US3773300A - Plant for processing casting resin - Google Patents

Plant for processing casting resin Download PDF

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Publication number
US3773300A
US3773300A US00228084A US3773300DA US3773300A US 3773300 A US3773300 A US 3773300A US 00228084 A US00228084 A US 00228084A US 3773300D A US3773300D A US 3773300DA US 3773300 A US3773300 A US 3773300A
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Prior art keywords
chamber
premixer
cylinder
piston
plant
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Expired - Lifetime
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US00228084A
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English (en)
Inventor
E Hauser
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Pfeiffer A Vakuumtechnik dt GmbH
PFEIFFER VAKUUMTECHNIK
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PFEIFFER VAKUUMTECHNIK
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Priority claimed from DE1902486A external-priority patent/DE1902486C3/de
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
    • B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00—Mixing; Kneading
    • B29B7/74—Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7476—Systems, i.e. flow charts or diagrams; Plants
    • B29B7/7485—Systems, i.e. flow charts or diagrams; Plants with consecutive mixers, e.g. with premixing some of the components
    • B29B7/749—Systems, i.e. flow charts or diagrams; Plants with consecutive mixers, e.g. with premixing some of the components with stirring means for the individual components before they are mixed together
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/40—Mixers with shaking, oscillating, or vibrating mechanisms with an axially oscillating rotary stirrer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F31/00—Mixers with shaking, oscillating, or vibrating mechanisms
    • B01F31/44—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement
    • B01F31/441—Mixers with shaking, oscillating, or vibrating mechanisms with stirrers performing an oscillatory, vibratory or shaking movement performing a rectilinear reciprocating movement
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/50—Improvements relating to the production of bulk chemicals
    • Y02P20/582—Recycling of unreacted starting or intermediate materials

