JPS606692B2 - Firing method and furnace - Google Patents

Firing method and furnace

Info

Publication number
JPS606692B2
JPS606692B2 JP12120982A JP12120982A JPS606692B2 JP S606692 B2 JPS606692 B2 JP S606692B2 JP 12120982 A JP12120982 A JP 12120982A JP 12120982 A JP12120982 A JP 12120982A JP S606692 B2 JPS606692 B2 JP S606692B2
Authority
JP
Japan
Prior art keywords
furnace
gas
peripheral wall
several
fired
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
JP12120982A
Other languages
Japanese (ja)
Other versions
JPS5912745A (en
Inventor
靖夫 広瀬
秀治 松尾
勝男 腰塚
俊明 田部井
光雄 望月
昭夫 鈴木
隆 大槻
裕 吉田
伸匡 田々楽
隆 田村
光正 島崎
仁 永井
雅男 川本
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.)
Takenaka Komuten Co Ltd
Original Assignee
Takenaka Komuten 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 Takenaka Komuten Co Ltd filed Critical Takenaka Komuten Co Ltd
Priority to JP12120982A priority Critical patent/JPS606692B2/en
Publication of JPS5912745A publication Critical patent/JPS5912745A/en
Publication of JPS606692B2 publication Critical patent/JPS606692B2/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J6/00Heat treatments such as Calcining; Fusing ; Pyrolysis
    • B01J6/001Calcining
    • B01J6/004Calcining using hot gas streams in which the material is moved

Landscapes

  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Compounds Of Iron (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【発明の詳細な説明】 本発明は、たとえば磁性酸化鉄あるいは石灰の焼成方法
および焼成炉に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to, for example, a method for firing magnetic iron oxide or lime, and a firing furnace.

〔発明の目的〕[Purpose of the invention]

本発明の一つの目的は熱効率の高い堅型キルンによる磁
性酸化鉄の仮焼方法の開示でありこの仮暁において製品
を劣化させる諸欠点が発生しないようにした堅型炉装置
の提供である。
One object of the present invention is to disclose a method for calcining magnetic iron oxide using a vertical kiln with high thermal efficiency, and to provide a vertical furnace apparatus that does not cause defects that degrade the product during calcining.

従来磁性酸化鉄の仮焼にロータリキルンを使用した場合
燃料原単位は製品lton当り130〜180×1ぴk
calであった。
Conventionally, when a rotary kiln is used for calcining magnetic iron oxide, the fuel consumption rate is 130 to 180 x 1 pk per ton of product.
It was cal.

ロータリキルンは排ガスによる特出顕熱が大きく炉壁放
熱や漏洩空気も大量であるから原単位は大になる。堅型
炉の場合は20n/日の小型炉における燃料原単位は8
0〜100×1ぴkcalであり、12bn/日規模の
実際の状態にスケールアップした場合の燃料原単位を試
算すると40×1ぴkcal程度に減少させることがで
きることが判明している。
In a rotary kiln, the specific sensible heat generated by the exhaust gas is large, and there is a large amount of heat dissipated from the furnace wall and leakage of air, so the basic unit is large. In the case of a rigid reactor, the fuel consumption rate in a small reactor is 20n/day.
It is 0 to 100×1 pkcal, and it has been found that the fuel consumption rate when scaled up to an actual state of 12 bn/day can be reduced to about 40×1 pkcal.

現在堅型炉で造る仮焼磁性酸化鉄はロータリキルンで造
るものより若干品質が劣るとされている。
Currently, the quality of calcined magnetic iron oxide produced in hard furnaces is said to be slightly inferior to that produced in rotary kilns.

しかしながら本発明の堅型炉は自然落下方式であって堅
型炉内に乾燥・子熱ひ焼成。
However, the vertical furnace of the present invention is of a natural fall type, and is used for drying and heating in the vertical furnace.

冷却のゾーンをすなわち4工程を設けている。被焼成材
料は上記4工程を経て製品となる。磁性酸化鉄の仮競に
おいては還元性ガスの発生は製品の品質に悪影響を与え
るので急速混合短炎バーナを採用しかっこのバーナはN
○x発生防止のため2段燃焼方式にする。
There are four cooling zones, that is, four steps. The material to be fired becomes a product through the above four steps. In the preliminary production of magnetic iron oxide, a rapid mixing short flame burner is used because the generation of reducing gas has a negative effect on the quality of the product.
○Use a two-stage combustion method to prevent the occurrence of x.

