[go: up one dir, main page]

US3765605A - Apparatus for ejecting a mixture of liquids - Google Patents

Apparatus for ejecting a mixture of liquids Download PDF

Info

Publication number
US3765605A
US3765605A US00310947A US3765605DA US3765605A US 3765605 A US3765605 A US 3765605A US 00310947 A US00310947 A US 00310947A US 3765605D A US3765605D A US 3765605DA US 3765605 A US3765605 A US 3765605A
Authority
US
United States
Prior art keywords
pumps
liquids
motor
pressure
ejection head
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US00310947A
Inventor
F Gusmer
C Sundberg
J Hayes
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.)
GUSMER ACQUISITION CORP A CORP OF
MIDLANTIC NATIONAL BANK A NATIONAL BANKING ASSOCIATION
PMC Inc
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Application granted granted Critical
Publication of US3765605A publication Critical patent/US3765605A/en
Assigned to MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSOCIATION reassignment MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSOCIATION ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBLIC BODY CORPORATE OF NEW JERSEY
Assigned to GUSMER CORPORATION reassignment GUSMER CORPORATION CERTIFIED COPY OF MERGER FILED IN THE OFFICE OF THE SECRETARY OF STATE OF DELAWARE, SHOWING MERGER OF ASSIGNORS AND CHANGE OF NAME OF THE SURVIVING CORPORATION ON JUNE 25, 1982. Assignors: GUSMER CORPORATION, A NJ CORP. (MERGED INTO) GUSMER ACQUISITION A DE CORP. (CHANGED TO)
Assigned to MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSOCIATION reassignment MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSOCIATION SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GUMSER ACQUISITION CORP. A CORP. OF DE
Assigned to GUSMER ACQUISITION CORP., A CORP. OF DE reassignment GUSMER ACQUISITION CORP., A CORP. OF DE ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: GUSMER CORPORATION A NJ CORP.
Assigned to NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBLIC BODY CORPORATE AND POLITIC OF reassignment NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBLIC BODY CORPORATE AND POLITIC OF SECURITY INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: GUSMER ACQUISITION CORP A DE CORP.
Assigned to PMC, INC., A CORP. OF DE. reassignment PMC, INC., A CORP. OF DE. MERGER (SEE DOCUMENT FOR DETAILS). EFFECTIVE: DEC. 24, 1986 Assignors: G.F.C. FOAM CORPORATION, GUSMER CORPORATION, I.P., INC., KLEER KAST, INC., P.M.C. EAST CORP., PLASTIC COLORCHIP, INC., PMC SPECIALITIES GROUP, INC., PMC, INC., TECHNICAL PLASTIC EXTRUDERS, INC., VCF PACKAGING FILMS, INC.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/88Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise
    • B01F35/882Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise using measuring chambers, e.g. volumetric pumps, for feeding the substances
    • B01F35/8822Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise using measuring chambers, e.g. volumetric pumps, for feeding the substances using measuring chambers of the piston or plunger type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/717Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7174Feed mechanisms characterised by the means for feeding the components to the mixer using pistons, plungers or syringes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/58Component parts, details or accessories; Auxiliary operations
    • B29B7/60Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material
    • B29B7/603Component parts, details or accessories; Auxiliary operations for feeding, e.g. end guides for the incoming material in measured doses, e.g. proportioning of several materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7404Mixing devices specially adapted for foamable substances
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/76Mixers with stream-impingement mixing head
    • B29B7/7615Mixers with stream-impingement mixing head characterised by arrangements for controlling, measuring or regulating, e.g. for feeding or proportioning the components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/76Mixers with stream-impingement mixing head
    • B29B7/7615Mixers with stream-impingement mixing head characterised by arrangements for controlling, measuring or regulating, e.g. for feeding or proportioning the components
    • B29B7/7626Mixers with stream-impingement mixing head characterised by arrangements for controlling, measuring or regulating, e.g. for feeding or proportioning the components using measuring chambers of piston or plunger type
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/76Mixers with stream-impingement mixing head
    • B29B7/7663Mixers with stream-impingement mixing head the mixing head having an outlet tube with a reciprocating plunger, e.g. with the jets impinging in the tube
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/76Mixers with stream-impingement mixing head
    • B29B7/7663Mixers with stream-impingement mixing head the mixing head having an outlet tube with a reciprocating plunger, e.g. with the jets impinging in the tube
    • B29B7/7684Parts; Accessories
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/8593Systems
    • Y10T137/85978With pump
    • Y10T137/86131Plural
    • Y10T137/86163Parallel

