Abstract:
Methods and apparatus for efficient utilization of a cryogen in inerting of solid and molten metals are presented. One method and apparatus of the invention includes providing a source of liquid cryogen; transporting the liquid cryogen through a conduit connected to the source of liquid cryogen to a gas/liquid separator, wherein a portion of the liquid cryogen transforms into gaseous cryogen en route; transporting a portion of the liquid cryogen through a first conduit connecting the gas/liquid separator to a cryogen supply nozzle; transporting the gaseous cryogen through a second conduit connecting the gas/liquid separator to a cryogen supply nozzle; and flowing at least a portion of liquid cryogen and at least a portion of the gaseous cryogen through the cryogen nozzle separately and near a surface of solid or molten metal. Thus liquid that transforms into gaseous cryogen en route from storage is not vented and not wasted, but used in inerting of solid or molten metals.

Description:
BACKGROUND OF THE INVENTION  
         [0001]    1. Brief Description of the Invention  
           [0002]    This invention generally addresses needs in the inerting of molten or solid metals, and in particular methods and apparatus to improve efficiency of use of cryogens such as argon in inerting molten or solid metals.  
           [0003]    2. Related Art  
           [0004]    In the metal casting industry, metals (ferrous or non-ferrous) are melted in a furnace, then poured into molds to solidify into castings. In the foundry melting operations, metals are commonly melted in electric induction furnaces. It is often advantageous to melt the metals under cover of inert gas (usually Ar or N 2 ), rather than expose the metal to atmospheric air. The inert gas cover minimizes oxidation of the metal (including its alloying components), which increases yield and alloy recovery efficiency, and also reduces formation of metallic oxides which can cause casting defects (inclusions). The inert gas cover also reduces the tendency of the molten metal to absorb gases (chiefly O 2  and H 2 ) from the atmosphere, which in turn reduces gas-related casting defects such as porosity. Other benefits of melt surface inerting include reduced slag formation, improved metal fluidity, increased furnace refractory life, and reduced need for de-oxidizers.  
           [0005]    As the electric induction furnace is generally an open-top, batch melter, the inert gas (N 2  or Ar) is usually applied from above the furnace. Inert gas is usually applied throughout the entire melting cycle.  
           [0006]    There are many types of furnace inerting techniques in practice today, but they can generally be classified into two major categories: Gas inerting, in which gaseous N 2  or Ar is (gently) blown into the top of the furnace; and liquid inerting, in which liquid N 2  or Ar is dripped or poured into the top of the furnace. In gas inerting, there are many different configurations of pipes and manifolds or distribution “rings” employed to blow the inert gas into the top of the furnace. These make use of varying gas pressures, velocities, discharge locations and angles of injection. Some try to minimize turbulence by creating gentle laminar flow. Some utilize a “swirling” pattern. Some techniques may employ a collar, shroud or cone-like assembly mounted on top of the furnace. However, with any gas inerting technique, it is difficult to produce and maintain a true inert (0% O 2 ) atmosphere directly at the metal surface, because hot thermal updrafts from within the hot furnace are continually pushing the incoming cold inert gas up and away from the metal surface. As the hot air and gases rise, the induced draft is continually pulling fresh cold air toward the furnace. The injected inert gas will also entrain ambient air along with it as it is injected into the furnace. Because of these effects, it is difficult, if not impossible, for gas inerting techniques to provide a true inert (0% O 2 ) atmosphere directly at the surface of the metal.  
           [0007]    With liquid inerting (such as taught in U.S. Pat. No. 4,806,156), the liquid cryogen (typically N 2  or Ar) has higher density than its gas phase and air, and is much less likely to be pushed up and away from the melt surface by the thermal updrafts. The liquid drops or stream are much better able to fall all the way down to the actual metal surface (hot solid metal or molten metal). After contacting the metal surface, within a short time, the liquid vaporizes into a gas. (The appearance is similar to drops of water “dancing” on a hot pancake griddle). As the N 2  or Ar boils from liquid to gas, it expands volumetrically by a factor of 600-800 times as it rises. This expansion pushes ambient air away from the surface of the metal. In this manner, liquid inerting provides a more effective, true inert (0% O 2 ) atmosphere directly at the metal surface, as compared to gas inerting. With liquid inerting, inert gas usage efficiency is generally increased; i.e. it requires a lower quantity of inert gas to achieve the same performance as gas inerting.  
