JPS61114008A - Soot blower device - Google Patents

Soot blower device

Info

Publication number
JPS61114008A
JPS61114008A JP23308784A JP23308784A JPS61114008A JP S61114008 A JPS61114008 A JP S61114008A JP 23308784 A JP23308784 A JP 23308784A JP 23308784 A JP23308784 A JP 23308784A JP S61114008 A JPS61114008 A JP S61114008A
Authority
JP
Japan
Prior art keywords
water
combustion gas
combustion
gas
mixing fluid
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
JP23308784A
Other languages
Japanese (ja)
Inventor
Akifumi Yoshioka
吉岡 昌文
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 JP23308784A priority Critical patent/JPS61114008A/en
Publication of JPS61114008A publication Critical patent/JPS61114008A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To prevent the loss of energy and the waste of a water supply treatment cost by a method wherein the mixing fluid of water steam generated by the direct injection of water into high temperature and high pressure combustion gas and combustion gas, is utilized. CONSTITUTION:The high pressure combustion chamber 2 of the mixing fluid generator 1 of the water steam and the combustion gas has the pressure of 10-20kg/cm<2>, fuel and high pressure air are injected into this combustion chamber from a burner 3. When a combustion is completed at the high temperature of 1,500-1,800 deg.C in the combustion chamber 2 thereof, the combustion gas arrives to a next water injection chamber 4. Here, The water injected from a water injection pipe 6 is evaporated by the combustion gas, and the temperature of the gas itself is decreased gradually while it becomes the proper mixing fluid of the water steam and the combustion gas, then, enters into a drain separating tank 8. The mixing fluid becomes complete gas and is leaded to the soot blower 17. According to this method, the loss of the energy may be prevented and the wast of the feed water treatment cost may be decreased.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、ボイラの付属装置であるスーツブロワ装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a soot blower device that is an auxiliary device to a boiler.

従来の技術 従来のスーツブロワ装置においては、一般にボイラ、用
スーツブロワに使用する噴射媒体は、ボイラ出口の主蒸
気を分岐したり、゛スーパーヒーターの中間部から抽気
したり、場合によってはボイラ蒸気ドラムから飽和蒸気
を導くなどして、スーツブロワ用噴射媒体として使用し
ている。
BACKGROUND OF THE INVENTION In conventional suit blower equipment, the injection medium used in the boiler and suit blower is generally used by branching the main steam at the boiler outlet, extracting air from the middle part of the super heater, or in some cases using boiler steam as the injection medium. Saturated steam is led from the drum and used as an injection medium for suit blowers.

そして、これらスーツブロワに使用する噴射媒体は、1
0〜20 #/、19程度の蒸気または圧縮空気を使用
するが、ボイ2から蒸気を導いて使用する場合はスーツ
ブロワ1台で5〜6 t/71にも及び、大容量のボイ
ラでは同時に3〜4台のスーツブロワを噴射する例もあ
る。さらに高圧ボイラでは、ioo〜150晦−9の高
圧蒸気をスーツブロワに適当な10〜20 kq7.I
 S)迄減圧して使用している。
The injection medium used in these suit blowers is 1
Steam or compressed air of about 0 to 20 #/, 19 is used, but when steam is led from boiler 2, it reaches 5 to 6 tons/71 with one suit blower, and in a large capacity boiler, it can be used at the same time. In some cases, three or four suit blowers are used to blow the fluid. Furthermore, in the high pressure boiler, high pressure steam of ioo~150 qq7. I
It is used after reducing the pressure to S).

発明が解決しようとする問題点 このように高圧蒸気をスーツブロワに使用するためにわ
ざわざ減圧することは、エネルギ的に大きな損失であシ
、更にボイラに使用する高質純水を多量に放出すること
となり、給水処理費の浪費にもなっている。
Problems to be Solved by the Invention In this way, taking the trouble to reduce the pressure of high-pressure steam for use in a suit blower results in a large loss of energy and also releases a large amount of high-quality pure water used in the boiler. This results in wasted water treatment costs.

こうした問題を解決するために、大型火力発電所等では
スーツブロワ専用の小型汎用ボイラ(圧力も10〜20
1q7,1 g程度のもの)を設けているとこ、ろもあ
るが、本発明は、このスーツブロワ専用の小型汎用ボイ
ラに代るものを提供しようとするものである。
In order to solve these problems, large thermal power plants use small general-purpose boilers (with a pressure of 10 to 20
However, the present invention aims to provide an alternative to a small general-purpose boiler dedicated to this suit blower.

問題点を解決するだめの手段 本発明は、スーツブロワ装置に水蒸気・燃焼ガス混合流
体発生器を設け、スーツブロワの噴射媒体発生源として
使用するようにしたものである。
Means for Solving the Problems According to the present invention, a soot blower device is provided with a steam/combustion gas mixed fluid generator, which is used as an injection medium generation source for the soot blower.

