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JPH0348405B2 - - Google Patents
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JPH0348405B2 - - Google Patents

Info

Publication number
JPH0348405B2
JPH0348405B2 JP24481683A JP24481683A JPH0348405B2 JP H0348405 B2 JPH0348405 B2 JP H0348405B2 JP 24481683 A JP24481683 A JP 24481683A JP 24481683 A JP24481683 A JP 24481683A JP H0348405 B2 JPH0348405 B2 JP H0348405B2
Authority
JP
Japan
Prior art keywords
coal
temperature
combustion
hot
hot air
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
JP24481683A
Other languages
Japanese (ja)
Other versions
JPS60140005A (en
Inventor
Koichi Ushio
Jiro Tamura
Masahiko Takashima
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP24481683A priority Critical patent/JPS60140005A/en
Publication of JPS60140005A publication Critical patent/JPS60140005A/en
Publication of JPH0348405B2 publication Critical patent/JPH0348405B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C1/00Combustion apparatus specially adapted for combustion of two or more kinds of fuel simultaneously or alternately, at least one kind of fuel being either a fluid fuel or a solid fuel suspended in a carrier gas or air

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Fuel Combustion (AREA)
  • Combustion Of Fluid Fuel (AREA)

Description

【発明の詳細な説明】 本発明は石炭を燃料とする石炭焚熱風炉に関す
るものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coal-fired hot air stove that uses coal as fuel.

第1図は代表的なストーカ式石炭燃焼炉からな
る石炭焚熱風炉を示すものであり、石炭焚熱風炉
で発生させた熱風は、例えば、石灰石などの焼成
炉へ送風されて利用されるようになつている。第
1図において、1は給炭機、2はスプレツダ、3
は図において反時計回り方向へ回転する移動式の
グレード、4は石炭灰取出フイーダ、5は1次空
気を取入れる燃焼用空気取入口、6は2次空気を
取入れる燃焼用空気吹込口、7は熱風取出ダクト
で、炉内は耐火レンガ8で内張りされている。
Figure 1 shows a coal-fired hot-air stove consisting of a typical stoker-type coal-fired furnace. It's getting old. In Figure 1, 1 is a coal feeder, 2 is a spreader, and 3 is a coal feeder.
is a movable grade that rotates counterclockwise in the figure, 4 is a coal ash removal feeder, 5 is a combustion air intake that takes in primary air, 6 is a combustion air inlet that takes in secondary air, 7 is a hot air extraction duct, and the inside of the furnace is lined with firebrick 8.

このストーカ式石炭燃焼炉は、さまざまな粒径
の石炭を燃焼する。そのため、給炭機1により供
給された石炭は、スプレツダ2により炉内に投炭
される。石炭の粒径は大きいほど燃焼時間は長
く、小さい径のものほど早く燃焼するので、大き
い径のものは遠くへ、小さい径のものは手前へ散
布され、グレード3は、投炭方向と逆方向へ移動
する。従つて、あらゆる粒径の石炭も炉内で完全
に燃焼される。
This stoker-type coal combustion furnace burns coal of various particle sizes. Therefore, the coal supplied by the coal feeder 1 is thrown into the furnace by the spreader 2. The larger the particle size of coal, the longer the combustion time, and the smaller the particle size, the faster it burns, so large diameter coal is scattered far away, small diameter coal is scattered towards you, and grade 3 is scattered in the opposite direction to the coal throwing direction. Move to. Therefore, coal of any particle size is completely combusted in the furnace.

燃焼用空気の一部は1次空気として、燃焼用空
気取入口5より供給され、グレード3を冷却した
後、グレード上の石炭層へ通風される。残りの燃
焼空気は2次空気として炉内側壁に開孔された多
数の燃焼用空気吹込口より供給され、石炭層上面
に吹き付けられる。
A part of the combustion air is supplied as primary air from the combustion air intake port 5, and after cooling grade 3, it is ventilated to the coal seam above the grade. The remaining combustion air is supplied as secondary air through a number of combustion air blowing holes formed in the inner wall of the furnace, and is blown onto the upper surface of the coal seam.

炉の燃焼コントロールと、熱風温度の調整は、
主として、この2種類の燃焼用空気量、グレート
の移動速度、給炭機による石炭給炭量、および、
スプレツダの回転数の制御によつて調整される。
Furnace combustion control and hot air temperature adjustment are
Mainly, the amount of combustion air for these two types, the moving speed of the grate, the amount of coal fed by the coal feeder, and
Adjusted by controlling the rotation speed of the spreader.

