System for melting solid metal

Abstract

A scrap melting system and method includes a vessel that is configured to retain molten metal and a raised surface about the level of molten metal in the vessel. Solid metal is placed on the raised surface and molten metal from the vessel is moved upward from the vessel and across the raised surface to melt at least some of the solid metal. The molten metal is preferably raised from the vessel to the raised surface by a molten metal pumping device or system. The molten metal moves from the raised surface and into a vessel or launder.

Description

BACKGROUND OF THE INVENTION

As used herein, the term “molten metal” means any metal or combination of metals in liquid form, such as aluminum, copper, iron, zinc and alloys thereof. The term “gas” means any gas or combination of gases, including argon, nitrogen, chlorine, fluorine, Freon, and helium, which are released into molten metal.

Known molten-metal pumps include a pump base (also called a housing or casing), one or more inlets (an inlet being an opening in the housing to allow molten metal to enter a pump chamber), a pump chamber of any suitable configuration, which is an open area formed within the housing, and a discharge, which is a channel or conduit of any structure or type communicating with the pump chamber (in an axial pump the chamber and discharge may be the same structure or different areas of the same structure) leading from the pump chamber to an outlet, which is an opening formed in the exterior of the housing through which molten metal exits the casing. An impeller, also called a rotor, is mounted in the pump chamber and is connected to a drive system. The drive shaft is typically an impeller shaft connected to one end of a motor shaft, the other end of the drive shaft being connected to an impeller. Often, the impeller (or rotor) shaft is comprised of graphite and/or ceramic, the motor shaft is comprised of steel, and the two are connected by a coupling. As the motor turns the drive shaft, the drive shaft turns the impeller and the impeller pushes molten metal out of the pump chamber, through the discharge, out of the outlet and into the molten metal bath. Most molten metal pumps are gravity fed, wherein gravity forces molten metal through the inlet and into the pump chamber as the impeller pushes molten metal out of the pump chamber. Other molten metal pumps do not include a base or support posts and are sized to fit into a structure by which molten metal is pumped. Most pumps have a metal platform, or super structure, that is either supported by a plurality of support posts attached to the pump base, or unsupported if there is no base. The motor is positioned on the superstructure, if a superstructure is used.

