JPH11148630A - Electric dust collector ash collection method for heavy oil fired boiler - Google Patents

Electric dust collector ash collection method for heavy oil fired boiler

Info

Publication number
JPH11148630A
JPH11148630A JP9319895A JP31989597A JPH11148630A JP H11148630 A JPH11148630 A JP H11148630A JP 9319895 A JP9319895 A JP 9319895A JP 31989597 A JP31989597 A JP 31989597A JP H11148630 A JPH11148630 A JP H11148630A
Authority
JP
Japan
Prior art keywords
fired boiler
heavy oil
ash
dust collector
electric dust
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
JP9319895A
Other languages
Japanese (ja)
Inventor
Kenichi Tokumitsu
賢一 徳光
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
Ishikawajima Harima Heavy Industries 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 Ishikawajima Harima Heavy Industries Co Ltd filed Critical Ishikawajima Harima Heavy Industries Co Ltd
Priority to JP9319895A priority Critical patent/JPH11148630A/en
Publication of JPH11148630A publication Critical patent/JPH11148630A/en
Pending legal-status Critical Current

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  • Combustion Of Fluid Fuel (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)

Abstract

(57)【要約】 【課題】 電気集塵機で捕集された重油焚ボイラの灰を
微粉炭焚ボイラの火炉内で再燃焼させセメント原料等と
して再利用することができ、産業廃棄物の削減並びにコ
ストダウンを図り得る重油焚ボイラの電気集塵機捕集灰
処理方法を提供する。 【解決手段】 電気集塵機7で捕集された重油焚ボイラ
の灰を、灰搬送ライン9を介して微粉炭焚ボイラの火炉
1aのバーナ2近傍に設けられたポート10から該火炉
1a内へ投入し再燃焼させるよう構成する。
[57] [Abstract] [Problem] The ash of a heavy oil fired boiler collected by an electric dust collector can be reburned in a furnace of a pulverized coal fired boiler and reused as cement raw material, etc., thereby reducing industrial waste and Provided is a method for collecting ash from an electric dust collector for a heavy oil fired boiler, which can reduce the cost. SOLUTION: Heavy oil-fired boiler ash collected by an electric dust collector 7 is injected into a furnace 1a of a pulverized coal-fired boiler through a port 10 provided near a burner 2 through the ash transfer line 9 into the furnace 1a. And make it burn again.

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、重油焚ボイラの電
気集塵機捕集灰処理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for collecting ash from an electric dust collector of a heavy oil fired boiler.

【0002】[0002]

【従来の技術】図3は火力発電所等における重油焚或い
は微粉炭焚のボイラの一例を表すものであって、図中、
1は火炉1aと後部伝熱部1bとを備えたボイラ本体、
2は重油或いは微粉炭等の主燃料が噴出されるバーナ、
3は燃焼用空気を圧送する押込通風機、4は押込通風機
3から圧送される燃焼用空気をバーナ2へ導く空気ライ
ン、5はボイラ本体1の後部伝熱部1bから延びる排ガ
スライン、6は空気ライン4を流れる燃焼用空気を排ガ
スライン5を流れる排ガスによって加熱するための空気
予熱器、7はボイラ本体1から排出される排ガス中に含
まれる灰を捕集するための電気集塵機、8は煙突であ
る。
2. Description of the Related Art FIG. 3 shows an example of a heavy oil fired or pulverized coal fired boiler in a thermal power plant or the like.
1 is a boiler body provided with a furnace 1a and a rear heat transfer section 1b,
2 is a burner from which main fuel such as heavy oil or pulverized coal is jetted out,
Reference numeral 3 denotes a forced air ventilator for feeding the combustion air, 4 denotes an air line for guiding the combustion air fed from the forced air vent 3 to the burner 2, 5 denotes an exhaust gas line extending from the rear heat transfer portion 1b of the boiler main body 1, 6 Is an air preheater for heating the combustion air flowing in the air line 4 with the exhaust gas flowing in the exhaust gas line 5; 7 is an electric precipitator for collecting ash contained in the exhaust gas discharged from the boiler body 1; Is a chimney.