Definitions

  • the present invention relates to apparatus for ejecting a mixture of liquids, more particularly a mixture of mutually reactive liquids such as those that form a foam on a substrate and that cure by reacting with each other, for example, the components of a polyurethane foam and elastomeric coatings.
  • Such mixtures of liquids are ejected from a mixing chamber under pressure onto a substrate, for example by apparatus such as is disclosed in Gusmer US. Pat. Nos. 2,890,836 and 3,263,928.
  • the liquids are highly reactive with each other, they cannot be mixed together in the apparatus until the last possible moment, or else they will react in the apparatus and clog the apparatus. Therefore, as the mixture must be ejected under pressure, it is necessary to pump the mutually reactive liquids to elevated pressure by separate pump means, the reactive liquids following generally parallel flow paths from separate sources of the respective liquids to the mixing chamber from which they are ejected onto the substrate.
  • proportion of the liquids in the mixture that is ejected must be maintained constant and must be closely controlled. Accordingly, it is necessary carefully to regulate the quantity of each of the liquids that is pumped to the mixing chamber; and for this purpose, proportioning pumps of the reciprocating piston type are often used, the valves of which pumps are arranged to create pumping action when stroked in either direction, thus providing continuous flow. Because the pumps are bifunctionally used as a measuring device,
  • Another object of the present invention is the provision of such apparatus which will be relatively simple and inexpensive to construct, easy to operate, maintain and repair, and rugged and durable in use.
  • the objects of the present invention are achieved by coupling the two proportioning pumps in opposed tandem relationship and driving them by a single double-acting fluid motor. Quite unexpectedly, it has been found that the undesirable pressure fluctuation at the outlet at both proportioning pumps is thus greatly reduced and under certain circumstances virtually eliminated.
  • apparatus for ejecting a mixture of liquids, comprising an ejection head 1 in the form of a barrel 3 with an elongated cylindrical mixing chamber 5 therein that is open at its discharge end, that is, at its right hand end as seen in the drawing.
  • a pair of opposed inlets 7 and 9 extend through the side walls of barrel 3 and open into chamber 5 substantially tangentially of chamber 5.
  • a plunger 11 is slidably disposed in barrel 3 and is manually actuable to reciprocate between the position shown in the drawing, in which the inlet openings 7 and 9 are both exposed for the flow of materials to be mixed into chamber 5, and a rightward position as seen in the drawing in which plunger 11 closes the inlet openings 7 and 9 fully fills the chamber 5 thereby completely to eject the reactive mixture from chamber 5.
  • ejection head 1 is known in the art and need not be further described. It can for example be as disclosed in the above-mentioned Gusmer US. Pat. No.
  • chamber 5 is of uniform cross sectional configuration substantially throughout its length, including the discharge opening, so that foam may be ejected from ejection head 1; or ejection head 1 can have the form shown in the above Gusmer US. Pat. No. 2,890,836, with a discharge opening reduced in diameter as compared to the mixing chamber, for the ejection of a spray.
  • the activator may come from a supply container 13 maintained under a positive pressure of, say, 2 or 3 p.s.i.g., by a source of nitrogen 15 which prevents the entry of air and water vapor into container 13.
  • Activator flows from container 13 through a check valve 17 and then through a piston pump 19 by which its pressure is elevated for the purpose described above, for example to p.s.i.g. From pump 19, the activator proceeds through a check valve 21 to the primary pump chamber of the activator proportioning pump 23 in which a piston 25 is reciprocable under the impetus of a displacement piston rod 27.
  • Piston 25 divides the double acting pump 23 into two chambers
  • activator flows through conduit 33 and check valve 35 toward conduit 37 which communicates with activator inlet opening 7, and also toward conduit 39 which communicates with chamber 31 of pump 23. It is during the rightward stroke of piston 25, as seen in the drawing, that the pressure imparted to the activator by pump 19 tends to be additive and the outlet pressure of pump 23 to be relatively high; while it is during the leftward stroke of the piston 25 as seen in the drawing that the pressure imparted by pump '19 becomes nullified and the outlet pressure of pump 23 I is proportionally lower. lt is this periodical fluctuation of the pump outlet pressure that the present invention largely overcomes.
  • the path of the liquid is similar, from a container 39 maintained under positive pressure by nitrogen 41, through a check valve 43, to higher pressure through a pump 45, then through a check valve 47 to pump 49 including a piston 51 that divides pump 49 into chambers 53 and 55. From chamber 53, resin flows through conduit 57 through a check valve 59 and thence to resin inlet conduit 61 communicating with resin inlet opening 9, and also to conduit 63 communicating with chamber 55.
  • piston 51 is on the same piston rod 27 as piston 25 and is axially aligned therewith, the piston rod also being the piston rod of a double-acting fluid motor 65 comprising a double-acting piston 67 that divides motor 65 into chambers 69 and 71.
  • fluid motor 65 is a hydraulic motor fed from a source of hydraulic liquid in a sump 73 through a constant pressure, variable volume pump 75 and thence through an automatically periodically reversing spool valve 77 actuated by a solenoid S, to conduits 79 and 81 that are alternately feed and return conduits, the hydraulic liquid returning to sump 73 through a return conduit 83.
  • motor 65 could be an air motor or an electric motor, so long as it remains a constant pressure motor.
  • the nature of the liquids, their flow rates and temperatures and the pressures imparted thereto by pumps 19, 29, 45 and 53 may all be conventional, for example as disclosed in the above-identified Gusmer patents, and hence need not be further mentioned.
  • the activator and the resin proceed from their respective containers l3 and 29 through their respective pumps 19 and 45, in which they are elevated in pressure; although it will be understood that pumps 19 and 45 can be eliminated and if the nitrogen or other dry inert gas at and 41 is of sufficiently high pressure. in any event, the liquid streams at elevated pressure flow along parallel paths to the respective pumps 23 and 49, the activator entering chamber 29 while the resin enters chamber 53.
  • Piston is moving to the left relative to chamber 29 at the same time that piston 51 is moving to the left relative to chamber 53, as seen in the drawing, so that the pumps 23 and 49 are acting in opposition to each other.
  • the valve 77 is in the position shown in the drawing, with hydraulic fluid being fed by pump 75 to chamber 71 and discharged from chamber 69.
  • solenoid S reverses the position of valve 77 so that hydraulic fluid under pressure is fed to chamber 69 and exhausted from chamber 71, whereupon piston 67 and with it the rod 27 and pistons 25 and 51 is driven to the right as seen in the drawing, which reverses the stroke of both pumps 23 and 49.
  • Apparatus for ejecting a mixture of liquids comprising an ejection head, means for separately feeding two streams of liquids from separate sources of said liquids to said ejection head and for mixing said streams of liquids in said ejection head, said feed means comprising a pair of double-acting reciprocating piston pumps one individual to each of said streams, means for supplying each of said pumps with liquid under elevated pressure from a respective one of said sources, means for separately delivering said liquids from said pumps to said ejection head, and means for driving said pumps in opposed tandem relationship comprising a double-acting reciprocating constant pressure motor common to said pistons of said pumps.
  • said motor being a fluid motor comprising piston means and piston rod means connected to said pistons of said pumps.
  • said fluid motor being a hydraulic motor, and means for alternately supplying hydraulic liquid to and exhausting hydraulic liquid from opposite sides of said hydraulic motor.
  • said means for supplying liquids to said pumps under elevated pressure comprising positive displacement transfer pumps one individual to each said stream.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nozzles (AREA)

