CA1064695A - Apparatus for melting and dispensing thermoplastic material - Google Patents
Apparatus for melting and dispensing thermoplastic materialInfo
- Publication number
- CA1064695A CA1064695A CA251,814A CA251814A CA1064695A CA 1064695 A CA1064695 A CA 1064695A CA 251814 A CA251814 A CA 251814A CA 1064695 A CA1064695 A CA 1064695A
- Authority
- CA
- Canada
- Prior art keywords
- hopper
- air
- thermoplastic material
- shroud
- molten
- 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
Links
Classifications
-
- 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
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/02—Conditioning or physical treatment of the material to be shaped by heating
- B29B13/022—Melting the material to be shaped
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04C—ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
- F04C13/00—Adaptations of machines or pumps for special use, e.g. for extremely high pressures
- F04C13/001—Pumps for particular liquids
- F04C13/002—Pumps for particular liquids for homogeneous viscous liquids
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Coating Apparatus (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Loading And Unloading Of Fuel Tanks Or Ships (AREA)
Abstract
APPARATUS FOR MELTING AND DISPENSING
THERMOPLASTIC MATERIAL
Abstract of the Disclosure An apparatus for melting and dispensing thermoplastic material comprising a hopper, a grid melter, a reservoir and a pump. At least a portion of the hopper is enclosed within a shroud so as to define an air flow chamber around the lower end of the hopper. Air is forced through this chamber when the appa-ratus is in use so as to cool the hopper and prevent molten mater-ial from backing up into the hopper.
THERMOPLASTIC MATERIAL
Abstract of the Disclosure An apparatus for melting and dispensing thermoplastic material comprising a hopper, a grid melter, a reservoir and a pump. At least a portion of the hopper is enclosed within a shroud so as to define an air flow chamber around the lower end of the hopper. Air is forced through this chamber when the appa-ratus is in use so as to cool the hopper and prevent molten mater-ial from backing up into the hopper.
Description
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j, This application is related to copending Canadian ' .l¦ application Serial No. 245,372, filed February 10, 1976, and ,;~ i, assigned to the assignee of the present arrlic~t;.~n.
This invention relates to apparatus for melting and dispensing thermoplastic material and more particularly to an ~ apparatus Eor melting and dispensing a large volume of thermo~
:: ! I ~ ;
plastic adhesive material with minimal degradation of the molten material prior to application by a dispenser.
I li Conventionally, thermoplastic adhesives or so-called ;l "hot melt" adhesives are converted from a solid to a molten state , ~ ; , ... . .
in a tank having heated walls. The melted material is maintained , -in the mol-ten state in the tank in sufficient volume to supply one or more applicators or dispensers. If the job or application re~uires a substarl~iaL volu~llc of hot mc:l.t adlleSiVC, a sufficicntly large volume of material must be maintained in the molten or melt-ed state to meet that need. That substantial volume usually necessitates a long warm-up or start-up time for the apparatus ! :~:
as well as prolonged exposure of at least some of the molten mater-ial to heat and/or to oxygen.
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! Most tll(rlllo~ stic adhesive Inlterills oxidize, char or decJrade when e~yosed to heat for a prolollcJed length of time and/or wherl exr?o~eil ~o oxy~Jen for ally ar~preciable len(~ith o~ time.
Conseciuelltly, it is desirable to minimi~e the time that an appli- I
jj cator system maintains the melted material in a molten state.
¦I This minimal duration molten s-tate of the adhesive material can be accomplished by balancing of the melt rate of the system with ' the application rate.
¦! . . `: :-In copending Canadian application Serial No. . ~ :
il 245,372, there is disclosed an apparatus for melting and !, dispensing a high throughput of thermoplastic ma-terials. That apparatus includes a melter having a very high melt rate and a ¦ purnp having a high capacity for pumping very viscous materials. -~
I have found that the high melt rate and the efficiency i~ Of the melter of the above identified application hav2created an unforeseen problem with some materials when the apparatus in in use but is not dispensing molten material at the rate for which it is designed. In that event, the mel-ter is operative to melt greater quantities of the thermoplastic material than is used, -with the result that the molten material fills the molten material ~ reservoir, the melter and eventually backs up or "melts back" into ! the hopper. If the apparatus is then turned off or shut down with I molten material contained in the hopper, that molten material !I solidifies and is then difficult or requires a long time to re- `~
melt with the result that it may form a bridge across the walls !
