JPS5857645B2 - Combustion ash removal device - Google Patents

Combustion ash removal device

Info

Publication number
JPS5857645B2
JPS5857645B2 JP13335081A JP13335081A JPS5857645B2 JP S5857645 B2 JPS5857645 B2 JP S5857645B2 JP 13335081 A JP13335081 A JP 13335081A JP 13335081 A JP13335081 A JP 13335081A JP S5857645 B2 JPS5857645 B2 JP S5857645B2
Authority
JP
Japan
Prior art keywords
chamber
water
combustion
pipe
combustion ash
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
JP13335081A
Other languages
Japanese (ja)
Other versions
JPS5835318A (en
Inventor
清巳 岡田
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.)
SANENERUGII KK
Original Assignee
SANENERUGII 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 SANENERUGII KK filed Critical SANENERUGII KK
Priority to JP13335081A priority Critical patent/JPS5857645B2/en
Priority to CA000391387A priority patent/CA1180954A/en
Priority to US06/327,258 priority patent/US4432288A/en
Priority to AU78371/81A priority patent/AU7837181A/en
Publication of JPS5835318A publication Critical patent/JPS5835318A/en
Publication of JPS5857645B2 publication Critical patent/JPS5857645B2/en
Expired 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 
    • F23C6/00Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion
    • F23C6/04Combustion apparatus characterised by the combination of two or more combustion chambers or combustion zones, e.g. for staged combustion in series connection
    • 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 
    • F23C3/00Combustion apparatus characterised by the shape of the combustion chamber
    • F23C3/006Combustion apparatus characterised by the shape of the combustion chamber the chamber being arranged for cyclonic combustion
    • F23C3/008Combustion apparatus characterised by the shape of the combustion chamber the chamber being arranged for cyclonic combustion for pulverulent fuel
    • 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
    • F23J1/02Apparatus for removing ash, clinker, or slag from ash-pits, e.g. by employing trucks or conveyors, by employing suction devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/02Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/027Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using cyclone separators

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【発明の詳細な説明】 本発明は、固形燃料燃焼装置の燃焼灰を該燃焼装置の運
転を停止することなく取り出せるようにした燃焼灰取出
装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a combustion ash removal device that allows combustion ash from a solid fuel combustion device to be taken out without stopping the operation of the combustion device.

固形燃料燃焼装置は小型のものであればその燃焼中に燃
焼灰を取り出すことが可能であるが、中型、大型のもの
では燃焼ガスが高温高圧となり、燃焼灰を取り出そうと
すると圧力が洩れるばかりか危険でもあるため、運転を
停止した後でなげれば灰取出作業を行なうことができな
かった。
If the solid fuel combustion device is small, it is possible to remove the combustion ash during combustion, but in medium or large-sized devices, the combustion gas becomes high temperature and high pressure, and when trying to remove the combustion ash, the pressure may leak. Because it was dangerous, it was impossible to remove the ash if it was thrown down after the operation was stopped.

このような制約は明らかに固形燃料燃焼装置の利用可能
分野を狭め、例えば24時間運転の場合には固形燃焼装
置を適用できない原因となっている。
Such restrictions obviously narrow the range of applications for solid fuel combustion devices, and are the reason why solid fuel combustion devices cannot be used, for example, in the case of 24-hour operation.

本発明は、このような事情に鑑み、燃焼を継続したまま
灰の取り出しができる装置を得ることを目的になされた
もので、固形燃料燃焼装置の燃焼室の下方に該燃焼室に
連通ずる燃焼灰落下室を設ける一方、この落下室と底部
の連通路で連通ずる、該落下室と等圧に保たれる密閉タ
ンクを設けて、常時は画室を一定レベルの水で満たし、
この落下室内の水を上記密閉タンク内に配設した水中ポ
ンプからの吐出水により撹拌した後、今度は水中ポンプ
の吐出水を固液分離装置に導くことによって燃焼灰を落
下室pよび密閉タンク内の水とともに外部に取り出すよ
うにしたことを特徴としている。
In view of these circumstances, the present invention was made with the aim of providing a device that can remove ash while continuing combustion. An ash falling chamber is provided, and a sealed tank is provided which communicates with this falling chamber through a communication passage at the bottom and is kept at the same pressure as the falling chamber, and the chamber is always filled with water at a certain level.
After the water in this falling chamber is stirred by water discharged from the submersible pump disposed in the sealed tank, the discharged water from the submersible pump is then led to a solid-liquid separator to separate the combustion ash from the falling chamber p and into the sealed tank. The feature is that the water inside is taken out to the outside.