Definitions

  • the pump piston has a reciprocating rod which extends upwardly through the premixer chamber where it supports and actuates a mixing disk.
  • Metering pumps receive the material from the premixers and deliver'it into a final mixer.
  • another reciprocating rod is provided with a mixing element for the final mixing and delivery of the materials to a metering head or a simple casting valve.
  • Valves are provided for controlling and integrating the various operations of the plant.
  • the invention is directed to a plant for processing casting resin formed of at least two constituent materials with the plant comprising at least onepremixer in which a vacuum can be established, a final mixer, and a metering pump for supplying selected amounts of the constituent materials from the premixer to the final mixer. More specifically, the invention concerns the construction of the premixer and the final mixer in which correlated reciprocating actions are provided for mixing and discharging the constituent materials.
  • Casting resins are used for many purposes.
  • One preferred field for such resins is in electrical engineering where they are used primarily for impregnating coils and other electrical parts where a good electrical insulation and good protection against external influences, such as moisture, are important.
  • a plant for preparing and casting multiple constituent material resins must meet the following requirements:
  • the constituent materials of the casting resin must be capable of being mixed rapidly and thoroughly in an exactly measured composition and it must be possible to use viscous casting materials containing a large amount of filler material.
  • the constituent materials must be capable of being degassed under a vacuum. Any new absorption of gas after the degassing operation must be avoided. It must be possible to measure the casting resin exactly in the processing plant in accordance with the size of the workpiece to be formed. To maintain the plant operative, hardening residues such as hardening casting resin or filler material must be avoided in the different parts of the plant.
  • premixers with stirrers are utilized in which electric motors are used as the drive means.
  • the discharge of the constituent materials from the premixers to metering pumps requires either the ventilation of the premixer chamber or the location of the premixer at such a height that the column of the constituent material can no longer be retained by a vacuum. If vacuum conditions are removed from the premixer chamber there is the risk that gases will again be absorbed into the materials, on the other hand by locating the premixer chamber at a considerable height greatly increases the cost of the plant and, frequently, for construction reasons it is not possible to locate the premixer chamber in such a manner.
  • the constituent materials are supplied to the final mixer in predetermined amounts and the amount charged into the mixer must be cast within an admissible pot time. If interruptions in the casting operation are to be avoided, it is important if an additional charge of the materials can be mixed during the casting of one charge.
  • the primary object of the present invention is to provide a processing plant in which the premixers can be maintained under a vacuum even while the constituent materials are being discharged so that continuous operation of the plant is possible.
  • the problems experienced in the past are overcome by employing a piston pump at the outlet from the premixer so that the pump cylinder extends inwardly into the body of material contained in the premixer and an opening is provided through the wall of the cylinder in communication with the body of material for admitting the material into the cylinder at the end of the suction stroke of the piston so that the material can be discharged during the exhaust stroke of the piston.
  • the constituent materials can be supplied from the premixer to the metering pump while maintaining the vacuum within the premixer and without positioning the premixer at a considerable height above the metering pump.
  • Such discharge of the material from the premixer is possible since no marked pressure gradient is required when the material is discharged by means of the piston pump. Since the cylinder of the pump is located below and extends into the body of material in the premixer when its opening is uncovered, the material flows by gravity into the cylinder. As the pump piston performs its pressure or exhaust stroke on the material within the cylinder, it is fed by positive displacement, without any overpressure, into the metering pump. Since the material is discharged by the piston the metering pump can be located above the outlet from the premixer. This arrangement is of great advantage for the construction of the entire plant.
  • a reciprocating rod extends through the chamber of the premixer into the cylinder of the piston pump.
  • a mixing element is supported on the rod and during a portion of the reciprocating stroke of the rod the mixing element passes through the material in the chamber.
  • the mixing element can be in the form of one or several members extending transversely from the rod, such as disks, and the piston portion of the pump is mounted on the lower end of the reciprocating rod for effecting its upward and downward movement within the pump.
  • its operation can be carried out with only the reciprocating movements of the rod.
  • the stirring-in of rising gas bubbles does not take place in the operation of the premixer constructed in accordance with the present invention.
  • the reciprocating action employed for the premixers can also be used for the metering pumps and the final mixer.
  • this type of drive it is possible to control the plant in such a way that the different reciprocating drives can be coordinated in accordance with the extent to which the final mixer is filled.
  • the premixer performs a discharge or exhaust stroke
  • the metering pump performs a suction stroke so that the constituent materials can be delivered into the metering pump.
  • a mixing element within the final mixer also performs a correlated operation.
  • a mixing element within the chamber of the final mixer which is reciprocated by means of a rod, with the rod being connected to the piston of a double acting pressure cylinder to provide the requisite reciprocating operation.
  • the mixing element can be disk-shaped and formed of multiple parts some only slightly spaced from the wall of the chamber and others spaced a greater distance-
  • FIG. 1 is a schematic representation of a plant for preparing'a casting resin in accordance with the present invention
  • FIG. 2 is a vertical sectional view through a mixer such as used in the plant shown in FIG. 1 with its reciprocating rod in its downward or discharge stroke;
  • FIG. 3 is a vertical sectional view similar to FIG. 2, however, the reciprocating bar is in its upward position, that is, the end of its suction stroke;
  • FIG. 4 is a horizontal sectional view taken along the line IV-IV in FIG. 2;
  • FIG. is a vertical sectional view through a final mixer as utilized in the plant set forth in FIG. 1;
  • FIG..6 is a diagram representing the timed operation of the different parts of the plant as set forth in FIG. 1.
  • FIG. I a plant for processing and mixing the constituent materials for a casting resin is shown comprised of the following elements: A pair of premixers 50, 51, a vacuum pump 52 is communication with the two premixers, a pair of metering pumps 53, 54 each arranged in communication with one of the premixers, a final mixer 55 arranged to receive the constituent materials from the metering pumps, a fine metering head 56 in communication with the outlet from the final mixer, and a vacuum casting tank 57 arranged to receive the casting resin from the metering head.
  • a solvent tank 58 is connected to the final mixer.
  • the operation of the plant is obtained through a pair of reversing valves 59, 60, another control valve 61 which is disposed in communication with the metering head, and two pairs of valves 62 and 63, 64 and 65, each pair in communication with the outlet lines from one of the metering pumps.
  • the outlets from the premixers 50, 51 are connected by pipe lines 66, 67 with the metering pumps 53, 54, respectively.
  • the metering pumps 53, 54 are each provided with a outlet line 68, 69, respectively, and each of the outlet lines branches into a pair of outlets 70, 72 and 71, 73.