Abstract

Two mutually reactive liquids, such as the components of a polyurethane foam, are mixed together and ejected onto a substrate by means of apparatus that pumps the liquids separately and remotely mixes them only at the last moment. Heretofore, the liquids were separately pumped by means of parallel reciprocating proportioning pumps to which the liquids are fed under pressure; and as a result of this feed pressure the outlet pressure of the pumps varied with respect to the direction of stroke. By rearranging the pumps in tandem opposed relation, and driving them by a constant pressure motor such as a double-acting fluid motor, a counterbalancing effect is created which effectively reduces the pressure variation as the stroking action reverses.

Description

United States Patent Gusmer et al.
[ Oct. 16, 1973 [76] Inventors: Frederick E. Gusmer, Mantoloking;
Carl W.'Sundberg, Jr., Chatham; Joseph E. Hayes, Jr., Manasquan, all of NJ.
[22] Filed: Nov. 30, 1972 [21] Appl. No.: 310,947
[52] US. Cl 239/61, 239/332, 239/413, 137/566 [51] Int. Cl B05b 7/04, B05b 9/04, B05b 7/12 [58] Field of Search 239/61, 93, 94, 321, 239/322, 331, 332, 407, 413; 137/566, 567
[56] References Cited UNITED STATES PATENTS 2,548,987 4/1951 Mayo 137/566X 2,819,928 l/1958 Liedberg 239/322 X 3,128,782 4/1964 Limpert et a1. 137/566 X 3,193,202 7/1965 Liggenstorfer et a1. 239/332 X 3,286,933 11/1966 Savage; 239/332 X 8/1967 Schoenecker et a1. 239 332X 8/1967 Tibbitt ..239/331x Primary Examiner-Robert S. Ward, Jr. Att0rneylrvin S. Thompson [5 7] ABSTRACT Two mutually reactive liquids, such as the components of a polyurethane foam, are mixed together and ejected onto a substrate by means of apparatus that pumps the liquids separately and remotely mixes them only at the last moment. I-leretofore, the liquids were separately pumped by means of parallel reciprocating proportioning pumps to which the liquids are fed under pressure; and as a result of this feed pressure the outlet pressure of the pumps varied with respect to the direction of stroke. By rearranging the pumps in tandem opposed relation, and driving them by a constant pressure motor such as a double-acting fluid mo-' tor, a counterbalancing effect is created which effectively reduces the pressure variation as the stroking action reverses.
5 Claims, 1 Drawing Figure ACTIVATOR l5 SUMP RESIN APPARATUS FOR EJECTING A MIXTURE OF LIQUIDS The present invention relates to apparatus for ejecting a mixture of liquids, more particularly a mixture of mutually reactive liquids such as those that form a foam on a substrate and that cure by reacting with each other, for example, the components of a polyurethane foam and elastomeric coatings.
Such mixtures of liquids are ejected from a mixing chamber under pressure onto a substrate, for example by apparatus such as is disclosed in Gusmer US. Pat. Nos. 2,890,836 and 3,263,928. As the liquids are highly reactive with each other, they cannot be mixed together in the apparatus until the last possible moment, or else they will react in the apparatus and clog the apparatus. Therefore, as the mixture must be ejected under pressure, it is necessary to pump the mutually reactive liquids to elevated pressure by separate pump means, the reactive liquids following generally parallel flow paths from separate sources of the respective liquids to the mixing chamber from which they are ejected onto the substrate.
The proportion of the liquids in the mixture that is ejected must be maintained constant and must be closely controlled. Accordingly, it is necessary carefully to regulate the quantity of each of the liquids that is pumped to the mixing chamber; and for this purpose, proportioning pumps of the reciprocating piston type are often used, the valves of which pumps are arranged to create pumping action when stroked in either direction, thus providing continuous flow. Because the pumps are bifunctionally used as a measuring device,
it is necessary to prevent cavitation; therefore the pumps must themselves be pressure fed.
The feeding of the proportioning pumps under pressure, however, gives rise to a problem: During the refill stroke of the proportioning pump, the feed pressure to the pump will add to the outlet pressure of the pump; while during the displacement stroke of the proportioning pump, the feed pressure becomes nullified by the closing of the inlet valve. There is thus a fluctuating variation in the outlet pressure of the proportioning pump, which in magnitude, by virtue of the mechanical design of the pump, actually is multiplied to twice the feed pressure to the proportioning pump.
Accordingly, it is an object of the .present invention to provide such apparatus in which the outlet pressure of the proportioning pumps tends to be much more uniform than heretofore.
Another object of the present invention is the provision of such apparatus which will be relatively simple and inexpensive to construct, easy to operate, maintain and repair, and rugged and durable in use.
Briefly, the objects of the present invention are achieved by coupling the two proportioning pumps in opposed tandem relationship and driving them by a single double-acting fluid motor. Quite unexpectedly, it has been found that the undesirable pressure fluctuation at the outlet at both proportioning pumps is thus greatly reduced and under certain circumstances virtually eliminated.
Other objects, features and advantages of the present invention will become apparent from a consideration of the following description, taken in connection with the accompanying drawing, which is a schematic view of apparatus according to the present invention.
Referring now to the drawing in greater detail, there is shown apparatus according to the present invention for ejecting a mixture of liquids, comprising an ejection head 1 in the form of a barrel 3 with an elongated cylindrical mixing chamber 5 therein that is open at its discharge end, that is, at its right hand end as seen in the drawing. A pair of opposed inlets 7 and 9 extend through the side walls of barrel 3 and open into chamber 5 substantially tangentially of chamber 5. A plunger 11 is slidably disposed in barrel 3 and is manually actuable to reciprocate between the position shown in the drawing, in which the inlet openings 7 and 9 are both exposed for the flow of materials to be mixed into chamber 5, and a rightward position as seen in the drawing in which plunger 11 closes the inlet openings 7 and 9 fully fills the chamber 5 thereby completely to eject the reactive mixture from chamber 5. The construction and operation of ejection head 1 is known in the art and need not be further described. It can for example be as disclosed in the above-mentioned Gusmer US. Pat. No. 3,263,928, in which case the chamber 5 is of uniform cross sectional configuration substantially throughout its length, including the discharge opening, so that foam may be ejected from ejection head 1; or ejection head 1 can have the form shown in the above Gusmer US. Pat. No. 2,890,836, with a discharge opening reduced in diameter as compared to the mixing chamber, for the ejection of a spray.