【0003】前述の如きボイラにおいては、押込通風機
3で昇圧され空気予熱器6を通過して加熱された燃焼用
空気が空気ライン4を介してバーナ2からボイラ本体1
の火炉1a内へ導入されると共に、重油或いは微粉炭等
の主燃料がバーナ2からボイラ本体1の火炉1a内へ供
給されて燃焼が行われ、ボイラ本体1の火炉1a内での
燃焼により発生した排ガスは、図示していない過熱器及
び節炭器等を備えた後部伝熱部1bにおいて熱回収され
てから排ガスライン5に流出し、空気予熱器6で前記空
気ライン4の燃焼用空気と熱交換することにより更に冷
却され、電気集塵機7で灰が捕集された後、煙突8から
大気に放出される。
In the boiler as described above, the combustion air heated by the pressurized ventilator 3 and passed through the air preheater 6 is heated from the burner 2 via the air line 4 to the boiler body 1.
And the main fuel such as heavy oil or pulverized coal is supplied from the burner 2 into the furnace 1a of the boiler body 1 and burns, and is generated by the combustion of the boiler body 1 in the furnace 1a. The exhaust gas thus collected is heat-recovered in a rear heat transfer section 1b provided with a superheater and a economizer (not shown) and then flows out to an exhaust gas line 5, where the air is heated by an air preheater 6 and the combustion air of the air line 4 is removed. The ash is further cooled by the heat exchange, and the ash is collected by the electric precipitator 7 and then discharged to the atmosphere from the chimney 8.

【0004】前記ボイラが微粉炭焚の場合、電気集塵機
7で捕集された灰は、セメント原料等としてリサイクル
可能であるが、前記ボイラが重油焚の場合、電気集塵機
7で捕集された灰は、未燃カーボンが主成分であり、微
粉炭焚ボイラのようにセメント原料等として再利用する
ことができないため、産業廃棄物として埋め立て等によ
り処理しているのが現状であった。
[0004] When the boiler is pulverized coal fired, the ash collected by the electric dust collector 7 can be recycled as a cement raw material or the like. However, when the boiler is heavy oil fired, the ash collected by the electric dust collector 7 is used. Is mainly composed of unburned carbon and cannot be reused as a cement raw material or the like as in a pulverized coal-fired boiler, and is currently treated as industrial waste by landfill.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、前述の
如く、電気集塵機7で捕集された重油焚ボイラの灰を産
業廃棄物として埋め立て等により処理するのでは、処分
場所を確保したり或いは産業廃棄物処理業者に処理を委
託したりしなければならなくなり、コストアップにつな
がるという欠点を有していた。
However, as mentioned above, if the ash of the heavy oil fired boiler collected by the electric dust collector 7 is treated as landfill by industrial landfill, it is necessary to secure a disposal place or to dispose of the industrial waste. There is a drawback that the processing must be entrusted to a material processing company, which leads to an increase in cost.

【0006】本発明は、斯かる実情に鑑み、電気集塵機
で捕集された重油焚ボイラの灰を微粉炭焚ボイラの火炉
内で再燃焼させセメント原料等として再利用することが
でき、産業廃棄物の削減並びに灰の処理費用と微粉炭焚
ボイラの燃料費の節約によるコストダウンを図り得る重
油焚ボイラの電気集塵機捕集灰処理方法を提供しようと
するものである。
[0006] In view of such circumstances, the present invention allows the ash of a heavy oil fired boiler collected by an electric dust collector to be reburned in a furnace of a pulverized coal fired boiler and reused as a cement raw material, etc. An object of the present invention is to provide a method for collecting ash from an electric dust collector of a heavy oil fired boiler, which can reduce costs by reducing the amount of ash, the cost of treating ash, and the fuel cost of the pulverized coal fired boiler.

【0007】[0007]

【課題を解決するための手段】第一の発明は、重油焚ボ
イラから排出される排ガス中に含まれる灰を捕集するた
めの電気集塵機を備えた重油焚ボイラの電気集塵機捕集
灰処理方法であって、電気集塵機で捕集された重油焚ボ
イラの灰を微粉炭焚ボイラの火炉へ投入し再燃焼させる
ことを特徴とする重油焚ボイラの電気集塵機捕集灰処理
方法にかかるものである。
SUMMARY OF THE INVENTION The first invention is a method for collecting ash from an electric dust collector of a heavy oil fired boiler, which is provided with an electric dust collector for collecting ash contained in exhaust gas discharged from the heavy oil fired boiler. Wherein the ash of the heavy oil fired boiler collected by the electric dust collector is charged into the furnace of the pulverized coal fired boiler and reburned, and the method is applied to the method of collecting ash from the heavy oil fired boiler. .

