US3755915A - Investment casting shell mold drying and desiccant reactivation apparatus - Google Patents

Investment casting shell mold drying and desiccant reactivation apparatus Download PDF

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Publication number
US3755915A
US3755915A US00206771A US3755915DA US3755915A US 3755915 A US3755915 A US 3755915A US 00206771 A US00206771 A US 00206771A US 3755915D A US3755915D A US 3755915DA US 3755915 A US3755915 A US 3755915A
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desiccant
funnel
bed
chamber
drying
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US00206771A
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C Nagell
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ChampionX LLC
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Nalco Chemical Co
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C9/00—Moulds or cores; Moulding processes
    • B22C9/12—Treating moulds or cores, e.g. drying, hardening

Definitions

  • ABSTRACT Drying slurry coatings on expendable patterns in making investment casting ceramic shell molds by moving the slurry coated patterns slowly through a fluidized bed of desiccant, and continuously reactivating the desiccant to provide an automated desiccant shell drying and desiccant reactivation process.
  • This invention relates in general to the making of ceramic shell molds used in the investment casting of metals, and, more particularly, to drying of slurry or slurry and stucco coats applied to an expendable pattern in the formation of a shell mold and, still more particularly, to shell drying in a fluidized bed of desiccant,
  • Ceramic shell molds produced for the investment casting of metals are formed by successively coating and drying an expendable pattern, such as a pattern made of wax, plastic or other suitable material, where the coatings comprise slurry or slurry and stucco sand.
  • a slurry layer may include aqueous colloidal silica sol having suspended therein silica particles of 200 mesh, such as a granular fused silica, while the stucco material may include silica particles, such as granular fused silica of+l mesh.
  • any number of layers of slurry and stucco material may be used in order to provide the desired characteristic for a shell mold, it being appreciated that a shell mold may be made up of one or more primary coats, together with one or more back-up coats and a final sealer coat.
  • the silica particle size may vary in the primary and back-up coats in order to provide the desired structural characteristics.
  • An example of some specific shell mold structures are disclosed in U. S. Pat. No. 2,948,032.
  • each slurry coat with or without stucco material must be dried before a successive coat may be applied. Drying generally has been accomplished by allowing the coats to set up in a controlled atmosphere, where it would take on the average a day and a half to produce a shell mold having about six laminations.
  • the present invention concerns drying of shell mold coatings where expendable patterns with coatings to be dried are advanced by a conveyor into, through, and out of a fluidized bed of desiccant.
  • the conveyor includes a monorail arranged in connection with a tank having a fluidized bed of desiccant and trolleys are provided on the monorail from which may be suspended expendable patterns.
  • the expendable patterns are coated with slurry or slurry and stucco materials and then advanced along the monorail through the fluidized bed of desiccant and returned to the point where additional coatings of slurry or slurry and stucco may be applied for successful drying operations.
  • the desiccant in the fluidized bed absorbs water from the slurry layers on the expendable patterns to dry the layers, and is continuously being reactivated by removing desiccant from one end of the fluidized bed, reactivating the removed desiccant and returning desiccant in reactivated condition to the other end of the bed.
  • the invention provides an automated shell drying and drying material reactivation method and apparatus which will reduce the overall drying time substantially in order to reduce the time needed to produce ceramic shell molds. Further, inasmuch as automated apparatus is provided, the cost of producing shell molds is similarly reduced by reduction of manual labor, and greater efficiency in shell drying is achieved.
  • Another object of this invention is in the provision of a new and improved method and apparatus for shell drying of ceramic shell molds which dries the molds in a fluidized desiccant bed and continually recirculates and reactivates the desiccant.
  • a further object of this invention is to provide a new apparatus for reactivating desiccant used in ceramic shell mold drying.
