JPH04191309A - Pre-reduction furnace in smelting reduction device for iron ore - Google Patents
Pre-reduction furnace in smelting reduction device for iron oreInfo
- Publication number
- JPH04191309A JPH04191309A JP32156890A JP32156890A JPH04191309A JP H04191309 A JPH04191309 A JP H04191309A JP 32156890 A JP32156890 A JP 32156890A JP 32156890 A JP32156890 A JP 32156890A JP H04191309 A JPH04191309 A JP H04191309A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- reduction
- gas supplying
- plate
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims description 12
- 238000003723 Smelting Methods 0.000 title claims description 7
- 229910052742 iron Inorganic materials 0.000 title claims description 6
- 238000005422 blasting Methods 0.000 claims abstract description 9
- 239000006185 dispersion Substances 0.000 claims description 18
- 239000000428 dust Substances 0.000 abstract description 19
- 239000002245 particle Substances 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 2
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 238000007664 blowing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 230000005587 bubbling Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、鉄鉱石の溶融還元設備における予備還元炉
の改良に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] This invention relates to an improvement of a preliminary reduction furnace in an iron ore smelting reduction facility.
鉄鉱石の溶融還元では、設備を溶融還元炉と流動層式の
予備還元炉とから構成し、溶融還元炉で発生する排ガス
を予備還元炉流動層の流動化、還元ガスとして利用する
方法が経済上好ましい。そして、この流動層としては、
技術的完成度が高く。For smelting reduction of iron ore, an economical method is to configure the equipment with a smelting reduction furnace and a fluidized bed pre-reduction furnace, and use the exhaust gas generated in the smelting reduction furnace to fluidize the fluidized bed of the pre-reduction furnace and as reducing gas. It is preferable. And as this fluidized bed,
High level of technical perfection.
しかも鉱石の予熱、還元に伴う粉化を抑制できるという
点から、バブリング流動層が特に有利である。Moreover, a bubbling fluidized bed is particularly advantageous in that it can suppress powdering caused by preheating and reduction of ore.
この予備還元炉は、その内部にガス噴出用の多数のノズ
ル孔(ガス通孔)を有する分散板を備えており、この分
散板の上方に形成される予備還元室に鉄鉱石が装入され
、分散板下方のガス吹込室(風箱)に溶融還元炉からの
排ガス(還元ガス)が導入される。この還元ガスは1分
散板のノズル孔を通じて上方の予備還元室に吹き出され
、これにより流動層が形成され、鉄鉱石の予備還元と予
熱がなされる。This pre-reduction furnace is equipped with a dispersion plate having a large number of nozzle holes (gas holes) for ejecting gas therein, and iron ore is charged into a pre-reduction chamber formed above the dispersion plate. The exhaust gas (reducing gas) from the melting reduction furnace is introduced into the gas blowing chamber (wind box) below the distribution plate. This reducing gas is blown out through the nozzle hole of one dispersion plate into the upper pre-reduction chamber, thereby forming a fluidized bed and pre-reducing and preheating the iron ore.
このような予備還元炉では、排ガス中に含まれるダスト
の分散板への付着が大きな問題となる。In such a preliminary reduction furnace, adhesion of dust contained in the exhaust gas to the dispersion plate poses a major problem.
すなわち、溶融還元炉から発生する排ガスには多量のダ
ストが含まれており、このうち10μm以下の微粒ダス
トは、多くの場合サイクロン等の除塵装置では除去でき
ず、このような微粒ダストを含む排ガスがそのまま予備
還元炉に導入されてしまう。In other words, the exhaust gas generated from the smelting reduction furnace contains a large amount of dust, and in many cases, fine dust of 10 μm or less cannot be removed by a dust removal device such as a cyclone. is directly introduced into the preliminary reduction furnace.
上記ダストはSやNa、 K等のアルカリ化合物を多く
含んでいるため、900℃を超えるような温度の排ガス
中では粘着性を持ち、このため予備還元炉に導入された
ダストは分散板下面やノズル孔内面(特にノズル孔入側
内面)に付着することになる。このようなダストによる
付看物は次第に成長し、遂には還元ガスの円滑な流れを
妨げ、適正な流動層を形成できなくなる。第2図はこの
ような状況を示すもので、1は流動層、2は分散板、3
は分散板下方のガス吹込室、4は付着、成長したダスト
である。Since the above dust contains a large amount of alkaline compounds such as S, Na, and K, it becomes sticky in the exhaust gas at a temperature exceeding 900°C. Therefore, the dust introduced into the pre-reduction furnace will stick to the bottom surface of the dispersion plate and the like. It will adhere to the inner surface of the nozzle hole (particularly the inner surface on the entry side of the nozzle hole). These dust particles gradually grow and eventually impede the smooth flow of the reducing gas, making it impossible to form a proper fluidized bed. Figure 2 shows this situation, where 1 is a fluidized bed, 2 is a dispersion plate, and 3 is a fluidized bed.