This application incorporates by reference the portions of the following publications that are not inconsistent with this disclosure: U.S. Pat. No. 4,598,899, issued Jul. 8, 1986, to Paul V. Cooper, U.S. Pat. No. 5,203,681, issued Apr. 20, 1993, to Paul V. Cooper, U.S. Pat. No. 5,308,045, issued May 3, 1994, by Paul V. Cooper, U.S. Pat. No. 5,662,725, issued Sep. 2, 1997, by Paul V. Cooper, U.S. Pat. No. 5,678,807, issued Oct. 21, 1997, by Paul V. Cooper, U.S. Pat. No. 6,027,685, issued Feb. 22, 2000, by Paul V. Cooper, U.S. Pat. No. 6,124,523, issued Sep. 26, 2000, by Paul V. Cooper, U.S. Pat. No. 6,303,074, issued Oct. 16, 2001, by Paul V. Cooper, U.S. Pat. No. 6,689,310, issued Feb. 10, 2004, by Paul V. Cooper, U.S. Pat. No. 6,723,276, issued Apr. 20, 2004, by Paul V. Cooper, U.S. Pat. No. 7,402,276, issued Jul. 22, 2008, by Paul V. Cooper, U.S. Pat. No. 7,507,367, issued Mar. 24, 2009, by Paul V. Cooper, U.S. Pat. No. 7,906,068, issued Mar. 15, 2011, by Paul V. Cooper, U.S. Pat. No. 8,075,837, issued Dec. 13, 2011, by Paul V. Cooper, U.S. Pat. No. 8,110,141, issued Feb. 7, 2012, by Paul V. Cooper, U.S. Pat. No. 8,178,037, issued May 15, 2012, by Paul V. Cooper, U.S. Pat. No. 8,361,379, issued Jan. 29, 2013, by Paul V. Cooper, U.S. Pat. No. 8,366,993, issued Feb. 5, 2013, by Paul V. Cooper, U.S. Pat. No. 8,409,495, issued Apr. 2, 2013, by Paul V. Cooper, U.S. Pat. No. 8,440,135, issued May 15, 2013, by Paul V. Cooper, U.S. Pat. No. 8,444,911, issued May 21, 2013, by Paul V. Cooper, U.S. Pat. No. 8,475,708, issued Jul. 2, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 12/895,796, filed Sep. 30, 2010, by Paul V. Cooper, U.S. patent application Ser. No. 12/877,988, filed Sep. 8, 2010, by Paul V. Cooper, U.S. patent application Ser. No. 12/853,238, filed Aug. 9, 2010, by Paul V. Cooper, U.S. patent application Ser. No. 12/880,027, filed Sep. 10, 2010, by Paul V. Cooper, U.S. patent application Ser. No. 13/752,312, filed Jan. 28, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 13/756,468, filed Jan. 31, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 13/791,889, filed Mar. 8, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 13/791,952, filed Mar. 9, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 13/841,594, filed Mar. 15, 2013, by Paul V. Cooper, U.S. patent application Ser. No. 14/027,237, filed Sep. 15, 2013, by Paul V. Cooper, U.S. Pat. No. 8,535,603 entitled ROTARY DEGASSER AND ROTOR THEREFOR, U.S. Pat. No. 8,613,884 entitled LAUNDER TRANSFER INSERT AND SYSTEM, U.S. Pat. No. 8,714,914 entitled MOLTEN METAL PUMP FILTER, U.S. Pat. No. 8,753,563 entitled SYSTEM AND METHOD FOR DEGASSING MOLTEN METAL, U.S. Pat. No. 9,011,761 entitled LADLE WITH TRANSFER CONDUIT, U.S. Pat. No. 9,017,597 entitled TRANSFERRING MOLTEN METAL USING NON-GRAVITY ASSIST LAUNDER, U.S. Pat. No. 9,034,244 entitled GAS-TRANSFER FOOT, U.S. Pat. No. 9,080,577 entitled SHAFT AND POST TENSIONING DEVICE, U.S. Pat. No. 9,108,244 entitled IMMERSION HEATHER FOR MOLTEN METAL, U.S. Pat. No. 9,156,087 entitled MOLTEN METAL TRANSFER SYSTEM AND ROTOR, U.S. Pat. No. 9,205,490 entitled TRANSFER WELL SYSTEM AND METHOD FOR MAKING SAME, U.S. Pat. No. 9,328,615 entitled ROTARY DEGASSERS AND COMPONENTS THEREFOR, U.S. Pat. No. 9,377,028 entitled TENSIONING DEVICE EXTENDING BEYOND COMPONENT, U.S. Pat. No. 9,382,599 entitled ROTARY DEGASSER AND ROTOR THEREFOR, U.S. Pat. No. 9,383,140 entitled TRANSFERRING MOLTEN METAL FROM ONE STRUCTURE TO ANOTHER, U.S. Pat. No. 9,409,232 entitled MOLTEN METAL TRANSFER VESSEL AND METHOD OF CONSTRUCTION, U.S. Pat. No. 9,410,744 entitled VESSEL TRANSFER INSERT AND SYSTEM, U.S. Pat. No. 9,422,942 entitled TENSION DEVICE WITH INTERNAL PASSAGE, U.S. Pat. No. 9,435,343 entitled GAS-TRANSFER FOOT, U.S. Pat. No. 9,464,636 entitled TENSION DEVICE GRAPHITE COMPONENT USED IN MOLTEN METAL, U.S. Pat. No. 9,470,239 THREADED TENSIONING DEVICE, U.S. Pat. No. 9,481,035 entitled IMMERSION HEATER FOR MOLTEN METAL, U.S. Pat. No. 9,482,469 entitled VESSEL TRANSFER INSERT AND SYSTEM, U.S. Pat. No. 9,506,129 entitled ROTARY DEGASSER AND ROTOR THEREFOR, U.S. Pat. No. 9,566,645 entitled MOLTEN METAL TRANSFER SYSTEM AND ROTOR, U.S. Pat. No. 9,581,388 entitled VESSEL TRANSFER INSERT AND SYSTEM, U.S. Pat. No. 9,587,883 entitled LADLE WITH TRANSFER CONDUIT, U.S. Pat. No. 9,643,247 entitled MOLTEN METAL TRANSFER AND DEGASSING SYSTEM, U.S. Pat. No. 9,657,578 entitled ROTARY DEGASSERS AND COMPONENTS THEREFOR, U.S. Pat. No. 9,855,600 entitled MOLTEN METAL TRANSFER SYSTEM AND ROTOR, U.S. Pat. No. 9,862,026 entitled METHOD OF FORMING TRANSFER WELL, U.S. Pat. No. 9,903,383 entitled MOLTEN METAL ROTOR WITH HARDENED TOP, U.S. Pat. No. 9,909,808 entitled SYSTEM AND METHOD FOR DEGASSING MOLTEN METAL, U.S. Pat. No. 9,925,587 entitled METHOD OF TRANSFERRING MOLTEN METAL FROM A VESSEL, entitled U.S. Pat. No. 9,982,945 MOLTEN METAL TRANSFER VESSEL AND METHOD OF CONSTRUCTION, U.S. Pat. No. 10,052,688 entitled TRANSFER PUMP LAUNDER SYSTEM, U.S. Pat. No. 10,072,891 entitled TRANSFERRING MOLTEN METAL USING NON-GRAVITY ASSIST LAUNDER, U.S. Pat. No. 10,126,058 entitled MOLTEN METAL TRANSFERRING VESSEL, U.S. Pat. No. 10,126,059 entitled CONTROLLED MOLTEN METAL FLOW FROM TRANSFER VESSEL, U.S. Pat. No. 10,138,892 entitled ROTOR AND ROTOR SHAFT FOR MOLTEN METAL, U.S. Pat. No. 10,195,664 entitled MULTI-STAGE IMPELLER FOR MOLTEN METAL, U.S. Pat. No. 10,267,314 entitled TENSIONED SUPPORT SHAFT AND OTHER MOLTEN METAL DEVICES, U.S. Pat. No. 10,274,256 entitled VESSEL TRANSFER SYSTEMS AND DEVICES, U.S. Pat. No. 10,302,361 entitled TRANSFER VESSEL FOR MOLTEN METAL PUMPING DEVICE, U.S. Pat. No. 10,309,725 entitled IMMERSION HEATER FOR MOLTEN METAL, U.S. Pat. No. 10,307,821 entitled TRANSFER PUMP LAUNDER SYSTEM, U.S. Pat. No. 10,322,451 entitled TRANSFER PUMP LAUNDER SYSTEM, U.S. Pat. No. 10,345,045 entitled VESSEL TRANSFER INSERT AND SYSTEM, U.S. Pat. No. 10,352,620 entitled TRANSFERRING MOLTEN METAL FROM ONE STRUCTURE TO ANOTHER, U.S. Pat. No. 10,428,821 entitled QUICK SUBMERGENCE MOLTEN METAL PUMP, U.S. Pat. No. 10,458,708 entitled TRANSFERRING MOLTEN METAL FROM ONE STRUCTURE TO ANOTHER, U.S. Pat. No. 10,465,688 entitled COUPLING AND ROTOR SHAFT FOR MOLTEN METAL DEVICES, U.S. Pat. No. 10,562,097 entitled MOLTEN METAL TRANSFER SYSTEM AND ROTOR, U.S. Pat. No. 10,570,745 entitled ROTARY DEGASSERS AND COMPONENTS THEREFOR, U.S. Pat. No. 10,641,279 entitled MOLTEN METAL ROTOR WITH HARDENED TIP, U.S. Pat. No. 10,641,270 entitled TENSIONED SUPPORT SHAFT AND OTHER MOLTEN METAL DEVICES, and U.S. patent application Ser. Nos. 16/877,267, 16/877,364, 16/877,296, 16/877,332, and 16/877,219, entitled MOLTEN METAL CONTROLLED FLOW LAUNDER, MOLTEN METAL TRANSFER SYSTEM AND METHOD, SYSTEM AND METHOD TO FEED MOLD WITH MOLTEN METAL, SMART MOLTEN METAL PUMP, and METHOD FOR MELTING SOLID METAL, all of which were filed on the same date as this Application.

