JP2000154052A - Furnace for ceramic-art object - Google Patents
Furnace for ceramic-art objectInfo
- Publication number
- JP2000154052A JP2000154052A JP10341083A JP34108398A JP2000154052A JP 2000154052 A JP2000154052 A JP 2000154052A JP 10341083 A JP10341083 A JP 10341083A JP 34108398 A JP34108398 A JP 34108398A JP 2000154052 A JP2000154052 A JP 2000154052A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- flue
- temperature gas
- gas
- high temperature
- 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
Links
- 230000001590 oxidative effect Effects 0.000 claims abstract description 25
- 238000002485 combustion reaction Methods 0.000 claims abstract description 23
- 230000001603 reducing effect Effects 0.000 claims abstract description 20
- 239000000919 ceramic Substances 0.000 claims description 7
- 239000000779 smoke Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- 238000010304 firing Methods 0.000 abstract description 7
- 238000004891 communication Methods 0.000 description 21
- 230000002829 reductive effect Effects 0.000 description 5
- 239000004071 soot Substances 0.000 description 4
- 239000003350 kerosene Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
Landscapes
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、灯油バーナ等を使
用する陶芸炉に関する。The present invention relates to a pottery furnace using a kerosene burner or the like.
【0002】[0002]
【従来の技術】陶芸炉として、特許第2748131号
公報に、炉底に設けた高温ガス導入口から酸化性又は還
元性の高温ガスが導入されると共に分流装置を介して炉
内部における陶芸成形物の焼成と炉内部から煙道を介し
て排気流路に送出される排気ガスの完全燃焼のために分
流して使用され、実質的に完全燃焼した排気ガスとして
排気流路から外部に排出されるようにしてなるものが開
示されている。2. Description of the Related Art As a pottery furnace, Japanese Patent Publication No. 2748131 discloses a pottery molded product inside a furnace through which a oxidizing or reducing high-temperature gas is introduced from a high-temperature gas inlet provided at the bottom of the furnace and through a flow dividing device. Is used for sintering and complete combustion of exhaust gas sent out of the furnace through a flue to an exhaust passage, and is used as a substantially completely burned exhaust gas, which is discharged to the outside from the exhaust passage. What is made is disclosed.
【0003】前記陶芸炉によれば、変化に富む陶芸作品
を得るために還元性の高温ガスを用いて陶芸成形物を還
元雰囲気下に焼成する場合において、不完全燃焼状態の
排気ガスを排気流路で完全燃焼させると共に外部環境へ
の煤煙の排出を防止することができ、住宅地等でも公害
発生の懸念なしに使用することが可能である。According to the pottery furnace, when a pottery molded article is fired in a reducing atmosphere using a reducing high-temperature gas in order to obtain a pottery work rich in change, exhaust gas in an incomplete combustion state is exhausted. It can be completely burned on the road and can prevent the emission of soot to the external environment, so that it can be used in residential areas and the like without causing any pollution.
【0004】しかしながら、従来の前記陶芸炉では、前
記排気ガスの完全燃焼のための高温ガスが炉内部とは区
画された排気流路に分流させられると共に該排気流路で
排気ガスの完全燃焼が行われるものであり、またこの種
の高温ガスを用いる陶芸炉全てについて言えることでも
あるが、炉内部における高温ガス導入口近辺に比べて排
気流路近辺の温度が低くなると共に両領域間に少なから
ず温度差が生じ、そのために燃焼効率の低下を招くと共
に陶芸成形物の均一な焼成が困難になり、焼成作業に不
具合を来すことがあった。However, in the conventional pottery furnace, a high-temperature gas for complete combustion of the exhaust gas is diverted to an exhaust passage partitioned from the inside of the furnace, and complete combustion of the exhaust gas is performed in the exhaust passage. This is done, and as can be said for all pottery furnaces using this kind of high-temperature gas, the temperature near the exhaust passage is lower than near the high-temperature gas inlet inside the furnace, and there is a small amount between both areas. In addition, a temperature difference occurs, which leads to a decrease in combustion efficiency, and makes it difficult to uniformly fire a ceramic molded product, which sometimes causes a trouble in the firing operation.
