JPH11351549A - Combustion facility for high moisture coal - Google Patents

Combustion facility for high moisture coal

Info

Publication number
JPH11351549A
JPH11351549A JP15896898A JP15896898A JPH11351549A JP H11351549 A JPH11351549 A JP H11351549A JP 15896898 A JP15896898 A JP 15896898A JP 15896898 A JP15896898 A JP 15896898A JP H11351549 A JPH11351549 A JP H11351549A
Authority
JP
Japan
Prior art keywords
coal
air
combustion
heat exchanger
high temperature
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.)
Pending
Application number
JP15896898A
Other languages
Japanese (ja)
Inventor
Yoshihiko Endo
喜彦 遠藤
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP15896898A priority Critical patent/JPH11351549A/en
Publication of JPH11351549A publication Critical patent/JPH11351549A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a combustion facility for a high moisture coal for effectively drying and burning the coal containing much moisture without giving an adverse influence to a combustion of a pulverized coal in a burner. SOLUTION: The combustion facility for a high moisture coal comprises a heat exchanger 10 for preheating the air with a high temperature gas from a boiler 1 to a high temperature (about 700 deg.C) (e.g. a rotary generative heat exchanger, thereby supplying preheated high temperature air to a coal pulverizer 2. Since the high temperature air is used, a high moisture coal containing much moisture can be effectively dried and burned. Since the high temperature air is used instead of a conventional exhaust gas, an oxygen concentration in a finely pulverized coal igniting area near a burner becomes high, thereby expediting a combustion of the pulverized coal.

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、湿分の高い石炭を
燃料とする燃焼設備に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion facility using high moisture coal as fuel.

【0002】[0002]

【従来の技術】図3は従来の微粉炭燃焼設備の構成図で
ある。この図に示すように、従来の微粉炭燃焼設備で
は、ボイラ1の付帯設備として、石炭粉砕機2(ミ
ル)、ガス空気熱交換器3(GAH)、押込送風機4
(FDF)、誘引送風機5(IDF)、スタック6等を
備え、ボイラ1の排ガスで空気を予熱し、その予熱空気
(約350℃前後)をミル2に供給して石炭を粉砕しな
がら乾燥させ、乾燥した微粉炭を空気と共にボイラの燃
焼器1a(バーナ)に供給して燃焼させていた。
2. Description of the Related Art FIG. 3 is a block diagram of a conventional pulverized coal combustion facility. As shown in this figure, in the conventional pulverized coal combustion equipment, as ancillary equipment of the boiler 1, a coal pulverizer 2 (mill), a gas air heat exchanger 3 (GAH), a forced air blower 4
(FDF), an induction blower 5 (IDF), a stack 6, etc., preheat air with exhaust gas from the boiler 1, supply the preheated air (about 350 ° C.) to a mill 2 and dry while pulverizing coal. Then, the dry pulverized coal was supplied to the combustor 1a (burner) of the boiler together with air to burn it.

【0003】[0003]

【発明が解決しようとする課題】図3の微粉炭燃焼設備
では、石炭の表面水分が5〜20%程度の場合にはその
まま適用できるが、水分が多い高湿分炭(例えば、褐炭
やリグナイト)はミル内での乾燥が不足して良好な粉砕
が困難になり、ボイラにおける燃焼にも悪影響がある問
題点があった。そのため、かかる高湿分炭を適用するた
めに、図4のような高湿分炭用燃焼設備が検討されてい
る。この微粉炭燃焼設備は、ボイラから高温(例えば8
00〜1000℃)の排ガスを抜き出して、この高温排
ガスをミル2に供給して石炭を粉砕しながら乾燥させ、
乾燥した微粉炭を空気と共にボイラのバーナ1aに供給
して燃焼させる構成であり、高温(例えば800〜10
00℃)の排ガスを乾燥に用いることから約30%以上
の水分を含む高湿分炭にも適用することができる。
The pulverized coal combustion equipment shown in FIG. 3 can be applied as it is when the surface moisture of the coal is about 5 to 20%. (2) has a problem that drying in the mill is insufficient and it is difficult to perform good pulverization, and combustion in the boiler is also adversely affected. Therefore, in order to apply such high-humidity coal, combustion equipment for high-humidity coal as shown in FIG. 4 is being studied. This pulverized coal combustion equipment is provided with a high temperature (for example, 8
(1000-1000 ° C.), and the high-temperature exhaust gas is supplied to a mill 2 and dried while pulverizing coal.
Dry pulverized coal is supplied to the burner 1a of the boiler together with air to burn it, and is heated at a high temperature (for example, 800 to
Since the exhaust gas of (00 ° C.) is used for drying, it can be applied to high-humidity coal containing about 30% or more of water.