このような石炭燃焼炉は、高い燃焼効率で高温
ガスを発生する事が出来るが、燃焼ガス温度の変
動、および、石炭灰の溶融によるクリンカトラブ
ルという弱点を持つている。その主たる原因に、
燃料石炭の性状変化に伴う燃焼ガスの変化が、石
炭燃焼炉本体での調整では困難という事が挙げら
れる。従つて、温度変動の許されない用途および
より高温条件での用途には、ストーカ式石炭焚熱
風炉の使用は困難とされていた。
Although such a coal combustion furnace can generate high temperature gas with high combustion efficiency, it has drawbacks such as fluctuations in combustion gas temperature and clinker trouble due to melting of coal ash. The main cause is
One problem is that it is difficult to adjust the changes in combustion gas due to changes in the properties of fuel coal in the coal combustion furnace itself. Therefore, it has been difficult to use a stoker-type coal-fired hot air stove for applications where temperature fluctuations are not allowed or where higher temperature conditions are required.

すなわち、その欠点は、つぎのとおりである。 That is, its drawbacks are as follows.

(1) 石炭性状変化に伴う燃焼ガス温度の変動に対
する調整が困難。
(1) Difficult to adjust for fluctuations in combustion gas temperature due to changes in coal properties.

(2) 石炭灰溶融点以上の高温ガスの発生が不可
能。
(2) It is impossible to generate gas at a temperature higher than the melting point of coal ash.

(3) 石炭灰の溶融によるクリンカトラブルの発
生。
(3) Clinker trouble occurs due to melting of coal ash.

本発明は、以上のような欠点を解消して、スト
ーカ式石炭焚熱風炉の用途範囲を拡大したもの
で、以下図面に示す実施例によつてその詳細を説
明する。
The present invention solves the above-mentioned drawbacks and expands the scope of application of the stoker-type coal-fired hot air stove, and details thereof will be explained below with reference to embodiments shown in the drawings.

第2図は本発明の1実施例を示す縦断面図であ
り、図中、第1図と同一部分には同一符号を付
し、その説明は省略する。
FIG. 2 is a longitudinal cross-sectional view showing one embodiment of the present invention. In the figure, the same parts as those in FIG.

第2図において、符号9で示すものは、ストー
カ式石炭燃焼炉の上部に設けた熱風取出部である
熱ガスダクト13部において、熱風取出方向に向
けて取付けた補助バーナであり、石炭燃焼後の熱
風を均等に昇温する適正位置に取付けられる。こ
の補助バーナ9は、燃量の微調整が可能な流体燃
料、すなわち、液体および気体の燃料を使用して
いる。補助バーナ9へは配管10を介して補助燃
料源12から流体燃料が送られる。配管10の途
中には流量調整用自動バルブ11が設けられてい
る。さらに、補助バーナ9により昇温された熱風
の温度を測定するため、熱ガスダクト13の適正
位置に、温度計14が設置されている。又、流量
調整用自動バルブ11を制御するための温度設定
器15が設置され、温度計14より熱ガスダクト
13内の温度がフイードバツクされ、あらかじめ
設定された温度になるように、流量調整用自動バ
ルブ11の開度を制御する。温度計14、温度設
定器15、流量調整用自動バルブ11等は、熱風
取出部の温度に応じて、補助バーナ9による燃焼
状態を制御して一定温度の熱風を発生させる熱風
温度制御装置を形成している。
In Fig. 2, the reference numeral 9 is an auxiliary burner installed in the hot air extraction direction in the hot gas duct 13, which is the hot air extraction part provided at the top of the stoker-type coal combustion furnace. It can be installed in an appropriate position to raise the temperature of hot air evenly. This auxiliary burner 9 uses fluid fuel whose fuel amount can be finely adjusted, that is, liquid and gas fuel. Fluid fuel is sent to the auxiliary burner 9 via a pipe 10 from an auxiliary fuel source 12 . An automatic valve 11 for flow rate adjustment is provided in the middle of the pipe 10. Further, in order to measure the temperature of the hot air heated by the auxiliary burner 9, a thermometer 14 is installed at an appropriate position in the hot gas duct 13. Further, a temperature setting device 15 is installed to control the automatic valve 11 for adjusting the flow rate, and the temperature inside the hot gas duct 13 is fed back from the thermometer 14, and the automatic valve for adjusting the flow rate is set to a preset temperature. 11 is controlled. The thermometer 14, temperature setting device 15, automatic flow rate adjustment valve 11, etc. form a hot air temperature control device that controls the combustion state of the auxiliary burner 9 and generates hot air at a constant temperature according to the temperature of the hot air outlet. are doing.

