JP5594812B2 - Rotary hearth furnace and operating method thereof - Google Patents
Rotary hearth furnace and operating method thereof Download PDFInfo
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- JP5594812B2 JP5594812B2 JP2009074514A JP2009074514A JP5594812B2 JP 5594812 B2 JP5594812 B2 JP 5594812B2 JP 2009074514 A JP2009074514 A JP 2009074514A JP 2009074514 A JP2009074514 A JP 2009074514A JP 5594812 B2 JP5594812 B2 JP 5594812B2
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- 238000011017 operating method Methods 0.000 title claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 62
- 238000010438 heat treatment Methods 0.000 claims description 27
- 238000007664 blowing Methods 0.000 claims description 9
- 239000000567 combustion gas Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 4
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 10
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 10
- 239000011701 zinc Substances 0.000 description 10
- 229910052725 zinc Inorganic materials 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 9
- 239000002994 raw material Substances 0.000 description 7
- 238000001556 precipitation Methods 0.000 description 5
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000011787 zinc oxide Substances 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Tunnel Furnaces (AREA)
Description
本発明は、主として、鉄鉱石、製鉄廃棄物等の酸化鉄含有原料から、還元鉄を製造する回転炉床炉及びその操業方法に関する。 The present invention mainly relates to a rotary hearth furnace for producing reduced iron from an iron oxide-containing raw material such as iron ore and ironmaking waste and an operating method thereof.
例えば特許文献1に開示されているように、古くから、鉄鉱石、製鉄廃棄物等の酸化鉄含有原料から、還元鉄を製造する回転炉床炉が実用化されている。この回転炉床炉は、円環状の回転炉床と、回転炉床の外周面に沿って配置された外周固定壁と、回転炉床の内周面に沿って配置された内周固定壁とを備える。そして、回転炉床の外周面及び内周面とその周りの外周固定壁及び内周固定壁の隙間は、図2に示すように双方に配せられたシールプレート11を水封することで密封され、炉外の大気を炉内に吸引したり、炉内のガスが炉外に漏洩したりすることを防ぐ構造になっている。
For example, as disclosed in
ところが、とくに製鉄所で発生する製鉄廃棄物には酸化亜鉛等の不純物が含まれており、酸化亜鉛を含む酸化鉄含有原料を回転炉床炉で処理すると、炉内に満ちた気化亜鉛が回転炉床の各周面と各固定壁の隙間に侵入した際、水封部の冷輻射により冷やされ固体として析出し、回転炉床の各周面や各固定壁に付着することが避けられなかった。この付着物(図2の符号12)は長期運転に伴い成長し、最終的には回転炉床の各周面と各固定壁の隙間を閉塞させ、回転炉床の回転障害をもたらす原因となっていた。また炉休止時に行われる、付着物除去作業には多大な労力が必要であった。
However, the ironmaking waste generated at steelworks contains impurities such as zinc oxide. When iron oxide-containing raw materials containing zinc oxide are processed in a rotary hearth furnace, zinc vapor filled in the furnace rotates. When entering the gap between each peripheral surface of the hearth and each fixed wall, it is unavoidably deposited as a solid that is cooled by the cold radiation of the water seal and adheres to each peripheral surface and each fixed wall of the rotary hearth. It was. This deposit (
本発明が解決しようとする課題は、回転炉床の外周面及び内周面やその周りの外周固定壁及び内周固定壁に気化亜鉛等の析出物が付着することを防止できる回転炉床炉及びその操業方法を提供することにある。 A problem to be solved by the present invention is a rotary hearth furnace capable of preventing deposits of vaporized zinc and the like from adhering to the outer peripheral surface and inner peripheral surface of the rotary hearth and the outer peripheral fixed wall and inner peripheral fixed wall around the outer peripheral surface and inner peripheral surface. And providing an operation method thereof.
