Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D27/00—Treating the metal in the mould while it is molten or ductile ; Pressure or vacuum casting
  • B22D27/04—Influencing the temperature of the metal, e.g. by heating or cooling the mould
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/16—Controlling or regulating processes or operations
  • B22D11/22—Controlling or regulating processes or operations for cooling cast stock or mould
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/001—Continuous casting of metals, i.e. casting in indefinite lengths of specific alloys
  • B22D11/003—Aluminium alloys
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/04—Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds
  • B22D11/049—Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds for direct chill casting, e.g. electromagnetic casting
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/14—Plants for continuous casting
  • B22D11/148—Safety arrangements
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/16—Controlling or regulating processes or operations
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
  • B22D11/16—Controlling or regulating processes or operations
  • B22D11/18—Controlling or regulating processes or operations for pouring
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D27/00—Treating the metal in the mould while it is molten or ductile ; Pressure or vacuum casting
  • B22D27/003—Treating the metal in the mould while it is molten or ductile ; Pressure or vacuum casting by using inert gases
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D27/00—Treating the metal in the mould while it is molten or ductile ; Pressure or vacuum casting
  • B22D27/04—Influencing the temperature of the metal, e.g. by heating or cooling the mould
  • B22D27/045—Directionally solidified castings
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D30/00—Cooling castings, not restricted to casting processes covered by a single main group
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D46/00—Controlling, supervising, not restricted to casting covered by a single main group, e.g. for safety reasons
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B22—CASTING; POWDER METALLURGY
  • B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
  • B22D7/00—Casting ingots, e.g. from ferrous metals
  • B22D7/005—Casting ingots, e.g. from ferrous metals from non-ferrous metals
• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22C—ALLOYS
  • C22C21/00—Alloys based on aluminium

