JPS63130726A - Method and device for operating rotary kiln for reducing chromium ore - Google Patents
Method and device for operating rotary kiln for reducing chromium oreInfo
- Publication number
- JPS63130726A JPS63130726A JP27804486A JP27804486A JPS63130726A JP S63130726 A JPS63130726 A JP S63130726A JP 27804486 A JP27804486 A JP 27804486A JP 27804486 A JP27804486 A JP 27804486A JP S63130726 A JPS63130726 A JP S63130726A
- Authority
- JP
- Japan
- Prior art keywords
- rotary kiln
- chromium ore
- cooler
- hood
- pellets
- 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
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 229910052804 chromium Inorganic materials 0.000 title claims abstract description 25
- 239000011651 chromium Substances 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 9
- 239000002994 raw material Substances 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims 2
- 239000008188 pellet Substances 0.000 abstract description 16
- 238000010304 firing Methods 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract description 2
- 238000010405 reoxidation reaction Methods 0.000 abstract description 2
- 238000006722 reduction reaction Methods 0.000 description 16
- 239000007789 gas Substances 0.000 description 6
- 230000001590 oxidative effect Effects 0.000 description 5
- 239000003575 carbonaceous material Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 1
- 229910000423 chromium oxide Inorganic materials 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000011946 reduction process Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、クロム鉱石還元用ロータリーキルンの操業方
法およびその装置に関し、さらに詳しくは、ロータリー
キルンにおけるクロム鉱石の還元率を向上させるための
施策に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for operating a rotary kiln for reducing chromium ore, and more particularly to measures for improving the reduction rate of chromium ore in a rotary kiln.
ロータリーキルンな用いてクロム鉱石を還元するプロセ
スフローシートの一例を第2図に示した。An example of a process flow sheet for reducing chromium ore using a rotary kiln is shown in Figure 2.
クロムサンド等の粉粒状クロム鉱石は貯槽11からベル
トコンベヤ13を経て、他の材料槽12からの混合材料
と共に、造粒機14に装入され、適当な大きさ、例えば
15〜20mmに造粒される。Powdered chromium ore such as chromium sand is passed from the storage tank 11 to the belt conveyor 13, and is charged into the granulator 14 together with the mixed material from the other material tank 12, where it is granulated into an appropriate size, for example, 15 to 20 mm. be done.
造粒された鉱石はプレヒータ20内でグレートコンベヤ
21等によって搬送されながら乾燥加熱される。プレヒ
ータ20は教室に区画され各室からファンで22.23
.24で熱風を吸引する。The granulated ore is dried and heated within the preheater 20 while being conveyed by a grate conveyor 21 or the like. The preheater 20 is divided into classrooms and is connected by fans from each room.
.. 24 to suck the hot air.
プレヒータは例えば3室に分れており、ガス温度は第1
室200℃、第2室550’C1第3室tooo〜10
50℃のようになっている。これらのガスは電気集塵機
25、主吸引ファン26、煙突27を経て大気放散する
かまたは他の熱源として利用する。The preheater is divided into, for example, three chambers, and the gas temperature is
Room 200℃, 2nd room 550'C1 3rd room too~10
It's like 50 degrees Celsius. These gases are dissipated into the atmosphere through the electrostatic precipitator 25, the main suction fan 26, and the chimney 27, or are used as other heat sources.
プレヒータ20内で乾燥、加熱された原料は、ホッパ2
8からシュート29を経て供給された外装炭材と共にロ
ータリーキルン1に供給される。The raw material dried and heated in the preheater 20 is transferred to the hopper 2
8 to the rotary kiln 1 together with the exterior carbon material supplied via the chute 29.
ロータリーキルンlではバーナ2によって燃料を燃焼さ
せ、原料を1300〜1400’Cに加熱して還元する
。このときの目標還元率は例えばCr50%以上、Fe
85%以上となって(Xる。In the rotary kiln 1, fuel is combusted by the burner 2, and the raw material is heated to 1300 to 1400'C and reduced. The target reduction rate at this time is, for example, 50% or more for Cr, Fe
85% or more (X).
ロータリーキルンで加熱され、還元された還元ペレット
はフード3、シュート5を経てクーラ30に入り、ここ
で冷却され成品となる。The reduced pellets heated and reduced in the rotary kiln pass through a hood 3 and a chute 5 and enter a cooler 30, where they are cooled and turned into finished products.
以上のようなりロム鉱石の還元工程において、ロータリ
ーキルン1内でバーナによって加熱され還元されたクロ
ム鉱石はロータリーキルンから排出され、フード3を通
ってクーラ30に供給される。As described above, in the chromium ore reduction process, the chromium ore that has been heated and reduced by the burner in the rotary kiln 1 is discharged from the rotary kiln, and is supplied to the cooler 30 through the hood 3.