           [0008]    One drawback of liquid inerting is the difficulty of efficiently delivering the liquid N 2  or Ar to the furnace interior in a liquid state. The liquefied gas (preferably N 2  or Ar) is extremely cold (approximately −184° C.). In the storage tank and distribution piping, the liquid inert gas is continually absorbing heat from the surroundings. This ambient heat pickup manifests itself by boiling some of the liquid to vapor inside the storage tank and distribution piping. The tank and piping is insulated as much as practically possible (typically 7 to 11 cm foam, or vacuum-jacket). The tank-to-furnace piping distance is kept as short as possible (in practice, usually about 15 to 50 m). In spite of these efforts, there is always some amount of liquid that will unavoidably boil to vapor, due to this ambient heat pickup. In addition, some liquid will always “flash” boil to vapor by virtue of pressure reduction alone. The liquid is stored at elevated pressure (typically 2 to 7 bar) in the storage tank, in equilibrium with its vapor phase. Elevated pressure is necessary to provide the driving force to “push” the liquid out of the tank, through the distribution piping. As a matter of practicality, there is usually a vertical elevation rise in the piping which needs to be overcome, and there is some pressure drop through the final liquid discharge device (diffuser). So, as the liquid N 2  or Ar travels through the piping, pressure decreases (eventually to atmospheric pressure at the discharge point), and more and more of the liquid boils to vapor. Due to these combined effects (ambient heat pickup and pressure drop), by the time the liquid N 2  or Ar reaches the discharge point at the furnace, it is estimated that roughly 0.5% to as much as 30% has boiled to vapor, depending on the parameters of the particular system.  
           [0009]    Due to volumetric expansion, the vapor (gas phase) occupies much more space than the liquid. In the piping, this expanding gas restricts, or “chokes” the flow of liquid by occupying a greater and greater portion of the volume available in the pipe. Hence the N 2  or Ar in the pipe can be mostly liquid by mass, but mostly vapor by volume.  
           [0010]    The result is that “sputtering” or “surging” flow is observed at the discharge end of the pipe. “Sputtering” flow is a combination of gas and “spraying” liquid, often unsteady in appearance with time, with respect to the observed amount of liquid flow. “Surging” flow is a more extreme condition, in that there is observed alternating time periods of “gas only” discharge, and “gas plus liquid sputtering” discharge. Sputtering and surging flow is caused by the generated vapor “bubbles” working their way out of the system piping. The greater the percentage of vaporization, the more extreme the observed sputtering and/or surging will be.  
           [0011]    Sputtering or surging flow will reduce the furnace inerting effectiveness, for liquid inerting processes. Compared to a compact, well organized and steady (small) liquid stream, or compared to relatively large droplets, a spray or mist of fine liquid droplets will have much greater surface area, and will therefore absorb heat from the furnace environment much more quickly, vaporizing more quickly, and therefore be less likely to fall all the way down to the metal surface in the liquid state, therefore providing a less effective inert atmosphere at the metal surface. The most effective liquid inerting is provided by a compact, well-organized and steady liquid stream, or by a steady succession of relatively large liquid droplets (minimum liquid surface area).  
           [0012]    It is common to use a diffuser, or tight mesh screen (typically sintered metal filter, approximately 40 micron size), at the discharge of the liquid pipe, in order to minimize sputtering flow. The diffuser “catches” the sputtering spray of gas and small liquid drops, reducing the liquid velocity and re-organizing the drops into larger liquid droplets or a steady liquid stream, which generally drips out the bottom portion of the diffuser, while the gas generally seeps out the top. This diffuser is surrounded by an outer shroud, or cone, which protects the diffuser from molten metal splash, and can also help to organize the emerging liquid droplets into a more focused, single stream. The diffuser/cone assembly, then, helps to provide a more compact, well-organized and steady liquid stream or succession of larger droplets, to improve furnace inerting effectiveness (i.e. reduces the percentage of emerging liquid droplets that evaporate in the furnace).  
