JPS6045260B2 - Zinc recovery equipment for zinc dust - Google Patents

Zinc recovery equipment for zinc dust

Info

Publication number
JPS6045260B2
JPS6045260B2 JP56043324A JP4332481A JPS6045260B2 JP S6045260 B2 JPS6045260 B2 JP S6045260B2 JP 56043324 A JP56043324 A JP 56043324A JP 4332481 A JP4332481 A JP 4332481A JP S6045260 B2 JPS6045260 B2 JP S6045260B2
Authority
JP
Japan
Prior art keywords
zinc
zinc dust
dust collection
hollow shaft
furnace
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
Application number
JP56043324A
Other languages
Japanese (ja)
Other versions
JPS57158338A (en
Inventor
健三 福本
杲平 野下
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 Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP56043324A priority Critical patent/JPS6045260B2/en
Publication of JPS57158338A publication Critical patent/JPS57158338A/en
Publication of JPS6045260B2 publication Critical patent/JPS6045260B2/en
Expired 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

  • Muffle Furnaces And Rotary Kilns (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 この発明は、製鉄所て鋼材への亜鉛めつき工程て発生す
る亜鉛ダストから亜鉛を回収するための亜鉛回収装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a zinc recovery device for recovering zinc from zinc dust generated during the process of galvanizing steel materials at a steelworks.

鋼材に対する防食用被覆法のなかで亜鉛の果す役割はき
わめて大きく、現在溶融亜鉛めつき、又は電気亜鉛めつ
きが広く行われている。
Zinc plays an extremely important role in anticorrosion coating methods for steel materials, and hot-dip galvanizing or electrolytic galvanizing is currently widely used.

この亜鉛めつきに伴にめつき工程中に多量の亜鉛ダスト
が。発生する。この亜鉛ダストは多量の亜鉛を含むため
、従来はサイクロンあるいはバグフイルターで捕集して
亜鉛再生業者に売却していた。
A large amount of zinc dust is generated during the galvanizing process. Occur. Since this zinc dust contains a large amount of zinc, it has traditionally been collected using cyclones or bag filters and sold to zinc recyclers.

亜鉛再生業者は、亜鉛ダストをブリケツトマシーン、タ
ブレットマシン、プレス等で固形化し、これを溶解槽て
再溶解して亜鉛を回収する成形回収法、亜鉛ダストを硫
酸液に溶かして亜鉛を精製回収する湿式回収法、又は亜
鉛ダストを電解液中に入れ、電気分解して亜鉛を回収す
る電解式回収法のいずれかにより金属亜鉛として再製し
ていた。
Zinc recyclers use a molding recovery method in which zinc dust is solidified using a briquette machine, tablet machine, press, etc., and then remelted in a melting tank to recover the zinc, and zinc dust is purified and recovered by dissolving it in a sulfuric acid solution. Metallic zinc has been remanufactured using either a wet recovery method, or an electrolytic recovery method, in which zinc dust is placed in an electrolytic solution and electrolyzed to recover zinc.