, of -the hopper and -thereby block infeed of solid stock from the ¦
Il hopper into the melter.
i~ It has tllerefore been a primary objective of this in~
j~ vention to prevent melt back of molten material into the hopper
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j, This application is related to copending Canadian ' .l¦ application Serial No. 245,372, filed February 10, 1976, and ,;~ i, assigned to the assignee of the present arrlic~t;.~n.
This invention relates to apparatus for melting and dispensing thermoplastic material and more particularly to an ~ apparatus Eor melting and dispensing a large volume of thermo~
:: ! I ~ ;
plastic adhesive material with minimal degradation of the molten material prior to application by a dispenser.
I li Conventionally, thermoplastic adhesives or so-called ;l "hot melt" adhesives are converted from a solid to a molten state , ~ ; , ... . .
in a tank having heated walls. The melted material is maintained , -in the mol-ten state in the tank in sufficient volume to supply one or more applicators or dispensers. If the job or application re~uires a substarl~iaL volu~llc of hot mc:l.t adlleSiVC, a sufficicntly large volume of material must be maintained in the molten or melt-ed state to meet that need. That substantial volume usually necessitates a long warm-up or start-up time for the apparatus ! :~:
as well as prolonged exposure of at least some of the molten mater-ial to heat and/or to oxygen.
~ , ' , l~i6~695 1 ~
ll : ~
! Most tll(rlllo~ stic adhesive Inlterills oxidize, char or decJrade when e~yosed to heat for a prolollcJed length of time and/or wherl exr?o~eil ~o oxy~Jen for ally ar~preciable len(~ith o~ time.
Conseciuelltly, it is desirable to minimi~e the time that an appli- I
jj cator system maintains the melted material in a molten state.
¦I This minimal duration molten s-tate of the adhesive material can be accomplished by balancing of the melt rate of the system with ' the application rate.
¦! . . `: :-In copending Canadian application Serial No. . ~ :
il 245,372, there is disclosed an apparatus for melting and !, dispensing a high throughput of thermoplastic ma-terials. That apparatus includes a melter having a very high melt rate and a ¦ purnp having a high capacity for pumping very viscous materials. -~
I have found that the high melt rate and the efficiency i~ Of the melter of the above identified application hav2created an unforeseen problem with some materials when the apparatus in in use but is not dispensing molten material at the rate for which it is designed. In that event, the mel-ter is operative to melt greater quantities of the thermoplastic material than is used, -with the result that the molten material fills the molten material ~ reservoir, the melter and eventually backs up or "melts back" into ! the hopper. If the apparatus is then turned off or shut down with I molten material contained in the hopper, that molten material !I solidifies and is then difficult or requires a long time to re- `~
melt with the result that it may form a bridge across the walls !
, of -the hopper and -thereby block infeed of solid stock from the ¦
Il hopper into the melter.
i~ It has tllerefore been a primary objective of this in~
j~ vention to prevent melt back of molten material into the hopper
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~1 and conse~luerlt "l~ridyin~J" of solid thermoplastic material across !
or between the walls o the hopper.
Another objective of this invention has been to limit the quantity of molten material contained within the reservoir by preventing melt back of molten material into the hopper. These objec-tives are accomplished by providing the meltiny and dispens~
ing apparatus with a device for maintaining the material at the , l bottom of the hopper a-t a temperature substantiaIly below -the ¦ solidification temperature of -the material. So long as the walls 1! f the hopper are maintained below the solidification temperature of the material, the material cannot melt back into the hopper and bridge the inside walls.
