JPS59500008A - Method and apparatus for submerging, conveying, melting and circulating metal charges in a molten medium - Google Patents
Method and apparatus for submerging, conveying, melting and circulating metal charges in a molten mediumInfo
- Publication number
- JPS59500008A JPS59500008A JP82501103A JP50110382A JPS59500008A JP S59500008 A JPS59500008 A JP S59500008A JP 82501103 A JP82501103 A JP 82501103A JP 50110382 A JP50110382 A JP 50110382A JP S59500008 A JPS59500008 A JP S59500008A
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- Prior art keywords
- melting
- tank
- molten metal
- medium
- molten
- 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
Links
- 229910052751 metal Inorganic materials 0.000 title claims description 91
- 239000002184 metal Substances 0.000 title claims description 91
- 230000008018 melting Effects 0.000 title claims description 63
- 238000002844 melting Methods 0.000 title claims description 62
- 238000000034 method Methods 0.000 title claims description 18
- 238000010438 heat treatment Methods 0.000 claims description 50
- 229910052782 aluminium Inorganic materials 0.000 claims description 25
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 25
- 238000012423 maintenance Methods 0.000 claims description 16
- 239000012530 fluid Substances 0.000 claims description 9
- 238000005192 partition Methods 0.000 claims description 8
- 230000003134 recirculating effect Effects 0.000 claims description 7
- 230000032258 transport Effects 0.000 claims description 7
- 230000009471 action Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 3
- 239000010931 gold Substances 0.000 claims description 3
- 229910052737 gold Inorganic materials 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000007790 scraping Methods 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims 2
- 238000004891 communication Methods 0.000 claims 1
- 230000000977 initiatory effect Effects 0.000 claims 1
- 239000000155 melt Substances 0.000 claims 1
- 239000011800 void material Substances 0.000 claims 1
- 239000000463 material Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000004907 flux Effects 0.000 description 4
- 239000011819 refractory material Substances 0.000 description 4
- 210000003746 feather Anatomy 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000010309 melting process Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 239000003923 scrap metal Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 241000723346 Cinnamomum camphora Species 0.000 description 1
- 241001676573 Minium Species 0.000 description 1
- 244000061458 Solanum melongena Species 0.000 description 1
- 235000002597 Solanum melongena Nutrition 0.000 description 1
- 229960000846 camphor Drugs 0.000 description 1
- 229930008380 camphor Natural products 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000009419 refurbishment Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/0084—Obtaining aluminium melting and handling molten aluminium
- C22B21/0092—Remelting scrap, skimmings or any secondary source aluminium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B9/00—General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
- C22B9/16—Remelting metals
-
- 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
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるため要約のデータは記録されません。 (57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】 溶融し、循環する方法および装置 技術分野 この発明は、金属装入物を溶融媒体内に沈漬し、搬送し、溶融し、再循環するた めの改良された方法と装置に関するものである。[Detailed description of the invention] Method and apparatus for melting and circulating Technical field This invention provides a method for submerging, transporting, melting and recycling metal charges in a melting medium. This invention relates to an improved method and apparatus for.
背景技術 大きな表面積対体積比を有するスクラップアルミニウムの再生においてはスクラ ップが溶融アルミニウムの表面に浮遊するようになる。沈降に抵抗するスクラッ プの存在は、アルミニウム再生処理装置に大小の不都合をもたらす。アルミニウ ムの再生方法の改良全役けるよう大量生産が主要な資源に制限されないことは、 再生処理装置の加熱および溶融相を介して溶融アルミニウムをポンプ供給する再 生処理装置に対して太いに不都合な形状にされるうこの様な処理装置は作用的な 配置状況の簡単にすべき引き込みにみられる。ポンプ羽根車を取囲む特別に形づ くられた壁や、或l−1:@融金属と一緒にスクラップがポンプに送られる容積 全形成する壁と協同するように正確につくられるポンプ?耐火材でつくるのに非 常に冒価につくことが言われている。ポンプを取囲んで収容する壁は耐火材でつ くられる。この(,2) 様な壁の製作、形成および管理には相当に費用がか\る。管理に関しては、再生 が行われる工場環境は、炉に装入される材料の乱暴な取扱いに関する限りは不都 合である。処理装置の装入と続いての清掃は壁に損傷を与える。この損傷は、ポ ンプの個所の正確につくられた壁面が含まれるときに特に取換えが高価につく。Background technology Scrap aluminum has a large surface area-to-volume ratio. The chips become suspended on the surface of the molten aluminum. Scraps that resist settling The presence of aluminum pipes causes major and minor inconveniences in aluminum reprocessing equipment. aluminum The fact that mass production is not limited to primary resources is essential to improving methods of recycling materials. A recycler that pumps molten aluminum through the heating and melt phase of the recycler. The processing equipment, which is thick and has an inconvenient shape compared to the raw processing equipment, is not effective. It is seen that the placement situation should be easy to attract. Specially shaped surrounding the pump impeller A collapsed wall or a volume where scrap is sent to the pump together with molten metal. A pump precisely made to cooperate with a full-forming wall? Although it is made of fireproof material, it is It is said that there is always a risk. The walls surrounding and housing the pump are made of fireproof material. I can't believe it. This(,2) The production, formation and maintenance of such walls can be quite expensive. Regarding management, playback The factory environment in which the This is the case. Loading the processing equipment and subsequent cleaning can cause damage to the walls. This damage Replacement is particularly expensive when precisely constructed walls are involved in the area of the pump.
構成と丁度説明した取換が高価につくことは、費用のために少しの再生に対し不 都合な手引きをもたらす。The construction and just-described replacements are expensive, making some refurbishments ineffective due to cost. Provide convenient guidance.