The mutually reactive liquids reach ejection head 1 along separate paths, as mentioned above. Thus, in the case of a polyurethane resin and the activator therefor, for example, as described in the above Gusmer US. Pat. No. 3,263,928, the activator may come from a supply container 13 maintained under a positive pressure of, say, 2 or 3 p.s.i.g., by a source of nitrogen 15 which prevents the entry of air and water vapor into container 13. Activator flows from container 13 through a check valve 17 and then through a piston pump 19 by which its pressure is elevated for the purpose described above, for example to p.s.i.g. From pump 19, the activator proceeds through a check valve 21 to the primary pump chamber of the activator proportioning pump 23 in which a piston 25 is reciprocable under the impetus of a displacement piston rod 27. Piston 25 divides the double acting pump 23 into two chambers,
,primary chamber 29 and displacement chamber 31.
From chamber 29, activator flows through conduit 33 and check valve 35 toward conduit 37 which communicates with activator inlet opening 7, and also toward conduit 39 which communicates with chamber 31 of pump 23. It is during the rightward stroke of piston 25, as seen in the drawing, that the pressure imparted to the activator by pump 19 tends to be additive and the outlet pressure of pump 23 to be relatively high; while it is during the leftward stroke of the piston 25 as seen in the drawing that the pressure imparted by pump '19 becomes nullified and the outlet pressure of pump 23 I is proportionally lower. lt is this periodical fluctuation of the pump outlet pressure that the present invention largely overcomes.
On the resin side, the path of the liquid is similar, from a container 39 maintained under positive pressure by nitrogen 41, through a check valve 43, to higher pressure through a pump 45, then through a check valve 47 to pump 49 including a piston 51 that divides pump 49 into chambers 53 and 55. From chamber 53, resin flows through conduit 57 through a check valve 59 and thence to resin inlet conduit 61 communicating with resin inlet opening 9, and also to conduit 63 communicating with chamber 55.
However, piston 51 is on the same piston rod 27 as piston 25 and is axially aligned therewith, the piston rod also being the piston rod of a double-acting fluid motor 65 comprising a double-acting piston 67 that divides motor 65 into chambers 69 and 71. In the illustrated embodiment, fluid motor 65 is a hydraulic motor fed from a source of hydraulic liquid in a sump 73 through a constant pressure, variable volume pump 75 and thence through an automatically periodically reversing spool valve 77 actuated by a solenoid S, to conduits 79 and 81 that are alternately feed and return conduits, the hydraulic liquid returning to sump 73 through a return conduit 83. Alternatively, motor 65 could be an air motor or an electric motor, so long as it remains a constant pressure motor.
in operation, the nature of the liquids, their flow rates and temperatures and the pressures imparted thereto by pumps 19, 29, 45 and 53, may all be conventional, for example as disclosed in the above-identified Gusmer patents, and hence need not be further mentioned. The activator and the resin proceed from their respective containers l3 and 29 through their respective pumps 19 and 45, in which they are elevated in pressure; although it will be understood that pumps 19 and 45 can be eliminated and if the nitrogen or other dry inert gas at and 41 is of sufficiently high pressure. in any event, the liquid streams at elevated pressure flow along parallel paths to the respective pumps 23 and 49, the activator entering chamber 29 while the resin enters chamber 53. Piston is moving to the left relative to chamber 29 at the same time that piston 51 is moving to the left relative to chamber 53, as seen in the drawing, so that the pumps 23 and 49 are acting in opposition to each other. During this particular stroke of the pumps, the valve 77 is in the position shown in the drawing, with hydraulic fluid being fed by pump 75 to chamber 71 and discharged from chamber 69. At the end of the stroke of the piston rod 77 with its associated pistons 25, 51 and 67, solenoid S reverses the position of valve 77 so that hydraulic fluid under pressure is fed to chamber 69 and exhausted from chamber 71, whereupon piston 67 and with it the rod 27 and pistons 25 and 51 is driven to the right as seen in the drawing, which reverses the stroke of both pumps 23 and 49.
As a result of the pistons 25 and 51 being thus coupled in opposed tandem relationship and actuated by the same reciprocating fluid motor, it is found that the discharge pressure in conduits 37 and 61, which in the past might have varied from, say, about 700 to about 900 p.s.i. depending upon the direction of stroke of the pumps 23 and 49, now varies very little from a means pressure of 800 p.s.i.
From a consideration of the foregoing disclosure, therefore, it will be evident that all of the initially recited objects of the present invention have been achieved.
Although the present invention has been described and illustrated in connection with a preferred embodiment, it is to be understood that modifications and variations may be resorted to without departing from the spirit of this invention, as those skilled in this art will readily understand. Such modifications and variations are considered to be within the purview and scope of the present invention as defined by the appended claims.
What is claimed is:
1. Apparatus for ejecting a mixture of liquids, comprising an ejection head, means for separately feeding two streams of liquids from separate sources of said liquids to said ejection head and for mixing said streams of liquids in said ejection head, said feed means comprising a pair of double-acting reciprocating piston pumps one individual to each of said streams, means for supplying each of said pumps with liquid under elevated pressure from a respective one of said sources, means for separately delivering said liquids from said pumps to said ejection head, and means for driving said pumps in opposed tandem relationship comprising a double-acting reciprocating constant pressure motor common to said pistons of said pumps.
2. Apparatus as claimed in claim 1, said motor being a fluid motor comprising piston means and piston rod means connected to said pistons of said pumps.
3. Apparatus as claimed in claim 2, said fluid motor being a hydraulic motor, and means for alternately supplying hydraulic liquid to and exhausting hydraulic liquid from opposite sides of said hydraulic motor.
4. Apparatus as claimed in claim 1, said motor and said pumps being in axially aligned relationship.
5. Apparatus as claimed in claim 1, said means for supplying liquids to said pumps under elevated pressure comprising positive displacement transfer pumps one individual to each said stream.