According to the practice of this invention, melt back 11 of molten material into the hopper is prevented by providing an ~j l! air chamber defining shroud around the bottom of the hopper and ¦
maintaining a flow of forced air through the air chamber when the j I apparatus is in use. This forced air flow over the walls of ,1 the hopper, cools the hopper and maintains it at a temperature substantially below the melting temperature o the thermoplastic 1il feedstock. In one embodiment a continuous flow of air through I the air chamber is maintained by a fan mounted in the wall of the i I! shroud. In another embodiment, the pump of the apparatus is driven by a rotary air motor and the exhaust of this air motor serves as the source of forced air into the air chamber. The ¦ `
particular source of air flow to the chamber is not critical to ¦ the practice of the invention. The importan-t point is tha-t the air flow be sufficien-t in quantity and the thermal conduc-tivity of ¦l the walls of the hopper be such tha-t heat is dissipated away from I
,,~,.. .. . . . .. . .
~469i~
~1 and conse~luerlt "l~ridyin~J" of solid thermoplastic material across !
or between the walls o the hopper.
Another objective of this invention has been to limit the quantity of molten material contained within the reservoir by preventing melt back of molten material into the hopper. These objec-tives are accomplished by providing the meltiny and dispens~
ing apparatus with a device for maintaining the material at the , l bottom of the hopper a-t a temperature substantiaIly below -the ¦ solidification temperature of -the material. So long as the walls 1! f the hopper are maintained below the solidification temperature of the material, the material cannot melt back into the hopper and bridge the inside walls.
According to the practice of this invention, melt back 11 of molten material into the hopper is prevented by providing an ~j l! air chamber defining shroud around the bottom of the hopper and ¦
maintaining a flow of forced air through the air chamber when the j I apparatus is in use. This forced air flow over the walls of ,1 the hopper, cools the hopper and maintains it at a temperature substantially below the melting temperature o the thermoplastic 1il feedstock. In one embodiment a continuous flow of air through I the air chamber is maintained by a fan mounted in the wall of the i I! shroud. In another embodiment, the pump of the apparatus is driven by a rotary air motor and the exhaust of this air motor serves as the source of forced air into the air chamber. The ¦ `
particular source of air flow to the chamber is not critical to ¦ the practice of the invention. The importan-t point is tha-t the air flow be sufficien-t in quantity and the thermal conduc-tivity of ¦l the walls of the hopper be such tha-t heat is dissipated away from I
3 !! the hopper at a faster rate than heat can be input or supplied 11, to the walls by incoming molten feedstock.
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~646915 In one r~rticular aspect the present i.nvent:Lon provides an al)parcl~us ror ~onvertillK ;o:l.:i.~l Lhermol):l.a~ti.c maLc~ria:l. to moltell -thermop].astic mater:ial and for dispensing the molten thermoplastic material., comprisLng a housing inc:l~ld:ing a hopper having side walls ?
for receiv:Lng solid thermoplast:Lc materi.al, a flow through grid melter having a continuo-ls side wall, a bottom wall, and an open top for receiving said solid thermoplastic material from said :.
hopper, said bottom wall comprising a plurality of spaced heating ,~ ' . ' ' ., sections, a plurality of discharge openings in said bottom wall of ;.~
: 10 said grid melter between said spaced heating sections, a reservoir .; . -mounted beneath the grid melter and adapted to receive molten material from said discharge openings of said grid melter, means for heating said bottom wall of said grid melter, a di.spenser operable to dispense said molten thermoplastic material, a pump for ;;~`
supplying said molten thermoplastic material from said reservoir .
: to said dispenser, and cooling means for maintaining said hopper .. ;~ -~
: side walls below the solidification temperature of said molten material so as to prevent the melt back of molten material from . said grid melter into said hopper, sald cooling means comprising 20 a shroud surrounding at least the lower portion of said hopper, .
said shroud defining an air chamber between the inner walls of . `~
said shroud and the outer walls of said hopper, and air flow means ~: for supplying a flow of forced air through said air chamber so as ~ to cool the lower portion of said hopper. .;~
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llese alld o~her aspects of tl~is inve~ntion will be more ~¦ readily apparerl~ from the followiny description of the drawings ¦ in which:
Fi~ure L is a pers~ective view oE one embodiment of a thermoplastic material melting and dispensing apparatus incor- ¦
porating the invention of this application.
