JPS58175710A - Combustion device - Google Patents

Combustion device

Info

Publication number
JPS58175710A
JPS58175710A JP5734582A JP5734582A JPS58175710A JP S58175710 A JPS58175710 A JP S58175710A JP 5734582 A JP5734582 A JP 5734582A JP 5734582 A JP5734582 A JP 5734582A JP S58175710 A JPS58175710 A JP S58175710A
Authority
JP
Japan
Prior art keywords
combustion
chamber
fuel
dust collector
cyclone 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
JP5734582A
Other languages
Japanese (ja)
Inventor
Kiyomi Okada
岡田 清已
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 JP5734582A priority Critical patent/JPS58175710A/en
Publication of JPS58175710A publication Critical patent/JPS58175710A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23KFEEDING FUEL TO COMBUSTION APPARATUS
    • F23K1/00Preparation of lump or pulverulent fuel in readiness for delivery to combustion apparatus
    • F23K1/04Heating fuel prior to delivery to combustion apparatus

Landscapes

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

Abstract

PURPOSE:To make possible the preheating of granular fuel by connecting a combustion chamber with a vertical cyclotron dust collector through a preheating pipe passing a fuel blowing chamber. CONSTITUTION:A part of the upper portion of the partition wall 7 between a fuel blowing chamber 1 and a combustion chamber 2 is notched to make up a connecting port 10 between these chambers and a preheating pipe 11 is located in the axial portion of both chambers 1, 2. One end of this preheating pipe 11 opens facing the control taper portion 12 of the end wall 6 of the combustion chamber 2 while the other opens in the upper tangential direction of a cylinder 13 outside a cyclone dust collector 4 through a fuel blowing chamber 1. Thus, before combustion, combustion gas preheats granular coal fuel blown into the fuel blowing chamber 1 through a preheating pipe 11 leading to the cyclone dust collector 4 and gasifies tar component contained in fuel to modify the fuel into non-caking one, to prevent foreign matters from attaching to the combustion chamber inside wall and combustion troubles from occurring.

Description

【発明の詳細な説明】 本発明は、給湯、暖房、温室、乾燥機等の熱源となる、
粒状固形燃料を用いる燃焼装置に係シ、特に粘結質の石
炭系燃料を燃焼させる場合に好適ガ燃焼装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides heat sources for hot water supply, space heating, greenhouses, dryers, etc.
The present invention relates to a combustion device using granular solid fuel, and particularly to a combustion device suitable for burning cohesive coal-based fuel.

石油の供給不安から石炭その他の固形燃料の見直しが叫
ばれているが、これら固形燃料は完全燃焼させること、
あるいは簡易な装置で高火力を得ることが困難である。
Due to concerns about oil supply, there are calls for a review of coal and other solid fuels, but these solid fuels must be completely combusted;
Or it is difficult to obtain high firepower with a simple device.

その中で固形燃料を粒状化(粉状化)シ、これを攪拌浮
上させた状態で燃焼させる、いわゆる流動床燃焼が上記
問題点を解決する燃焼方法として注目されているが、構
造の簡易な小型の燃焼装置により上記のような燃焼を完
全に行なわせることは困難であった。
Among these, so-called fluidized bed combustion, in which solid fuel is granulated (pulverized) and then combusted while being agitated and floated, is attracting attention as a combustion method that solves the above problems. It has been difficult to completely carry out the above-mentioned combustion using a small-sized combustion device.

本出願人は、このような背景に鎌み、既に小−3− 型の装置であって粒状燃料を攪拌浮上状態で燃焼させる
ことができる燃焼装置を提案している。
Taking advantage of this background, the present applicant has already proposed a combustion device which is a small 3-type device and is capable of burning granular fuel in an agitated floating state.

この燃焼装置は基本的には横向きの筒状燃焼室内に渦流
を生ぜしめて粒状燃料を燃焼させ、その燃焼ガスを燃焼
ガス取出室に導いて該取出室内に臨ませた燃焼ガス取出
管から外部に取シ出すようにし友ものであり、良好な燃
焼を行なわせることができる。
This combustion device basically creates a vortex in a horizontally oriented cylindrical combustion chamber to burn granular fuel, guides the combustion gas into a combustion gas extraction chamber, and then exits it outside through a combustion gas extraction pipe facing into the extraction chamber. It is easy to take out the fuel and allows for good combustion.