4 is the gas blowing chamber below the dispersion plate, and 4 is the deposited and grown dust.
本発明は、このような従来の問題に鑑みなされたもので
、分散板に対するダストの付着、成長を効果的に防止で
きる予備還元炉の提供をその目的とする。The present invention was made in view of such conventional problems, and an object of the present invention is to provide a pre-reduction furnace that can effectively prevent dust from adhering to and growing on a dispersion plate.
〔課題を解決するための手段〕
このため本発明は、多数のノズル孔が貫設された分散板
を炉内部に有する流動層式の千m還元炉において、炉の
底部に、炉の底板上面に設けられる複数の凹部と、底板
内部に前記各凹部の底部に開口するようにして設けられ
るガス供給孔と、該ガス供給孔に炉外からガスを供給す
る供給手段とからなるブラスト装置を設けたことをその
特徴とする。[Means for Solving the Problems] For this reason, the present invention provides a fluidized bed reduction furnace having a dispersion plate in which a large number of nozzle holes are penetrated. A blasting device is provided, which comprises a plurality of recesses provided in the bottom plate, gas supply holes provided in the bottom plate so as to open at the bottoms of the respective recesses, and a supply means for supplying gas from outside the furnace to the gas supply holes. Its characteristic is that
ショット等の粒子を底板上面の凹部内に装入しておき、
炉の操業中、定期的に供給手段からガス供給孔に高圧ガ
スを供給し、凹部内の粒子を分散板下面に向けて噴射さ
せる。この粒子の噴射により、第2図に示すように分散
板下面およびノズル孔の入口近傍に付着したダストが除
去される。Particles such as shot are charged into the recess on the top of the bottom plate,
During operation of the furnace, high-pressure gas is periodically supplied from the supply means to the gas supply hole to inject the particles in the recesses toward the lower surface of the dispersion plate. As shown in FIG. 2, by spraying the particles, dust adhering to the lower surface of the dispersion plate and near the entrance of the nozzle hole is removed.
除去されたダストの凝集物は落下して凹部内に溜り1次
のブラストのための粒子として用いられる。このダスト
の凝集物はある程度の硬度を有しており、ブラスト用の
粒子として十分使用に耐え得るものである。したがって
、基本的には本発明の装置では炉外からのブラスト用粒
子の補給は必要としない。The removed dust aggregates fall and accumulate in the recesses, where they are used as particles for primary blasting. This dust agglomerate has a certain degree of hardness and can be used sufficiently as particles for blasting. Therefore, basically, the apparatus of the present invention does not require replenishment of blasting particles from outside the furnace.
通常、分散板下方のガス吹込室内のガス流速は数m/s
ee前後であり、このため前記粒子の噴射速度が数十m
1sec以上となるよう高圧ガスを供給することが好ま
しい。Normally, the gas flow velocity in the gas blowing chamber below the distribution plate is several m/s.
ee, and therefore the injection speed of the particles is several tens of meters.
It is preferable to supply high pressure gas for 1 sec or more.
第1図は本発明の一実施例を示すもので、5は分散板、
6はこの分散板に多数設けられるノズル孔、7は炉の底
板である。分散板5は予備還元炉の内部を上下に仕切る
もので、その上部が予備還元室12を、また、下部がガ
ス吹込室13をそれぞれ構成しているにのガス吹込室1
3にはガス吹込口(図示せず)が設けられ、これに溶融
還元炉からのガス導管が接続されている。FIG. 1 shows an embodiment of the present invention, in which 5 is a dispersion plate;
Reference numeral 6 indicates a large number of nozzle holes provided in this distribution plate, and 7 indicates a bottom plate of the furnace. The dispersion plate 5 partitions the interior of the pre-reduction furnace into upper and lower parts, with the upper part forming the pre-reduction chamber 12 and the lower part forming the gas blowing chamber 13.
3 is provided with a gas inlet (not shown), to which a gas conduit from the melting reduction furnace is connected.
炉の底板上面には多数の凹部8が設けられている。本実
施例では、これら凹部8は断面コーン状に構成されてい
る。なお、この凹部8は、除去したダストの凝集物をブ
ラスト用の粒子としてその内部に回収するため、底板上
面になるべく密に設けるようにすることが好ましい。A large number of recesses 8 are provided on the upper surface of the bottom plate of the furnace. In this embodiment, these recesses 8 have a cone-shaped cross section. The recesses 8 are preferably provided as densely as possible on the upper surface of the bottom plate in order to collect the removed dust aggregates therein as particles for blasting.