  • the branch outlets 70, '71 form bypass lines returning to the premixers 50, 51, respectively, and each of the branch outlets contains a valve 62, 65 respectively.
  • the other two branch outlets 72, 73 contain valves 63, 64 and terminate at the final mixer 55.
  • the outlet from the final mixer is connected by a line 74 to the fine metering head 56.
  • FIG. 5 While the plant is shown schematically in FIGQI, in FIGS. 2, 3 and 4 the premixers 50, 51 are set forth in detail and, similarly, the details of the final mixer 55 are illustrated in FIG. 5.
  • the premixer 50 is formed of an upright tank 1 through which a rod 2 is reciprocated', that is, moved in an up and down manner by a double-acting pressure cylinder 3 located above the upper end of the tank.
  • a pump piston 4 is secured to the lower end of the rod 2 and moves in the vertical direction within a pump cylinder 5.
  • Se cured to and extending transversely from the rod 2 within the tank 1 and above the pump cylinder 5 is a mixing element 6 in the form of a disk.
  • the tank 1 has a vertically arranged cylindrically shaped upper part 7, a frusto conically shaped part 8 is secured to the lower end of the upper part and extends downwardly to another cylindrically shaped part 9 which has a diameter substantially smaller than that of the diameter of the part 7.
  • the top of the tank 1 is sealed in a vacuum tight manner by means of a cover 10.
  • a filler hole is arranged and is closed by a smaller cover 10.
  • Adjacent the upper end of the tank, on the left-hand side as shown in FIG. 2, a suction pipe 11 is provided which connects the interior of the tank with the vacuum pump 52, see FIG. 1.
  • Another pipe connection 12 is arranged on the opposite side of the tank from the vacuum connection for the return of excess material into the premixer from the metering pump 53, in FIG. 1 note the branch line 70.
  • the tank At the lower end of its upper part 7 the tank is carried by means of brackets 41, 42 on supports.
  • the rod 2 is connected to a piston 13 which is vertically displaceable within the cylindrically shaped chamber 14 of the double-acting pressure cylinder 3.
  • the piston 13 is sealed against the inner wall of the chamber 14.
  • a pair of pressure lines 15 and 16 are connected to the lower and upper ends of the chamber 14 for alternately admitting a pressure medium, for instance, compressed air, for reciprocating the rod in an upward and downward movement through the premixer 50.
  • the piston 4 consists of a bell-shaped upper part 17 and a screen plate 18 extending transversely across the lower end face of the upper part and forming a chamber 20 within the upper part.
  • a plurality of bores 19 are provided through the screen plate communicating between the chamber 20 and the interior of the cylinder 5.
  • the lower end of the rod 2 is hollow and provides a bore 21 extending upwardly from the chamber 20 to a point within the upper part 7 of the premixer chamber.
  • four lines 22a, 22b, 22 c, and 22d are equally angularly spaced about the rod and extend radially outwardly toward but in spaced relation-.
  • Each of the lines 22a 22d contains a valve 23 and terminates in a nozzle 24 which, as can be seen in FIG. 4, extends tangentially to a circle passing through the outer ends of the lines.
  • the nozzles 24 are directed slightly downwardly providing the spray action indicated by the dotted lines shown in FIGS. 2 and 4.
  • the outside diameter of the bell-shaped upper part 17 forming the piston 4 has a diameter which is smaller than the inside diameter of the cylinder so that an annular space 35 is formed between the exterior of the piston and the inner surface of the pump cylinder 5.
  • the pump cylinder 5 At its lower end the pump cylinder 5 is closed by a scree-plate 25 containing a plurality of bores 26.
  • the cylinder 5 extends upwardly into the lower end of the premixer chamber formed by the frusto-conically shaped part 8.
  • Four feed openings 27 are provided in the circumferential wall of the cylinder 5 for providing communication between the interior of the cylinder and the body of material located within the premixer chamber.
  • the lower end of the bottom part 9 of the tank 1 is closed by means of a cover 28 to which a pipe connection 29 is attached.
  • the pipe connection 29 extends downwardly and terminates in a valve 30 and, as indicated in FIG. 1, the line 66 extends from valve 30 to the metering pump 53.
  • the mixing element 6 secured to the rod 2 within the premixer chamber has a disk-like form whose outside diameter is less than the inside diameter of the cylindrically shaped part 7 of the tank so that an annular space 34 is provided between the outer edge of the mixing element and the inner surface of the premixer chamber.
  • the constituent material 36 is supplied to the premixer chamber to a level so that the chamber is about half filled, that is, up to the level 37 as shown in FIGS. 2 and 3. If the material 36 is to be degassed, the chamber formed by the tank 1 is connected by means of the suction pipe 11 to the vacuum pump 52. The exhaust of gases under the vacuum is indicated by the dotted lines 38 in FIG. 2.
  • the rod 2 is reciprocated in an up and down manner within the premixer. In this type of drive overstressing of the parts is avoided since the pressure acting within the cylinder 3 limits the driving forces correspondingly.
  • the rod 2 is in the process of moving downwardly. As the rod 2 moves downwardly the disk-like mixing element 6 is forced into the body of material 36 so that it flows around the peripheral edges of the element through the annular space 34 as indicated by the arrows 40.
  • the upper dead center position f the piston 4 is represented, that is, at of end of its suction stroke and at the beginning of its exhaust or discharge stroke. Additionally, it will be noted that the mixing element 6 has been lifted upwardly by the rod 2 until it is positioned above the level 37 of the body of material 36 within the premixer chamber. In the position shown in FIG. 3, the piston 4 is located above the openings 27 which communicate between the interior of the cylinder 5 and the body of material 36 within the premixer chamber. As a result, the material 36 flows by gravit into the cylinder and such action can be increased by an overpressure on the level 37 when the plant is not operating under a vacuum.
  • the mixing element 6 When the mixing element 6 has been lifted upwardly out of the body of material 36, it carries some of the material along with it so that the surface of the material is considerably increased which is advantageous for the degasification of the material. As indicated above, the dotted lines indicate how the gas is withdrawn from the material.
  • the final mixer is formed of a lower body part on which a cylindrically shaped upper part 76 is mounted.
  • the lower body part has an upwardly extending opening through which a rod 77 extends into the upper part 76.
  • the rod 77 is rigidly attached to a piston 78 located within a cylinder 81 formed in the lower end of the lower part 75.
  • a piston ring 79 is inserted into an annular slot 80 formed about the periphery of the piston 78 and forms a seal with the inner wall of the part 75 within the cylinder 81.
  • the piston 78 is displaceable in the vertical direction through the cylinder 81 by means of a line 82 which opens into the upper end of the cylinder and another line 84 which opens through a cover 83 into the cylinder.
  • the cover 83 closes the lower end of the cylinder.
  • a chamber 85 Spaced above the cylinder 81 a chamber 85 encircles the rod 77 and a pair of lines 86, 87 extending through the wall of the lower part 75 are connected to the chamber 85 for flushing the space within the chamber.
  • a gasket 88 provides a seal about the rod 77 and above the chamber 85 in the lower part 75 a gasket provides a seal about the rod 77 at a point closely spaced below lower end of the upper part 76.
  • the upper end of the lower body part 75 forms a closure for the lower end of a mixing chamber 89 within the upper part 76 of the final mixer.
  • the rod 77 extends into the mixing chamber 89 and a mixing element 91 is located at its upper end within the chamber.
  • the mixing element 91 is composed of and the inner surface of the mixing chamber is nonuniform in width as indicated by the reference numerals 99, 100 which indicate the wider portion of the annular gap for each of these disks.