¦ Figure 2 is an exploded perspective view of a portion ¦ of the apparatus of Figure 1.
Figure 3 is a side elevational view, partially broken 'I away, of a portion of the apparatus of Figure 1.
Figure 4 is a cross sectional view taken on line 4-4 of ¦
Figure 3.
' Figure 5 is a cross sectional view, similar to Figure ', 4, but illustrating a second embodiment of the inven-tion.
Figure 6 is a fragmentary view in section, similar to t 11 Figure 5, but illus-trating a third embodiment of the invention.
¦¦ Figure 7 is a cross sectional view taken on line 7-7 , ~ ;
of Figure 6.
j Referring first to Figures 1 and 2, it will be seen ' that the thermoplastic material melting and dispensing apparatus 5 of this invention comprises a housing 10 within which there is located a hopper 11, a grid melter 12, a reservoir 13, a gear ¦ 1! pump 14, and a manifold block 15. Solid thermoplastic material 6~1 ,1 in the form of chunks ~Fig. 4), pelle-ts (Fig. 6), or blocks 1, are placed in *he top of the hopper 11 from which they flow ¦ through the open bottom into contact with the top surface of the grid mel-ter 12. The grid melter 12 is heated so that surface contact of the solid thermoplastic material wi-th the top surface !~ f the grid causes the solid thermoplastic material to be melted ', il and converted to a molten state. The molten thermoplastic material ¦ 7 then flows downwardly through bottom passageways 16 in the grid ~
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, ' ' ,: ,'.,, . ' :' 10~i46~5 , ' ' rnel~er into tllc rcservoir 13 locaLed irnmedi~tcly beneath the melter 12. The reservoir has sloping bottom walls 17, 18 and 19 which direc~ the molten material toward the inlet 20 of -the pump 14. The pump -then moves the molten rnaterial into the Manifold block 15 from whence it is directed to one or more conventional applicators or dispensers 22 via hoses or conduits 21.
~ 11 , .
Housing, Hopper The housing 10 comprises a shee-t metal base pla-te 25 and a cover 26 mounted atop the base plate. The cover 26 encloses ~, 10 ¦¦ two sections of the applicator, the melt section 27 and the con-¦ trol section 28. The two sections are separated by an insulative barrier (not ShOWll). Within the control section 28 are all of ¦¦ the electrical components for controlling the temperature of the ¦I components throughout the system. These controls form no part of !
the invention of this application and are conventional in commer-cially available equipment, as for example equipment of the type ¦~
jl shown in U. S. Patent No~ 3,792,901, issued February 19, 1974 and ¦
j 1' assigned to the assignee of this application.
~ The top 30 of the cover has an opening 31 into which ;¦~ 20 Ij there is fitted the hopper 11 and a surrounding shroud 29. The hopper comprises a vertical tube 32, the bottom 33 of which is ii open ~and the top of which is closed by a lid 34. Around the periphery of the hopper there is a flange 35 which is welded or ¦ j fixed to the exterior of the hopper and which in turn functions as the at;tachment for the hopper surrounding shroud 29, as is 1 1l explained more fully hereinafter.