処理装置に装入されるスクラップ中に鋼のような非アルミニウムスクラップの不 用意な包含物があるときに、ポンプの詰りの問題の異常な発生がない。非アルミ ニウムスクラップはポンプ羽根車と、このポンプ羽根車全取囲む協同する壁との 間に入って羽根車を停止するようになる。この様な羽根車の停止が起るときには 、壁とポンプ羽根車はしばしば損傷される、丁度説明した型式のポンプ羽根車と 周囲の壁の設計に関して技術が如何に進展したかの例がパン・リンデンの米国特 許第3,977、、E J A号や同第t、lコJll/夕号、クラクストン等 の米国特許第3.9g’l、23Q号明細書に見出すことができる。これら特許 は本質的に自己沈下しないスクラップを沈漬する問題金認めて処理している。更 に、これらの特許は溶融アルミニウムの表面に表われるスキムの間@を認めて処 理するよう試みている。アルミニウム溶融処理におけるスキムやドロス、と叶ぶ ことができる、の成形は、主に酸化アルミニラ特表昭59−500008 (3 ) ムであるスキムがアルミニウムの大きな反応特性や高温の溶融金属の存在によシ 強調される雰囲気にもとづいて迅速に形成されることによる特に不都合な問題で ある。上述の各米国特許におけるポンプ羽根車は、ポンプ作用を高めるか或はポ ンプにスクラップを運ぶ溶融アルミニウムを案内する′ようになすポンプ羽根車 と協同する壁に近接して配置される。上述の特許にても考えられるポンプ羽根車 の詰りゃスキム発生等の問題は避けられなかった。これは特にアルミニウムと同 一比重をもった耐火材料の様な非溶融性の材料の部片が溶融金属中に流れ込んで 処理装置のポンプ部分に送られるときに詰りか実際に起る。Contains non-aluminum scrap such as steel in the scrap charged to the processing equipment. When there is a ready inclusion, there is no unusual occurrence of pump clogging problems. non-aluminum The aluminum scrap is attached to the pump impeller, and the cooperating wall that surrounds this entire pump impeller. The impeller will be stopped in time. When such impeller stoppage occurs, , walls and pump impellers are often damaged, with pump impellers of the type just described. An example of how technology has advanced in the design of perimeter walls is Pan Linden's US special. No. 3,977, E J A No. t, l co Jll/Evening No., Claxton, etc. No. 3.9g'l, 23Q. These patents The problem of submerging scrap that essentially does not self-sink is being handled in an acknowledged manner. Change These patents recognize and treat the skim that appears on the surface of molten aluminum. I'm trying to understand. Eliminates skim and dross in aluminum melting process The molding process is mainly done using aluminum oxide special table 1985-500008 (3 ) Due to the highly reactive properties of aluminum and the presence of high-temperature molten metal, the skim Particularly inconvenient problems due to the rapid formation of an atmosphere that emphasizes be. The pump impellers in each of the above-mentioned U.S. patents either enhance pumping action or Pump impeller designed to guide molten aluminum transporting scrap to the pump placed close to a wall that cooperates with the Pump impeller also considered in the above patent Problems such as skimming were unavoidable if the pipes were clogged. This is especially true for aluminum A piece of non-melting material, such as a refractory material with a specific gravity, flows into the molten metal. The blockage actually occurs when it is delivered to the pump section of the processing equipment.
特に、この発明は、自己沈下できない部片から成るアルミニウムスクラップを沈 潰し 搬送し、溶融し、循環する方法および装置に係わるものである。この発明 の溶融装置は、加熱された溶融金属の流入点の下の点にて溶融金属の表面の下に 沈漬された溶融金属スクラップ搬送確環器の作用により溶融金属の表面の下の流 入点から引き入れられる加熱された@融金属を有する開放槽にスクラップの供給 を導く手段を備えている。In particular, this invention sinks aluminum scrap consisting of pieces that cannot self-sink. It concerns a method and apparatus for crushing, conveying, melting, and circulating. this invention The melting equipment of The action of a submerged molten metal scrap conveyor causes a flow below the surface of the molten metal. Feed of scrap into an open tank with heated molten metal drawn from the entry point It has the means to guide
循環器はスクラップを含む加熱された溶融金属をイ盾環器内に連続的に引き込み 、こ\でスクラップは溶融金属中に完全に運び入れられて溶融金属循環通路内に 送り出され、そこで循環器への再循環物を続いて加熱溶(弘 ) 融すべく溶融金属内に運ばれるスクラップ金属を送り出す。The circulator continuously draws heated molten metal, including scrap, into the circulator. , where the scrap is completely carried into the molten metal and placed in the molten metal circulation path. The recirculated material is sent to the circulatory system, where it is then heated and melted (Hiro). Dispense scrap metal that is carried into the molten metal to be melted.
以下に十分に説明されるこの発明は、従来技術における羽根車に近接した壁の必 要を完全に除去すると共に、スキム形成の同時的減少と一緒に溶融金属へのスク ラップの搬送を同時に設けている。The present invention, which will be fully described below, overcomes the need for walls proximate to the impeller in the prior art. completely eliminates the risk of scraping into molten metal with a simultaneous reduction in skim formation. Wrap transport is also provided at the same time.
従って、この発明の主な目的は、自己沈漬できないことにて特徴づけられるアル ミニウムスクラップを沈潰し、搬送し、溶融し、循環するための安価な方法と装 置を提供することにある。Therefore, the main object of this invention is to An inexpensive method and equipment for sinking, transporting, melting and circulating minium scrap. The aim is to provide a
この発明の別の目的は、自己沈降しないスクラップを溶融金属に引き入れて溶融 する状態に溶融金属媒体と協同する溶融金属循環器を設けることにある。Another object of this invention is to draw non-self-sedimenting scrap into molten metal and melt it. A molten metal circulator is provided which cooperates with the molten metal medium in such a manner that the molten metal medium is in contact with the molten metal medium.