【0005】[0005]
【発明が解決しようとする課題】本発明の解決すべき課
題は、炉内部における高温ガス導入口近辺と排気流路近
辺との温度差を緩和すると共に炉内部の温度分布の均一
化を図り、それによって陶芸成形物の均一な焼成と燃焼
効率の向上を可能にする陶芸炉を提供することにある。The problem to be solved by the present invention is to reduce the temperature difference between the vicinity of the high-temperature gas inlet and the vicinity of the exhaust passage inside the furnace and to make the temperature distribution inside the furnace uniform. Accordingly, it is an object of the present invention to provide a pottery furnace capable of uniformly firing a pottery molded article and improving combustion efficiency.
【0006】[0006]
【課題を解決するための手段】本発明に係る陶芸炉は、
炉底又は炉胴下部に設けた高温ガス導入口から酸化性又
は還元性の高温ガスが導入されると共に分流装置を介し
て炉内部における陶芸成形物の焼成と炉内部から煙道を
介して排気流路に送出される排気ガスの完全燃焼のため
に分流して使用され、実質的に完全燃焼した排気ガスと
して排気流路から外部に排出されるようにしてなる陶芸
炉において、前記排気ガスの完全燃焼のための高温ガス
を煙道に分流させ、且つ煙道における少なくとも高温ガ
スの分流位置から排気流路に至るまでの煙道部分を炉底
に配置すると共に該煙道部分の中間位置に酸化炎生成の
ための空気導入口を設けたことを特徴としている。The pottery furnace according to the present invention comprises:
An oxidizing or reducing high-temperature gas is introduced from a high-temperature gas inlet provided in a furnace bottom or a lower part of a furnace body, and a ceramic molded article is baked in the furnace through a branching device and exhausted from a furnace through a flue. In a pottery furnace, which is divided and used for complete combustion of exhaust gas sent out to the flow path and is discharged to the outside from the exhaust flow path as substantially completely burned exhaust gas, The hot gas for complete combustion is diverted to the flue, and at least the flue section from the hot gas diverting position to the exhaust flow path in the flue is arranged at the furnace bottom and at the intermediate position of the flue section. It is characterized in that an air inlet for oxidizing flame is provided.
【0007】前記構成において、高温ガス導入口からの
高温ガスが還元性の場合に、高温ガスの分流位置から排
気流路に至るまでの煙道部分では不完全燃焼状態の排気
ガスが完全燃焼させられ、煤煙を含まない状態で排気流
路から排出される。この場合、前記煙道部分には高温ガ
ス導入口からの還元性の高温ガスの一部が直接分流され
ると共に空気導入口から空気を添加されて酸化炎を生成
し、炉内部からの前記不完全燃焼状態の排気ガスは前記
酸化炎により点火されてその可燃分を燃焼させられ、黒
煙や煤を含まない完全燃焼状態の排気ガスとされる。ま
た、前記煙道部分は炉底に配置されているので、前記煙
道部分における前記完全燃焼時に発生する燃焼熱が、炉
底における高温ガス導入口から離れた排気流路寄りの部
分、即ち炉内部でも最も温度の低い部分の温度を上昇さ
せ、燃焼効率を向上させると共に結果的に燃料消費量を
低減させる。この点、既述の従来技術では、前記排気ガ
スの完全燃焼のための高温ガスが炉外に区画された排気
流路に分流させられると共にここで空気を添加され、該
排気流路で排気ガスの完全燃焼が行われるので、この構
造では炉内部の温度分布の均一化や不完全燃焼状態の排
気ガス中における可燃分の有効利用を図ることができな
い。なお、本発明では、高温ガス導入口からの高温ガス
が酸化性の場合にも、前記分流装置で前記煙道部分に高
温ガスの一部を分流させることにより炉底の温度が高め
られるので、炉内部の温度分布の均一化を図ることが可
能になる。In the above structure, when the high-temperature gas from the high-temperature gas inlet is reducing, the exhaust gas in an incompletely combusted state is completely burned in the flue from the hot gas diverting position to the exhaust passage. The exhaust gas is discharged from the exhaust passage without containing soot. In this case, a part of the reducing high-temperature gas from the high-temperature gas inlet is directly diverted into the flue portion, and air is added from the air inlet to generate an oxidizing flame. The exhaust gas in the completely burned state is ignited by the oxidizing flame to burn its combustible components, and is turned into a completely burned exhaust gas containing no black smoke or soot. Further, since the flue portion is disposed at the bottom of the furnace, the combustion heat generated at the time of the complete combustion in the flue portion is a portion of the furnace bottom near the exhaust passage away from the high-temperature gas inlet, that is, the furnace. It raises the temperature of the lowest temperature