. Il Grid Melter ; ;1 1 .
i' Referring to Figures 2, 3 and 4, i-t will be seen that 1 the grid melter 12 comprises a receptacle into which solid !l `........... I --5--':1 1, . I
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-thermoplastic rnaterial flows from the hopper 11. '~'his receptacle Il comprises four side walls 37, 38, 39 and ~0 and a bottom flange ¦l ~1. The bo-ttom itself comprises a plurality of vertical pro~
¦ trusions or heater elements 43, each one of which is hexagonal ¦ in cross section at the base ~2 and has an upper end shaped as jl a truncated cone. The protrusions are arranyed in longitudinal ¦¦ rows 44 with -the base 42 of each protrusion 45 interconnected and integral with the adjacent protrusions 45 of the same row ¦1 44. The pro-trusions 45 of adjacent rows 44 are longitudinally ; 10 ~ offset from each of the protrusions of the adjacent rows such that when viewed in top plan -the protrusions create a staggered I pattern or rows and columns, but with the protrusions of the I ~ j', columns spaced apart and separated by~an intermediate row of ! protrusions. There are open passageways 16 located on opposite , I~ sides of each row and extending for the length of the row. These ~ passageways 16 open into the top of the reservoir 13.
`' ¦ In the melting of thermoplastic materials it is critical ~ that the melter have a large surface area in contact with the : i l ~
poor heat conductive blocks or pellets of thermoplastic material.
~; 20 il Prior to this inventlon attempts have been made to increase the surface area by forming ribs on the bottom of the grid melter as ln U. S. Patent No. 3,531,023. The grid melter 12 of this , invention incorporating~the truncated cone shaped heater elements ~ j has been Lound to increase the throughput of the grid melter over :!~ ¦ rib type grids by as much as 30 or 40~ while maintaining the same surface temperature of the grid so as to avoid degrading of the ¦ material.
¦~ The protrusions are formed as truncated cones or pyra-¦¦ mids having flat or blunt -topmost end surfaces 50. As used ~l throughout this application and in the claims the term "cone"
is used in the generic sense to include pyramids which have ~' 1, , ..... , ~
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~L064695 Il anywhere frolll three to an infinite nurnber of sides. When the ¦¦ pyramid has an infinite nul~er of sides it is of course circular ¦
in cross sec-tion. The truncation or bluntiny of the topmost sur-¦
'¦ face 50 of the "cone" increases the area in contact with the solid thermoplastic ma-terial and enables the surface temperature of the complete "cone" to be evenly main-tainecl with a minimal power input.
Ii In one preferred embodiment the grid melter 12 is I ! formed as an integral casting. This casting has three lugs 52 I formed on each end wall and a pair of lugs 53 formed on each of the front and rear walls. Each lug is vertically bored to accommol-¦ date bolts (not shown) for mounting the grid melter upon the top !
¦¦ of the reservoir 13 and securement of a gasket hold-down plate 55 1 to the top of the grid melter. A gasket 56 is clamped between the top of the grid melter and the hold-down plate 55. It extends inwardly into contact with the side walls of the hopper tube 32 so l '~ as to form a seal to prevent gases from escaping around the edge ¦l of the hopper to the atmosphere. The gasket 56 also enables the hopper ll to be evacuated or to maintain a blanket of inert gas 2Q l over the top of the thermoplastic material. Such evacuation of the hopper or maintenance of an inert blanket are employed in ~ , some applications to retard or minimize degradation of the molten !
,' ! l material.
,~ I In the illustrated embodlment the grid melter has an integral annular boss 54 extending forwardly frorn its front wall.
I 1I The boss 54 also has three lugs 57 equidistantly spaced about its outer wall and bored as illustrated at 58 to accommodate bolts (not shown) ~or mounting the grid melter atop the reservoir.
¦¦ There are nine horizontal bores 60 which extend through 30 1¦ the front wall and through the base portions of each row of heater , . . .