Definitions

• U.S. Patent No. 4,651,804 describes a more modern aluminum casting pit design. It has become standard practice to mount the metal melting furnace slightly above ground level with the casting mould at, or near to, ground level and the cast ingot is lowered into a water containing pit as the casting operation proceeds. Cooling water from the direct chill flows into the pit and is continuously removed there-from while leaving a permanent deep pool of water within the pit. This process remains in current use and, throughout the world, probably in excess of 5 million tons of aluminum and its alloys are produced annually by this method.
• a "bleed-out” or “run-out” occurs where the aluminum ingot being cast is not properly solidified in the casting mold, and is allowed to leave the mold unexpectedly and prematurely while in a liquid state.
• Molten aluminum in contact with water during a "bleed- out” or “run-out” can cause an explosion from (1) conversion of water to steam from the thermal mass of the aluminum heating the water to >212°F or (2) the chemical reaction of the molten metal with the water resulting in release of energy causing an explosive chemical reaction.
• the recommended depth of at least three feet of water is generally employed for vertical DC casting and in some foundries (notably in continental European countries) the water level is brought very close to the underside of the mold in contrast to recommendation (2) above.
• the aluminum industry, casting by the DC method has opted for the safety of a deep pool of water permanently maintained in the pit.
• the codes of practice are based upon empirical results; what actually happens in various kinds of molten metal/water explosions is imperfectly understood.
• attention to the codes of practice has ensured the virtual certainty of avoiding accidents in the event of "run-outs" with aluminum alloys.
• 0-150-922 describes a sloped pit bottom (preferably three percent to eight percent inclination gradient of the pit bottom) with accompanying off-set water collection reservoir, water pumps, and associated water level sensors to make sure water cannot collect in the cast pit, thus reducing the incidence of explosions from water and the Al-Li alloy having intimate contact.
• the ability to continuously remove the ingot coolant water from the pit such that a build-up of water cannot occur is critical to the success of the patent's teachings.
• Other work has also demonstrated that the explosive forces associated with adding lithium to aluminum alloys can increase the nature of the explosive energy several times than for aluminum alloys without lithium.
• Claim 1 of the 5,212,343 patent claims the method to perform this intense interaction for producing a water explosion via the exothermic reaction.
• This patent describes a process wherein the addition of elements such as lithium results in a high energy of reaction per unit volume of materials.
• the addition of lithium or some other chemically active element promotes an explosion.
• These patents teach a process where an explosive reaction is a desirable outcome.
• These patents reinforce the explosiveness of the addition of lithium to the "bleed-out” or "run-out", as compared to aluminum alloys without lithium.
• U.S. Patent 5,212,343 describes making an explosive reaction by mixing water with a number of elements and combinations, including Al and Li to produce large volumes of hydrogen containing gas.
• column 3 it states "the reactive mixture is chosen that, upon reaction and contact with water, a large volume of hydrogen is produced from a relatively small volume of reactive mixture.”
• lines 39 and 40 identify aluminum and lithium.
• column 5, lines 21-23 show aluminum in combination with lithium.
• lines 28-30 refer to a hydrogen gas explosion.
• patents In another method of conducting DC casting, patents have been issued related to casting Al-LI alloys using an ingot coolant other than water to provide ingot cooling without the water-lithium reaction from a 'bleed-out" or "run-out".
• U.S. Patent No. 4,593,745 describes using a halogenated hydrocarbon or halogenated alcohol as ingot coolant.
• U.S. Patents Nos. 4,610,295; 4,709,740, and 4,724,887 describe the use of ethylene glycol as the ingot coolant.
• the halogenated hydrocarbon typically ethylene glycol
• the halogenated hydrocarbon must be free of water and water vapor.
• a fire suppression system will be required within the casting pit to contain potential glycol fires.
• the cooling capability of glycol or other halogenated hydrocarbons is different than that for water, and different casting practices as well as casting tooling are required to utilize this type of technology.
• glycol has a lower heat conductivity and surface heat transfer coefficient than water
• the microstructure of the metal cast with 100% glycol as a coolant has coarser undesirable metallurgical constituents and exhibits higher amount of centerline shrinkage porosity in the cast product. Absence of finer microstructure and simultaneous presence of higher concentration of shrinkage porosity has a deleterious effect on the properties of the end products manufactured from such initial stock.
• U.S. Patent No. 4,237,961 suggests removing water from the ingot during DC casting.
• European Patent No. 0-183-563 a device is described for collecting the "breakout” or “run-out” molten metal during direct chill casting of aluminum alloys. Collecting the "break-out” or “run-out” molten metal would concentrate this mass of molten metal.
• This teaching cannot be used for Al-Li casting since it would create an artificial explosion condition where removal of the water would result in a pooling of the water as it is being collected for removal.