  • an outlet line 101 extends downwardly and outwardly through the lower part 75 of the final mixer.
  • a pair of inletlines 102, 103 are provided at the upper end of the mixing chamber.
  • the line 102 opens into an enclosed annular duct 104 which is limited on the outside by the interior surface of the upper part 76 and on the inside by a ringshaped part 105 having a U-shaped cross section for forming the annular duct 104.
  • a plurality of openings 106 are provided through the ring-shaped part 105 communicating between the annular duct 104 and the interior of the mixing chamber 89.
  • the'line 103 terminates in an annular duct 107 which is defined on the outside by the interior surface of the upper part 76 and on the inside by a storage piston 108.
  • the storage piston 108 is located within the opening formed by the cylindrically shaped upper part above the mixing chamber 89 and a plurality of vertically spaced gaskets 109, 110 and 111 are provided between the exterior surface of the piston 108 and the inner surface of the upper part 76. Between the gaskets 109, 1 10 an annular duct 112 is provided between the outer surface of the piston 108 and the inner surface of the upper part 76 and the duct is connected to a pair of lines 1 13, 1 14 for performing a flushing or rinsing cycle about the storage piston.
  • annular duct 115 is provided between the outer surface of the storage piston and the inner surface of the upper part 76 and a feeler member 116 extends through an opening in the upper part 76 into the annular duct 115.
  • the feeler member 1 16 is biased into surface contact with the outer surface of the storage piston.
  • an annular groove 117 is provided about the storage piston 108 located above the level of the feeler 116, however, if the storage piston drops downwardly until the annular slot is at the level of the feeler member 116, the feeler member is biased inwardly by means of a contact spring 118 acting on its outer end so that the feeler member seats itself within the annular groove 117 and a contact stud 119 on the spring 118 comes in contact with a corresponding and oppositely disposed contact stud 120.
  • the storage piston 108 is located within a chamber 121 which has a larger diameter than the remainder of the opening through the upper part 76 through which the storage piston projects.
  • a cover 122 provides a closure for the upper part 76 and a line 123 formed in the cover communicates with the top of the chamber 121.
  • the storage piston has a narrow outwardly extending flange 124 which acts as a stop to limit the downward movement of the storage piston through the vertically disposed opening within the upper part 76.
  • the plant works in the following manner:
  • the constituent materials for forming the castin resin are initially prepared in the premixers 50, 51 that is, they are degassed by means of a vacuum produced by the vacuum pump 52 and they are mixed with filler material, and or other colorants and modifying substances.
  • the premixers 50, 51 operate along in connection with the vacuum pump.
  • the premixers are controlled by means of electrical time switches, not shown, which actuate the reversing valve 59 for affording the desired reciprocating action.
  • the metering pumps 53, 54 are rinsed with the valves 62 and opened, in order to prevent the deposit of solids.
  • the pneumatically or hydraulically operated valves 62, 63, 64 and 65 are arranged so that only the return or bypass lines 70, 71 are open for returning the materials to the premixer chamber but preventing passage to the final mixer 55.
  • the casting process is commenced electrically.
  • the working cycle of the premixer depends on the metering pumps 53, 54 and on the final mixer 55 that is, the control valves 59 and 60 are actuated synchronously to provide the proper correlation of operation.
  • the pistons, not shown, of the meter ing pumps 53, 54 move into the receiving position, the pistons 4 in the cylinders 5 at the lower ends of the premixers 50, 51 displace the constituent materials to the metering pumps so that a rapid supply is provided.
  • the valves 63, 64 are closed and the valves 62, 65 are opened so that any excess material supplied by the pistons can flow back into the premixer chambers.
  • the final mixer 55 also performs a mixing movement. It is possible to provide several mixing movements. to the metering pump stroke, however, this is unnecessary in most cases.
  • control contacts 1 19 If the storage volume, that is the mixing chamber 89, in the final mixer is empty, as is the case at the outset of operations, or if it is used up to the minimum level during the casting operation, the control contacts 1 19,
  • the reciprocating rods 2 in the premixers 50, 51 move into the upper position that is, the end of the suction and the beginning of the discharge stroke and the mixing element 91 in the final mixer is moved into the starting position.
  • valves For admitting the constituent materials into the final mixer 55, the valves are at first reversed, that is, the valves 62, 65 are closed and the valves 63, 64 are opened.
  • the mixture within the final mixer 55 is under pressure and is cast intermittently from the fine metering head into the vacuum casting tank 57 or under atmospheric pressure conditions. Since a regulable pressure of several atmospheres is available for filling the metering head 56, it is possible to supply charges of the casting resing in rapid succession.
  • the pistons move into the receiving position and they are replenished with the constituent materials from the premixers.
  • the constituent materials flow to the final mixer through the lines 102, 103.
  • the material passing through the V line103 flows through the narrow gap at the lower end of the annular duct 107 formed between the outer surface of the storage piston 108 and the inner surface of through the openings 106 into the mixing chamber 89 in the form of jets which mix with the material entering through the line 103 which flows downwardly past the openings 106. Due to this type of constituent material supply to the mixing chamber 89, a good mixing of the materials is achieved.
  • the mixing element 91 moves upwardly and downwardly within the mixing chamber 89, the mixing of the constituent materials supplied into the upper end of the chamber is continued.
  • the mixing element moves upwardly the mixed constituent materials pass through the bores 98 in the upper disk 92 and are forced by the disks 93 and 94 to flow through a somewhat spiraling path due to the spacing between the outer edges of the disks 93 and 94 and the inner surface of the mixing chamber.
  • the mixed constituent materials are forced through the bores 98 in the lowermost disk 96 and as a result of this action a very thorough mixing is accomplished.
  • the constituent materials in the premixer can be prepared under a vacuum, the subsequent final mixing can also be carried under vacuum conditions and then the mixed constituent materials can be cast under atmospheric pressure.
  • the rate of flow of the mixture of the constituent materials from the final mixer 55 is controlled by a pot time relay, not shown, and is made dependent on the number of strokes of the metering pump per unit of time.
  • the risk that the final mixer 55 or the fine metering head 56 will become jammed is thus indicated optically or acoustically and can be eliminated by increasing the casting velocity (washing out with fresh material) or by flushing the final mixer and the other parts coming into contact with the mixed material with solvents from the tank 58.
  • the fine metering head 56 is replaced by a simple casting valve with a reducing nozzle.
  • the maximum rate of flow through the casting nozzle is so great that the metering pumps 53, 54 are ready to deliver the constituent materials when the final mixer makes contact.
  • the storage volume of the final mixer is never completely used up.
  • the supply of the casting material into the mold can be performed by the metering pumps 53, 54.
  • the sum of the weights of the individual constituent materials is equal to the weight of the material being supplied from the casting valve.
  • the processing plant has a heating system so that all parts coming in contact with the material can be heated.
  • the control of the plant is described below based on the time diagram represented in FIG. 6. Though the control is automatic, it is extremely simple since the movements of the pneumatically or hydraulically operated parts run in synchronization during the processing and casting operation.