ll 7_ - ' 101i4695 element pro~.~us LOnS 45. ~n electrica:l resistance hea-ter 61 is mountcd within e~ach of these bores 60 so that one heater extends in-to and through the bases o~ each row of frustoconicaL heater ll elements. I'here is~also a bore 63 which ex-tends through the rear : ll wall of the rnel-ter within which a temperature sensor device (not ll shown) is mounted. This device is used to control and maintain : ¦¦ the temperature of -the hea-ter elements 61 at a preset temperature.;
.' , There is also a transverse bore 64 formed in the rear wall of ; I the grid melter block. This transverse bore accommodates a con-ll ventional temperature measuring gauge 65, the front face 66 of .~ Il ; I which is located upon the control panel of the housing 26. 1 Reservoir ~¦ The reservoir 13 comprises an open top, closed bottom ~¦ receptacle which is fixedly secured to the bottom of the grid I li melter. Preferably there is an insulative gasket 67 located be-','2:~ ij tween the top of the reservoir 13 and the bottom of the grid melter 12. The reservolr has shallow side walls 70, 71 and a ;
shallow rear wall 72.: The front wall 73 is slightly deeper such ¦
that the bottom of the reservoir slopes downwardly from the front I
20 1 and side walls toward a front opening 75 in the front wall 73. ~ 1 This openlng 75 functions as the entrance Eor molten material into a blind recess 76 formed in a pump mounting boss 77 of the reser-boir. The blind recess 76 of the pump mounting boss 77 is inter- il sected by a vertical bore 83 which extends from the bottom :of the ¦
~ boss 77 into the recess 76. The:pump 14 is located within this f 1I bore 83 and bolted to the manifold block 15.
The boss 77 has a base portion 78, the bottom flat ~i ¦ surface of which rests atop and is supported by the manifold ;¦ block 15. The manifold block in turn rests upon and is supported ¦ from the base 25 of the housing. The maniEold block 15 and pump ! l ,i! , .
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rnountinc;~ boss 77 of ihe reservoir are secl~rcd tocJether by bolts (not shown) WhiCIl exterld throuyh and are thread~d into aligned ver-tical bores ;, In the preferred embodiment there are two identical l "U" shaped resistance heaters 85 molded within ~he bottom walls ¦ 17, 18 and 19 of the reservoir. There is also a tube 87 molded I within the bottom wall 18. A temperature sensor is inserted into the tube 87 and is u-tilized to control the flow of electrical current to the hea-ters 85 so as to maintain the bottom wall at a I preset temperature. There is also a transverse bore 82 located ¦
¦j beneath the side wall of the reservoir. The bore 82 accommodates ¦
¦ a conventional temperature measuring gauge 89, the front face 90 ¦
of which is located on the control panel of the housing 26. The I heaters 85, as shown in Figure S, aré positioned~on opposite sidesl of the pump 14 to insure uniform heating of the pump 14 and mani- ¦
fold 15.
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, ; The pump 14 has a top surface 92 which;is co-planar , wlth and forms a cont1nuation of the sloping surface 93 of the i' reservoir bottom wall 18. In the preferred ernbodiment lt slopes at an angle of approximately 5 to the horizontal plane. The slope is such~that the natural flow of moltenlmaterial~over the j bottom wall of the reservoir~is toward the pump inlet 20. 1 ~;
The pump 14 comprises a pair of counter-rotating shafts ! 94, 95 which extend;above the top surface 92 of the pump and which tend because of their rota-tion to force material between the two : . ~ i :
il toward an overhanyiny re~ar wall 97 formed on the~inside of an ¦1 overhanying hood 98. The wall 97 overhanys the entrance port 20 ¦
!! o the pump and slopes toward the entrance port so that material i,', .
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contacl:in~.l tl~e walL 97 is caused to ELow toward the inlet port 20 of the pump.
The rema:inder of the pump, other than the end plate : l 96 and the associa-ted infeed mechanism comprises a pair of interconnected gears 103, 104 which are drivingly keyed to a ¦I drive shaft 94 and idler shaft 95. These gears rotate within a ¦ generally four leaved clover-shaped recess 105 of the gear stator ¦j 106. One "leaf" 107 of the clover-shaped opening in the stator ,1 106 is open to communicate with the inlet port 20 and the opposite ~-I "leaf" 108 of the recess communicates with an outlet port 109 of a lower end plate 110. The other "leaves" 111 and 112 of the 1 ! clover-shaped recess 105 accommodate -the counter-rotating inter-~ ~ engaged gears. . I ~:
¦I. The lower end plate 110 includes in addition to the ~ out]et por-t 109, a pressure balancing port 115 which extends :J~ . ¦ through the end plate 110 and communicates with a pressure bal~
ancing port 116 of the maniEold block 15. Additionally, the end plate 110 includes a pair of vertical apertures 117 and 118 which :~
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accommodate the lower ends of the shafts 94, 95 and function as ~:l 20 ,I bearings or journals for those lower ends. Between the bottom surface 120 of the end plate 110 and the top surface of the mani- ¦
: j !