part inside, thereby improving the combustion efficiency and consequently reducing the fuel consumption. In this regard, in the above-described conventional technology, the high-temperature gas for complete combustion of the exhaust gas is diverted to an exhaust passage partitioned outside the furnace and air is added thereto, and the exhaust gas is exhausted through the exhaust passage. Therefore, this structure cannot make the temperature distribution inside the furnace uniform and cannot effectively use the combustibles in the exhaust gas in the incomplete combustion state. In the present invention, even when the high-temperature gas from the high-temperature gas inlet is oxidizing, the temperature of the furnace bottom is increased by diverting a part of the high-temperature gas to the flue portion by the flow dividing device. The temperature distribution inside the furnace can be made uniform.
【0008】前記構成の陶芸炉では、高温ガスが1個所
の高温ガス導入口から導入されると共に該高温ガスから
生じた排気ガスが1個所の排気流路に送出されるように
構成してもよいが、炉内部のより均一な温度分布を得る
ために、例えば、高温ガス導入口を炉底又は炉胴下部の
対向する両側に個別に設けると共に共通の排気流路を前
記両側の高温ガス導入口間に設け、高温ガスが互いに離
れた2個所の高温ガス導入口から導入されると共に該高
温ガスから生じた各排気ガスが両側の高温ガス導入口間
に設けた1個所の共通の排気流路に送出されるように構
成することもできる。[0008] In the ceramic pottery furnace having the above-mentioned structure, the hot gas may be introduced from one hot gas inlet and exhaust gas generated from the hot gas may be sent to one exhaust flow path. In order to obtain a more uniform temperature distribution inside the furnace, for example, hot gas inlets are separately provided on opposite sides of the furnace bottom or the lower portion of the furnace body, and a common exhaust passage is provided for the hot gas introduction on both sides. The hot gas is introduced between two hot gas inlets separated from each other, and each exhaust gas generated from the hot gas is supplied to one common exhaust flow provided between the hot gas inlets on both sides. It can also be configured to be sent to the road.
【0009】前記分流装置については、炉内部の温度や
温度分布の調節、前記煙道部分における燃焼状態の調節
等を容易にするために、炉内部及び排気流路に向かう煙
道部分への高温ガスの各分流の流量調節を可能とするこ
とが好ましい。高温ガス導入口からの高温ガスが酸化性
の場合には、既述のように、炉内部及び排気流路に向か
う煙道部分への高温ガスの各分流の流量を調節すると共
に該煙道部分に酸化性の高温ガスを導入させることによ
り、炉内部の温度分布の均一化を図ることができる。ま
た、高温ガス導入口からの高温ガスが還元性の場合に
は、既述のように、炉内部及び排気流路に向かう煙道部
分への高温ガスの各分流の流量を調節すると共に該煙道
部分において酸化炎を生成させることにより、排気ガス
の完全燃焼とそれによる炉内部の温度分布の均一化を図
ることができる。In order to easily adjust the temperature and temperature distribution inside the furnace, the combustion state in the flue section, etc., it is preferable that the flow dividing device has a high temperature inside the furnace and the flue section toward the exhaust passage. It is preferable to be able to adjust the flow rate of each branch of the gas. When the hot gas from the hot gas inlet is oxidizing, as described above, the flow rate of each branch of the hot gas to the inside of the furnace and to the flue section toward the exhaust passage is adjusted and the flue section is controlled. By introducing an oxidizing high-temperature gas into the furnace, the temperature distribution inside the furnace can be made uniform. When the high-temperature gas from the high-temperature gas inlet is reducing, as described above, the flow rate of each of the high-temperature gas to the inside of the furnace and the flue portion toward the exhaust flow path is adjusted and the smoke is reduced. By generating the oxidizing flame in the road portion, it is possible to achieve complete combustion of the exhaust gas and thereby to make the temperature distribution inside the furnace uniform.