【0004】しかし、図4に示した高湿分炭用燃焼設備
では、ミル2へ供給された排ガスが、粉砕した微粉炭を
バーナ1aまで搬送し、そのまま、微粉炭と共にボイラ
内に供給されるため、排ガスを用いると燃焼の安定性が
低下することがある問題点があった。すなわち、ボイラ
の高温排ガスは、高温ではあるが酸素濃度が非常に低い
(例えば3〜4%)ため、バーナ部での微粉炭の燃焼に
悪影響を与えていた。
However, in the high-humidity coal combustion facility shown in FIG. 4, the exhaust gas supplied to the mill 2 transports the pulverized pulverized coal to the burner 1a and is supplied as it is to the boiler together with the pulverized coal. Therefore, there has been a problem that the stability of combustion may be reduced when exhaust gas is used. That is, although the high-temperature exhaust gas of the boiler has a high temperature but a very low oxygen concentration (for example, 3 to 4%), the combustion of the pulverized coal in the burner section is adversely affected.

【0005】本発明は、かかる問題点を解決するために
創案されたものである。すなわち、本発明の目的は、バ
ーナ部での微粉炭の燃焼に悪影響を与えることなく、水
分が多い高湿分炭を効果的に乾燥させ燃焼させることが
できる高湿分炭用燃焼設備を提供することにある。
The present invention has been made to solve such a problem. That is, an object of the present invention is to provide a high-humidity coal combustion facility capable of effectively drying and burning high-moisture coal with high moisture content without adversely affecting the combustion of pulverized coal in the burner section. Is to do.

【0006】[0006]

【課題を解決するための手段】本発明によれば、ボイラ
(1)からの高温排ガスで空気を高温に予熱する熱交換
器(10)を備え、予熱した高温空気を石炭粉砕機
(2)に供給することを特徴とする高湿分炭用燃焼設備
が提供される。
According to the present invention, there is provided a heat exchanger (10) for preheating air to a high temperature with high temperature exhaust gas from a boiler (1), and the preheated high temperature air is used as a coal crusher (2). The present invention provides a high-humidity coal combustion facility characterized in that it is supplied to a high-humidity coal coal.

【0007】本発明の構成によれば、高温排ガスで空気
を高温に予熱する熱交換器(10)を備えているので、
例えば800〜1000℃の排ガスにより、空気を約7
00℃前後の高温まで加熱することができる。従って、
この高温空気を用いて水分が多い高湿分炭を効果的に乾
燥、粉砕させバーナに供給することができる。更に、排
ガスの代わりに高温空気を用いるので、酸素濃度が十分
に高く、バーナ部での微粉炭の燃焼に悪影響を与えるお
それがない。すなわち、従来技術と比較してバーナ近傍
の微粉炭着火領域での酸素濃度が高くなり、その結果、
微粉炭の燃焼を促進することができる。
According to the structure of the present invention, since the heat exchanger (10) for preheating the air to a high temperature with the high-temperature exhaust gas is provided,
For example, with exhaust gas at 800 to 1000 ° C.,
It can be heated to a high temperature of around 00 ° C. Therefore,
Using this high-temperature air, high-moisture coal with high moisture content can be effectively dried, pulverized and supplied to the burner. Furthermore, since high-temperature air is used instead of exhaust gas, the oxygen concentration is sufficiently high, and there is no possibility that the combustion of pulverized coal in the burner section will be adversely affected. That is, compared to the prior art, the oxygen concentration in the pulverized coal ignition region near the burner becomes higher, and as a result,
Pulverized coal combustion can be promoted.