  • the top line indicates the activity of the fine metering head 56. It will be noted that the top line is divided into sections designated a and b, during the time period designated a the casting cycle performed by the fine metering head is carried out, and during the time period b the mixed constituent materials are charged from the final mixer into the fine metering. head. It is assumed in the diagram that the casting cycle is somewhat longer than the charging interval.
  • the contact 119, 120 When the amount of the mixed casting material from the final mixer has dropped to a level that the storage piston is displaced downwardly under the action of air pressure introduced above it though the line 123 so that the feeler 116 engages the slot 117 then the contact 119, 120 is closed and the elapsed time indicated by the line 0 is reached. Accordingly, at the time designated by the line 0, an electric timer is connected for a time period indicated by d. During the time period d the metering pumps 53, 54 complete a discharge stroke for supplying material into the final mixer 55. While this filling process is being accomplished, the casting operation continues, as can be noted from the diagram in FIG. 6. After about another six casting cycles the contact 119, 120 closes again and the timer commences the time period d for filling the final mixer.
  • the lines e to m indicate the operation of various parts of the processing plant.
  • the heavy solid line indicates that the mixing element 91 within the final mixer 55 is in its upper position, that is, in the position adjacent the lower end of the storage piston 108.
  • the line f indicates when the mixing element of the final mixer is moving downwardly within the mixing chamber 89.
  • the lines g and h indicate the activity of the metering pumps 53, 54.
  • the metering pumps deliver the constituent materials to the final mixer during the time intervals d and discontinue operation at the termination of the time period 01.
  • the time period d is completed the metering pumps return to the charging position and are filled by the pistons 4 within the premixers which are moving downwardly into the discharge or exhaust position. After the casting cycles again reach the time designated c the filled metering pumps commence a new delivery stroke for filling the final mixer 55.
  • the lines i and k represent the operation of the premixers 50, 51.
  • the reciprocating parts of the premixers 50, 51 are in their lower positions and when the time c is reached they move rapidly into their upper end position.
  • the cylinder 5 at the lower ends or outlets of the premixers 50, 51 is filled with the constituent material from the body of material in the premixer chamber.
  • the lines land m indicate the operation of the valves 62, 63, 64 and 65.
  • the solid portions designate the open position and the broken or dashed portions designate the closed position.
  • the valves 62, 65 that is the valves in the return lines 70, 71 are closed and the valves 63, 64 are open that is, the valves controlling flow from the metering pumps into the final mixer. Accordingly, during the time period d the constituent materials can flow only into the final mixer since they can flow in no other direction with the valves 62, 65 closed.
  • valves 63, 64 are closed and the valves 62, 65 are opened so that any excess constituent materials can flow through the lines 70 and 71 back into the premixer chambers.
  • intensive flushing or rinsing is provided for all parts which might be exposed to such conditions.
  • the rinsing or flushing action is accomplished by the metering pumps which are provided for this purpose with stepped delivery pistons, that is, the metering pumps also deliver the suitable flushing or rinsing agent along with the constituent material.
  • the flushing agent is supplied to and removed from the final mixer through the lines 86, 87 and 113, 114, as shown in FIG. 5.
  • a plant for preparing casting resin from at least two constituent materials in which the plant comprises at least one upwardly extending premixer having an outlet at its lower end, said premixer having an upwardly extending axis and forming an axially extending chamber in which a vacuum can be established and said chamber arranged to receive one of the constituent materials and to provide a level of the material below the upper limit of the chamber in said premixer, a final mixer, at least one metering pump for supplying selected quantities of the constituent material from said premixer to said final mixer, and conduit means for conveying the material from said premixer to said metering pump and from said metering pump to said final mixer, wherein the improvement comprises means located at the outlet end of said premixer, said means forming a cylinder within said premixer which is in communication with the lower end of said chamber formed therein, said cylinder having an inlet and an outlet with its outlet located below its inlet and adjacent to the outlet from said premixer, said means including a piston pump having a piston axially displaceable
  • a plant as set forth in claim 1, wherein said piston is axially displaceable through said cylinder in a suction stroke which terminates at a location remote from the outlet from said cylinder and an exhaust stroke which terminates at a location closer to said outlet than the location of the termination of the suction stroke, said cylinder extending from the outlet of said premixer into the body of material within said chamber in said premixer, said cylinder having at least one opening in the circumferential periphery thereof intermediate its ends for admitting material from the body of material in said premixer into said cylinder, and the opening in said cylinder being located between the outlet end of said cylinder and the location of the end of the suction stroke of said piston within said cylinder 3.
  • a plant as set forth in claim 2, wherein a plate is secured to and extends across the lower end of said cylinder adjacent the outlet end of said premixer, and said plate having a plurality of openings therethrough for discharging material from said cylinder during the downward exhaust stroke of said piston within said cylinder.
  • a plant as set forth in claim 2, wherein a bypass line having an inlet end and an outlet end is secured at its inlet end to the outlet from said premixer and at its outlet end into said chamber in said premixer above the level of the body of material therein.
  • said means includes a reciprocating rod positioned within and extending axially upwardly through said chamber in said premixer, said piston in said piston pump is secured to the lower end of said reciprocating rod and is located within said cylinder for executing a suction stroke and an exhaust stroke therein, and said mixing element in said chamber formed by said premixer is secured to and extends transversely from said reciprocating rod within said chamber in said premixer.
  • a plant as set forth in claim 6, wherein a pressure cylinder disposed above said premixer and in axially alignment with said reciprocating rod, the upper end of said reciprocating rod extending into said pressure cylinder, a piston secured to the upper end of said reciprocating rod within said pressurecylindcr, and means for supplying a pressurized fluid into said pressure cylinder on the opposite sides of said piston for effecting the reciprocating action of said reciprocating rod.
  • sly-73300 8.
  • said piston of said piston pump located on the lower end of said reciprocating rod within said cylinder comprises walls forming the chamber in said piston which is open at its downward end, a plate extending across and forming a closure for the lower end of said chamber in said piston, said plate having a plurality of bores therethrough communicating between the interior of said cylinder and the interior of said chamber in said piston, and said reciprocating rod forming the bore which extends axially through said reciprocating rod from said chamber in said piston upwardly to a location in said reciprocating rod above the level of the body of material within said chamber in said premixer so that material entering into the chamber formed by said piston passes upwardly through said bore for return into the body of material within said premixer chamber.