• Figure 1 is a simplified cross sectional side view of an embodiment of a direct chill casting pit.
• Figure 2 is a process flow diagram of an embodiment of a process addressing a "bleed-out” or a "run-out” in a casting operation.
• Figure 3 is a process flow diagram of another embodiment of a process addressing a "bleed-out” or a "run-out” in a casting operation.
• the instantly described apparatus and method improve the safety of DC casting of Al- Li alloys by minimizing or eliminating ingredients that must be present for an explosion to occur. It is understood that water (or water vapor or steam) in the presence of the molten Al- Li alloy will produce hydrogen gas.
• a representative chemical reaction equation is believed to be:
• Hydrogen gas has a density significantly less than a density of air. Hydrogen gas that evolves during the chemical reaction, being lighter than air, tends to gravitate upward, toward the top of a cast pit, just below the casting mold and mold support structures at the top of the casting pit. This typically enclosed area allows the hydrogen gas to collect and become concentrated enough to create an explosive atmosphere. Heat, a spark, or other ignition source can trigger the explosion of the hydrogen 'plume' of the as-concentrated gas.
• the molten "bleed-out” or “run-out” material when combined with the ingot cooling water that is used in a DC process (as practiced by those skilled in the art of aluminum ingot casting) will create steam and water vapor.
• the water vapor and steam are accelerants for the reaction that produces the hydrogen gas. Removal of this steam and water vapor by a steam removal system will remove the ability of the water to combine with Al-LI creating Li-OH, and the expulsion of H 2 .
• the instantly described apparatus and method minimizes the potential for the presence of water and steam vapor in the casting pit by, in one embodiment, placing steam exhaust ports about the inner periphery of the casting pit, and rapidly activating the vents upon the detection of an occurrence of a "bleed-out".
• the exhaust ports are located in several areas within the casting pit, e.g., from about 0.3 meters to about 0.5 meters below the casting mold, in an intermediate area from about 1.5 meters to about 2.0 meters from the casting mold, and at the bottom of the cast pit.
• a casting mold is typically placed at a top of a casting pit, from floor level to as much as one meter above floor level.
• the horizontal and vertical areas around the casting mold below the mold table are generally closed-in with a pit skirt and a Lexan glass encasement except for the provision to bring in and ventilate outside air for dilution purpose, such that the gasses contained within the pit are introduced and exhausted according to a prescribed manner.
• an inert gas is introduced into the casting pit interior space to minimize or eliminate the coalition of hydrogen gas into a critical mass.
• the inert gas is a gas that has a density less than a density of air and that will tend to occupy the same space just below the top of the casting pit that hydrogen gas would typically inhabit.
• Helium gas is one such example of suitable inert gas with a density less than a density of air.
• argon has been described in numerous technical reports as a cover gas for protecting Al-Li alloys from ambient atmosphere to prevent their reaction with air. Even though argon is completely inert, it has a density greater than a density of air and will not provide the inerting of the casting pit upper interior unless a strong upward draft is maintained. Compared to air as a reference (1.3 grams/liter), argon has density on the order of 1.8 grams/liter and would tend to settle to the bottom of a cast pit, providing no desirable hydrogen displacement protection within the critical top area of the casting pit. Helium, on the other hand, is nonflammable and has a low density of 0.2 grams per liter and will not support combustion.
• the dangerous atmosphere in the casting pit may be diluted to a level where an explosion cannot be supported. Also, while this exchange is occurring, water vapor and steam are also removed from the casting pit. In one embodiment, during steady state casting and when non- emergency condition pertaining to a 'bleed-out' is not being experienced, the water vapor and steam are removed from the inert gas in an external process, while the 'clean' inert gas can be re-circulated back through the casting pit.
• FIG. 1 shows a cross-section of an embodiment of a DC casting system.
• DC system 5 includes casting pit 16 that is typically formed into the ground. Disposed within casting pit 16 is casting cylinder 15 that may be raised and lowered, for example, with a hydraulic power unit (not shown). Attached to a superior or top portion of casting cylinder 15 is platen 18 that is raised and lowered with casting cylinder 15. Above or superior to platen 18 in this view is stationary casting mold 12. Molten metal (e.g., Al-Li alloy) is introduced into mold 12.
• Casting mold 12 in one embodiment, includes, coolant inlets to allow coolant (e.g., water) to flow onto a surface of an emerging ingot providing a direct chill and solidification of the metal.
• coolant e.g., water
• a gasket or seal 29 fabricated from, for example, a high temperature resistant silica material is located between the structure of mold 12 and table 31. Gasket 29 inhibits steam or any other atmosphere from below mold table 31 to reach above the mold table and thereby inhibits the pollution of the air in which casting crewmen operate and breathe.
• system 5 includes molten metal detector 10 positioned just below mold 12 to detect a bleed-out or run-out.
