US 4,606,760 AGranted

Method and apparatus for simultaneously separating volatile and non-volatile metals

AssigneesHuron Valley Steel Corporation, Fritz Enterprises, Inc.

InventorsLeonard Fritz, Richard R. Osterberg, Richard B. Wolanski, Joseph E. Arvay

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Abstract

A method and apparatus for simultaneously separating volatile metals, including zinc and lead, and non-volatile metals, including copper, from mixtures of metallic and metallic oxide and the like materials, includes a reactor having a lower, reactor, chamber, an upper, reflux, chamber and a vertically arranged, hollow shaft interconnecting the two chambers. The shaft is substantially filled with a mixture of pieces of metallic material, having minimal oxide content, and carbonaceous material, such as coke. The reactor chamber is intensely heated by a transferred arc plasma generator to provide sufficient heat energy which together with reducing gases cause a reducing reaction and melt the non-volatile copper and other metals which form a puddle upon the floor of the reaction chamber and to form a layer of slag covering the puddle, and simultaneously to vaporize the volatile zinc, lead and the like metals. The reflux chamber is maintained at a temperature and vapor pressure suitable to condense the lead vapor, but insufficient to condense zinc vapor. Thus, condensed lead gravity flows back down the shaft through the filling for deposit in the puddle. The zinc and any other uncondensed metal vapors are removed from the upper, reflux, chamber and are condensed in an external condenser to form a commercial grade zinc product.

Claims7

Dependent claims

A method for simultaneously separating non-volatile metals and volatile metals from metal compositions including zinc, lead and copper contained in waste by-products resulting from zinc, brass and steel manufacturing processes and from low grade zinc ore, comprising:

(a) providing a reactor formed of a vertical open-ended shaft which interconnects an enlarged, lower reaction chamber having a floor and an enlarged upper chamber;
(b) continuously feeding finely pulverized metallic materials including metallic or metallic oxide zinc, lead and copper bearing materials, and carbonaceous material, and oxygen containing gas into the lower reaction chamber;
(c) periodically feeding pieces of metallic material, including zinc bearing materials, characterized by having little, if any, oxide content, and carbonaceous material, through the upper chamber and into the upper open end of the shaft to load the shaft and to maintain the loading of the shaft therewith;
(d) applying sufficient, intense plasma and electrically produced heat energy along with reducing gases in the lower chamber to reduce and vaporize metallic oxides and to melt the non-volatile metals so that they gravity flow to and form a puddle upon the lower chamber floor, and to vaporize the volatile metals and to form a slag layer that accumulates over the puddle;
(e) flowing the volatile metal vapors upwardly through the shaft and its loading and into the upper chamber, to allow for the scrubbing of the rising vapors by the descending condensed lead and provide for entrapment in the filled shaft of any particulate being mechanically carried by the ascending gases and vapors;
(f) maintaining the temperature and pressure in the upper chamber within a range that will cause lead vapors to condense into metallic lead, but which are too high to condense zinc, and thereby condensing the lead and gravity flowing the molten lead downwardly through the shaft and shaft loading to the puddle on the lower chamber floor;
(g) continuously removing the zinc and zinc chloride vapor and any other non-condensed vapors from the upper chamber and condensing such vapors outside of the reactor to form separately a commercial grade metallic zinc and a zinc chloride product;
(h) periodically tapping the lower chamber to remove molten metal from the puddle therein, and removing slag from the lower chamber.

5 more elements

A method for simultaneously producing commercial grade zinc and commercially useful copper alloys and non-toxic commercially useful slag material from waste by-products of zinc and brass and steel processes, and which by-products may contain metallic mixtures and metallic oxides, of volatile and non-volatile metals which are predominantly zinc and copper containing, comprising essentially the steps of:

(a) providing a vertically arranged reactor formed within a closed lower chamber, a closed upper chamber and a vertically elongated connecting shaft extending vertically between and opening into each chamber;
(b) filling the shaft with a mixture of pieces of metallic material characterized by having a substantial zinc content and little, if any, metallic oxide content, and a carbonaceous material, and maintaining the level of the shaft filling by periodically dropping filling material into the top of the upper chamber so that the filling falls into the top of the shaft, but without substantially changing the pressure in the upper chamber or permitting substantial flow of air into the chamber during the time that such filling material is dropped therein;
(c) feeding finely pulverized metallic and non-metallic material, which has a high zinc content, and includes copper and lead, and carbonaceous material, into the lower chamber along with an oxygen containing gas;
(d) applying an intense heat within the lower chamber along with reducing gases, sufficient to cause reduction of the oxides, melting of the copper and other non-volatile metals and vaporization of the zinc, lead and other volatile metals;
(e) forming a molten puddle of copper and any other non-volatile metals upon the floor of the lower chamber to produce a copper alloy, and simultaneously forming a molten layer of slag upon the puddle;
(f) periodically withdrawing from the reactor some of the copper alloy metal from the puddle and periodically withdrawing from the reactor slag from the molten layer of slag;
(g) flowing the reducing gases and vapors upwardly through the shaft and its filling for scrubbing and for maintaining a reduction reaction;
(h) maintaining the upper chamber at a temperature and pressure sufficient to condense the lead vapor, but insufficient to condense the zinc vapor;
(i) condensing the lead vapor so that the molten lead gravity flows back down the shaft to the puddle and tends to pick up lead carried upwardly by the vapors;
(j) removing the uncondensed vapors, which are predominantly zinc, from the upper chamber and condensing it outside the reactor to provide a commercial grade metallic zinc.

7 more elements

Dependencies are inferred from the claim text.