この混合流体発生器は、高圧高温燃焼ガスと噴射水とを
混合撹乱して噴射水を蒸発させ、これにより高温ガスを
スーツブロワの噴射媒体として適当な温度(300〜4
00℃程度)まで減温し、いわゆる水蒸気・燃焼ガス混
合流体を造るものである。
This mixed fluid generator mixes and agitates high-pressure, high-temperature combustion gas and injection water to evaporate the injection water, thereby raising the high-temperature gas to an appropriate temperature (300 to 400℃) as the injection medium for the suit blower.
The temperature is reduced to approximately 00°C) and a so-called water vapor/combustion gas mixed fluid is produced.

つまり、本発明によるスーツブロワ装置は、スーツブロ
ワの噴射媒体として、高圧燃焼室内で燃焼した高温・高
圧燃焼ガス中に直接水を噴射して発生させた水蒸気・燃
焼ガス混合流体を利用するものである。
In other words, the soot blower device according to the present invention uses, as the injection medium of the soot blower, a mixed fluid of water vapor and combustion gas, which is generated by directly injecting water into high-temperature, high-pressure combustion gas burned in a high-pressure combustion chamber. be.

実施例 以下添付図面を参照して本発明の好適な実施例について
詳述する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will now be described in detail with reference to the accompanying drawings.

1    第1図は、本発明の一実施例によるスーツブ
ロワ装置の概要を示す。
1 FIG. 1 shows an outline of a soot blower device according to an embodiment of the present invention.

第1図において、参照符号1は水蒸気・燃焼ガス混合流
体発生器、2は燃焼室、3はバーナ、4は水噴射室、5
は水噴射室用熱衝撃防止装置、6は水噴射管、7は水噴
射用送水ポンプ、8はドレン分離タンク、9は混合流体
出口管、10は高圧空気溜、11はニアコンプレッサー
、12は燃料吹込み管、13は燃焼用高圧空気噴込み用
管、14は混合流体溜、15はスーツブロワ用配管、1
6はボイラ、17はスーツブロワをそれぞれ示す。
In FIG. 1, reference numeral 1 is a water vapor/combustion gas mixed fluid generator, 2 is a combustion chamber, 3 is a burner, 4 is a water injection chamber, and 5 is a combustion chamber.
1 is a thermal shock prevention device for a water injection chamber, 6 is a water injection pipe, 7 is a water injection pump, 8 is a drain separation tank, 9 is a mixed fluid outlet pipe, 10 is a high pressure air reservoir, 11 is a near compressor, 12 is a 13 is a fuel injection pipe, 13 is a combustion high pressure air injection pipe, 14 is a mixed fluid reservoir, 15 is suit blower piping, 1
6 indicates a boiler, and 17 indicates a suit blower.

次にその作用について説明する。Next, its effect will be explained.

水蒸気・燃焼ガス混合流体発生器1の高圧燃焼室2は1
0〜20ψ−9となっておシ、燃料(液体またはガス体
)及び高圧空気がバーナ3からこの中に吹き込まれる。
The high pressure combustion chamber 2 of the steam/combustion gas mixed fluid generator 1 is 1
0 to 20ψ-9, fuel (liquid or gaseous) and high pressure air are blown into this from the burner 3.

そして、この燃焼室2内で1500〜1800℃の高温
で燃焼を完結すると、次の水噴射室4に到シ、ここで、
水噴射管6から噴射された水を蒸発させるとともに燃焼
ガス自体はその温度を徐々に下げながら適当な水蒸気°
・燃焼ガス混合流体となって、ドレン分離タンク8に到
  iする。
When combustion is completed in this combustion chamber 2 at a high temperature of 1500 to 1800°C, it moves to the next water injection chamber 4, where
While the water injected from the water injection pipe 6 is evaporated, the temperature of the combustion gas itself is gradually lowered and the temperature is gradually reduced to an appropriate amount of water vapor.
- The combustion gas becomes a mixed fluid and reaches the drain separation tank 8.

このとき、この混合流体は300〜400 ℃に制御さ
れているので微粒水滴も殆ど蒸発し、ドレンの発生は殆
どないが、更にこのタンク8で完全なガス体となって、
スーツブロワ17まで導かれていく。
At this time, since this mixed fluid is controlled at 300 to 400 °C, most of the fine water droplets evaporate, and there is almost no drainage, but it becomes a complete gas in this tank 8,
It will lead you to suit blower 17.

第2図は本発明によるスーツブロワ装置の他の実施例を
示す。
FIG. 2 shows another embodiment of the soot blower device according to the present invention.

第2図において、混合流体発生器1で発生した水蒸気・
燃焼ガス混合流体の一部は、ドレン分離タンク8からガ
スエキスパンダ18に導かれるようKされている。そし
て、この混合流体の一部は、混合流体発生器1に供給さ
れる燃焼用高圧空気のコンプレッサ19の駆動源として
、ガスエキスパンダ18で使用される。
In Fig. 2, water vapor and
A portion of the combustion gas mixture fluid is directed from the drain separation tank 8 to the gas expander 18 . A portion of this mixed fluid is used by the gas expander 18 as a driving source for the compressor 19 of high-pressure combustion air supplied to the mixed fluid generator 1 .