【0010】[0010]
【発明の実施の形態】〔実施例1〕図1は本発明の実施
例1に係る陶芸炉の縦断面図であり、(A)は外側にあ
る第一の煙道において切断したもの、(B)は内側にあ
る第二の煙道において切断したものを示している。ま
た、図2は図1に示す陶芸炉における炉蓋を取り外した
ときの平面図である。FIG. 1 is a longitudinal sectional view of a pottery furnace according to a first embodiment of the present invention, wherein FIG. B) shows a cut in the inner second flue. FIG. 2 is a plan view of the pottery furnace shown in FIG. 1 with a furnace lid removed.
【0011】同図において、陶芸炉1は炉底2、炉胴
3、炉蓋4及び煙突5を備え、炉底2には炉内部6と前
方の上下連通孔7を介して連通し、炉胴3と各隔壁8で
囲まれた第一の煙道9が両側に配置されると共に該第一
の煙道9と後方の左右連通孔10を介して連通し、両側
の隔壁8で囲まれた第二の煙道11が中央に配置され、
第二の煙道11は煙突5内の排気流路12と前方の排気
連通孔13を介して連通し、また炉底2には該第二の煙
道11の中間位置において空気導入口14が穿設されて
いる。炉底2後端には酸化性又は還元性の高温ガスを発
生する灯油バーナ15の高温ガス導入口16が開口され
ると共に高温ガス導入口16は炉内部6及び第二の煙道
11と各々炉内連通孔17及び煙道連通孔18を介して
連通し、該高温ガス導入口16と前記炉内連通孔17及
び煙道連通孔18との間に分流装置19が介設されてい
る。In the figure, a pottery furnace 1 includes a furnace bottom 2, a furnace body 3, a furnace cover 4, and a chimney 5, and the furnace bottom 2 communicates with the furnace interior 6 through a vertical communication hole 7 in front of the furnace. A first flue 9 surrounded by the body 3 and each partition 8 is disposed on both sides, and communicates with the first flue 9 via a left and right communication hole 10 at the rear, and is surrounded by the partition 8 on both sides. The second flue 11 is located in the center,
The second flue 11 communicates with an exhaust passage 12 in the chimney 5 through a front exhaust communication hole 13, and an air inlet 14 is provided in the furnace bottom 2 at an intermediate position of the second flue 11. Has been drilled. At the rear end of the furnace bottom 2, a hot gas inlet 16 of a kerosene burner 15 that generates oxidizing or reducing hot gas is opened, and the hot gas inlet 16 is connected to the inside 6 of the furnace and the second flue 11 respectively. A communication device 19 is provided through the in-furnace communication hole 17 and the flue communication hole 18, and a flow dividing device 19 is provided between the high-temperature gas inlet 16 and the in-furnace communication hole 17 and the flue communication hole 18.
【0012】前記構成において、高温ガス導入口16か
ら導入された酸化性又は還元性の高温ガスの内、主流分
は、分流装置19及び炉内連通孔17を介して炉内部6
に入ると共に陶芸成形物(図示省略)の焼成に供され、
その燃焼により生じた排気ガスは、同図(A)に示すよ
うに、上下連通孔7を介して第一の煙道9に入ると共に
高温ガス導入口16方向へと移動し、さらに、同図
(B)に示すように、左右連通孔10を介して第二の煙
道11に入ると共に排気連通孔13を介して排気流路1
2へと送出され、煙突5から排出される。また、高温ガ
ス導入口16から導入された酸化性又は還元性の高温ガ
スの一部は、同図(B)に示すように、分流装置19及
び煙道連通孔18を介して第二の煙道11に直接入り、
前記高温ガスが還元性の場合には、左右連通孔10から
導入された排気ガスに空気導入口14からの空気が添加
されて再燃焼し、酸化炎を生成して、前記高温ガス中の
不燃分を空気導入口14と排気連通孔13の間で完全燃
焼させる。In the above configuration, of the oxidizing or reducing high-temperature gas introduced from the high-temperature gas inlet 16, the main stream is supplied to the inside of the furnace 6 through the flow dividing device 19 and the communication hole 17 in the furnace.