  • FIG. I is a diagrammatic top plan view of an installation illustrating the present invention which includes a conveyor and an associated apparatus for drying ceramic shell molds by passing expendable patterns with coatings to be dried through a fluidized bed of desiccant, and apparatus for reactivating the desiccant;
  • FIG. 2 is a side elevational view of the apparatus of FIG. I;
  • FIG. 3 is a greatly enlarged longitudinal sectional view taken through the fluidized bed desiccant drying tank and showing some parts in elevation for purposes of clarity;
  • FIG. 4 is a vertical transverse view taken along line 4-4 of FIG. 3;
  • FIG. 5 is an enlarged elevational view of the desiccant reactivator according to the invention showing some parts broken away for purposes of clarity;
  • FIG. 6 is a still further enlarged fragmentary detailed sectional view taken through the reactivator hopper and illustrating the discharge end of the reactivator tube;
  • FIG. 7 is a top plan view of the reactivator hopper
  • FIG. 8 is a vertical sectional view taken through the cooling tower utilized in the reactivating loop
  • FIG. 9 is a top plan view of the cooling tower
  • FIG. 10 is a greatly enlarged elevational view of a modified funnel structure that may be utilized in the fluidized bed tank or the cooling tower for discharging desiccant from a fluidized bed;
  • FIG. 11 is a top plan view of the funnel structure of FIG. 10.
  • apparatus according to the invention for drying slurry and slurry and stucco coatings on expendable patterns in making ceramic shell molds, and reactivating the drying material or desiccant used for drying is illustrated in one form where a conveyor 15 along which expendable patterns in the form of wax clusters or trees or the like may be advanced between coating and drying stations.
  • the conveyor includes a monorail or track 16 adapted to support any number of trolleys 17, there being illustrated in FIG. 2 trolleys 17a, 17b and 170 where the trolleys support therefrom expendable patterns 18.
  • a tank 19 containing fluidized desiccant provides the drying station wherein the coated expendable patterns are moved through the desiccant bed by a pusher which controls movement of the trolleys along the monorail track 16.
  • a closed desiccant reactivation loop 20 continuously takes desiccant from one end of the tank 19, reactivates the desiccant in a reactivator 21, cools the desiccant in a cooling tower 22, then returns it to the desiccant tank in reactivated condition.
  • a coating station ahead of the drying tank 19 is provided which includes a pair of slurry pots 23 and a pair of stucco bins 24.
  • the slurry pots may include two different slurries such as where a primary and backup slurry arrangement is utilized for making up a shell mold.
  • the stucco bins would provide stucco sand of different sizes for use on primary and secondary layers.
  • the stucco sand is fluidized in the stucco bins to facilitate the immersion and withdrawal of a pattern in the sand.
  • an expendable pattern would first be immersed in the slurry of one of the pots and/or next immersed in the stucco sand of one of the bins, after which it would be subjected to a drying operation.
  • the expendable patterns may be easily demounted from the trolleys and thereafter remounted during the coating operation.
  • an air set loop 30 having a power driven pusher member 31 may then be used only for the first and last coats of slurry on the expendable pattern. Thereafter the air set loop may be by-passed for successive coatings which may be directly desiccant dried.
  • the path of'travel along the monorail track for the expendable patterns is counterclockwise.
  • the trolleys having coated patterns to be dried are first advanced to a downwardly inclined section 32 of the monorail track where the trolleys advance by gravity to an indexing wheel 33.
  • the indexing wheel 33 will be operated in synchronism with an endless pusher 34 which sequentially advances the trolleys along a section 35 of monorail track directly mounted above the drying tank 19 and along an upwardly inclined section of track 36 to a turn-around section 37.
  • a plurality of equally spaced apart pusher members 38 are provided on the endless pusher 34 which maintain the trolleys in spaced relation along the track section 35 during the advancing of the coated expendable patterns through the drying tank 19.
  • the desiccant bed in the tank 19 is fluidized, it is self-leveling and presents negligible resistance to the patterns as they are moving through the bed. Accordingly, the power needed for driving the endless pusher 34 need not be too great and only sufficient to advance the trolleys and expendable patterns along the upwardly inclined section 36 of the track to the turn-around section 37.
  • the time period in which the patterns will be driven through the drying bed of desiccant depends upon the complexity of the pattern wherein the drying time may vary anywhere from 12 to 20 minutes but in any event would be long enough to effect the desired drying action on the coating.
  • the first slurry coat and the last slurry coat which would be a sealer are initially traversed through the air set loop 30, while the intermediate coats need not be subjected to an air dry operation and may therefore go directly into the fluidized bed of desiccant.
  • trolley 17a has just been picked up by a pusher on the pusher member 35, while trolley 17b has been released by the indexer 33 to be caught by the next pusher on the pusher member, and trolley 170 is being held by the indexer until the pusher member is clear to accept the next trolley.
