JPS5935712A - Method of preventing corrosion of combustion device - Google Patents

Method of preventing corrosion of combustion device

Info

Publication number
JPS5935712A
JPS5935712A JP14476582A JP14476582A JPS5935712A JP S5935712 A JPS5935712 A JP S5935712A JP 14476582 A JP14476582 A JP 14476582A JP 14476582 A JP14476582 A JP 14476582A JP S5935712 A JPS5935712 A JP S5935712A
Authority
JP
Japan
Prior art keywords
ash
water
coal
hopper
control valve
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
JP14476582A
Other languages
Japanese (ja)
Inventor
Manabu Orimoto
折本 学
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 Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP14476582A priority Critical patent/JPS5935712A/en
Publication of JPS5935712A publication Critical patent/JPS5935712A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J1/00Removing ash, clinker, or slag from combustion chambers

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)

Abstract

PURPOSE:To prevent the lowering of pH of ash treating water by transferring a part of scattered coal ashes arrested by a coal ash arrester provided in a flue or the like to a water-immersion type ash hopper, upon driving a coal-burning combustion device having at the furnace bottom the water-immersion type ash hopper in which ash treating water circulates. CONSTITUTION:In order to cause the device to carry out the pH adjusting operation of ash treating water due to the injection of scattered coal ashes and an operation to prevent contact with circulated combustion waste gas due to suspention in correspondence to the pH of the ash treating water, it is advisable to provide a pH meter 20 concurrently used for a ash water transfer control valve 21 in the water-immersion type ash hopper 2 and an ash water transfer pipe 25, respectively and connect them to each other, and further an ash air transfer control valve 23 in an ash air transfer pipe 24. For instance, if the ash water transfer control valve 21 is set to operate when the pH is lowered to a predetermined value, and the ash air transfer control valve 23 is set to operated at every predetermined time, the lowering of the pH of the ash treating water can be prevented constantly, automatically and stably.

Description

【発明の詳細な説明】 本発明は、燃焼装置の腐食防止方法に関し、特に窒素酸
化物低減対策を実施している石炭だき燃焼装置の腐食防
止方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing corrosion of a combustion device, and particularly to a method of preventing corrosion of a coal-fired combustion device in which measures are taken to reduce nitrogen oxides.

従来、石炭だき燃焼装置、例えば微粉炭だきボイラの運
転においては、一般に、燃焼された石炭中の灰分の一部
(例えば、全灰量のコ0〜15%)は、濾底の水浸式ア
ッシュホッパに落下され、他の灰分は排ガスとともに煙
道に誘引されて種々の石炭灰捕集器で捕集され、これら
の石炭灰は合体されて廃棄処理されていた。
Conventionally, in the operation of a coal-fired combustion device, such as a pulverized coal-fired boiler, a portion of the ash in the combusted coal (e.g., 0 to 15% of the total ash amount) is generally absorbed into the water-immersed filter bottom. The ash is dropped into an ash hopper, and other ash is drawn into the flue along with the exhaust gas and collected in various coal ash collectors, and these coal ash are combined and disposed of.