【0008】第二の発明は、重油焚ボイラから排出され
る排ガス中に含まれる灰を捕集するための電気集塵機を
備えた重油焚ボイラの電気集塵機捕集灰処理方法であっ
て、電気集塵機で捕集された重油焚ボイラの灰を微粉炭
焚ボイラのバーナから微粉炭と一緒に火炉へ投入し再燃
焼させることを特徴とする重油焚ボイラの電気集塵機捕
集灰処理方法にかかるものである。
[0008] The second invention is an electric dust collector ash collection method for a heavy oil fired boiler provided with an electric dust collector for collecting ash contained in the exhaust gas discharged from the heavy oil fired boiler. The ash collected from the fuel oil-fired boiler from the burner of the coal-fired coal-fired boiler is put into a furnace together with the coal powder and reburned, and the method is applied to a method for collecting ash from an electric dust collector of a fuel oil-fired boiler. is there.

【0009】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0010】第一の発明においては、電気集塵機で捕集
された重油焚ボイラの灰は、微粉炭焚ボイラの火炉へ投
入され再燃焼され、微粉炭焚ボイラにおける電気集塵機
で捕集された灰は、セメント原料等として再利用され
る。
[0010] In the first invention, the ash of the heavy oil fired boiler collected by the electric dust collector is charged into the furnace of the pulverized coal fired boiler and reburned, and the ash collected by the electric dust collector in the pulverized coal fired boiler is collected. Is reused as a raw material for cement and the like.

【0011】第二の発明においては、電気集塵機で捕集
された重油焚ボイラの灰は、微粉炭焚ボイラのバーナか
ら微粉炭と一緒に火炉へ投入され再燃焼され、微粉炭焚
ボイラにおける電気集塵機で捕集された灰は、セメント
原料等として再利用される。
[0011] In the second invention, the ash of the heavy oil fired boiler collected by the electric dust collector is put into a furnace together with the pulverized coal from the burner of the pulverized coal fired boiler and reburned, and the electric power in the pulverized coal fired boiler is reduced. The ash collected by the dust collector is reused as a raw material for cement and the like.

【0012】この結果、第一の発明並びに第二の発明に
おいては、電気集塵機で捕集された重油焚ボイラの灰を
産業廃棄物として埋め立て等により処理する必要がなく
なり、処分場所を確保したり或いは産業廃棄物処理業者
に処理を委託したりしなくて済み、コストダウンにつな
がる。
As a result, in the first invention and the second invention, it is not necessary to dispose of the ash of the heavy oil-fired boiler collected by the electric dust collector as industrial waste by landfill or the like, and it is possible to secure a disposal place. Alternatively, it is not necessary to outsource the treatment to an industrial waste disposal company, which leads to cost reduction.

【0013】[0013]

【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0014】図1は本発明を実施する形態の一例であっ
て、図中、図3と同一の符号を付した部分は同一物を表
しており、基本的な構成は図3に示す従来のものと同様
であるが、本図示例の特徴とするところは、図1に示す
如く、電気集塵機7で捕集された重油焚ボイラの灰を、
灰搬送ライン9を介して微粉炭焚ボイラの火炉1aのバ
ーナ2近傍に設けられたポート10から該火炉1a内へ
投入し再燃焼させるよう構成した点にある。
FIG. 1 shows an example of an embodiment of the present invention. In the figure, portions denoted by the same reference numerals as those in FIG. 3 represent the same components, and the basic configuration is the same as that of the conventional device shown in FIG. As shown in FIG. 1, the ash of the heavy oil fired boiler collected by the electric dust collector 7 is the same as that of FIG.
The point is that it is configured to be injected into the furnace 1a from a port 10 provided near the burner 2 of the furnace 1a of the pulverized coal-fired boiler via the ash transfer line 9 and reburn.

【0015】本図示例の場合、ポート10は、微粉炭焚
ボイラの火炉1aのバーナ2の上方に設けてあるが、熱
負荷の高い位置であれば、微粉炭焚ボイラの火炉1aの
バーナ2の下方に設けるようにしてもよいことは言うま
でもない。
In the illustrated example, the port 10 is provided above the burner 2 of the furnace 1a of the pulverized coal-fired boiler. If the heat load is high, the port 10 is connected to the burner 2 of the furnace 1a of the pulverized coal-fired boiler. It is needless to say that it may be provided below.

【0016】尚、図中、11は電気集塵機7で捕集され
た重油焚ボイラの灰を搬送するためのコンプレッサ、1
2は電気集塵機7の下流側に設けられた誘引通風機であ
る。
In the figure, reference numeral 11 denotes a compressor for conveying the ash of the heavy oil fired boiler collected by the electric dust collector 7;
Reference numeral 2 denotes an induction ventilator provided downstream of the electric dust collector 7.