以下図示実施例について本発明を説明する。The invention will now be described with reference to illustrated embodiments.

燃焼灰落下室1は固形燃料燃焼装置2の下方に設けられ
、燃焼室3と連通している。
The combustion ash fall chamber 1 is provided below the solid fuel combustion device 2 and communicates with the combustion chamber 3.

燃焼装置2は固形燃料を燃焼させるものであればその構
造形式を問わないが、この実施例では横向きの筒状燃焼
室内で渦流を発生させ、その渦流中で粒状または粉状の
固形燃料を燃焼させて燃焼ガスを横向きの燃焼ガス取出
管2aから取り出すタイプの燃焼装置を予定している。
The structure of the combustion device 2 does not matter as long as it burns solid fuel, but in this embodiment, a vortex is generated in a horizontally oriented cylindrical combustion chamber, and granular or powdered solid fuel is combusted in the vortex. A type of combustion device is planned in which combustion gas is taken out from a sideways combustion gas take-off pipe 2a.

燃焼灰落下室1内には断面三角形状の区画板4が配設さ
れて該室1の下方を二室IA、IBに分割している。
A partition plate 4 having a triangular cross section is disposed within the combustion ash falling chamber 1 to divide the lower part of the chamber 1 into two chambers IA and IB.

室1Aは燃焼室3の下側に位置してかり、また両室IA
、IB間は液密か保たれていて、液面レベルが区画板4
の」一端を超えると、画室間で液(水)が流通する。
Chamber 1A is located below the combustion chamber 3, and both chambers IA
, IB is kept liquid-tight, and the liquid level is at partition plate 4.
Beyond one end of the chamber, liquid (water) flows between the chambers.

しかしてこの燃焼灰落下室1の外側には密閉タンク5が
設けられ、このタンク5の底部と燃焼灰落下室1Bの底
部とは連通路6を介して連通している。
However, a closed tank 5 is provided outside the combustion ash falling chamber 1, and the bottom of this tank 5 and the bottom of the combustion ash falling chamber 1B communicate with each other via a communication passage 6.

また落下室1の上部と密閉タンク5の上部とは等圧管7
によって連通し、画室は常時回jJ二に保たれている。
Also, the upper part of the drop chamber 1 and the upper part of the sealed tank 5 are the equal pressure pipe 7.
The painting room is always kept at 2 times.

密閉タンク5内には水中(ザンド)ポンプ8、定レベル
給水装置9:$、−よび液面レベル検出器10が設げら
れている。
A submersible pump 8, a constant level water supply device 9, and a liquid level detector 10 are provided in the sealed tank 5.

水中ポンプ8の吐出管11は密閉タンク5を出て分岐し
、一方の分岐管11aは燃焼灰落下室IA、IBの撹拌
パイプ12A。
A discharge pipe 11 of the submersible pump 8 exits the closed tank 5 and branches, and one branch pipe 11a is a stirring pipe 12A for the combustion ash falling chambers IA and IB.

12Bに、他方の分岐管11bは沈澱バッグ13にそれ
ぞれ接続されている。
12B and the other branch pipe 11b are connected to the sedimentation bag 13, respectively.

撹拌パイプ12A。12Bは周面に多数の噴水ノズルを
穿設したもので、水中ポンプ8の吐出水が噴射されると
、落下室IA、IB内に沈澱している燃焼灰と水とがよ
く撹拌される。
Stirring pipe 12A. 12B has a large number of fountain nozzles bored on its circumferential surface, and when water discharged from the submersible pump 8 is injected, the combustion ash and water precipitated in the falling chambers IA and IB are thoroughly stirred.

t−た沈澱バッグ13は固液分離装置として最も単純な
ものであって、槽14中に「材15を置き、P材15の
上に吐出管11.11bから吐出される有塵水を注ぎ、
P材15によって清浄にされた水を排出管16から外に
流すようにしている。
The sedimentation bag 13 is the simplest type of solid-liquid separator, and a material 15 is placed in a tank 14, and dusty water discharged from a discharge pipe 11.11b is poured onto the P material 15. ,
The water purified by the P material 15 is allowed to flow out from the discharge pipe 16.

