JPH04115238U - boiler equipment - Google Patents

boiler equipment

Info

Publication number
JPH04115238U
JPH04115238U JP1991024673U JP2467391U JPH04115238U JP H04115238 U JPH04115238 U JP H04115238U JP 1991024673 U JP1991024673 U JP 1991024673U JP 2467391 U JP2467391 U JP 2467391U JP H04115238 U JPH04115238 U JP H04115238U
Authority
JP
Japan
Prior art keywords
coal
pulverized coal
supply duct
air
duct
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
JP1991024673U
Other languages
Japanese (ja)
Inventor
政弘 小沢
芳雄 赤井
Original Assignee
石川島播磨重工業株式会社
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 石川島播磨重工業株式会社 filed Critical 石川島播磨重工業株式会社
Priority to JP1991024673U priority Critical patent/JPH04115238U/en
Publication of JPH04115238U publication Critical patent/JPH04115238U/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

Abstract

(57)【要約】 【目的】 空気予熱器出側の排ガスの温度に影響を与え
ずに高湿分炭を充分乾燥させる。 【構成】 火炉2にバーナ3を有すると共に後部伝熱部
4に節炭器5を有するボイラ本体1と、石炭を微粉砕し
てバーナ3へ供給する燃料用の微粉炭を製造するための
微粉炭ミル14と、微粉炭ミル14へ微粉炭搬送用及び
石炭乾燥用の空気10を供給する一次空気供給ダクト1
3とを備えたボイラ装置において、後部伝熱部4の節炭
器5入側と微粉炭ミル14へ空気10を供給する一次空
気供給ダクト13との間を節炭器バイパスダクト21で
接続する。
(57) [Summary] [Purpose] To sufficiently dry high-humidity coal without affecting the temperature of the exhaust gas on the outlet side of the air preheater. [Structure] A boiler main body 1 having a burner 3 in a furnace 2 and a coal saver 5 in a rear heat transfer section 4, and pulverized coal for producing pulverized coal for fuel to be supplied to the burner 3 by pulverizing coal. A charcoal mill 14 and a primary air supply duct 1 that supplies air 10 to the pulverized coal mill 14 for transporting pulverized coal and drying the coal.
In the boiler apparatus equipped with 3, the inlet side of the economizer 5 of the rear heat transfer section 4 and the primary air supply duct 13 that supplies air 10 to the pulverized coal mill 14 are connected by an economizer bypass duct 21. .

Description

【考案の詳細な説明】[Detailed explanation of the idea]

【0001】0001

【産業上の利用分野】[Industrial application field]

本考案は、ボイラ装置に関するものである。 The present invention relates to a boiler device.

【0002】0002

【従来の技術】[Conventional technology]

以下、従来のボイラ装置を図3を用いて説明する。 Hereinafter, a conventional boiler device will be explained using FIG. 3.

【0003】 図中1はボイラ本体、2はボイラ本体1を構成する火炉、3は火炉2に設置さ れたバーナ、4は火炉2の出側に接続された後部伝熱部、5は後部伝熱部4内に 設置された節炭器である。0003 In the figure, 1 is the boiler body, 2 is the furnace that constitutes the boiler body 1, and 3 is the furnace installed in the furnace 2. 4 is a rear heat transfer part connected to the outlet side of the furnace 2, 5 is a burner in the rear heat transfer part 4. This is an installed energy saver.

【0004】 6は後部伝熱部4の節炭器5出側に接続され、排ガス7を煙突8へ導く排ガス ダクトである。0004 6 is connected to the exit side of the economizer 5 of the rear heat transfer section 4 and guides the exhaust gas 7 to the chimney 8. It's a duct.

【0005】 9は図示しない押込み通風ファンによってバーナ3へ燃焼用の空気10を供給 するための空気供給ダクト、11は空気供給ダクト9及び排ガスダクト6の途中 に設けられて空気10と排ガス7とを熱交換する空気予熱器である。[0005] 9 supplies combustion air 10 to the burner 3 by a forced ventilation fan (not shown) An air supply duct 11 is located between the air supply duct 9 and the exhaust gas duct 6. This is an air preheater installed in the exhaust gas 7 to exchange heat between the air 10 and the exhaust gas 7.