Claims (5)

1. Apparatus for ejecting a mixture Of liquids, comprising an ejection head, means for separately feeding two streams of liquids from separate sources of said liquids to said ejection head and for mixing said streams of liquids in said ejection head, said feed means comprising a pair of double-acting reciprocating piston pumps one individual to each of said streams, means for supplying each of said pumps with liquid under elevated pressure from a respective one of said sources, means for separately delivering said liquids from said pumps to said ejection head, and means for driving said pumps in opposed tandem relationship comprising a double-acting reciprocating constant pressure motor common to said pistons of said pumps.
2. Apparatus as claimed in claim 1, said motor being a fluid motor comprising piston means and piston rod means connected to said pistons of said pumps.
3. Apparatus as claimed in claim 2, said fluid motor being a hydraulic motor, and means for alternately supplying hydraulic liquid to and exhausting hydraulic liquid from opposite sides of said hydraulic motor.
4. Apparatus as claimed in claim 1, said motor and said pumps being in axially aligned relationship.
5. Apparatus as claimed in claim 1, said means for supplying liquids to said pumps under elevated pressure comprising positive displacement transfer pumps one individual to each said stream.
US00310947A 1972-11-30 1972-11-30 Apparatus for ejecting a mixture of liquids Expired - Lifetime US3765605A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US31094772A 1972-11-30 1972-11-30

Publications (1)

Publication Number Publication Date
US3765605A true US3765605A (en) 1973-10-16

Family

ID=23204728

Family Applications (1)

Application Number Title Priority Date Filing Date
US00310947A Expired - Lifetime US3765605A (en) 1972-11-30 1972-11-30 Apparatus for ejecting a mixture of liquids

Country Status (1)

Country Link
US (1) US3765605A (en)