• Molten metal detector 10 may be, for example, an infrared detector of the type described in U.S. Patent No. 6,279,645, a "break out detector" as described in U.S. Patent No. 7,296,613 or any other suitable device that can detect the presence of a "bleed-out".
• system 5 also includes exhaust system 19.
• exhaust system 19 includes, in this embodiment, exhaust ports 20A, 20A', 20B, 20B', 20C and 20C positioned in casting pit 16.
• the exhaust ports are positioned to maximize the removal of generated gases including ignition sources (e.g., H 2 (g)) and reactants (e.g., water vapor or steam) from the inner cavity of the casting pit.
• ignition sources e.g., H 2 (g)
• reactants e.g., water vapor or steam
• exhaust ports 20 A, 20 A' are positioned about 0.3 meters to about 0.5 meters below mold 12; exhaust ports 20B, 20B' are positioned about 1.5 meters to about 2.0 meters below the mold 12; and exhaust ports 20C, 20C are positioned at a base of casting pit 16 where bleed-out metal is caught and contained.
• Exhaust system 19 also includes remote exhaust vent 22 that is remote from casting mold 12 (e.g., about 20 to 30 meters away from mold 12) to allow exit of exhausted gases from the system.
• Exhaust ports 20A, 20A, 20B, 20B', 20C, 20C are connected to exhaust vent 22 through ducting (e.g., galvanized steel or stainless steel ducting).
• exhaust system 19 further includes an array of exhaust fans to direct exhaust gases to exhaust vent 22.
• Figure 1 further shows gas introduction system 24 including, in this embodiment, inert gas introduction ports (e.g., inert gas introduction ports 26A, 26A, 26B, 26B', 26C and 26C) disposed around the casting pit and connected to an inert gas source or sources 27.
• inert gas introduction ports e.g., inert gas introduction ports 26A, 26A, 26B, 26B', 26C and 26C
• inert gas introduction ports 26A, 26A, 26B, 26B', 26C and 26C disposed around the casting pit and connected to an inert gas source or sources 27.
• inert gas introduction ports e.g., inert gas introduction ports 26A, 26A, 26B, 26B', 26C and 26C
• there are positioned excess air introduction ports to assure additional in-transit dilution of the evolved hydrogen gas.
• gas introduction ports are selected to provide a flood of inert gas to immediately replace the gases and steam within the pit, via a gas introduction system 24 that introduces inert gas as and when needed (especially upon the detection of a bleed-out) through inert gas introduction ports 26 into casting pit 16 within a predetermined time (e.g., about a maximum of 30 seconds) of the detection of a "bleed-out" condition.
• Figure 1 shows gas introduction ports 26A and 26A' positioned near a top portion of casting pit 16; gas introduction ports 26B and 26B' positioned at an intermediate portion of casting pit 16; and gas introduction ports 26C and 26C positioned at a bottom portion of casting pit 16.
• Pressure regulators may be associated with each gas introduction port to control the introduction of an inert gas.
• the gas introduction ports are shown in pairs at each level. It is appreciated that, in an embodiment, where there are arrays of gas introduction ports at each level, there may be more than two gas introduction ports at each level. For example, in another embodiment, there may be three or four gas introduction ports at each level. In another embodiment, there may be less than two (e.g., one) at each level.
• the inert gas introduced through gas introduction ports 26 A and 26 A' at top 14 of casting pit 16 should impinge on the solidified, semi-solid and liquid aluminum lithium alloy below mold 12, and inert gas flow rates in this area are, in one embodiment, at least substantially equal to a volumetric flow rate of a coolant prior to detecting the presence of a "bleed-out" or a "run-out".
• flow rates through such gas introduction ports may be the same as a flow rate through the gas introduction ports at top 14 of casting pit 16 or may be different (e.g., less than a flow rate through the gas introduction ports at top 14 of casting pit 16).
• the replacement inert gas introduced through the gas introduction ports is removed from casting pit 16 by an upper exhaust system 28 which is kept activated at lower volume on continuous basis but the volume flow rate is enhanced immediately upon detection of a "bleed-out" and directs inert gas removed from the casting pit to the exhaust vent 22.
• atmosphere purification system 30 of, for example, moisture stripping columns and steam desiccants thus keeping the atmosphere in the upper region of the pit reasonably inert.
• the removed gas while being circulated is passed through atmosphere purification system 30 and any water vapor is removed to purify the upper pit atmosphere containing inert gas.
• the purified inert gas may then be re-circulated to inert gas injection system 24 via a suitable pump 32.
• inert gas curtains are maintained, between the ports 20A and 26A and similarly between the ports 20A' and 26A' to minimize the escape of the precious inert gas of the upper region of the casting pit through the pit ventilation and exhaust system.
• exhaust ports 20A, 20A', 20B, 20B', 20C, 20C and inert gas introduction ports 26A, 26A', 26B, 26B', 26C, 26C will be a function of the size and configuration of the particular casting pit being operated and these are calculated by the skilled artisan practicing DC casting in association with those expert at recirculation of air and gases. It is most desirable to provide the three sets (e.g., three pairs) of exhaust ports and inert gas introduction ports as shown Figure 1. Depending on the nature and the weight of the product being cast, a somewhat less complicated and less expensive but equally effective apparatus can be obtained using a single array of exhaust ports and inert gas introduction ports about the periphery of the top of casting pit 16.