ところがこの燃焼装置では、オイルコークス、石炭コー
クス等の非粘結質の石炭系燃料を燃焼させる場合には燃
焼室内壁に異物、つまシ燃焼生成物が付着することは少
ないが、タール分を多く含有する粘結質の石炭系燃料を
燃焼させると、燃焼室内壁に異物が付着堆積することが
あり、これが不完全燃焼等の燃焼トラブルを発生させ、
あるいは繁煩な分解掃除を余儀なくさせる原因となって
いた。またこの燃焼装置では燃焼ガス中の燃焼灰の含有
率が比較的高く、塵を嫌う用途゛にあってはさらに効果
的に燃焼灰を除去することが望まれている。
However, with this combustion device, when burning non-caking coal-based fuels such as oil coke and coal coke, there is little chance of foreign matter or scum combustion products adhering to the combustion chamber wall, but it does produce a large amount of tar. When coal-based fuel containing cohesive substances is burnt, foreign matter may adhere to and accumulate on the combustion chamber walls, causing combustion troubles such as incomplete combustion.
Otherwise, it may be necessary to carry out troublesome disassembly and cleaning. Further, in this combustion device, the content of combustion ash in the combustion gas is relatively high, and in applications where dust is averse, it is desired to remove combustion ash even more effectively.

特開昭58−175710(2) 本発明は、このような問題点を解消してより優れた燃焼
装置を得ることを目的になされたもので、筒状燃焼室に
吹き込む石炭系粒状燃料を予熱することによシ骸燃料に
含まれるタール分をガス化して非粘結質燃料に変化させ
ること、および上記予熱は該燃料の燃焼によって生ずる
熱を利用して行なうこと、の二点に着目してよシ完全な
燃焼を行なわせることができるようにし、他方燃焼灰の
問題についてはサイクロン集塵装置を用いてより効率的
な集塵ができるようにしている。
JP-A-58-175710 (2) The present invention was made for the purpose of solving these problems and obtaining a better combustion device. We focused on two points: by doing this, the tar content contained in the carcass fuel is gasified and changed into a non-caking fuel, and the above-mentioned preheating is performed using the heat generated by combustion of the fuel. A cyclone dust collector is used to achieve more efficient dust collection in order to ensure complete combustion.

このような着眼に基きなされた本発明燃焼装置は、燃料
吹込室の一側に燃焼室、他側に内部にサイクロン集塵装
置を設けた燃焼ガス取出室を設け、燃焼室で燃焼させた
燃焼ガスを上記燃料吹込室を通る予熱管を介してサイク
ロン集塵装置に導くことによシ、燃料吹込室に吹き込ま
れる粒状燃料を該予熱管によシ予熱できるようにし、他
方サイクロン集塵装置に導いた燃焼ガスは、燃焼ガス取
出室に連通させた該集塵装置S − の排気筒、および燃焼ガス取出室に開口させた燃焼ガス
取出管を介して外部に導くようにしたことを特徴として
いる。
The combustion apparatus of the present invention, which was created based on such considerations, has a combustion chamber on one side of the fuel injection chamber, and a combustion gas extraction chamber equipped with an internal cyclone dust collector on the other side, and the combustion By guiding the gas to the cyclone dust collector through a preheating pipe passing through the fuel injection chamber, the granular fuel blown into the fuel injection chamber can be preheated by the preheating pipe, while the cyclone dust collector The guided combustion gas is led to the outside through the exhaust pipe of the dust collector S- which is communicated with the combustion gas extraction chamber, and the combustion gas extraction pipe opened into the combustion gas extraction chamber. There is.

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.