Three basic types of pumps for pumping molten metal, such as molten aluminum, are utilized: circulation pumps, transfer pumps and gas-release pumps. Circulation pumps are used to circulate the molten metal within a bath, thereby generally equalizing the temperature of the molten metal. Circulation pumps may be used in any vessel, such as in a reverbatory furnace having an external well. The well is usually an extension of the charging well, in which scrap metal is charged (i.e., added).

Standard transfer pumps are generally used to transfer molten metal from one structure to another structure such as a ladle or another furnace. A standard transfer pump has a riser tube connected to a pump discharge and supported by the superstructure. As molten metal is pumped it is pushed up the riser tube (sometimes called a metal-transfer conduit) and out of the riser tube, which generally has an elbow at its upper end, so molten metal is released into a different vessel from which the pump is positioned.

Gas-release pumps, such as gas-injection pumps, circulate molten metal while introducing a gas into the molten metal. In the purification of molten metals, particularly aluminum, it is frequently desired to remove dissolved gases such as hydrogen, or dissolved metals, such as magnesium. As is known by those skilled in the art, the removing of dissolved gas is known as “degassing” while the removal of magnesium is known as “demagging.” Gas-release pumps may be used for either of both of these purposes or for any other application for which it is desirable to introduce gas into molten metal.

Gas-release pumps generally include a gas-transfer conduit having a first end that is connected to a gas source and a second end submerged in the molten metal bath. Gas is introduced into the first end and is released from the second end into the molten metal. The gas may be released downstream of the pump chamber into either the pump discharge or a metal-transfer conduit extending from the discharge, or into a stream of molten metal exiting either the discharge or the metal-transfer conduit. Alternatively, gas may be released into the pump chamber or upstream of the pump chamber at a position where molten metal enters the pump chamber. The gas may also be released into any suitable location in a molten metal bath.

Molten metal pump casings and rotors often employ a bearing system comprising ceramic rings wherein there are one or more rings on the rotor that align with rings in the pump chamber (such as rings at the inlet and outlet) when the rotor is placed in the pump chamber. The purpose of the bearing system is to reduce damage to the soft, graphite components, particularly the rotor and pump base, during pump operation.

Generally, a degasser (also called a rotary degasser) includes (1) an impeller shaft having a first end, a second end and a passage for transferring gas, (2) an impeller, and (3) a drive source for rotating the impeller shaft and the impeller. The first end of the impeller shaft is connected to the drive source and to a gas source and the second end is connected to the impeller.

Generally a scrap melter includes an impeller affixed to an end of a drive shaft, and a drive source attached to the other end of the drive shaft for rotating the shaft and the impeller. The movement of the impeller draws molten metal and scrap metal downward into the molten metal bath in order to melt the scrap. A circulation pump is preferably used in conjunction with the scrap melter to circulate the molten metal in order to maintain a relatively constant temperature within the molten metal.

The materials forming the components that contact the molten metal bath should remain relatively stable in the bath. Structural refractory materials, such as graphite or ceramics, that are resistant to disintegration by corrosive attack from the molten metal may be used. As used herein “ceramics” or “ceramic” refers to any oxidized metal (including silicon) or carbon-based material, excluding graphite, or other ceramic material capable of being used in the environment of a molten metal bath. “Graphite” means any type of graphite, whether or not chemically treated. Graphite is particularly suitable for being formed into pump components because it is (a) soft and relatively easy to machine, (b) not as brittle as ceramics and less prone to breakage, and (c) less expensive than ceramics.

