JPS61266527A - Method for recycling water crushed slag generated in nonferrous metal smelting - Google Patents
Method for recycling water crushed slag generated in nonferrous metal smeltingInfo
- Publication number
- JPS61266527A JPS61266527A JP60109632A JP10963285A JPS61266527A JP S61266527 A JPS61266527 A JP S61266527A JP 60109632 A JP60109632 A JP 60109632A JP 10963285 A JP10963285 A JP 10963285A JP S61266527 A JPS61266527 A JP S61266527A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- boiler
- smelting
- drying
- water
- 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
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)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
不発明は製錬工程から排出される媛%I:製錬工程にリ
サイクルする方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The invention relates to a method for recycling %I discharged from a smelting process into a smelting process.
非鉄金属製錬で発生する鏝には、目的とする貧属が相当
皺含まれており、通常これを製錬工程にリサイクルして
金属を回収している。The trowels produced in non-ferrous metal smelting contain a considerable amount of the target poor metal, which is usually recycled into the smelting process to recover the metal.
今、鋼の製錬を代表例として説明する。鋼製錬工程は、
8g5図に示す工うにm錬炉1分離炉、製鋼炉からなり
、#錬炉においては、JIjl[科鉱石、浴剤を混合溶
融し空気を吹込んで鋼成分の多量に含まれた溶錬嶺と饅
錬緩が生成される。久いでこれらを分離炉において、七
〇比皇差によって二層に分離し、上ノーの浴錬緩を排棄
し、下層の浴錬貢は、製鋼炉に送る。製鋼炉にSいては
、再び溶剤を添加し、空気を吹込んで、粗鋼と製鋼緩か
生成されるが、a鋼媛中には、鋼が担当量含肩されてい
るので1通常水砕によって粉砕されて溶錬炉にリサイク
ルされている。Now, we will explain steel smelting as a representative example. The steel smelting process is
The furnace shown in Figure 8g5 consists of a smelting furnace, a separation furnace, and a steelmaking furnace. and a steamed rice cake is generated. After a long time, these are separated into two layers by a 70% difference in a separation furnace, the upper layer of sulfur is discarded, and the lower layer of sulfur is sent to a steelmaking furnace. In the steelmaking furnace, solvent is added again and air is blown into the steelmaking furnace to produce crude steel and steelmaking. It is crushed and recycled into the smelting furnace.
また1分離炉、および製鋼炉エリ排出されるガスは、廃
熱ボイラーに導入され、廃熱回収され。In addition, the gas discharged from the separation furnace and steelmaking furnace is introduced into a waste heat boiler and the waste heat is recovered.
煙灰が除去された後、硫酸工場等に送られ含有するSO
2が有効利用され、また、除去された煙灰は、王記製鋼
媛とともに溶錬炉にリサイクルされている。After the smoke ash is removed, it is sent to a sulfuric acid factory and the SO contained therein is
2 is effectively utilized, and the removed smoke ash is recycled to the smelting furnace along with Wangji Steelmaking.
上記リサイクル工程において、水砕された製鋼緩(以下
鏝と称する)が濡れていると、静錬炉への供給系シュー
トに詰りなどのトラブル?招く懸念がある。In the above-mentioned recycling process, if the pulverized steel trowel (hereinafter referred to as trowel) is wet, it may cause problems such as clogging of the feed system chute to the still furnace. There are concerns that this may lead to
そのため、従来、上記水砕した−は、第5図にそのリサ
イクル系路を示す工うに一旦ホツバーに貯留し、水切り
して、水分約3係とする。この水切りした鰻を連続して
取り出し、ロータリードライヤーで乾燥する。乾燥され
た−は、温度70〜80°Cでロータリードライヤーエ
リ排出され、これをベルトコンベアで受けてリサイクル
設備に搬送している。Therefore, conventionally, the pulverized water is temporarily stored in a hopper, the recycling route of which is shown in FIG. 5, and drained to reduce the water content to about 3 parts. The drained eel is taken out one after another and dried using a rotary dryer. The dried material is discharged from the rotary dryer area at a temperature of 70 to 80°C, and is received by a belt conveyor and transported to a recycling facility.
ところで、上記ロータリードライヤーによる乾燥は、例
えば鏝の発生i12〜3T/時の場合、電油0.6〜1
.OkJ/日が必要であるのみならず。By the way, when drying with the above-mentioned rotary dryer is performed, for example, when the generation rate of the iron is 12 to 3 T/hour, the electric oil is 0.6 to 1
.. Not only is OkJ/day required.
ロータリードライヤー出ロエリ排出する緩の温度が高い
ため、これy!−受けて搬送するベルトコンベアのベル
トの損耗が激しく、2〜3ケ月で交換しなければならな
い欠点があった。This is because the temperature of the rotary dryer discharged from the rotary dryer is high. -The belt of the belt conveyor that receives and transports the food is subject to severe wear and tear, and has to be replaced every 2 to 3 months.
本発明は上記の、4I情に鑑み、乾燥のみのための燃料
を使用せず、また装置を損耗することがない水砕媛のリ
サイクル方云乞提供することt目面とする。In view of the above-mentioned 4I circumstances, the present invention aims to provide a method for recycling water granules that does not use fuel only for drying and does not cause wear and tear on the equipment.