  • the trolleys and patterns are returned to the opposite end of the conveyor by gravitational force which drives them along a downwardly inclined track section 40 to the base of an upwardly inclined track section 41 where an endless pusher member 42 suitably synchronized in movement relative to the endless pusher 34 drives the trolleys and patterns up the inclined section 41 to a second turnaround track section 43. That brings the trolleys and patterns around to the horizontal inlet track section 44, where they may dwell while the patterns may be removed for subsequent coating operations and thereafter advanced to the downwardly inclined track section 32 feeding to the desiccant drying tank or removed for other processing. Accordingly, the monorail track 16 of the conveyor 15 provides a continoous loop for movement of the trolleys and expendable patterns during the drying operation which essentially automates the drying operation of the slurry coats.
  • the desiccant drying tank 19 may take any suitable form, it is preferably elongated, as illustrated, to provide an elongated fluidized bed of desiccant through which the expendable patterns with coatings to be dried may be advanced to effect the proper drying operation.
  • the tank 19 includes a bottom wall 50, opposite end walls 51 and 52 and opposite side walls 53 and 54.
  • the end walls 51 and 52 include at their upper ends flared wall sections 51a and 52a in order to provide clearance for the patterns as they enter and leave the bed of desiccant.
  • Spaced upwardly from the bottom wall on suitable. supports is a defuser plate 55 upon which the desiccant bed 56 is supported and through which air is forced to effect the fluidizing of the desiccant.
  • the defuser plate may take any suitable form wherein it is sufficiently porous to allow air to be forced therethrough and may, for example, be of the porous ceramic type which is commercially available.
  • Partitions 57 and 58 arranged between the defuser plate 55 and the bottom wall 50 of the tank define air chambers 59, and 61, having respectivelyair inlets 59a, 60a and 61a.
  • Compressed air is delivered to the air chambers and forced upwardly through the defuser plate through the bed of desiccant 56 and out the upper surface of the bed, thereby fluidizing the desiccant.
  • Any suitable desiccant may be used, such as a silica gel, preferably having a particle size of-ZO mesh.
  • the desiccant be of a type that will create a mechanical bond between water and the desiccant where subsequent application of heat will remove at least part of the water.
  • the fluidized bed of desiccant is selfleveling and self-mixing by the air flow.
  • the amount of compressed air delivered to the air chambers is such as to provide the desired fluidizing condition in the bed. It has not been heretofore known to dry shell molds by moving a coated expendable pattern continuously through a fluidized bed of desiccant.
  • the reactivator 21 and cooling tower 22 in the reactivation loop continuously removes desiccant from one end of the tank and replenishes the desiccant in the other end of the tank.
  • desiccant is removed from the tank by mounting a funnel 65 in inverted position at the outlet end of the tank 19.
  • the large end of the funnel is spaced slightly above the defuser plate 55 and the necked down end of the funnel is connected to a conduit 66 leading from the tank.
  • Any suitable conduit may be used providing it is essentially smooth on its interior surface to reduce friction to the lowest possible amount.
  • Desiccant by being in the fluidized condition in the tank, will flow around the bottom end of the funnel 65 and part of the air moving up through the defuser plate will be trapped within the funnel, which will force desiccant through the funnel, the conduit 66, and to the reactivatdr 21 where the desiccant is reactivated.
  • Reactivated desiccant is reintroduced into the tank 19 at the inlet end of the tank through an inlet nozzle 67 which may merely take the form of the open end of a piece of conduit.
  • the reactivator 21 includes a vertically arranged reactivator tube 70 into which desiccant to be reactivated is delivered through conduit 66 to a fitting arranged within the reactivator tube having its open end arranged substantially centrally within the tube and facing upwardly.
  • heat in the form of hot gases is introduced through an inlet 71 by any suitable means.
  • the hot gases produced by a gas flame would be discharged into the inlet 71. It should be appreciated, however, that hot gases may be produced by any suitable means, and which will be introduced at the lower end of the reactivator tube 70.
  • compressed air is introduced into the tube through a compressed air line 72, which terminates within the reactivator tube in the form of a fitting arranged centrally within the tube and with an open end facing upwardly.