この発明の他の目的−は、溶融金属媒体と垂直に設けられた壁とに協同し、これ によって溶融装置全通って溶融金属が移動すべく流体流通路がなす溶融金属媒体 に流体流通路を形成する溶融金属循環器を備えた溶融−表置を提供することにあ る。Another object of the invention is to co-operate the molten metal medium with a vertically disposed wall; A molten metal medium with fluid flow paths for moving molten metal throughout the melting apparatus. To provide a melting surface with a melting metal circulator forming a fluid flow path in the Ru.
この発明の更に別の目的は、構造が筒型で掃除および保守が簡単であるflおよ び溶融省属保持槽を提供することにある。Yet another object of the invention is to provide fl and and to provide a melting and metal-saving holding tank.
この発明の他の目的や利点・・ま以下に示される象付図面に沿っての詳細な説明 から明かになろう。Other objects and advantages of the invention are detailed below with reference to the illustrated drawings. Let's find out from.
第1図はこの発明を実施した再循環スクラップ溶融装置の概要図、第2図はこの 発明の推奨実施例における溶融装置の平面図、第3図は第2図の3−3碗に沿っ た断面図、第4図は第一図の<c −lI線に沿った断面図、第5図は溶融金属 スクラップ搬送循環器の斜視図、第6図は第S図の6−6線に沿った断面図、第 7図はこの発明を実施した炉、維持槽および溶融媒体循環装置の平面図、第g図 は第7図のt−r殊に沿った断面図、第9図は第7図の9−94に沿った断面図 である。Figure 1 is a schematic diagram of a recirculating scrap melting device that implements this invention, and Figure 2 is a schematic diagram of the recirculating scrap melting equipment that implements this invention. A plan view of the melting apparatus in the preferred embodiment of the invention, FIG. 3 is taken along the line 3-3 of FIG. Figure 4 is a cross-sectional view taken along the <c-lI line in Figure 1, Figure 5 is a cross-sectional view of molten metal. FIG. 6 is a perspective view of the scrap conveying circulator, and FIG. 6 is a sectional view taken along line 6-6 in FIG. Figure 7 is a plan view of the furnace, maintenance tank, and molten medium circulation device in which this invention is implemented, and Figure g. is a cross-sectional view taken along line tr in FIG. 7, and FIG. 9 is a cross-sectional view taken along line 9-94 in FIG. It is.
第1図全いま参照するに、同図にはこの発明’t+施した再循環スクラップ溶融 装置がブロック図で示されている。この再循環スクラップ溶融装置は閉@別熱槽 l/と開放槽/2f有している。開放槽12にはスクラップとフラックスが導入 される。開放槽12内に設けられる後に詳しく述べられるスクラップ搬送@融金 属・盾壇器は閉鎖加熱styから矢印13により示される様に開放槽lλ内に溶 融金属を盾環するようにする。Referring now to FIG. 1, this figure shows the invention't + recirculating scrap melting process. The apparatus is shown in block diagram form. This recirculating scrap melting equipment is closed @separate heat tank It has 1/2 f and an open tank/2 f. Scrap and flux are introduced into open tank 12. be done. Scrap conveyance @ financing provided in the open tank 12 and described in detail later The metal and shield vessels are melted in the open tank lλ as shown by arrow 13 from the closed heating sty. Make it a shield ring for molten metal.
溶融金属はそこで矢印/4’により示される様に閉鎖加熱槽12内に確穣される 。スクラップとフラックスは矢印/6により示される様に開放槽12の一端に導 入され、スキムすなわち金くそが矢印17により示される様に開放槽/2の反対 の端から除去される。再循環スクラップ溶融装置の首長製品は矢印15により示 される様に開鎖加熱st/から放出されるスキムのない#融アルミニウムである 。The molten metal is then deposited in a closed heating tank 12 as indicated by arrow /4'. . The scrap and flux are led to one end of the open tank 12 as shown by arrow /6. The skim or gold waste is placed in the opposite direction of open tank/2 as shown by arrow 17. removed from the edge. The principal product of the recirculating scrap melter is indicated by arrow 15. It is #molten aluminum without skim released from open chain heating st/ as shown in .
(6) 第ユ、3図に就いていま説明するに、これらの図にはこの発明の推奨実施例の詳 at示す平面図と前面図が示されている。(6) Referring now to Figures U and 3, these figures show details of a preferred embodiment of the invention. A plan view and a front view are shown.
以下の説明は同時に第2,3図の溶融装置を説明しよう。第2図には1−1鎖加 熱槽/、/と開放槽12が示される。閉鎖加熱槽//とその詳細な構造はカバー igが閉鎖加熱槽llに設けられることで普泗である。閉鎖加熱槽//と開放槽 12は・11七人材でつくられる。第3図に明示される保に、耐火材は金属被覆 /9により被われる。金属被覆/qは耐熱鋼である。一対のバーナユ1..2/ aが加熱槽//内にて下向きに示されている。バーナ、2/、21aの性質と作 用は当業者にて今日使用されているバーナと同じである。二つのバーナだけが図 示されている。バーナの配置と数は、燃焼工程に用いられる燃料の性質と有用な バーナの型式とに基づいた設計事項であることが理解されるべきである。閉鎖加 熱槽//と開放槽7.2は溶融金洟票体ノ0で構たされるよう示されており、推 奨実施例では溶融金属はアルミニウムである。The following description will simultaneously describe the melting apparatus of FIGS. 2 and 3. Figure 2 shows 1-1 chain addition. A thermal bath /, / and an open bath 12 are shown. Closed heating tank // and its detailed structure are covered It is common that the ig is provided in a closed heating tank. Closed heating tank // and open tank 12 is made up of 117 human resources. As shown in Figure 3, refractory materials are metal coated. Covered by /9. Metal coating /q is heat-resistant steel. A pair of burnayu 1. .. 2/ a is shown facing downward in the heating tank //. Properties and operation of burner, 2/, 21a The use is the same as the burners used today by those skilled in the art. Only two burners are shown It is shown. The location and number of burners depend on the nature of the fuel used in the combustion process and the useful It should be understood that this is a design matter based on the type of burner. closure The heat bath// and the open bath 7.2 are shown to be constructed of molten metal material No. 0 and are recommended. In the preferred embodiment, the molten metal is aluminum.