【0006】 12は後部伝熱部4の節炭器5入側と排ガスダクト6の空気予熱器11入側と の間を接続する節炭器バイパスダクトである。[0006] 12 is the inlet side of the energy saver 5 of the rear heat transfer section 4 and the inlet side of the air preheater 11 of the exhaust gas duct 6. This is an energy saver bypass duct that connects the

【0007】 13は空気供給ダクト9の空気予熱器11入側から分岐して、石炭を微粉砕し て燃料用の微粉炭を製造する微粉炭ミル14の入側へ接続する一次空気供給ダク ト、20は微粉炭ミル14出側とバーナ3との間を接続する微粉炭供給管、15 は空気供給ダクト9の空気予熱器11出側と一次空気供給ダクト13との間を接 続する加熱一次空気供給ダクト、16は一次空気供給ダクト13の途中の微粉炭 ミル14の入側に設けられた一次空気ファン、17,18,19はそれぞれ節炭 器バイパスダクト12及び一次空気供給ダクト13並びに加熱一次空気供給ダク ト15に設けられたダンパである。[0007] 13 branches from the air preheater 11 inlet side of the air supply duct 9 and pulverizes the coal. A primary air supply duct connected to the inlet side of a pulverized coal mill 14 that produces pulverized coal for fuel. 20 is a pulverized coal supply pipe 15 connecting between the outlet side of the pulverized coal mill 14 and the burner 3; connects the outlet side of the air preheater 11 of the air supply duct 9 and the primary air supply duct 13. The heating primary air supply duct 16 is connected to the pulverized coal in the middle of the primary air supply duct 13. The primary air fans 17, 18, and 19 installed on the inlet side of the mill 14 are each designed to save energy. device bypass duct 12, primary air supply duct 13, and heated primary air supply duct This is a damper provided in the seat 15.

【0008】 図示しない押込み通風ファンにより空気供給ダクト9を介してバーナ3へ燃焼 用の空気10を供給すると共に、空気供給ダクト9を流れる空気10の一部を一 次空気供給ダクト13及び加熱一次空気供給ダクト15を介して微粉炭ミル14 へ送り、微粉炭ミル14で石炭を微粉砕してなる燃料用の微粉炭を微粉炭管20 を介してバーナ3へ搬送させる。[0008] Combustion is carried out into the burner 3 via the air supply duct 9 by a forced ventilation fan (not shown). In addition to supplying the air 10 for use, a part of the air 10 flowing through the air supply duct 9 is Pulverized coal mill 14 via secondary air supply duct 13 and heated primary air supply duct 15 The pulverized coal for fuel is sent to the pulverized coal pipe 20 by finely pulverizing the coal in the pulverized coal mill 14. It is conveyed to the burner 3 via.

【0009】 そして、火炉2内でバーナ3により微粉炭供給管20からの微粉炭を空気供給 ダクト9からの空気10で燃焼させる。[0009] Then, air is supplied to the pulverized coal from the pulverized coal supply pipe 20 by the burner 3 in the furnace 2. Combustion is carried out with air 10 from duct 9.

【0010】 すると、燃焼により発生した燃焼ガスはボイラ本体1を構成する火炉2から後 部伝熱部4へ向って流れ、途中、火炉2や後部伝熱部4を構成する各種伝熱管類 、及び火炉2や後部伝熱部4に設けられた図示しない過熱器や節炭器5等を加熱 して蒸気を発生させ、その後、排ガス7として排ガスダクト6へ排出される。0010 Then, the combustion gas generated by combustion is discharged from the furnace 2 that constitutes the boiler body 1. Various heat transfer tubes that flow toward the heat transfer section 4 and constitute the furnace 2 and the rear heat transfer section 4 on the way. , and heats the superheater, economizer 5, etc. (not shown) provided in the furnace 2 and the rear heat transfer section 4. to generate steam, which is then discharged into the exhaust gas duct 6 as exhaust gas 7.