           [0013]    However, even by using a diffuser/cone assembly, and after minimizing the piping distance, insulating the pipe and tank as much as possible, and reducing the tank pressure to as low a level as possible, what emerges from the diffuser is still a combination of liquid and gas. Vaporization of some of the liquid to gas is unavoidable. In many cases, sputtering flow, or even surging flow is still observed. The greater the percentage of vapor mixed with gas, the more extreme the sputtering and/or surging will be, and the greater the reduction in furnace inerting effectiveness. As the ambient heat input to the system (tank plus piping) is relatively constant (function of total surface area and temperature difference), the absolute amount of liquid boiling to vapor will be essentially fixed, for a given system. So, as liquid flowrate is increased, the percentage of vapor will be reduced. In practice, then, in order to achieve a stable and consistent liquid flow, as opposed to surging, furnace operators will increase the total N 2  or Ar (liquid) flow higher and higher until surging is eliminated (i.e. flood the system with liquid). In many cases, due to high levels of vaporization (caused by high ambient heat pickup or large pressure drop), the total N 2  or Ar flowrate is higher than what it really needs to be, to provide effective and consistent inerting for a given furnace. This increases operating cost, and can create potential for explosions, by having too large a quantity of liquid pooling on top of the molten metal. Hence, in many cases, if vaporization could be reduced, then total flowrates could be reduced, and operating cost could be reduced while improving operator safety.  
           [0014]    One way to reduce surging and to provide a more consistent, stable liquid flow is to remove the generated gas bubbles from the piping, prior to the diffuser. This is described in U.S. Pat. No. 4,848,751 (special lance). This method utilizes a double-wall (concentric) pipe as the last section of liquid Ar or N 2  piping before the diffuser. A small hole is located in both the inner and outer pipes, pointing vertically upward, with the inner hole at the discharge end and the outer hole at the inlet end. Vapor generated inside the piping is allowed to escape through the inner hole. This cold “sacrificial” vapor travels through the annular region between the inner and outer pipe, counter to the flow of liquid (and gas) in the inner pipe, and escapes to atmosphere through the hole in the outer pipe. Thus, some of the vapor is allowed to escape the piping system before the gas/liquid mixture discharges through the diffuser, and the escaping vapor is utilized to help cool (insulate from further heat pickup) the last section of pipe (generally positioned over the hot furnace) to reduce further evaporation. However, the chemical value of the escaping vapor is wasted, in that it is vented to atmosphere, rather than being sent into the furnace. Also, it is not clear that the size and location of the holes is optimum for each individual installation. Also, since gas bubbles generated in the piping generally will rise to the highest point in the piping system, it is not clear that all of the vapor will consistently and effectively be purged through these holes in the concentric pipe lance, since it is located at the discharge end of the piping (at the furnace), which is usually the lowest point in the system piping.  
           [0015]    Another technique for removing vapor bubbles from the piping is to utilize a gas-liquid phase separator device in the piping. These are sometimes referred to as gas vents, or “keep-full” devices. These are commercially available devices. One or more are mounted, typically, in the highest point in the piping system, generally close to the discharge end. The gas vent device typically includes an internal float and valve mechanism, inside a small chamber. Liquid accumulates in the bottom of the chamber, raising the float by buoyancy force, which closes the gas vent valve on top of the chamber. As gas accumulates in the piping, generally rising to the highest point, it will accumulate in the “dome” or upper portion of the chamber, displacing liquid in the chamber, until eventually the float drops low enough to open the top gas vent valve. This allows gas to vent out the top, until enough liquid re-fills the bottom of the chamber to push the float up, which closes the vent valve. The cycle then repeats, indefinitely. This simple mechanical device helps to continually and automatically vent gas from the system piping, which increases the percentage of liquid, which helps to reduce surging flow, and allows the operator to reduce the total liquid flow required to maintain stable, consistent liquid flow. However, the purged gas is vented to atmosphere, and again, its chemical (inerting) value is wasted. Also, while the gas vent valve periodically opens to vent gas to atmosphere, system pressure is reduced. This can reduce the driving force for pushing liquid through the piping system, causing the operator to increase tank pressure, which results in additional flash vaporization. Or, the periodic venting to atmosphere with subsequent pressure reduction can cause additional liquid to vaporize, due to the premature reduction in pressure.  
