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JPS589915B2 - Anzatu formation prevention device and method in cement firing process - Google Patents

Anzatu formation prevention device and method in cement firing process

Info

Publication number
JPS589915B2
JPS589915B2 JP54058707A JP5870779A JPS589915B2 JP S589915 B2 JPS589915 B2 JP S589915B2 JP 54058707 A JP54058707 A JP 54058707A JP 5870779 A JP5870779 A JP 5870779A JP S589915 B2 JPS589915 B2 JP S589915B2
Authority
JP
Japan
Prior art keywords
kiln
preheating device
cement firing
water
anzatu
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
JP54058707A
Other languages
Japanese (ja)
Other versions
JPS55152379A (en
Inventor
小川正
小野舜一郎
色川喜理
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.)
Sumitomo Cement Co Ltd
Original Assignee
Sumitomo Cement 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 Sumitomo Cement Co Ltd filed Critical Sumitomo Cement Co Ltd
Priority to JP54058707A priority Critical patent/JPS589915B2/en
Publication of JPS55152379A publication Critical patent/JPS55152379A/en
Publication of JPS589915B2 publication Critical patent/JPS589915B2/en
Expired legal-status Critical Current

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  • Furnace Details (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【発明の詳細な説明】 本発明はセメント焼成工程におけるアンザッ生成防止に
間する。
DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to the prevention of ANZA formation during the cement firing process.

セメント焼成において、重油を熱源とする場合、重油を
予熱するための蒸気が必要である。
In cement firing, when heavy oil is used as a heat source, steam is required to preheat the heavy oil.

従来はボイラを設置し,重油を焚いてこの予熱蒸気を作
るかあるいはエアクエンチングクーラー(以lFAQC
と略記する)の余剰排気を廃熱回収ボイラヘ通して蒸気
を得ている。
Conventionally, a boiler was installed and heavy oil was burned to create this preheated steam, or an air quenching cooler (hereinafter referred to as FAQC) was installed.
Steam is obtained by passing the excess exhaust gas (abbreviated as ) to a waste heat recovery boiler.

セメント焼成工程においてはアルカリ等の低融点物質を
含むダストが沈着生長してアンザツを形成し7、それが
正常運転を阻害し熱効率を悪化させ、ひどい場合には運
転不能に至らしめる個所がある。
In the cement firing process, dust containing low-melting substances such as alkali deposits and grows to form ants7, which impedes normal operation and deteriorates thermal efficiency, and in severe cases can lead to inoperability.

これに対しては通常突き棒や高田水流を用いて外部から
人力で定期または不定期的に突落す方法か、アンザツ附
着位置に水冷箱をおいて冷却しアンザツ附着を防止する
方法がとられている。
To deal with this, the usual methods are to use a push rod or a Takada water stream to manually plunge the fish from the outside on a regular or irregular basis, or to cool it by placing a water-cooled box at the Anzatu attachment location to prevent Anzatu attachment. There is.

アンザツを突落す方法においては除去作業期間中に外部
から冷風が掃除孔を通して吸込まれるので正常通風を阻
害するから、この期間中の減産と熱効率悪化が起る。
In the method of dropping Anzatu, cold air is sucked in from the outside through the cleaning hole during the removal work, which obstructs normal ventilation, resulting in reduced production and deterioration of thermal efficiency during this period.

また、水冷箱を設置する方法においては、箱中に管群を
配設し、箱内の空間には熱媒体油を満たし、この熱媒体
油が高温となり、これにより管群中の冷却水が蒸気或は
温水となって熱媒油を通じて、セメント焼成工程の予熱
装置の壁面が間接的に冷却されるので、冷却効率が悪く
、設備自体も複雑である。
In addition, in the method of installing a water-cooled box, a group of tubes is placed in the box, and the space inside the box is filled with heat transfer oil, which becomes hot and causes the cooling water in the group of tubes to cool. The wall surface of the preheating device for the cement firing process is indirectly cooled through the heat transfer oil as steam or hot water, so the cooling efficiency is poor and the equipment itself is complicated.