【0011】 排ガスダクト6へ排出された排ガス7は排ガスダクト6を介して煙突8から大 気へ放出され、途中、空気予熱器11を通って空気供給ダクト9を流れる空気1 0との間で熱交換が行われ、バーナ3へ供給される燃焼用の空気10を加熱する 。[0011] The exhaust gas 7 discharged to the exhaust gas duct 6 is sent from the chimney 8 through the exhaust gas duct 6. Air 1 flows through the air supply duct 9 passing through the air preheater 11 on the way 0 and heats the combustion air 10 supplied to the burner 3. .

【0012】 又、空気予熱器11で加熱された空気10の一部は、加熱一次空気供給ダクト 15を介して一次空気供給ダクト13を流れる空気10に混合されて微粉炭ミル 14へ供給される空気10の温度を上昇させ、微粉炭ミル14で微粉砕される石 炭を乾燥するのに利用される。0012 Also, a part of the air 10 heated by the air preheater 11 is transferred to the heated primary air supply duct. The air 10 flowing through the primary air supply duct 13 through the pulverized coal mill The temperature of the air 10 supplied to the pulverized coal mill 14 is increased, and the stone is pulverized by the pulverized coal mill 14. Used for drying charcoal.

【0013】 ボイラ本体1の起動時や負荷低下時などのように、排ガス7の温度が低くて空 気予熱器11で空気10を充分に加熱できない時などには、節炭器バイパスダク ト12を用いて、節炭器5を加熱して温度が下がる以前の温度の高い燃焼ガスを 、排ガスダクト6の空気予熱器11入側へ直接導き、空気予熱器11へ導入され る排ガス7の温度を上げるようにする。[0013] When the temperature of the exhaust gas 7 is low and it is empty, such as when the boiler body 1 is started or the load is reduced, etc. When the air 10 cannot be sufficiently heated by the air preheater 11, use the energy saving bypass duct. 12 to heat the economizer 5 to remove the high temperature combustion gas before its temperature drops. , is led directly to the inlet side of the air preheater 11 of the exhaust gas duct 6, and is introduced into the air preheater 11. The temperature of the exhaust gas 7 is increased.

【0014】[0014]

【考案が解決しようとする課題】[Problem that the idea aims to solve]

しかしながら、上記従来のボイラ装置には、以下のような問題があった。 However, the conventional boiler device described above has the following problems.

【0015】 即ち、ボイラに対し高品質炭に代えて様々な種類の石炭(低品質炭など)を使 用する機会が今後一層増えていくことが予想されているが、中でも水分を多く含 んでいる石炭つまり高湿分炭を使用する場合には、微粉炭ミル14において高湿 分炭を充分乾燥できるようにするために微粉炭ミル14へ供給する空気10の温 度を通常よりも上げることが必要となる。[0015] In other words, different types of coal (such as low-quality coal) can be used in the boiler instead of high-quality coal. It is expected that the opportunities for using water will continue to increase in the future, but in particular, When using pulverized coal, that is, high humidity coal, the pulverized coal mill 14 The temperature of the air 10 supplied to the pulverized coal mill 14 in order to sufficiently dry the separated coal. It is necessary to raise the level higher than normal.

【0016】 そのために、高湿分炭を使用する場合には、節炭器バイパスダクト12を積極 的に使用して空気予熱器11へ供給される排ガス7の温度を上げるようにし、以 て微粉炭ミル14へ供給する空気10の温度を上げることが行われているが、こ のようにすると、煙突8から排出される排ガス7の温度が高くなりすぎてしまう という問題や、空気予熱器11における熱交換効率の面から規制されてしまうの で空気予熱器11入側の排ガス7の温度を上げても空気10が必要温度まで加熱 されないという問題があった。[0016] For this reason, when using high-moisture coal, the energy saving device bypass duct 12 is actively installed. The temperature of the exhaust gas 7 supplied to the air preheater 11 is increased by using The temperature of the air 10 supplied to the pulverized coal mill 14 is raised by If you do this, the temperature of the exhaust gas 7 discharged from the chimney 8 will become too high. It is regulated due to the problem of heat exchange efficiency in the air preheater 11. Even if the temperature of the exhaust gas 7 on the inlet side of the air preheater 11 is raised, the air 10 will still be heated to the required temperature. There was a problem that it was not done.