【0008】本発明の好ましい実施形態によれば、前記
熱交換器(10)は、回転再生式熱交換器である。かか
る回転再生式熱交換器を用いることにより、空気を約7
00℃前後の高温まで加熱する場合でも、プレートフィ
ン等の他の形式の熱交換器に比較して設備費を下げるこ
とができ、かつ高い熱交換率を維持することができる。
According to a preferred embodiment of the present invention, the heat exchanger (10) is a regenerative heat exchanger. By using such a rotary regenerative heat exchanger, air is reduced to about 7
Even when heating to a high temperature of about 00 ° C., equipment costs can be reduced and a high heat exchange rate can be maintained as compared with other types of heat exchangers such as plate fins.

【0009】[0009]

【発明の実施の形態】以下、本発明の好ましい実施形態
を図面を参照して説明する。図1は、本発明による高湿
分炭用燃焼設備の構成図であり、図2は、微粉炭用バー
ナの構成図である。図1に示すように、本発明の高湿分
炭用燃焼設備は、ボイラ1の付帯設備として、石炭粉砕
機2(ミル)、ガス空気熱交換器3(GAH)、押込送
風機4(FDF)、誘引送風機5(IDF)及びスタッ
ク6を備え、ボイラ1の排ガスで空気を予熱し、その予
熱空気(約350℃前後)をボイラの燃焼器1a(バー
ナ)に供給するようになっている。なお、この図で、P
AFは1次通風機である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of a combustion facility for high-humidity coal according to the present invention, and FIG. 2 is a configuration diagram of a burner for pulverized coal. As shown in FIG. 1, the high-humidity coal combustion facility of the present invention includes a coal pulverizer 2 (mill), a gas-air heat exchanger 3 (GAH), a forced air blower 4 (FDF) as ancillary facilities of the boiler 1 , An air blower 5 (IDF) and a stack 6 for preheating air with exhaust gas from the boiler 1 and supplying the preheated air (about 350 ° C.) to a combustor 1 a (burner) of the boiler. In this figure, P
AF is a primary ventilator.

【0010】また、図2に示すように、ボイラの燃焼器
1a、すなわち微粉炭用バーナは、ミル2から供給され
る1次空気と微粉炭をボイラ1の火炉1b内(この図で
右側)に向けて噴射する微粉炭ノズル部7aと、この回
りにガス空気熱交換器3で予熱した2次空気を供給する
2次空気ダクト7bとを備えている。図2の構成から明
らかなように、2次空気自体の酸素濃度が高くても、1
次空気の代わりに酸素濃度が非常に低い排ガスを用いる
と、微粉炭を取り巻くバーナ近傍の微粉炭着火領域での
酸素濃度が低くなり、微粉炭の安定した燃焼が困難にな
るおそれがある。
As shown in FIG. 2, a burner 1a of the boiler, that is, a burner for pulverized coal, converts primary air and pulverized coal supplied from the mill 2 into a furnace 1b of the boiler 1 (right side in FIG. 2). And a secondary air duct 7b around which the secondary air preheated by the gas air heat exchanger 3 is supplied. As is clear from the configuration of FIG. 2, even if the oxygen concentration of the secondary air itself is high,
If the exhaust gas having a very low oxygen concentration is used instead of the secondary air, the oxygen concentration in the pulverized coal ignition region near the burner surrounding the pulverized coal may decrease, and stable combustion of the pulverized coal may be difficult.