また磁性酸化鉄の炉内の下降すなわち進行は自重によっ
て行なわれるがその下降を生ぜしめる排出機はその回転
数が制御可能構造であるスクリュフィダーが採用される
Further, the descent or advancement of the magnetic iron oxide in the furnace is performed by its own weight, and the discharge machine that causes the descent is a screw feeder whose rotation speed can be controlled.

排気へッダーの粒による閉塞を防止するため6個の吸引
孔を設け各吸引孔は内筒を取付けた構造にする。
In order to prevent blockage due to particles in the exhaust header, six suction holes are provided, and each suction hole has an inner cylinder attached to it.

乾燥ゾーンのブリッジの発生を防止するため発生水蒸気
が急速に排気吸引孔によって吸引されるように風量を大
にする。
To prevent bridging of the drying zone, increase the air volume so that the generated water vapor is rapidly sucked through the exhaust suction hole.

かつその炉内における流れを活溌にすることによって焼
成ゾーンのブリッジの発生を防止し原料の昇温による膨
脹と表面が高温になって融着される現象が発生しないよ
うにする。焼成ゾーンの熱ガス温度を磁性酸化鉄の溶融
温度150000より低い1200〜13000Cにし
この燃焼ガスを大量の並流と少量の向流に分けて流す構
造にする。
Moreover, by making the flow in the furnace active, the occurrence of bridging in the firing zone is prevented, and the phenomenon of expansion due to rising temperature of the raw material and fusion of the surface due to high temperature is prevented from occurring. The temperature of the hot gas in the firing zone is set to 1,200 to 13,000 C, which is lower than the melting temperature of magnetic iron oxide, which is 150,000, and the combustion gas is divided into a large amount of cocurrent flow and a small amount of countercurrent flow.

燃焼ゾーンの火炎温度を120000以上にするため側
壁を断熱煉瓦で巻いて放熱防止を図って炉内の焼成温度
の低下を防止する。空気比を1.0朝蓮度にするとブリ
ッジが発生されやすくその融着物をX線回析により検査
した結果酸化第1鉄であることが判明し、これは還元ガ
スの発生によるものと判断されるので空気比を1.05
以下に低下させないようにコントロールする。
In order to keep the flame temperature in the combustion zone above 120,000, the side walls are wrapped with insulating bricks to prevent heat radiation and prevent the firing temperature in the furnace from decreasing. When the air ratio is set to 1.0, bridging tends to occur and the resulting fused material was examined by X-ray diffraction and was found to be ferrous oxide, which was determined to be due to the generation of reducing gas. Therefore, the air ratio is set to 1.05.
Control so that it does not fall below.

燃焼ガスが上下に振り分けられ最高温度位置がバーナか
ら若干下の位置であるようにしかつ炉中がだんだん広く
なる構造にしてブリッジの発生を防止している。〔従釆
の技術〕 本願の出願人の1人である竹中工務店は侍願昭51−1
58030(特関昭53−80400)で「不定形フェ
ライト焼成炉」の特許出願をしている。
The combustion gas is divided into upper and lower parts so that the highest temperature point is slightly below the burner, and the furnace is designed to gradually become wider to prevent bridging from occurring. [Successful technology] Takenaka Corporation, one of the applicants of the present application, is the owner of the Samurai Gansho 51-1
58030 (Special Seki Sho 53-80400), filed a patent application for ``amorphous ferrite firing furnace''.

その内容は特許請求の範囲の記載によれば下記4構成要
件よりなる堅型炉である。1 耐火材内張りの筒状炉体
を縦方向不回動に設置し2 該炉体の月同壁所定高さ位
置周囲には燃料ノズルを貫通槽設装備し3 かつその下
方所定位置周囲には冷却用空気ノズルを貫通楯設装備し
4 該炉体の下端閉口より下方所定間隔離して回転駆動
掻取板付備のフェライト受取用ロータリテーブルを設置
してなる不定形フェライト焼成炉本発明は上述の堅型炉
より高い堅型炉を採用し、炉内に乾燥・子熱・焼成・冷
却ゾーンを設け、前者が向流式であるのに対し本発明は
向並流式で主として並流である焼成炉にし頂部が径が小
さく底部が径が大であるようにテーパ−を設けた構造に
してブリッジの形成を防止している。
According to the claims, the content is a vertical furnace consisting of the following four constituent elements. 1. A cylindrical furnace body lined with refractory material is installed so as not to rotate in the vertical direction. 2. A fuel nozzle is installed in a penetrating tank around a predetermined height position on the same wall of the furnace body. An amorphous ferrite firing furnace comprising a cooling air nozzle installed in a penetrating shield, and a rotary table for receiving ferrite equipped with a rotationally driven scraping plate installed at a predetermined distance below the closed bottom end of the furnace body. A vertical furnace is used, which is taller than a vertical furnace, and drying, child heating, baking, and cooling zones are provided in the furnace.While the former is a countercurrent type, the present invention is a countercurrent type, mainly cocurrent flow. The firing furnace has a tapered structure with a small diameter at the top and a large diameter at the bottom to prevent the formation of bridges.