このような従来の灰分捕集処理状況の1例を第1図によ
り、詳細に説明する。燃焼室で発生した高温の石炭灰の
一部は、炉底部1に設けられた水浸式アッシュホッパ2
の水中に落下し、急冷されて非常にもろい組織のクリン
カとなる。このクリンカ状石炭灰は、時々(例えば8時
間に1回の割合で)高圧水の通るジェットノズル11に
よりアッシュゲートから水と共にホッパ2外に排出され
、次いでクリンカクラツシャ3で粉砕される。このよう
にして生成した粉砕石炭灰は、高圧水によりハイエジェ
クタ4に移送され、さらに灰移送管5を経て脱水槽6に
送られて脱水された後、運搬用トラック12により灰捨
場へ輸送される。脱水槽6で分離された汚水は、分離水
配管7を経て沈降槽8に移送され、残存する石炭灰を沈
降分離し、随時、高圧水ポンプ9により高圧水にされ、
高圧水管10を経て上記各部所に循環使用される。また
、との循環水の一部は、炉底部1と水浸式アツシュホッ
パ2の接続部をシールするシール水14としても使用さ
れ、シール部をオーツ(−フローしたシール水14は、
オーバーフロー管15を経て前記循環水に合流して循環
さfする。なお、水浸式アッシュホッパ2内のクリンカ
状石炭灰は、クリンカクラッシャ3で粉砕された後、)
へイエジエクタ4から上記のような経路を経る他に、ノ
・イエジエクタ4から灰捨配管工3を経て灰捨場へ直接
輸送させるととも可能である。[7かしながら、近年は
水資源の効率的使用と水質汚濁防止との観点から、廃水
量の少ない前記循環方式が主流である。
An example of such a conventional ash collection process will be explained in detail with reference to FIG. A portion of the high-temperature coal ash generated in the combustion chamber is transferred to a water-immersed ash hopper 2 installed at the bottom of the furnace 1.
It falls into water and is rapidly cooled to form clinker, a very brittle tissue. This clinker-like coal ash is discharged from the ash gate to the outside of the hopper 2 together with water by a jet nozzle 11 through which high-pressure water is passed from time to time (for example, once every 8 hours), and then crushed by a clinker crusher 3. The pulverized coal ash generated in this way is transferred to a high ejector 4 using high-pressure water, and then sent to a dehydration tank 6 via an ash transfer pipe 5 to be dehydrated, and then transported to an ash dump site by a transport truck 12. Ru. The wastewater separated in the dewatering tank 6 is transferred to the sedimentation tank 8 via the separated water pipe 7, where the remaining coal ash is sedimented and separated, and the water is made into high pressure water by the high pressure water pump 9 at any time.
The water is circulated through the high-pressure water pipe 10 to each of the above locations. In addition, a part of the circulating water is also used as seal water 14 that seals the connection between the furnace bottom 1 and the water-immersed ash hopper 2, and the seal water 14 that flows through the seal part is
It joins the circulating water through the overflow pipe 15 and is circulated. In addition, after the clinker-like coal ash in the water-immersed ash hopper 2 is crushed by the clinker crusher 3,
In addition to transporting the ash from the ash ejector 4 through the above-mentioned route, it is also possible to transport the ash directly from the ash ejector 4 to the ash disposal site via the ash disposal plumber 3. [7] However, in recent years, from the viewpoint of efficient use of water resources and prevention of water pollution, the above-mentioned circulation method, which uses a small amount of wastewater, has become mainstream.

一方、水浸式アツシュホツノく2に落下しなかった石炭
灰は、排ガスとともに煙道に入るが(以下、このような
石炭灰を飛散石炭灰ということがある)煙道には種々な
装置、例えば節炭器、集じん器(マルチサイクロン、コ
ットレル)、空気予熱器等が順次設けられており、排ガ
ス中の飛散石炭灰はこれらの各装置で捕集または分離さ
れ、それぞれ例えば節炭器ホッパ17、集じん器ホツノ
く18、空気予熱器ホッパ19に落下し、貯留さi]、
る。節炭器と空気予熱器とで捕集される灰量は全灰量の
例えば6〜10%程度であり、残る大部分は集じん器で
捕集される。上記各ホッパl’i’、1B、19に貯え
られた飛散石炭灰は、適時、循環する高圧水で作動する
ハイドロベアエキゾースタ16によって脱水槽6に移送
され、前記粉砕石炭灰と同様に処理される。上記のよう
に、石炭灰の冷却、移送などの処理に使用される一連の
水を灰処理水ということがある。
On the other hand, the coal ash that has not fallen into the water-immersed ash pipe 2 enters the flue along with the exhaust gas (hereinafter, such coal ash may be referred to as scattered coal ash). A coal economizer, a dust collector (multi-cyclone, Cottrell), an air preheater, etc. are installed in sequence, and the scattered coal ash in the exhaust gas is collected or separated by each of these devices, for example, a coal economizer hopper 17. , falls into the dust collector hotsunoku 18 and air preheater hopper 19 and is stored],
Ru. The amount of ash collected by the economizer and the air preheater is, for example, about 6 to 10% of the total ash amount, and most of the remaining amount is collected by the dust collector. The scattered coal ash stored in each of the above-mentioned hoppers l'i', 1B, and 19 is transferred to the dehydration tank 6 by the Hydrobear exhauster 16 operated by circulating high-pressure water at appropriate times, and is treated in the same way as the crushed coal ash. It is processed. As mentioned above, a series of water used for processing coal ash, such as cooling and transporting it, is sometimes referred to as ash treatment water.

