JPS6115929A - Method for burning steel-making dust and sludge - Google Patents

Method for burning steel-making dust and sludge

Info

Publication number
JPS6115929A
JPS6115929A JP59136364A JP13636484A JPS6115929A JP S6115929 A JPS6115929 A JP S6115929A JP 59136364 A JP59136364 A JP 59136364A JP 13636484 A JP13636484 A JP 13636484A JP S6115929 A JPS6115929 A JP S6115929A
Authority
JP
Japan
Prior art keywords
dust
roasting
heavy metals
sludge
briquette
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.)
Granted
Application number
JP59136364A
Other languages
Japanese (ja)
Other versions
JPH0249376B2 (en
Inventor
Takashi Oshiumi
鴛海 任
Mitsuo Morita
森田 光雄
Kazuhiko Hayashi
一彦 林
Seishiro Matsuzuka
松塚 征四郎
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 Jiryoku Senko Co Ltd
Original Assignee
Nippon Jiryoku Senko 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 Jiryoku Senko Co Ltd filed Critical Nippon Jiryoku Senko Co Ltd
Priority to JP59136364A priority Critical patent/JPS6115929A/en
Publication of JPS6115929A publication Critical patent/JPS6115929A/en
Publication of JPH0249376B2 publication Critical patent/JPH0249376B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To eliminate the pollution at low cost by kneading the dust generated in steel making and contg. harmful heavy metals, etc. with a carbonaceous fuel to form a briquette, and burning the briquette in a combustion box with a vent at the bottom under specified conditions to reduce and volatilize the metals. CONSTITUTION:A carbonaceous fuel such as coke powder is added to dust and sludge contg. harmful heavy metals, etc. and generated in a steel making operation, and the mixture is kneaded to form a briquette 4, which is packed into a combustion box body 1 equipped with a bottom surface part 2 and a partition plate 3 in 200-600mm. thickness. The box body 1 is placed on slag 14 wherein dust is already charged, and burnt with the sensible heat of the slag under natural ventilation. The harmful heavy metals are reduced and volatilized, and recovered. The briquette 4 from which a part of the heavy metals is removed is transferred into a hopper 8, charged into molten slag 12 discharged from a steel-making furnace 10 while keeping the briquette at high temps., agitated by the bubbling 13 of a high-pressure gas, and completely slagged into the molten slag.

Description

【発明の詳細な説明】 一般に製鋼工場より発生するダスト、スラッジ類(以下
ダストと言う)は、酸化亜鉛、酸化鉛、酸化カドミュー
ム等の有害重金属を含み、しかも産業廃棄物の廃棄基準
を大幅に越えるために、このまま廃棄することは公害上
問題であって、その処理に困難性を有し、その処分に多
額の費用を要している。   ′ 一方製鋼工場から多量に発生するスラグは、高温の溶滓
として排出され多大の熱エネルギーを有しながら未利用
のまま無駄に放冷されている。
[Detailed Description of the Invention] Dust and sludge (hereinafter referred to as dust) generally generated from steel factories contain hazardous heavy metals such as zinc oxide, lead oxide, and cadmium oxide, and furthermore, they significantly exceed the disposal standards for industrial waste. In order to overcome this problem, it is a pollution problem to dispose of it as it is, and it is difficult to dispose of it, and a large amount of money is required to dispose of it. ' On the other hand, slag generated in large quantities from steel factories is discharged as high-temperature slag, and although it contains a large amount of thermal energy, it is left to cool unusedly.

本発明者等は、これらに注目して、溶滓の顕熱を利用し
てダストを溶滓中に溶融滓化すると共に有害重金属を除
去回収する処理法を発明して特願昭50−53680、
特願昭50−69268等既にとして出願し、更にその
改良法としてダストを溶滓中に滓化せしめるに先立って
、予備焙焼を行い高温状態のダストで溶滓中に反応せし
める方法を、特許5g−,236755として出願して
いる。
The present inventors paid attention to these problems and invented a treatment method for converting dust into molten slag in slag using the sensible heat of slag and removing and recovering harmful heavy metals. ,
Patent Application No. 50-69268 has already been filed, and as an improvement on the method, a patent has been granted for a method in which the dust is pre-roasted and reacted with the hot dust in the slag before being converted into slag. 5g-, 236755.

