JP2504842B2 - Crucible furnace equipment - Google Patents

Crucible furnace equipment

Info

Publication number
JP2504842B2
JP2504842B2 JP22699589A JP22699589A JP2504842B2 JP 2504842 B2 JP2504842 B2 JP 2504842B2 JP 22699589 A JP22699589 A JP 22699589A JP 22699589 A JP22699589 A JP 22699589A JP 2504842 B2 JP2504842 B2 JP 2504842B2
Authority
JP
Japan
Prior art keywords
crucible furnace
crucible
combustion
fuel mixture
catalyst layer
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 - Lifetime
Application number
JP22699589A
Other languages
Japanese (ja)
Other versions
JPH0391691A (en
Inventor
治郎 中丸
勇 菊池
義之 佐野
英雄 吉川
宏 一柳
宣雄 松尾
三夫 今村
正行 松田
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.)
NITSUKAN CHIKURO KOGYO KK
Tokyo Gas Co Ltd
Mitsubishi Power Ltd
Original Assignee
NITSUKAN CHIKURO KOGYO KK
Babcock Hitachi KK
Tokyo Gas Co 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 NITSUKAN CHIKURO KOGYO KK, Babcock Hitachi KK, Tokyo Gas Co Ltd filed Critical NITSUKAN CHIKURO KOGYO KK
Priority to JP22699589A priority Critical patent/JP2504842B2/en
Publication of JPH0391691A publication Critical patent/JPH0391691A/en
Application granted granted Critical
Publication of JP2504842B2 publication Critical patent/JP2504842B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Crucibles And Fluidized-Bed Furnaces (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はアルミ溶解保持等に使用するルツボ炉装置に
関するものである。
TECHNICAL FIELD The present invention relates to a crucible furnace apparatus used for holding and melting aluminum.

(従来技術と問題点) 第4図に於いて、ルツボ炉本体aの内面には、耐火材
bが内張されており、その内側にルツボcが耐火材bと
一定の間隔を保持した状態で設置されている。ルツボc
の内部には、アルミ塊等の被加熱物dが入っている。ル
ツボ炉本体aの側壁には接線方向的にバーナeが設置さ
れており、バーナeは、主として高速噴射型バーナが用
いられている。
(Prior Art and Problems) In FIG. 4, a state in which a refractory material b is lined on the inner surface of the crucible furnace main body a, and the crucible c is kept inside the refractory material b at a constant distance. It is installed in. Crucible c
An object to be heated d such as a lump of aluminum is contained in the inside of. A burner e is installed tangentially on the side wall of the crucible furnace body a, and the burner e is mainly a high-speed injection burner.

バーナeで燃焼した高温燃焼ガスfは高速で炉内に噴
射され、ルツボcと耐火材b間の環状路gを高速で旋回
し、ルツボc内部の被加熱物dを強制対流によりできる
だけ均一にルツボc外面を加熱する様に考慮されてい
る。
The high-temperature combustion gas f burned by the burner e is injected into the furnace at high speed, swirls at a high speed in the annular path g between the crucible c and the refractory material b, and the heated object d inside the crucible c is made as uniform as possible by forced convection. Consideration is given to heating the outer surface of the crucible c.

ルツボcと耐火材b間の環状路gを旋回しながら上昇
した燃焼ガスfは炉本体上部の排気口hより排気され
る。
Combustion gas f rising while swirling in an annular path g between crucible c and refractory material b is exhausted from an exhaust port h in the upper part of the furnace body.

更に排気口部に燃焼用空気を予熱し熱回収をはかるた
め空気予熱器を設けたものもある。
Further, there is also one in which an air preheater is provided at the exhaust port to preheat combustion air to recover heat.

かかる従来技術は、通常のバーナを使用し、更にアル
ミ塊等を溶解するために高負荷燃焼が必要である。この
ため燃焼音による騒音も大きく排ガス中のNOxは一定値
以下に低減することは困難であり、通常60〜100ppm程度
が限界とされている。
In such a conventional technique, a normal burner is used, and high-load combustion is required to melt aluminum lumps and the like. Therefore, it is difficult to reduce the NO x in the exhaust gas below a certain value due to the large noise caused by combustion noise, and the limit is usually about 60 to 100 ppm.