水中ポンプ8からの吐出水は、分岐管11atたは11
bに択一的に供給されるものであって、そのため分岐管
11a、11bの分岐部には流路切換装置17が設けら
れている。
The water discharged from the submersible pump 8 is transferred to a branch pipe 11at or 11.
For this purpose, a flow path switching device 17 is provided at the branch portion of the branch pipes 11a and 11b.

この流路切換装置17は水中ポンプ8の運転開始直後に
は一定の時間吐出水を分岐管11a側に流し、その後は
分岐管1ib側に流す公知の切換弁からなっている。
This flow path switching device 17 is composed of a known switching valve that allows discharged water to flow to the branch pipe 11a side for a certain period of time immediately after the submersible pump 8 starts operating, and thereafter to flow to the branch pipe 1ib side.

上記定レベル給水装置9は液面レベルによって上下する
フロート18により、給水管19の開閉弁20を開閉す
るようにしたもので、給水管19から密閉タンク5あ・
よび燃焼灰落下室1内に供給される水位レベルの最高位
を規制する。
The constant level water supply device 9 is configured to open and close an on-off valve 20 of a water supply pipe 19 using a float 18 that moves up and down depending on the liquid level.
and regulates the maximum water level supplied into the combustion ash fall chamber 1.

この高水位レベルHは落下室1内の区画板4の上端位置
より高い。
This high water level H is higher than the upper end position of the partition plate 4 in the drop chamber 1.

また上記液面レベル検出器10は水中ポンプ8により密
閉タンク5内の水位レベルが一定値以下となってときフ
ロート21によりこれを検出し該水中ポンプ8の運転停
止信号を発する。
Further, when the water level in the sealed tank 5 is lower than a certain value by the submersible pump 8, the liquid level detector 10 detects this using the float 21 and issues a signal to stop the operation of the submersible pump 8.

水中ポンプ8の運転開始(pよび停止)信号は操作者の
判断で与えることも勿論可能であるが、自動運転のため
にはタイマ22により定期的に運転開始するのがよい。
Although it is of course possible to give the operation start (p and stop) signal for the submersible pump 8 at the discretion of the operator, it is preferable to start operation periodically using the timer 22 for automatic operation.

上記構成に係る本装置は、燃焼装置2にかげる固形燃料
の燃焼により生ずる燃焼灰が高水位レベルに保たれてい
る室1内の水中に落下する。
In this apparatus having the above-mentioned configuration, combustion ash produced by combustion of the solid fuel heated in the combustion device 2 falls into water in the chamber 1 maintained at a high water level.

そして燃焼が継続すると室1の水中に溶は込むばかりか
水面上に堆積状となってぐる。
As the combustion continues, it not only dissolves into the water in chamber 1, but also forms a deposit on the water surface.

このような状態にかいてタイマー22により水中ポンプ
8を駆動すると、その吐出水が1ず吐出管11、流路切
換装置17pよび分岐管11aを介して撹拌パイプ12
A、12Bに供給され噴射ノズルから室1A1B内に噴
射されるため室IA、IBの水pよび燃焼灰が撹拌混合
されることとなる。
When the submersible pump 8 is driven by the timer 22 in such a state, the discharged water is first transferred to the stirring pipe 12 via the discharge pipe 11, the flow path switching device 17p and the branch pipe 11a.
A and 12B and is injected from the injection nozzle into the chamber 1A1B, so that the water p and combustion ash in the chambers IA and IB are stirred and mixed.

水位レベルは室IA、IB間の区画板4の上端より高い
からこの攪拌混合は画室間に渡って行なわれ、特に燃焼
室3の直下にあって灰の多い室1人側から室1B側に灰
を含む水が移動する。
Since the water level is higher than the upper end of the partition plate 4 between chambers IA and IB, this agitation and mixing is carried out between the compartments, especially from the 1-person side of the chamber where there is a lot of ash, which is directly below the combustion chamber 3, to the chamber 1B side. Water containing ash moves.