しかし、前者は回収率が悪く、又不純物を含んだまま成
形するため比重が小さく再使用時にめつき槽で浮上して
溶解しにくい。後者は良質の亜鉛を回収できるが、コス
トが高くつく欠点がある。この発明は、かかる欠点を除
くとともに、自社で精製回収して亜鉛めつき用に再使用
することにより、亜鉛めつきコストの低減を図るための
亜鉛ダストの亜鉛回収装置を提案するものである。すな
わち、この発明は、サイクロン等の同党分離装置を内設
し、かつ中空軸で軸支して駆動装置により回転する回転
炉体と、その炉体外周面に沿つて設けた加熱装置からな
る回転溶解炉の溶融亜鉛取出し口を有しない側の中空軸
に、亜鉛ダスト収集装置及び亜鉛ダストと不活性ガスの
混合器からなる亜鉛ダスト供給装置の上記混合器に接続
した供給配管の先端を気密に挿着し、他方の中空軸に、
上記亜鉛ダスト収集装置に接続した亜鉛ダスト収集ダク
トの配管途中に接続した排出配管の先端を気密に挿着し
た亜鉛ダストの亜鉛回収装置を要旨とする。この発明は
亜鉛めつき工程で発生する亜鉛グス卜を窒素又はアルゴ
ン等の不活性ガスを媒体として移送し、かつ炉内に不活
性ガスを充満して非酸化雰囲気のもとに、亜鉛ダストを
溶解処理して亜鉛を回収するためのものであるから配管
及び回転溶解炉は閉回路で接続することが望ましい。
However, the former has a poor recovery rate, and because it is molded with impurities still in it, it has a low specific gravity and floats up in the plating bath when it is reused, making it difficult to dissolve. Although the latter can recover high quality zinc, it has the disadvantage of high cost. This invention proposes a zinc recovery device for zinc dust that eliminates these drawbacks and reduces the cost of galvanizing by refining and recovering the zinc dust in-house and reusing it for galvanizing. That is, this invention consists of a rotary furnace body which is equipped with a combustible separation device such as a cyclone, is rotatably supported by a hollow shaft and rotated by a drive device, and a heating device provided along the outer circumferential surface of the furnace body. Airtightly connect the tip of the supply pipe connected to the above-mentioned mixer of the zinc dust supply device, which consists of a zinc dust collection device and a mixer of zinc dust and inert gas, to the hollow shaft of the rotary melting furnace on the side that does not have a molten zinc outlet. and the other hollow shaft.
The gist of this invention is a zinc recovery device for zinc dust, in which the tip of a discharge pipe connected to the middle of the piping of a zinc dust collection duct connected to the zinc dust collection device is airtightly inserted. This invention transfers the zinc gas generated in the galvanizing process using an inert gas such as nitrogen or argon, and fills the furnace with the inert gas to generate zinc dust in a non-oxidizing atmosphere. Since the purpose is to recover zinc by melting, it is desirable that the piping and rotary melting furnace be connected in a closed circuit.

又亜鉛ダスト収集装置は、サイクロンやバグフイルター
等を使い、かつその複数を直列して微粒ダストをも十分
に収集できるようにすることが望ましい。次に、この発
明を鋼管亜鉛めつき処理に実施した場合を図面について
説明する。
Further, it is desirable that the zinc dust collecting device uses a cyclone, a bag filter, etc., and a plurality of them are connected in series to be able to sufficiently collect fine dust. Next, a case in which the present invention is applied to steel pipe galvanizing treatment will be explained with reference to the drawings.

回転溶解炉1は、横置き円筒体の両端面中心に突設した
中空軸2〜2を回転自在に軸支し、一方の中空軸2には
歯車3が外嵌されており、駆動装置5の主軸に設けた歯
車4に噛合しており、駆動装置5の作動により回転する
回転炉体6と、炉体外周面に間隔をおいてかぶせた外筒
7に設けたバーナー等を挿着した加熱装置8よりなり、
炉体内にはサイクロンからなる固気分離装置9を内設し
、かつ一方の端面には溶融亜鉛取出し口10を設けてな
る。
The rotary melting furnace 1 rotatably supports hollow shafts 2 to 2 protruding from the centers of both end faces of a horizontally placed cylindrical body, and a gear 3 is externally fitted to one of the hollow shafts 2. A rotary furnace body 6 is meshed with a gear 4 provided on the main shaft of the rotary furnace body 6 and rotates by the operation of a drive device 5, and a burner etc. provided on an outer cylinder 7 that is placed over the outer peripheral surface of the furnace body at intervals is inserted. Consisting of a heating device 8,
A solid-gas separator 9 consisting of a cyclone is installed inside the furnace body, and a molten zinc outlet 10 is provided on one end face.