【0017】次に、上記図示例の作動を説明する。Next, the operation of the illustrated example will be described.

【0018】重油焚ボイラ並びに微粉炭焚ボイラにおい
てはそれぞれ、押込通風機3で昇圧され空気予熱器6を
通過して加熱された燃焼用空気が空気ライン4を介して
バーナ2からボイラ本体1の火炉1a内へ導入されると
共に、主燃料(重油焚ボイラにおいては重油であり、微
粉炭焚ボイラにおいては微粉炭)がバーナ2からボイラ
本体1の火炉1a内へ供給されて燃焼が行われ、ボイラ
本体1の火炉1a内での燃焼により発生した排ガスは、
図示していない過熱器及び節炭器等を備えた後部伝熱部
1bにおいて熱回収されてから排ガスライン5に流出
し、空気予熱器6で前記空気ライン4の燃焼用空気と熱
交換することにより更に冷却され、電気集塵機7で灰が
捕集された後、煙突8から大気に放出されるが、前記電
気集塵機7で捕集された重油焚ボイラの灰は、コンプレ
ッサ11の作動により灰搬送ライン9を介して搬送さ
れ、微粉炭焚ボイラの火炉1aのバーナ2近傍に設けら
れたポート10から該火炉1a内へ投入され、バーナ2
から噴出される微粉炭と一緒に再燃焼される。
In the heavy oil fired boiler and the pulverized coal fired boiler, the combustion air heated by the pressurized air blower 3 and passed through the air preheater 6 is passed through the air line 4 from the burner 2 to the boiler body 1. While being introduced into the furnace 1a, the main fuel (heavy oil in a heavy oil-fired boiler, pulverized coal in a pulverized coal-fired boiler) is supplied from the burner 2 into the furnace 1a of the boiler main body 1, where combustion is performed. The exhaust gas generated by the combustion of the boiler body 1 in the furnace 1a is as follows:
Heat is recovered in the rear heat transfer section 1b provided with a superheater and a economizer (not shown) and then flows out to the exhaust gas line 5, where heat exchange with the combustion air in the air line 4 is performed by the air preheater 6. After the ash is collected by the electric precipitator 7, the ash is released to the atmosphere from the chimney 8. It is conveyed through the line 9 and is charged into the furnace 1a through a port 10 provided near the burner 2 of the furnace 1a of the pulverized coal-fired boiler.
It is reburned together with the pulverized coal escaping from the coal.

【0019】ここで、前記電気集塵機7で捕集された重
油焚ボイラの灰は、約6000[kcal/kg]の発
熱量を有し、これは微粉炭の発熱量と略同等である一
方、前記電気集塵機7で捕集された重油焚ボイラの灰の
粒径は、およそ10〜100[μm]程度であって、こ
れも微粉炭の粒径と略同等であり、前記電気集塵機7で
捕集された重油焚ボイラの灰と微粉炭との混焼が可能で
あることは、基礎燃焼試験炉において実際に確認されて
いる。
Here, the ash of the heavy oil fired boiler collected by the electric dust collector 7 has a calorific value of about 6000 kcal / kg, which is substantially equal to the calorific value of the pulverized coal. The particle size of the ash of the heavy oil fired boiler collected by the electric dust collector 7 is about 10 to 100 [μm], which is also substantially equal to the particle size of the pulverized coal. It has been actually confirmed in a basic combustion test furnace that co-firing of collected ash and pulverized coal from a heavy oil-fired boiler is possible.

【0020】又、前記電気集塵機7で捕集された重油焚
ボイラの灰の微粉炭に対する混焼率は、およそ2〜5%
程度に設定すればよく、この程度の混焼率とすれば、重
油焚ボイラの灰は略全量処理することが可能であり、し
かも、微粉炭焚ボイラにおける電気集塵機7で捕集され
た灰をセメント原料等として再利用することにも何等支
障を来すことはない。
The co-firing rate of the ash of the heavy oil-fired boiler collected by the electric dust collector 7 with respect to the pulverized coal is approximately 2 to 5%.
At this level of co-firing, it is possible to treat almost all of the ash from the heavy oil-fired boiler, and the ash collected by the electric dust collector 7 in the pulverized coal-fired boiler is cemented. There is no hindrance to reusing it as a raw material.