取出にはロータリテーブルでなくて取出量が調節可能で
あるスクリュ式取出手段を設け被焼成原料は自重により
供給される構造である。〔発明の構成〕 本発明に係る磁性酸化鉄の仮焼成炉をその実施例を示し
た第1図によって説明する。
For taking out, instead of a rotary table, a screw type taking out means is provided which allows the amount taken out to be adjusted, and the raw material to be fired is fed by its own weight. [Configuration of the Invention] A magnetic iron oxide calcining furnace according to the present invention will be explained with reference to FIG. 1 showing an embodiment thereof.

この仮焼成炉はその高さが約ahであり、頂部内蓬が約
80cm、底部内径が160伽の戦頭円錐形である。
This calcining furnace has a height of about ah, a warhead conical shape with an inner diameter of about 80 cm at the top and an inner diameter of 160 cm at the bottom.

その内周壁は耐火材、保温材で充分に保護されている。
該炉の頂部に造粒された磁性酸化鉄の材料の供給手段2
を設ける。該供給手段2はたとえばホッパーと供給管と
で構成されており、炉内の材料が下方に降下すれば自重
によって自然に上方から下方へ落下し、逐次補給が行な
われる供給方式である。該炉1のほぼ中間の適当高さ位
置、すなわち約4肌の高さの位置5の内周壁に数基のガ
スバーナ8,8′…を設ける。
Its inner peripheral wall is well protected with fireproof and heat insulating materials.
Supply means 2 for granulated magnetic iron oxide material at the top of the furnace
will be established. The supply means 2 is composed of, for example, a hopper and a supply pipe, and is a supply system in which when the material in the furnace falls downward, it naturally falls from above to below due to its own weight, and is successively replenished. Several gas burners 8, 8', . . . are provided on the inner circumferential wall of the furnace 1 at a suitable height position approximately in the middle, that is, at a position 5 at a height of about four skins.

これらガスバーナ8はそれぞれガス燃料供給管】0と風
箱9を有し、その噴出端は耐熱構造である。位置5は水
柱約5物の正圧に保たれガスバーナ8,8′…から勢よ
く噴出される燃料と空気は炉中心部まで達する火炎を作
る。該炉1の下部の適当位置たとえば約2肌の高さ位置
6の内周壁にその吸引端を耐熱構造にして教本の吸入管
14,14′・・・を設ける。
Each of these gas burners 8 has a gas fuel supply pipe 0 and a wind box 9, and the ejection end thereof has a heat-resistant structure. Position 5 is maintained at a positive pressure of about 5 columns of water, and the fuel and air vigorously jetted out from gas burners 8, 8', . . . create a flame that reaches the center of the furnace. Suction pipes 14, 14', . . . are provided on the inner circumferential wall of the furnace 1 at a suitable position, for example, at a height of about 2 skins, at a height 6 of the furnace 1, with the suction ends of the suction pipes having a heat-resistant structure.

これら吸入管は環状管15でまとめられ、該環状管15
は調節弁16を有する送風機17のサクション管と連結
されている。該調節弁16を調節して炉内の位置6を水
柱約1仇肋の負圧に保たしめることができる。炉内の位
置6が水柱約1仇協の負圧であるために炉内の位置5に
吹込まれた火炎および高温燃焼ガスはとの大部分量が下
方に流れる。
These suction pipes are put together by an annular pipe 15, and the annular pipe 15
is connected to a suction pipe of a blower 17 having a regulating valve 16. The control valve 16 can be adjusted to maintain a negative pressure of about one column of water at location 6 within the furnace. Since location 6 in the furnace is under negative pressure of about 1 column of water, most of the flame and hot combustion gases blown into location 5 in the furnace flow downward.