  • the compressed air at ambient temperature, mixes with and tempers the hot gases and then forces or draws the mixture upwardly in the tube, and which will then pick up desiccant as it is discharged from the desiccant inlet and remove water from the desiccant as it then travels upwardly through the tube to be discharged through the upper end 73 of the tube into a hopper 74 which collects the desiccant following reactivation in the reactivation tube.
  • the hopper 74 is defined by an inclined bottom wall 75, an upstanding cylindrical wall 76 and a cover or top wall 77.
  • the hopper and reactivation tube are suitably supported together and in upright position by a post 78 suitably anchored on the floor.
  • the upper end of the reactivation tube 70 which extends within the hopper 74 is doublewalled to inhibit the conducting of heat to the desiccant in the hopper.
  • the cover 77 includes a fine mesh screen 80, closing an opening in the cover, allowing the pressure within the collection chamber to equalize with the atmosphere.
  • the screen is of about 80 mesh so that it will only allow fines to escape from the collecting hopper.
  • the angle of the bottom wall 76 is dietated by the angle of repose of the desiccant and, for
  • the temperature of the hot gases from the heat source and the amount of compressed air at ambient preferably combines to provide a temperature at the desiccant exit of about 400 to 420 F. which is believed to be the most effective for removing water from the desiccant.
  • the opening in the cover which gives the desired amount of action with respect to the proper movement of desiccant through the reactivation tube and into the collecting hopper 74.. Movement of desiccant through the conduit 66 into the reactivation tube may be regulated by a valve 81 in the conduit. Similarly, the discharge of desiccant from the collecting hopper 74 may be regulated by a valve 82. It can also be appreciated that suitable instruments may be provided for controlling the compressed air supply and the heat supply so that the desired removal of absorbed water from the desiccant is accomplished by the reac tivator 21.
  • the desiccant is delivered through a conduit or pipe 85 to the cooling tower 22 which removes a sufficient amount of heat so that when the desiccant is returned to the fluidized bed it is about the same temperature as the desiccant already in the bed, which is mandatory in order to prevent improper drying of the slurry coats and improper heating of the expendable patterns.
  • the expendable patterns and the coatings thereon are at about room temperature and therefore the desiccant into which they are immersed must also be at about room temperature.
  • the cooling tower 22 includes a bottom wall 86, an upstanding cylindrical side wall 87 and a top wall 88. Spaced upwardly from the bottom wall 86 is a defuser plate 89 which defines therebelow an air chamber 90.
  • the defuser plate is of porous ceramic like the defuser plate in the desiccant tank 19, which permits fluidizing of the desiccant while it is in the cooling tower.
  • a suitable source of compressed air is supplied to the air chamber 90 through a pipe 91 and a regulating valve 92.
  • the conduit 85 which brings desiccant from the reactivator under gravitational force discharges the desiccant within the cooling tower into a cooling chamber 92.
  • the desiccant is introduced into the cooling chamber from an inlet 94 at the upper erid of the cooling chamber where it falls by gravitational force downwardly toward the defuser plate 89.
  • the air within the air chamber 90 is forced upwardly through the defuser plate and through desiccant as it moves downwardly to the defuser plate.
  • the air moves upwardly through the cooling chamber 93 and then out a standpipe 95 having its discharge end covered by fine mesh screen 96. This prevents a positive pressure from building up within the cooling chamber which would prevent desiccant from entering the cooling chamber through the inlet 94.
  • the open end of the standpipe 95 is on an angle in order to increase the screen area.
  • the screen is about 80 mesh size to prevent the desiccant from being accidentally discharged from the cooling tower.
  • a funnel 100 arranged in inverted position on the defuser plate 89 with the large end resting on the plate and the necked down end connected to a discharge conduit or pipe 101 leading from the cooling tower and back to the desiccant drying tank 19 to the inlet nozzle 67.
  • a plurality of openings 102 are formed in the funnel 100 and through which desiccant gravitationally falls and enters the inside of the funnel 100. Air trapped by the funnel forces the desiccant within the funnel upwardly out the cooling tower through the discharge conduit 101 and back to the desiccant drying tank.
  • part of the air moving through the defuser plate becomes trapped in the funnel 100 and the other part of the air moves up and around the funnel to maintain the desiccant in the cooling tower in fluidized condition.