【0017】 本考案は、上述の実情に鑑み、空気予熱器出側の排ガスの温度に影響を与えず に高湿分炭を充分乾燥し得るようにしたボイラ装置を提供することを目的とする ものである。[0017] In view of the above-mentioned circumstances, this invention does not affect the temperature of the exhaust gas on the outlet side of the air preheater. The purpose of the present invention is to provide a boiler device capable of sufficiently drying high-humidity coal. It is something.

【0018】[0018]

【課題を解決するための手段】[Means to solve the problem]

本考案は、火炉にバーナを有すると共に後部伝熱部に節炭器を有するボイラ本 体と、石炭を微粉砕してバーナへ供給する燃料用の微粉炭を製造するための微粉 炭ミルと、微粉炭ミルへ微粉炭搬送用及び石炭乾燥用の空気を供給する一次空気 供給ダクトとを備えたボイラ装置において、後部伝熱部の節炭器入側と微粉炭ミ ルへ空気を供給する一次空気供給ダクトとの間を節炭器バイパスダクトで接続し たことを特徴とするボイラ装置にかかるものである。 This invention is based on a boiler that has a burner in the furnace and a energy saver in the rear heat transfer section. and pulverized powder for producing pulverized coal for the fuel used to pulverize coal and supply it to burners. Coal mill and primary air supplying air for transporting pulverized coal and drying coal to the pulverized coal mill. In boiler equipment equipped with a supply duct, the power saving device inlet side of the rear heat transfer section and the pulverized coal mixer An energy saver bypass duct connects the primary air supply duct that supplies air to the The present invention relates to a boiler device characterized by the following.

【0019】[0019]

【作用】[Effect]

本考案によれば、後部伝熱部の節炭器入側の温度の高い燃焼ガスが、節炭器バ イパスダクトを介して一次空気供給ダクトからの空気と混合され、直接微粉炭ミ ルへ供給されるので、高湿分炭であっても微粉炭ミルで充分乾燥させることがで きる。 According to the present invention, the high-temperature combustion gas on the inlet side of the economizer in the rear heat transfer section is The pulverized coal is mixed with air from the primary air supply duct through the Ipass duct and directly Even high-humidity coal can be sufficiently dried in the pulverized coal mill. Wear.

【0020】[0020]

【実施例】【Example】

以下、本考案の実施例を図面を参照しつつ説明する。 Embodiments of the present invention will be described below with reference to the drawings.

【0021】 図1は、本考案の第一の実施例である。[0021] FIG. 1 shows a first embodiment of the present invention.

【0022】 又、図中、図3と同一の部分については同一の符号を付すことによって説明を 省略するものとし、以下、本考案に特有の構成についてのみ説明して行く。[0022] In addition, in the figure, the same parts as in Figure 3 are given the same reference numerals for explanation. The description will be omitted, and only the configuration unique to the present invention will be explained below.

【0023】 ボイラ本体1を構成する後部伝熱部4の節炭器5入側と、微粉炭ミル14に微 粉炭搬送用及び石炭乾燥用の空気10を供給する一次空気供給ダクト13との間 を節炭器バイパスダクト21で接続し、節炭器バイパスダクト21の途中に排ガ ス供給ファン22を設ける。[0023] The inlet side of the economizer 5 of the rear heat transfer section 4 that constitutes the boiler body 1 and the pulverized coal mill 14 are Between the primary air supply duct 13 that supplies air 10 for transporting powdered coal and drying coal are connected with the economizer bypass duct 21, and an exhaust gas is connected in the middle of the economizer bypass duct 21. A gas supply fan 22 is provided.

【0024】 尚、23は節炭器バイパスダクト21の途中に設けられたダンパである。[0024] In addition, 23 is a damper provided in the middle of the economizer bypass duct 21.

【0025】 次に、作動について説明する。[0025] Next, the operation will be explained.