高温燃焼ガスは降下する焼成される材料と並行に流れ、
位置5て位置6間においてたとえば1200つ0程度の
適温に保たれ、焼成反応が行なわれる。位置5と位置6
間は焼成ゾーンである。該炉1の底部近くの位置7の炉
周壁に数個の冷却用空気噴出孔11,11′・・・を設
ける。
The hot combustion gases flow parallel to the descending material to be fired,
The temperature between position 5 and position 6 is maintained at an appropriate temperature of, for example, about 1,200 degrees Celsius, and a calcination reaction is carried out. position 5 and position 6
In between is the firing zone. Several cooling air injection holes 11, 11', . . . are provided in the furnace peripheral wall at a position 7 near the bottom of the furnace 1.

これら冷却空気噴出孔11は環状管12と連結されてお
り、該環状管12は調節弁13を有する冷却用空気供給
管と連結されている。従って冷却用空気の適量が適量が
底部位置7から炉内へ吹込まれ、上方へ流れて焼成品と
熱交換をし高温の空気になった後に位置6の吸引管14
によって焼成ガスと共に炉外に取出される。位置6と位
置7の間は冷却ゾーンである。該炉1の上部適当位置た
とえば約6の高さ位置4の炉周囲に教本の噴出管19,
19′…を設ける。
These cooling air jet holes 11 are connected to an annular pipe 12, and the annular pipe 12 is connected to a cooling air supply pipe having a control valve 13. Therefore, an appropriate amount of cooling air is blown into the furnace from the bottom position 7, flows upward, exchanges heat with the fired product, becomes high-temperature air, and then enters the suction pipe 14 at position 6.
is taken out of the furnace along with the firing gas. Between positions 6 and 7 is a cooling zone. A textbook blowout pipe 19 is installed around the furnace at a suitable upper part of the furnace 1, for example, at a height position 4 of about 6.
19'... is provided.

これら噴出管19は環状管20と連結されており、該環
状管20はさきに述べた送風機17のデリベリ管18と
連結されている。従って噴出管19からは高温燃焼ガス
と高温になった空気との混合ガスが噴出される。位置4
は水柱約IW舷の正庄に保たれる。この位置4に可成高
温かつ可成の量の浪合ガスが噴出管19によって勢よく
噴出される。該炉1の頂部に近い位置すなわち該炉1の
約8肌の高さ位置3の炉周壁に教本の排出管21,21
′・・・を設ける。
These ejection pipes 19 are connected to an annular pipe 20, and the annular pipe 20 is connected to the delivery pipe 18 of the blower 17 mentioned above. Therefore, a mixed gas of high-temperature combustion gas and high-temperature air is ejected from the ejection pipe 19. position 4
is maintained at the front of the ship, approximately IW in the water column. At this position 4, a relatively high temperature and a considerable amount of mercury gas is vigorously jetted out by the jetting pipe 19. Textbook discharge pipes 21, 21 are installed on the furnace peripheral wall at a position near the top of the furnace 1, that is, at a position 3 at a height of about 8 skins of the furnace 1.
'... is provided.

これら排出管21は環状管22にまとめられ、該環状管
22は調節弁23を有する送風機24のサクション管と
連結されている。該調節弁23を調節して炉内の位置3
を水柱約20柵の負圧上に保たしめることができる。炉
内の位置3が水柱約2仇剛の負圧であり位置4は水柱約
1仇吻の正圧であるため位置41こおいて吹込まれた混
合ガスは活溌に材料層内を通って上昇し炉内の位置3に
至るまでに原料と熱交換をして可成低温になってから排
出管21によって排出される。
These discharge pipes 21 are combined into an annular pipe 22, which is connected to a suction pipe of a blower 24 having a regulating valve 23. Adjust the control valve 23 to set position 3 in the furnace.
can be maintained above a negative pressure of about 20 bars of water. Since position 3 in the furnace has a negative pressure of approximately 2 mm water column and position 4 has a positive pressure of approximately 1 mm water column, the mixed gas injected at position 41 actively rises through the material layer. By the time it reaches position 3 in the furnace, it exchanges heat with the raw material and reaches a fairly low temperature before being discharged through the discharge pipe 21.