開放槽lコには耐火材でつくられた壁部分フコが設けられ、この壁部分コ2は閉 鎖加熱槽/lと開放槽lコの長手方向に延びる隔壁コ3に一体的に連結されてい る。開放槽12は@壁、24Iと前壁コア奮有している。閉鎖加熱槽//は後壁 λgfもっている。The open tank 1 is equipped with a wall section made of fireproof material, and this wall section 2 is closed. It is integrally connected to a partition wall 3 extending in the longitudinal direction of the chain heating tank/l and the open tank l. Ru. The open tank 12 has a @ wall, 24I and a front wall core. Closed heating tank // is rear wall It has λgf.
隔壁λ3は2つの開口:1.q、31を有している。隔1N表口Q 59−50 0008 (4)壁23と開ロコ9,3/の位置は再循環スクラップ溶融装置の 作動とこの発明全包含する方法に重要である。The partition wall λ3 has two openings: 1. q, has 31. 1N Front Exit Q 59-50 0008 (4) The position of the wall 23 and the open loco 9, 3/ of the recirculating scrap melting device It is important to the operation and method that this invention encompasses.
溶融金属スクラップ搬送循環器32は駆動軸33によりモータ3ダに連結される 。モータ3ダは速度を選択できる電動機や他の適宜なモータとすることができる 。The molten metal scrap conveying circulator 32 is connected to the motor 3 da by a drive shaft 33 . The motor 3 can be an electric motor with selectable speed or any other suitable motor. .
循環器3コが壁部分ユニと端壁ユ6の間の中間に設けられているのが理解できる 。また、開口31も、循環器32の上で且つ溶融金属媒体コθの表面35の下の 点にて壁部分ココと端壁2乙との間の中間に設けられる。循環器3コと開口31 と壁部分コニの相対位置は図示される様にこの発明の方法における最適な実施全 行う。モータ、7弘により駆動される循環器3コは溶融金属の流体流路を生じる 。矢印だけで示されるこの溶融金属流路は溶融金属を開口31全通って吸込み、 溶融金属全開放槽7.2を通り、次いで開ロッテを通って循環して閉頭加熱槽/ lに戻す。図面には示されていないが、閉鎖加熱槽//内の溶融金属の表面には スキムが殆んどならことが理解されよう。勿論、閉鎖加熱槽11の溶融金属の表 面には非常に薄い酸化膜の層がある。閉鎖加熱槽//および開放槽12の全ての 壁は耐火材にて簡単且つ安価につくられる簡単な真直ぐの垂直に設けられた壁で あることが注意されよう。用語の安価に、先に注意される今日有用な最も悪い壁 の形のスクラップ再循環装置全考慮しての相対的な用語であることをV図してい る。浴融金属スクラップ搬送循(g ) 壌器32の動的作用を以下に詳しく説明しよう。隔壁コ3の開口29#−i、下 側が閉鎖加熱槽//と開放槽lコの床36と同じ高さになるように設けられる。It can be seen that the 3 circulators are installed in the middle between the wall unit 6 and the end wall unit 6. . The opening 31 is also located above the circulator 32 and below the surface 35 of the molten metal medium θ. It is provided at a point midway between the wall part here and the end wall 2B. 3 circulatory systems and 31 openings The relative positions of the wall portions and walls are as shown for optimum implementation of the method of the present invention. conduct. Three circulators driven by a motor, 7-hiro, create a fluid flow path for molten metal. . This molten metal flow path, indicated only by an arrow, draws molten metal through the entire opening 31; The molten metal passes through the fully open tank 7.2 and then circulates through the open lot to the closed heating tank/ Return to l. Although not shown in the drawing, the surface of the molten metal inside the closed heating tank // It would be understandable if most of it was skim. Of course, the surface of the molten metal in the closed heating tank 11 There is a very thin layer of oxide on the surface. All of the closed heating tank//and open tank 12 The wall is a simple straight vertical wall that is easily and inexpensively made of fireproof material. One thing should be noted. To the term cheap, the worst wall available today is noted earlier. This is a relative term considering all types of scrap recirculation equipment. Ru. Bath molten metal scrap transport circulation (g) The dynamic operation of the rotator 32 will be explained in detail below. Opening 29#-i of partition wall 3, bottom The sides are placed at the same height as the floor 36 of the closed heating tank// and the open tank.
開口λ9の位置は、大きくて容易に沈下するスクラップ37が開放槽!2の底部 に沈んで循環器3コにより生である。実際的に言えば、スクラップ3りは底に沈 んで大半がこの静止する位置にて浴融される。The position of the opening λ9 is an open tank where the scrap 37, which is large and easily sinks, is located! bottom of 2 It sinks into the water and is alive due to the three circulatory systems. Practically speaking, scrap metal sinks to the bottom. Most of the liquid is melted in the bath at this stationary position.
第3図にては、コンベヤ3g、39により一端にて開放槽lユにスクラップ37 .II/が供給されることが容易に理解できよう。既に注意される様にコンベヤ 3g土のスクラップ3りは大きくて、その重さと形状のために自ら沈下するもの である。In Fig. 3, scrap 37 is transferred to an open tank 1 at one end by conveyors 3g and 39. .. It can be easily seen that II/ is supplied. Conveyor as already noted 3g soil scraps are large and sink by themselves due to their weight and shape. It is.
しかし、コンベヤ39は容積に対する表面積の比が大きな性質のスクラップ1I tf運ぶもので、これは自ら沈下できないものである。分断されたアルミニウム 罐や丸ごとの罐および製造工程で集められた小片は代表的な自己沈下できないス クラップである。However, the conveyor 39 is used for scrap 1I, which has a large ratio of surface area to volume. tf transport, which cannot sink by itself. segmented aluminum Cans, whole cans, and small pieces collected during the manufacturing process are typical non-self-sinking wastes. It's crap.