【0026】 ボイラ装置の基本的な作動自体については図3と同様なので説明を省略する。[0026] The basic operation of the boiler device itself is the same as that shown in FIG. 3, so a description thereof will be omitted.

【0027】 本考案では、高湿分炭を使用する場合には、節炭器バイパスダクト21を用い て、節炭器5を加熱して温度が下がる以前の温度の高い燃焼ガスを、一次空気供 給ダクト13の微粉炭ミル14入側へ直接導き、一次空気供給ダクト13及び加 熱一次空気供給ダクト15から微粉炭ミル14へ導入される空気10の温度を上 げるようにする。[0027] In this invention, when using high-moisture coal, a coal saver bypass duct 21 is used. The high-temperature combustion gas before its temperature is lowered by heating the energy saver 5 is supplied as primary air. Directly leads the supply duct 13 to the inlet side of the pulverized coal mill 14, and connects the primary air supply duct 13 and the processing The temperature of the air 10 introduced from the hot primary air supply duct 15 to the pulverized coal mill 14 is increased. make it grow.

【0028】 これにより、空気予熱器11へ供給される排ガス7の温度を変えることなく微 粉炭ミル14へ導入される空気10の温度を上げることができるので、空気予熱 器11出側の排ガス7の温度に影響を与えることが防止でき、しかも、空気予熱 器11を使用していないので熱交換効率の面から規制をうけることがなく高湿分 炭を充分に乾燥することができる。[0028] As a result, the temperature of the exhaust gas 7 supplied to the air preheater 11 can be slightly reduced without changing the temperature. Since the temperature of the air 10 introduced into the pulverized coal mill 14 can be increased, air preheating is possible. It is possible to prevent the temperature of the exhaust gas 7 on the outlet side of the vessel 11 from being affected, and to prevent air preheating. Since the heat exchanger 11 is not used, there are no regulations regarding heat exchange efficiency and high humidity can be avoided. Charcoal can be sufficiently dried.

【0029】 しかも、高湿分炭は一般に比較的若い炭であり乾燥すると自然発火を起こしや すいが、空気10に排ガス7を混合して微粉炭ミル14へ供給することにより酸 素濃度が低下するので、乾燥された高湿分炭の自然発火を防止することができる 。[0029] Moreover, high-humidity coal is generally relatively young coal and is susceptible to spontaneous combustion when dried. Water is mixed with air 10 and exhaust gas 7 and supplied to the pulverized coal mill 14 to produce acid. Since the elemental concentration decreases, spontaneous combustion of dried high-humidity coal can be prevented. .

【0030】 図2は、本考案の第二の実施例であり、加熱一次空気供給ダクト15等がない 構成とした他は、前記図1の実施例と同様の構成を備えており、このようにして も図1の実施例同様の作用・効果を得ることができる。本実施例の構造は、既存 の油焚ボイラで高湿分炭を使用できるように改造する場合に適している。[0030] FIG. 2 shows a second embodiment of the present invention, in which there is no heated primary air supply duct 15, etc. Other than the configuration, it has the same configuration as the embodiment shown in FIG. It is also possible to obtain the same functions and effects as the embodiment shown in FIG. The structure of this example is based on the existing Suitable for modifying oil-fired boilers to use high-moisture coal.

【0031】 尚、本考案は、上述の実施例にのみ限定されるものではなく、本考案の要旨を 逸脱しない範囲内において種々変更を加え得ることは勿論である。[0031] Note that the present invention is not limited to the above-mentioned embodiments, and the gist of the present invention is Of course, various changes can be made within the scope.

【0032】[0032]

【考案の効果】[Effect of the idea]

以上説明したように、本考案のボイラ装置によれば、空気予熱器出側の排ガス の温度に影響を与えずに高湿分炭を充分乾燥し得、しかも、乾燥された高湿分炭 の自然発火を防止できるという優れた効果を奏し得る。 As explained above, according to the boiler device of the present invention, the exhaust gas on the outlet side of the air preheater High-humidity coal can be sufficiently dried without affecting the temperature of the dry high-humidity coal. It can have an excellent effect of preventing spontaneous combustion.