材料は位置3から位置4に至るまでに充分乾燥され、充
分子熱される。
The material is sufficiently dried and heated sufficiently from position 3 to position 4.

位置3から位置4間は乾燥ゾーンであり、位置4から位
置5間は予熱ゾーンである。該炉1の底部に生成品の取
出手段26を設ける。
The area between positions 3 and 4 is a drying zone, and the area between positions 4 and 5 is a preheating zone. A product removal means 26 is provided at the bottom of the furnace 1.

該取出手段26はたとえばスクリュコンベャであって、
すでに焼成され、かつ冷却用空気によって可成低温に冷
却された仮焼成の磁性酸化鉄を連続的に恒量づつ取出す
ことができる。またこの敬出によって炉内原料の降下と
炉頂部の供給手段2からの原材料の自重落下による供給
が行なわれ、これら材料の自動供給と自動落下は該焼成
炉1がさき‘こ述べた程度のテーパーであるため、かつ
3ケ所の噴出2ケ所の吸引を設けて炉内を活溌化させて
いるため、ブリッジを生ぜしめることなく円滑な降下が
行なわれ、かつ所望の焼成を行うことができる。バーナ
8による火炎の噴射と噴出管19による混合ガスの吹込
みは、それぞれ位置5および位置4の炉内圧力がそれぞ
れ水柱IQ肌と水柱5柳となるように勢よく噴出させ、
これら噴出はいづれも炉中心部にまで達せしめることが
できる。第2図は第1図の磁性酸化鉄の仮焼成炉におけ
る炉内各位層における圧力と炉内における気流の流れを
示し、第3図は第1図の磁性酸化鉄の仮焼成炉内の温度
分布を示す。
The take-out means 26 is, for example, a screw conveyor,
It is possible to continuously take out a constant amount of pre-fired magnetic iron oxide that has already been fired and cooled to a reasonably low temperature by cooling air. In addition, due to this ejection, the raw materials are lowered into the furnace and the raw materials are supplied by their own weight falling from the supply means 2 at the top of the furnace, and the automatic supply and automatic fall of these materials are carried out to the extent that the firing furnace 1 is as described above. Because it is tapered, and because the inside of the furnace is activated by providing suction at three locations and two locations, it is possible to descend smoothly without causing bridging, and to perform the desired firing. The injection of the flame by the burner 8 and the injection of the mixed gas by the ejection pipe 19 are performed so that the pressure in the furnace at the positions 5 and 4 becomes the water column IQ skin and the water column 5 willow, respectively.
All of these jets can reach the center of the furnace. Figure 2 shows the pressure in each layer in the furnace and the air flow in the furnace in the calcining furnace for magnetic iron oxide in Figure 1, and Figure 3 shows the temperature in the calcining furnace for magnetic iron oxide in Figure 1. Show the distribution.

第3図のグラフは縦軸に炉の高さをとり、横軸に炉内の
温度をとり仮焼成炉内の各高さの温度を示している。こ
のグラフにおいて位置3から位置4までの間は乾燥ゾー
ンであり、位置4から位置5までの間は子熱・昇温ゾー
ンであり、位置5から位置6までの間は焼成反応ゾーン
であり、本発明の炉および焼成方法においては焼成温度
をこのゾーンにおいてほぼ1200℃の一定温度に保ち
従って完全に焼成反応が行なわれる。位置6から位置7
までの間は冷却ゾーンである。〔発明の効果〕 本発明の焼成方法および焼成炉においては比較的少量の
ガス燃料で焼成を行うことができ、熱エネルギーが有効
に使用されて燃料費を大幅に節約することができる。
In the graph of FIG. 3, the vertical axis represents the height of the furnace, and the horizontal axis represents the temperature inside the furnace, indicating the temperature at each height within the pre-calcination furnace. In this graph, the area from position 3 to position 4 is the drying zone, the area from position 4 to position 5 is the child heating/heating zone, and the area from position 5 to position 6 is the firing reaction zone. In the furnace and firing method of the present invention, the firing temperature is maintained at a constant temperature of approximately 1200° C. in this zone, so that the firing reaction takes place completely. position 6 to position 7
This is a cooling zone. [Effects of the Invention] In the firing method and firing furnace of the present invention, firing can be performed with a relatively small amount of gas fuel, thermal energy is used effectively, and fuel costs can be significantly reduced.