トの焙焼法をより簡単な設備で効率良〈実施出来る様に
したものであって、その要旨とするところは、ダストに
少量のコークス粉を混合してブリケット又はペレット等
に塊成化した後に、底面に通気孔を有するパレット状の
焙焼ボックスに約200mm〜600IIII11の層
厚となる様に充填して、焙焼ボックスのまま製鋼炉から
排出された高温スラグの上に乗せて、底部のダストに着
火せしめ、着火後は焙焼による発煙を回収集塵し得る場
所に放置して自然通気による焙焼を行うところにある。
It is a method that can be carried out more efficiently using simpler equipment than the conventional roasting method. Afterwards, a pallet-shaped roasting box with ventilation holes on the bottom is filled with a layer thickness of about 200 mm to 600III11, and the roasting box is placed on top of the high-temperature slag discharged from the steelmaking furnace. The dust is ignited, and after ignition, the roasting process is carried out through natural ventilation by leaving it in a place where the smoke from the roasting can be collected and collected.

以下説明図にもとづいて本願方法を詳述する。The method of the present application will be described in detail below based on explanatory diagrams.

第1図はダストの焙焼ボックスの構造を示し たもので
、(1)は焙焼ボックス本体、(2)は格子状の通気孔
を有する底面部、(3)は約500 rnrn間隔で垂
直方向に挿入され脱着可能な仕切板を示し、ダストにコ
ークス粉等を混合して作っtこ魂成化物(4)を約20
0mm 〜600mmの層厚になる様に充填して、下方
からの熱源よって底部の魂成化物に着火せしめ、自然通
風で焙焼するものであるが、充填層厚を薄くすると着火
後のダスト焙焼温度が不充分となり、充填層厚が厚過ぎ
ると焙焼時間が大幅に遅延すると同時にダスト焙焼温度
が高温となし過ぎて焼結現象を起こして好ましくない。
Figure 1 shows the structure of the dust torrefaction box. (1) is the torrefaction box body, (2) is the bottom part with grid-like ventilation holes, and (3) is the vertical part at intervals of approximately 500 rnrn. It shows a removable partition plate that is inserted in the direction of
It is filled to a layer thickness of 0 mm to 600 mm, and a heat source from below ignites the soul compound at the bottom, which is then roasted with natural ventilation. However, if the packed layer thickness is thinner, the dust roasting after ignition is reduced. If the firing temperature is insufficient and the packed layer thickness is too thick, the roasting time will be significantly delayed, and at the same time, the dust roasting temperature will be too high, causing a sintering phenomenon, which is undesirable.

ダストの焙焼温度は有害重金属を還元揮化せしめて、し
かもしく、自然通風による焙焼では充填層厚を約200
mm〜600Iamとすることが適当である。仕切板(
3)は焙焼ボックス(1)の−辺が約50011II1
1以下の小型の場合には必要としないが、大型の場合に
は充填された魂成化物(4)を均一に焙焼する働きをす
るもので、充填層の通気抵抗を適当に調節する効果を有
し、幅広い充填層に対して約50011Im間隔で垂直
に入れる必要がある。しかし仕切板の間隔は充填層厚と
の相関があり、充填層厚を大きくするほど仕切板間隔を
狭くする必要があって、これらの調節によって焙焼時間
と焙焼温度を制御する所に本願方法の特徴がある。
The roasting temperature of the dust is such that harmful heavy metals are reduced and volatilized, and when roasted with natural ventilation, the packed layer thickness is approximately 200 mm.
It is appropriate to set it as mm - 600Iam. Partition plate (
3) The - side of the roasting box (1) is approximately 50011II1
It is not necessary in small cases of 1 or less, but in large cases it works to uniformly roast the filled soul compound (4), and has the effect of appropriately adjusting the ventilation resistance of the packed bed. , and should be inserted perpendicularly to the wide packed bed at intervals of about 50011 Im. However, the spacing between the partition plates is correlated with the thickness of the packed bed, and the larger the thickness of the packed bed, the narrower the gap between the partition plates. There are characteristics of the method.

なお焙焼ボックス、仕切板の材質は鉄製で充分であるが
、耐火物の内張又はカロライズ処理等をほどこすことを
妨げるものではない。
It is sufficient that the roasting box and the partition plates are made of iron, but this does not preclude them from being lined with a refractory material or calorized.