このような構造を採用すると、石炭性状の変化
又はストーカ式石炭燃焼炉内での状況変化等に伴
う燃焼ガスの変動があつても、発生する熱風は常
に一定の温度に保持出来る。又、石炭灰の溶融に
より、熱風温度に制限があつたものが、この補助
バーナの作用により、さらに高温にする事が出来
る。さらに、ストーカ式石炭燃焼炉の熱風温度を
任意に低く出来るので、クリンカトラブルがなく
なり、石炭燃焼炉は、従来のように、炉内に付着
したクリンカ除去のための操業停止をしなくても
よいため、効率の良い連続操業が可能となつた。
さらに、熱風取出ダクト7を必要数に分岐し、そ
の各々を本装置を採用する事により、1基の石炭
燃焼炉より、必要温度に応じた数種類の熱風を取
出す事が出来る。
If such a structure is adopted, the generated hot air can always be maintained at a constant temperature even if there are fluctuations in combustion gas due to changes in coal properties or changes in conditions within the stoker type coal combustion furnace. Furthermore, the temperature of the hot air, which is limited due to the melting of coal ash, can be increased to a higher temperature by the action of this auxiliary burner. Furthermore, since the hot air temperature of the stoker-type coal combustion furnace can be lowered arbitrarily, clinker troubles are eliminated, and coal combustion furnaces do not have to shut down to remove clinker that has adhered to the inside of the furnace, unlike conventional methods. This enabled efficient continuous operation.
Furthermore, by branching the hot air extraction duct 7 into the required number and employing this device for each of them, several types of hot air can be extracted from one coal combustion furnace depending on the required temperature.

以上の説明で明らかなように、本発明によれ
ば、ストーカ式石炭燃焼炉の熱風取出ダクト部に
おいて、補助バーナを設置し、かつ、熱風取出ダ
クト内の温度が所望の値になるように補助バーナ
による燃焼状態を制御しうるようにしたので、石
炭性状の変化および石炭燃焼炉内の状況変化に関
係なく、一定の高温熱風を供給でき、また、従来
のように、クリンカトラブルにより炉の操業を停
止しなくても良いため、効率の良い操業を行うこ
とができるという優れた効果が得られる。
As is clear from the above description, according to the present invention, an auxiliary burner is installed in the hot air extraction duct of a stoker-type coal combustion furnace, and an auxiliary burner is installed to assist the temperature inside the hot air extraction duct to a desired value. Since the combustion state of the burner can be controlled, a constant high-temperature hot air can be supplied regardless of changes in coal properties or conditions inside the coal combustion furnace. Since there is no need to stop the operation, an excellent effect can be obtained in that efficient operation can be performed.

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

第1図は従来構造を説明する縦断面図、第2図
は本発明の一実施例を示す縦断面図。 1……給炭機、2……スプレツダ、3……移動
式グレート、4……石炭灰取出フイーダ、5,6
……燃焼用空気取入口、7……熱風取出ダクト、
9……補助バーナ、11……流量調整用自動バル
ブ、12……補助燃料源、13……熱ガスダク
ト、14……温度計、15……温度設定器。
FIG. 1 is a vertical cross-sectional view illustrating a conventional structure, and FIG. 2 is a vertical cross-sectional view showing an embodiment of the present invention. 1... Coal feeder, 2... Spreader, 3... Mobile grate, 4... Coal ash removal feeder, 5, 6
...Combustion air intake, 7...Hot air extraction duct,
9... Auxiliary burner, 11... Automatic valve for flow rate adjustment, 12... Auxiliary fuel source, 13... Hot gas duct, 14... Thermometer, 15... Temperature setting device.

Claims (1)

【特許請求の範囲】[Claims] 1 ストーカ式石炭燃焼炉の熱風取出部に補助バ
ーナを設置し、熱風取出部の温度に応じて補助バ
ーナによる燃焼状態を制御して一定温度の熱風を
発生させる熱風温度制御装置を備えた石炭焚熱風
炉。
1. A coal-fired coal-fired furnace equipped with a hot-air temperature control device that installs an auxiliary burner in the hot-air outlet of a stoker-type coal combustion furnace and controls the combustion state of the auxiliary burner according to the temperature of the hot-air outlet to generate hot air at a constant temperature. Hot stove.
JP24481683A 1983-12-27 1983-12-27 Coal burning air heating furnace Granted JPS60140005A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24481683A JPS60140005A (en) 1983-12-27 1983-12-27 Coal burning air heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24481683A JPS60140005A (en) 1983-12-27 1983-12-27 Coal burning air heating furnace

Publications (2)

Publication Number Publication Date
JPS60140005A JPS60140005A (en) 1985-07-24
JPH0348405B2 true JPH0348405B2 (en) 1991-07-24

Family

ID=17124374

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24481683A Granted JPS60140005A (en) 1983-12-27 1983-12-27 Coal burning air heating furnace

Country Status (1)

Country Link
JP (1) JPS60140005A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6351389B2 (en) * 2014-06-10 2018-07-04 大阪瓦斯株式会社 Exhaust reburning system

Also Published As

Publication number Publication date
JPS60140005A (en) 1985-07-24

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