【0011】図1に示すように、本発明の高湿分炭用燃
焼設備は、更に、ボイラ1からの高温排ガス8aで空気
を高温(好ましくは700℃以上)に予熱する熱交換器
10を備えている。この熱交換器10は、例えば特開平
8−327262号公報に開示されているような、回転
再生式熱交換器を用いるのがよい。かかる回転再生式熱
交換器は、プレートフィン等の他の形式の熱交換器に比
較して製造コストが低く、かつ約700℃前後の高温ま
で空気を容易に加熱することができる。従ってかかる回
転再生式熱交換器を用いることにより、設備費を下げ、
かつ高い熱交換率を維持することができる。
As shown in FIG. 1, the high-humidity coal combustion facility of the present invention further includes a heat exchanger 10 for preheating air to a high temperature (preferably 700 ° C. or higher) with the high-temperature exhaust gas 8a from the boiler 1. Have. As the heat exchanger 10, it is preferable to use a rotary regeneration type heat exchanger as disclosed in, for example, Japanese Patent Application Laid-Open No. 8-327262. Such a regenerative heat exchanger has a lower manufacturing cost than other types of heat exchangers such as plate fins, and can easily heat air to a high temperature of about 700 ° C. Therefore, by using such a regenerative heat exchanger, equipment costs can be reduced,
And a high heat exchange rate can be maintained.

【0012】上述した本発明の構成によれば、ボイラの
高温排ガスで空気を高温に予熱する熱交換器10を備え
ているので、例えば800〜1000℃の排ガスによ
り、空気を約700℃前後の高温まで加熱することがで
きる。従って、この高温空気8bを用いてミル2内で水
分が多い高湿分炭を効果的に乾燥させ、これをボイラの
燃焼器1aで燃焼させることができる。更に、従来の排
ガスの代わりに高温空気8bを用いるので、酸素濃度が
十分に高く、バーナ部での微粉炭の燃焼に悪影響を与え
るおそれがない。すなわち、従来技術と比較してバーナ
近傍の微粉炭着火領域での酸素濃度が高くなり、その結
果、微粉炭の燃焼を促進することができる。
According to the configuration of the present invention described above, the heat exchanger 10 for preheating the air to a high temperature with the high temperature exhaust gas of the boiler is provided. Can be heated to high temperatures. Accordingly, the high-humidity coal having a high moisture content can be effectively dried in the mill 2 using the high-temperature air 8b, and can be burned in the combustor 1a of the boiler. Further, since the high-temperature air 8b is used instead of the conventional exhaust gas, the oxygen concentration is sufficiently high, and there is no possibility that the combustion of the pulverized coal in the burner section will be adversely affected. That is, as compared with the prior art, the oxygen concentration in the pulverized coal ignition region near the burner is increased, and as a result, the combustion of the pulverized coal can be promoted.

【0013】なお、本発明は上述した実施形態及び実施
例に限定されず、本発明の要旨を逸脱しない範囲で種々
変更できることは勿論である。
It should be noted that the present invention is not limited to the above-described embodiments and examples, and it is needless to say that various changes can be made without departing from the gist of the present invention.

【0014】[0014]

【発明の効果】上述したように、本発明の高湿分炭用燃
焼設備は、高温空気を用いて水分が多い高湿分炭を効果
的に乾燥させ燃焼させることができ、かつ排ガスの代わ
りに高温空気を用いるので、バーナ近傍の微粉炭着火領
域での酸素濃度が高くなり、バーナ部での微粉炭の燃焼
に悪影響を与えることない等の優れた効果を有する。
As described above, the high-humidity coal combustion facility of the present invention can effectively dry and burn high-moisture high-content coal using high-temperature air, and can substitute for exhaust gas. Since high-temperature air is used, the oxygen concentration in the pulverized coal ignition region near the burner is increased, and excellent effects such as not adversely affecting the combustion of the pulverized coal in the burner portion are obtained.

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

【図1】本発明による高湿分炭用燃焼設備の構成図であ
る。
FIG. 1 is a configuration diagram of a high-humidity coal combustion facility according to the present invention.

【図2】微粉炭用バーナの構成図である。FIG. 2 is a configuration diagram of a burner for pulverized coal.

【図3】従来の微粉炭燃焼設備の構成図である。FIG. 3 is a configuration diagram of a conventional pulverized coal combustion facility.

【図4】従来の高湿分炭用燃焼設備の構成図である。FIG. 4 is a configuration diagram of a conventional high-humidity coal combustion facility.