溶融金属コθに入れられるための自己沈下できないスクラップは、溶融金属2θ の上に形成されるスキム400層の表面張力に打勝たねばならない。Scrap that cannot self-sink to be placed in the molten metal 2θ The surface tension of the 400 layer of skim formed on top must be overcome.
自己沈下できないスクラップμlは循環−器3コによシ生じられる穏やかな洞l I2に図示される樟に供給される。激しい渦は、溶融金属内に自己沈下しないス クラップを引き入れるときに周囲の入党も洞内に引き入れて非常に不都合な副霊 物?なすスキムの形成を大いに促進するために避けられるべきである。穏ヤかな 渦a、2 Vi開口31を通りて引き入れられる溶融金属と協同して自己沈下で きないスクラップ4/i溶融金属コθ内に沈下するようなす。循環器32は説明 される動的作用によってスクラップ’J/を完全に溶融金属2θ内に運び込んで スクラップが溶融され始める。循環器3ユは運び込まれたスクラップと一緒に溶 融金属全流体流路に供給する。スクラップはそこで開放槽/、2を通る流路にお いて次続の浴融金属媒体から抽出をれる熱によって溶融され、循環する溶融媒体 の一部となる。The scrap that cannot self-sink is a gentle sinus produced by the three circulatory systems. It is fed to the camphor shown in I2. Violent vortices create a stream that does not self-sink into the molten metal. When you pull Clap in, the people around you will also be drawn into the cave, creating a very inconvenient side spirit. thing? Should be avoided to greatly encourage the formation of eggplant skims. Calm Vortex a, 2 Self-sinking in cooperation with the molten metal drawn in through the Vi opening 31 The scrap 4/i is made to sink into the molten metal θ. Circulatory system 32 explained The scrap 'J/ is completely carried into the molten metal 2θ by the dynamic action of Scrap begins to melt. The 3 units of the circulatory system were melted together with the scrap that was brought in. Supplies molten metal to all fluid channels. The scrap is then transferred to a flow path passing through an open tank/2. The circulating molten medium is melted by the heat extracted from the molten metal medium in subsequent baths. become part of.
閉鎖加熱槽itは、溶融アルミニウムのないスキムが放出される開口30を後壁 2gに有している。第3図にて、後壁ユざの開口30は、閉鎖加熱槽ll内にあ るスキムが最終の溶融金属15に入らないように浴融金属λθの表面の下の点に 位置することが理解できる。最終の溶融金属15は、開放槽lコへの固体スクラ ップの供給量と釣合った量が特別に形成された開口30を通って!;?1m加熱 槽/lから流出する。The closed heating tank it has an opening 30 in the rear wall through which skim free of molten aluminum is discharged. It has 2g. In FIG. 3, the opening 30 in the rear wall is located in the closed heating tank ll. At a point below the surface of the bath molten metal λθ to prevent the skim from entering the final molten metal 15. I can understand the location. The final molten metal 15 is sent to an open tank as a solid scrubber. Through the specially formed opening 30, a quantity commensurate with the supply of the liquid! ;? 1m heating flows out from the tank/l.
スキムの除去と浴融装置へのフラッフ剤の供給は第3図の考案によって理解でき る。フラックス供給器qlIは図示される様に穏やかな狗lコにフラックス剤ヲ 惧給するよう図示されている。The removal of skim and the supply of fluffing agent to the bath melter can be understood by the invention in Figure 3. Ru. The flux feeder qlI applies the flux agent to a gentle dog as shown in the diagram. It is illustrated to be helpful.
スキム除去は端壁21の頂部に傾斜した形の頂而、2A′i設けることによって 第3図に示される様に行われる。スキムダOが形成されて移動する溶融金属コθ の働きにより動か、されるときに、手動または図示されない自動装置によって除 去できるよう傾斜した頂面2にの上に築成されるようになる。The skim can be removed by providing an inclined apex, 2A'i, on the top of the end wall 21. This is done as shown in FIG. Molten metal θ where skimda O is formed and moves removed manually or by an automatic device not shown. It is constructed on a sloped top surface 2 so that it can be removed easily.
第4図に就いて説明するに、第1,3図に用いられたと同じ符号が同一部材全表 わすよう用いられている。To explain Fig. 4, the same reference numerals used in Figs. 1 and 3 indicate the same parts. It is used to make things worse.
溶融金属スクラップ搬送循環器32・は、溶融金属全閉鎖加熱槽iiから開口3 1全通って循環器32の中央部りOに引き入れられるように溶融金属、20に循 環器32が作用するだけでの動的作用の説明ケ容易にするために断面で示されて いる。閉鎖加熱槽/lからの溶融金属の流体流路は点線の矢印!;/、!;2で 示される。The molten metal scrap conveying circulator 32 is connected to the molten metal completely closed heating tank ii to the opening 3. 1. The molten metal is circulated through 20 so that it is drawn into the central part O of the circulator 32. The annulus 32 is shown in cross section to facilitate explanation of the dynamic action. There is. The fluid flow path of molten metal from the closed heating tank/l is indicated by the dotted arrow! ;/,! ; at 2 shown.
上方から穏やかな渦<jjに入るよう図示される自己非沈下形のスクラップ4’ /は環流中に捕えられて循環器3.2の中央部よθの開口内に吸込1れ、そこで スクラップは動いている溶融金属内に完全に引き入れられる。@環器32は、断 面にて図示される截頭円錐形のボスl17に内端にて連結された羽根33.!; ’If有する。溶融金属内に引き入札られたスクラップqlは羽根タ3.Sダに よって外方に押しやられる。at環器3コとその特別な作動の詳細Vi第S、6 図に就いての説明において十分に説明されよう。Self-submerging scrap 4' shown entering a gentle vortex from above / is caught in the reflux and sucked into the opening at θ from the center of the circulator 3.2, where it The scrap is drawn completely into the moving molten metal. @ Ring device 32 is disconnected. A vane 33 connected at its inner end to a frusto-conical boss l17 shown in plan view. ! ; 'If you have. The scrap ql drawn into the molten metal is transferred to the vane 3. To S da Therefore, it is pushed outward. Details of the three at ring devices and their special operations VI Chapter S, 6 This will be fully explained in the description of the figures.