第2図は本願方法を予備焙焼工程に利用した場合のダス
ト処理工程を示したもので、ダスト魂成化物(4)を充
填した焙焼ボックス(1)を、ダスト投入処理の完了し
たスラグ(14)上に乗せて、約30分間放置し焙焼ボ
ックス底部のダスト魂成化物にスラグ顕熱によって着火
せしめ、着火した焙焼ボックス(5)は集塵機に連通結
せしめる。底部に着火されたダスト魂成化物(4)は自
然通風よって上部へ燃焼層(8)を移動しながら全体が
赤熱高温に焙焼されるが、その際充填層(7)内は高温
になると共にコークス粉による還元雰囲気となり、有害
重金属であるZn5PbXCd等の酸化物は還元揮化さ
れ白煙となって集塵装置に回収される。斯くして焙焼が
完結するまで放置するに際し、焙焼ボックスを多数積み
重ねる場合も生じるが、この場合に下方向からの通気を
阻害しないような考慮が必要である。
Figure 2 shows the dust treatment process when the present method is used in the preliminary roasting process. (14) Place it on top and leave it for about 30 minutes to ignite the dust particles at the bottom of the roasting box by the sensible heat of the slag, and connect the ignited roasting box (5) to a dust collector. The dust particles (4) ignited at the bottom move upward through the combustion layer (8) due to natural ventilation, and are roasted to a red-hot temperature as a whole, but at this time, the inside of the packed layer (7) becomes high temperature. At the same time, a reducing atmosphere is created due to coke powder, and oxides such as Zn5PbXCd, which are harmful heavy metals, are reduced and volatilized and collected in a dust collector as white smoke. When the roasting is left until the roasting is completed, a large number of roasting boxes may be stacked on top of each other, but in this case, consideration must be given to not impeding ventilation from below.

次に以上の焙焼によって有害重金属の一部が除去され、
全体が高温となったダスト魂成化物は、溶滓投入用のホ
ッパー(8)に移され、製鋼炉(10)より排出され集
塵用フード(11)内に移動された溶滓(12)中へ、
高温のまま投入されて、高圧気体を使用したバブリング
(13)による攪拌と共に完全に溶滓中へ滓化される。
Next, some of the harmful heavy metals are removed by the above roasting process,
The dust particles, which have reached a high temperature as a whole, are transferred to a hopper (8) for charging molten slag, and the molten slag (12) is discharged from the steelmaking furnace (10) and moved into a dust collection hood (11). Inside,
The slag is poured into the slag at a high temperature and stirred by bubbling (13) using high-pressure gas, and is completely converted into slag.

この処理反応によって焙焼後も残留している若干の有害
重金属は、完全に揮化されてs!1回収され、ダストの
無公害化処理が完成するものである。
Through this processing reaction, some harmful heavy metals that remain after roasting are completely volatilized and s! 1 is collected, completing the dust pollution-free treatment.

以下実施例を述べる。Examples will be described below.

〈実施例〉 普通鋼電気炉ダス) 100重量部に対して、コークス
粉15重量部と、ベントナイト5重量部とを混練して豆
炭状のブリケットを作9、縦1000rn横1000、
、m深さ700mrnの鉄製焙焼ボックスに、充填層厚
が5oornrnとなる様に装入して、約3 の電気炉
スラグ(表面温度600℃)上に乗せて放置し焙焼した
結果を、垂直方向に十字状の仕切板(本体と仕切板との
間隔が5001ntnとなる)を入れて場合と、仕切板
無しの場合とを比較して示すと、次の様であった。
<Example> 100 parts by weight of ordinary steel electric furnace dust), 15 parts by weight of coke powder, and 5 parts by weight of bentonite were kneaded to make charcoal-like briquettes9, 1000 rn in length and 1000 rn in width.
The result was charged into an iron roasting box with a depth of 700 mrn so that the packed layer thickness was 50 mrn, and was placed on electric furnace slag (surface temperature 600°C) of about 3 m and left to roast. A comparison between a case in which a cross-shaped partition plate (the distance between the main body and the partition plate is 5001 ntn) in the vertical direction and a case without a partition plate is as follows.

仕切板を使用した場合が、焙焼時間が短くて、しかも均
一焙焼の出来ることを示している。
This shows that when the partition plate is used, the roasting time is short and even roasting is possible.