本燃焼装置は、中央部の燃料吹込室lと、この吹込室l
の一側(第1図右側)に設けた燃焼室λと、他側(同左
側)に設けた燃焼ガス取出室3とを有し、燃焼ガス取出
室3内には周囲との隙間を保ってサイクロン集塵装置弘
が配設されている。上記室/2.2はいずれも軸を水平
にした横向きの円筒状、室3は縦型のサイクロン集塵装
置Vに見合う形状であって、耐火材料からなる外殻体j
1端壁6および隔壁7,1等から構成されている。りは
外殻体j内に埋込んだ冷却水または冷却空気の循環パイ
プ、りα、ybはその入口と出口である。− 燃料吹込室lと燃焼室2間の隔壁7は、その上方一部を
切欠いて両室間の連通口lOを構成しておシ、また両室
l2.2の軸部には予熱管/lが配設されている。この
予熱管//はその一端が燃j− 焼室コの端壁6の中央テーバ部/2に臨んで開口してお
り、他端は燃料吹込室/を通ってサイクロン集塵装置弘
の外側円筒体/3の上部接線方向に開口している。
This combustion device has a fuel injection chamber l in the center and a fuel injection chamber l in the center.
It has a combustion chamber λ provided on one side (right side in Figure 1) and a combustion gas extraction chamber 3 provided on the other side (left side of the same), and a gap is maintained in the combustion gas extraction chamber 3 with the surroundings. A cyclone dust collector is installed. The above-mentioned chambers 2.2 and 2.2 each have a horizontal cylindrical shape with horizontal axes, and chamber 3 has a shape suitable for a vertical cyclone dust collector V, and has an outer shell made of a refractory material.
It is composed of one end wall 6, partition walls 7, 1, etc. ri is a circulation pipe for cooling water or cooling air embedded in the outer shell j, and ri α and yb are its inlet and outlet. - The upper part of the partition wall 7 between the fuel injection chamber l and the combustion chamber 2 is cut out to form a communication port lO between the two chambers, and a preheating pipe/ l is arranged. One end of this preheating pipe // is open facing the central tapered part /2 of the end wall 6 of the combustion chamber, and the other end passes through the fuel injection chamber / to the outside of the cyclone dust collector. It opens in the tangential direction of the upper part of the cylinder body /3.

サイクロン集塵装置≠は周知のように外側円筒体13の
下方を徐々に縮径する縮径部/≠としてその下方に集塵
室/jを連設する一方、外側円筒体13の軸部に排気筒
/6を配設して形成されている。予熱管//は外側円筒
体/3の接線方向に開口しているため、該円筒体内に吹
き込まれる燃焼ガスは渦巻形に円筒体13内に流れ込み
、比重の重い塵が外側に移りつつガスと分離して下方の
集塵室/jに落ち、清浄ガスが軸部排気筒/乙に導かれ
る。排気筒/6は燃焼ガス取出室3と連通しており、燃
焼ガス取出室3には適宜位置に燃焼ガス取出管17が開
口している。
As is well known, in the cyclone dust collector≠, the lower part of the outer cylindrical body 13 has a diameter reducing part /≠ that gradually reduces the diameter, and the dust collection chamber /j is connected to the lower part of the lower part of the outer cylindrical body 13. It is formed by arranging an exhaust pipe/6. Since the preheating pipe // is open in the tangential direction of the outer cylindrical body /3, the combustion gas blown into the cylindrical body flows into the cylindrical body 13 in a spiral shape, and the dust with heavy specific gravity moves to the outside and is mixed with gas. It separates and falls into the dust collection chamber /j below, and the clean gas is led to the shaft exhaust pipe /b. The exhaust pipe/6 communicates with the combustion gas extraction chamber 3, and a combustion gas extraction pipe 17 opens at an appropriate position in the combustion gas extraction chamber 3.