Cited By (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3980231A (en) * 1975-04-24 1976-09-14 Eastside Spraying Service Inc. Proportioning sprayer device
FR2366116A1 (en) * 1976-09-29 1978-04-28 Gusmer Corp FEEDER FOR A DEVICE FOR EJECTING A MIXTURE OF SEVERAL LIQUIDS, IN PARTICULAR POLYURETHANE SYSTEM
FR2426561A1 (en) * 1978-05-25 1979-12-21 Saint Gobain Plastics injection system for multiple glazing - includes pressure detector in pump delivery transmitting signal to amplifier comparator
DE2914684A1 (en) * 1979-04-11 1981-04-02 Durol Gmbh & Co Kg Chemische Fabrik Lindau-Bodensee, 8990 Lindau Reactive viscous media mixing and metering - by passing-compressed air first through moisture insensitive medium before sensitive medium
US4360157A (en) * 1980-09-22 1982-11-23 Quenneville Marc A Plural component system
US4516725A (en) * 1982-09-30 1985-05-14 501 Binks Manufacturing Co. Dual component pumping system
US4529000A (en) * 1982-12-28 1985-07-16 Davey Tree Expert Company Flow volume proportioning system
US4628861A (en) * 1983-06-21 1986-12-16 Chembond Corporation Metering and proportioning system for a two-component liquid resin and liquid hardener adhesive
US4690308A (en) * 1986-01-09 1987-09-01 Binks Manufacturing Company Pail mount pump with integral cover
US4809909A (en) * 1985-06-13 1989-03-07 Glas-Craft, Inc. Plural component application system
US4879859A (en) * 1983-12-09 1989-11-14 Dykmans Max J Method and apparatus for constructing circumferentially wrapped prestressed structures utilizing a membrane
US4884747A (en) * 1987-05-14 1989-12-05 Dykmans Max J Ripple-free flow, accurate mix, and automated spray system
EP0421378A1 (en) * 1989-10-04 1991-04-10 Kurashiki Boseki Kabushiki Kaisha Automatic solution dispensing apparatus
US5092522A (en) * 1987-05-14 1992-03-03 Dykmans Max J Automated accurate mix application system for fiber reinforced structures
US5094044A (en) * 1983-12-09 1992-03-10 Dykmans Maximilliaan J Multi-purpose dome structure and the construction thereof
US5134830A (en) * 1983-12-09 1992-08-04 Dykmans Max J Method and apparatus for constructing circumferentially wrapped prestressed structures utilizing a membrane
US5408793A (en) * 1983-12-09 1995-04-25 Dykmans; Max J. Multi-purpose dome structure and the method of construction thereof
US5675941A (en) * 1983-12-09 1997-10-14 Dykmans; Maximiliaan J. Method and apparatus for constructing prestressed structures utilizing a membrane and floating dome assembly
US20070187531A1 (en) * 2006-02-14 2007-08-16 The U.S. Of America As Represented By The Secretary Of The Navy Apparatus and method to amalgamate substances
US20070286745A1 (en) * 2006-06-09 2007-12-13 Maynard Chance Integrated mixing pump
US20090068034A1 (en) * 2007-09-12 2009-03-12 Pumptec, Inc. Pumping system with precise ratio output
WO2014195312A1 (en) * 2013-06-05 2014-12-11 Basf Se Metering pump and metering system
US9038929B1 (en) 2011-06-17 2015-05-26 Pmc, Inc. Air spray gun with pattern control tip
US10167863B1 (en) 2012-03-28 2019-01-01 Pumptec, Inc. Proportioning pump, control systems and applicator apparatus
WO2020048624A1 (en) * 2018-09-07 2020-03-12 Kraussmaffei Technologies Gmbh Device and method for producing reaction plastics
US10760557B1 (en) 2016-05-06 2020-09-01 Pumptec, Inc. High efficiency, high pressure pump suitable for remote installations and solar power sources
US10823160B1 (en) 2017-01-12 2020-11-03 Pumptec Inc. Compact pump with reduced vibration and reduced thermal degradation
US20220177290A1 (en) * 2017-12-29 2022-06-09 At Group, Llc, Dba U.S. Foam Systems Apparatus for dispensing a mixture of at least two liquid components
WO2023009504A1 (en) * 2021-07-28 2023-02-02 Sunless, Inc. System and method for spray tan customization using multipart tanning solution

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2548987A (en) * 1949-08-24 1951-04-17 Robert D Mayo Auxiliary fuel tank and pump
US2819928A (en) * 1954-05-18 1958-01-14 Atlas Copco Ab Apparatus for simultaneously discharging materials
US3128782A (en) * 1961-02-13 1964-04-14 Alexander S Limpert Small volume feeder pump and process of proportional feeding
US3193202A (en) * 1962-04-28 1965-07-06 Liggenstorfer Arnold Proportioning apparatus and method for mixing and feeding liquid resin impregnant with setting agent through single orifice discharge
US3286933A (en) * 1964-07-13 1966-11-22 Donald W Barlow Duplex chemical feeding system
US3335671A (en) * 1964-04-29 1967-08-15 Union Tank Car Co Pumping and injection system
US3338523A (en) * 1965-07-28 1967-08-29 Ross A Tibbitt Dispensing apparatus

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2548987A (en) * 1949-08-24 1951-04-17 Robert D Mayo Auxiliary fuel tank and pump
US2819928A (en) * 1954-05-18 1958-01-14 Atlas Copco Ab Apparatus for simultaneously discharging materials
US3128782A (en) * 1961-02-13 1964-04-14 Alexander S Limpert Small volume feeder pump and process of proportional feeding
US3193202A (en) * 1962-04-28 1965-07-06 Liggenstorfer Arnold Proportioning apparatus and method for mixing and feeding liquid resin impregnant with setting agent through single orifice discharge
US3335671A (en) * 1964-04-29 1967-08-15 Union Tank Car Co Pumping and injection system
US3286933A (en) * 1964-07-13 1966-11-22 Donald W Barlow Duplex chemical feeding system
US3338523A (en) * 1965-07-28 1967-08-29 Ross A Tibbitt Dispensing apparatus