また炉内を降下する材料の速度を取出手段の速度調節に
より容易に調節することができる。なは炉内の各高さに
おける温度と圧力は各論節弁によって容易に調節するこ
とができる。以上は磁性酸化鉄であるバリウムフェライ
ト母○餌e203の約12側めの造粒を原料としこれを
仮暁する堅型炉について述べたのであるが、本発明の堅
型炉は石炭粒から石炭ガスの乾溜をする乾溜炉として使
用することができ、石灰岩の焼成セメントの製造に使用
することも、またその他の用途にも応用することができ
る。
Furthermore, the speed of the material descending within the furnace can be easily adjusted by adjusting the speed of the removal means. The temperature and pressure at each height in the furnace can be easily adjusted by each control valve. The above has described a vertical furnace that uses as a raw material the granules of about 12 sides of barium ferrite matrix feed e203, which is magnetic iron oxide, and freezes it. It can be used as a dry distillation furnace for dry distillation of gas, and can also be used for producing calcined limestone cement, as well as for other uses.

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

第1図は本発明に係る磁性酸化鉄の仮焼成炉を示す縦断
面図である。 第2図は第1図に示す仮焼成炉において、炉内の圧力お
よび炉内気体の流れを示し、第3図は第1図に示す仮焼
成炉において炉内の温度分布を示したグラフである。1
は磁性酸化鉄の仮焼成炉、2は供給手段、3は炉頂に近
い擬ガス取出位置、4は燃焼ガスと空気の混合ガスの吹
込位置、5はガスバーナの取付位置6は吸引管取付装置
、7は冷却用空気吹込位置、8はバ−ナ、9は風箱、1
0はガス燃料供給管、11‘ま冷却用空気噴出孔、12
は環状管、13は調節弁、14は吸引管、15は環状管
、16は調節弁、17は送風機、18はデリベリ管、1
9は混合ガス噴出管、20は環状管、21は排出管、2
2は環状管、23は調節弁、24は送風機、25はデリ
ベリ管、26は取出手段。 第「図 家2図 第3図
FIG. 1 is a longitudinal cross-sectional view showing a temporary firing furnace for magnetic iron oxide according to the present invention. Figure 2 is a graph showing the pressure in the furnace and the flow of gas in the furnace in the calcining furnace shown in Figure 1, and Figure 3 is a graph showing the temperature distribution in the furnace in the calcining furnace shown in Figure 1. be. 1
2 is a temporary firing furnace for magnetic iron oxide, 2 is a supply means, 3 is a pseudo gas extraction position near the top of the furnace, 4 is a blowing position for a mixture of combustion gas and air, 5 is a gas burner mounting position, and 6 is a suction pipe mounting device. , 7 is the cooling air blowing position, 8 is the burner, 9 is the wind box, 1
0 is a gas fuel supply pipe, 11' is a cooling air outlet, 12 is
1 is an annular pipe, 13 is a control valve, 14 is a suction pipe, 15 is an annular pipe, 16 is a control valve, 17 is a blower, 18 is a delivery pipe, 1
9 is a mixed gas ejection pipe, 20 is an annular pipe, 21 is a discharge pipe, 2
2 is an annular pipe, 23 is a control valve, 24 is a blower, 25 is a delivery pipe, and 26 is a take-out means. Figure 2 Figure 3

Claims (1)