           [0016]    Finally, in many liquid inerting systems, a small metering orifice is placed just upstream from the diffuser. This is sized to allow a constant “correct” amount of flow to the diffuser downstream. However, this can compound the severity of observed surging, since all liquid and gas must pass through this small orifice—it can take longer for gas bubbles to work their way through this orifice. Also, with time, as system insulation value deteriorates, and heat input to the system increases, the percent vaporization increases, and the metering orifice may in fact become “too small”, and surging flow is exhibited where at one time it was steady. The operator then is forced to increase the size of the metering orifice (open up the metering orifice valve). It would be an advance in the art if more efficient methods and apparatus were developed to overcome some or all of the above problems.  
         SUMMARY OF THE INVENTION  
         [0017]    In accordance with the present invention, methods and apparatus are presented which overcome some or all of the mentioned disadvantages of previous systems.  
           [0018]    One aspect of the invention is an apparatus for efficient utilization of a cryogen in inerting of molten or solid metals, the apparatus comprising:  
           [0019]    a) a source of liquid cryogen;  
           [0020]    b) a conduit connected to said source of liquid cryogen for transporting said liquid cryogen to a gas/liquid separator (also denoted as a “gas vent device” herein);  
           [0021]    c) a first conduit connecting the gas/liquid separator to a cryogen inerting nozzle and adapted to supply liquid cryogen to the cryogen inerting nozzle, the cryogen inerting nozzle positioned over molten or solid metal in a container; and  
           [0022]    d) a second conduit connecting the gas/liquid separator to the container at a position over the molten or solid metal, the second conduit adapted to supply gaseous cryogen to the molten or solid metal.  
           [0023]    Preferably, the second conduit connects the gas/liquid separator to an outer section of the cryogen inerting nozzle, as further described herein. Preferred apparatus also comprise insulation for the first and second conduits to maintain temperature as low as possible.  
           [0024]    A second aspect of the invention is a method for efficient utilization of a cryogen in inerting of solid or molten metals, the method comprising:  
           [0025]    a) providing a source of liquid cryogen;  
           [0026]    b) transporting said liquid cryogen through a conduit connected to the source of liquid cryogen to a gas/liquid separator (also denoted a gas vent device herein), wherein a portion of the liquid cryogen transforms into gaseous cryogen;  
           [0027]    c) transporting a portion of the liquid cryogen through a first conduit connecting the gas/liquid separator to a cryogen supply nozzle positioned over solid or molten metal in a container;  
           [0028]    d) transporting at least a portion of said gaseous cryogen through a second conduit connecting the gas/liquid separator to the container, and preferably to the cryogen inerting nozzle; and  
           [0029]    e) flowing the portion of liquid cryogen through the cryogen inerting nozzle near a surface of solid or molten metal in the container, and flowing at least a portion of the gaseous cryogen near the same surface of solid or molten metal, preferably through the cryogen inerting nozzle.  