本発明の第1の発明は、セメント焼成工程の予熱装置に
、その壁面を冷却させる水管群を設置することを特徴と
するセメント焼成工程における予熱装置のアンザツ生成
防止装置である。
A first aspect of the present invention is an anzatu formation prevention device for a preheating device in a cement firing process, characterized in that a group of water pipes for cooling the wall surface of the preheating device is installed in the preheating device for the cement firing process.

さらに第2の発明は、セメント焼成工程の予熱装置に、
水管群を設置し、該予熱装置からの放散熱並びに排熱を
該水管群内の供給水と熱交換させて該予熱装置の壁面を
冷却させてアンザツの生成を防止することを特徴とする
セメント焼成工程における予熱装置のアンザツ生成防止
方法である。
Furthermore, the second invention is a preheating device for a cement firing process,
A cement characterized in that a group of water pipes is installed, and the radiated heat and exhaust heat from the preheating device are exchanged with the supply water in the group of water tubes to cool the wall surface of the preheating device and prevent the formation of Anzatu. This is a method for preventing the formation of anzatz in a preheating device during the firing process.

次に実施例によって本発明を更に具体的に説明する。Next, the present invention will be explained in more detail with reference to Examples.

実施例1レポルプレヒーターへの適用 図1はレポルプレヒーターの構造とそこに附着するアン
ザツを示している。
Example 1 Application to Repol preheater FIG. 1 shows the structure of Repol preheater and the anzatz attached thereto.

原料1は供給口3から粒状で供給され、移動格子4に乗
って移動し、途中キルン9からのガスと熱交換しながら
、スクレーパ−7、供給ガイド8を経てキルン9へと送
入される。
Raw material 1 is supplied in granular form from a supply port 3, moves on a moving grid 4, and is sent to a kiln 9 via a scraper 7 and a supply guide 8 while exchanging heat with gas from a kiln 9 along the way. .

一方キルン9からの排ガスはプレヒーター室6&こ入り
、第1次ファン10に吸引されて原料層1、移動格子4
を通過して第1次ファン10に至り、ここから第2室5
へ送られ、同様に原料層、移動格子を通過(,て第2次
ファン11に吸引され、ここから外部へ排出される。
On the other hand, the exhaust gas from the kiln 9 enters the preheater chamber 6 & is sucked by the primary fan 10, and is transferred to the raw material layer 1 and the moving grid 4.
It passes through to the primary fan 10, and from there it flows into the second chamber 5.
Similarly, it passes through a raw material layer and a moving grid (and is sucked into the secondary fan 11, from where it is discharged to the outside).

移動格子の隙間からこぼれ落ちた小粒の原料はホッパ=
12へ集められる。
The small particles of raw material that have fallen through the gaps in the moving grid are transferred to the hopper.
Collected to 12.

キルン9からの排ガスにはダストが含まれ、これがプレ
ヒーター流し,込み部天井14並び同一室の天井17、
プレヒーター流し,込み部側壁16並び同一室側壁18
に附着し,、アンザツを形成する。
The exhaust gas from the kiln 9 contains dust, and this is poured into the preheater, the ceiling 14 of the recess, and the ceiling 17 of the same room.
Preheater sink, side wall 16 in the same room side wall 18
It is attached to the island, forming Anzatu.

また原料層へ沈着し、原料と共に運ばれキルン9へ入る
際、係給ガイド8の斜面上で粘着固化して、アンザツを
形成する。
Further, it is deposited on the raw material layer, and when it is carried along with the raw material and enters the kiln 9, it adheres and solidifies on the slope of the engaging guide 8, forming an anzatu.

これに対し、キルンへの原料流入部の天井14、同部の
側壁15及び16、更に一室天井17の各所に掃除孔を
設け、ここからアンザツを高圧水流などにより突落すの
が従来の仕方であった。
In contrast, the conventional method is to provide cleaning holes at various locations in the ceiling 14 of the raw material inflow section to the kiln, the side walls 15 and 16 of the same section, and the ceiling 17 of one room, and the Anzatsu is dropped from there using a high-pressure water stream. Met.