【0021】この結果、電気集塵機7で捕集された重油
焚ボイラの灰を産業廃棄物として埋め立て等により処理
する必要がなくなり、処分場所を確保したり或いは産業
廃棄物処理業者に処理を委託したりしなくて済み、コス
トダウンにつながる。
As a result, it is not necessary to dispose of the ash of the heavy oil fired boiler collected by the electric precipitator 7 as landfill, etc., and it is not necessary to secure a disposal place or to entrust the treatment to an industrial waste disposal company. It eliminates the need for waste, leading to cost reduction.

【0022】こうして、電気集塵機7で捕集された重油
焚ボイラの灰を微粉炭焚ボイラの火炉1a内で再燃焼さ
せセメント原料等として再利用することができ、産業廃
棄物の削減並びにコストダウンを図り得る。
In this way, the ash of the heavy oil fired boiler collected by the electric dust collector 7 can be reburned in the furnace 1a of the pulverized coal fired boiler and reused as cement raw material, etc., thereby reducing industrial waste and cost. Can be achieved.

【0023】図2は本発明を実施する形態の他の例であ
って、図中、図1と同一の符号を付した部分は同一物を
表わしており、電気集塵機7で捕集された重油焚ボイラ
の灰を、灰搬送ライン9を介して微粉炭焚ボイラの少な
くとも一つのバーナ2から微粉炭と一緒に火炉1aへ投
入し再燃焼させるよう構成したものである。
FIG. 2 shows another example of the embodiment of the present invention. In the figure, the portions denoted by the same reference numerals as those in FIG. 1 represent the same components, and the heavy oil collected by the electric dust collector 7 The ash of the boiler is fed into the furnace 1a together with the pulverized coal from at least one burner 2 of the pulverized coal-fired boiler via the ash transfer line 9 and reburned.

【0024】図2に示す例においては、電気集塵機7で
捕集された重油焚ボイラの灰は、コンプレッサ11の作
動により灰搬送ライン9を介して搬送され、微粉炭焚ボ
イラのバーナ2から微粉炭と一緒に火炉1a内へ投入さ
れ再燃焼され、微粉炭焚ボイラにおける電気集塵機7で
捕集された灰は、セメント原料等として再利用される。
In the example shown in FIG. 2, the ash of the heavy oil-fired boiler collected by the electric dust collector 7 is conveyed through the ash conveying line 9 by the operation of the compressor 11 and is pulverized from the burner 2 of the pulverized coal-fired boiler. The ash charged into the furnace 1a together with the charcoal and reburned, and collected by the electric precipitator 7 in the pulverized coal-fired boiler is reused as a cement raw material or the like.

【0025】この結果、図2に示す例においても、図1
に示す例と同様、電気集塵機7で捕集された重油焚ボイ
ラの灰を産業廃棄物として埋め立て等により処理する必
要がなくなり、処分場所を確保したり或いは産業廃棄物
処理業者に処理を委託したりしなくて済み、コストダウ
ンにつながる。
As a result, in the example shown in FIG.
As in the example shown in (1), there is no need to dispose of the ash of the heavy oil fired boiler collected by the electric dust collector 7 as landfill, thereby securing a disposal place or entrusting the treatment to an industrial waste disposal contractor. It eliminates the need for waste, leading to cost reduction.

【0026】こうして、図2に示す例の場合も、図1に
示す例の場合と同様、電気集塵機7で捕集された重油焚
ボイラの灰を微粉炭焚ボイラの火炉1a内で再燃焼させ
セメント原料等として再利用することができ、産業廃棄
物の削減並びにコストダウンを図り得る。
Thus, in the case of the example shown in FIG. 2, as in the case of the example shown in FIG. 1, the ash of the heavy oil fired boiler collected by the electric dust collector 7 is reburned in the furnace 1a of the pulverized coal fired boiler. It can be reused as a raw material for cement and the like, which can reduce industrial waste and cost.

【0027】尚、本発明の重油焚ボイラの電気集塵機捕
集灰処理方法は、上述の図示例にのみ限定されるもので
はなく、本発明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。
The method for collecting ash from an electric dust collector of a heavy oil fired boiler according to the present invention is not limited to the illustrated example described above, and various modifications can be made without departing from the gist of the present invention. Of course.