Ceramic, however, is more resistant to corrosion by molten aluminum than graphite. It would therefore be advantageous to develop vertical members used in a molten metal device that are comprised of ceramic, but less costly than solid ceramic members, and less prone to breakage than normal ceramic.

SUMMARY OF THE INVENTION

A scrap melting system and method includes a vessel that is configured to retain molten metal and a raised surface about the level of molten metal in the vessel. Solid metal is placed on the raised surface and molten metal from the vessel is moved upward from the vessel and across the raised surface to melt at least some of the metal. The molten metal is preferably raised from the vessel to the raised surface by a molten metal pumping device or system. The molten metal moves off of the raised surface and into a vessel of any suitable type, or launder. Any suitable method for moving molten metal onto the raised surface may be used, and the claims are not limited to the exemplary embodiments disclosed herein.

One exemplary embodiment of a system for transferring molten metal onto a raised surface comprises at least (1) a vessel for retaining molten metal, (2) a dividing wall (or overflow wall) within the vessel, the dividing wall having a height H1 and dividing the vessel into at least a first chamber and a second chamber, and (3) a molten metal pump in the vessel, preferably in the first chamber. The system may also include other devices and structures such as one or more of a launder, a third chamber, an additional vessel, a rotary degasser, one or more additional pumps, and a pump control system.

In one embodiment, the second chamber has a wall or opening with a height H2 that is lower than height H1 and the second chamber is juxtaposed the raised surface. The pump (either a transfer, circulation or gas-release pump) is submerged in the first chamber (preferably) and pumps molten metal from the first chamber past the dividing wall and into the second chamber causing the level of molten metal in the second chamber to rise. When the level of molten metal in the second chamber exceeds height H2, molten metal flows out of the second chamber and onto the raised surface onto which solid metal, such as scrap aluminum, has been placed. If a circulation pump, which is most preferred, or a gas-release pump is utilized, the molten metal would be pumped through the pump discharge and through an opening in the dividing wall wherein the opening is preferably completely below the surface of the molten metal in the first chamber.

In addition, preferably the pump used to transfer molten metal from the first chamber to the second chamber is a circulation pump (most preferred) or gas-release pump, preferably a variable speed pump. When utilizing such a pump there is an opening in the dividing wall beneath the level of molten metal in the first chamber during normal operation. The pump discharge communicates with, and may be received partially or totally in the opening. When the pump is operated it pumps molten metal through the opening and into the second chamber thereby raising the level in the second chamber until the level surpasses H2 and flows out of the second chamber.

Further, if the pump is a variable speed pump, which is preferred, a control system may be used to speed or slow the pump, either manually or automatically, as the amount of scrap to the melted, or remaining to be melted, varies.

Utilizing such a variable speed circulation pump or gas-release pump further reduces the chance of splashing and formation or dross, and reduces the chance of lags in which there is no molten metal being transferred or that could cause a device, such as a ladle, to be over filled. It leads to even and controlled transfer of molten metal from the vessel into another device or structure.

The problems with splashing or turbulence, or a difficult to control molten metal flow, are greatly reduced or eliminated by utilizing this system. Molten metal can be smoothly flowed across the raised surface and the level of molten metal raised or lowered as desired to melt the scrap on the raised surface. As solid metal is melted and becomes part of the molten (or liquid) metal, this melt (which includes the original molten metal and the melted, former solid metal) flows past the back, or second, side of the raised surface. From there the melt may enter any suitable structure, such as a launder, another vessel, or another chamber of the same vessel in which the molten metal pump and dividing wall are positioned. The melt may be degassed, such as by a rotary degasser, pumped, or demagged, such as by using a gas-release pump that releases chlorine gas into the melt.

Preferably, before or after the melt moves off the raised surface it is filtered to remove at least some solid particles. The filtering can be done by a grate positioned near or at the rear side of the raised surface. Solid particles that remain on the raised surface are removed, such as by using a steel arm that is lowered onto the raised surface and pulled across the surface to remove the solid particles.

Although one specific system is disclosed herein for raising molten metal to flow across the raised surface, and suitable system, method, or device may be utilized to move molten metal across the raised surface with little splashing or turbulence, and to evenly control the flow across the entire raised surface on which the solid metal is positioned.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a cross-sectional side view of a system according to this disclosure for melting solid metal on a raised surface.

FIG. 1A is a cross-sectional side view of a system according to this disclosure for melting solid metal on a raised surface and that includes one or more side walls.

FIG. 2 is the system of FIG. 1 showing the level of molten metal in the furnace being increased.

FIG. 2A shows the system of FIG. 1 with side walls on the raised surface that help contain the molten metal.

FIG. 2B shows the system of FIGS. 1 and 2 and displays how heights H1 and H2 are determined.

FIG. 3 is a top, partial cross-sectional view of the system of FIG. 2A.

FIG. 3A is a partial, cross-sectional side view of a system according to this disclosure.

FIG. 4 is a partial, cross-sectional side view of a system according to this disclosure that is utilized to fill a ladle.

FIG. 5 is a partial, cross-sectional side view of an alternate embodiment of the present disclosure.