この発明では図2に示すように、キルンへの原料流込部
の天井19、同部正面側壁20及び同部左右側壁21、
更に一室側壁23にそれぞれ1インチ高温配管用炭素鋼
管の水管群をレンガ壁土に敷設、また供給ガイド8上に
水冷箱22を設置して冷却水を流して運転した。
In this invention, as shown in FIG. 2, the ceiling 19 of the raw material inflow section to the kiln, the front side wall 20 of the section, the left and right side walls 21 of the section,
Furthermore, water pipe groups of 1-inch carbon steel pipes for high-temperature piping were laid on the brick wall soil on the side walls 23 of each room, and a water cooling box 22 was installed on the supply guide 8 to allow cooling water to flow therethrough.

これによれば従来悩まされたアンザツ附着生長が著しく
減少して、アンザツ防止の目的を達することができた。
According to this method, the epiphytic growth of the Japanese lanternfly, which had been a problem in the past, was significantly reduced, and the purpose of preventing the Japanese lanternfly was achieved.

次に冷却水を絞って蒸気発生実験を行ない、通常使用さ
れる150°05気圧の飽和蒸気を得ることができた。
Next, we conducted a steam generation experiment by squeezing the cooling water, and were able to obtain the normally used saturated steam at 150°05 atm.

この時の水管の伝熱係数は2 7 Krai / m2
)1’0,であった。
The heat transfer coefficient of the water pipe at this time is 2 7 Krai / m2
) 1'0.

この実験をもとに改めて焼成用重油予熱に必要な蒸気量
22kg/tを得るための水管群を設計施工し,た。
Based on this experiment, we designed and constructed a group of water pipes to obtain the steam volume of 22 kg/t required for preheating heavy oil for firing.

グレートプレヒーターのキルンへの原料流込み部分の天
井及び側壁には、蒸気発生に必要な水管群を設備する十
分な壁面積はあるけれども、アンザツ附着防止のため重
要局部に設備した水管をそのまま利用し、追加分はプレ
ヒーター二室へ敷設した。
Although there is sufficient wall area on the ceiling and side walls of the area where raw materials flow into the kiln of the great preheater to install the water pipes necessary for steam generation, the water pipes installed in important areas are used as they are to prevent Anzatu from sticking. The additional amount was installed in two preheater rooms.

これは夏期と冬期での蒸気必要量変化に対処する目的も
ある。
This is also intended to address changes in steam requirements between summer and winter.

以上の工事を実施して運転し、所期の目的であるアンザ
ツ防止と蒸気発生を実現することができた。
By carrying out the above construction work and operating the plant, we were able to achieve the intended objectives of preventing Anzatu and generating steam.

実施例2サスペンションプレヒーターへの適用図3は助
燃炉付サスペンションプレヒーターキルン(SF式)を
表わしている。
Embodiment 2 Application to suspension preheater FIG. 3 shows a suspension preheater kiln (SF type) with an auxiliary combustion furnace.

図3において原料は25より投入され下から上って来る
排ガスと混合して熱交換し、最初のサイクロン28にお
いて分離され、以下順次に排ガスと混合一熱交換一分離
しながら、下方へ降りて来る。
In Fig. 3, the raw material is introduced from 25, mixes with the exhaust gas coming up from below, exchanges heat, is separated in the first cyclone 28, and then descends downward while sequentially mixing with the exhaust gas, exchanging heat, and separating. come.

本例においてはサイクロン30から、助燃炉32に入り
、ここで助燃炉燃焼37により仮焼されてサイクロン3
1に入り分離後、窯入流込35を経てキルン9に入り、
キルン燃焼燃料36によって焼成されクリンカとなり、
エアクエンチングクーラー27(AQC)に入り、空気
で冷却され、排出される。
In this example, the cyclone 30 enters the auxiliary combustion furnace 32, where it is calcined by the auxiliary combustion furnace 37, and the cyclone 3
1, after separation, enters the kiln 9 via the kiln inlet 35,
It is burned by the kiln combustion fuel 36 and becomes clinker,
It enters an air quenching cooler 27 (AQC), is cooled with air, and is discharged.