As it enters, it is served for firing of ceramics moldings (not shown),
The exhaust gas generated by the combustion enters the first flue 9 through the upper and lower communication holes 7 and moves toward the high-temperature gas inlet 16 as shown in FIG. As shown in (B), the gas enters the second flue 11 through the left and right communication holes 10 and the exhaust passage 1 through the exhaust communication holes 13.
2 and discharged from the chimney 5. In addition, a part of the oxidizing or reducing high-temperature gas introduced from the high-temperature gas inlet 16 is supplied to the second smoke through the flow dividing device 19 and the flue communication hole 18 as shown in FIG. Directly into Road 11,
When the high-temperature gas is reductive, the air from the air inlet 14 is added to the exhaust gas introduced from the left and right communication holes 10 and recombusted, generating an oxidizing flame, and the non-combustible The part is completely burned between the air inlet 14 and the exhaust communication hole 13.
【0013】高温ガス導入口16から導入された酸化性
又は還元性の高温ガスは、既述のように、分流装置19
を介して炉内部6と第二の煙道11とに所要の配分で分
流される。図3は、図1に示す陶芸炉における分流装置
部分の断面図であり、(A)は高温ガスが炉内部と第二
の煙道の両方に配分された状態、(B)は高温ガスが炉
内部のみに配分された状態を示し、該分流装置19は、
炉内部6と第二の煙道11への高温ガスの各分流の流量
を前記(A)の状態と(B)の状態との間で連続的に調
整することが可能とされる。同図において、分流装置1
9は、第二の煙道11後端の天井部から垂下された三角
形断面を有する調整ブロック20と炉底2上に摺接され
た摺動板21とからなり、調整ブロック20先端部と摺
動板21の矩形調整孔22とが対向配置されている。同
図(A)では、摺動板21が、その調整孔22前端を調
整ブロック20先端部より幾分前方に配置させるように
調節され、この場合、高温ガス導入口16から導入され
た高温ガスは、炉内部6と第二の煙道11とに各々炉内
連通孔17及び煙道連通孔18を介して分流される。ま
た、同図(B)では、摺動板21が、その調整孔22前
端を調整ブロック20先端部と整合させるように調節さ
れ、この場合、高温ガス導入口16から導入された高温
ガスは、炉内部6のみに炉内連通孔17を介して導入さ
れている。The oxidizing or reducing high-temperature gas introduced from the high-temperature gas inlet 16 is supplied to the flow dividing device 19 as described above.
Through the furnace 6 and the second flue 11 at a required distribution. 3A and 3B are cross-sectional views of a flow dividing device in the pottery furnace shown in FIG. 1, wherein FIG. 3A shows a state in which the high-temperature gas is distributed to both the inside of the furnace and the second flue, and FIG. It shows a state distributed only inside the furnace, and the flow dividing device 19
It is possible to continuously adjust the flow rate of each branch of the high-temperature gas into the furnace interior 6 and the second flue 11 between the state (A) and the state (B). In FIG.
Reference numeral 9 denotes an adjustment block 20 having a triangular cross section suspended from the ceiling at the rear end of the second flue 11 and a slide plate 21 slidably contacting the furnace bottom 2. The rectangular adjustment hole 22 of the moving plate 21 is disposed to face. In FIG. 3A, the slide plate 21 is adjusted so that the front end of the adjustment hole 22 is disposed slightly forward of the front end of the adjustment block 20. In this case, the high-temperature gas introduced from the high-temperature gas introduction port 16 is used. Is diverted into the furnace interior 6 and the second flue 11 via the in-furnace communication hole 17 and the flue communication hole 18, respectively. In FIG. 2B, the slide plate 21 is adjusted so that the front end of the adjustment hole 22 is aligned with the front end of the adjustment block 20. In this case, the high-temperature gas introduced from the high-temperature gas inlet 16 is It is introduced only into the furnace interior 6 through the furnace communication hole 17.