【符号の説明】[Explanation of symbols]

1 ボイラ 1a 燃焼器(バーナ) 2 石炭粉砕機(ミル) 3 ガス空気熱交換器(GAH) 4 押込送風機(FDF) 5 誘引送風機(IDF) 6 スタック 7a 微粉炭ノズル部 7b 2次空気ダクト 8a 高温排ガス 8b 高温空気 10 熱交換器(回転再生式熱交換器) DESCRIPTION OF SYMBOLS 1 Boiler 1a Combustor (burner) 2 Coal crusher (mill) 3 Gas-air heat exchanger (GAH) 4 Push-in blower (FDF) 5 Induction blower (IDF) 6 Stack 7a Pulverized coal nozzle 7b Secondary air duct 8a High temperature Exhaust gas 8b High-temperature air 10 Heat exchanger (rotary regeneration heat exchanger)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ボイラ(1)からの高温排ガスで空気を
高温に予熱する熱交換器(10)を備え、予熱した高温
空気を石炭粉砕機(2)に供給することを特徴とする高
湿分炭用燃焼設備。
A high-humidity air supply system comprising a heat exchanger (10) for preheating air to a high temperature with high-temperature exhaust gas from a boiler (1), and supplying the preheated high-temperature air to a coal crusher (2). Combustion equipment for coal splitting.
【請求項2】 前記熱交換器(10)は、回転再生式熱
交換器であることを特徴とする請求項1に記載の高湿分
炭用燃焼設備。
2. The high-humidity coal combustion facility according to claim 1, wherein the heat exchanger is a regenerative heat exchanger.
JP15896898A 1998-06-08 1998-06-08 Combustion facility for high moisture coal Pending JPH11351549A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15896898A JPH11351549A (en) 1998-06-08 1998-06-08 Combustion facility for high moisture coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15896898A JPH11351549A (en) 1998-06-08 1998-06-08 Combustion facility for high moisture coal

Publications (1)

Publication Number Publication Date
JPH11351549A true JPH11351549A (en) 1999-12-24

Family

ID=15683315

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15896898A Pending JPH11351549A (en) 1998-06-08 1998-06-08 Combustion facility for high moisture coal

Country Status (1)

Country Link
JP (1) JPH11351549A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2010202597B2 (en) * 2009-07-28 2014-09-11 Rwe Power Aktiengesellschaft Method for operating a steam turbine power plant and also device for generating steam

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2010202597B2 (en) * 2009-07-28 2014-09-11 Rwe Power Aktiengesellschaft Method for operating a steam turbine power plant and also device for generating steam

Similar Documents

Publication Publication Date Title
CA1243549A (en) Coal fired furnace light-off and stabilization using microfine pulverized coal
JPH09293525A (en) Solid electrolyte fuel cell power generation system
JPH11351549A (en) Combustion facility for high moisture coal
JP2001255018A (en) Fan heater
JP2002243110A (en) Pulverized coal boiler
JP3599477B2 (en) Combustion equipment
JP3793276B2 (en) Heat storage switching burner
JP3469003B2 (en) Charcoal-fired burner with high volatile content and high moisture content
KR100948515B1 (en) Boiler NOx reduction method and system with humidifying combustion air
JPS609205B2 (en) coal combustion equipment
JPH028610A (en) Pulverized coal combustion device
JP2000028129A (en) Pulverized coal combustor
JPH07233920A (en) Burning method for oxygen burner
RU2032851C1 (en) Method of joint operation of power-generating boiler and drying unit
KR19980083457A (en) Unburned Gas Reduced Hot Air Heater
JPH0245620Y2 (en)
JPH0424272Y2 (en)
JPS6036813A (en) Catalyst combustion device
JPS6347770B2 (en)
TW552373B (en) Superatmospheric combustor for combusting lean concentrations of a burnable gas
JP2832288B2 (en) Low nitrogen oxide combustion method
JPH0666421A (en) Combustion device
SU846924A1 (en) Boiler unit operation method
JPH0548062Y2 (en)
CN115597073A (en) Waste gas self-afterburning waste heat boiler