AQCにおいて押込まれた空気はクリンカを冷却後3つ
に分れ、一つはキルンを通り、一つは渦巻室33、助燃
炉32を経て、両者合流し,てサスペンションタワーを
上昇し、排ガスとなって出、他の一つはAQC余剰排気
として排出される。
After cooling the clinker, the air forced in the AQC is divided into three parts: one passes through the kiln, the other passes through the volute chamber 33 and the auxiliary combustion furnace 32, and then the two join together, ascend the suspension tower, and are separated from the exhaust gas. The other one is discharged as AQC surplus exhaust.

この系において原料中に含まれるアルカリ等の低融点低
沸点物質はキルン9において揮発しガスと共に上昇する
中で原料により固化し原料に附着し、再度キルンヘ入る
循環路を形成し濃縮されて来て、もつと融着性が強くな
る温度の点において、装置のレンガ表面へ附着生長して
アンザツを形成する。
In this system, low-melting and low-boiling substances such as alkalis contained in the raw materials are volatilized in the kiln 9, solidified by the raw materials as they rise with the gas, and attached to the raw materials, forming a circulation path that enters the kiln again and becoming concentrated. When the temperature reaches a point where the fusion property becomes strong, it grows attached to the brick surface of the device and forms anzatu.

図4で云えば窯入流込35、立上り風管34、渦巻室3
3である。
In Fig. 4, there is a kiln inlet 35, a rising wind pipe 34, and a swirl chamber 3.
It is 3.

これらの位置へ渦巻室33に水管群38、立上り風管に
水管群39、窯入流込に水管群40を設置して通水し冷
却することによりアンザツ生成を防止する一方、水を蒸
発させて蒸気として取出し、これを重油予熱あるいはそ
の他に使用する。
A water pipe group 38 in the swirl chamber 33, a water pipe group 39 in the rising wind pipe, and a water pipe group 40 in the inlet of the kiln are installed at these positions to flow water and cool it, thereby preventing the formation of Anzatu, while evaporating the water. It is extracted as steam and used for preheating heavy oil or for other purposes.