FIG. 6 is a partial cross-sectional, side view of an embodiment of this disclosure.

FIG. 7 is a top, partial cross-sectional view of the embodiment of FIG. 6 with a pump.

FIG. 8 is a side, partial cross-sectional view of the system of FIG. 6.

FIG. 9 is a partial perspective, side view of a system according to this disclosure.

FIG. 10 is a cross-sectional, side view of an embodiment of this disclosure that further includes a launder.

FIG. 11 is a cross-sectional, side view of an embodiment of this disclosure that further includes an additional vessel or chamber.

FIG. 12 is a side, cross-sectional view of an alternate system of this disclosure that includes an additional vessel or chamber that has a molten metal pump.

FIG. 13 is a side, cross-sectional view of an alternate system of this disclosure that includes an additional vessel or chamber that has a rotary degasser.

DETAILED DESCRIPTION

Turning now to the Figures, where the purpose is to describe preferred embodiments of the invention and not to limit same, FIGS. 1-3A show a system 10 for moving molten metal M onto a raised surface 20 in order to melt solid metal, such as aluminum scrap. System 10 includes a furnace 1 that can retain molten metal M, which includes a holding furnace 1A, a vessel 12, a raised surface 20, and a pump 22. System 10 preferably has a vessel 12, a dividing wall 14 to separate vessel 12 into at least a first chamber 16 and a second chamber 18, and a device or structure, which may be pump 22, for generating a stream of molten metal from first chamber 16 into second chamber 18.

Using heating elements (not shown in the figures), furnace 1 is raised to a temperature sufficient to maintain the metal therein (usually aluminum or zinc) in a molten state. The level of molten metal M in holding furnace 1A and in at least part of vessel 12 changes as metal is added or removed to furnace 1A, as can be seen in FIGS. 2 and 11.

For explanation, furnace 1 includes a furnace wall 2 having an archway 3. Archway 3 allows molten metal M to flow into vessel 12 from holding furnace 1A. In this embodiment, furnace 1A and vessel 12 are in fluid communication, so when the level of molten metal in furnace 1A rises, the level also rises in at least part of vessel 12. It most preferably rises and falls in first chamber 16, described below, as the level of molten metal rises or falls in furnace 1A. This can be seen in FIGS. 2 and 11.

Dividing wall 14 separates vessel 12 into at least two chambers, a pump well (or first chamber) 16 and a skim well (or second chamber) 18, and any suitable structure for this purpose may be used as dividing wall 14. As shown in this embodiment, dividing wall 14 has an opening 14A and an optional overflow spillway 14B (best seen in FIG. 3), which is a notch or cut out in the upper edge of dividing wall 14. Overflow spillway 14B is any structure suitable to allow molten metal to flow from second chamber 18, past dividing wall 14, and into first chamber 16 and, if used, overflow spillway 14B may be positioned at any suitable location on wall 14. The purpose of optional overflow spillway 14B is to prevent molten metal from overflowing the second chamber 18, or a launder in communication with second chamber 18 (if a launder is used with the invention), by allowing molten metal in second chamber 18 to flow back into first chamber 16. Optional overflow spillway 14B would not be utilized during normal operation of system 10 and is to be used as a safeguard if the level of molten metal in second chamber 18 improperly rises to too high a level.

At least part of dividing wall 14 has a height H1 (best seen in FIG. 2A), which is the height at which, if exceeded by molten metal in second chamber 18, molten metal flows past the portion of dividing wall 14 at height H1 and back into first chamber 16. In the embodiment shown in FIGS. 1-3A, overflow spillway 14B has a height H1 and the rest of dividing wall 14 has a height greater than H1. Alternatively, dividing wall 14 may not have an overflow spillway, in which case all of dividing wall 14 could have a height H1, or dividing wall 14 may have an opening with a lower edge positioned at height H1, in which case molten metal could flow through the opening if the level of molten metal in second chamber 18 exceeded H1. H1 should exceed the highest level of molten metal in first chamber 16 during normal operation.

Second chamber 18 has a portion 18A, which has a height H2, wherein H2 is less than H1 (as can be best seen in FIG. 2A) so during normal operation molten metal pumped into second chamber 18 flows past wall 18A and out of second chamber 18 rather than flowing back over dividing wall 14 and into first chamber 16.

Dividing wall 14 may also have an opening 14A that is located at a depth such that opening 14A is submerged within the molten metal during normal usage, and opening 14A is preferably near or at the bottom of dividing wall 14. Opening 14A preferably has an area of between 6 in.² and 24 in.², but could be any suitable size. Further, dividing wall 14 need not have an opening if a transfer pump were used to transfer molten metal from first chamber 16, over the top of wall 14, and into second chamber 18 as described below.

Dividing wall 14 may also include more than one opening between first chamber 16 and second chamber 18 and opening 14A (or the more than one opening) could be positioned at any suitable location(s) in dividing wall 14 and be of any size(s) or shape(s) to enable molten metal to pass from first chamber 16 into second chamber 18.

