JPH0249376B2 - - Google Patents
Info
- Publication number
- JPH0249376B2 JPH0249376B2 JP13636484A JP13636484A JPH0249376B2 JP H0249376 B2 JPH0249376 B2 JP H0249376B2 JP 13636484 A JP13636484 A JP 13636484A JP 13636484 A JP13636484 A JP 13636484A JP H0249376 B2 JPH0249376 B2 JP H0249376B2
- Authority
- JP
- Japan
- Prior art keywords
- dust
- roasting
- box
- sludge
- heavy metals
- 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.)
- Expired - Lifetime
Links
- 239000000428 dust Substances 0.000 claims description 33
- 238000000034 method Methods 0.000 claims description 16
- 238000005192 partition Methods 0.000 claims description 11
- 238000009423 ventilation Methods 0.000 claims description 11
- 229910001385 heavy metal Inorganic materials 0.000 claims description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000010802 sludge Substances 0.000 claims description 6
- 238000009628 steelmaking Methods 0.000 claims description 4
- 239000008188 pellet Substances 0.000 claims description 2
- 239000000446 fuel Substances 0.000 claims 3
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000002893 slag Substances 0.000 description 14
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 229910000278 bentonite Inorganic materials 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 description 1
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 229910000464 lead oxide Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
一般に製鋼工場より発生するダスト、スラツジ
類(以下ダストと言う)は、酸化亜鉛、酸化鉛、
酸化カドミユ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つて、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。
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開
昭51−129802号公報及び特開昭51−145528号公報
に示される如く既に出願し、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つて、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、特願58−236755号として出願して
いる。
本発明はこれらダスト処理法におけるダストの
焙焼法をより簡単な設備で効率良く実施出来る様
にしたものであつて、その要旨するところは、ダ
ストに少量のコークス粉を混合してブリケツト又
はペレツトに塊成化した後に、底面に通気孔を有
するパレツト状の焙焼ボツクスに200mm〜600mmの
層厚となる様に充填して、焙焼ボツクスのまま製
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。
以下説明図にもとづいて本願方法を詳述する。
第1図はダストの焙焼ボツクスの構造を示したも
ので、1は焙焼ボツクス本体、2は格子状の通気
孔を有する底面部、3は500mm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つた塊成化物4を約200mm
〜600mmの層厚になる様に充填して、下方からの
熱源よつ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り過ぎて焼結現象
を起こして好ましくない。ダストの焙焼温度は有
害重金属を還元揮化せしめて、しかも焼結しない
温度約900〜1000℃とすることが好ましく、自然
通風による焙焼では充填層厚を200mm〜600mmとす
ることが適当である。仕切板3は焙焼ボツクス1
の一辺が500mm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塊成化物4を均
一に焙焼する働きをするもので、充填層の通気抵
抗をを適当に調節する効果を有し、幅広い充填層
に対して500mm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、
充填層厚をを大きくするほど仕切板間隔を狭くす
る必要があつて、これらの調節によつて焙焼時間
と焙焼温度を制御する所に本願方法の特徴があ
る。
なお焙焼ボツクス、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。
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、ダスト塊成
化物4を充填した焙焼ボツクス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
放置し焙焼ボツクス底部のダスト魂成化物にスラ
グ顕熱によつて着火せしめ、着火した焙焼ボツク
ス5は集塵機に連通したフード9内に放置し自然
通風によつて焙焼を完結せしめる。底部に着火さ
れたダスト塊成化物4は自然通風によつて上部へ
燃焼層6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Zn,Pb,Cd等の酸化物は還元揮化され白煙
となつ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、焙焼ボツクスを多
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。
次に以上の焙焼によつて有害重金属の一部が除
去され、全体が高温となつたダスト塊成化物は、
溶滓投入用のホツパー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
用したバブリング用ランス13による撹拌と共に
完全に溶滓中へ滓化される。この処理反応によつ
て焙焼後も残留している若干の有害重金属は、完
全に揮化されて集塵回収され、ダストの無公害化
処理が完成するものである。
以下実施例を述べる。
<実施例>
普通鋼電気炉ダスト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ツトを作り、縦1000m横
1000mm深さ700mmの鉄製焙焼ボツクスに、充填層
厚が500mmとなる様に装入して、約3t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500mmとなる)を入れた場合と、
仕切板無しの場合とを比較して示すと、次の様で
あつた。
Dust and sludge (hereinafter referred to as dust) generally generated from steel factories include zinc oxide, lead oxide,
Since it contains toxic heavy metals such as cadmium oxide and far exceeds the disposal standards for industrial waste, it is a pollution problem to dispose of it as it is, and it is difficult to dispose of it, and it costs a lot of money to dispose of it. It takes. On the other hand, slag generated in large quantities from steel factories is discharged as high-temperature slag, and although it has a large amount of thermal energy, it is left unused and wasted to cool. The present inventors paid attention to these problems and invented a treatment method that utilizes the sensible heat of the molten slag to turn dust into molten slag and remove and recover harmful heavy metals. As shown in Japanese Patent Publication No. 51-145528, an application has already been filed, and as an improved method, prior to converting the dust into slag, preliminary roasting is performed and the dust is heated during slag in a high temperature state. A method of reacting with the above has been filed as Japanese Patent Application No. 58-236755. The present invention enables the roasting of dust in these dust processing methods to be carried out efficiently with simpler equipment.The gist of the present invention is to mix a small amount of coke powder with dust and roast it into briquettes or pellets. After the slag is agglomerated, it is filled into a pallet-shaped roasting box with ventilation holes on the bottom to a layer thickness of 200 mm to 600 mm, and placed on top of the high-temperature slag discharged from the steelmaking furnace in the roasting box. The dust on the bottom is ignited, and after ignition, the roaster is left in a place where the smoke from the roasting can be collected and the dust can be collected and roasted through natural ventilation. The method of the present application will be described in detail below based on explanatory diagrams.