【特許請求の範囲】 1 炉内径が上部から下部に至るほど大である堅型炉1
を用い、該炉の中間の適当位置5の炉周壁に設けた数基
のガスバーナ8,8′…による火炎と燃焼ガスの大部分
量を被焼成材料の進向方向と同一方向である下方の負圧
部位置6方向へ流して位置5から6に至る間において被
焼成材料の焼成が行なわれるようにし、該炉の底部近く
の位置7の炉周壁に設けた数個の冷却用空気噴出孔11
,11′…による冷却用空気流を上方の負圧部位置6方
向へ流して位置6から位置7に至る間において焼成され
た材料の冷却が行なわれるようにし、位置6の炉周壁に
数本の吸引管14,14′…を設けてこれら吸引管で吸
引した燃焼ガスと空気の混合ガスを位置5と頂部近くの
位置3の中間高さ位置4の炉周壁に設けた数本の混合ガ
ス噴出管19,19′…から噴出させ、位置3の炉周壁
に数本の排出管21,21′…を設けてこれら排出管で
気体の吸引をして負圧部を作って位置4附近において頂
部から供給された被焼成材料の乾燥と予熱が行なわれる
ようにし、炉底に設けた取出手段26によって焼成品を
取出すことによって炉頂に設けた供給手段2から材料が
自重により逐次補給されるようにした焼成方法。 2 炉内径が上部から下部に至るほど大である堅型炉1
を設け、該炉1の頂部に焼成すべき材料の供給手段2を
設け、該炉1の中間の適当高さ位置5の炉周壁に数基の
ガスバーナ8,8′…を設け、該炉1の底部近くの位置
7の炉周壁に数個の冷却用空気噴出孔11,11′…を
設け、位置5と位置7の中間高さ位置6の炉周壁に燃焼
ガスと空気を吸引する数本の吸引管14,14…を設け
、該炉のバーナ位置5と頂部近くの位置3の中間高さ位
置4の炉周壁に数本の混合ガス噴出管19,19′…を
設け、該炉の頂部近くの位置3の炉周壁に数本の排出管
21,21′…を設け、該炉1の底部に焼成物の取出手
段26を設けた焼成炉。
[Claims] 1. A vertical furnace 1 in which the inner diameter of the furnace increases from the top to the bottom.
The majority of the flame and combustion gas from several gas burners 8, 8'... installed on the peripheral wall of the furnace at an appropriate position 5 in the middle of the furnace is directed downward in the same direction as the advancing direction of the material to be fired. The material to be fired is sintered between positions 5 and 6 by flowing in the direction of the negative pressure section position 6, and several cooling air jet holes are provided in the furnace peripheral wall at position 7 near the bottom of the furnace. 11
, 11'... are caused to flow upward toward the negative pressure section position 6 to cool the fired material from position 6 to position 7. Suction pipes 14, 14', etc. are provided, and the mixed gas of combustion gas and air sucked by these suction pipes is transferred to several mixed gas pipes installed on the furnace peripheral wall at position 5 and position 4 at an intermediate height between position 3 near the top. Gas is ejected from the ejection pipes 19, 19'..., and several exhaust pipes 21, 21'... are provided on the furnace peripheral wall at position 3, and the gas is sucked through these exhaust pipes to create a negative pressure section, and the gas is discharged near position 4. The material to be fired fed from the top is dried and preheated, and the fired product is taken out by the take-out means 26 provided at the bottom of the furnace, so that the material is successively replenished by its own weight from the supply means 2 provided at the top of the furnace. This is the firing method. 2 Vertical furnace 1 whose inner diameter is large from the top to the bottom
A supply means 2 for the material to be fired is provided at the top of the furnace 1, and several gas burners 8, 8'... are provided on the furnace peripheral wall at a suitable height position 5 in the middle of the furnace 1. Several cooling air jet holes 11, 11'... are provided on the furnace peripheral wall at position 7 near the bottom of the furnace, and several cooling air jet holes 11, 11'... are provided on the furnace peripheral wall at position 6, which is at an intermediate height between positions 5 and 7, to suck combustion gas and air. Several mixed gas ejection pipes 19, 19'... are provided on the furnace peripheral wall at an intermediate height position 4 between the burner position 5 and the position 3 near the top of the furnace. A firing furnace is provided with several discharge pipes 21, 21', .
JP12120982A 1982-07-14 1982-07-14 Firing method and furnace Expired JPS606692B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12120982A JPS606692B2 (en) 1982-07-14 1982-07-14 Firing method and furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12120982A JPS606692B2 (en) 1982-07-14 1982-07-14 Firing method and furnace

Publications (2)

Publication Number Publication Date
JPS5912745A JPS5912745A (en) 1984-01-23
JPS606692B2 true JPS606692B2 (en) 1985-02-20

Family

ID=14805571

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12120982A Expired JPS606692B2 (en) 1982-07-14 1982-07-14 Firing method and furnace

Country Status (1)

Country Link
JP (1) JPS606692B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61216728A (en) * 1985-03-20 1986-09-26 Murata Mfg Co Ltd Vertical ceramics calcinator
DE102018133362A1 (en) * 2018-12-21 2020-06-25 Eisenmann Se Injection device for dispensing a gas, process gas system for supplying a process gas, and device and method for the thermal or thermo-chemical treatment of material

Also Published As

Publication number Publication date
JPS5912745A (en) 1984-01-23

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