Molten metal pump 22 may be any device or structure capable of pumping or otherwise conveying molten metal, and may be a transfer, circulation or gas-release pump. Pump 22 is preferably a circulation pump (most preferred) or gas-release pump that generates a flow of molten metal from first chamber 16 to second chamber 18 through opening 14A. Pump 22 generally includes a motor 24 surrounded by a cooling shroud 26, a superstructure 28, support posts 30 and a base 32. Some pumps that may be used with the invention are shown in U.S. Pat. Nos. 5,203,681, 6,123,523 and 6,354,964 to Cooper, and pending U.S. application Ser. No. 10/773,101 to Cooper. Molten metal pump 22 can be a constant speed pump, but is most preferably a variable speed pump. Its speed can be varied depending on the amount of molten metal in a structure such as a ladle or launder, as discussed below.

Utilizing system 10, as pump 22 pumps molten metal from first chamber 16 into second chamber 18, the level of molten metal in chamber 18 rises. When a pump with a discharge submerged in the molten metal bath, such as circulation pump or gas-release pump is utilized, there is essentially no turbulence or splashing during this process, which reduces the formation of dross and reduces safety hazards. The flow of molten metal is smooth and generally at an even flow rate.

A system according to this disclosure could also include one or more pumps in addition to pump 22, in which case the additional pump(s) may circulate molten metal within first chamber 16 and/or second chamber 18, or from chamber 16 to chamber 18, and/or may release gas into the molten metal first in first chamber 16 or second chamber 18. For example, first chamber 16 could include pump 22 and a second pump, such as a circulation pump or gas-release pump, to circulate and/or release gas into molten metal M.

If pump 22 is a circulation pump or gas-release pump, it is at least partially received in opening 14A in order to at least partially block opening 14A in order to maintain a relatively stable level of molten metal in second chamber 18 during normal operation and to allow the level in second chamber 18 to rise independently of the level in first chamber 16. Utilizing this system the movement of molten metal from one chamber to another and from the second chamber into a launder does not involve raising molten metal above the molten metal surface. As previously mentioned this alleviates problems with blockage forming (because of the molten metal cooling and solidifying), and with turbulence and splashing, which can cause dross formation and safety problems. As shown, part of base 32 (preferably the discharge portion of the base) is received in opening 14A. Further, pump 22 may communicate with another structure, such as a metal-transfer conduit, that leads to and is received partially or fully in opening 14A. Although it is preferred that the pump base, or communicating structure such as a metal-transfer conduit, be received in opening 14A, all that is necessary for the invention to function is that the operation of the pump increases and maintains the level of molten metal in second chamber 18 so that the molten metal ultimately moves out of chamber 18 and into another structure. For example, the base of pump 22 may be positioned so that its discharge is not received in opening 14A, but is close enough to opening 14A that the operation of the pump raises the level of molten metal in second chamber 18 independent of the level in chamber 16 and causes molten metal to move out of second chamber 18 and into another structure. A sealant, such as cement (which is known to those skilled in the art), may be used to seal base 32 into opening 14A, although it is preferred that a sealant not be used.

A system according to this disclosure could also be operated with a transfer pump, although a pump with a submerged discharge, such as a circulation pump or gas-release pump, is preferred since either would be less likely to create turbulence and dross in second chamber 18, and neither raises the molten metal above the surface of the molten metal bath nor has the other drawbacks associated with transfer pumps that have previously been described. If a transfer pump were used to move molten metal from first chamber 16, over dividing wall 14, and into second chamber 18, there would be no need for opening 14A in dividing wall 14, although an opening could still be provided and used in conjunction with an additional circulation or gas-release pump. As previously described, regardless of what type of pump is used to move molten metal from first chamber 16 to second chamber 18, molten metal would ultimately move out of chamber 18 and into a structure, such as ladle 52 or launder 20, when the level of molten metal in second chamber 18 exceeds H2.

Once pump 22 is turned off, the respective levels of molten metal level in chambers 16 and 18 essentially equalize. Alternatively, the speed of pump 22 could be reduced to a relatively low speed to keep the level of molten metal in second chamber 18 relatively constant but not exceed height H2. To move molten metal onto raised surface 20, pump 22 is simply turned on again and operated as described above.

A system for melting scrap according to this disclosure includes a molten metal pump and a raised surface 20 on which solid metal S, such as scrap aluminum, can be positioned, wherein molten metal is flowed onto and across the raised surface 20 in order to melt at least some of the solid metal S. As described above, the pump 22 generates a flow of molten metal M from first chamber 16 into second chamber 18. When the level of molten metal M in second chamber 18 exceeds H2, the molten metal moves out of second chamber 18 and onto the raised surface 20 to melt scrap placed on surface 20. The level of molten metal M in the second chamber 18 rises until it flows onto raised surface 20, and flows along the raised surface 20 until it melts at least some of the solid metal S on the raised surface 20 melts. The amount of molten metal flowed across raised surface 20 can be varied based on any suitable factor, such as based on the amount of solid metal S on raised surface 20.

The raised surface 20 has a first side 20A adjacent the second chamber 18 and a second side 20B. Raised surface 20 can be the upper surface of a refractory block 23, which may be inside or outside of vessel 1. A refractory grate 75 is preferably positioned at, or just before or just after, second side 20B. The refractory grate 75 acts as a filter that blocks pieces of unmelted metal, such as pieces of iron or steel, from being mixed with the molten metal M and moving off of raised surface 20. Any suitable filter could be used for this purpose.