@融金属スクラップ搬送循環器32を三次元的に示す第S図に就いていま説明し よう。循環器32は耐火材料にて、通常の技術により構成される。循環器32は 、底板ダ5および頂板’iI−と呼ぶことができるものを有している。底板l/ 、Sと頂板ダ6は図示される様に隔っておシ、一体的に固着された復数個の放射 方向に延びる羽根!;3.!r’l、!左、!;J!;’7.Kgを有している 。I will now explain Figure S, which shows a three-dimensional diagram of the molten metal scrap transport circulator 32. Good morning. The circulator 32 is constructed of refractory material and using conventional techniques. The circulatory system 32 , has what can be called a bottom plate 5 and a top plate 'iI-. Bottom plate l/ , S and the top plate 6 are separated from each other as shown in the figure, and a plurality of radiators are integrally fixed. Feathers extending in the direction! ;3. ! r’l,! left,! ;J! ;'7. has Kg .
截頭円錐形のボスlI?は底板lIsの中央に一体的に固着されている。截頭円 錐形のボスク7には図示しない手段にて駆動軸33がボスq7に固着されている 。ボスlI7の高さは底板lIsと頂板ダ乙の間の間隔よりも低い。羽根!;3 .!’I、!!r、夕A、!r7.!;gは放射方向の内端が、図示される截頭 円錐形のボスq7の底板4’5と頂板q乙の間のボスq7の外面の一点にてボス l17に一体的に固着されている。羽根sJ、s41,5B5b。A truncated conical boss lI? is integrally fixed to the center of the bottom plate IIs. truncated circle A drive shaft 33 is fixed to the boss q7 of the conical boss 7 by means not shown. . The height of the boss lI7 is lower than the distance between the bottom plate lIs and the top plate Dao. Feather! ;3 .. ! 'I,! ! r, evening A,! r7. ! ;g is the truncated radial inner end shown; The boss is located at a point on the outer surface of the boss q7 between the bottom plate 4'5 and the top plate qB of the conical boss q7. It is integrally fixed to l17. Feather sJ, s41, 5B5b.
st、rgの底部の放射方向に延びる縁部は底板ダSに同着され、羽根タ3.s ダ、!;!;、!;A、!’I、!!:の外端は図示される様に頂板グ6に固着 される。頂板’IAは中央に円形の開口qg2有しており、この開口qgは枢動 軸33の軸心と同軸をなしている。中央のこの開口lIgの内径が截頭円錐形の ボスlI7の台部の外径より大きいことが循環器32の作動において大切である 。The radially extending edges of the bottoms of st and rg are attached to the bottom plate S, and the blades 3. s Da! ;! ;、! ;A,! 'I,! ! The outer end of : is fixed to the top plate 6 as shown in the figure. be done. The top plate 'IA has a circular opening qg2 in the center, and this opening qg It is coaxial with the axis of the shaft 33. The inner diameter of this central opening lIg is truncated conical. It is important for the operation of the circulatory system 32 that the diameter be larger than the outer diameter of the base of the boss lI7. .
截頭円錐形のボスグツと底板/ISおよび頂板lI乙と協同する羽根!;3.! ;II、!!t、!t、37.!;g(D下方に傾斜した側部!;9.AO,A I、12.乙3,6qは循環器3ユの上と囲りに延びる広い吸込部分(点線で示 される)を生じるように作用する。矢印A1で示される特い流体流れは先に説明 した様に閉鎖加熱槽/Iから供給された溶融金属が自己非沈下形のスクラップと 一緒に循環器32内に引き込まれ、そこでスクラップは完全に吸込まれて先に述 べた開放槽/、20周壁に向って外方に押しやられる。A vane that cooperates with the truncated conical boss and the bottom plate/IS and the top plate! ;3. ! ;II,! ! T,! t, 37. ! ;g(D downwardly sloping side!;9.AO,A I, 12. Otsu 3 and 6q are wide suction parts (indicated by dotted lines) that extend above and around the circulatory system 3 units. act so as to cause The special fluid flow indicated by arrow A1 is explained first. As shown in the figure, the molten metal supplied from the closed heating tank/I becomes self-sinking scrap. Together they are drawn into the circulator 32, where the scrap is completely suctioned and processed as described above. Solid open tank/, 20 forced outwards towards the surrounding wall.
第2図に戻って、循環器3:lの時計方向回転によって壁部分、2−の側部7/ 、隔壁コ3、端26、前壁コクに対して圧力の築成音生じるために矢印6左、6 乙。Returning to FIG. 2, by clockwise rotation of the circulator 3:l, the wall portion, the side 7/ of the 2- , partition wall 3, end 26, arrow 6 left, 6 to cause pressure build-up against the front wall. Otsu.