このように石炭灰を処理する方法は、窒素酸化物(NO
X)低減対策として、燃焼排ガスの一部循環や空気比の
調整などを実施する燃焼装置においても、同様に実施さ
れてきたが、最近、燃焼装置、特にNOx低減対策を実
施している燃焼装置で、灰移送管5、シール水14のオ
ーバーフロー管15、シルボックストラフ、ホッパシー
ル管外と、石炭灰の処理工程で灰処理水と接触する部分
が腐食減肉し、その補修のために燃焼装置の運転を停市
する必要を生じた。そこで本発明者は、その原因を検討
した結果、次のようなことが判明した。
This method of treating coal ash produces nitrogen oxides (NO
X) Similar reduction measures have been implemented in combustion equipment that partially recirculates combustion exhaust gas and adjusts the air ratio, but recently, combustion equipment, especially combustion equipment that implements measures to reduce NOx, have recently been implemented. The ash transfer pipe 5, the overflow pipe 15 of the seal water 14, the sill box trough, the outside of the hopper seal pipe, and the parts that come into contact with the ash treatment water during the coal ash treatment process were corroded and thinned, and the combustion equipment was installed to repair them. It became necessary to stop driving. The inventor of the present invention investigated the cause and found the following.

すなわち、近年、環境浄化のために実施されるようにな
ったNOx低減対策によって、燃焼装置内のバーナ下流
の火炎温度が低下したため、燃焼室の熱負荷容量が低下
しており、そのだめ、燃焼室の氷壁部へ付着するクリン
カ状石炭灰が減少し、燃焼室から水浸式アツシュホツノ
(へ落下するクリンカ状石炭灰が大幅に減少し7ている
。また、一方ではNOx低減対策として燃焼排ガスの一
部を炉底部を経由して燃焼室へ循環させることから、燃
焼排ガスに含有されるBoxなどの酸性成分が、水浸式
アッシュホッパの灰処理水に吸収されてその1)Hを低
下させるように作、用している。そしてこのpH低下作
用は、灰処理水を循環使用することによって酸性成分が
著積して強化されていることと、燃焼室から落下するク
リンカ状石炭灰が少量となったこととによって、燃焼排
ガスのpH低下作用と石炭灰による中和作用とのバラン
スがとれなくなり、灰処理水のpHが低下して腐食現象
を起こさせていることが判明した。
In other words, due to NOx reduction measures that have been implemented in recent years to purify the environment, the flame temperature downstream of the burner in the combustion device has decreased, resulting in a decrease in the heat load capacity of the combustion chamber. The amount of clinker-like coal ash that adheres to the ice wall of the combustion chamber has been reduced, and the amount of clinker-like coal ash that falls from the combustion chamber to the water-immersed combustion chamber has been significantly reduced. Since a part of the gas is circulated to the combustion chamber via the bottom of the furnace, acidic components such as Box contained in the combustion exhaust gas are absorbed into the ash treatment water of the water-immersed ash hopper, reducing 1) H. It is made and used as such. This pH lowering effect is caused by the fact that acidic components are significantly accumulated and strengthened by recycling the ash-treated water, and by the fact that a small amount of clinker-like coal ash falls from the combustion chamber. It was found that the balance between the pH lowering effect of coal ash and the neutralizing effect of coal ash was no longer maintained, and the pH of the ash treated water was lowered, causing corrosion phenomena.

このような酸性を中和するのに薬剤を使用することは繁
雑力士に、薬剤の消費量が大きく、経済的な負担が大き
くなる。
The use of drugs to neutralize such acidity imposes a heavy economic burden on the wrestlers due to the large consumption of drugs.

本発明の屈曲は、上記従来技術に鑑み、特別な薬剤を使
用しないで石炭灰処理水による各機器の腐食を防止する
ことができる燃焼装置の腐食防止方法を提供することに
ある。
In view of the above-mentioned prior art, an object of the present invention is to provide a method for preventing corrosion of combustion equipment, which can prevent corrosion of various equipment caused by treated coal ash water without using special chemicals.

本発明は、灰処理水が循環する水浸式アッシュホッパを
炉底部に有する石炭焚き燃焼装置を運転する際に、煙道
等に設けられた石炭灰捕集器で捕集される飛散石炭灰の
一部を前記水浸式アッシュホッパに移送することにより
、前記灰処理水のpHの低下を防止することを特徴とす
る。
The present invention provides for scattered coal ash that is collected by a coal ash collector installed in a flue or the like when operating a coal-fired combustion device that has a water-immersed ash hopper at the bottom of the furnace through which ash treatment water circulates. By transferring a portion of the ash to the water-immersed ash hopper, a decrease in the pH of the ash treatment water is prevented.