Preferably, before or after the melt moves off the raised surface 20 it is filtered to remove at least some solid particles. The filtering can be done by grate 75. Solid particles, such as iron or steel, that remain on the raised surface 20 are removed, such as by using a steel arm that is lowered onto the raised surface 20 and pulled across the raised surface 20 to remove the solid particles. The method of adding solid metal S and melting it can then be repeated.

The raised surface 20 may also include one or more side walls 29 (as shown, for example, in FIG. 1A) that help retain molten metal on the raised surface.

The molten metal M could pass from the raised surface 20 into another vessel or chamber 2000, or move into a launder 31 (as shown in FIG. 10) or any suitable structure.

Furthermore, molten metal can be moved across the raised surface 20 in any suitable manner, such as by using pumping and transfer devices incorporated by reference herein. The specific system described herein using a dividing wall, however, is most preferred because the flow of molten metal can be carefully controlled and spread over a large area, in order to cover the width of the raised surface 20 or a large portion of the width of the raised surface 20.

Although one specific system is disclosed herein for raising molten metal to flow across the raised surface, and suitable system, method, or device may be utilized to move molten metal across the raised surface with little splashing or turbulence, and to evenly control the flow across the entire raised surface on which the solid metal is positioned.

The problems with splashing or turbulence, or a difficult to control molten metal flow, are greatly reduced or eliminated by utilizing this system. Molten metal M can be smoothly flowed across the raised surface 20 and the level of molten metal M raised or lowered as desired to melt the solid metal S on the raised surface 20. As solid metal S is melted and becomes part of the molten (or liquid) metal, this melt (which includes the original molten metal and the melted, former solid metal) flows past the back, or second, side 20B of the raised surface 20. From there the melt may enter any suitable structure, such as a launder 31, another vessel, or another chamber of the same vessel, 2000 in which the molten metal pump and dividing wall are positioned. The melt may be degassed, such as by a rotary degasser, pumped, or demagged, such as by using a gas-release pump that releases chlorine gas into the melt.

As shown in FIG. 10, launder 31 is any structure or device for transferring molten metal from raised surface 20 to one or more structures, such as one or more ladles, molds (such as ingot molds) or other structures in which the molten metal is ultimately cast into a usable form, such as an ingot. Launder 31 may be either an open or enclosed channel, trough or conduit and may be of any suitable dimension or length, such as one to four feet long, or as much as 100 feet long or longer. Launder 31 may be completely horizontal or may slope gently upward or downward. Launder 31 may have one or more taps (not shown), i.e., small openings stopped by removable plugs. Each tap, when unstopped, allows molten metal to flow through the tap into a ladle, ingot mold, or other structure. Launder 31 may additionally or alternatively be serviced by robots or cast machines capable of removing molten metal M from launder 31.

Launder 31 has a first end 31A juxtaposed the second end 20B of raised surface 20 and a second end 31B that is opposite first end 31B. An optional stop may be included in a launder according to the invention. The stop, if used, is preferably juxtaposed the second end 31B of the launder. If launder 31 has a stop, the stop can be opened to allow molten metal to flow past end 31B, or closed to prevent molten metal from flowing past end 31B. The stop preferably has a height H3 greater than height H1 so that if launder 31 becomes too filled with molten metal, the molten metal would back up on raised surface 20, and spill back over dividing wall 14A (over spillway 14B, if used) rather than overflow raised surface 20 and launder 31.

FIG. 4 shows an alternate system 10′ that is in all respects the same as system 10 except that it has a shorter, downward, sloping surface 20′ for retaining solid metal to be melted, a wall 18A′ past which molten metal moves when it exits second chamber 18 and it fills a ladle 52.

FIG. 12 shows an alternate system 10 that is in all respects the same as system 10 except that it includes an optional second pump 1500 in a third chamber, or second vessel, 2000 having a basin 2012.

FIG. 13 shows an alternate system 10A″ that is in all respects the same as system 10 except that it includes an optional rotary degasser 110 in a third chamber, or second vessel, 2000 having a basin 2012.

Some non-limiting examples of this disclosure are as follows:

Example 1: A system for melting aluminum, the system comprising:

a vessel having a first chamber and a second chamber;

a raised surface juxtaposed the second chamber;

a molten metal pump in the first chamber;

a first dividing wall between the first chamber and second chamber, the first dividing wall having a first height, and an opening that is beneath the first height; and

a second dividing wall between the second chamber and the raised surface, the second dividing wall having a second height that is less that the first height; and

Example 2: The system of example 1 that further comprises a grate at a second side of the raised surface.

Example 3: The system of example 1, wherein the molten metal pump is a circulation pump.

Example 4: The system of example 1, wherein the molten metal pump is a gas-release pump.

Example 5: The system of example 1, wherein the opening is between 6 in2 and 24 in2.

Example 6: The system of example 1, wherein the molten metal pump has a pump housing and an outlet, and the outlet is positioned 6″ or less from the opening.

Example 7: The system of example 1, wherein a bracket is connected to the dividing wall and the bracket is also connected to the molten metal pump and configured to maintain the molten metal pump in position in the first chamber.

Example 8: The system of example 1, wherein the raised surface is comprised of ceramic.

Example 9: The system of example 1, wherein the raised surface is comprised of silicon carbide.

Example 10: The system of example 1, wherein there is no structure between the second chamber and the second dividing wall.