この場合第1図に示すように、ロータリーキルン1から
クロム鉱石還元ペレット4が排出される落ち口近傍やバ
ーナ焚口フード3内は、主/<−す2の主流流れのエジ
ェクタ効果や、温度によるシュート5内、フード3内上
昇流、フード3とキルンシェルとのシール部、クーラ3
0の入口シール部その他からの空気侵入およびクーラで
発生する多量の蒸気によって酸化性雰囲気となる。この
酸化性雰囲気のためにクロム鉱石ペレット4の還元が阻
害され、またその表面が酸化する。この酸化層は厚さが
薄くても、ペレット外表面の面積が大きい部分であるの
で、酸化量(容積)は大きくなり、還元率が著しく低下
する。In this case, as shown in Fig. 1, near the outlet where the chromium ore reduced pellets 4 are discharged from the rotary kiln 1 and inside the burner hood 3, the ejector effect of the mainstream flow of the main stream 2 and the chute due to temperature. 5, upward flow within hood 3, seal between hood 3 and kiln shell, cooler 3
An oxidizing atmosphere is created due to air intrusion from the inlet seal portion of the cooler and other places, and a large amount of steam generated in the cooler. This oxidizing atmosphere inhibits the reduction of the chromium ore pellets 4 and oxidizes their surfaces. Even if this oxidized layer is thin, since it is a large area of the outer surface of the pellet, the amount of oxidation (volume) becomes large and the reduction rate decreases significantly.
酸化クロムは本来難還元性であり、高温と還元雰囲気の
保持が重要である。なかでも、ロータリーキルンでは吸
い込まれる空気、あるいはクーラで発生する蒸気は酸化
性ガスであるためキルンあるいはプレヒータ内でペレッ
ト内装炭を消費し、還元に寄与する炭材量をへらしてし
まう。Chromium oxide is inherently difficult to reduce, so it is important to maintain a high temperature and a reducing atmosphere. In particular, in a rotary kiln, the air sucked in or the steam generated by the cooler is an oxidizing gas, which consumes the coal contained in the pellets in the kiln or preheater, reducing the amount of carbon material contributing to reduction.
このような還元率の低下を防止するには、■ 酸化雰囲
気を排除すること
■ 還元剤を多量に含有させておくこと■ 高温に保た
ないこと
などが考えられる。Possible ways to prevent such a decrease in the reduction rate are: (1) Eliminating the oxidizing atmosphere; (2) Containing a large amount of reducing agent; and (2) Not maintaining the temperature at high temperatures.
還元剤をペレット中に過分に含有させるとベレー2トの
強度が低下し粉化の原因となるので制限される。そこで
本発明は上記■に特に着目し、ロータリーキルン内への
空気漏風あるいはクーラで発生する多量の蒸気等のキル
ン内への吸込を防止する手段を提供し、クロム鉱石ペレ
ットの還元を促進し再酸化を防止し高還元率を維持する
ことを目的とする。If the reducing agent is contained in an excessive amount in the pellet, the strength of the beret will decrease and it will cause powdering, so it is limited. Therefore, the present invention focuses on the above-mentioned point (1) and provides a means to prevent air leakage into the rotary kiln or suction of a large amount of steam generated by the cooler into the rotary kiln, thereby promoting the reduction and reoxidation of the chromium ore pellets. The aim is to prevent this and maintain a high return rate.
本発明方法はロータリーキルンの原料装入側の気流を還
元雰囲気に保持し、クロム鉱石の還元率を向上させるこ
とを特徴とするクロム鉱石還元用ロータリーキルンの操
業方法である。またこの方法を好適に実施するための本
発明の装置は、第1図に示すように、ロータリーキルン
の焚口側フード3とクーラ30との接続部近傍あるいは
クーラ排出側に前記フード3内め空気を吸引する吸引フ
ァン7を接続することによって上記目的を達成するもの
である。The method of the present invention is a method of operating a rotary kiln for reducing chromium ore, which is characterized by maintaining the airflow on the raw material charging side of the rotary kiln in a reducing atmosphere to improve the reduction rate of chromium ore. Further, the apparatus of the present invention for suitably carrying out this method, as shown in FIG. The above object is achieved by connecting a suction fan 7 for suction.
本発明によれば、プレヒータやキルン内の低温部におい
て、クロム鉱石ペレットの中の炭材が消耗しないので、
還元反応域において炭材による還元が進行する。According to the present invention, the carbonaceous material in the chromium ore pellets is not consumed in the preheater or the low-temperature part of the kiln.
Reduction by the carbonaceous material progresses in the reduction reaction zone.