また、バーナで燃焼した燃焼ガスは、ルツボを均一且
つ急速に加熱するために、高速で炉内に噴出されてい
る。このため、高温高速の燃焼ガスは直接ルツボに接触
しルツボの寿命(半年〜1年)を通常を縮める原因とな
っている。
Further, the combustion gas burned by the burner is jetted into the furnace at a high speed in order to uniformly and rapidly heat the crucible. For this reason, the high-temperature and high-speed combustion gas directly contacts the crucible and causes the life of the crucible (half a year to 1 year) to be shortened.

本発明の目的は、上記した問題点、即ち、騒音が高
い、NOx低減が困難、るつぼの寿命が短い等を解決
するにある。
An object of the present invention is to solve the above-mentioned problems, namely, high noise, difficulty in reducing NO x , short life of crucible, and the like.

(問題を解決するための手段) 第1図に於いて、符号1は一次混合気室であって、2
はその下流側に設けたパネル上触媒層である。該パネル
状触媒層2の中央に、先端部に噴出孔3を設けた二次混
合気管4を突出させて燃焼部5を構成する。かかる構成
の燃焼部5をルツボ炉6の側壁7に単数又は複数個設け
る構成とする。
(Means for Solving the Problem) In FIG. 1, reference numeral 1 is a primary air-fuel mixture chamber and 2
Is the on-panel catalyst layer provided on the downstream side. At the center of the panel-shaped catalyst layer 2, a secondary mixture pipe 4 having a jet hole 3 at its tip is projected to form a combustion section 5. The combustion unit 5 having such a configuration is provided on the side wall 7 of the crucible furnace 6 in a single or plural number.

請求項2記載のものは、第2図に対応するものであっ
て、燃焼部5全体を小さく構成して、この燃焼部5を先
細り構成の噴出口8を具えた燃焼完結室9内に装入し
て、前記噴出口8をルツボ炉6内に開口させた構成であ
り、請求項3記載のものは、パネル状触媒層2の温度を
600〜1000℃に保持する構成であり、請求項4記載のも
のは、一次混合気室1の外周には一次混合気通路10を設
けた構成であり、第5項記載のものは二次混合気管4に
設けた噴出孔3を横方向に設けた構成である。前記した
パネル状触媒層2としては、例えば白金、パラジウム又
はそれらの混合物等から成るものでよい。
A second aspect of the present invention corresponds to FIG. 2, in which the entire combustion section 5 is made small, and the combustion section 5 is mounted in a combustion completion chamber 9 having a tapered ejection port 8. The temperature of the panel-shaped catalyst layer 2 can be controlled by introducing the jet port 8 into the crucible furnace 6 and opening the jet port 8 in the crucible furnace 6.
The composition is maintained at 600 to 1000 ° C., the composition according to claim 4 is a composition in which the primary mixture passage 10 is provided on the outer periphery of the primary mixture chamber 1, and the composition according to claim 5 is the secondary mixture. This is a configuration in which the ejection holes 3 provided in the trachea 4 are provided in the lateral direction. The above-mentioned panel-shaped catalyst layer 2 may be made of platinum, palladium, or a mixture thereof, for example.

(作用) 第1図に於いて、燃料ガスと空気の一次混合気室が一
次混合気導入部13から一次混合気室1内に導入されてパ
ネル状触媒層2に達すると、一次混合気は着火器11によ
り着火されて、パネル状触媒層2の表面全面に火炎を形
成し、触媒層2の温度を600〜1000℃の範囲に保持す
る。かかる温度の保持は温度検出器14により触媒層2の
温度を検出して燃焼量の制御により行なう。かかる状態
で、二次混合器が二次混合器管4内に導入され、その先
端の噴出孔3から横方向に噴出すると、パネル状触媒層
2の温度が600〜1000℃に達しているので、その熱によ
り即座に反応し燃焼を開始する。
(Operation) In FIG. 1, when the primary air-fuel mixture chamber of the fuel gas and air is introduced into the primary air-fuel mixture chamber 1 from the primary air-fuel mixture inlet 13 and reaches the panel-shaped catalyst layer 2, the primary air-fuel mixture is It is ignited by the igniter 11 to form a flame on the entire surface of the panel-shaped catalyst layer 2, and the temperature of the catalyst layer 2 is maintained in the range of 600 to 1000 ° C. The temperature is maintained by detecting the temperature of the catalyst layer 2 by the temperature detector 14 and controlling the combustion amount. In this state, when the secondary mixer is introduced into the secondary mixer pipe 4 and ejected laterally from the ejection hole 3 at the tip thereof, the temperature of the panel-shaped catalyst layer 2 reaches 600 to 1000 ° C. , The heat immediately reacts and starts combustion.