【0014】〔実施例2〕図4は本発明の実施例2に係
る陶芸炉の、内側にある第二の煙道において切断した縦
断面図であり、図5は図4に示す陶芸炉における炉蓋及
び煙道天上部を取り外したときの平面斜視図である。Embodiment 2 FIG. 4 is a vertical cross-sectional view of a pottery furnace according to a second embodiment of the present invention, taken along a second flue inside, and FIG. 5 is a vertical sectional view of the pottery furnace shown in FIG. It is a plane perspective view at the time of removing the furnace lid and the upper part of the flue.
【0015】同図において、実施例2に係る陶芸炉1
は、既述の実施例1に示す2個の陶芸炉が1個の煙突5
を共有するように接合されてなり、両側の各高温ガス導
入口16から導入された酸化性又は還元性の高温ガスの
内、主流分は、各分流装置19を介して各側の炉内部6
に入ると共に陶芸成形物の焼成に供され、その燃焼によ
り生じた排気ガスは、各第一の煙道9に入って各高温ガ
ス導入口16方向へと移動し、さらに各左右連通孔10
を介して各第二の煙道11に入ると共に共通の排気連通
孔13を介して下方の排気流路12へと送出され、煙突
5から排出される。また、各高温ガス導入口16から導
入された酸化性又は還元性の高温ガスの一部は、各分流
装置19を介して各第二の煙道11に直接入り、前記高
温ガスが還元性の場合には、各左右連通孔10から導入
された排気ガスに各空気導入口14からの空気が添加さ
れて再燃焼し、酸化炎を生成して、前記高温ガス中の不
燃分を各空気導入口14と各排気連通孔13の間で完全
燃焼させる。In FIG. 1, a pottery furnace 1 according to a second embodiment is shown.
Means that the two pottery furnaces shown in Example 1 described above are
Of the oxidizing or reducing high-temperature gas introduced from each of the high-temperature gas inlets 16 on both sides, the main stream is separated through the respective flow dividing devices 19 into the furnace interior 6 on each side.
The exhaust gas generated by the combustion enters the first flue 9 and moves toward the high-temperature gas inlet 16, and is further subjected to the firing of the ceramics molded product.
, And is sent out to the lower exhaust passage 12 through the common exhaust communication hole 13 and discharged from the chimney 5. A part of the oxidizing or reducing high-temperature gas introduced from each high-temperature gas inlet 16 directly enters each second flue 11 through each branching device 19, and the high-temperature gas is reduced. In this case, the air from each air inlet 14 is added to the exhaust gas introduced from each of the left and right communication holes 10 and recombusted to generate an oxidizing flame. Complete combustion is performed between the port 14 and each exhaust communication hole 13.
【0016】[0016]
【発明の効果】本発明の請求項1に係る陶芸炉は以上の
ように構成され、酸化性又は還元性の高温ガスが分流装
置を介して炉内部のみならず排気流路に向かう煙道部分
にも導入されるので、炉内部における高温ガス導入口近
辺と排気流路近辺との温度差を緩和すると共に炉内部の
温度分布の均一化を図り、それによって陶芸成形物の均
一な焼成と燃焼効率の向上を可能にする。The pottery furnace according to the first aspect of the present invention is constructed as described above, and the oxidizing or reducing high-temperature gas passes through the flow dividing device not only to the inside of the furnace but also to the flue section toward the exhaust passage. So that the temperature difference between the vicinity of the high-temperature gas inlet and the vicinity of the exhaust passage inside the furnace is reduced, and the temperature distribution inside the furnace is made uniform, so that uniform firing and combustion of the pottery molded product is achieved. Enables increased efficiency.