次いで流路切換装置17が水中ポンプ8の吐出水を分岐
管11b側に流し、沈澱バッグ13の評材15上に灰を
含む水を供給するようになると、密閉タンク5および該
タンクと連通路6によって連通ずる燃焼灰落下室1内の
水位は低下してゆきついには液面レベル検出器10が水
中ポンプ8の運転を停止する。
Next, the flow path switching device 17 causes the discharge water of the submersible pump 8 to flow to the branch pipe 11b side, and when water containing ash is supplied onto the evaluation material 15 of the sedimentation bag 13, the closed tank 5 and the communication path with the tank are connected. 6, the water level in the combustion ash falling chamber 1, which is communicated with, decreases, and finally the liquid level detector 10 stops the operation of the submersible pump 8.

つ1り燃焼灰が水とともに取り出されるわけである。The combustion ash is taken out along with water.

この間燃焼灰落下室1B側の水位はタンク5の水位の低
下とともに低下していくが、室1人は区画板4により室
1Bと分離されているため、該室1人の水位は区画板4
の上端より下がることはない。
During this time, the water level in the combustion ash fall chamber 1B side decreases as the water level in the tank 5 decreases, but since one person in the chamber is separated from the chamber 1B by the partition plate 4, the water level for one person in the chamber is lower than the one in the partition plate 4.
It cannot fall below the upper limit of .

このため水中ポンプ8の運転中にも継続されている燃焼
装置2からの燃焼灰を室1Aの水中に確実に捕捉するこ
とができる。
Therefore, even while the submersible pump 8 is in operation, the combustion ash from the combustion device 2 can be reliably captured in the water in the chamber 1A.

そして水中ポンプ8が停止するときには既にフロート1
8により開閉弁20が開いて給水管19により密閉タン
ク5内に給水が開始されているため、やがて密閉タンク
5および燃焼灰落下室1内には最初の状態の高水位レベ
ルH迄水が供給される。
When the submersible pump 8 stops, the float 1 is already
8 opens the on-off valve 20 and starts supplying water into the closed tank 5 through the water supply pipe 19, so water is eventually supplied into the closed tank 5 and the combustion ash falling chamber 1 up to the initial high water level H. be done.

したがって一定時間後には上記と全く同じ動作で燃焼灰
の取り出しを行なうことができる。
Therefore, after a certain period of time, the combustion ash can be removed by the same operation as above.

なp沈澱バッグ13の胛材15上に供給された有塵水は
、炉水15によって灰を分離した後排出管16から排水
される。
The dusty water supplied onto the slag material 15 of the p-sedimentation bag 13 is drained from the discharge pipe 16 after the ash is separated by the reactor water 15.

胛材15上の燃焼灰は後に適宜取り除くことができる。The combustion ashes on the lint 15 can be appropriately removed later.

筺た水中ポンプ8の吐出水を分岐管11b側に流しなが
ら給水管19から密閉タンク5内に給水してもよい。
Water may be supplied into the closed tank 5 from the water supply pipe 19 while flowing the water discharged from the submersible pump 8 into the branch pipe 11b.

上記実施例では燃焼灰落下室1を二基に分割して一方の
室には常時水が存在するようにしているため、燃焼灰取
出動作中も確実に燃焼灰を水中に捕えることができると
いう利点があるが、二基、に分割しなくとも燃焼灰の自
動取出を行なうことが可能である。
In the above embodiment, the combustion ash falling chamber 1 is divided into two parts so that water is always present in one of the chambers, so that the combustion ash can be reliably trapped in the water even during the combustion ash removal operation. An advantage is that it is possible to automatically remove combustion ash without having to divide the system into two units.

また水中ポンプの運転開始あ・よび停止は手動操作によ
ってもよく、さらに固液分離装置として沈澱バック13
以外の他の装置を用いることができる。
In addition, the operation of the submersible pump can be started and stopped by manual operation.
Other devices can be used.