           [0030]    Liquid inerting effectiveness can be decreased due to vaporization of liquid in the system piping, as described. Removal of this gas before reaching the discharge diffuser can improve inerting effectiveness. The new method utilizes this vented gas in the furnace to assist with inerting, rather than venting the gas to atmosphere. The known diffuser/cone assembly is replaced with a novel cryogen supply nozzle, preferably shaped like a cone, which incorporates a second connection for this gas. The gas vented from the piping (via a gas vent device) is fed to this novel cryogen supply nozzle. Preferably, a pressure regulator or similar device can be used in the gas vent line to maintain the desired back pressure on the gas vent device and system piping, while venting gas from the piping system. 
       
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS  
       [0031]    [0031]FIG. 1 is a schematic process flow diagram of methods and apparatus of the invention in a first embodiment;  
         [0032]    [0032]FIG. 2 is a schematic process flow diagram of a second embodiment of process and apparatus in accordance with the present invention;  
         [0033]    [0033]FIG. 3 is a cross-section, side elevation view of a cryogen inerting nozzle in accordance with one embodiment of the invention;  
         [0034]    [0034]FIG. 4 is a view of the cryogen inerting nozzle of FIG. 3 viewed from one end denoted A-A in FIG. 3;  
         [0035]    [0035]FIG. 4A illustrates an end elevation sectional view of an alternate embodiment of the device illustrated in FIG. 3; and  
         [0036]    [0036]FIG. 5 is a cross-sectional, side elevation view of an alternate cryogen inerting nozzle in accordance with the present invention.  
     
    
     DESCRIPTION OF PREFERRED EMBODIMENTS  
       [0037]    Referring now to the drawing figures, FIG. 1 illustrates schematically one embodiment of the process and apparatus in accordance with the present invention for inerting solid or molten metals. FIG. 1 illustrates a bulk liquid cryogen storage tank, where the cryogen is preferably N 2 , Ar, CO 2 . The liquid cryogen is preferably in a saturated liquid state, where the saturated liquid is in equilibrium with vapor phase at an elevated pressure. Liquid bulk storage tank  2  feeds liquid cryogen via a shut-off valve  4  through distribution piping  8 , where distribution pipe  8  preferably includes a safety pressure relief valve  6  to relieve in case of overpressure. Distribution piping  8  is generally outdoors, originates at ground level, and generally and preferably is routed to an elevated header inside of a melt shop or other building, and then has individual “drop legs” as explained herein. The drop legs are typically flex hoses which are routed to each furnace or pair of furnaces. The distribution piping can have one or more drop legs from each header.  
         [0038]    The system in FIG. 1 preferably includes a shut-off valve  10  which connects the distribution piping to a gas liquid separation device  12 , which preferably includes a chamber with an internal float connected to an internal upper gas vent valve. A safety pressure relief valve  14  can also be included as shown. Liquid cryogen flows through piping  11  through a flex hose  18 , liquid shut-off valve  20 , a metering orifice  21 , and piping connection  24 , and eventually exits through a diffuser  26  which is located inside cryogen inerting nozzle  28 . Preferably, the piping connection  24  is a double wall lance pipe as described in U.S. Pat. No. 4,848,751, incorporated herein by reference. Gas liquid separation device  12  could be also a simple pipe “tee,” (preferably larger than piping  11  in diameter), installed at or near the highest point, with a gas vent pointing vertically.  
         [0039]    Following the gas flow through the system illustrated in FIG. 1, a pressure regulator or in-line pressure relief valve  16  is preferably provided. Pressure regulator  16  maintains the desired back pressure to the gas liquid separation device  12 , and to distribution piping  8 , rather than allowing the gas vent  12  to discharge to atmosphere, which can reduce system pressure. A flex hose  34  connects with a gas adjusting valve  36 , piping connection  31 , and nozzle  33  for allowing gaseous cryogen to be routed toward the molten or solid metal  1 , being held in container  32 . Preferably, an adjusting valve or orifice can be provided as indicated at  38 , to allow additional gas purged from the liquid line  18  and  24  into the gas line  31 . Valve  38  preferably includes a check valve (one-way valve) to allow gas to flow into the gas system, but not to allow gas to flow back into the liquid piping system  18  and  24 . Valve connection  38  may also include a pressure regulator or in-line relief valve, to maintain pressure in liquid lines  11 ,  18 , and  24 .  