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

図1はレポール式プレヒータの断面図、並びそのA−A
′断面図、図2は各位置に本発明の水管群を設置したレ
ポール式プレヒーターの断面図、図3は助燃炉付サスペ
ンションプレヒーターキルンによるセメントクリンカー
製造工程図説明図、図4は図3の渦巻室、立上り風管、
窯入流込み部に設置された本発明の水管群説明図である
。 1・・・・・・原料、2・・・・・・グレートフレヒー
ター、3・・・・・・原料供給口、4・・・・・・移動
格子、5・・・・・・プレヒーター第2室、6・・・・
・・プレヒーター第1室、7・・・・・・スクレーパー
、8・・・・・・供給ガイド、9・・・・・・キルン、
10・・・・・・第1次ファン、11・・・・・・第2
次ファン、12・・・・・・ホツパー、13・・・・・
・仕切壁、14・・・・・・キルンへの原料流込み部分
の天井、15・・・・・・キルンへの原料流込み部分の
側壁(キルン長手方向直角)、16・・・・・・キルン
への原料流込み部分の側壁(キルン長手方向平行)、1
7・・・・・・プレヒーター一室側壁天井、j8・・・
・・・プレヒーター一室側壁、19・・・・・・キルン
への原料流込み部分の天井にとりつけた水管群、20・
・・・・・キルンへの原料流込み部分の正面側壁にとり
つけた水管群、21・・・・・・キルンへの原料流込み
部分の左右側壁にとりつけた水管群、22・・・・・・
キルンへの原料流込み部分の傾斜壁にとりつけた水管、
23・・・・・・プレヒーター一室側壁にとりつけた水
管群、24・・・・・・プレヒーター二室仕切壁裏にと
りつけた水管群、25・・・・・・原料投入口、26・
・・・・・助燃炉付サスペンションプレヒーター、27
・・・・・・AQC、28・・・・・・4段サイクロン
、29・・・・・・3段サイクロン、30・・・・・・
2段サイクロン、31・・・・・・1段サイクロン、3
2・・・・・・SF式助燃炉、33・・・・・・渦巻室
、34・・・・・・立上り風管、35・・・・・・窯入
流込、36・・・・・・キルン焼成燃料、37・・・・
・・助燃炉燃料、38・・・・・・渦巻室にとりつけた
水管群、39・・・・・・立上り風管にとりつけた水管
群、40・・・・・・窯入流込にとりつけた水管群。
Figure 1 is a cross-sectional view of a Lepore type preheater, and its A-A
' Cross-sectional view, Figure 2 is a cross-sectional view of a Lepore type preheater in which the water tube group of the present invention is installed at each position, Figure 3 is an explanatory diagram of a cement clinker manufacturing process using a suspension preheater kiln with an auxiliary furnace, and Figure 4 is a diagram volute chamber, rising wind pipe,
It is an explanatory view of a group of water pipes of the present invention installed in a kiln inflow part. 1... Raw material, 2... Great flame heater, 3... Raw material supply port, 4... Moving grid, 5... Preheater 2nd room, 6...
... Preheater chamber 1, 7 ... Scraper, 8 ... Supply guide, 9 ... Kiln,
10...1st fan, 11...2nd fan
Next fan, 12...Hopper, 13...
・Partition wall, 14...Ceiling of the part where raw materials flow into the kiln, 15...Side wall of the part where raw materials flow into the kiln (perpendicular to the longitudinal direction of the kiln), 16...・Side wall of the part where raw materials flow into the kiln (parallel to the longitudinal direction of the kiln), 1
7... Preheater room side wall ceiling, j8...
... Side wall of the preheater room, 19 ... Water pipes attached to the ceiling of the area where raw materials flow into the kiln, 20.
...A group of water tubes attached to the front side wall of the part where raw materials flow into the kiln, 21...A group of water pipes attached to the left and right side walls of the part where raw materials flow into the kiln, 22...・
A water pipe attached to the sloped wall where raw materials flow into the kiln,
23... Water pipe group attached to the side wall of one preheater room, 24... Water pipe group attached to the back of the partition wall of two preheater rooms, 25... Raw material input port, 26・
...Suspension preheater with auxiliary combustion furnace, 27
...AQC, 28...4 stage cyclone, 29...3 stage cyclone, 30...
2-stage cyclone, 31...1-stage cyclone, 3
2...SF type auxiliary combustion furnace, 33...Vortex chamber, 34...Rising wind pipe, 35...Kiln inflow, 36...・Kiln firing fuel, 37...
... Fuel for the auxiliary combustion furnace, 38 ... Water tube group attached to the volute chamber, 39 ... Water tube group attached to the rising wind pipe, 40 ... ... Water tube group attached to the kiln inlet. Water pipe group.

Claims (1)