【0017】また、請求項2に係るものでは、炉内部中
間にある共通の排気流路近辺の炉底が各煙道部分におけ
る高温ガスにより両側から加熱されるので、炉内部のよ
り均一な温度分布が得られる。請求項3に係るもので
は、高温ガス導入口からの高温ガスを炉内部及び排気流
路に向かう煙道部分に適宜の所要の配分で自在に分流さ
せることにより、炉内部及び該煙道部分における温度調
整等が容易に可能になる。請求項4に係るものでは、高
温ガス導入口からの高温ガスが酸化性の場合に、煙道部
分への酸化性高温ガスの導入により該煙道部分及び炉底
の温度を上昇させると共に炉内部の温度分布の均一化を
図ることができる。また、請求項5に係るものでは、高
温ガス導入口からの高温ガスが還元性の場合に、煙道部
分における排気ガスの再燃焼により煙道部分及び炉底の
温度を上昇させると共に炉内部の温度分布の均一化を図
り、しかも炉内部における陶芸成形物を所要の還元雰囲
気下に還元焼成すると共に煤煙を含まない完全燃焼状態
の排気ガスを排出させることができる。According to the second aspect of the present invention, since the bottom of the furnace near the common exhaust passage in the middle of the furnace is heated from both sides by the high-temperature gas in each of the flue portions, a more uniform temperature inside the furnace is obtained. A distribution is obtained. According to the third aspect, the high-temperature gas from the high-temperature gas inlet is freely diverted to the inside of the furnace and the flue portion toward the exhaust flow passage at an appropriate required distribution, so that the inside of the furnace and the flue portion can be separated. Temperature adjustment and the like can be easily performed. According to the present invention, when the high-temperature gas from the high-temperature gas inlet is oxidizing, the temperature of the flue portion and the furnace bottom is increased by introducing the oxidizing high-temperature gas into the flue portion, and the inside of the furnace is increased. Temperature distribution can be made uniform. According to the fifth aspect of the present invention, when the high-temperature gas from the high-temperature gas inlet is reducing, the temperature of the flue portion and the bottom of the furnace is increased by reburning the exhaust gas in the flue portion, and the inside of the furnace is increased. The temperature distribution can be made uniform, and the pottery molded product inside the furnace can be reduced and fired in a required reducing atmosphere, and exhaust gas in a completely burned state containing no soot can be discharged.
【図1】本発明の実施例1に係る陶芸炉の縦断面図であ
り、(A)は外側にある第一の煙道において切断したも
の、(B)は内側にある第二の煙道において切断したも
のを示している。FIG. 1 is a longitudinal sectional view of a pottery furnace according to a first embodiment of the present invention, in which (A) is cut in a first flue on the outside, and (B) is a second flue on the inside. In FIG.
【図2】図1に示す陶芸炉における炉蓋を取り外したと
きの平面図である。FIG. 2 is a plan view of the pottery furnace shown in FIG. 1 with a furnace lid removed.
【図3】図1に示す陶芸炉における分流装置部分の断面
図であり、(A)は高温ガスが炉内部と第二の煙道の両
方に配分された状態、(B)は高温ガスが炉内部のみに
配分された状態を示している。3A and 3B are cross-sectional views of a flow dividing device in the pottery furnace shown in FIG. 1, wherein FIG. 3A shows a state in which high-temperature gas is distributed to both the inside of the furnace and a second flue, and FIG. This shows a state of distribution only inside the furnace.
【図4】本発明の実施例2に係る陶芸炉の、内側にある
第二の煙道において切断した縦断面図である。FIG. 4 is a vertical cross-sectional view of a pottery furnace according to a second embodiment of the present invention, taken along a second flue inside.
【図5】図4に示す陶芸炉における炉蓋及び煙道天上部
を取り外したときの平面斜視図である。5 is a plan perspective view of the pottery furnace shown in FIG. 4 when a furnace lid and an upper portion of a flue are removed.