Cited By (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3980231A (en) * 1975-04-24 1976-09-14 Eastside Spraying Service Inc. Proportioning sprayer device
FR2366116A1 (en) * 1976-09-29 1978-04-28 Gusmer Corp FEEDER FOR A DEVICE FOR EJECTING A MIXTURE OF SEVERAL LIQUIDS, IN PARTICULAR POLYURETHANE SYSTEM
FR2426561A1 (en) * 1978-05-25 1979-12-21 Saint Gobain Plastics injection system for multiple glazing - includes pressure detector in pump delivery transmitting signal to amplifier comparator
DE2914684A1 (en) * 1979-04-11 1981-04-02 Durol Gmbh & Co Kg Chemische Fabrik Lindau-Bodensee, 8990 Lindau Reactive viscous media mixing and metering - by passing-compressed air first through moisture insensitive medium before sensitive medium
US4360157A (en) * 1980-09-22 1982-11-23 Quenneville Marc A Plural component system
AU577348B2 (en) * 1982-09-30 1988-09-22 Binks Manufacturing Company Dual fluid component pumping system
US4516725A (en) * 1982-09-30 1985-05-14 501 Binks Manufacturing Co. Dual component pumping system
US4529000A (en) * 1982-12-28 1985-07-16 Davey Tree Expert Company Flow volume proportioning system
US4628861A (en) * 1983-06-21 1986-12-16 Chembond Corporation Metering and proportioning system for a two-component liquid resin and liquid hardener adhesive
US5408793A (en) * 1983-12-09 1995-04-25 Dykmans; Max J. Multi-purpose dome structure and the method of construction thereof
US4879859A (en) * 1983-12-09 1989-11-14 Dykmans Max J Method and apparatus for constructing circumferentially wrapped prestressed structures utilizing a membrane
US5881530A (en) * 1983-12-09 1999-03-16 Dykmans; Maximiliaan J. Method and apparatus for constructing prestressed structures utilizing a membrane and floating dome assembly
US5675941A (en) * 1983-12-09 1997-10-14 Dykmans; Maximiliaan J. Method and apparatus for constructing prestressed structures utilizing a membrane and floating dome assembly
US5094044A (en) * 1983-12-09 1992-03-10 Dykmans Maximilliaan J Multi-purpose dome structure and the construction thereof
US5134830A (en) * 1983-12-09 1992-08-04 Dykmans Max J Method and apparatus for constructing circumferentially wrapped prestressed structures utilizing a membrane
US4809909A (en) * 1985-06-13 1989-03-07 Glas-Craft, Inc. Plural component application system
US4690308A (en) * 1986-01-09 1987-09-01 Binks Manufacturing Company Pail mount pump with integral cover
US5092522A (en) * 1987-05-14 1992-03-03 Dykmans Max J Automated accurate mix application system for fiber reinforced structures
US4884747A (en) * 1987-05-14 1989-12-05 Dykmans Max J Ripple-free flow, accurate mix, and automated spray system
US5177693A (en) * 1989-10-04 1993-01-05 Kurashiki Boseki Kabushiki Kaisha Automatic solution mixing apparatus
EP0421378A1 (en) * 1989-10-04 1991-04-10 Kurashiki Boseki Kabushiki Kaisha Automatic solution dispensing apparatus
US20070187531A1 (en) * 2006-02-14 2007-08-16 The U.S. Of America As Represented By The Secretary Of The Navy Apparatus and method to amalgamate substances
US20070286745A1 (en) * 2006-06-09 2007-12-13 Maynard Chance Integrated mixing pump
US20090068034A1 (en) * 2007-09-12 2009-03-12 Pumptec, Inc. Pumping system with precise ratio output
US9038929B1 (en) 2011-06-17 2015-05-26 Pmc, Inc. Air spray gun with pattern control tip
US10724515B1 (en) * 2012-03-28 2020-07-28 Pumptec, Inc. Proportioning pump, control systems and applicator apparatus
US10167863B1 (en) 2012-03-28 2019-01-01 Pumptec, Inc. Proportioning pump, control systems and applicator apparatus
WO2014195312A1 (en) * 2013-06-05 2014-12-11 Basf Se Metering pump and metering system
US10221838B2 (en) 2013-06-05 2019-03-05 Basf Se Metering pump and metering system
US10760557B1 (en) 2016-05-06 2020-09-01 Pumptec, Inc. High efficiency, high pressure pump suitable for remote installations and solar power sources
US10823160B1 (en) 2017-01-12 2020-11-03 Pumptec Inc. Compact pump with reduced vibration and reduced thermal degradation
US20220177290A1 (en) * 2017-12-29 2022-06-09 At Group, Llc, Dba U.S. Foam Systems Apparatus for dispensing a mixture of at least two liquid components
WO2020048624A1 (en) * 2018-09-07 2020-03-12 Kraussmaffei Technologies Gmbh Device and method for producing reaction plastics
KR20210040153A (en) * 2018-09-07 2021-04-12 크라우스마파이 테크놀로지스 게엠베하 Device and method for making reactive plastics
CN112654481A (en) * 2018-09-07 2021-04-13 克劳斯马菲技术有限公司 Device and method for producing reactive plastics
US11298852B2 (en) * 2018-09-07 2022-04-12 Kraussmaffei Technologies Gmbh Device and method for producing reaction plastics
CN112654481B (en) * 2018-09-07 2022-12-20 克劳斯马菲技术有限公司 Device and method for producing reactive plastics
WO2023009504A1 (en) * 2021-07-28 2023-02-02 Sunless, Inc. System and method for spray tan customization using multipart tanning solution

