JP5594812B2 - Rotary hearth furnace and operating method thereof - Google Patents

Rotary hearth furnace and operating method thereof Download PDF

Info

Publication number
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
Authority
JP
Japan
Prior art keywords
rotary hearth
fixed wall
outer peripheral
peripheral surface
inner peripheral
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.)
Active
Application number
JP2009074514A
Other languages
Japanese (ja)
Other versions
JP2010223556A (en
Inventor
真司 嶋
俊孝 中山
彦文 谷石
親司朗 内田
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.)
Nippon Steel Engineering Co Ltd
Original Assignee
Nippon Steel Engineering 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 Nippon Steel Engineering Co Ltd filed Critical Nippon Steel Engineering Co Ltd
Priority to JP2009074514A priority Critical patent/JP5594812B2/en
Publication of JP2010223556A publication Critical patent/JP2010223556A/en
Application granted granted Critical
Publication of JP5594812B2 publication Critical patent/JP5594812B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Manufacture Of Iron (AREA)
  • 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 Patent Document 1, a rotary hearth furnace for producing reduced iron from iron oxide-containing raw materials such as iron ore and ironmaking waste has been put into practical use for a long time. The rotary hearth furnace includes an annular rotary hearth, an outer peripheral fixed wall disposed along the outer peripheral surface of the rotary hearth, an inner peripheral fixed wall disposed along the inner peripheral surface of the rotary hearth, Is provided. The gap between the outer peripheral surface and inner peripheral surface of the rotary hearth and the outer peripheral fixed wall and inner peripheral fixed wall around it is sealed by water-sealing the seal plates 11 disposed on both sides as shown in FIG. In this structure, the atmosphere outside the furnace is sucked into the furnace and the gas inside the furnace is prevented from leaking out of the furnace.

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 (symbol 12 in FIG. 2) grows with long-term operation, and eventually clogs the gap between each peripheral surface of the rotary hearth and each fixed wall, causing rotation failure of the rotary hearth. It was. Moreover, a great deal of labor was required for the deposit removal work performed when the furnace was stopped.

特公昭45−19569号公報Japanese Patent Publication No. 45-19569

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.

本発明の回転炉床炉の実施形態を示し、(a)はその平面透視による概略図、(b)は(a)のA−A断面図であって加熱手段の一例を示し、(c)は(a)のA−A断面図であって加熱手段の他の例を示す。Embodiment of the rotary hearth furnace of this invention is shown, (a) is the schematic by the plane perspective, (b) is AA sectional drawing of (a), and shows an example of a heating means, (c) [FIG. 4] It is AA sectional drawing of (a), Comprising: Another example of a heating means is shown. 従来の回転炉床炉における回転炉床の外周面と外周固定壁の隙間部分の構成を示す断面図である。It is sectional drawing which shows the structure of the clearance gap part of the outer peripheral surface of a rotary hearth, and an outer peripheral fixed wall in the conventional rotary hearth furnace.

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 rotary hearth 1, an outer peripheral fixed wall 2 arranged along the outer peripheral surface of the rotary hearth 1, and an inner circumference arranged along the inner peripheral surface of the rotary hearth 1. And a fixed wall 3. The iron oxide-containing raw material is supplied onto the rotary hearth 1 by the raw material supply device 4. In the embodiment, the rotary hearth 1 rotates clockwise, and while the rotary hearth 1 rotates, the iron oxide-containing raw material is reduced to become reduced iron and is discharged out of the furnace by the reduced iron discharge device 5.

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 rotary hearth 1 and the outer peripheral fixed wall 2 and the gap between the inner peripheral surface of the rotary hearth 1 and the inner peripheral fixed wall 3, heating means 6 for heating the respective gaps, Eight points are provided at equal intervals in the circumferential direction of each gap.

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 burner 6a and a hot air blowing device 6b can be arranged. 1B and 1C show the heating means on the outer peripheral fixed wall 2 side, the cooling means on the inner peripheral fixed wall 2 side can also have the same configuration.

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 rotary hearth 1 in rotation, and region C is the middle of the cart. It is an area below the height.

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.

Figure 0005594812
Figure 0005594812

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
DESCRIPTION OF SYMBOLS 1 Rotary hearth 2 Outer peripheral fixed wall 3 Inner peripheral fixed wall 4 Raw material supply apparatus 5 Reduced iron discharge apparatus 6 Heating means 6a Burner 6b Hot air blowing apparatus 11 Seal plate 12 Deposit

Claims (5)