以上の本発明によれば、パネル状触媒層2では希薄燃
料燃焼が行なわれるので、局部過熱がなく、且つ600〜1
000℃の低温燃焼を実行するので、窒素酸化物(NOx)の
発生を極少に抑制することができると同時に前記希薄燃
料燃焼により低騒音燃焼が実現できる。また、二次混合
気による燃焼は、触媒層2に囲まれた燃焼、即ち前記温
度範囲にある雰囲気中で行なわれる燃焼であるので、第
一に燃焼の安定化が図かられると共に発生する火炎が非
常に短炎である。第二に、二次空気を噴出孔3から、そ
の周囲に噴射して行なわれる燃焼でもあるので、混合気
の拡散によって局部過熱のない低NOx燃焼と低騒音燃焼
が達成できる。
According to the present invention described above, since lean fuel combustion is performed in the panel-shaped catalyst layer 2, there is no local overheating, and 600 to 1
Since the low temperature combustion of 000 ° C. is performed, the generation of nitrogen oxides (NO x ) can be suppressed to a minimum, and at the same time, low noise combustion can be realized by the lean fuel combustion. Further, since the combustion with the secondary air-fuel mixture is the combustion surrounded by the catalyst layer 2, that is, the combustion performed in the atmosphere in the temperature range, firstly, the combustion is stabilized and the generated flame is generated. Is a very short flame. Secondly, since the combustion is performed by injecting secondary air from the ejection holes 3 to the periphery thereof, diffusion of the air-fuel mixture can achieve low NO x combustion without local overheating and low noise combustion.

更に、ルツボ12は、パネル状触媒層2からの輻射熱に
よって主として加熱されるので、広い面積からの輻射加
熱により均一加熱を行なうことができ、直接火炎とあた
ることがないので、ルツボ12の寿命を著しく向上させる
ことができる。また、ルツボ12はアルミ溶解の際と、そ
れを保持する場合とで、必要熱量が異なるが、溶湯保持
の場合には、例えば二次混合器管4からの二次混合気の
噴射をやめるか、その噴射量を制御するだけでよく、本
発明装置はその溶解、保持の両者に使用することができ
る。かかることにより、触媒層2の温度は触媒層2での
燃焼を維持するに必要な温度(600〜1000℃)を保持す
ればよく、むやみに触媒層2の温度をあげる必要がな
く、触媒寿命を延長できる利点がある。
Further, since the crucible 12 is mainly heated by the radiant heat from the panel-shaped catalyst layer 2, the crucible 12 can be uniformly heated by the radiant heating from a large area and does not directly hit the flame, so that the life of the crucible 12 is improved. It can be significantly improved. The amount of heat required for the crucible 12 differs depending on whether the crucible 12 is melted or held, but in the case of holding the molten metal, for example, is the injection of the secondary mixture from the secondary mixer pipe 4 stopped? However, it is only necessary to control the injection amount, and the device of the present invention can be used for both melting and holding. As a result, the temperature of the catalyst layer 2 may be maintained at a temperature (600 to 1000 ° C.) required to maintain combustion in the catalyst layer 2, and it is not necessary to unnecessarily raise the temperature of the catalyst layer 2 and the catalyst life There is an advantage that can be extended.

第2図は、他の実施例を示すものであって、燃焼部5
を全体的に小さく構成し、これを噴出口8を具えた燃焼
完結室9内に装入して、前記噴出口8を前記ルツボ炉6
内に開口させた構成である。かかる実施例では、燃焼部
5で前記の如く発生した燃焼ガスは、燃焼完結室9内で
完全に燃焼して噴出口8から噴出し、ルツボ12の外周を
循環してルツボ12を加熱するが、その循環ガスは燃焼を
完結した熱流であるため火炎がルツボ12にそのままあた
るようなことはなく、ルツボ12の寿命を長くすることが
できる。かかる構成の実施例は、またその構成上、従来
のルツボ炉装置に取着けたバーナを交換するだけで、前
記した種々の利点をもたらすことができる。
FIG. 2 shows another embodiment of the combustion unit 5
Is configured as a whole and is inserted into a combustion completion chamber 9 having an ejection port 8 so that the ejection port 8 is connected to the crucible furnace 6
It is a structure that is opened inside. In this embodiment, the combustion gas generated in the combustion section 5 as described above is completely combusted in the combustion completion chamber 9 and ejected from the ejection port 8 to circulate around the crucible 12 to heat the crucible 12. Since the circulating gas is a heat flow that has completed combustion, the flame does not hit the crucible 12 as it is, and the life of the crucible 12 can be extended. Due to the structure, the embodiment having such a structure can provide the above-mentioned various advantages only by replacing the burner attached to the conventional crucible furnace apparatus.