しかして上記燃料吹込室lには、第5図に明らかなよう
に、円筒状の該吹込室の接線方向に向けて下方に空気供
給管2!が、そのやや上方に燃料供給管ムがそれぞれ開
口している。燃料供−7− 給管26は第5図に示すように、燃料貯留ホッパ27の
燃料混合管l♂およびブロワ2Pに順次接続され、燃料
混合管jIr内には駆動装置30(第6図)によって駆
動される搬送スクリュ31が挿入されていて、このスク
リュの回転によりホッハ、2Z内の粒状(粉粒)燃料が
燃料供給管−6内に導かれる。燃料の供給量は搬送スク
リュ31の回転速度の変更により調整することができ、
空気tは流量調整弁3λの開度により調整できる。
As is clear from FIG. 5, the fuel injection chamber 1 has an air supply pipe 2 extending downward in the tangential direction of the cylindrical injection chamber! However, fuel supply pipes open slightly above them. Fuel Supply-7- As shown in FIG. 5, the supply pipe 26 is sequentially connected to the fuel mixing pipe l♂ of the fuel storage hopper 27 and the blower 2P, and a drive device 30 (see FIG. 6) is installed in the fuel mixing pipe jIr. A conveyance screw 31 driven by a conveyor screw 31 is inserted, and the rotation of this screw guides the granular (powder) fuel in the Hoch 2Z into the fuel supply pipe 6. The amount of fuel supplied can be adjusted by changing the rotational speed of the conveying screw 31.
The air t can be adjusted by the opening degree of the flow rate regulating valve 3λ.

また燃焼室λには、燃料吹込室/の空気供給管コjと同
様に、該室の接線方向に向けて空気供給管33,3弘が
開口している。これらの空気供給管、2j 、 !! 
、 j弘はそれぞれ開閉弁34 、37 、311を介
して上記ブロワλりに接続されている。
Further, air supply pipes 33, 3 are opened in the combustion chamber λ in the tangential direction of the combustion chamber, similar to the air supply pipes 33 and 3 of the fuel injection chamber. These air supply pipes, 2j,! !
, and are connected to the blower λ via on-off valves 34, 37, and 311, respectively.

さらに燃焼室コには着火炎導入管≠lが開口している。Furthermore, an ignition flame introduction pipe≠l opens into the combustion chamber.

この導入管は最上流が開閉弁≠2を介して上記ブロワ、
2りに接続されておシ、その途中にはエジェクタ≠3お
よび開閉弁t≠を介してガスボンベ弘jが接続されてい
る。この着火装置は、エジェクタ≠3により着火ガスと
空気とを混合してこれに点火プラグ≠4によシ着火し、
その着火炎を導入管弘lから燃焼室λ内に噴出させるも
のである。なお符号≠7.4Zざ、≠りはそれぞれ室l
、2゜3の点検覗き窓を、jOは燃焼室コの14壁乙に
設けた温度検知器を示す。
The most upstream side of this introduction pipe is connected to the blower via the on-off valve≠2.
2, and in the middle thereof, a gas cylinder hiroj is connected via an ejector≠3 and an on-off valve t≠. This ignition device mixes ignition gas and air using an ejector≠3 and ignites the mixture using a spark plug≠4.
The ignition flame is ejected from the introduction pipe 1 into the combustion chamber λ. Note that the symbols ≠7.4Zza and ≠ri are room l, respectively.
, 2°3 inspection viewing window, and jO indicates a temperature sensor installed on the 14th wall of the combustion chamber.

上記構成に係る本装置は、ブロワλりと燃料貯留ホッパ
27の駆動装置30を同時に駆動すると、タール分を含
む右脚系粒状燃料が燃料供給管26から燃料吹込室/に
吹き出され、これが空気供給管コjからの空気流によシ
攪拌されて渦状となる。空気供給管コ!は燃料供給管2
60吹出部近傍に開口しているため、この粒状燃料の攪
拌浮上は効果的に行なわれる。
In this device having the above configuration, when the blower λ and the driving device 30 of the fuel storage hopper 27 are driven simultaneously, the right leg type granular fuel containing tar is blown out from the fuel supply pipe 26 into the fuel injection chamber/ It is stirred by the air flow from the supply pipe and becomes vortex-like. Air supply pipe! is fuel supply pipe 2
Since the opening is in the vicinity of the outlet 60, the granular fuel is effectively stirred and floated.