本発明は上記の目的な達成するためになされたもので、
その手段は水砕した鐘?廃熱ボイラーの煙灰抜出しチェ
ンコンベアのテールに供給し、煙灰とともにボイラー内
を移動させて乾燥し、これをリサイクル設備によって製
錬工程にリサイクルする方法である。The present invention has been made to achieve the above objectives,
Is the method a crushed bell? In this method, ash is supplied to the tail of a chain conveyor for extracting ash from a waste heat boiler, moved along with the ash inside the boiler, dried, and then recycled to the smelting process using recycling equipment.
以下不発明な図面を参照して説明する。 The following description will be made with reference to non-inventive drawings.
@1図および′j42図は不発明の方法を冥施する鋼製
錬装置およびフローの一例を示すもので、図中符号lは
廃熱ボイラーである。廃熱ボイラーlの下部には、ボイ
ラー内で発生した煙灰を外部に抜出す、チェンコンベア
2が設けられている。このチェンコンベア2のテールに
鐘の導入口2a’に設け、@2図のフローに示す工うに
ホッパーに貯留して水切りし2含水媛をベルトコンベア
3で連続して取出し、チェンコンベアの導入口2aに導
入する。導入された緩は煙灰とともにボイラーの高温に
さらされながら移動し、排出口2bより排出され、リサ
イクル設備に導入され、′1#錬炉に戻される。したが
って、−?乾燥するロータリードライヤーは不要となり
、さらに、廃熱ボイラーの熱′lt直接利用するので、
fa乾燥のみのために鷹泊を便用することもない。また
、煙灰は第3図に粒度分布を示す工うに#粉状で、かつ
吸湿性のため固まり易く、チェンケースや抜出しシュー
トの閉基、或いは塊l1分けのスクリーンの目詰りが発
生し易いが、水砕媛は、第4図に所定粒度エリ人ぎいも
のの合計含有率な示すように粒度が煙灰に比してはるか
に粗(、これを煙灰と混合することによって媛に煙灰が
まぶされた状態となり、上記閉基に孟るトラブルが解消
される。Figure @1 and Figure 'j42 show an example of a steel smelting apparatus and flow in which the uninvented method is implemented, and the reference numeral 1 in the figures is a waste heat boiler. A chain conveyor 2 is provided at the bottom of the waste heat boiler 1 for extracting smoke generated within the boiler to the outside. A bell inlet 2a' is provided at the tail of the chain conveyor 2, and the water-containing sea urchin is stored in a hopper and drained as shown in the flow shown in Fig. 2a. The introduced sludge moves along with the smoke ash while being exposed to the high temperature of the boiler, is discharged from the discharge port 2b, is introduced into the recycling equipment, and is returned to the '1# furnace. Therefore, −? There is no need for a rotary dryer for drying, and the heat from the waste heat boiler is directly used.
Takadomari is not used only for fa drying. In addition, smoke ash is powder-like, as shown in Figure 3, and because of its hygroscopic properties, it tends to harden easily, causing clogging of the chain case and extraction chute, or clogging of the screen that separates the lumps. As shown in Figure 4, which shows the total content of particles with a given particle size, Suizakuhime has a much coarser particle size than smoke ash (by mixing it with smoke ash, it is possible to sprinkle smoke ash on the water ash). The problem caused by the group closure described above is resolved.
以下実施例を示して、不考案なさらに詳しく説明する。Hereinafter, the invention will be explained in more detail by showing examples.
1!!#jA製鋼炉工リ2〜3′r/時の割合で排出す
る製鋼炉媛な水砕してホッパーに貯留した。この水砕曖
はホッパーにおいて水切されて含水量的3wtチとなる
。これを約2T/時の速度で連続して抜出り、4m/f
+のスピードで移動しているチェンコンベア2のテール
2aK4人した。ゲイ2−内では、1100’eの製錬
排ガスが出口において600°Cに鐸下し、チェンコン
ベア2はこの温度の降下した出口ガスにさらされている
。また。1! ! #jA steelmaking furnace The water from the steelmaking furnace is discharged at a rate of 2 to 3'r/hour, and the water is crushed and stored in a hopper. This crushed water is drained in a hopper and has a water content of 3wt. This was extracted continuously at a speed of about 2T/hour, and 4m/f
There were 4 people on the tail 2aK of chain conveyor 2 moving at + speed. In the gay 2-, the 1100'e smelting exhaust gas cools down to 600°C at the outlet, and the chain conveyor 2 is exposed to the outlet gas at this reduced temperature. Also.
ボイラー内では、煙灰が200〜aooky/時発生し
、上記チェンコンベア2によって連続して抜出されてい
る。上記導入口2a工り導入された含水量は、上記チェ
ンコンベア2上で廃熱ボイラーの出口ガスにさらされて
移動しながら乾燥され、水分0.5〜0.5wt%とな
り、煙灰とともに排出口2b工り排出されリサイクル設
備に導入される。Inside the boiler, 200~aooky/hour of smoke is generated and is continuously extracted by the chain conveyor 2. The water content introduced through the inlet 2a is dried while being moved on the chain conveyor 2 while being exposed to the outlet gas of the waste heat boiler, and becomes 0.5 to 0.5 wt% of moisture, and the water content is removed from the outlet along with smoke ash. 2b is discharged and introduced into recycling equipment.