本発明方法においては、灰処理水のpH低下に対応させ
て、煙道で捕集した飛散石炭灰の一部を水浸式アッシュ
ホッパに移送して、灰処理水のpHの低下を防止する。
In the method of the present invention, a portion of the scattered coal ash collected in the flue is transferred to a water-immersed ash hopper in response to a decrease in the pH of the ash treatment water, thereby preventing a decrease in the pH of the ash treatment water. .

水浸式アッシュホッパに移送された飛散石炭灰の作用の
一つは、灰中に含有されるC、01Mg01Fe203
などのアルカリ性成分によって、灰処理水のpHを中性
またはアルカリ側に移行させることである。このように
作用させるにけ、水浸式アッシュホッパ中の灰処理水に
飛散石炭灰を注入すればよい。石炭灰の他の作用は、水
浸式アッシュホッパ中の灰処理水の表面に飛散石炭灰を
浮遊させ、p■低下作用をする循環燃焼排ガスとの接触
を防Iトすることである。上記の移送される石炭灰の性
状としては、循環燃焼排ガスとの接触防止を図るために
は飛散性であることが必要であるが、pH調節のために
は、飛散性でも水との混合物であってもよい。上記2つ
の作用は必ずしも同時である必要はなく、灰処理水のp
Hに応じて適時、石炭灰を注入または浮遊させればよい
One of the effects of the scattered coal ash transferred to the water-immersed ash hopper is that the carbon contained in the ash, 01Mg01Fe203
The purpose is to shift the pH of the ash treatment water to the neutral or alkaline side by using alkaline components such as. To achieve this effect, scattered coal ash may be injected into the ash treatment water in the submerged ash hopper. Another function of the coal ash is to suspend the scattered coal ash on the surface of the ash treatment water in the submerged ash hopper, thereby preventing it from coming into contact with the circulating combustion exhaust gas, which has the effect of lowering the p. As for the properties of the above-mentioned transported coal ash, it is necessary to be scattering in order to prevent contact with circulating combustion exhaust gas, but in order to adjust the pH, even if it is scattering, it must be mixed with water. There may be. The above two effects do not necessarily have to be simultaneous, and the p
Coal ash may be injected or suspended at appropriate times depending on H.

以下、本発明を図面によりさらに詳細に説明する。第2
図は本発明の腐食防止方法の1実施例を説明するだめの
系統図である。第2図において、クリンカ状の石炭灰が
水浸式アラツユホッパ2の灰処理水中に落下し、クリン
カクラッシャ3で粉砕され、ハイエジェクタ4で灰移送
管5を経て脱水槽6に移送され、脱水された石炭灰は灰
捨場へ輸送され、分離水は沈降槽8から随時各部所に灰
処理水として昇圧されて循環使用され、その1部はシー
ル水14としてオーバーフロー管15を経て循環経路に
戻ることは、第1図の場合と同様である。燃焼装置の炉
底部1の近傍には、第3図にその概略を示すように、燃
焼排ガス炉底ダクト26が開口しており、そのため、循
環されて来た燃焼排ガスと水浸式アッシュホッパ2の灰
処理水とが常に気液接触しており、前記した理由によっ
て灰処理水のpJ(は除々に低下する。
Hereinafter, the present invention will be explained in more detail with reference to the drawings. Second
The figure is a system diagram for explaining one embodiment of the corrosion prevention method of the present invention. In Fig. 2, clinker-like coal ash falls into the ash treatment water of the water-immersed hopper 2, is crushed by the clinker crusher 3, is transferred to the dehydration tank 6 via the ash transfer pipe 5 by the high ejector 4, and is dehydrated. The separated coal ash is transported to the ash dump, and the separated water is pressurized and circulated from the settling tank 8 to various locations as ash treatment water, and a portion of it is returned to the circulation path as seal water 14 via the overflow pipe 15. is the same as in FIG. As schematically shown in FIG. 3, a combustion exhaust gas furnace bottom duct 26 is opened near the furnace bottom 1 of the combustion device, so that the flue gas that has been circulated and the water-immersed ash hopper 2 are opened. is always in gas-liquid contact with the ash-treated water, and the pJ of the ash-treated water gradually decreases for the reasons described above.