  • the fluidizing air being at ambient will therefore cool the desiccant as it moves downwardly through the cooling tower to be discharged therefrom back to the drying tank.
  • the heat absorbed by the air is then removed from the cooling tower through the standpipe 95.
  • the temperature of the desiccant incoming to the cooling tower would be about l20F. and the outgoing desiccant temperature would be about ambient.
  • the reactivator and cooling tower assembly could be remotely located from the ceramic shell mold building area so as to remove the heat generated by the reactivator from the shell building area. This would permit the maintaining of a more constant temperature in the shell building area in order to eliminate any adverse effect on the shells or expendable patterns.
  • the compressed air used by the drying tank, the reactivator, and the cooling tower is taken from a single manifold and thereafter volume regulated as needed.
  • FIGS. and 11 Another form of funnel structure that may be utilized for removing desiccant from a fluidized bed is illustrated in FIGS. and 11, it being appreciated that the funnel shown in these Figs. and generally designated by the numeral 105 could be utilized in the desiccant drying tank or in the cooling tower.
  • the funnel 105 includes a conical wall 106 having the large end facing downwardly and the small end facing upwardly, a cylindrical necked down wall 107 at the upper end of the conical wall, and a cylindrical wall 108 extendin downwardly from the lower larger conical wall.
  • the necked down wall 107 defines at its upper end an outlet 109 which may be connected to a conduit for delivering desiccant to another station.
  • the lower end of the cylindrical wall 108 is open to define an air inlet 110 into which air is introduced to force desiccant upwardly through the conical wall 106 and to the outlet 109.
  • a plurality of upwardly opening scoops 111 are formed along the lower cylindrical wall 108 which have inlet openings 112 facing outwardly that receive desiccant from the bed, and outlet openings 113 through which desiccant is discharged into and within the cylindrical wall 108 and into the air stream.
  • the funnel 105 illustrates another funnel structure that may be used to remove desiccant from a fluidized bed.
  • Apparatus for desiccant drying investment casting shell molds and reactivating the desiccant comprising, an elongated drying tank containing a fluidized bed of desiccant, conveyor means for supporting and transporting expendable patterns dipped in slurry or slurry and stucco through the desiccant bed, and means continuously taking desiccant from the bed, reactivating the desiccant, and returning it to the bed.
  • said last named means includes a funnel-shaped member and conduit for taking desiccant from the tank, said tank including a defuser plate for supporting the desiccant and means forcing air upwardly therethrough, said funnel-shaped member including a large open end facing the defuser plate and in slightly spaced relation therefrom to define an opening with the plate through which desiccant passes to a point below the funnel, and a necked end connected to the conduit, wherein the funnel traps air to drive desiccant through the conduit.
  • the reactivator includes an elongated upstanding tube terminating in an upper open end, a hot gases inlet at the lower end of the tube, means producing and driving hot gases into said hot gases inlet, a desiccant inlet in the tube spaced upwardly from the hot gases inlet, a compressed air inlet in the tube spaced intermediate the hot gases inlet and the desiccant inlet, a hopper defining a collecting chamber mounted on the upper end of the tube so the upper open end is arranged within said chamber, a cover on said hopper having a screened opening, a bottom wall in the hopper supporting regenerated desiccant, said bottom wall being at an angle, and a discharge opening for the hopper at the lower end of the bottom wall to permit gravitational discharge of desiccant.