: ~ ! fold block 15 there is a conventional O-ring 121 which fits with- ¦
in a semi-circular cross~ sectional annular ring 122 in the top ¦I surface of the manifold block. This O-ring 121 functions as a ~¦ seal between the bottom surface of the reservoir 13 and the top .:~ !! surface of the manifold 15. Except for this seal between the ~ ¦! manifold and the reservoir 13 there are no gaskets or seals.
.. iI While leakage does occur around the periphery of the shafts 94, 'I jl 95 with.in -the pump that leakaye is accommodated by permitting .~ 30 ¦~ it to flow through a T-shaped slot 123 in the -top surface of the i 1~ manifold block back to the inlet or suc-tion side of the pump.
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I Witll reference to ii<Jure 2 it will be seen that the Il T-shapcd slot 123 interconnects -the vertical bores 117, 118 of ¦¦ the lower elld plate as well as the vertical por-t 115 of the end plate. Consequelltly, leakage of mol-ten material flowing between - jl the rotating shafts 94, 95 and the inside surface of the bores 117, 118 is simply routed -through -the T-shaped slot 123 back to !I the suction side of the pump through the connecting bore 115 of the pump end plate 110.
The pump 14 is secured to the top of the manifold o !¦ block by bol-ts (not shown) which extend vertically -through verti-! cal bores 126, 127. In the preferred embodiment of the pump, I spacer sleeves (not shown) are located within the bores 126, 127 between the bolts and the inner surfaces of the bores 126, 127.
Manifold Block ~`~ I The manifold block 15 is ported such that the molten material flowing from the outlet port 109 of the pump flows into the vertical inlet port 130 of the mani~old. This inlet port ¦ communicates with a longitudinal passage 131, a transverse pass-age 132, a longitudInal passage 133 on the front side of the l, block and ou-tlet ports 134 and 135. Conventional dispensers, as for example conventional hot melt applicator guns or dispensers of the~type shown ln United tates Reissue Patent No. 27,865 or United States Patent No. 3,690,518 may be attached to the outlet ports 134, 135 of the mani~old block, either directly or by con- I
ventional heated hoses. The number of outlet ports and connected j I dispensers will vary depending upon the particular applicati.on to ¦, whlch -the system is applied.
Intersecting the longitudinal passageway 131 and extending coaxially with it there is a filter mounting bore 137.
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1~4~Cj This bore accommodates a conventional filter, one end of which comprises a plug 138 threaded into a threaded end section 139 of the bore 137. A complete description of the filter assembly may be found in United States Patent No. ~:
3,224,590 which issued Dec~mber 21, 1965. :
Intersecting the longitudinal passage 133 there is a one-way check valve mounting bore 149 which extends in~
wardly rom the front surface 150 of the manifold block into communication with the pressure balancing port 116. This . .- -check valve mounting bore also intersects the longitudinal passage 133 in the front of the manifold. Threaded i~to the .~.-bore 149 there is a conventional pressure relief one-way check valve (not shown).
Pum~ Drive Svstem -The pump 14 may be driven in rotation by any con, ventional type of drive motor 165 and ïnterconnected drive ~ :
shaft 166. In the preferred embodiment illustrated in Figures 1-4, the motor drive shaft has a key 168 on its .
outer end which fits within a key-way slot 169 at the upper end o~ the pump drive shaft 94. The motor 165 is mounted . atop the cover 26 of the housing, and is a rotary pneumatic motor driven by conventional shop air pressure and operative .
