JPS5847460B2 - Zinc recovery equipment for zinc dust - Google Patents
Zinc recovery equipment for zinc dustInfo
- Publication number
- JPS5847460B2 JPS5847460B2 JP55107434A JP10743480A JPS5847460B2 JP S5847460 B2 JPS5847460 B2 JP S5847460B2 JP 55107434 A JP55107434 A JP 55107434A JP 10743480 A JP10743480 A JP 10743480A JP S5847460 B2 JPS5847460 B2 JP S5847460B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- tank
- dust
- melter
- zinc dust
- 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
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)
Description
【発明の詳細な説明】
本発明は、製鉄所の亜鉛メッキ工程で発生する亜鉛ダス
トから亜鉛を回収するための装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for recovering zinc from zinc dust generated in a galvanizing process in a steel mill.
溶融亜鉛メッキ工程のアツシュ・ドロスや鋼管の溶融亜
鉛メッキ直後の鋼管内面ブロー過程では副産物としてダ
ストが発生するが、このダストには多量の亜鉛分が含ま
れているため、サイクロンやバッグ・フィルタ等で捕捉
して亜鉛分を回収し、再使用するようにしている。Dust is generated as a by-product during the hot-dip galvanizing process and during the internal blowing process of steel pipes immediately after hot-dip galvanizing, but since this dust contains a large amount of zinc, it can be used in cyclones, bags, filters, etc. The zinc content is captured and reused.
しかしながら、バッグ・フィルタ等で捕捉したダストを
ブリケット・マシンやタブレット・マシンを使用して成
形回収する従来の回収方法においては、戒形性が悪く回
収率が低く、また比重が小さいので再使用時6こ溶融亜
鉛上面6こ浮上する難点があり、純度も低いなど不都合
な点が多かった。However, in the conventional collection method of forming and collecting dust captured by bags, filters, etc. using a briquette machine or tablet machine, the collection rate is low due to poor formability, and the specific gravity is small, so it is difficult to reuse it. There were many disadvantages such as molten zinc floating on the upper surface and low purity.
一方、硫酸液を使った湿式法や電解法などの回収方法も
あり比較的良質の亜鉛が回収できるが、コスト高となる
欠点があった。On the other hand, there are recovery methods such as a wet method using a sulfuric acid solution and an electrolytic method, which allow relatively high quality zinc to be recovered, but they have the disadvantage of being expensive.
本発明の目的は、従来の亜鉛回収手段における欠点を排
除しうる比較的簡単な構造の回収装置を得て、回収コス
トの低減化を図ることにある。An object of the present invention is to obtain a recovery device with a relatively simple structure that can eliminate the drawbacks of conventional zinc recovery means, and to reduce recovery costs.
本発明の装置を添附図面によって具体的に説明する。The apparatus of the present invention will be specifically explained with reference to the accompanying drawings.
本装置6こおいては、亜鉛ダストの貯槽1と均圧槽2と
、充填槽3と溶解器4とを順次上方から下方に向かって
連続設置して全体を塔状(こ形成、してあり、貯槽1か
ら順次下部槽へ亜鉛ダストを供給して溶解器4から溶融
亜鉛を排出させるようGこなっている。In this device 6, a storage tank 1 for zinc dust, a pressure equalization tank 2, a filling tank 3, and a dissolver 4 are successively installed from top to bottom in order to form a tower-like structure. The arrangement is such that zinc dust is sequentially supplied from the storage tank 1 to the lower tank and molten zinc is discharged from the melter 4.
貯槽1と均圧槽2との連絡路にはローダリ・フイーダ5
が設置されていており、均圧槽2から充填槽3へ送り込
む導入口の先端6こはスイング弁6を設けてある。A loader feeder 5 is installed in the communication path between the storage tank 1 and the pressure equalization tank 2.
is installed, and a swing valve 6 is provided at the tip 6 of the inlet that feeds from the pressure equalization tank 2 to the filling tank 3.
均圧槽2には、この槽内の圧力を変化させるための圧力
導入管路7が設けてある。The pressure equalization tank 2 is provided with a pressure introduction pipe 7 for changing the pressure inside the tank.
充填槽3と溶解器4とは連通状に連結してある。The filling tank 3 and the dissolver 4 are connected in communication.
溶解器4は亜鉛の溶解温度6こ耐えるセラミック製また
は黒鉛製の密封容器であって、ほぼU字状6こ形成され
、充填槽連結側に比較して他端を低い位置6こして排出
口41を形成してある。The melter 4 is a sealed container made of ceramic or graphite that can withstand the melting temperature of zinc, and is formed into a roughly U-shape. 41 is formed.