6り、 1.g 、 Aデ、70によシ明らかな如く放射方向外方への流れが見 ることができる。この圧力の放出だけは壁部分、2コの端部72と前壁−17の 間に形成される開口を介してなされる。開放槽12f通って運ばれるスクラップ と溶融金属を供給し、次いで新しく溶融された3クラツプと筒りの溶融金属の組 合せにもとづく溶融金属全開口2?および閉鎖加熱槽//を経て開口31へと供 給する溶融金属媒体が流れる強い流体環流を達成するこの圧力の一定の放出がな される。開口31において、循環器3コは溶融金属を循環器3コ内に引き入れて サイクルを再び始めるようになす。循環器32は、循環器3コを取囲む壁から離 れていて循環器32と壁との間に不溶性のスクラップの大きな部片が詰まるのを 防止していることを注意するのが重要である。この種の詰りによって循環器32 −と壁に損傷を与えることが従って除去される。6ri, 1. As is clear from G, A and 70, there is a flow outward in the radial direction. can be done. This pressure is only released from the wall portions, the two ends 72 and the front wall 17. This is done through an opening formed between them. Scrap transported through open tank 12f and molten metal, and then the newly molten three-clap and barrel molten metal set. Molten metal full opening 2 based on alignment? and a closed heating tank// to the opening 31. This constant release of pressure achieves a strong fluid reflux through which the molten metal medium flows. be done. At the opening 31, the circulator 3 draws molten metal into the circulator 3. Allow the cycle to start again. The circulatory system 32 is separated from the wall surrounding the three circulatory systems. to prevent large pieces of insoluble scrap from becoming stuck between the circulator 32 and the wall. It is important to note that we are preventing This type of blockage causes the circulatory system 32 - and damage to the walls are therefore removed.
第S図の循環器3コを断面で示す第6図に就いて説明する。先に注意される・珠 に、不溶性のスクラップや耐火材の部片が溶融金属媒体中に混じって、溶融装置 金経て流動するよう設けられたどの様な装置とも接触するようKなる可能性があ るう第6図には、中央部!0の開口にひつか\りた物体73が示されている。Referring to FIG. 6, which shows a cross section of the three circulators in FIG. S, a description will be given below. Be warned first/Tama In some cases, insoluble scrap or pieces of refractory material become mixed into the molten metal medium and are removed from the melting equipment. There is a possibility that the metal may come into contact with any device installed to allow the flow of gold. In Figure 6 of Ruu, the central part! An object 73 is shown stuck in the aperture.
物体73を取除くのは簡単なことで、電動機を止めた後に溶融金属から循環器3 2を一時的に持上けて、物体73全はさみ具で取り除くだけである。この様な異 質の物体が中央の開口に入らないで頂板lI乙に当る場合例は、物体は循環器3 ユと間隔全行いた壁との曲に循環器3ユの近くに落下する。捷た、第6図の循環 器3コは図示の様に底板lI5に溝部97aが形成されていることが注意される 。この溝部グツaは、循環器3.2の異った断面の耐火鋳造物の硬化率の相違に もとづく割れを防止する。Removing the object 73 is a simple matter and removes the circulator 3 from the molten metal after the motor has been shut down. 2 is temporarily lifted and the entire object 73 is removed using scissors. This kind of difference For example, if an object hits the top plate without entering the central opening, the object is in the circulatory system 3. The circulatory system falls near the 3rd wall as it hits the wall. The cycle shown in Figure 6 is broken. It is noted that the three vessels have a groove 97a formed in the bottom plate lI5 as shown in the figure. . This groove part a is due to the difference in the hardening rate of the refractory castings of different cross sections of the circulator 3.2. Prevents cracking.
第6図の断面は、循環器3ユ全流通する溶融金属媒体の流路7#a 、りqb、 りllcを明示している。The cross section of FIG. 6 shows flow paths 7#a, riqb, and molten metal medium flowing through all three circulatory units. llc is specified.
この発明全実施した炉、維持槽および溶融媒体循環装置の頂面図を示す第7図に 就いていま説明する。溶7 融金属すなわち媒体の循環器との関係や、スクラッ プを入れて溶融するよう循環器が好適に作動する具合に就いての説明は前に行っ ている。第7.g、9図はこの発明が完全な装置にて有用性を見出すようこの発 明の別の特長を詳細に示している。FIG. 7 shows a top view of the furnace, maintenance tank, and molten medium circulation device in which this invention is fully implemented. I'll explain it now that I'm here. Molten 7 The relationship between the molten metal, that is, the medium, and the circulatory system, and the We have previously explained how the circulatory system works properly to melt the liquid. ing. 7th. Figures g and 9 illustrate this development so that the invention finds utility in a complete device. Another feature of Ming is shown in detail.
特に、閉鎖された加熱槽7sと維持槽g5が示されている。加熱槽7Sと維持槽 g!;Id:、前壁り6と後壁77とカバー7gと第1の端壁7’と第2の端壁 gθと床tyとによって形成される一t′通の室につくられて・いる。カバー7 gは第7図には示されていない。隔壁g2は、加熱槽7Sの加熱部分を維持槽g 5の維持部分から隔て\いる。隔壁gユは、加熱槽7Sと維持槽gsとの間を連 通すべく設けられた多数の通路gJ。In particular, the closed heating tank 7s and maintenance tank g5 are shown. Heating tank 7S and maintenance tank g! ;Id:, front wall 6, rear wall 77, cover 7g, first end wall 7' and second end wall It is made up of one t' chamber formed by gθ and the floor ty. cover 7 g is not shown in FIG. The partition wall g2 connects the heated portion of the heating tank 7S to the maintenance tank g. It is separated from the maintenance part of 5. The partition g-yu connects the heating tank 7S and the maintenance tank gs. A large number of passages gJ are provided to pass through.
1らff&、ざ7を有している。It has 1, ff&, and 7.
第7図に明示される様に、通路g、3.IIIは溶融媒体が加熱槽7Sから維持 槽gsに自由に流動できるようにしている。第7,1図に示される様に、通路g ba。As clearly shown in FIG. 7, passage g, 3. In III, the melting medium is maintained from the heating tank 7S. It is allowed to flow freely into tank gs. As shown in Figure 7.1, the passage g ba.
tt、gりは、加熱槽り左から維持槽g5への浴融媒体の表面上を、油またはガ ス処理器gg、gqからの燃焼、ガスが自由に流動できるようしている。燃焼ま たは煙道ガスは呼称される様に煙突ql全通って排気される。tt, g are oil or gas on the surface of the bath melting medium from the left side of the heating tank to the maintenance tank g5. The combustion gas from the gas processors gg and gq is allowed to flow freely. Burning Or flue gas is exhausted through the entire chimney ql as it is called.