1 陶芸炉 2 炉底 6 炉内部 9 第一の煙道 11 第二の煙道 12 排気流路 14 空気導入口 16 高温ガス導入口 19 分流装置 DESCRIPTION OF SYMBOLS 1 Ceramic art furnace 2 Furnace bottom 6 Furnace interior 9 First flue 11 Second flue 12 Exhaust flow path 14 Air inlet 16 Hot gas inlet 19 Separating device
Claims (5)
口から酸化性又は還元性の高温ガスが導入されると共に
分流装置を介して炉内部における陶芸成形物の焼成と炉
内部から煙道を介して排気流路に送出される排気ガスの
完全燃焼のために分流して使用され、実質的に完全燃焼
した排気ガスとして排気流路から外部に排出されるよう
にしてなる陶芸炉において、前記排気ガスの完全燃焼の
ための高温ガスを煙道に分流させ、且つ煙道における少
なくとも高温ガスの分流位置から排気流路に至るまでの
煙道部分を炉底に配置すると共に該煙道部分の中間位置
に酸化炎生成のための空気導入口を設けたことを特徴と
する陶芸炉。An oxidizing or reducing high-temperature gas is introduced from a high-temperature gas inlet provided in a furnace bottom or a lower part of a furnace body, and a ceramics molded article is baked in the furnace through a branching device and smoke is generated from the furnace. In a pottery furnace which is used by being diverted for complete combustion of exhaust gas sent out to an exhaust passage through a road, and is discharged from the exhaust passage to the outside as substantially completely burned exhaust gas. Diverting the hot gas for complete combustion of the exhaust gas into the flue, and arranging at least a portion of the flue in the flue from the hot gas diverting position to the exhaust passage at the furnace bottom, A pottery furnace characterized by having an air inlet for generating an oxidizing flame at an intermediate position of the portion.
向する両側に個別に設けると共に共通の排気流路を前記
両側の高温ガス導入口間に設けた請求項1記載の陶芸
炉。2. The pottery furnace according to claim 1, wherein hot gas inlets are individually provided on opposite sides of the furnace bottom or the lower part of the furnace body, and a common exhaust passage is provided between the hot gas inlets on both sides.
に向かう煙道部分への高温ガスの各分流の流量調節を可
能とした請求項1又は2記載の陶芸炉。3. The pottery furnace according to claim 1, wherein the flow dividing device is capable of adjusting the flow rate of each branch of the high-temperature gas to the inside of the furnace and to a flue portion toward the exhaust flow path.
の場合に、炉内部及び排気流路に向かう煙道部分への高
温ガスの各分流の流量を調節すると共に該煙道部分に酸
化性の高温ガスを導入させた請求項1、2又は3記載の
陶芸炉。4. When the high-temperature gas from the high-temperature gas inlet is oxidizing, the flow rate of each branch of the high-temperature gas to the flue section toward the inside of the furnace and the exhaust passage is adjusted, and the high-temperature gas is oxidized. The pottery furnace according to claim 1, wherein a high-temperature gas having a characteristic property is introduced.
の場合に、炉内部及び排気流路に向かう煙道部分への高
温ガスの各分流の流量を調節すると共に該煙道部分にお
いて酸化炎を生成させた請求項1、2又は3記載の陶芸
炉。5. When the high-temperature gas from the high-temperature gas inlet is reducing, the flow rate of each branch of the high-temperature gas to the flue section toward the inside of the furnace and the exhaust passage is adjusted, and oxidation is performed in the flue section. 4. The pottery furnace according to claim 1, wherein the flame is generated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10341083A JP2000154052A (en) | 1998-11-15 | 1998-11-15 | Furnace for ceramic-art object |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10341083A JP2000154052A (en) | 1998-11-15 | 1998-11-15 | Furnace for ceramic-art object |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000154052A true JP2000154052A (en) | 2000-06-06 |
Family
ID=18343101
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10341083A Pending JP2000154052A (en) | 1998-11-15 | 1998-11-15 | Furnace for ceramic-art object |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000154052A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100717244B1 (en) | 2005-11-24 | 2007-05-15 | 유나이티드피엠(주) | Melting furnace equipped with gas injection means for impurities elimination |
CN106524160A (en) * | 2017-01-10 | 2017-03-22 | 中冶华天工程技术有限公司 | No-open-flame fuel gas uniform-temperature heating device |
-
1998
- 1998-11-15 JP JP10341083A patent/JP2000154052A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100717244B1 (en) | 2005-11-24 | 2007-05-15 | 유나이티드피엠(주) | Melting furnace equipped with gas injection means for impurities elimination |
CN106524160A (en) * | 2017-01-10 | 2017-03-22 | 中冶华天工程技术有限公司 | No-open-flame fuel gas uniform-temperature heating device |
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