Example 11: The system of example 2, wherein the grate is comprised of ceramic.

Example 12: The system of example 11, wherein the grate is comprised of silicon carbide.

Example 13: The system of example 1, wherein the raised surface is flat.

Example 14: The system of example 1 that further includes a launder in fluid communication with the raised surface.

Example 15: The system of example 1 that includes a third chamber in communication with, and downstream of, the raised surface.

Example 16: The system of example 15, wherein there is no structure between the raised surface and the third chamber.

Example 17: The system of example 15 that includes a second molten metal pump in the third chamber.

Example 18: The system of example 7, wherein the dividing wall has an upper edge and the bracket is on the upper edge.

Example 19: The system of example 7, wherein the molten metal pump has a superstructure that is a metal platform, and the bracket is connected to the superstructure.

Example 20: The system of example 1, wherein the vessel that includes the first chamber and the second chamber is a reverbatory furnace.

Example 21: A system for melting aluminum, the system comprising:

a vessel configured to hold molten metal;

a raised surface juxtaposed the vessel;

a molten metal pump in the vessel and an uptake chamber leading to an outlet that is at or above the raised surface.

Example 22: The system of example 21 that further comprises a grate at a second side of the raised surface.

Example 23: The system of example 21, wherein the molten metal pump is a circulation pump.

Example 24: The system of example 21, wherein the molten metal pump is a gas-release pump.

Example 25: The system of example 21, wherein the opening is between 6 in2 and 24 in2.

Example 26: The system of example 21, wherein the molten metal pump has a housing and an outlet, and the outlet is positioned 6″ or less from the opening.

Example 27: The system of example 21, wherein a bracket is connected to the dividing wall and the bracket is also connected to the molten metal pump and configured to maintain the molten metal pump in position in the first chamber.

Example 28: The system of example 21, wherein the raised surface is comprised of ceramic.

Example 29: The system of example 21, wherein the raised surface is comprised of silicon carbide.

Example 30: The system of example 21, wherein there is no structure between the vessel and the dividing wall.

Example 31: The system of example 22, wherein the grate is comprised of ceramic.

Example 32: The system of example 31, wherein the grate is comprised of silicon carbide.

Example 33: The system of example 21, wherein the raised surface is flat.

Example 34: The system of example 21 that further includes a launder in fluid communication with the top surface.

Example 35: The system of example 21 that includes a chamber in communication with, and downstream of, the raised surface.

Example 36: The system of example 27, wherein there is no structure between the raised surface and the fourth chamber.

Example 37: The system of example 37 that includes a second molten metal pump in the chamber.

Example 38: The system of example 27, wherein the dividing wall has an upper edge and the bracket is on the upper edge.

Example 39: The system of example 27, wherein the molten metal pump has a superstructure that is a metal platform, and the bracket is connected to the superstructure.

Example 40: The system of example 1, wherein the pump is a variable speed pump.

Having thus described different embodiments of the invention, other variations and embodiments that do not depart from the spirit thereof will become apparent to those skilled in the art. The scope of the present invention is thus not limited to any particular embodiment, but is instead set forth in the appended claims and the legal equivalents thereof. Unless expressly stated in the written description or claims, the steps of any method recited in the claims may be performed in any order capable of yielding the desired product or result.

Claims

1. A system for melting aluminum, the system comprising: (a) a vessel having a first chamber and a second chamber;(b) a molten metal pump in the first chamber;(c) a first dividing wall between the first chamber and second chamber, the first dividing wall having a first height, and an opening that is beneath the first height;(d) a raised surface that comprises a first side juxtaposed the second chamber and a second side;(e) an arm configured to be lowered onto the raised surface and to be pulled across the raised surface;(f) a grate at the second side of the raised surface, and(g) a third chamber in communication with and downstream of the raised surface.

2. The system of claim 1, wherein the molten metal pump is a circulation pump.

3. The system of claim 1, wherein the molten metal pump is a gas-release pump.

4. The system of claim 1, wherein the opening is between 6 in2 and 24 in2.

5. The system of claim 1, wherein the molten metal pump has a pump housing and an outlet, and the outlet is positioned 6″ or less from the opening.

6. The system of claim 1, wherein a bracket is connected to the first dividing wall and the bracket is also connected to the molten metal pump and configured to maintain the molten metal pump in position in the first chamber.

7. The system of claim 1, wherein the raised surface is comprised of ceramic.

8. The system of claim 1, wherein the raised surface is comprised of silicon carbide.

9. The system of claim 1 that further includes a second dividing wall with a second height that is less than the first height, and wherein there is no structure between the second chamber and the second dividing wall.

10. The system of claim 1, wherein the grate is comprised of ceramic.

11. The system of claim 10, wherein the grate is comprised of silicon carbide.

12. The system of claim 1, wherein the raised surface is flat.

13. The system of claim 1 that further includes a launder in fluid communication with the second end of the raised surface.

14. The system of claim 1 that further includes a second molten metal pump in the third chamber.

15. The system of claim 6, wherein the first dividing wall has an upper edge and the bracket is on the upper edge.

16. The system of claim 6, wherein the molten metal pump has a superstructure that is a metal platform, and the bracket is connected to the superstructure.

17. The system of claim 1, wherein the vessel that includes the first chamber and the second chamber is a reverberatory furnace.