         [0040]    Also indicated in FIG. 1 is a connection  40  for routing liquid cryogen to another furnace, and a connection  42  for routing gaseous cryogen to another container. Distribution pipe  8  can be a header pipe to distribute cryogen to multiple furnace containers  32 . Cryogen can be supplied to each furnace via its own nozzles  28 ,  31  and  33 , and diffuser  26 . Hence, items  10 - 38  can be replicated as needed for multiple furnaces.  
         [0041]    Referring now to FIG. 2, illustrated is another embodiment of a method and apparatus suitable for practicing the invention. The system illustrated in FIG. 2 differs only from that illustrated in FIG. 1 in the construction of cryogen inerting nozzle  28 , which has also a gas providing connection  35  taking feed from gaseous cryogen conduit  31 . This version of the nozzle  28  and connection  35  is better viewed with reference to FIGS. 3 and 4. FIG. 3 is a side elevation cross-sectional view of the nozzle  28  and connection  35 , illustrating certain dimensions. Liquid cryogen enters at  27 , while gaseous cryogen enters at  29 . The internal diameter of liquid cryogen nozzle  28 , denoted as D, preferably ranges from about 2 cm up to about 10 cm, more preferably ranging from about 2 cm to about 5 cm, depending on the amount of cryogen desired. The exit end of nozzle  28  has a larger diameter D′, than the internal diameter D of nozzle  28 . This slight flaring of the exit of the nozzle provides certain advantages, for example, the liquid may have a better drip characteristic, and the gaseous cryogen may spread to a wider area of the molten or solid metal in container  32 . The ratio of a diameter D divided by D′ typically and preferably ranges from about 0.5 to 1, up to 1 to 1. FIG. 3 also illustrates diameter d of diffuser  26 , with diameter d ranging from about 5% up to about 90% of the diameter D. It should be recognized by those skilled in the art that diffuser  26  need not be cylindrical or round in construction but could be rectangular or any other shape including a T-shaped element. A distance l from terminal tip of diffuser  26  to the entrance of connection  35  typically ranges from about 0 to about 3 diameters equal to d, the diameter of diffuser  26 . Lengths denoted as L d  and L n  are also illustrated in FIG. 3. The dimension L d  corresponds to the axial length of diffuser  26 , while the length denoted L n  denotes the distance from the end of diffuser  26  to the exit of nozzle  28 . Preferably, the distance L d  ranges from about 0.5 to about 3 times the diameter D, while the length dimension L n  is preferably 0.1 to 1.5 times the length dimension L d .  
         [0042]    [0042]FIG. 4 illustrates the end view along the view A-A denoted in FIG. 3, illustrating that diffuser  26  is substantially centered within a cylindrical cryogen inerting nozzle  28 . It should be noted that this is preferred only and that diffuser  26  could be located in a non-central location in reference to the axial center line of nozzle  28 . Also as illustrated in FIG. 4, gaseous cryogen connection  35  is indicated as being connected non-tangentially to nozzle  28 , however, connection  35  could be tangentially connected as indicated in FIG. 4A. FIG. 4A shows an alternate embodiment where gas connection  35  is tangentially connected to cryogen delivery nozzle  28 . The embodiment of FIG. 4A would tend to give a swirling motion to the gaseous cryogen as it exits nozzle  28 . It can also be envisioned to install swirling elements on an internal surface of nozzle  28  to create more swirl for gaseous cryogen. With either FIG. 4 OR  4 A, it can also be envisioned to utilize a substantially larger diameter D of the nozzle  28 , to provide broader gas coverage in the furnace  32 .  