本発明の回転炉床炉は、円環状の回転炉床と、回転炉床の外周面に沿って配置された外周固定壁と、回転炉床の内周面に沿って配置された内周固定壁とを備える回転炉床炉において、回転炉床の外周面と外周固定壁の隙間、及び回転炉床の内周面と内周固定壁の隙間を加熱する加熱手段を、前記各隙間の下方の全周にわたって設けたことを特徴とするものである。 The rotary hearth furnace of the present invention includes an annular rotary hearth, an outer peripheral fixed wall disposed along the outer peripheral surface of the rotary hearth, and an inner peripheral fixed disposed along the inner peripheral surface of the rotary hearth. In a rotary hearth furnace comprising a wall, heating means for heating the gap between the outer peripheral surface of the rotary hearth and the outer peripheral fixed wall, and the gap between the inner peripheral surface of the rotary hearth and the inner peripheral fixed wall, It is characterized by being provided over the entire circumference .
このように、加熱手段によって前記各隙間を加熱することで、炉内の気化亜鉛等が前記各隙間で冷やされて析出し回転炉床の外周面及び内周面やその周りの外周固定壁及び内周固定壁に付着することを防止できる。 In this way, by heating the gaps by the heating means, the vaporized zinc in the furnace is cooled and precipitated in the gaps, and the outer peripheral surface and inner peripheral surface of the rotary hearth and the outer peripheral fixed wall around it and It can prevent adhering to the inner peripheral fixed wall.
本発明において、加熱手段は前記各隙間の下方の全周にわたって設ける。すなわち、加熱手段を前記各隙間の全周にわたって設けることで、前記各隙間の全周を加熱することができるので、気化亜鉛等の析出及び付着をより確実に防止できる。さらに、加熱手段を前記各隙間の下方に設けることで、前記各隙間に高温の上昇気流が生じるので、炉内の気化亜鉛等が前記各隙間に侵入しにくくなり、その析出及び付着を防止できる。 In this invention, a heating means is provided over the perimeter below each said clearance gap . That is, by providing the heating means over the entire circumference of each gap, the entire circumference of each gap can be heated, so that precipitation and adhesion of vaporized zinc and the like can be prevented more reliably. Furthermore, by providing a heating means below each of the gaps, a high temperature rising air flow is generated in each of the gaps, so that it is difficult for zinc vapor or the like in the furnace to enter each of the gaps, and precipitation and adhesion thereof can be prevented. .
このような加熱手段としては、バーナ又は熱風吹き込み装置を使用することができる。 As such a heating means, a burner or a hot air blowing device can be used.
また、本発明の回転炉床炉の操業方法は、前記各隙間の下方から上向きに燃焼ガス又は熱風を前記各隙間の全周にわたって吹き込むことを特徴とするものである。これによって、前記各隙間の全周が加熱されると共に、前記各隙間の全周にわたって上昇気流が生じるので、気化亜鉛等の析出及び付着を防止できる。 Moreover, the operating method of the rotary hearth furnace of the present invention is characterized in that combustion gas or hot air is blown upward from the lower side of each gap over the entire circumference of each gap. Accordingly, the entire circumference of each gap is heated and an updraft is generated over the whole circumference of each gap, so that precipitation and adhesion of zinc vaporized or the like can be prevented.
この場合、燃焼ガス又は熱風の温度は900℃以上とすることが好ましい。その温度を900℃以上とすることで、とくに問題となる気化亜鉛の析出をより確実に防止することができる。燃焼ガス又は熱風の温度にとくに上限はないが、現実的には1350℃程度が上限である。 In this case, the temperature of the combustion gas or hot air is preferably 900 ° C. or higher. By setting the temperature at 900 ° C. or higher, it is possible to more reliably prevent particularly problematic zinc vapor deposition. There is no particular upper limit to the temperature of the combustion gas or hot air, but in reality, the upper limit is about 1350 ° C.