溶解器内には溶融亜鉛を集溜されるものであるので、上
部域の位置(こ排滓口42が設けられ、最も低い底部に
は掃除口43を設けてある。Since molten zinc is collected in the melter, a slag discharge port 42 is provided in the upper region, and a cleaning port 43 is provided at the lowest bottom.
さら6こ、溶解器4の外周而全体(こわたって水冷コイ
ル44を巻装させてある。Additionally, a water cooling coil 44 is wrapped around the entire outer periphery of the melter 4.
水冷コイル446こ高周波電流を流して溶解器4I?C
高周波るつぼ型誘導炉としての機能を持たせるようにし
てある。Is the melter 4I by passing high frequency current through the water cooling coil 446? C
It is designed to function as a high frequency crucible induction furnace.
次(こ、本装置の作用6こついて説明する。Next, we will explain the 6 functions of this device.
まず捕集した亜鉛ダストを貯槽1に装入する。First, the collected zinc dust is charged into the storage tank 1.
次いで、不活性ガス導入管路8のピストン弁81を開い
て均圧槽2の内圧を不活性ガスにて大気圧Oこ維持した
のち、ロークリ・フイーダ5cこよって貯槽1内の亜鉛
ダストの定量を均圧槽2内に供給し、そののちピストン
弁81を閉止すると共6こ、圧力導入管路7のピストン
弁71を開いて均圧槽2の内圧を不活性ガス6こて大気
圧よりも5〜15mmAq程度上昇させる。Next, the piston valve 81 of the inert gas introduction pipe 8 is opened to maintain the internal pressure of the pressure equalizing tank 2 to atmospheric pressure O with the inert gas, and then the zinc dust in the storage tank 1 is quantified by using the rotary feeder 5c. is supplied into the pressure equalizing tank 2, and then the piston valve 81 is closed, and the piston valve 71 of the pressure introduction pipe 7 is opened to reduce the internal pressure of the pressure equalizing tank 2 from atmospheric pressure using the inert gas 6. Also increase the amount by about 5 to 15 mmAq.
ここで、スイング弁6を開放して均圧槽2内の亜鉛ダス
トを充填槽3へ移し込む。Here, the swing valve 6 is opened to transfer the zinc dust in the pressure equalization tank 2 to the filling tank 3.
充填槽3(こ送り込まれた亜鉛ダストは自動的に溶解器
4内へ降下し、溶解器4の高周波誘導加熱によって溶解
されて溶解器4の底部(こ下降して滞留する。The zinc dust fed into the filling tank 3 automatically descends into the melter 4, where it is melted by the high-frequency induction heating of the melter 4, and falls to the bottom of the melter 4, where it remains there.
溶解器4の上側部分に充満されている亜鉛ダストに対し
ては、圧力調整弁72によって圧力調整したN2 ,
Arなとの不活性ガスまたは還元ガスを大気圧より高く
保って導入し、亜鉛ダスト溶解中の酸化反応(発火反応
)を抑制するようにしている。The zinc dust filling the upper part of the melter 4 is treated with N2, whose pressure is regulated by the pressure regulating valve 72.
An inert gas such as Ar or a reducing gas is introduced at a pressure higher than atmospheric pressure to suppress the oxidation reaction (ignition reaction) during dissolution of the zinc dust.
溶解器4内の溶融亜鉛は見掛容積が縮小して溶解器4の
底部域に降下するが、本装置においては電力効率を高め
るため6こ、溶解器の中に一定レベルの溶融亜鉛が滞留
するように亜鉛排出口41を設け、亜鉛排出口41から
流出する亜鉛を、亜鉛メッキ槽9または亜鉛インゴット
・ケースに入れて回収する。The apparent volume of the molten zinc in the melter 4 decreases and it falls to the bottom area of the melter 4, but in this device, a certain level of molten zinc remains in the melter in order to increase power efficiency. A zinc discharge port 41 is provided so that the zinc discharge port 41 is discharged, and the zinc flowing out from the zinc discharge port 41 is collected in a galvanizing tank 9 or a zinc ingot case.
排滓口42からは亜鉛中の浮遊不純物を適時排出して曲
鉛の溶解速度が低下することを防止し、また、掃除口4
3からは鉄分などの沈澱した不純物を適時排出させる。The slag discharge port 42 discharges floating impurities in the zinc in a timely manner to prevent the dissolution rate of bent lead from decreasing, and the cleaning port 4
From step 3, precipitated impurities such as iron are discharged in a timely manner.