以上要するに本発明は、燃焼室で生ずる燃焼灰を落下室
の水中に落下させ、この燃焼灰を含む水を、落下室に通
ずる密閉タンク内に配設した水中ポンプからの吐出水に
より攪拌混合した後、該水中ポンプにより外部の固液分
離装置に導ぐようにしたものであって、落下室pよび密
閉タンクにはその後再び定レベル迄水が供給されるもの
であるから、上記動作を定時間毎に繰り返すことにより
燃焼装置の燃焼を停止させることなく燃焼灰の取り出し
を行なうことができる。
In summary, the present invention allows combustion ash generated in a combustion chamber to fall into water in a falling chamber, and the water containing this combustion ash is stirred and mixed by water discharged from a submersible pump disposed in a sealed tank communicating with the falling chamber. After that, water is introduced to an external solid-liquid separator by the submersible pump, and water is then supplied to the falling chamber p and the closed tank again to a certain level, so the above operation is not determined. By repeating this every hour, the combustion ash can be removed without stopping the combustion of the combustion device.

したがって固形燃料燃焼装置の24時間運転を可能とし
、その実用性を高めることができる。
Therefore, the solid fuel combustion device can be operated for 24 hours, and its practicality can be improved.

またこの出願の発明にかいて、最初の水中ポンプ運転中
は供給水が分岐管11aを通って室1Aの攪拌パイプ1
2A及び室1Bの攪拌パイプ12Bから噴射し燃焼室か
ら落下する燃焼灰は先づ攪拌パイプ12Aによって水と
混合し、次いで攪拌パイプ12Bによって混合が重複し
、この混合水は連通管6を経て密閉タンク5に入り、水
中ポンプ8に吸入され、ポンプの吐出管11を介して分
岐管11aに循環するがこの循環混合回路は再度重複さ
れて行はれるので燃焼灰と水は連続的に完全に混合され
た後、流路切換装置17の切換えにより上記の混合水は
分岐管11bから沈澱タンク13に入り、燃焼灰と水が
分離し燃焼灰の取出が行はれる。
Further, according to the invention of this application, during the first submersible pump operation, the supply water passes through the branch pipe 11a to the stirring pipe 1 of the chamber 1A.
The combustion ash that is injected from the stirring pipes 12B of the chambers 2A and 1B and falling from the combustion chamber is first mixed with water by the stirring pipes 12A, and then the mixing is repeated by the stirring pipes 12B, and this mixed water is passed through the communication pipe 6 and sealed. It enters the tank 5, is sucked into the submersible pump 8, and is circulated through the pump's discharge pipe 11 to the branch pipe 11a, but this circulation mixing circuit is repeated again, so that the combustion ash and water are continuously completely removed. After being mixed, by switching the flow path switching device 17, the mixed water enters the settling tank 13 from the branch pipe 11b, the combustion ash and water are separated, and the combustion ash is taken out.

そして、この燃焼灰取出行程中に燃焼室から落下室内に
燃焼灰が落下堆積しても次の攪拌混合行程により充分な
混合が行はれるから炉の連続運転による燃焼灰の連続落
下があっても充分灰を処理することができる。
Even if combustion ash falls and accumulates in the falling chamber from the combustion chamber during this combustion ash removal process, sufficient mixing is achieved in the next stirring and mixing process, so the continuous operation of the furnace prevents the combustion ash from falling continuously. It is also possible to dispose of ash sufficiently.

したがってこの発明によれば水と燃焼灰の混合効率がき
わめて良く、混合状態を良くするための特別な装置、そ
れに要する動力がなくてよいので経費と動力を節約する
ことができる。
Therefore, according to the present invention, the mixing efficiency of water and combustion ash is extremely high, and there is no need for a special device for improving the mixing state or the power required for it, so that cost and power can be saved.

また上記の混合水の循環には水を補給する必要がないた
め燃焼灰取出装置に送る水量はポンプの能力範囲内であ
り他のポンプを使用する必要がなく、動力と補給水の節
約を図ることができ経済的に有利である。
In addition, since there is no need to replenish water to circulate the above mixed water, the amount of water sent to the combustion ash removal device is within the capacity of the pump, and there is no need to use other pumps, saving power and replenishment water. It is economically advantageous.