  • the cooling tower includes an upstanding body having a desiccant receiving chamber and an air chamber separated by a defuser plate upon which is supported a bed of desiccant, an inlet to the desiccant chamber connected to the reactivator, means for supplying compressed air to the air chamber to force air upward through the plate, a funnel in said desiccant chamber having a large open end resting on the defuser plate and an opposing necked end connected to conduit leading from the tower, openings in said funnel through which desiccant falls to the inside of the funnel, and a screened opening in the upper end of the tower to permit communication between the desiccant chamber and atmosphere, wherein the compressed air fluidizes and cools the desiccant in the desiccant chamber and forces desiccant within the funnel through the conduit.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Ceramic Products (AREA)
  • Silicon Compounds (AREA)
  • Casting Devices For Molds (AREA)
  • Drying Of Solid Materials (AREA)
US00206771A 1971-12-10 1971-12-10 Investment casting shell mold drying and desiccant reactivation apparatus Expired - Lifetime US3755915A (en)

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US20677171A 1971-12-10 1971-12-10

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US (1) US3755915A (enExample)
CA (1) CA989588A (enExample)
DE (1) DE2246459C3 (enExample)
FR (1) FR2162354B1 (enExample)
GB (1) GB1388704A (enExample)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3858499A (en) * 1971-03-24 1975-01-07 Res Dev Systems Inc Dehydration and packaging of foodstuffs
US4888213A (en) * 1988-04-19 1989-12-19 Brunswick Corporation Method and apparatus for drying coatings on articles
US5104594A (en) * 1989-02-02 1992-04-14 Hochtief Aktiengesellschaft Vorm. Gebr. Helfmann Drying the surface of a fresh concrete body
US5577333A (en) * 1994-12-21 1996-11-26 The Dow Chemical Company Solid media parts drying using fluidized beds
US5885493A (en) * 1997-11-04 1999-03-23 Lockheed Martin Energy Research Corporation Method of drying articles
US6749006B1 (en) * 2000-10-16 2004-06-15 Howmet Research Corporation Method of making investment casting molds
US20070266585A1 (en) * 2005-04-16 2007-11-22 Michael Arno Portable Disposable Air/Gas Dryer
US20090071621A1 (en) * 2007-09-18 2009-03-19 Sturm, Ruger & Company, Inc. Method and system for drying casting molds
US8087450B2 (en) 2007-01-29 2012-01-03 Evonik Degussa Corporation Fumed metal oxides for investment casting

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441695A (en) * 1944-05-31 1948-05-18 Austenal Lab Inc Casting mold
US3254625A (en) * 1960-03-31 1966-06-07 Cecil W Armstrong Apparatus for producing a fluidized bed of pulverant material
US3307232A (en) * 1965-01-04 1967-03-07 Edward J Mellen Jr Method and apparatus for forming shell molds by the use of a fluidized bed drying system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2441695A (en) * 1944-05-31 1948-05-18 Austenal Lab Inc Casting mold
US3254625A (en) * 1960-03-31 1966-06-07 Cecil W Armstrong Apparatus for producing a fluidized bed of pulverant material
US3307232A (en) * 1965-01-04 1967-03-07 Edward J Mellen Jr Method and apparatus for forming shell molds by the use of a fluidized bed drying system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3858499A (en) * 1971-03-24 1975-01-07 Res Dev Systems Inc Dehydration and packaging of foodstuffs
US4888213A (en) * 1988-04-19 1989-12-19 Brunswick Corporation Method and apparatus for drying coatings on articles
US5104594A (en) * 1989-02-02 1992-04-14 Hochtief Aktiengesellschaft Vorm. Gebr. Helfmann Drying the surface of a fresh concrete body
US5577333A (en) * 1994-12-21 1996-11-26 The Dow Chemical Company Solid media parts drying using fluidized beds
US5885493A (en) * 1997-11-04 1999-03-23 Lockheed Martin Energy Research Corporation Method of drying articles
US6749006B1 (en) * 2000-10-16 2004-06-15 Howmet Research Corporation Method of making investment casting molds
US20070266585A1 (en) * 2005-04-16 2007-11-22 Michael Arno Portable Disposable Air/Gas Dryer
US8087450B2 (en) 2007-01-29 2012-01-03 Evonik Degussa Corporation Fumed metal oxides for investment casting
US20090071621A1 (en) * 2007-09-18 2009-03-19 Sturm, Ruger & Company, Inc. Method and system for drying casting molds
WO2009039032A1 (en) * 2007-09-18 2009-03-26 Sturm, Ruger, & Company, Inc. Method and system for drying casting molds
US8006744B2 (en) 2007-09-18 2011-08-30 Sturm, Ruger & Company, Inc. Method and system for drying casting molds

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DE2246459B2 (de) 1974-03-14
DE2246459A1 (de) 1973-06-14
GB1388704A (en) 1975-03-26
FR2162354A1 (enExample) 1973-07-20
DE2246459C3 (de) 1974-10-17
FR2162354B1 (enExample) 1975-03-14
CA989588A (en) 1976-05-25

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