Similar Documents

Publication Publication Date Title
US3765605A (en) Apparatus for ejecting a mixture of liquids
US3975128A (en) System for filling a mold with reactive synthetic-resin components
US2894732A (en) Fluid mixing device
US4705461A (en) Two-component metering pump
US5127547A (en) Metering and dispensing apparatus
US4126399A (en) Method and apparatus for preparing multi-component plastic materials, particularly polyurethane, with solid material additives or at least one highly viscous component
US3930756A (en) Metering pulse pump
JPS6251764A (en) Quantity control pump
US7066353B2 (en) Fluid powered additive injection system
US4436230A (en) Arrangement for pulsation-free feeding of a liquid medium
US4349130A (en) Liquid metering pump
GB1293920A (en) Apparatus for kneading doughy explosives
US5524797A (en) Double acting metering cylinder
JPH0369291B2 (en)
JP2852541B2 (en) Concrete delivery device
US3481587A (en) High pressure injector and system for pressurizing ingredients
US4600312A (en) Impingement mix-head for rim process
US4806079A (en) Apparatus for simultaneously pumping a plurality of liquids
US4030860A (en) Variable proportional metering apparatus
GB1579806A (en) Metering pumps
US3114379A (en) Automatic fluid supply actuated motor and piston additive device
GB1319888A (en) Single or double acting pump for discharging a liquid or a viscous substance
DE59303903D1 (en) DOSING PUMP WITH BLEEDING VALVE
US3450053A (en) Additive proportioning and injection system
US3213796A (en) Variable proportioner

Legal Events

Date Code Title Description
AS Assignment

Owner name: GUSMER CORPORATION, NEW YORK

Free format text: CERTIFIED COPY OF MERGER FILED IN THE OFFICE OF THE SECRETARY OF STATE OF DELAWARE, SHOWING MERGER OF ASSIGNORS AND CHANGE OF NAME OF THE SURVIVING CORPORATION ON JUNE 25, 1982;ASSIGNOR:GUSMER CORPORATION, A NJ CORP. (MERGED INTO) GUSMER ACQUISITION A DE CORP. (CHANGED TO);REEL/FRAME:004020/0694

Effective date: 19820625

Owner name: GUSMER ACQUISITION CORP., A CORP. OF DE, CALIFOR

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GUSMER CORPORATION A NJ CORP.;REEL/FRAME:004020/0699

Effective date: 19820625

Owner name: NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBL

Free format text: SECURITY INTEREST;ASSIGNOR:GUSMER ACQUISITION CORP A DE CORP.;REEL/FRAME:004020/0705

Effective date: 19820625

Owner name: MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSOC

Free format text: SECURITY INTEREST;ASSIGNOR:GUMSER ACQUISITION CORP. A CORP. OF DE;REEL/FRAME:004020/0712

Effective date: 19820625

Owner name: MIDLANTIC NATIONAL BANK, A NATIONAL BANKING ASSO

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBLIC BODY CORPORATE OF NEW JERSEY;REEL/FRAME:004020/0719

Effective date: 19820625

Owner name: MIDLANTIC NATIONAL BANK, TWO BROAD ST., BLOOMFIELD

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, A PUBLIC BODY CORPORATE OF NEW JERSEY;REEL/FRAME:004020/0719

Effective date: 19820625

Owner name: GUSMER CORPORATION

Free format text: CERTIFIED COPY OF MERGER FILED IN THE OFFICE OF THE SECRETARY OF STATE OF DELAWARE, SHOWING MERGER OF ASSIGNORS AND CHANGE OF NAME OF THE SURVIVING CORPORATION ON JUNE 25, 1982.;ASSIGNOR:GUSMER CORPORATION, A NJ CORP. (MERGED INTO) GUSMER ACQUISITION A DE CORP. (CHANGED TO);REEL/FRAME:004020/0694

Effective date: 19820625

Owner name: GUSMER ACQUISITION CORP., 12243 BRANFORD ST., P.O.

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:GUSMER CORPORATION A NJ CORP.;REEL/FRAME:004020/0699

Effective date: 19820625

Owner name: MIDLANTIC NATIONAL BANK, TWO BROAD ST., BLOOMFIELD

Free format text: SECURITY INTEREST;ASSIGNOR:GUMSER ACQUISITION CORP. A CORP. OF DE;REEL/FRAME:004020/0712

Effective date: 19820625

Owner name: NEW JERSEY ECONOMIC DEVELOPMENT AUTHORITY, CAPITOL

Free format text: SECURITY INTEREST;ASSIGNOR:GUSMER ACQUISITION CORP A DE CORP.;REEL/FRAME:004020/0705

Effective date: 19820625

STCF Information on status: patent grant

Free format text: PATENTED FILE - (OLD CASE ADDED FOR FILE TRACKING PURPOSES)

AS Assignment

Owner name: PMC, INC., A CORP. OF DE.

Free format text: MERGER;ASSIGNORS:PMC, INC.;VCF PACKAGING FILMS, INC.;G.F.C. FOAM CORPORATION;AND OTHERS;REEL/FRAME:005014/0191

Effective date: 19870508