【特許請求の範囲】 1 セメント焼成工程の予熱装置に、その壁面を冷却さ
せる水管群を設置することを特徴とするセメント焼成工
程における予熱装置のアンザツ生成防止装置。 2 水管群を予熱装置の原料流し込み部分の天井、側壁
、ロータリーキルンへの原料供給傾斜壁、ガス立上り風
管並びに渦巻室に設置する特許請求の範囲第1項記載の
装置。 3 セメント焼成工程がレポール式プレヒーターキルン
から構成されている特許請求の範囲第1項または第2項
記載の装置。 4 セメント焼成工程がサスペンションプレヒーターキ
ルンまたは助燃炉付サスペンションキルンから構成され
ている特許請求の範囲第1項または第2項記載の装置。 5 セメント焼成工程の予熱装置に、水管群を設置し7
、該予熱装置からの放散熱並びに排熱を該水管群内の供
給水と熱交換させ該予熱装置の壁面を冷却させてアンザ
ツの生成を防止することを特徴とするセメント焼成工程
における予熱装置のアンザツ生成防止方法。 6 水管群を予熱装置の原料流し込み部分の天井、ロー
タリーキルンへの原料供給傾斜壁、ガス立上り風管並げ
に渦巻室に設置し、これらからの放散熱並びに排熱を該
水管内の供給水と熱交換させ、該予熱装置のこれらの場
所の壁面を冷却させてアンザツの生成を防止する特許請
求の範囲第5項記載の方法。 7 セメント炉成工程がレポール式プレーヒーターキル
ンから構成されている特許請求の範囲第5項または第6
項記載の方法。 8 セメント焼成工程がサスペンションプレヒーターキ
ルンまたは助燃炉付サスペンションキルンから構成され
ている特許請求の範囲第5項または第6項記載の方法。
[Scope of Claims] 1. Anzatu formation prevention device for a preheating device in a cement firing process, characterized in that a group of water pipes for cooling the wall surface of the preheating device is installed in the preheating device for the cement firing process. 2. The apparatus according to claim 1, wherein the water tube group is installed on the ceiling and side wall of the raw material pouring part of the preheating device, on the inclined wall for supplying raw material to the rotary kiln, on the gas rising wind pipe, and on the swirl chamber. 3. The apparatus according to claim 1 or 2, wherein the cement firing step comprises a Lepore type preheater kiln. 4. The apparatus according to claim 1 or 2, wherein the cement firing process comprises a suspension preheater kiln or a suspension kiln with an auxiliary combustion furnace. 5 A group of water pipes is installed in the preheating device for the cement firing process.7
A preheating device in a cement firing process, characterized in that the radiated heat and exhaust heat from the preheating device are exchanged with the supply water in the water tube group to cool the wall surface of the preheating device and prevent the formation of anzatu. How to prevent Anzatu formation. 6. A group of water pipes is installed in the ceiling of the raw material pouring part of the preheating device, the inclined wall for supplying raw material to the rotary kiln, and the swirl chamber along with the gas riser wind pipes, and the radiated heat and exhaust heat from these are combined with the supply water in the water pipes. 6. The method according to claim 5, wherein the preheating device is cooled at these locations to prevent the formation of ants. 7. Claim 5 or 6 in which the cement furnace formation process is comprised of a Lepore type play heater kiln.
The method described in section. 8. The method according to claim 5 or 6, wherein the cement firing step comprises a suspension preheater kiln or a suspension kiln with an auxiliary combustion furnace.
JP54058707A 1979-05-15 1979-05-15 Anzatu formation prevention device and method in cement firing process Expired JPS589915B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54058707A JPS589915B2 (en) 1979-05-15 1979-05-15 Anzatu formation prevention device and method in cement firing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54058707A JPS589915B2 (en) 1979-05-15 1979-05-15 Anzatu formation prevention device and method in cement firing process

Publications (2)

Publication Number Publication Date
JPS55152379A JPS55152379A (en) 1980-11-27
JPS589915B2 true JPS589915B2 (en) 1983-02-23

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Application Number Title Priority Date Filing Date
JP54058707A Expired JPS589915B2 (en) 1979-05-15 1979-05-15 Anzatu formation prevention device and method in cement firing process

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Country Link
JP (1) JPS589915B2 (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5327736A (en) * 1976-08-25 1978-03-15 Toyota Motor Corp Over-heating prevention means for catalytic converter
JPS5365047U (en) * 1976-11-04 1978-06-01
JPS5435102A (en) * 1977-08-25 1979-03-15 Nippon Steel Corp Recovering method for sensible heat of granular matter of high temperature

Also Published As

Publication number Publication date
JPS55152379A (en) 1980-11-27

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