第3図は燃焼部の拡大説明図であり、燃焼部5の一次
混合気室1の外周に一次混合気流路13を設けた実施例で
あり、この構成により一次混合気の予熱を図かることが
できる。
FIG. 3 is an enlarged explanatory view of the combustion section, which is an embodiment in which the primary mixture channel 13 is provided on the outer periphery of the primary mixture chamber 1 of the combustion section 5, and the preheating of the primary mixture is achieved by this configuration. You can

(発明の効果) 本発明は以上の通りであるので、低騒音で且つ窒素酸
化物の発生を極少に抑制することができると共に独特の
構成によって火炎を直接ルツボにあてることのないよう
にして、ルツボの寿命を大幅に向上させた等の諸効果を
持つものである。
(Effects of the Invention) Since the present invention is as described above, it is possible to suppress the generation of nitrogen oxides to a minimum with a low noise and to prevent the flame from directly hitting the crucible by the unique configuration, It has various effects such as a drastic improvement in the life of the crucible.

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

第1図は本発明の断面的説明図、第2図は本発明の他の
実施例の断面的説明図、第3図(A)は燃焼部の一例を
示す断面的説明図、同(B)は説明的正面図である。第
4図は従来のルツボ炉の断面的説明図である。 符号1…一次混合気室、2…パネル状触媒層、3…噴出
孔、4…二次混合気管、5…燃焼部、6…ルツボ炉、7
…側壁、8…噴出口、9…燃焼完結室、10…一次混合気
通路、11…着火器、12…ルツボ、13…一次混合気導入
部、14…温度検出器。15…整流板
FIG. 1 is a cross-sectional explanatory view of the present invention, FIG. 2 is a cross-sectional explanatory view of another embodiment of the present invention, and FIG. 3 (A) is a cross-sectional explanatory view showing an example of a combustion part. ) Is an explanatory front view. FIG. 4 is a cross-sectional explanatory view of a conventional crucible furnace. Reference numeral 1 ... Primary air-fuel mixture chamber, 2 ... Panel-shaped catalyst layer, 3 ... Injection hole, 4 ... Secondary air-fuel mixture tube, 5 ... Combustion section, 6 ... Crucible furnace, 7
... Side wall, 8 ... Jet port, 9 ... Combustion completion chamber, 10 ... Primary mixture passage, 11 ... Ignition device, 12 ... Crucible, 13 ... Primary mixture introduction section, 14 ... Temperature detector. 15 ... Current plate

───────────────────────────────────────────────────── フロントページの続き (72)発明者 佐野 義之 東京都豊島区東池袋1―48―6―1101 (72)発明者 吉川 英雄 東京都大田区東糀谷5―3―9 (72)発明者 一柳 宏 広島県呉市宝町6―9 (72)発明者 松尾 宣雄 広島県呉市宝町6―9 (72)発明者 今村 三夫 広島県呉市宝町6―9 (72)発明者 松田 正行 広島県呉市宝町6―9 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Yoshiyuki Sano 1-48-6-1101 Higashiikebukuro, Toshima-ku, Tokyo (72) Inventor Hideo Yoshikawa 5-3-9 Higashi-Kojiya, Ota-ku, Tokyo (72) Inventor Hiroshi Ichiyanagi 6-9 Takaracho, Kure-shi, Hiroshima (72) Nobuo Matsuo 6-9 Takaracho, Kure-shi, Hiroshima (72) Inventor Mitsuo Imamura 6-9 Takaracho, Kure-shi, Hiroshima (72) Masayuki Matsuda Takaracho, Kure-shi, Hiroshima 6-9