  • a plant as set forth in claim 9, wherein means secured to said reciprocating rod in communication with said bore therethrough for returning the material into said premixer chamber, said means comprising an overpressure valve through which the material passes before it is returned into said premixer chamber.
  • said means connected to said bore in said reciprocating rod comprising a plurality of lines extending radially outwardly from said reciprocating rod, one said overpressure valve located in each said line, and a nozzle secured to the outlet end of each said line for discharging the material into said premixer chamber with a tangential component relative to an imaginary cylinder within said premixer chamber passing through the outlet ends of said lines and a downward component directed toward the level of the body of material within said premixer chamber.
  • a plant as set forth in claim 1, wherein means for initiating a reciprocating action within said final mixer and said metering pump.
  • said final mixer comprises a lower upwardly extending part and an upper part extending upwardly from the upper end of said lower part, said upper part forming an upwardly extending cylindrical space closed at its lower end by the upper end of said lower part and having an inside surface with an inside diameter, said lower part forming a pressure cylinder and an opening extending through said lower part from said pressure cylinder to said cylindrical space in said upper part, and said means for effecting reciprocating action in said final mixer comprosing a reciprocating rod extending up wardly from said pressure cylinder in said lower part into said cylindrical space in said upper part, seal means disposed between said reciprocating rod and said lower part in the opening extending through said lower part communicating with said cylindrical space in said upper part, a piston secured to the lower end of said reciprocating rod within said pressure cylinder in said lower part, and a mixing element secured to the upper end of said reciprocating rod within said cylindrical space in said upper part.
  • said mixing element secured to the upper end of said reciprocating rod in said final mixer comprises a diskshaped element having an outside diameter slightly smaller than the inside diameter of said cylindrical space in said upper part so that a narrow annular space is provided between the outside periphery of said mixing element and the inside surface of said cylindrical space in said upper part, and said disk-shaped element being perforated to permit constituent materials supplied into said cylindrical space in said upper part to pass therethrough.
  • said mixing element comprises a plurality of transversely arranged disks secured to said reciprocating rod and extending transversely therefrom, said disks comprising an upper disk and a lower disk having a diameter slightly smaller than the inside diameter of said cylindrical space in said upper part for forming narrow annular gaps between the outside periphery of said disks and the inside surface of said cylindrical space in said upper part, said upper and lower disks being perforated for passing constituent materials therethrough, and at least one intermediate disk spaced between said upper and lower disks and having an eccentric peripheral surface spaced a greater distance from the inside surface of said cylindrical space in said upper part at one point than at a diametrically opposed point so that an annular space of non-uniform width is formed between the outside of said intermediate disk and the inside surface of said cylindrical space in said upper part, so that material passing through the perforations in said upper and lower disks effects at least partly circular motion due to the eccentric shape of said intermediate disk.
  • a plant as set forth in claim 14, wherein means are disposed within said cylindrical in said upper part of said final mixer for forming a movable transversely extending wall defining the upper end of a mixing chamber formed within the lower part of said cylindrical within said upper part.
  • said means comprises a storage piston, a resiliently biased feeler member extending through the wall of said upper part of said final mixer into contact with a surface on said storage piston defining the upper end of the mixing chamber, a groove in the surface on said storage piston for receiving said feeler when said means move downwardly, a first electrical contact positioned on the outer surface of said upper part in engagement with said feeler, a second electrical contact disposed on the outside of said upper part and arranged to be contacted by said electrical contact when said feeler is seated within the groove in the surface of said storage piston when said storage piston has reached a predetermined lower level within said cylindrical space in said upper part.
  • a plant as set forth in claim 18, wherein means are provided for responding to the contact between said first electrical contact and said second electrical contact for effecting coordinated reciprocal movements in said premixers, metering pumps, and final mixer for supplying constituent materials from the cylinder in said premixer to said metering pumps and then to the mixing chamber in said final mixer.
  • said means defining the upperlimit of the'mixing chamber within said cylindrical space in said upper part of said final mixer comprises a storage piston located within said cylindrical space and extending upwardly therethrough above said mixing element therein, said cylindrical space in said upper part forming a pressure chamber at its upper end within which the upper end of said storage piston is located, seal means disposed between the sides of said storage piston and the inside surface of said cylindrical space in said upper part, and an inlet duct connected to said pressure chamber for admitting a pressurized fluid therein for urging said storage piston in the downward direction through said cylindrical space in the upper part.
  • a plant as set forth in claim 20, wherein said lower part of said fixed mixer having an annular groove formed in the opening extending between said pressure chamber and the upper end of said lower part, an annular groove formed in the inner surface of said upper part in the range of said storage piston and duct means communicating with both of said annular grooves for effecting a flushing action therethrough.
  • a plant as set forth in claim 20, wherein means disposed within said cylinder in the upper part of said final mixer for supplying constituent materials into the mixing chamber formed in the lower end of said cylindrical space in said upper part.
  • said means for supplying constituent materials into said mixing chamber comprises an annular member positioned within said cylinder and having a portion of its outer surface in contact with the inner surface of said cylindrical space in said upper part, said annular member extending transversely across said cylindrical space in said upper part and having an annular channelshaped groove formed about its outer surface so that in combination with the inner surface of said cylindrical space in said upper part said groove provides an annular inlet chamber, an inlet duct extending through said upper part into communication with said inlet chamher, said annular member having a plurality of angularly spaced openings therethrough communicating between the inlet chamber and the interior of said mixing chamber in said cylindrical space in said upper part for supplying a constituent material into said mixing chamber in a plurality of jets.
  • a plant as set forth in claim 23, wherein said upper part having an annular groove formed in its inner surface extending upwardly from the upper end of said annular member, the lower end of said storage piston being disposed opposite said annular groove and forming therewith a second inlet chamber for supplying constituent material into said mixing chamber in said final mixer, the outside diameter of said storage piston being slightly less than the inside diameter of said annular member located below said annular groove so that a narrow annular outlet opening is provided from said second inlet chamber for admitting a thin film-like flow of the constituent material from said second inlet chamber into the mixing chamber passing downwardly through the jets from said inlet chamber formed by said annular member.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
US00228084A 1969-01-18 1972-02-22 Plant for processing casting resin Expired - Lifetime US3773300A (en)