         [0043]    [0043]FIG. 5 illustrates an alternate embodiment  50  of a nozzle useful for delivering liquid and gaseous cryogen for the purposes of the invention. A nozzle  28  as in previous embodiments is fitted with an annular section  52  basically surrounding the nozzle  28 , and creating an annular space for gaseous cryogen to enter through a piping connection  54 . Thus, only liquid would exit through the nozzle  28  via diffuser  26 , whereas, gaseous cryogen would exit the annular region formed between nozzle  28  and annular section  52 . Annular section  52  may be connected to nozzle  28  such as by welds  56  and  58 . Piping connection  54  may be non-tangentially connected to annular connection  52  or it may be tangentially connected to provide a swirling flow of cryogen.  
       EXAMPLE  
       [0044]    At initial startup of liquid cryogen flow (such as after a weekend shutdown or the like), valves  4 ,  10 ,  20 , and  21  are fully opened. Since the piping ( 8 ,  11 , etc.) is initially warm (room temperature), liquid cryogen will be vaporized as it travels through the pipe. Typically, several minutes are required in order to cool the piping system to cryogenic temperatures, and attain steady state flow conditions. Hence valve  21  is kept full open, initially, while 100% gas discharges through the diffuser  26  and nozzle  28 . As liquid begins to appear out the nozzle  28 , this is an indication that the piping is beginning to cool, and valve  21  is gradually closed in order to maintain the desired (small) liquid flow rate. At steady state conditions, when the piping system has fully cooled to its ultimate steady state temperature, ideally valve  21  will be fully closed, and the desired liquid flowrate is maintained through the fixed metering orifice hole in valve  21 . Valve  36  (gas vent line) is opened at some point during this cool down process (either at beginning or after some time).  
         [0045]    Once the system has reached steady state with respect to piping cool down, then valve  36  and/or regulator  16  can be adjusted, along with valve  21 , in order to provide optimum performance (consistent, stable liquid flow, without surging or sputtering, at minimum flowrate). Without the gas vent line  34  and/or gas vent device  12 , in many cases, total cryogen flow is increased unnecessarily (by opening valve  21 ) in order to maintain consistent, stable liquid flow without surging. By opening and adjusting the (optional) one-way valve  38 , further fine-tuning can be accomplished, by creating an additional “gas escape path” for vapor generated in the piping in close proximity to the hot furnace, i.e. pipe  24 .  
         [0046]    In one experimental setup, at steady state flow conditions, when valve  36  (gas vent valve) was closed, it was observed that valve  21  had to be opened wider in order to maintain stable, consistent liquid flow without surging. When valve  36  was opened, creating an escape path for gas generated in the piping, then stable liquid flow (no surging) could be maintained with valve  21  in a more closed position. This suggests that by segregating the liquid and gas flow in this manner, the required overall flowrate of cryogen for a given system potentially can be reduced. Or, at minimum, the consistency and quality of liquid cryogen delivered to the furnace is improved, thereby increasing inerting effectiveness. And with the novel technique of utilizing the vented gas in the furnace (via nozzle  33  or connection  35 ), as opposed to wasting it by venting to atmosphere, efficient utilization of cryogen is further improved.  
         [0047]    Recognizing that in the absence of a gas vent line  34  or a gas vent device  12 , a certain percentage of the cryogen discharging from the diffuser  26  and nozzle  28  will always be gas, the novelty is that, first, the gas and liquid flow is segregated, in order to provide greater uniformity, stability and consistency of liquid flow (with potentially reduced overall flow requirement), and second, the vented gas is now routed back to the furnace in order to utilize its inerting value, rather than wasting it by venting to atmosphere, which further contributes to increased efficiency of cryogen utilization.  
         [0048]    This apparatus and method, therefore, can provide greater economy (reduced overall cryogen consumption) with improved inerting effectiveness (through more consistent, stable liquid flow) while improving operator safety (minimized liquid flowrate reduces risk of explosion from liquid “pooling” on molten metal surface).  
         [0049]    Preferred processes for practicing the present invention have been described. It will be understood and readily apparent to the artisan that many changes and modifications may be made to the above-described embodiments without departing from the spirit and the scope of the present invention. The foregoing is illustrative only and that other embodiments of the integrated process can be employed without departing from the true scope of the invention defined in the following claims