• each of a movement of platen 18/casting cylinder 15, a molten metal supply inlet to mold 12 and a water inlet to the mold are controlled by controller 35.
• Molten metal detector 10 is also connected to controller 35.
• Controller 35 contains machine- readable program instructions as a form of non-transitory tangible media.
• the program introductions are illustrated in the method of Figure 2.
• molten metal detector 10 block 110
• the machine readable instructions cause movement of platen 18 and molten metal inlet supply (not shown) to stop (blocks 120, 130), coolant flow (not shown) into mold 12 to stop and/or be diverted (block 140), and higher volume exhaust system 19 to be activated simultaneously or within about 15 seconds and in another embodiment, within about 10 seconds, to divert the water vapor containing exhaust gases and/or water vapor away from the casting pit via exhaust ports 20A, 20A, 20B, 20B', 20C and 20C to exhaust vent 22 (block 150).
• the machine readable instructions further activate gas introduction system and an inert gas having a density less than a density of air, such as helium, is introduced through gas introduction ports 26A, 26A, 26B, 26B', 26C and 26C (block 160).
• the introduced inert gas is subsequently collected via the exhaust system and may then be purified (block 170). It is to be noted that those skilled in the art of melting and direct chill casting of aluminum alloys except the melting and casting of aluminum- lithium alloys may be tempted to use nitrogen gas in place of helium because of the general industrial knowledge that nitrogen is also an 'inert' gas.
• nitrogen is really not an inert gas when it comes to interacting with liquid aluminum-lithium alloys. Nitrogen does react with the alloy and produces ammonia which in turns reacts with water and brings in additional reactions of dangerous consequences, and hence its use should be completely avoided. The same holds true for another presumably inert gas carbon dioxide. Its use should be avoided in any application where there is a finite chance of molten aluminum lithium alloy to get in touch with carbon dioxide.
• Figure 3 shows another embodiment of a method. Referring to Figure 3 and method
• molten metal detector 10 (block 210).
• coolant flow into mold 12 is reduced (block 240); metal supply into the mold is stopped (block 230); and a movement of platen 18 is reduced (block 220).
• a reduction of a coolant flow and reduction of platen movement such reduction may be a complete reduction (stop or halt) or a partial reduction.
• a coolant flow rate may be reduced to a rate that is greater than a flow rate of zero, but less than a predetermined flow rate selected to flow onto an emerging ingot providing a direct chill and solidification of the metal.
• the flow rate is reduced to a rate that is acceptably safe (e.g., a few liters per minute or less) given the additional measures that are implemented to address the "bleed-out" or "run-out".
• platen 18 can continue to move through casting pit 16 at a rate that is acceptably safe but that is reduced from a predetermined selected rate to cast metal.
• a reduction in coolant flow and platen movement need not be related in the sense that they are either both reduced to complete cessation or to a rate greater than complete cessation.
• a coolant flow rate may be stopped or halted (i.e., reduced to a flow rate of zero) following a detection of a "bleed-out" and a platen movement may be reduced to a rate tending to halting or stopping, but not halted or stopped, i.e., a rate of movement greater than zero.
• a movement of platen 18 may be halted or stopped (i.e., reduced to a rate of zero) while a rate of coolant flow reduced to rate tending to halting or stopping, but not halted or stopped, i.e., a rate of flow greater than zero.
• coolant flow and movement of platen 18 are both halted or stopped.
• machine readable instructions implementing the method of Figure 3 direct an evacuation of exhaust gases and/or water vapor from casting pit 16 (block 250); introduce inert gas into the pit (block 260); and optionally collect and/or purify inert gas removed from the pit (block 270) similar to the method described above with respect to Figure 2.
• system 5 included molten metal detector 10 configured to detect a "bleed-out” or a "run-out”.
• a detection device such as molten metal detector 10
• controller 35 in system 5 of Figure 1
• a molten metal detector 10 detects a "bleed-out” or a "run-out” and communicates the condition to controller 35.
• a "bleed-out" and "run-out” may be detected.
• controller 35 may communicate with controller 35 to implement actions by controller 35 to minimize effects of a "bleed-out” or a “run-out” (e.g., exhausting generated gas from the casting pit, introducing an inert gas into the casting pit, stopping flow of metal, reducing or stopping flow of coolant, reducing or stopping movement of platen, etc.).
• a "bleed-out” or a "run-out” e.g., exhausting generated gas from the casting pit, introducing an inert gas into the casting pit, stopping flow of metal, reducing or stopping flow of coolant, reducing or stopping movement of platen, etc.
• communication may be, for example, pressing a key or keys on a keypad associated with controller 35.
• the process and apparatus described herein provide a unique method to adequately contain Al-Li "bleed-outs" or "run-outs” such that a commercial process can be operated successfully without utilization of extraneous process methods, such as casting using a halogenated liquid like ethylene glycol that render the process not optimal for cast metal quality, a process less stable for casting, and at the same time a process which is