加熱槽7Sには浄化傾斜部q2が設けられていて上端にギロチン形の扉q3の形 の閉鎖体がある。維持槽gsには浄化傾斜部9qとギロチン形nqSがある。The heating tank 7S is provided with a purification inclined part q2, and a guillotine-shaped door q3 is provided at the upper end. There is a closed body. The maintenance tank gs has a purification slope part 9q and a guillotine type nqS.
前壁76には、概略図示される溶融媒体用循環器9gによって循環される溶融媒 体が流れる開口96゜ヲ7がある。循環器9gは開放槽100内に設けられてい る。開放槽tOθは図示される様にす−くい取り用の傾斜部10/と壁io二を 有している。The front wall 76 contains a melting medium which is circulated by a schematically illustrated melting medium circulator 9g. There is an opening 96°7 through which the body flows. The circulator 9g is installed in the open tank 100. Ru. The open tank tOθ has an inclined part 10 for scooping and a wall io2 as shown in the figure. have.
溶融金属すなわち媒体用の注入口IO夕が第7図に示される様に設けられる。レ ールt07.tOt により支持されfc浴湯列車lle&が次の工程にて溶融 金属すなわち溶湯運搬できるように注入口10rは配置されているう加熱槽およ び維持槽周の注入口/θデが図示される様に設けられている。An inlet IO for molten metal or media is provided as shown in FIG. Re rule t07. Supported by tOt, the fc bath train lle& is melted in the next process. The injection port 10r is located between the heating tank and the molten metal. Inlet ports/θ de around the periphery of the tank and maintenance tank are provided as shown in the figure.
容器/10.///、//コはレール/ /3 、 / /41により運ばれる 。Container/10. ///, //ko are carried by rails / /3, / /41 .
ギロチン形の扉q3が開かれたときに、開口q乙。When the guillotine-shaped door q3 is opened, the opening q2.
9りと通路g3.gll、l:A、g7ffうよう容易に接近できることがこの 発明におけるギロチン形扉q3の位置として重要である。9rit passage g3. This means that gll, l: A, g7ff can be easily accessed. This is important as the position of the guillotine-shaped door q3 in the invention.
上述の説明において、この発明の溶融装置と溶融装置の操作方法が、従来有効な ものよりも簡単に且つ安価な具合に従来以上に明確な改良をなすことが大いに明 らかである。In the above description, the melting device and the method of operating the melting device of the present invention are different from conventionally effective methods. It is very clear that a clear improvement can be made more easily and cheaply than before. It is clear.
この発明の1つの実施例が図示説明されたが、この発明の精神と範囲を逸脱する ことなく種々の変形および変更ができることが当業者には明らかであろう。Although one embodiment of this invention has been illustrated and described, it departs from the spirit and scope of this invention. It will be apparent to those skilled in the art that various modifications and changes can be made without requiring any modification.
1緒0359−500008(7) 国際調査報告100359-500008 (7) international search report
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US1982/000232 WO1983002958A1 (en) | 1982-02-23 | 1982-02-23 | Method and apparatus for submerging, entraining, melting and circulating metal charge in molten media |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59500008A true JPS59500008A (en) | 1984-01-05 |
JPS6314055B2 JPS6314055B2 (en) | 1988-03-29 |
Family
ID=22167829
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP82501103A Granted JPS59500008A (en) | 1982-02-23 | 1982-02-23 | Method and apparatus for submerging, conveying, melting and circulating metal charges in a molten medium |
Country Status (2)
Country | Link |
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JP (1) | JPS59500008A (en) |
WO (1) | WO1983002958A1 (en) |
Cited By (1)
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JP2020531778A (en) * | 2017-08-28 | 2020-11-05 | ディーエス リキッド カンパニー リミテッドDs Liquid Co., Ltd. | Aluminum melting furnace |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA1226738A (en) * | 1983-03-14 | 1987-09-15 | Robert J. Ormesher | Metal scrap reclamation system |
GB9025759D0 (en) * | 1990-11-27 | 1991-01-09 | Copermill Ltd | Apparatus for melting aluminium |
GB9217802D0 (en) * | 1992-08-21 | 1992-10-07 | Cookson Aluminium Ltd | A furnace |
AT514891B1 (en) * | 2013-10-08 | 2015-06-15 | Hertwich Engineering Gmbh | Melting furnace for aluminum scrap |
KR101711362B1 (en) * | 2015-03-03 | 2017-03-02 | 윤수현 | Aluminum melting furnace |
KR101735425B1 (en) * | 2015-12-14 | 2017-05-16 | (주)디에스리퀴드 | System and method for aluminium black dross recycling |
KR102753263B1 (en) * | 2020-04-29 | 2025-01-14 | 노벨리스 인크. | Waste sedimentation devices and related processes |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3997336A (en) * | 1975-12-12 | 1976-12-14 | Aluminum Company Of America | Metal scrap melting system |
Family Cites Families (1)
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US2660525A (en) * | 1952-01-22 | 1953-11-24 | Charles B Foster | Method of extracting lead from its sulfides |
-
1982
- 1982-02-23 JP JP82501103A patent/JPS59500008A/en active Granted
- 1982-02-23 WO PCT/US1982/000232 patent/WO1983002958A1/en unknown
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3997336A (en) * | 1975-12-12 | 1976-12-14 | Aluminum Company Of America | Metal scrap melting system |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2020531778A (en) * | 2017-08-28 | 2020-11-05 | ディーエス リキッド カンパニー リミテッドDs Liquid Co., Ltd. | Aluminum melting furnace |
Also Published As
Publication number | Publication date |
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WO1983002958A1 (en) | 1983-09-01 |
JPS6314055B2 (en) | 1988-03-29 |
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