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

図は本発明に係る燃焼灰取出装置の実施例を示すもので
、第1図は燃焼装置の燃焼室と燃焼灰落下室部分の縦断
面図、第2図は燃焼灰落下室、密閉タンクpよび沈澱バ
ッグ間の接続関係を示す斜視図である。 1・・・燃焼灰落下室、2・・・固形燃料燃焼装置、3
・・・燃焼室、4・・・区画板、5・・・密閉タンク、
6・・・連通路、7・・・等圧管、8・・・水中ポンプ
、9・・穴レベル給水装置、10・・・液面レベル検出
器、11・・・吐出管、11a、 1 l b=分岐管
、12A、12B・・・攪拌パイプ、13・・・沈澱バ
ッグ、17・・・流路切換装置、21・・・タイマ。
The figures show an embodiment of the combustion ash removal device according to the present invention, and FIG. 1 is a longitudinal cross-sectional view of the combustion chamber and combustion ash falling chamber of the combustion device, and FIG. 2 shows the combustion ash falling chamber and the sealed tank p. FIG. 1... Combustion ash fall chamber, 2... Solid fuel combustion device, 3
... Combustion chamber, 4... Partition plate, 5... Sealed tank,
6... Communication path, 7... Equal pressure pipe, 8... Submersible pump, 9... Hole level water supply device, 10... Liquid level detector, 11... Discharge pipe, 11a, 1 l b = Branch pipe, 12A, 12B... Stirring pipe, 13... Sedimentation bag, 17... Channel switching device, 21... Timer.

Claims (1)

【特許請求の範囲】[Claims] 1 燃焼灰落下室内に前後二本の攪拌パイプを通すと共
に、一方の攪拌パイプの上方を固形燃料の燃焼室下方に
臨1せ、他方の攪拌パイプのある側の室の底部を密閉タ
ンクに連通ずると共に密閉タンクと上記落下室の各上部
を等圧管で連通し、密閉タンクには定レベル給水装置と
水中ポンプを設けると共に水中ポンプの吐出管には撹拌
パイプに接続する分岐管と固液分離装置に接続する分岐
管を設け、その分岐位置にポンプの運転開始後一定時間
中は上記撹拌パイプに給水し、其の後固液分離装置に切
換えて給水する流路切換装置を設けたことを特徴とする
燃焼灰取出装置。
1 Pass two stirring pipes in the front and back inside the combustion ash falling chamber, and place the upper part of one stirring pipe facing below the solid fuel combustion chamber, and connect the bottom of the chamber on the side where the other stirring pipe is located to the closed tank. The closed tank is connected to the upper part of the above-mentioned drop chamber by an equal pressure pipe, and the closed tank is equipped with a constant level water supply device and a submersible pump, and the discharge pipe of the submersible pump is equipped with a branch pipe connected to the stirring pipe and solid-liquid separation. A branch pipe connected to the device is provided, and a flow path switching device is installed at the branch position to supply water to the stirring pipe for a certain period of time after the pump starts operating, and then switch to the solid-liquid separation device to supply water. Characteristic combustion ash removal device.
JP13335081A 1980-06-10 1981-08-27 Combustion ash removal device Expired JPS5857645B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP13335081A JPS5857645B2 (en) 1981-08-27 1981-08-27 Combustion ash removal device
CA000391387A CA1180954A (en) 1980-12-09 1981-12-02 Combustion apparatus for granular solid fuel
US06/327,258 US4432288A (en) 1980-12-09 1981-12-03 Combustion apparatus for granular solid fuel
AU78371/81A AU7837181A (en) 1980-06-10 1981-12-08 Combustion apparatus for solid granular fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13335081A JPS5857645B2 (en) 1981-08-27 1981-08-27 Combustion ash removal device

Publications (2)

Publication Number Publication Date
JPS5835318A JPS5835318A (en) 1983-03-02
JPS5857645B2 true JPS5857645B2 (en) 1983-12-21

Family

ID=15102661

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13335081A Expired JPS5857645B2 (en) 1980-06-10 1981-08-27 Combustion ash removal device

Country Status (1)

Country Link
JP (1) JPS5857645B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62147851U (en) * 1986-03-13 1987-09-18
JPH0416111Y2 (en) * 1983-05-30 1992-04-10

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0416111Y2 (en) * 1983-05-30 1992-04-10
JPS62147851U (en) * 1986-03-13 1987-09-18

Also Published As

Publication number Publication date
JPS5835318A (en) 1983-03-02

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