【0028】[0028]

【発明の効果】以上、説明したように本発明の重油焚ボ
イラの電気集塵機捕集灰処理方法によれば、電気集塵機
で捕集された重油焚ボイラの灰を微粉炭焚ボイラの火炉
内で再燃焼させセメント原料等として再利用することが
でき、産業廃棄物の削減並びにコストダウンを図り得る
という優れた効果を奏し得る。
As described above, according to the method for collecting ash from an electric dust collector of a heavy oil fired boiler according to the present invention, the ash of the heavy oil fired boiler collected by the electric dust collector is placed in the furnace of the pulverized coal fired boiler. It can be re-burned and reused as a cement raw material and the like, and an excellent effect of reducing industrial waste and reducing costs can be achieved.

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

【図1】本発明を実施する形態の一例の全体概要構成図
である。
FIG. 1 is an overall schematic configuration diagram of an example of an embodiment of the present invention.

【図2】本発明を実施する形態の他の例の全体概要構成
図である。
FIG. 2 is an overall schematic configuration diagram of another example of an embodiment of the present invention.

【図3】従来例の全体概要構成図である。FIG. 3 is an overall schematic configuration diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 ボイラ本体 1a 火炉 2 バーナ 7 電気集塵機 9 灰搬送ライン 10 ポート 11 コンプレッサ DESCRIPTION OF SYMBOLS 1 Boiler main body 1a Furnace 2 Burner 7 Electric precipitator 9 Ash transport line 10 Port 11 Compressor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 重油焚ボイラから排出される排ガス中に
含まれる灰を捕集するための電気集塵機を備えた重油焚
ボイラの電気集塵機捕集灰処理方法であって、電気集塵
機で捕集された重油焚ボイラの灰を微粉炭焚ボイラの火
炉へ投入し再燃焼させることを特徴とする重油焚ボイラ
の電気集塵機捕集灰処理方法。
1. A method for collecting ash from a heavy oil-fired boiler provided with an electric dust collector for collecting ash contained in exhaust gas discharged from a heavy oil-fired boiler, wherein the ash is collected by the electric dust collector. A method for collecting ash from an electric dust collector for a heavy oil fired boiler, wherein the ash from the heavy oil fired boiler is put into a furnace of a pulverized coal fired boiler and reburned.
【請求項2】 重油焚ボイラから排出される排ガス中に
含まれる灰を捕集するための電気集塵機を備えた重油焚
ボイラの電気集塵機捕集灰処理方法であって、電気集塵
機で捕集された重油焚ボイラの灰を微粉炭焚ボイラのバ
ーナから微粉炭と一緒に火炉へ投入し再燃焼させること
を特徴とする重油焚ボイラの電気集塵機捕集灰処理方
法。
2. A method for collecting ash from a heavy oil fired boiler provided with an electric dust collector for collecting ash contained in exhaust gas discharged from a heavy oil fired boiler, wherein the method is performed by an electric dust collector. A method for collecting ash from an electric dust collector for a heavy oil fired boiler, wherein the ash from the heavy oil fired boiler is put into a furnace together with the fine coal from the burner of the pulverized coal fired boiler and reburned.
JP9319895A 1997-11-20 1997-11-20 Electric dust collector ash collection method for heavy oil fired boiler Pending JPH11148630A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9319895A JPH11148630A (en) 1997-11-20 1997-11-20 Electric dust collector ash collection method for heavy oil fired boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9319895A JPH11148630A (en) 1997-11-20 1997-11-20 Electric dust collector ash collection method for heavy oil fired boiler

Publications (1)

Publication Number Publication Date
JPH11148630A true JPH11148630A (en) 1999-06-02

Family

ID=18115438

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9319895A Pending JPH11148630A (en) 1997-11-20 1997-11-20 Electric dust collector ash collection method for heavy oil fired boiler

Country Status (1)

Country Link
JP (1) JPH11148630A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6427597B1 (en) 2000-01-27 2002-08-06 Patrice M. Aurenty Method of controlling image resolution on a substrate
JP2007333347A (en) * 2006-06-16 2007-12-27 Chugoku Electric Power Co Inc:The Method for improving dust collecting efficiency of dust collector
CN110500609A (en) * 2019-08-23 2019-11-26 润电能源科学技术有限公司 A kind of boiler waste heat utilization system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6427597B1 (en) 2000-01-27 2002-08-06 Patrice M. Aurenty Method of controlling image resolution on a substrate
JP2007333347A (en) * 2006-06-16 2007-12-27 Chugoku Electric Power Co Inc:The Method for improving dust collecting efficiency of dust collector
CN110500609A (en) * 2019-08-23 2019-11-26 润电能源科学技术有限公司 A kind of boiler waste heat utilization system
CN110500609B (en) * 2019-08-23 2021-05-04 润电能源科学技术有限公司 Boiler waste heat utilization system

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