このようにして攪拌浮上状態となった粒状燃料は、隔壁
7に設けた上部連通口ioを介して燃焼室λに入り、空
気供給管33 、34Lからの空気流により渦流を強化
され、着火炎導入管弘lからの着火ガスによシ着火され
る。したがって流動状態の燃焼が開始され、燃焼ガスは
予熱管1lt−通って燃焼ガス取出室3内のサイクロン
集塵it2− 弘に噴出する。燃焼室λ内では未燃分を多く含む重量の
大な燃料は渦流の遠心力により該室の外側に位置し、燃
焼後の軽いガスが予熱管ti内に入るから、よシ完全な
燃焼を行なわせることができる。
The granular fuel thus stirred and floated enters the combustion chamber λ via the upper communication port io provided in the partition wall 7, and the vortex is strengthened by the air flow from the air supply pipes 33 and 34L, causing an ignition flame. It is ignited by the ignition gas from the inlet pipe. Therefore, combustion in a fluid state is started, and the combustion gas passes through the preheating pipe 1lt and is ejected to the cyclone dust collection part 2 in the combustion gas extraction chamber 3. In the combustion chamber λ, the heavy fuel containing a large amount of unburned matter is located outside the chamber due to the centrifugal force of the vortex, and the light gas after combustion enters the preheating tube ti, ensuring more complete combustion. I can make you do it.

以上の燃焼が定常的に行なわれると、予熱管//U高温
となシ、したがって燃料吹出室/も高温となる。本発明
はこの熱を利用して燃焼前のタール分を含む粘結質の石
炭°糸粒状燃料を予熱するのである。すなわち上記燃料
が加熱状態となると、該燃料に含まれるタール分がガス
化し、粘結質であった粒状燃料が非粘結質に変化するの
である。この変化は化学的には主として石炭系燃料を燃
焼の前工程において乾留するのに相当する。燃料吹込室
lにおける加熱温度は予熱管//の表面積、粒状燃料の
滞留時間等にょシ異なるが、これらのi素を適尚に設定
して上記乾留が行なわれるようKするのである。特に予
熱管/Iの長iと太さ、連通口10の大きさは大きな要
因である。
When the above combustion is carried out steadily, the temperature of the preheating pipe//U becomes high, and therefore the temperature of the fuel blowing chamber// becomes high as well. The present invention utilizes this heat to preheat the tar-containing cohesive coal/string granular fuel before combustion. That is, when the fuel is heated, the tar contained in the fuel is gasified, and the granular fuel, which was a caking substance, changes to a non-caking substance. Chemically, this change corresponds primarily to carbonization of coal-based fuels in the pre-combustion process. The heating temperature in the fuel injection chamber 1 varies depending on the surface area of the preheating tube, the residence time of the granular fuel, etc., but these elements are appropriately set so that the above carbonization is carried out. In particular, the length i and thickness of the preheating tube/I and the size of the communication port 10 are major factors.

10− したがって燃焼室−で行なわれる定常的な燃焼は、性質
を非粘結質に変化させた粒状燃料について行なわれるこ
ととなるから、該室Jの壁面、予熱管l/の壁面等に異
物が付着堆積する可能性は極めて少なくなる。
10 - Therefore, the steady combustion that takes place in the combustion chamber - is carried out using granular fuel whose properties have been changed to non-caking, so there is no foreign matter on the wall surface of the chamber J, the wall surface of the preheating tube L/, etc. The possibility of adhesion and accumulation is extremely reduced.

予熱管l/からサイクロン集塵装置≠に入った燃焼ガス
は、前述のように渦状のガス流と塵の自重の作用により
、塵を集塵室lj内に落下分離した後、軸部の排気筒1
6がら燃焼ガス取出室3内に入シ、燃焼ガス取出管/7
がら清浄な高温ガスとして取り出される。
The combustion gas that enters the cyclone dust collector≠ from the preheating pipe l/ falls into the dust collection chamber lj and is separated by the action of the swirling gas flow and the dust's own weight as described above, and then is discharged from the shaft part. cylinder 1
6 enters combustion gas extraction chamber 3, combustion gas extraction pipe/7
It is extracted as clean high-temperature gas.