この場合、抜出された乾燥緩の温度は約45°Cであり
、fた長期間運転?行なったが糸路の閉基を1発生しな
かった。In this case, the temperature of the extracted drying material was about 45°C, and it was not possible to operate it for a long period of time. However, no closure of the yarn path occurred.
なお、嫌の乾燥程度は、上記チェンコンベアの走行速度
を変えることにエリ自由に調整9罷であつたO
以上の説明は鋼の製錬を代表例として行なったが、非鉄
金属の製錬において発生する目的貧kI4含itの多い
頒も同月にして処理することが出来る。The degree of dryness was freely adjusted by changing the running speed of the chain conveyor. Distributions that occur with a large number of target-poor kI4 items can also be processed in the same month.
以上述べたように本発明に係る方法は、水砕媛乾燥のみ
を目的とし2装置ll1t或いは燃料を必要とせず、さ
らに微粉末でかつ吸湿性の煙灰による糸路の閉基ya′
解消するなと、多くの長所をMする。As described above, the method according to the present invention is intended only for drying granulated water, does not require two devices or fuel, and furthermore, it uses fine powder and hygroscopic smoke ash to close the yarn path.
Don't get rid of it, M's many strengths.
第1因および第2図は1本発明の方@を実施する鋼喪錬
装置の一例を示すもので、第11は、氷砕媛を乾燥する
廃熱ボイフー下部のチェンコンベアを示す図、第2図は
フロー?示す図%第3図は煙灰の粒度分′4ン示す図、
第4図は水砕緩の所定粒度工つ大きいYIA分の割合乞
示す図、第5図は従来の鋼製錬方法のフローχ示す図で
ある。
工・・・・・・廃熱ボイラー、2°°°°・・チェンコ
ンベア、2a・・・・・・水砕a4人口、2t3・・・
・・・排出口、3・・・・・・ベルトコンベア。Figures 1 and 2 show an example of a steel refining device implementing the method of the present invention; Figure 11 shows a chain conveyor at the bottom of the waste heat boiler for drying ice crushers; Is diagram 2 a flow? Figure 3 shows the particle size of smoke ash,
FIG. 4 is a diagram showing the proportion of large YIA in a predetermined grain size of loose water granulation, and FIG. 5 is a diagram showing the flow of a conventional steel smelting method. Engineering... Waste heat boiler, 2°°°°... Chain conveyor, 2a... Water crusher A4 population, 2t3...
...Discharge port, 3...Belt conveyor.
Claims (1)
リサイクルする方法において、該水砕処理した■を製錬
炉の廃熱ボイラーの煙灰抜出しチエンコンベアを通すこ
とによつて乾燥し、煙灰と共に製錬工程にリサイクルす
ることを特徴とする非鉄金属製錬において発生する水砕
■のリサイクル方法。In a method of pulverizing ■ generated during the smelting of nonferrous metals and recycling it to the smelting process, the pulverized ■ is dried by passing it through a chain conveyor for extracting smoke ash from the waste heat boiler of the smelting furnace. A method for recycling fracked water generated in non-ferrous metal smelting, which is characterized by recycling it together with smoke and ash into the smelting process.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60109632A JPS61266527A (en) | 1985-05-22 | 1985-05-22 | Method for recycling water crushed slag generated in nonferrous metal smelting |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60109632A JPS61266527A (en) | 1985-05-22 | 1985-05-22 | Method for recycling water crushed slag generated in nonferrous metal smelting |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61266527A true JPS61266527A (en) | 1986-11-26 |
Family
ID=14515196
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60109632A Pending JPS61266527A (en) | 1985-05-22 | 1985-05-22 | Method for recycling water crushed slag generated in nonferrous metal smelting |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61266527A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5397379A (en) * | 1993-09-22 | 1995-03-14 | Oglebay Norton Company | Process and additive for the ladle refining of steel |
CN104109759A (en) * | 2014-08-12 | 2014-10-22 | 昆明泰仕达科技有限公司 | High-titanium slag wet-process processing system and processing method |
CN105624393A (en) * | 2015-12-31 | 2016-06-01 | 耒阳市焱鑫有色金属有限公司 | Proportioning method for sintering arsenic-removing and sulfur-removing raw material |
-
1985
- 1985-05-22 JP JP60109632A patent/JPS61266527A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5397379A (en) * | 1993-09-22 | 1995-03-14 | Oglebay Norton Company | Process and additive for the ladle refining of steel |
CN104109759A (en) * | 2014-08-12 | 2014-10-22 | 昆明泰仕达科技有限公司 | High-titanium slag wet-process processing system and processing method |
CN105624393A (en) * | 2015-12-31 | 2016-06-01 | 耒阳市焱鑫有色金属有限公司 | Proportioning method for sintering arsenic-removing and sulfur-removing raw material |
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