
高炉ガスコンビネーション段(11)の配置は、上記下
段のものと反対の配置となっている。この配置は上・下
段とも同じでも良いが、重油段(12)に近い方に濃混
合気コンパートメント(15)を配置する方が、石炭の
着火が良くなる。
In the lower coal / blast furnace gas combination stage (13), auxiliary combustion air is introduced in order from the bottom, the AUX compartment (18), the pulverized coal concentration low mixture mixture compartment (17), and the blast furnace gas compartment ( 16) and a dense mixture compartment (15) with a high pulverized coal concentration. Also the upper coal
The arrangement of the blast furnace gas combination stage (11) is the opposite of that of the lower stage. This arrangement may be the same for the upper and lower stages, but the ignition of the coal will be better if the rich mixture compartment (15) is placed closer to the heavy oil stage (12).

【0018】本実施例ではまた、図2の右半部に示され
るように石炭・高炉ガスコンビネーション段(11),
(13)の各コンパートメントを下向き角度に設置し、
各投入燃料および空気が火炉(2)内に滞留する時間が
長くなるようにしている。
In this embodiment, as shown in the right half of FIG. 2, the coal / blast furnace gas combination stage (11),
Install each compartment of (13) at a downward angle,
Each input fuel and air is made to stay for a long time in the furnace (2).

【0019】このようにして本実施形態の高炉ガス混焼
石炭焚きボイラは、濃混合気と淡混合気とを組合わせる
従来の石炭焚きバーナの特徴である低NOx 効果を維持
し、かつ微粉炭・高炉ガスの安定燃焼により灰中未燃分
の低下を図るものである。
In this way, the blast furnace gas co-firing coal-fired boiler of the present embodiment maintains the low NO x effect, which is the characteristic of the conventional coal-burning burner that combines a rich mixture and a light mixture, and pulverized coal.・ It is intended to reduce unburned matter in ash by stable combustion of blast furnace gas.

【0020】[0020]

【発明の効果】本発明では、石炭(微粉炭)と高炉ガス
の混焼ボイラにおいて、バーナ風箱の最適構成により灰
中未燃分を低減するので、ボイラ効率を改善するととも
に、煙道機器の安全性を高めることができる。また濃淡
の混合気を組合わせる従来の微粉炭焚き低NOx バーナ
の作用を合わせて持つので、NOx の発生量も低く抑え
られる。
According to the present invention, in the co-firing boiler of coal (powdered coal) and blast furnace gas, the unburned content in ash is reduced by the optimum configuration of the burner air box, so that the boiler efficiency is improved and the flue equipment The safety can be improved. Further, since it also has the function of the conventional pulverized coal burning low NO x burner that combines a mixture of dark and light, the amount of NO x generated can be suppressed to a low level.

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

【図1】図1は本発明の実施の一形態に係る高炉ガス混
焼石炭焚きボイラを示す縦断面図である。
FIG. 1 is a vertical cross-sectional view showing a blast furnace gas co-firing coal-fired boiler according to an embodiment of the present invention.

【図2】図2は図1中の主バーナ(1)の風箱配置を示
す正面図および一部側面図である。
FIG. 2 is a front view and a partial side view showing a wind box arrangement of a main burner (1) in FIG.

【図3】図3は従来の高炉ガス混焼重油焚きボイラのバ
ーナ風箱の一例を示す正面図である。
FIG. 3 is a front view showing an example of a burner air box of a conventional blast furnace gas mixed burning heavy oil fired boiler.

【図4】図4は従来の微粉炭焚きボイラのバーナ風箱の
一例を示す正面図である。
FIG. 4 is a front view showing an example of a burner wind box of a conventional pulverized coal burning boiler.