また、燃焼ガス又は熱風の流速は0.7m/s以上とすることが好ましい。本発明者の実験によると、その流速を0.7m/s以上とすることで、十分な上昇気流が生成して気化亜鉛等の析出及び付着防止の効果が向上することが確認されている。燃焼ガス又は熱風の流速にとくに上限はないが、流速を4m/sより速くしても効果は飽和するので、この点からは5m/sを上限と考えることができる。 Moreover, it is preferable that the flow velocity of combustion gas or hot air shall be 0.7 m / s or more. According to the experiment by the present inventor, it has been confirmed that by setting the flow rate to 0.7 m / s or more, a sufficient ascending airflow is generated and the effect of preventing precipitation and adhesion of zinc vapor or the like is improved. There is no particular upper limit to the flow velocity of the combustion gas or hot air, but even if the flow velocity is made higher than 4 m / s, the effect is saturated. From this point, 5 m / s can be considered as the upper limit.
なお、本発明において、加熱手段を前記各隙間の全周にわたって設けるとは、加熱手段を前記各隙間の全周の全てに連続して設けることのほか、加熱手段を前記各隙間の周方向に沿ってほぼ均等な間隔で複数設けることも含むものである。同様に、燃焼空気又は熱風を前記各隙間の全周にわたって吹き込むとは、燃焼空気又は熱風を前記各隙間の全周の全ての箇所に吹き込むことのほか、燃焼空気又は熱風を前記各隙間の周方向のほぼ均等な間隔の複数箇所に吹き込むことも含むものである。 In the present invention, providing the heating means over the entire circumference of each gap means that the heating means is provided continuously over the entire circumference of each gap, and the heating means is provided in the circumferential direction of each gap. It also includes providing a plurality at substantially equal intervals along the line. Similarly, blowing the combustion air or hot air over the entire circumference of each gap means that the combustion air or hot air is blown into all parts of the circumference of each gap and the combustion air or hot air is blown around the gap. It includes blowing into a plurality of locations at substantially equal intervals in the direction.
本発明によれば、回転炉床の外周面及び内周面やその周りの外周固定壁及び内周固定壁に気化亜鉛等の析出物が付着することを防止できる。したがって、付着物の成長による回転炉床の回転障害をなくすことができ、また従来、炉休止時に行っていた付着物除去作業を行う必要もなくなる。 ADVANTAGE OF THE INVENTION According to this invention, it can prevent that deposits, such as zinc vapor, adhere to the outer peripheral surface and inner peripheral surface of a rotary hearth, the outer peripheral fixed wall around it, and an inner peripheral fixed wall. Therefore, the rotation obstacle of the rotary hearth due to the growth of deposits can be eliminated, and it is not necessary to perform the deposit removal operation that has been conventionally performed when the furnace is stopped.
以下、図面を参照して本発明の実施の形態を説明する。 Embodiments of the present invention will be described below with reference to the drawings.
図1(a)は本発明の回転炉床炉の実施形態を示す平面透視による概略図である。回転炉床炉は、円環状の回転炉床1と、回転炉床1の外周面に沿って配置された外周固定壁2と、回転炉床1の内周面に沿って配置された内周固定壁3とを備える。酸化鉄含有原料は、原料供給装置4によって回転炉床1の上に供給される。回転炉床1は実施例では時計回りに回転し、回転炉床1が回転する間に酸化鉄含有原料は還元されて還元鉄となり、還元鉄排出装置5によって炉外に排出される。
Fig.1 (a) is the schematic by planar seeing which shows embodiment of the rotary hearth furnace of this invention. The rotary hearth furnace includes an annular
回転炉床1の外周面と外周固定壁2の隙間、及び回転炉床1の内周面と内周固定壁3の隙間の下方には、前記各隙間を加熱するための加熱手段6が、前記各隙間の周方向において等間隔で8箇所に設けられている。
Below the gap between the outer peripheral surface of the
加熱手段6としては、図1(b)及び(c)に示すように、バーナ6aや熱風吹き込み装置6bを配置することができる。なお、図1(b)及び(c)では、外周固定壁2側の加熱手段を示したが、内周固定壁2側の冷却手段も同様の構成とすることができる。
As the heating means 6, as shown in FIGS. 1B and 1C, a
この加熱手段6によって、回転炉床炉の操業中に、前記各隙間の全周が加熱されると共に、前記各隙間の全周にわたって上昇気流が生じるので、気化亜鉛等の析出及び付着を防止できる。 The heating means 6 heats the entire circumference of each gap during the operation of the rotary hearth furnace, and an upward air flow is generated over the entire circumference of each gap, so that precipitation and adhesion of zinc vapor and the like can be prevented. .