排気筒/4は直接燃焼ガス電出管17と接続して吃よい
が、図示例のように燃焼ガス取出室3を設けてことに連
通させれば、取出管17を取出室3の任意の位置に開口
させることができるという利点が得られる。
The exhaust pipe 4 can be directly connected to the combustion gas discharge pipe 17 for better performance, but if the combustion gas extraction chamber 3 is provided as shown in the figure and communicated with the combustion gas extraction chamber 3, the exhaust pipe 17 can be connected to any part of the extraction chamber 3. The advantage is that it can be opened at any position.

ま友すイクロン集塵装置弘は、第7図に示すように予熱
管/lに関する平面的に略対称な位置に二個設け、両集
塵装置44A、4CBに予熱管1/がら燃焼ガスを供給
するようにしてもよい。この場−//− 合排気筒tAA、ttBは別個に燃焼ガス取出室3に開
口させ、あるいは集合させて直接外部に取り出すことが
できる。なおサイクロン集塵装置tは外側円筒体/3の
直径をDとしたとき、第8図のように各寸法を定めると
良好な集塵効果が得られる。
As shown in Fig. 7, two Mahyusu Ikron dust collectors are installed at substantially symmetrical positions in a plane with respect to the preheating tube/l, and both dust collectors 44A and 4CB are supplied with combustion gas from the preheating tube 1/l. It may also be supplied. In this case, the combined exhaust pipes tAA and ttB can be opened separately into the combustion gas extraction chamber 3, or can be brought together and taken out directly to the outside. In addition, when the diameter of the outer cylindrical body /3 is D, the cyclone dust collector t can obtain a good dust collection effect if each dimension is determined as shown in FIG.

燃焼室λにおける燃焼は渦流の中で行なわれるため、燃
料の攪拌浮上状態を長い時間維持することができる。こ
のような流動状態での燃焼はNOx、SOxの発生を低
減させることが知られており、したがって大気汚染の防
止に寄与しうる。
Since combustion in the combustion chamber λ takes place in a vortex, the agitation and floating state of the fuel can be maintained for a long time. Combustion in such a fluidized state is known to reduce the generation of NOx and SOx, and can therefore contribute to the prevention of air pollution.

また高灰分、高硫黄分などの低質炭の利用が可能という
利点もある。
Another advantage is that low quality coal with high ash and sulfur content can be used.

なお燃焼室内温度が約800℃を超えると、微lの水と
酸素(燃焼空気)の存在で次の反応式により水性ガス化
反応が生じ、粉炭0が燃焼しやすくなるとともに、燃焼
室壁面がアーツシュの溶解温度以上の高温にならないこ
とが知られている。
When the temperature in the combustion chamber exceeds approximately 800℃, a water gasification reaction occurs according to the following reaction equation due to the presence of a small amount of water and oxygen (combustion air), which makes it easier to burn pulverized coal and causes the wall surface of the combustion chamber to It is known that the temperature does not exceed the melting temperature of artshu.

H*O+ C+Co + Ha Co+H!+Ot→Cot + HlOまた燃料吹込室
lに微量の水を供給できるようにすれば該室の壁面の温
度を調整することができる。
H*O+ C+Co+Ha Co+H! +Ot→Cot+HlO Furthermore, if a small amount of water can be supplied to the fuel injection chamber l, the temperature of the wall surface of the chamber can be adjusted.

このため本装置では点検覗き窓≠7.弘lVc開閉lp
 jt、z、2’k 介してタンクj≠に連なる水供給
パイプ66、!6を開口させ、各室に微量の水を供給で
きるようにしている。特に燃焼室コに連なる水供給パイ
プjtの開閉弁5.2は、燃焼室−に臨ませた温度検知
器60によシ開度を制御し、燃焼室2が異常高温になる
のを防止するのが好ましい。
Therefore, in this device, the inspection viewing window≠7. Hiroshi Vc opening/closing lp
Water supply pipe 66, which is connected to tank j≠ via jt, z, 2'k! 6 is opened so that a small amount of water can be supplied to each chamber. In particular, the opening/closing valve 5.2 of the water supply pipe jt connected to the combustion chamber 2 is controlled by a temperature detector 60 facing the combustion chamber 2 to prevent the combustion chamber 2 from becoming abnormally high temperature. is preferable.