上記回転溶解炉1は、亜鉛めつき槽24に近接して設置
[2、回収した溶融亜鉛を取出し口10から直接槽内に
装入できるようにする。
The rotary melting furnace 1 is installed close to the galvanizing tank 24 [2, so that recovered molten zinc can be directly charged into the tank from the outlet 10.

そして、亜鉛めつき槽24の近傍にめつき鋼管30の内
面ブロー装置25を設け、蒸気又は不活性ガスのアキュ
ムレータ26から送出される蒸気又は不活性ガスで管内
面の清浄化を行うようにする。一方サイクロン又はバグ
フイルタからなる亜鉛ダスト収集装置11,12を直列
し上記内面ブロー装置25との間を亜鉛ダスト収集ダク
ト22で接続し、排風機13の吸引作用により亜鉛ダス
トを収集できるように設ける。亜鉛ダスト収集装置11
,12には、それぞれ不活性ガスと混合するための混合
器14,15が.接続されて亜鉛ダスト供給装置16が
構成される。そして、各混合器14,15の底には送入
配管17の二また分岐部を接続し、配管先端は取出し口
10を有しない側の中空軸2より炉内に気密に挿着、又
不活性ガスアキュムレータ18と各混・合気14,15
及び各配管分岐部との間を開閉弁19を有する供給管2
0,21で接続する。一方取出し口10を有する側の中
空軸2には亜鉛ダスト収集ダクト22に接続した排出配
管23の先端を気密に挿着する。図中31は送風機、2
7は亜鉛ダスト収集装置11,12と混合器14,15
の間に設けた止弁、28は送入配管17の各分岐部に設
けた止弁、29は排出配管23に設けた止弁、30はめ
つき鋼管である。今上記装置において、めつき処理され
ためつき鋼管30を内面ブロー装置25に取付け、排風
機13及び内面ブロー装置25を作動して管内に蒸気を
吹込む。
Then, an inner surface blowing device 25 for the galvanized steel pipe 30 is provided near the galvanizing tank 24, and the inner surface of the pipe is cleaned with steam or inert gas sent from the steam or inert gas accumulator 26. . On the other hand, zinc dust collection devices 11 and 12 consisting of cyclones or bag filters are connected in series and connected to the inner surface blowing device 25 through a zinc dust collection duct 22, so that zinc dust can be collected by the suction action of an exhaust fan 13. Zinc dust collection device 11
, 12 have mixers 14 and 15 for mixing with inert gas, respectively. A zinc dust supply device 16 is configured by being connected. A bifurcated branch of the feed pipe 17 is connected to the bottom of each mixer 14, 15, and the tip of the pipe is airtightly inserted into the furnace from the hollow shaft 2 on the side that does not have the outlet 10. Active gas accumulator 18 and each mixture/aiki 14, 15
and a supply pipe 2 having an on-off valve 19 between each pipe branch part.
Connect with 0,21. On the other hand, the tip of a discharge pipe 23 connected to a zinc dust collection duct 22 is airtightly inserted into the hollow shaft 2 on the side having the outlet 10. In the figure, 31 is a blower, 2
7 is a zinc dust collection device 11, 12 and a mixer 14, 15
28 is a stop valve provided at each branch of the feed pipe 17, 29 is a stop valve provided in the discharge pipe 23, and 30 is a fitted steel pipe. Now, in the above-mentioned apparatus, the plated steel pipe 30 is attached to the internal blowing device 25, and the exhaust fan 13 and the internal blowing device 25 are operated to blow steam into the pipe.