、 また焙焼によるダスト中の重金属成分量変化を分析
により比較した結果は下表のごとくであって、重金属成
分除去率においても、仕切板を使用した場合が高く、良
結果を示している。
In addition, the results of an analytical comparison of changes in the amount of heavy metal components in the dust due to roasting are as shown in the table below, and the removal rate of heavy metal components is also higher when using the partition plate, indicating good results.

以上説明しtコ如く、本発明方法は製鋼ダスト、スラッ
ジ類を無公害化処理するtコめに簡単な焙焼ボックスを
準備するだけで実施し得るものであって安価に無公害化
処理を行う方法として、小規模工場での適用も可能であ
り、産業上の意義は大きいという効果がある。
As explained above, the method of the present invention can be carried out by simply preparing a simple roasting box for the purpose of decontaminating steelmaking dust and sludge, and can be done at low cost. This method can be applied in small-scale factories and has great industrial significance.

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

第1図は本願発明で使用する焙焼ボックスの説明図、第
2図は本願発明方法の工程を示す概要親図である。
FIG. 1 is an explanatory diagram of a roasting box used in the present invention, and FIG. 2 is a schematic diagram showing the steps of the method of the present invention.

Claims (1)

【特許請求の範囲】 1、製鋼操業に伴って発生した有害重金属等を含むダス
ト、スラッジ類に、コークス粉等の炭材燃料単味または
液体燃料を加えた混合燃料を混練して、ブリケット、ペ
レット等に魂成化後、底部に通気孔を有する焙焼ボック
ス内に、約200mm〜600mmの層厚となるように
充填して、下方からの熱源によりダスト、スラッジ類に
着火せしめた後に、焙焼ボックスを集塵機に連通したフ
ード内に放置して、自然通風で焙焼して含有重金属を還
元揮化せしめることを特徴とするダスト、スラッジ類の
焙焼法。 2、焙焼ボックス内に仕切板を垂直方向に入れてダスト
、スラッジ類の魂成化物を焙焼することを特徴とする、
特許請求の範囲第1項記載のダスト、スラッジ類の焙焼
法。
[Claims] 1. Briquettes, etc. are produced by kneading dust and sludge containing harmful heavy metals generated during steelmaking operations with a single carbon fuel such as coke powder or a mixed fuel with liquid fuel added. After the pellets are formed, they are packed in a roasting box with ventilation holes at the bottom to a layer thickness of approximately 200 mm to 600 mm, and the dust and sludge are ignited by a heat source from below. A method of roasting dust and sludge, which is characterized by leaving a roasting box in a hood connected to a dust collector and roasting with natural ventilation to reduce and volatilize the heavy metals contained. 2. It is characterized by inserting a partition plate vertically into the roasting box to roast dust and sludge.
A method for roasting dust and sludge according to claim 1.
JP59136364A 1984-06-30 1984-06-30 Method for burning steel-making dust and sludge Granted JPS6115929A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59136364A JPS6115929A (en) 1984-06-30 1984-06-30 Method for burning steel-making dust and sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59136364A JPS6115929A (en) 1984-06-30 1984-06-30 Method for burning steel-making dust and sludge

Publications (2)

Publication Number Publication Date
JPS6115929A true JPS6115929A (en) 1986-01-24
JPH0249376B2 JPH0249376B2 (en) 1990-10-30

Family

ID=15173439

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59136364A Granted JPS6115929A (en) 1984-06-30 1984-06-30 Method for burning steel-making dust and sludge

Country Status (1)

Country Link
JP (1) JPS6115929A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6623573B2 (en) 1999-09-29 2003-09-23 Nkk Corporation Steel sheet and method for manufacturing the same
US6652670B2 (en) 1999-09-29 2003-11-25 Tadashi Inoue Steel sheet and method for manufacturing the same
US6663725B2 (en) 1999-09-16 2003-12-16 Nkk Corporation High strength steel sheet and method for manufacturing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6663725B2 (en) 1999-09-16 2003-12-16 Nkk Corporation High strength steel sheet and method for manufacturing the same
US6623573B2 (en) 1999-09-29 2003-09-23 Nkk Corporation Steel sheet and method for manufacturing the same
US6652670B2 (en) 1999-09-29 2003-11-25 Tadashi Inoue Steel sheet and method for manufacturing the same

Also Published As

Publication number Publication date
JPH0249376B2 (en) 1990-10-30

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