圧力導入管路および導出管路にはサイクロン10を設置
しておき、ピストン弁やリリーフ弁の作動時6こ、弁の
シール部に付着するダストを捕集して適宜排出し、他の
捕集ダストと共に再度貯槽1へ送り込むよう6こする。A cyclone 10 is installed in the pressure introduction pipe and the pressure outlet pipe, and when the piston valve or relief valve is activated, it collects dust adhering to the seal part of the valve and discharges it as appropriate. Rub it 6 times so that it is sent to the storage tank 1 again together with the dust.
本発明の装置の使用により、1工場の月間発生量が12
0トンCこもおよぶ亜鉛ダストから約80%の良質亜鉛
を回収することができる。By using the device of the present invention, the monthly amount generated per factory can be reduced to 12
Approximately 80% of high-quality zinc can be recovered from 0 tons of zinc dust.
また、装置自体は比較的簡単であり、回収コストも低廉
であると共に粒度の小さいバグ・フィルタ・ダストの回
収も可能となる。Further, the device itself is relatively simple, the collection cost is low, and it is possible to collect small-sized bag filter dust.
図面は本発明に係る亜鉛回収装置の全体構成を概略的に
示す説明図。
1:貯槽、2:均圧槽、3:充填槽、4:溶解器、9:
回収槽。The drawing is an explanatory diagram schematically showing the overall configuration of the zinc recovery apparatus according to the present invention. 1: storage tank, 2: pressure equalization tank, 3: filling tank, 4: dissolver, 9:
Collection tank.
Claims (1)
内圧力の調整が可能であり、ロータリ・フイーダをかい
して前記貯槽内の亜鉛ダストを適時供給される均圧槽と
、スイング弁をかいして前記均圧槽内の亜鉛ダストを適
時供給される充填槽と、前記充填槽の下部に連設された
セラミック製または黒鉛製のほぼU字筒状の気密容器で
あって上部位置に排滓口を有し底部6こ掃除口を有し他
端を亜鉛排出口として形成され、高周波電流が通電され
る水冷コイルを周囲に巻装して高周波るつぼ型誘導炉6
こ機能化された容解器と、前記溶解器の亜鉛排出口(こ
配置した亜鉛回収槽と、前記溶解器内部へ不活性ガスま
たは還元性ガスを導入する配管系とを備えた亜鉛ダスト
の亜鉛回収装置。1. A storage tank for storing a predetermined amount of collected zinc dust, a pressure equalization tank whose internal pressure can be adjusted and the zinc dust in the storage tank is supplied in a timely manner using a rotary feeder, and a swing valve. A filling tank to which the zinc dust in the pressure equalization tank is supplied in a timely manner, and a substantially U-shaped cylindrical airtight container made of ceramic or graphite connected to the lower part of the filling tank, and located in the upper position. A high-frequency crucible-type induction furnace 6 is constructed by winding a water-cooled coil around which a high-frequency current is applied, which has a slag discharge port, a cleaning port at the bottom end, and a zinc discharge port at the other end.
A method for producing zinc dust, which is equipped with a functionalized container, a zinc discharge port of the melter (a zinc recovery tank located therein, and a piping system for introducing an inert gas or a reducing gas into the melter). Zinc recovery equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55107434A JPS5847460B2 (en) | 1980-08-05 | 1980-08-05 | Zinc recovery equipment for zinc dust |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP55107434A JPS5847460B2 (en) | 1980-08-05 | 1980-08-05 | Zinc recovery equipment for zinc dust |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5732340A JPS5732340A (en) | 1982-02-22 |
JPS5847460B2 true JPS5847460B2 (en) | 1983-10-22 |
Family
ID=14459037
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55107434A Expired JPS5847460B2 (en) | 1980-08-05 | 1980-08-05 | Zinc recovery equipment for zinc dust |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5847460B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0360630B2 (en) * | 1985-04-02 | 1991-09-17 | Daifuku Kk |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0587166U (en) * | 1991-07-31 | 1993-11-22 | 三宝産業株式会社 | Grave front equipment |
-
1980
- 1980-08-05 JP JP55107434A patent/JPS5847460B2/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0360630B2 (en) * | 1985-04-02 | 1991-09-17 | Daifuku Kk |
Also Published As
Publication number | Publication date |
---|---|
JPS5732340A (en) | 1982-02-22 |
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