すると発生した亜鉛ダストは吸引さ゛れて亜鉛ダスト収
集装置11,12にいたる。こ)で、まずサイクロンで
大方の亜鉛ダストが補足され、残つた微粒亜鉛ダストは
次のバグフイルタで補足され、ほ〜全部の亜鉛ダストが
収集される。収集された亜鉛ダストが量的にまとまれば
、止弁27を開いて混合器14,15に切出し、開閉弁
19を開いて不活性ガスを送入して混合する。
Then, the generated zinc dust is sucked and reaches the zinc dust collection devices 11 and 12. In this step, most of the zinc dust is first captured by the cyclone, and the remaining fine particles of zinc dust are captured by the next bag filter, and almost all of the zinc dust is collected. When the collected zinc dust is concentrated in quantity, the stop valve 27 is opened to cut it into the mixers 14 and 15, and the on-off valve 19 is opened to feed inert gas and mix it.

そして、止弁28を開いて不活性ガスと亜鉛ダストの混
合物を回転溶解炉1に送入する。予め加熱装置8により
加熱され、駆動装置の駆動により回転している回転溶解
炉1に送入された亜鉛ダストは不活性ガス雰囲気のなか
で、固気分離装置9により分離され、回転している炉壁
及びすでに溶解している亜鉛浴にひんぱんに接触しなが
ら速かに加熱溶解する。
Then, the stop valve 28 is opened to feed the mixture of inert gas and zinc dust into the rotary melting furnace 1. Zinc dust is heated in advance by a heating device 8 and fed into the rotary melting furnace 1, which is rotated by the drive of a drive device, and is separated by a solid-gas separator 9 and rotated in an inert gas atmosphere. It is rapidly heated and melted while frequently contacting the furnace wall and the already melted zinc bath.

回転溶解炉の回転の仕方は90に〜180す程度の往復
揺動が好ましい。上記亜鉛ダスト供給装置16から回転
溶解炉1への亜鉛ダストの供給は間歇的に行われるが、
止弁28を閉止し亜鉛ダストの供給を停止している間は
供給管21の止弁19を開いてアキユムータより不活性
ガスを炉内に送入しながら非酸化雰囲気を保持しながら
操業する。又炉内では送入側より取出し側へ進むに従つ
て溶融亜鉛がたまるが、適当にたまつたとき取出し口1
0が図に示す想像線位置に来たとき炉を止め、取出し口
10を開いて溶融亜鉛を亜鉛めつき槽24内に装入する
It is preferable that the rotary melting furnace rotates in a reciprocating manner of about 90 to 180 degrees. Although the supply of zinc dust from the zinc dust supply device 16 to the rotary melting furnace 1 is performed intermittently,
While the stop valve 28 is closed and the supply of zinc dust is stopped, the stop valve 19 of the supply pipe 21 is opened and inert gas is fed into the furnace from the accumulator, and the furnace is operated while maintaining a non-oxidizing atmosphere. Also, in the furnace, molten zinc accumulates as it progresses from the inlet side to the outlet side, and when it accumulates appropriately, the outlet 1
0 reaches the phantom line shown in the figure, the furnace is stopped, the outlet 10 is opened, and molten zinc is charged into the galvanizing tank 24.

そして炉内に未溶解の亜鉛ダストが存在するときは止弁
29を開いて排出配管23より亜鉛ダスト収集ダクト2
2を経て、亜鉛ダスト供給装置16にもどす。
When undissolved zinc dust exists in the furnace, the stop valve 29 is opened and the zinc dust collection duct 2 is discharged from the discharge pipe 23.
2 and then returned to the zinc dust supply device 16.

この発明は、固気分離装置を有する回転溶解炉と、これ
に亜鉛ダストを不活性ガスと混合して連続的に或は間歇
的に供給する亜鉛ダスト供給装置からなるため、収集し
た亜鉛ダストを非酸化雰囲気中で能率よく回収し、か溶
融亜鉛のまま亜鉛めつき槽に装入できるため、亜鉛めつ
きのコストをも低減できる。
This invention consists of a rotary melting furnace having a solid-gas separator and a zinc dust supply device that mixes zinc dust with an inert gas and supplies it continuously or intermittently. Since it can be efficiently recovered in a non-oxidizing atmosphere and charged into the galvanizing tank as molten zinc, the cost of galvanizing can also be reduced.