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DE1902486A DE1902486C3 (de) 1969-01-18 1969-01-18 Mischer, insbesondere Vormischer für Anlagen zur Verarbeitung von Mehrkomponenten-Gießharzen

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CH (1) CH504942A (de)
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GB (1) GB1300092A (de)

Cited By (28)

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FR2418068A1 (fr) * 1978-02-25 1979-09-21 Hedrich Vakuumanlagen Wilhelm Dispositifs de controle pour installations de preparation de resine de moulage par coulee
WO1980001495A1 (fr) * 1979-01-16 1980-07-24 Sred Az Nii Pritodnogo Gaza Methode et dispositif de preparation d'une boue de forage
US4252447A (en) * 1978-06-23 1981-02-24 Borodin Sergei I Peristaltic batcher and peristaltic batching system realized therewith
US4291991A (en) * 1978-08-28 1981-09-29 Bayer Aktiengesellschaft Apparatus for the preparation of a reaction mixture from fluid components
US4688944A (en) * 1984-08-24 1987-08-25 Fritz Mumenthaler Mixer head for plastics material components
US5217146A (en) * 1991-04-03 1993-06-08 Wilhelm Hedrich Vakumanlagen GmbH & Co. KG Device for filling one or more molds with flowable materials
US5257722A (en) * 1991-04-03 1993-11-02 Wilhelm Hedrich Vakuumanlagen Gmbh & Co. Kg Device for filling one or more molds with flowable materials
US5423607A (en) * 1991-05-03 1995-06-13 Dolco Packaging Corp. Method for blending diverse blowing agents
US5529212A (en) * 1991-06-13 1996-06-25 Verfahrenstechnik Hubers Gmbh Method of and apparatus for transporting and conditioning casting materials and for charging casting machines with them
US5636972A (en) * 1993-04-26 1997-06-10 Carbotech Device for extrusion of two component synthetic resins
WO2000024556A1 (de) * 1998-10-22 2000-05-04 Krauss-Maffei Kunststofftechnik Gmbh Homogenisier- und temperierbehälter
EP0895844A3 (de) * 1997-08-04 2001-01-03 Bruno Blatt Harzeinfüllgefäss mit Schliessvorrichtung
US20020044494A1 (en) * 2000-09-29 2002-04-18 Michael Steinberger Process for the continuous production of mixtures of substances and reaction mixtures and device for its implementation
US6446644B1 (en) 1999-07-06 2002-09-10 Semitool, Inc. Chemical solutions system for processing semiconductor materials
WO2003045653A1 (de) * 2001-11-24 2003-06-05 Krauss-Maffei Kunststofftechnik Gmbh Gasbeladungseinheit einer polyurethanspritzgiessanlage
EP1325801A1 (de) * 2002-01-08 2003-07-09 MCP Tooling Technologies Limited Gegossene Gegenstände aus Kunststoff
US6681959B2 (en) 1994-04-29 2004-01-27 N.V. Soudan Patrimonium And Consulting System for shutting-off and relieving the pressure in a liquid supply line
US7144552B1 (en) * 1999-12-24 2006-12-05 Fujitsu Limited Method and apparatus for preparing chemical solutions
NL2012572A (en) * 2014-04-04 2016-01-13 Heerema Marine Contractors Nl System and method of manufacturing a Field Joint Coating.
US20160185538A1 (en) * 2014-02-20 2016-06-30 Novatec, Inc. Resin delivery apparatus and method with plural air flow limiters
US10131506B2 (en) 2014-12-09 2018-11-20 Maguire Products, Inc. Selective matrix conveyance apparatus and methods for granular resin material
US10138076B2 (en) 2015-02-25 2018-11-27 Stephen B. Maguire Method for resin delivery including metering introduction of external air to maintain desired vacuum level
US10144598B2 (en) 2014-02-20 2018-12-04 Novatec, Inc. Variable frequency drive combined with flow limiter set for limiting flow to selected level above design choice
US10175701B2 (en) 2014-02-20 2019-01-08 Stephen B. Maguire Air flow regulator with detector and method for regulating air flow
US10179708B2 (en) 2014-02-20 2019-01-15 Maguire Products, Inc. Granular material delivery system with air flow limiter
US10179696B2 (en) 2015-01-27 2019-01-15 Novatec, Inc. Variable opening slide gate for regulating material flow into airstream
US10280015B2 (en) 2014-02-20 2019-05-07 Stephen B. Maguire Method for adjustably restricting air flow and apparatus therefor
US10414083B2 (en) 2014-02-20 2019-09-17 Novatec, Inc. Multiple sensor resin delivery optimizing vacuum pump operation

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GB1557184A (en) 1975-11-26 1979-12-05 Baker Perkins Holdings Ltd Mixing machines
DE102008014340B4 (de) * 2008-03-14 2014-06-26 Scheugenpflug Ag Fassfolgepumpe

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US2570079A (en) * 1950-02-09 1951-10-02 Corning Glass Works Glass stirrer and feeder
DE949163C (de) * 1950-05-11 1956-09-13 Mueller Hans Vorrichtung zum Mischen von Fluessigkeiten mit Gas durch Umpumpen der Fluessigkeit
US3521789A (en) * 1968-02-20 1970-07-28 Automatic Process Control Inc Handling fluid materials

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US2570079A (en) * 1950-02-09 1951-10-02 Corning Glass Works Glass stirrer and feeder
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US3521789A (en) * 1968-02-20 1970-07-28 Automatic Process Control Inc Handling fluid materials