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

【図1】本考案の第一の実施例の全体系統図である。FIG. 1 is an overall system diagram of a first embodiment of the present invention.

【図2】本考案の第二の実施例の全体系統図である。FIG. 2 is an overall system diagram of a second embodiment of the present invention.

【図3】従来例の全体系統図である。FIG. 3 is an overall system diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 ボイラ本体 2 火炉 3 バーナ 4 後部伝熱部 5 節炭器 10 空気 13 一次空気供給ダクト 14 微粉炭ミル 21 節炭器バイパスダクト 1 Boiler body 2 Furnace 3 burners 4 Rear heat transfer section 5. Carbon saver 10 Air 13 Primary air supply duct 14 Pulverized coal mill 21 Energy saving bypass duct

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 火炉にバーナを有すると共に後部伝熱部
に節炭器を有するボイラ本体と、石炭を微粉砕してバー
ナへ供給する燃料用の微粉炭を製造するための微粉炭ミ
ルと、微粉炭ミルへ微粉炭搬送用及び石炭乾燥用の空気
を供給する一次空気供給ダクトとを備えたボイラ装置に
おいて、後部伝熱部の節炭器入側と微粉炭ミルへ空気を
供給する一次空気供給ダクトとの間を節炭器バイパスダ
クトで接続したことを特徴とするボイラ装置。
Claim 1: A boiler body having a burner in the furnace and a coal saver in the rear heat transfer section; a pulverized coal mill for producing pulverized coal for fuel to be supplied to the burner by pulverizing coal; In a boiler device equipped with a primary air supply duct that supplies air for transporting pulverized coal and for drying coal to a pulverized coal mill, the primary air supply duct supplies air to the economizer inlet side of the rear heat transfer section and to the pulverized coal mill. A boiler device characterized in that a supply duct is connected to the supply duct by an energy saver bypass duct.
JP1991024673U 1991-03-20 1991-03-20 boiler equipment Pending JPH04115238U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1991024673U JPH04115238U (en) 1991-03-20 1991-03-20 boiler equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1991024673U JPH04115238U (en) 1991-03-20 1991-03-20 boiler equipment

Publications (1)

Publication Number Publication Date
JPH04115238U true JPH04115238U (en) 1992-10-13

Family

ID=31909566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1991024673U Pending JPH04115238U (en) 1991-03-20 1991-03-20 boiler equipment

Country Status (1)

Country Link
JP (1) JPH04115238U (en)

Similar Documents

Publication Publication Date Title
JPH0229372Y2 (en)
RU62341U1 (en) Dry Blast Furnace Drying Equipment
CN102047039A (en) Method of and system for generating power by oxyfuel combustion
CN106895390A (en) A kind of station boiler multi-element heterogeneous afterheat utilizing system
CN107420933B (en) Exhaust-heat primary air heat exchanger system for hot air powder feeding system of ball mill
CN103573311A (en) Steam exhaust energy utilizing system of driving steam turbine of thermal power plant and thermal power unit
CN210179607U (en) Combustion system for grinding high-moisture lignite by adopting medium-speed mill
JP2001041439A (en) Boiler
CN208253553U (en) A kind of system improving the wide load operation thermal efficiency of coal unit
CN206281365U (en) A kind of high-temp waste gas afterheat utilizing system
JP2002243110A (en) Pulverized coal boiler
JPH04115238U (en) boiler equipment
US20170023244A1 (en) Booster air heater for high moisture fuels
CN208418705U (en) A kind of pyrolysis installation
JPH04122933U (en) boiler equipment
CN219624088U (en) Adjusting system for temperature of medium-temperature SCR denitration flue gas
JPH025237Y2 (en)
CN217928780U (en) Circulating fluidized bed hot blast stove system
CN217274082U (en) Flue gas recirculation system
CN220601505U (en) Boiler flue gas flow regulating system based on flue gas recirculation
CN220379716U (en) Intermediate bin type pulverizing system for bituminous coal
CN215294990U (en) Boiler hot air circulating system
CN216976821U (en) System for heating boiler air inlet in starting stage
CN215892434U (en) System for heating primary air of boiler
JP2708795B2 (en) Combined plant