本発明の装置は、焚口フード3内の圧力をノくランスさ
せ、フード3の各隙間から吸引した多量の空気あるいは
クーラで発生する蒸気を吸引するので、キルンあるいは
プレヒータ内で内装炭が消費されるのを抑制し、もって
クロム鉱石ベレー/ トの還元率を高めることができる
。The device of the present invention releases the pressure inside the firing hood 3 and sucks in a large amount of air or steam generated by the cooler from each gap in the hood 3, so that the internal coal is not consumed in the kiln or preheater. The reduction rate of chromium ore berets can be increased.
クロム鉱石還元用ロータリーキルンの焚口側フードに吸
引ファンを取り付けて本発明を実施した。The present invention was carried out by attaching a suction fan to the hood on the firing side of a rotary kiln for reducing chromium ore.
第1表に実施前と実施後の諸元を比較して示した。Table 1 shows a comparison of the specifications before and after implementation.
フード内酸化性ガスを吸引することで、ツイード回りの
吸込空気は、キルン内に入ることなく、吸引ファンに引
っばられる。従って、キルン排ガス組成から計算で求め
られる推定吸込空気量が低下しており、排出ペレットの
還元率が向上する。By suctioning the oxidizing gas in the hood, the suction air around the tweed is drawn by the suction fan without entering the kiln. Therefore, the estimated intake air amount calculated from the kiln exhaust gas composition is reduced, and the reduction rate of the discharged pellets is improved.
但し、吸込空気量がOになる程度まで、吸引量を増すと
、同一還元率でコークス炉ガス燃焼量が増すため、得策
ではない。However, if the suction amount is increased to such an extent that the amount of suction air becomes O, the amount of coke oven gas burned will increase at the same reduction rate, which is not a good idea.
第1表から明らかなように、本発明装置を用いた本発明
方法の実施により、クロム鉱石ペレットの還元率の向上
を図ることができた。As is clear from Table 1, by implementing the method of the present invention using the apparatus of the present invention, it was possible to improve the reduction rate of chromium ore pellets.
本発明により、ロータリーキルンを用いる場合のクロム
鉱石ペレットの還元率が向上した。The present invention has improved the reduction rate of chromium ore pellets when using a rotary kiln.
第1図は本発明の実施例を示すキルンフード付近の断面
図、第2図はロータリーキルンを用いてクロム鉱石を還
元するプロセスフローシートである。
1・・・ロータリーキルン′
2・・・バーナ
3・・・焚口フード
4・・・クロム鉱石還元ペレット
5・・・シュート
7・・・吸引ファンFIG. 1 is a sectional view of the vicinity of a kiln hood showing an embodiment of the present invention, and FIG. 2 is a process flow sheet for reducing chromium ore using a rotary kiln. 1... Rotary kiln' 2... Burner 3... Burner hood 4... Chrome ore reduction pellets 5... Chute 7... Suction fan
Claims (1)
に保持し、クロム鉱石の還元率を向上させることを特徴
とするクロム鉱石還元用ロータリーキルンの操業方法。 2 ロータリーキルンに焚口フードを接続して成るクロ
ム鉱石還元用ロータリキルンにおいて、該焚口フードに
漏洩空気を吸引する吸引ファンを備えたことを特徴とす
るクロム鉱石還元用ロータリーキルン。[Claims] 1. A method for operating a rotary kiln for reducing chromium ore, characterized by maintaining the air flow on the raw material charging side of the rotary kiln in a reducing atmosphere to improve the reduction rate of chromium ore. 2. A rotary kiln for reducing chromium ore comprising a rotary kiln connected to a combustion chamber hood, characterized in that the combustion chamber hood is equipped with a suction fan for sucking leaked air.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27804486A JPS63130726A (en) | 1986-11-21 | 1986-11-21 | Method and device for operating rotary kiln for reducing chromium ore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27804486A JPS63130726A (en) | 1986-11-21 | 1986-11-21 | Method and device for operating rotary kiln for reducing chromium ore |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63130726A true JPS63130726A (en) | 1988-06-02 |
Family
ID=17591864
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27804486A Pending JPS63130726A (en) | 1986-11-21 | 1986-11-21 | Method and device for operating rotary kiln for reducing chromium ore |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63130726A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5815050A (en) * | 1981-07-16 | 1983-01-28 | 川崎重工業株式会社 | Apparatus for baking cement powder raw material or like |
JPS61272329A (en) * | 1985-05-23 | 1986-12-02 | サマンカー・リミテツド | Reduction of iron-containing chromium ore |
-
1986
- 1986-11-21 JP JP27804486A patent/JPS63130726A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5815050A (en) * | 1981-07-16 | 1983-01-28 | 川崎重工業株式会社 | Apparatus for baking cement powder raw material or like |
JPS61272329A (en) * | 1985-05-23 | 1986-12-02 | サマンカー・リミテツド | Reduction of iron-containing chromium ore |
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