、また、ガスエキスパンダ18に導かれなかった混合流
体については、上記実施例と同様にスーツブロワ(図示
せず)の噴射媒体として使用される。
Also, the mixed fluid that is not guided to the gas expander 18 is used as an injection medium for a soot blower (not shown) in the same manner as in the above embodiment.

なお、第1図及び第2図共に、混合流体発生器1は1台
しか示してないが、スーツブロワの噴射媒体の使用量が
多くなるようならば、2台、3台と複数台を組み合せて
もよいことは勿論である。
Note that only one mixed fluid generator 1 is shown in both Figures 1 and 2, but if the amount of jetting medium used by the soot blower increases, two or three or more units may be combined. Of course, it is possible.

発明の効果 本発明によるスーツブロワ装置は、以上に述べた構成で
あるので、次のような効果がある。
Effects of the Invention Since the soot blower device according to the present invention has the configuration described above, it has the following effects.

まず、通常ボイラと呼ばれるボイラにおいて灯油100
01vhの燃焼で発生できる10〜20階−9の蒸気は
概略12〜13t/11 であるのに対し、こよって得
られる蒸気・ガス混合流体はaot/)1以上にもなる
First, in a boiler called a boiler, 100% of kerosene
The steam on the 10th to 20th floors-9 that can be generated by combustion of 0.1 vh is approximately 12 to 13 t/11, whereas the steam/gas mixed fluid thus obtained is more than aot/)1.

逆に通常ボイラ並みに12〜13t/INの蒸気・ガス
混合流体を得るために必要な燃料は、前述の灯油の場合
僅か400 kV11程度ですむ。
On the other hand, in order to obtain a steam/gas mixed fluid of 12 to 13 t/IN, which is the same as in a normal boiler, the fuel required is only about 400 kV11 in the case of the above-mentioned kerosene.

つまり、通常ボイラの熱効率の2倍以上と言うことにな
る。
In other words, the thermal efficiency is more than twice that of a normal boiler.

また、通常ボイラが大気圧の空気を使用しているのに対
し、本装置では10〜20ψd9の圧縮空気を使用しな
ければならないのではあるが、今仮シに10ψ−9のニ
アコンプレッサを使用するとすれば、これに要する動力
費を考慮しても、燃料使用量は通常ボイラより30〜4
0%も少なくてすむ。
Also, while boilers normally use air at atmospheric pressure, this device must use compressed air of 10 to 20ψd9, but we are currently using a 10ψ-9 near compressor. If so, even considering the power cost required for this, the amount of fuel used will be 30 to 4 times lower than that of a normal boiler.
0% less.

更に有利なことは燃焼ガス中に噴射する水はごく一般の
工業用水程度の水質が使用できると言う点である。
A further advantage is that the water injected into the combustion gas can be of the same quality as ordinary industrial water.

雄側を示す概略図、第2図は他の実施例を示す概略図で
ある。
A schematic diagram showing the male side, and FIG. 2 is a schematic diagram showing another embodiment.

l・・水蒸気・燃焼ガス混合流体発生器、2・・高圧燃
焼室、4・・水噴射室、6・・水噴射管、8・・ドレン
分離タンク、17拳・スーツブロワ、1°811・ガス
エキスパンダ、19・・コンプレッサ。
1. Steam/combustion gas mixed fluid generator, 2. High pressure combustion chamber, 4. Water injection chamber, 6. Water injection pipe, 8. Drain separation tank, 17 fists, suit blower, 1°811. Gas expander, 19...compressor.

Claims (1)

【特許請求の範囲】[Claims] スーツブロワの噴射媒体として、高圧燃焼室内で燃焼し
た高温・高圧燃焼ガス中に直接水を噴射して発生させた
水蒸気・燃焼ガス混合流体を利用してなるスーツブロワ
装置。
A soot blower device that uses a mixed fluid of water vapor and combustion gas generated by directly injecting water into high-temperature, high-pressure combustion gas burned in a high-pressure combustion chamber as the injection medium of the soot blower.
JP23308784A 1984-11-07 1984-11-07 Soot blower device Pending JPS61114008A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23308784A JPS61114008A (en) 1984-11-07 1984-11-07 Soot blower device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23308784A JPS61114008A (en) 1984-11-07 1984-11-07 Soot blower device

Publications (1)

Publication Number Publication Date
JPS61114008A true JPS61114008A (en) 1986-05-31

Family

ID=16949585

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23308784A Pending JPS61114008A (en) 1984-11-07 1984-11-07 Soot blower device

Country Status (1)

Country Link
JP (1) JPS61114008A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012241971A (en) * 2011-05-19 2012-12-10 Hitachi Ltd Biomass combusting boiler
CN104089291A (en) * 2014-07-25 2014-10-08 邓雪明 Gas-liquid mixed soot blowing device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012241971A (en) * 2011-05-19 2012-12-10 Hitachi Ltd Biomass combusting boiler
CN104089291A (en) * 2014-07-25 2014-10-08 邓雪明 Gas-liquid mixed soot blowing device
CN104089291B (en) * 2014-07-25 2016-10-05 邓雪明 A kind of gas-liquid mixed soot blower

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