pJ(が低下してきた時点で、節炭器ホッパ17、集じ
ん器ホッパ18、空気予熱器ホッパ19などに著えられ
ている飛散石炭灰が、ハイドロベアエキゾースタ16に
より、高圧水と共に入水移送管25を経て水浸式アッシ
ュホッパ2の灰処理水中に注入される。この入水移送管
25は、第1図で説明したハイドロベアエギゾースタ1
6から脱水槽への飛散石炭灰の移送に際して使用する配
管から分岐すればよい。捷だ、上記各ホッパ]−ツ、1
B、19からの飛散石炭は、ハイドロベアエキゾースタ
16によらないで、灰空気移送管24を通って空勿、輸
送し、灰吹出し管22から水浸式アッシュホッパ2の灰
処理水中に注入してもよい。このようにして灰処理水の
pHが調節され、各機器の腐食が防止される。一方、水
浸式アッシュホッパ2の灰処理水面上には、上記灰吹出
し管22から飛散石炭灰が吹出し速度や角度を調節しで
吹き出され、灰処理水の表面に灰浮遊層2′yを形成し
、灰処理水と循環燃焼排ガスとの接触を防止してその酸
性化を極力防止される。このように1−て灰処理水のp
Hの低下が防止される。
When the pJ (pJ) decreases, the scattered coal ash concentrated in the economizer hopper 17, dust collector hopper 18, air preheater hopper 19, etc., enters the water together with high-pressure water by the Hydrobear exhauster 16. The ash is injected into the ash treatment water of the water immersion type ash hopper 2 through the transfer pipe 25.This inlet water transfer pipe 25 is connected to the Hydrobear exhauster 1 explained in FIG.
6 to the dewatering tank. The above hoppers]-tsu, 1
The scattered coal from B, 19 is transported through the ash air transfer pipe 24 without using the hydrobear exhauster 16, and is transported from the ash blowing pipe 22 into the ash treatment water of the water-immersed ash hopper 2. May be injected. In this way, the pH of the ash treatment water is adjusted and corrosion of each device is prevented. On the other hand, scattered coal ash is blown out from the ash blowing pipe 22 onto the ash treatment water surface of the water-immersed ash hopper 2 by adjusting the blowing speed and angle, forming an ash floating layer 2'y on the surface of the ash treatment water. This prevents the ash treatment water from coming into contact with the circulating combustion exhaust gas, thereby preventing its acidification as much as possible. In this way, 1-p of the ash treated water is
A decrease in H is prevented.

上記のような飛散石炭灰の注入による灰処理水のpH調
節作用や浮遊による循環燃焼排ガスとの接触防+)、作
用を、灰処理水のpHに応じて自動的に適時、行わせる
には、第2図に示すように、 pH計兼制御器20と入
水移送制御弁21とをそれぞれ水浸式アッシュホッパ2
と入水移送管25に設けて連結し、また灰空気移送管2
4に灰空気移送制御弁23を設ければよい。そして例え
ば入水移送制御弁31はpHが一定値に低下したときに
作動すると共に、灰空気移送制御弁23は一定時間毎に
作動するように設定しておけば、常に自動的にかつ安定
して灰処理水のpH低下を防止するととができる。
To automatically and timely perform the above-mentioned effects of adjusting the pH of ash treated water by injecting scattered coal ash and preventing contact with circulating combustion exhaust gas by floating the ash, depending on the pH of the ash treated water. , as shown in FIG.
and connected to the inlet water transfer pipe 25, and the ash air transfer pipe 2
4 may be provided with an ash air transfer control valve 23. For example, if the inlet water transfer control valve 31 is set to operate when the pH drops to a certain value, and the ash air transfer control valve 23 is set to operate at fixed intervals, the valve will always operate automatically and stably. This can prevent the pH of the ash treatment water from decreasing.

以上、本発明によれば、何ら特別表薬剤を使用すること
なく、灰処理水のpH低下を防いで燃焼装置の腐食を防
止することができる。従って、今後さらに進むと予想さ
れる低NOx対策においても、腐食のための燃焼装置の
保守が容易となり、安定した運転が可能となる。また、
薬剤の不使用や保守費用の低減により、運転コストも安
価となる。
As described above, according to the present invention, it is possible to prevent the pH of the ash treatment water from decreasing and to prevent corrosion of the combustion device without using any special chemicals. Therefore, even with measures to reduce NOx that are expected to become more advanced in the future, maintenance of combustion equipment for corrosion becomes easier and stable operation becomes possible. Also,
Operating costs are also lower due to no use of chemicals and lower maintenance costs.