Figure 1 shows the structure of the dust roasting box. 1 is the roasting box body, 2 is the bottom with grid-like ventilation holes, and 3 is removable partitions inserted vertically at 500 mm intervals. The board shows a 200mm agglomerated material 4 made by mixing dust with coke powder, etc.
It is filled to a layer thickness of ~600 mm, and the heat source from below ignites the soul compound at the bottom, which is then roasted using 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 become too high, causing a sintering phenomenon, which is undesirable. The temperature for roasting the dust is preferably about 900 to 1000°C, which reduces and volatilizes harmful heavy metals but does not cause sintering. When roasting with natural ventilation, it is appropriate to set the packed layer thickness to 200 mm to 600 mm. be. Partition plate 3 is roasting box 1
It is not necessary for small-sized cases with a side of 500 mm or less, but for large-sized cases, it serves to evenly roast the packed agglomerate 4, and the ventilation resistance of the packed bed can be adjusted appropriately. It has the effect of creating a wide filling layer, and must be placed vertically at intervals of 500mm.
However, the spacing between the partition plates has a correlation with the packed layer thickness.
The method of the present invention is characterized in that the larger the packed layer thickness, the narrower the distance between the partition plates, and the roasting time and roasting temperature are controlled by these adjustments. Note that iron is sufficient as the material for the roasting box and partition plate, but this does not preclude lining with refractory material or colorizing treatment. Figure 2 shows the dust treatment process when the method of the present invention is used in the preliminary roasting process, in which a roasting box 1 filled with dust agglomerates 4 is placed on top of the slag 14 that has undergone the dust charging process. The ignited roasting box 5 is left in a hood 9 connected to a dust collector and roasted by natural ventilation. to complete. The dust agglomerates 4 ignited at the bottom are moved to the upper part of the combustion layer 6 by natural ventilation, and the whole is roasted to a red-hot high temperature. At this time, the inside of the packed bed 7 becomes high temperature and is heated by coke powder. A reducing atmosphere is created, and oxides of harmful heavy metals such as Zn, Pb, and Cd 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. Next, some of the harmful heavy metals are removed through the above roasting process, and the dust agglomerates are heated to a high temperature.
The molten slag is transferred to a hopper 8 for charging the slag, and is charged into the slag 12 discharged from the steelmaking furnace 10 and moved into the dust collection hood 11 while still at a high temperature, and then heated by a bubbling lance 13 using high-pressure gas. As the mixture is stirred, it is completely converted into slag. Through this treatment reaction, some harmful heavy metals remaining after roasting are completely volatilized and collected and collected, completing the dust pollution-free treatment. Examples will be described below. <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 briquettes,
It was charged into a 1000 mm deep iron roasting box with a depth of 700 mm so that the packed layer thickness was 500 mm, and the result was placed on about 3 tons of electric furnace slag (surface temperature 600℃) and roasted. When a cross-shaped partition plate is inserted in the direction (the distance between the main body and the partition plate is 500 mm),
A comparison with the case without the partition plate shows the following results.
【表】
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。
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つ
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。[Table] This shows that when using a partition plate, the roasting time is short and even roasting is possible. 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.
【表】
以上説明した如く、本発明方法は製鋼ダスト、
スラツジを無公害化処理するために簡単な焙焼ボ
ツクスを準備するだけで実施し得るものであつて
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。[Table] As explained above, the method of the present invention uses steelmaking dust,
This process can be carried out by simply preparing a simple roasting box to make sludge non-polluting, and can be applied in small-scale factories as a low-cost method of non-polluting processing. The effect is that it has great significance.
第1図は本願発明で使用する焙焼ボツクスの説
明図、第2図は本願発明方法の工程を示す概要説
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)
ダスト、スラツジに、コークス粉から成る炭材燃
料単味または液体燃料を加えた混合燃料を混練し
て、ブリケツト、ペレツトに塊成化後、底部に通
気孔を有する焙焼ボツクス内に、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、スラツジに着火せしめた後に、焙焼ボ
ツクスを集塵機に連通して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、スラツジの焙焼法。 2 焙焼ボツクス内に仕切板を垂直方向に入れて
ダスト、スラツジの塊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、
スラツジの焙焼法。[Scope of Claims] 1 Dust and sludge containing harmful heavy metals generated during steelmaking operations are kneaded with a single carbon fuel consisting of coke powder or a mixed fuel with liquid fuel added to form briquettes or pellets. After the formation, the torrefaction box with ventilation holes at the bottom is filled with a layer thickness of 200 mm to 600 mm, the dust and sludge are ignited by a heat source from below, and the torrefaction box is placed in a dust collector. Connect it and leave it in the hood,
A method of roasting dust and sludge, which is characterized by roasting with natural ventilation to reduce and volatilize the heavy metals contained. 2. The dust according to claim 1, characterized in that the agglomerated product of dust and sludge is roasted by inserting a partition plate vertically into the roasting box.
Suratji roasting method.
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 JPS6115929A (en) | 1986-01-24 |
| JPH0249376B2 true 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) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP2166122A1 (en) | 1999-09-16 | 2010-03-24 | JFE Steel Corporation | Method of manufacturing high strength steel |
| EP1149925B1 (en) | 1999-09-29 | 2010-12-01 | JFE Steel Corporation | Sheet steel and method for producing sheet steel |
| WO2001023624A1 (en) | 1999-09-29 | 2001-04-05 | Nkk Corporation | Sheet steel and method for producing sheet steel |
-
1984
- 1984-06-30 JP JP59136364A patent/JPS6115929A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6115929A (en) | 1986-01-24 |
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