Cited By (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2418068A1 (fr) * 1978-02-25 1979-09-21 Hedrich Vakuumanlagen Wilhelm Dispositifs de controle pour installations de preparation de resine de moulage par coulee
US4279360A (en) * 1978-02-25 1981-07-21 Wilhelm Hedrich Vakuumanlagen Gmbh & Co. K.G. System for feeding two synthetic-resin components to a mold
US4252447A (en) * 1978-06-23 1981-02-24 Borodin Sergei I Peristaltic batcher and peristaltic batching system realized therewith
US4291991A (en) * 1978-08-28 1981-09-29 Bayer Aktiengesellschaft Apparatus for the preparation of a reaction mixture from fluid components
WO1980001495A1 (fr) * 1979-01-16 1980-07-24 Sred Az Nii Pritodnogo Gaza Methode et dispositif de preparation d'une boue de forage
US4688944A (en) * 1984-08-24 1987-08-25 Fritz Mumenthaler Mixer head for plastics material components
US5217146A (en) * 1991-04-03 1993-06-08 Wilhelm Hedrich Vakumanlagen GmbH & Co. KG Device for filling one or more molds with flowable materials
US5257722A (en) * 1991-04-03 1993-11-02 Wilhelm Hedrich Vakuumanlagen Gmbh & Co. Kg Device for filling one or more molds with flowable materials
US5423607A (en) * 1991-05-03 1995-06-13 Dolco Packaging Corp. Method for blending diverse blowing agents
US5529212A (en) * 1991-06-13 1996-06-25 Verfahrenstechnik Hubers Gmbh Method of and apparatus for transporting and conditioning casting materials and for charging casting machines with them
US5636972A (en) * 1993-04-26 1997-06-10 Carbotech Device for extrusion of two component synthetic resins
US6681959B2 (en) 1994-04-29 2004-01-27 N.V. Soudan Patrimonium And Consulting System for shutting-off and relieving the pressure in a liquid supply line
EP0895844A3 (de) * 1997-08-04 2001-01-03 Bruno Blatt Harzeinfüllgefäss mit Schliessvorrichtung
US6561266B1 (en) 1998-10-22 2003-05-13 Krauss-Maffei Kunststofftechnik Gmbh Homogenization and heating container for a mixing head
WO2000024556A1 (de) * 1998-10-22 2000-05-04 Krauss-Maffei Kunststofftechnik Gmbh Homogenisier- und temperierbehälter
US6446644B1 (en) 1999-07-06 2002-09-10 Semitool, Inc. Chemical solutions system for processing semiconductor materials
US7144552B1 (en) * 1999-12-24 2006-12-05 Fujitsu Limited Method and apparatus for preparing chemical solutions
US20020044494A1 (en) * 2000-09-29 2002-04-18 Michael Steinberger Process for the continuous production of mixtures of substances and reaction mixtures and device for its implementation
US20040207101A1 (en) * 2001-11-21 2004-10-21 Krauss-Maffei Kunststofftechnik Gmbh Gas charging unit of a polyurethane injection molding assembly
WO2003045653A1 (de) * 2001-11-24 2003-06-05 Krauss-Maffei Kunststofftechnik Gmbh Gasbeladungseinheit einer polyurethanspritzgiessanlage
US6957805B2 (en) 2001-11-24 2005-10-25 Krauss-Maffei Kunststofftechnik Gmbh Gas charging unit of a polyurethane injection molding assembly
EP1325801A1 (de) * 2002-01-08 2003-07-09 MCP Tooling Technologies Limited Gegossene Gegenstände aus Kunststoff
US9937651B2 (en) * 2014-02-20 2018-04-10 Novatec, Inc. Resin delivery apparatus and method with plural air flow limiters
US10414083B2 (en) 2014-02-20 2019-09-17 Novatec, Inc. Multiple sensor resin delivery optimizing vacuum pump operation
US10988328B2 (en) 2014-02-20 2021-04-27 Novatec, Inc. Flow limiting and variable frequency drive apparatus for limiting flow to selected level
US10913195B2 (en) 2014-02-20 2021-02-09 Novatec, Inc. Plural air flow regulator delivery apparatus and method
US20160185538A1 (en) * 2014-02-20 2016-06-30 Novatec, Inc. Resin delivery apparatus and method with plural air flow limiters
US10144598B2 (en) 2014-02-20 2018-12-04 Novatec, Inc. Variable frequency drive combined with flow limiter set for limiting flow to selected level above design choice
US10175701B2 (en) 2014-02-20 2019-01-08 Stephen B. Maguire Air flow regulator with detector and method for regulating air flow
US10179708B2 (en) 2014-02-20 2019-01-15 Maguire Products, Inc. Granular material delivery system with air flow limiter
US10280015B2 (en) 2014-02-20 2019-05-07 Stephen B. Maguire Method for adjustably restricting air flow and apparatus therefor
NL2012572A (en) * 2014-04-04 2016-01-13 Heerema Marine Contractors Nl System and method of manufacturing a Field Joint Coating.
US10131506B2 (en) 2014-12-09 2018-11-20 Maguire Products, Inc. Selective matrix conveyance apparatus and methods for granular resin material
US10179696B2 (en) 2015-01-27 2019-01-15 Novatec, Inc. Variable opening slide gate for regulating material flow into airstream
US10138076B2 (en) 2015-02-25 2018-11-27 Stephen B. Maguire Method for resin delivery including metering introduction of external air to maintain desired vacuum level
US10906225B2 (en) 2015-03-12 2021-02-02 Novatec, Inc. Multiple sensor resin delivery method for optimizing vacuum pump operation
US11059212B2 (en) 2015-03-12 2021-07-13 Novatec, Inc. Resin delivery method and apparatus using multiple sensors for optimal vacuum pump operation

Also Published As

Publication number Publication date
GB1300092A (en) 1972-12-20
FR2028595A1 (de) 1970-10-09
CH504942A (de) 1971-03-31

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