【符号の説明】[Explanation of symbols]

(1) 主バーナ (2) 火炉 (3) 過熱器 (4) 再熱器 (5) 節炭器等 (6) 排ガスダクト (7) 後部煙道 (10) OFA段 (11) 上部石炭・高炉ガスコンビネーション段 (12) 重油段 (13) 下部石炭・高炉ガスコンビネーション段 (14) LFA段 (15) 濃混合気コンパートメント (16) 高炉ガスコンパートメント (17) 淡混合気コンパートメント (18) AUXコンパートメント (1) Main burner (2) Furnace (3) Superheater (4) Reheater (5) Economizer (6) Exhaust gas duct (7) Rear flue (10) OFA stage (11) Upper coal / blast furnace Gas combination stage (12) Heavy oil stage (13) Lower coal / blast furnace gas combination stage (14) LFA stage (15) Rich mixture compartment (16) Blast furnace gas compartment (17) Light mixture compartment (18) AUX compartment

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F23D 17/00 103 F23D 17/00 103 Continuation of the front page (51) Int.Cl. 6 Identification number Office reference number FI technical display location F23D 17/00 103 F23D 17/00 103

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 微粉炭と空気との混合気および高炉ガス
をボイラ火炉に投入して燃焼させる高炉ガス混焼石炭焚
きボイラにおいて、微粉炭濃度の高い濃混合気を投入す
るコンパートメントと微粉炭濃度の低い淡混合気を投入
するコンパートメントとの間に高炉ガスを投入するコン
パートメントを配置するとともに、各コンパートメント
を下向きに傾斜させたことを特徴とする高炉ガス混焼石
炭焚きボイラ。
Claim: What is claimed is: 1. In a blast furnace gas mixed firing coal-fired boiler in which a mixture of pulverized coal and air and a blast furnace gas are introduced into a boiler furnace and burned, a compartment in which a dense mixture having a high pulverized coal concentration is introduced and a pulverized coal concentration A blast-furnace gas co-firing coal-fired boiler characterized by arranging a compartment for injecting blast furnace gas between a compartment for injecting a low light air-fuel mixture and sloping each compartment downward.
JP07278891A 1995-10-26 1995-10-26 Blast furnace gas co-firing coal-fired boiler Expired - Fee Related JP3073434B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07278891A JP3073434B2 (en) 1995-10-26 1995-10-26 Blast furnace gas co-firing coal-fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07278891A JP3073434B2 (en) 1995-10-26 1995-10-26 Blast furnace gas co-firing coal-fired boiler

Publications (2)

Publication Number Publication Date
JPH09119606A true JPH09119606A (en) 1997-05-06
JP3073434B2 JP3073434B2 (en) 2000-08-07

Family

ID=17603549

Family Applications (1)

Application Number Title Priority Date Filing Date
JP07278891A Expired - Fee Related JP3073434B2 (en) 1995-10-26 1995-10-26 Blast furnace gas co-firing coal-fired boiler

Country Status (1)

Country Link
JP (1) JP3073434B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008008522A (en) * 2006-06-27 2008-01-17 Nippon Steel Corp Boiler fuel charging amount deciding method, boiler fuel control device and program
JP2015072118A (en) * 2014-11-26 2015-04-16 三菱重工業株式会社 Oil firing burner, solid fuel firing burner unit and boiler for solid fuel firing
US9702545B2 (en) 2011-11-16 2017-07-11 Mitsubishi Heavy Industries, Ltd. Oil-fired burner, solid fuel-fired burner unit, and solid fuel-fired boiler
JP2020125859A (en) * 2019-02-01 2020-08-20 三菱日立パワーシステムズ株式会社 Bfg burner device, boiler comprising the same, and method of operating bfg burner device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008008522A (en) * 2006-06-27 2008-01-17 Nippon Steel Corp Boiler fuel charging amount deciding method, boiler fuel control device and program
US9702545B2 (en) 2011-11-16 2017-07-11 Mitsubishi Heavy Industries, Ltd. Oil-fired burner, solid fuel-fired burner unit, and solid fuel-fired boiler
JP2015072118A (en) * 2014-11-26 2015-04-16 三菱重工業株式会社 Oil firing burner, solid fuel firing burner unit and boiler for solid fuel firing
JP2020125859A (en) * 2019-02-01 2020-08-20 三菱日立パワーシステムズ株式会社 Bfg burner device, boiler comprising the same, and method of operating bfg burner device

Also Published As

Publication number Publication date
JP3073434B2 (en) 2000-08-07

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