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回転炉床炉。 In a rotary hearth furnace comprising an annular rotary hearth, an outer peripheral fixed wall disposed along the outer peripheral surface of the rotary hearth, and an inner peripheral fixed wall disposed along the inner peripheral surface of the rotary hearth The 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 is provided over the entire circumference below the respective gaps. Rotating hearth furnace. 加熱手段が、前記各隙間の下方に配置したバーナ又は熱風吹き込み装置である請求項1に記載の回転炉床炉。   The rotary hearth furnace according to claim 1, wherein the heating means is a burner or a hot air blowing device disposed below each of the gaps. 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の操業方法において、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回転炉床炉の操業方法。   A rotary hearth furnace comprising an annular rotary hearth, an outer peripheral fixed wall disposed along the outer peripheral surface of the rotary hearth, and an inner peripheral fixed wall disposed along the inner peripheral surface of the rotary hearth In the operation method, combustion gas or hot air is blown in from the lower part of the clearance between the outer peripheral surface of the rotary hearth and the outer peripheral fixed wall and the lower surface of the inner peripheral surface of the rotary hearth and the inner peripheral fixed wall over the entire periphery of each of the clearances. A method for operating a rotary hearth furnace. 前記燃焼ガス又は熱風の温度を900℃以上とする請求項に記載の回転炉床炉の操業方法。 The operating method of the rotary hearth furnace of Claim 3 which makes the temperature of the said combustion gas or a hot air 900 degreeC or more. 前記燃焼ガス又は熱風の流速を0.7m/s以上とする請求項3又は4に記載の回転炉床炉の操業方法。 The operation method of a rotary hearth furnace according to claim 3 or 4 , wherein a flow velocity of the combustion gas or hot air is 0.7 m / s or more.
JP2009074514A 2009-03-25 2009-03-25 Rotary hearth furnace and operating method thereof Active JP5594812B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009074514A JP5594812B2 (en) 2009-03-25 2009-03-25 Rotary hearth furnace and operating method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009074514A JP5594812B2 (en) 2009-03-25 2009-03-25 Rotary hearth furnace and operating method thereof

Publications (2)

Publication Number Publication Date
JP2010223556A JP2010223556A (en) 2010-10-07
JP5594812B2 true JP5594812B2 (en) 2014-09-24

Family

ID=43040925

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009074514A Active JP5594812B2 (en) 2009-03-25 2009-03-25 Rotary hearth furnace and operating method thereof

Country Status (1)

Country Link
JP (1) JP5594812B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5882139B2 (en) * 2012-06-08 2016-03-09 新日鉄住金エンジニアリング株式会社 Rotary hearth furnace and operating method thereof

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001240908A (en) * 2000-02-29 2001-09-04 Kobe Steel Ltd Method for operating rotary hearth furnace for producing reduced iron
JP2002167622A (en) * 2000-11-27 2002-06-11 Nippon Steel Corp Method for producing reduced iron agglomerated product
JP2004315852A (en) * 2003-04-11 2004-11-11 Nippon Steel Corp Method for reducing metal oxide in rotary hearth type reduction furnace
JP2008215649A (en) * 2007-02-28 2008-09-18 Sumitomo Heavy Ind Ltd Rotary kiln furnace and operation method for it

Also Published As

Publication number Publication date
JP2010223556A (en) 2010-10-07

Similar Documents

Publication Publication Date Title
EP2861771B1 (en) Device for recovering heat and fumes from slag resulting from the steel production cycle
JP2016094630A (en) Sintered ore cooling device
JP2001288504A (en) Method for producing molten metallic iron
CN106544639B (en) It prevents the gas extraction arrangement of blocking and the MOCVD device of the device is set
JP5594812B2 (en) Rotary hearth furnace and operating method thereof
JP5384226B2 (en) Hot air heating device
TWI684740B (en) Cooler for cooling hot bulk material and use of such a cooler
CN203798173U (en) Exhaust device
US2980412A (en) Rotary furnace
JP2007285683A (en) Rotary kiln
JP2010223555A (en) Rotary hearth furnace
CN106091680A (en) A kind of rotary hearth furnace
JP2010223557A (en) Rotary hearth furnace
CN205919669U (en) Rotary hearth furnace
CN103966466A (en) Water-cooled furnace cover for titanium slag electric furnace
JP2015108474A (en) Rotary kiln
CN109307427A (en) A kind of double horn mouth formula shaft furnace kiln bottom discharge bucket structure and its working method
RU2013114443A (en) GAS FLOW DEVICE FOR WASTE GAS OVENS WITH ROTATING BURNERS AND METHOD OF OPERATION
CN206204389U (en) A kind of environment-friendly type blast furnace processes cupro-nickel device of sludge
KR200195870Y1 (en) Device for coating prevent of roater kiln
CN209276677U (en) A kind of ingot furnace
JP5494990B2 (en) Automatic dissolution apparatus for dry assay samples
JP2017075710A (en) Sintered ore cooling device
SU954761A1 (en) Cup-type cooler for lumpy materials
JP2010286172A (en) Heating furnace

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20111109

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130926

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20131001

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20140708

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20140801

R150 Certificate of patent or registration of utility model

Ref document number: 5594812

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313121

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350