Landscapes

• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• Chemical & Material Sciences (AREA)
• Materials Engineering (AREA)
• Metallurgy (AREA)
• Organic Chemistry (AREA)
• Continuous Casting (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Mold Materials And Core Materials (AREA)
• Casting Support Devices, Ladles, And Melt Control Thereby (AREA)
• Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Priority Applications (21)

Applications Claiming Priority (2)

Related Parent Applications (2)

Related Child Applications (3)

Publications (3)

Family

ID=47603241

Family Applications (2)

Family Applications After (1)

Country Status (9)

Families Citing this family (11)

Citations (12)

Family Cites Families (129)

• 2012
  • 2012-05-17 US US13/474,614 patent/US8365808B1/en active Active
• 2013
  • 2013-01-09 EP EP14198973.1A patent/EP2878399B1/en active Active
  • 2013-01-09 EP EP13150673.5A patent/EP2664397B1/en active Active
  • 2013-05-16 US US14/401,107 patent/US9895744B2/en active Active
  • 2013-05-16 WO PCT/US2013/041459 patent/WO2013173651A2/en not_active Ceased
  • 2013-05-16 JP JP2015512862A patent/JP6174686B2/ja active Active
  • 2013-05-16 KR KR1020147035380A patent/KR102098419B1/ko active Active
  • 2013-05-16 BR BR112014028382-6A patent/BR112014028382A2/pt not_active IP Right Cessation
  • 2013-05-16 US US14/401,458 patent/US9849507B2/en active Active
  • 2013-05-16 IN IN10495DEN2014 patent/IN2014DN10495A/en unknown
  • 2013-05-16 RU RU2014150998A patent/RU2639901C2/ru active
  • 2013-05-16 WO PCT/US2013/041457 patent/WO2013173649A2/en not_active Ceased
  • 2013-05-16 CN CN201380037685.0A patent/CN104470654B/zh active Active
• 2017
  • 2017-12-05 US US15/832,382 patent/US10946440B2/en active Active
• 2018
  • 2018-01-29 US US15/882,703 patent/US10646919B2/en active Active

Patent Citations (13)

Non-Patent Citations (2)

Also Published As

Similar Documents

Legal Events