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

第1図は従来の灰分捕集・処理系統図、第2図は本発明
の腐食防止方法の1実施例を示す系統図、第3図は燃焼
装置の炉底部近傍の概略図である。 l・・・・・・炉、Wm、2・・・・・・水浸式アツシ
コ4ホッパ、     ′3・・・・・・クリンカクラ
ッシャ、4・・・・・・ノ為イエジエクタ、5・・・・
・・灰移送管、6・・・・・・脱水槽、フ・・・・・・
分離 ・水配管、8・・・・・・沈降槽、9・・・・・
・高圧水ポンプ、10・・・・・・高圧水管、11・・
・・・・ジェットノズル、12・・・・・・トラック、
13・・・・・・灰捨配管、14・・・・・・シール水
、15・・・・・・オーバーフロー管、16・・・・・
・ハイドロベアエキゾースタ、17・・・−・・節炭器
ホッパ、18・・・・・・集じん器ホッパ、19・・・
・・・空気予熱器ホッパ、20・・・・・・pH計兼制
御器、21・・・・・・天水移送制御弁、22・・・・
・・灰吹出し管、23・・・・・・灰空気移送制御弁、
24・・・・・・灰空気移送管、25・・・・・・戻水
移送管、26・・・・・・燃焼排ガス炉底ダクト、27
・・・・・・浮遊灰層。 代理人 弁理士 川 北 武 長 第1図
FIG. 1 is a conventional ash collection and treatment system diagram, FIG. 2 is a system diagram showing one embodiment of the corrosion prevention method of the present invention, and FIG. 3 is a schematic diagram of the vicinity of the bottom of a combustion apparatus. l... Furnace, Wm, 2... Water immersion type Atsushiko 4 hopper, '3... Clinker crusher, 4... Ejector, 5...・・・
...Ash transfer pipe, 6...Dehydration tank, Fu...
Separation ・Water piping, 8... Sedimentation tank, 9...
・High pressure water pump, 10... High pressure water pipe, 11...
... Jet nozzle, 12 ... Truck,
13...Ash disposal pipe, 14...Seal water, 15...Overflow pipe, 16...
・Hydrobear exhauster, 17...--Energy saver hopper, 18...Dust collector hopper, 19...
... Air preheater hopper, 20 ... pH meter and controller, 21 ... Rainwater transfer control valve, 22 ...
...Ash blow-off pipe, 23...Ash air transfer control valve,
24... Ash air transfer pipe, 25... Return water transfer pipe, 26... Combustion exhaust gas furnace bottom duct, 27
...Floating ash layer. Agent Patent Attorney Takenaga Kawakita Figure 1

Claims (1)

【特許請求の範囲】[Claims] (1)灰処理水が循環する水浸式アッシュホッパを炉底
部に有する石炭焚き燃焼装置を運転する際に、煙道等に
設けられた石炭灰捕集器で捕集される飛散石炭灰の一部
を前記水浸式アッシュホッパに移送することにより、前
記灰処理水のp、 Hの低下を防止することを特徴とす
る燃焼装着の腐食防止方法。
(1) When operating a coal-fired combustion equipment that has a water-immersed ash hopper at the bottom of the furnace where ash treatment water circulates, scattered coal ash is collected by a coal ash collector installed in the flue, etc. A method for preventing corrosion of combustion equipment, characterized in that a portion of the ash treated water is transferred to the water-immersed ash hopper to prevent a decrease in P and H of the ash treated water.
JP14476582A 1982-08-23 1982-08-23 Method of preventing corrosion of combustion device Pending JPS5935712A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14476582A JPS5935712A (en) 1982-08-23 1982-08-23 Method of preventing corrosion of combustion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14476582A JPS5935712A (en) 1982-08-23 1982-08-23 Method of preventing corrosion of combustion device

Publications (1)

Publication Number Publication Date
JPS5935712A true JPS5935712A (en) 1984-02-27

Family

ID=15369883

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14476582A Pending JPS5935712A (en) 1982-08-23 1982-08-23 Method of preventing corrosion of combustion device

Country Status (1)

Country Link
JP (1) JPS5935712A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4870517A (en) * 1987-01-21 1989-09-26 Sony Corporation Magnetic tape cassette loading mechanism in recording and/or reproducing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4870517A (en) * 1987-01-21 1989-09-26 Sony Corporation Magnetic tape cassette loading mechanism in recording and/or reproducing apparatus

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