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】一次混合気室の下流側にパネル状触媒層を
設け、該パネル状触媒層の中央部に、先端部に噴出孔を
設けた二次混合気管を突出させて構成した燃焼部を、ル
ツボ炉の側壁に単数又は複数個設けたルツボ炉装置。
1. A combustion section constituted by providing a panel-shaped catalyst layer on the downstream side of a primary air-fuel mixture chamber, and projecting a secondary air-fuel mixture tube having an injection hole at its tip in the central portion of the panel-shaped catalyst layer. A crucible furnace device in which one or more are provided on the side wall of the crucible furnace.
【請求項2】前記燃焼部を、先細り構成の噴出口を具え
た燃焼完結室内に装入して、前記噴出口を、ルツボ炉内
に開口させた請求項1記載のルツボ炉装置。
2. The crucible furnace apparatus according to claim 1, wherein the combustion section is inserted into a combustion completion chamber having a tapered jet outlet, and the jet outlet is opened in the crucible furnace.
【請求項3】前記パネル状触媒層の温度を600〜1000℃
の範囲内に保持するようにした請求項1又は2記載のル
ツボ炉装置。
3. The temperature of the panel-shaped catalyst layer is 600 to 1000 ° C.
The crucible furnace apparatus according to claim 1 or 2, wherein the crucible furnace apparatus is held within the range.
【請求項4】前記一次混合気室の外周には、一次混合気
通路を設けた請求項1,2又は3記載のルツボ炉装置。
4. The crucible furnace apparatus according to claim 1, 2 or 3, wherein a primary air-fuel mixture passage is provided on the outer periphery of the primary air-fuel mixture chamber.
【請求項5】前記二次混合気管に設けた噴出孔は、横方
向に二次混合気を噴出するように設けた請求項1,2,3又
は4記載のルツボ炉装置。
5. The crucible furnace apparatus according to claim 1, 2, 3 or 4, wherein the ejection holes provided in the secondary air-fuel mixture tube are provided so as to eject the secondary air-fuel mixture laterally.
JP22699589A 1989-09-01 1989-09-01 Crucible furnace equipment Expired - Lifetime JP2504842B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22699589A JP2504842B2 (en) 1989-09-01 1989-09-01 Crucible furnace equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22699589A JP2504842B2 (en) 1989-09-01 1989-09-01 Crucible furnace equipment

Publications (2)

Publication Number Publication Date
JPH0391691A JPH0391691A (en) 1991-04-17
JP2504842B2 true JP2504842B2 (en) 1996-06-05

Family

ID=16853862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22699589A Expired - Lifetime JP2504842B2 (en) 1989-09-01 1989-09-01 Crucible furnace equipment

Country Status (1)

Country Link
JP (1) JP2504842B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102353080A (en) * 2011-09-06 2012-02-15 蚌埠市添利厨房设备有限公司 Low-noise gas hearth

Also Published As

Publication number Publication date
JPH0391691A (en) 1991-04-17

Similar Documents

Publication Publication Date Title
US5490775A (en) Forward injection oxy-fuel burner
US5403181A (en) Method of low-NOx combustion and burner device for effecting same
KR970001465B1 (en) Radiant tube burner
US4150539A (en) Low pollution combustor
JP2683545B2 (en) Combustion method in furnace
CA1170562A (en) Recirculating burner
CN1152953A (en) Low Nox burner
JPS60132035A (en) Method and apparatus for reducing dischage of nitrogen oxidefrom gaseous fuel burner
US6461145B1 (en) Flat flame burners
US6047565A (en) Method and device for reducing the NOx emission in a glass furnace
KR100653029B1 (en) Combustion in a porous wall furnace
JP2504842B2 (en) Crucible furnace equipment
JPH07318018A (en) Operating method of premix burner
JP3176786B2 (en) Oxygen burner
US3846066A (en) Fuel burner apparatus
JPS60202225A (en) Luminous flame generating combustion device
JPH0777310A (en) Low nitrogen oxide generating burner and burning method therefor
JPH0223764B2 (en)
JPH08157916A (en) Blowing of pulverized fine coal into blast furnace and lance for blowing pulverized fine coal
JPH0344966Y2 (en)
JPH0128847B2 (en)
JPH0449452Y2 (en)
JPH0140969Y2 (en)
KR960003680Y1 (en) Burner
JPS602408Y2 (en) call burner