底板7の内部には、上端が前記各四部8の底部に開口す
るようにしてガス供給孔9が設けられている。そして、
これらガス供給孔9の下端には。Gas supply holes 9 are provided inside the bottom plate 7 so that their upper ends open at the bottoms of each of the four sections 8 . and,
At the lower ends of these gas supply holes 9.
炉外からガスを供給するガス供給管10が接続されてい
る。なお、11はガス供給管10に設けられるバルブで
ある。A gas supply pipe 10 that supplies gas from outside the furnace is connected. Note that 11 is a valve provided in the gas supply pipe 10.
以上のような構成によれば、最初にショット等の粒子を
底板上面の凹部8に装入しておく。そして、炉の操業中
、定期的にガス供給管10からガス供給孔9にN2等の
高圧ガスを供給し、凹部8内の粒子Aを分散板5の下面
に向けて噴射させる。According to the above configuration, particles such as shot are first charged into the recess 8 on the upper surface of the bottom plate. During operation of the furnace, a high pressure gas such as N2 is periodically supplied from the gas supply pipe 10 to the gas supply hole 9 to inject the particles A in the recess 8 toward the lower surface of the dispersion plate 5.
この粒子Aの噴射により、分散板5の下面およびノズル
孔6の入口近傍に付着したダストが除去される。By spraying the particles A, dust adhering to the lower surface of the dispersion plate 5 and near the entrance of the nozzle hole 6 is removed.
除去されたダストの凝集物は落下して凹部8内に溜り、
次のブラストのための粒子として用いられる。The removed dust aggregates fall and accumulate in the recess 8,
Used as particles for the next blast.
前記ガス供給管10からの高圧ガスは、通常、粒子の噴
射速度が数十m/sec以上となるような圧力で1〜2
秒間供給される。The high-pressure gas from the gas supply pipe 10 is normally supplied at a pressure of 1 to 2 m/sec or more so that the particle injection speed is several tens of m/sec or more.
Supplied for seconds.
以上述べた本発明によれば、分散板下面やノズル孔の入
口近傍でのダストの付着、成長が効果的に防止されるた
め、排ガスの流動層内への吹き込みを安定して行わせる
ことができる。According to the present invention described above, since the adhesion and growth of dust on the lower surface of the dispersion plate and near the entrance of the nozzle hole is effectively prevented, it is possible to stably blow exhaust gas into the fluidized bed. can.
第1図は本発明の一実施例を示す縦断面図である。第2
図は従来の予備還元炉におけるダストの付着状況を示す
説明図である。
図において、5は分散板、6はノズル孔、7は底板、8
は凹部、9はガス供給孔、10はガス供給管である。FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention. Second
The figure is an explanatory diagram showing the state of dust adhesion in a conventional preliminary reduction furnace. In the figure, 5 is a dispersion plate, 6 is a nozzle hole, 7 is a bottom plate, and 8
9 is a recessed portion, 9 is a gas supply hole, and 10 is a gas supply pipe.
Claims (1)
動層式の予備還元炉において、炉の底部に、炉の底板上
面に設けられる複数の凹部と、底板内部に前記各凹部の
底部に開口するようにして設けられるガス供給孔と、該
ガス供給孔に炉外からガスを供給する供給手段とからな
るブラスト装置を設けたことを特徴とする鉄鉱石の溶融
還元設備における予備還元炉。In a fluidized bed pre-reduction furnace which has a dispersion plate with a large number of nozzle holes penetrated inside the furnace, the bottom of the furnace has a plurality of recesses provided on the upper surface of the bottom plate of the furnace, and the bottom of each of the recesses inside the bottom plate. A preliminary reduction furnace in iron ore smelting and reduction equipment, characterized in that it is equipped with a blasting device consisting of a gas supply hole provided so as to open into the gas supply hole, and a supply means for supplying gas from outside the furnace to the gas supply hole. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32156890A JPH04191309A (en) | 1990-11-26 | 1990-11-26 | Pre-reduction furnace in smelting reduction device for iron ore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32156890A JPH04191309A (en) | 1990-11-26 | 1990-11-26 | Pre-reduction furnace in smelting reduction device for iron ore |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04191309A true JPH04191309A (en) | 1992-07-09 |
Family
ID=18134019
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32156890A Pending JPH04191309A (en) | 1990-11-26 | 1990-11-26 | Pre-reduction furnace in smelting reduction device for iron ore |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04191309A (en) |
-
1990
- 1990-11-26 JP JP32156890A patent/JPH04191309A/en active Pending
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