なお点検覗き窓≠7.り、≠りにそれぞれブロワλりに
連なる微量空気供給管jり、 40 、 A/を開口さ
せたのは、該窓のくもシ止めの九めである。
In addition, the inspection window≠7. It was at the ninth stop of the window that the small amount air supply pipes 40 and A/ connected to the blower λ were opened.

以上要するに本発明に係る燃焼装置によれば燃焼ガスを
サイクロン集塵装置に導く予熱管によシ、燃焼前に燃料
吹込室に吹込まれる石炭系粒状燃料を予熱し、鋏燃料に
含まれるタール分をガス化して該燃料を非粘結質に変え
ることができる。したがって燃焼室内壁に異物が付着す
73− るのを防止し、あるいは異物の付着堆積速度を遅くシ、
燃焼トラブルの発生を防止して燃焼室内清掃の一度を減
少させることができる。特に本発明によれば燃料を予熱
するにつき特別の熱源を要することな〈従来使用が困難
であった粘結質の燃料を燃焼させることができるからそ
の利用価ffiは高い。さらに本発明は燃焼ガスを最終
的にサイクロン集塵装置に導いて塵を分離した彼取り出
゛tものであるから、特にII&を嫌う乾燥機や乾燥室
に用いて好遇である。またサイクロン集塵装置を炉焼ガ
ス取出室内に配置して排気筒からの燃焼ガスを一旦該取
出室内に放出すれば、蚊取出室に開口させる取出管の位
置を自由に設定することができる。
In summary, according to the combustion device according to the present invention, the preheating pipe that guides the combustion gas to the cyclone dust collector preheats the coal-based granular fuel that is blown into the fuel injection chamber before combustion, and removes the tar contained in the shear fuel. can be gasified to turn the fuel into a non-caking substance. Therefore, it is possible to prevent foreign matter from adhering to the inner wall of the combustion chamber, or to slow down the rate at which foreign matter is deposited.
It is possible to prevent the occurrence of combustion troubles and reduce the number of times the combustion chamber must be cleaned. In particular, according to the present invention, a special heat source is not required for preheating the fuel (caking fuel, which has been difficult to use in the past, can be combusted), so its utilization value ffi is high. Furthermore, since the present invention is designed to ultimately lead the combustion gas to a cyclone dust collector and separate the dust therefrom, it is particularly suitable for use in dryers and drying rooms where II& is not desirable. Furthermore, once the cyclone dust collector is placed in the furnace gas extraction chamber and the combustion gas from the exhaust stack is discharged into the extraction chamber, the position of the extraction pipe that opens into the mosquito extraction chamber can be freely set.

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

第1図は本発明に係る燃焼装置の実施例を示す縦断面図
、第2図、第5図、第4図はそれぞれ第1図0n−n線
、■−厘線、N−IV線に沿う断面図、第5図は本燃焼
装置に対する燃料その他の供給配管系統を示す一部を断
面斜視図と一/4L− した系統接続図、第6図は第5図の■−■線に沿う断面
図、第7図はサイクロン集塵装置を二個用いる場合の配
置例を示す平面図、第8図はサイクロン集塵装置の各部
の寸法比を示す断面図である。 l・・・燃料吹込室、コ・・・燃焼室、3・・・燃焼ガ
ス取出室、弘・・・サイクロン集塵装置、7.l・・・
隔壁、lO・・°連通口、l/・・・予熱管、lj・・
・集塵室、/フ・・・排気筒、/7・・・燃焼ガス取出
管、−よ、 33 、3≠・・・空気供給管、ム・・・
燃料供給管、27・・・燃料貯留ホッパ、参k・・着火
炎導入管。 特許出願人 サンエネルギー株式会社 代 理 人  弁理士 福 1)弐 通 、代 理 人
  弁理士 福 1)賢 三  ゛(碧1−一 1 ・ 1B2?ei 第4凶
FIG. 1 is a longitudinal cross-sectional view showing an embodiment of the combustion device according to the present invention, and FIGS. Figure 5 is a cross-sectional perspective view of a part of the fuel and other supply piping system for this combustion device, and a system connection diagram taken along the 1/4 L- line; Figure 6 is a system connection diagram taken along the ■-■ line in Figure 5. A sectional view, FIG. 7 is a plan view showing an arrangement example when two cyclone dust collectors are used, and FIG. 8 is a sectional view showing the dimensional ratio of each part of the cyclone dust collector. l... Fuel injection chamber, K... Combustion chamber, 3... Combustion gas extraction chamber, Hiroshi... Cyclone dust collector, 7. l...
Partition wall, lO...° communication port, l/... preheating tube, lj...
・Dust collection chamber, /F...Exhaust pipe, /7...Combustion gas take-off pipe, -yo, 33,3≠...Air supply pipe, M...
Fuel supply pipe, 27...Fuel storage hopper, 3.k...Ignition flame introduction pipe. Patent Applicant Sun Energy Co., Ltd. Agent Patent Attorney Fuku 1) Nitoshi, Agent Patent Attorney Fuku 1) Ken San゛ (Aoi 1-11 ・ 1B2?ei 4th evil)