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

第1図はこの発明の実施例における装置の概略を示す説
明図である。 図中1・・・・・・回転溶解炉、2・・・・・・中空軸
、5・・・・・駆動装置、6・・・・・・回転炉体、7
・・・・・・外筒、8・・・・加熱装置、9・・・・・
・固気分離装置、10・・・・・・取出し口、11,1
2・・・・・・亜鉛ダスト収集装置、14,15・・・
・・混合器、16・・・・・・亜鉛ダスト供給装置、1
7・・・・・・送入配管、18・・・・・・不活性ガス
アキュムレータ、23・・・・・排出配管、25・・・
・・・内面ブロー装置、26・・・・・・蒸気又は不活
性ガスのアキュムレータ。
FIG. 1 is an explanatory diagram showing an outline of an apparatus in an embodiment of the present invention. In the figure, 1...Rotary melting furnace, 2...Hollow shaft, 5...Drive device, 6...Rotary furnace body, 7
...Outer cylinder, 8...Heating device, 9...
・Solid-gas separator, 10... Outlet, 11, 1
2... Zinc dust collection device, 14, 15...
...Mixer, 16...Zinc dust supply device, 1
7...Inlet piping, 18...Inert gas accumulator, 23...Discharge piping, 25...
. . . Internal blowing device, 26 . . . Steam or inert gas accumulator.

Claims (1)

【特許請求の範囲】[Claims] 1 サイクロンからなる固気分離装置を内設し、かつ中
空軸で軸支して駆動装置で回転する回転炉体と、その炉
体外周面に沿つて設けた加熱装置からなる回転溶解炉の
溶融亜鉛取出し口を有しない側の中空軸に、亜鉛ダスト
収集装置及び亜鉛ダストと不活性ガスの混合器からなる
亜鉛ダスト供給装置の上記混合器に接続した供給配管の
先端を気密に挿着し、他方の中空軸に、上記亜鉛ダスト
収集装置に接続した亜鉛ダスト収集ダクトの配管途中に
接続した排出配管の先端を気密に挿着した亜鉛ダストの
亜鉛回収装置。
1. Melting in a rotary melting furnace consisting of a rotary furnace body equipped with a solid-gas separator consisting of a cyclone, supported by a hollow shaft and rotated by a drive device, and a heating device installed along the outer circumferential surface of the furnace body. The tip of the supply pipe connected to the mixer of the zinc dust supply device consisting of a zinc dust collection device and a mixer of zinc dust and inert gas is airtightly inserted into the hollow shaft on the side that does not have a zinc outlet, A zinc recovery device for zinc dust, in which the tip of a discharge pipe connected to the middle of the piping of a zinc dust collection duct connected to the zinc dust collection device is airtightly inserted into the other hollow shaft.
JP56043324A 1981-03-24 1981-03-24 Zinc recovery equipment for zinc dust Expired JPS6045260B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56043324A JPS6045260B2 (en) 1981-03-24 1981-03-24 Zinc recovery equipment for zinc dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56043324A JPS6045260B2 (en) 1981-03-24 1981-03-24 Zinc recovery equipment for zinc dust

Publications (2)

Publication Number Publication Date
JPS57158338A JPS57158338A (en) 1982-09-30
JPS6045260B2 true JPS6045260B2 (en) 1985-10-08

Family

ID=12660628

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56043324A Expired JPS6045260B2 (en) 1981-03-24 1981-03-24 Zinc recovery equipment for zinc dust

Country Status (1)

Country Link
JP (1) JPS6045260B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE187986T1 (en) * 1995-04-25 2000-01-15 Jarkko Linnainmaa INSTALLATION FOR METAL SCRAP TREATMENT

Also Published As

Publication number Publication date
JPS57158338A (en) 1982-09-30

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