なお、この実施形態では、加熱手段6を前記各隙間の周方向において等間隔で8箇所に設けたが、加熱手段6の設置数はこれに限定されるものではない。ただし、前記各隙間の全周をほぼ均一に加熱する点からは、加熱手段は、前記各隙間の周方向において等間隔で8〜50箇所に設けることが好ましい。 In this embodiment, the heating means 6 is provided at eight positions at equal intervals in the circumferential direction of each gap, but the number of the heating means 6 is not limited to this. However, from the viewpoint of heating the entire circumference of each gap substantially uniformly, it is preferable to provide the heating means at 8 to 50 locations at equal intervals in the circumferential direction of each gap.
無論、加熱手段は、前記各隙間に全周の全てに連続して設けることもできる。例えば図1(c)に示す熱風吹き込み装置6bにおいて熱風吹き出し口を前記各隙間の下方全周に連続して設けても良い。 Of course, the heating means can be provided continuously in all the circumferences in each gap. For example, in the hot air blowing device 6b shown in FIG. 1 (c), hot air blowing ports may be provided continuously all around the lower part of each gap.
図1(a)に示す本発明の回転炉床炉において加熱手段6として図1(c)の熱風吹き込み装置6bを使用し、この熱風吹き込み装置6bから前記各隙間に吹き込む熱風の流速を変化させ、前記各隙間近傍における付着物の状況を観察した。熱風の温度は1350℃とした。 In the rotary hearth furnace of the present invention shown in FIG. 1 (a), the hot air blowing device 6b shown in FIG. The state of deposits in the vicinity of each gap was observed. The temperature of the hot air was 1350 ° C.
付着物の状況は、領域A〜Cの3つの領域に分けて観察した。領域Aは回転炉床の上面より上方の領域、領域Bは回転炉床の上面より下方であって回転炉床1を回転支持する台車の中間高さより上方の領域、領域Cは前記台車の中間高さより下方の領域である。
The state of the deposit was observed by dividing it into three areas A to C. Region A is a region above the upper surface of the rotary hearth, region B is lower than the upper surface of the rotary hearth and above the intermediate height of the cart that supports the
各領域A〜Cにおける付着物の状況を表1に示す。表1に示すように、熱風の流速が0すなわち熱風を吹き込まなかった場合は領域A及びBにおいて強固な付着物が観察されたが、熱風を吹き込んだ場合は強固な付着物は観察されなかった。とくに、熱風の流速を0.7m/s以上にすると、領域B及びCにおいて付着物がなくなった。 Table 1 shows the state of deposits in each of the areas A to C. As shown in Table 1, when the flow rate of hot air was 0, that is, when hot air was not blown, strong deposits were observed in regions A and B, but when hot air was blown, no strong deposits were observed. . In particular, when the flow velocity of hot air was set to 0.7 m / s or more, deposits disappeared in the regions B and C.
1 回転炉床
2 外周固定壁
3 内周固定壁
4 原料供給装置
5 還元鉄排出装置
6 加熱手段
6a バーナ
6b 熱風吹き込み装置
11 シールプレート
12 付着物
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