Claims (3)

【特許請求の範囲】[Claims] (1)石炭系粒状燃料を吹き込む横向き筒状の燃料吹込
室の一側に、同じく横向き筒状の燃焼室を、他側に縦型
サイクロン集塵装置を設け、上記燃料吹込室と燃焼室と
を両者間の隔壁の上部に開口させた連通口を介して連通
させるとともに1上記燃焼室と縦型サイクロン集塵装置
とを上記燃料吹込室を通る予熱管を介して連通させ、か
つ上記燃焼室に着火装置を設け、上記サイクロン集塵装
置を介して燃焼ガスを取出すようにしたことを特徴とす
る燃焼装置。
(1) A horizontally cylindrical combustion chamber is installed on one side of the horizontally cylindrical fuel injection chamber into which coal-based granular fuel is injected, and a vertical cyclone dust collector is installed on the other side, so that the fuel injection chamber and the combustion chamber are connected to each other. 1. The combustion chamber and the vertical cyclone dust collector are communicated with each other through a preheating pipe passing through the fuel injection chamber, and A combustion device characterized in that an ignition device is provided in the combustion device, and combustion gas is taken out through the cyclone dust collector.
(2)  特許請求の範囲第1項において、縦型サイク
ロン集塵装置は予熱管に関する平面的な略対称位置に二
個設けられている燃焼装置。
(2) The combustion device according to claim 1, wherein two vertical cyclone dust collectors are provided at substantially symmetrical positions in a plane with respect to the preheating tube.
(3)%許請求の範囲第1項または第2項におい2− て、縦型サイクロン集塵装置は燃焼ガス取出管を開口さ
せた燃焼ガス取出室内に配設され、その軸部排気筒が該
燃焼ガス取出室に連通している燃焼装置。
(3) Percentage of Claims In paragraph 1 or 2, the vertical cyclone dust collector is disposed in a combustion gas extraction chamber with a combustion gas extraction pipe opened, and the shaft exhaust pipe is arranged in a combustion gas extraction chamber with an open combustion gas extraction pipe. A combustion device communicating with the combustion gas extraction chamber.
JP5734582A 1982-04-08 1982-04-08 Combustion device Pending JPS58175710A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5734582A JPS58175710A (en) 1982-04-08 1982-04-08 Combustion device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5734582A JPS58175710A (en) 1982-04-08 1982-04-08 Combustion device

Publications (1)

Publication Number Publication Date
JPS58175710A true JPS58175710A (en) 1983-10-15

Family

ID=13052979

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5734582A Pending JPS58175710A (en) 1982-04-08 1982-04-08 Combustion device

Country Status (1)

Country Link
JP (1) JPS58175710A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03128237U (en) * 1990-04-03 1991-12-24

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4721684U (en) * 1971-02-26 1972-11-10
JPS4845245U (en) * 1971-09-28 1973-06-13
JPS5147636U (en) * 1974-10-07 1976-04-08

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4721684U (en) * 1971-02-26 1972-11-10
JPS4845245U (en) * 1971-09-28 1973-06-13
JPS5147636U (en) * 1974-10-07 1976-04-08

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03128237U (en) * 1990-04-03 1991-12-24

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