. ,.~ .
to effect rotation of the shaft 166 at a predetermined speed through a conventional gear reduction unit mounted interiorly .
.;~ of :the motor housing.
..... .. ............ ..... , ................. . ~ , . Hopper Melt Back Prevention ~
The thermoplastic material melting and dispensing ~ :
:: .
~ appara-tus heretofore described except for the shroud 29 is ., ~
completely disclosed in aforementioned co-pending application .- ;
Serial No. 24S~72. The invention of this application re- -~
sides in the provision of means for ') : ~, ' : .
r~
Il prevcnkincJ moLten material melted by the gri~ melter 12 from ¦¦ backiny up into the hopper 11. If khe feedstock material is I¦ rneltecl by the grid melter 12 ak a faste.r rate than it is dispensed : through -the dispensèr 22, this condition can occur. To prevent such melt back the shroud 29 is loca-ted over and spaced from , the bo-tt.om ex-terior walls of the hopper so as to provide an air ~ ¦I chamber 200 through which forced air may be continually moved i ¦ when the appara-tus 5 is in use. That air flow is operative.to ~; ¦ dissipate or carry heat away from the exterior walls of tube 32 ¦ of the hopper 11 at a faster rate than heat may be imparted to l. ~ those walls by incoming molten thermoplastic material from the ::` melter 12. Consequently, the cool walls 32 of the hopper act as a thermal barrier to prevent back-up of molten material into the ::
1~ I hopper.
: l I The shroud 29 comprises a base section 201 and an upper ~ I section 202. The base section consists of four interconnected ; ¦I side walls which are spaced ou-twardly from the vertical walls 32 ¦ of the hopper, a lower flange 203, and an upper flange 204. The lower flange 203 extends outwardly from the bottom surface~of the ¦I base section 201 and rests atop the gasket hold-down plate 55.
~ The upper.section 202 of the shroud also has four ! ¦I vertical walls spaced outwardly from the walls 32 of the hopper,a lower flange 205, and an upper flange 206. The lower flange ~¦ 1 of the upper section 202 extends inwardly from the four side walls `! ¦ of the upper section 202 and rests atop the outwardly extending flange 204 of the bottom section 201. The top flange 206 of the -top section 202 extends inwardly inko contact with the exterior ~i !surface of the side walls 32 of the hopper. In the preferred ! ¦ embodiment, the lower sec-tion 201 of the shroud is bolted or 1 1, 1 6~69S i, !
I otherwise fi~ecl to the top section 202 and i.o the -top of the grid¦
¦l melter by corlveni;onal connectors (not shown). ~rhe hopper 11 is ¦
¦ simply inse~t:ed into thc shroud an~ forced downwardly until the flanye 35 of the ~lopuer abuts the top flange 20f, of the shroud.
, ,li The flange 35 is generall~ not bolted or o-therwise Eixed to the ¦¦ shroud so that the hopper can easily be removed by simply pulling it upwardly through the top of the shroud. I
¦l In the embodiment of Fic3ures 1-4, a conventional elect- !
¦ rical motor driven fan 210 is mounted within one side wall 211 of ' 10 j the upper section 202 of the shroud 29. This fan is operative to blow a continuous stream of forced air through the interior of the shroud and out through orifices 212 in the bottom section i ,~
¦~ j; 201 of the shroud so long as the melting and dispensing apparatus~
i 5 is in use. I
I have found that the side walls 32 of the hopper 11 are preferably made from aluminum so as -to facilitate heat trans-¦
fer away from and out of the hopper side walls by the continuously ~, moving air stream from the fan 210. If the air stream is to pre- ¦ ' .i ;, . , , vent bridging of molten material within the hopper resulting from~
,I the molten material freezing therein, the air flow through the j II chamber 200 must be capable of dissipating heat at a faster rate j, l~ than it may be imparted to the side walls 32 by,incoming molten "~ ~ jl material. Construction of the side walls of the hopper from ! aluminum'facilitates this dissipation of heat from the side walls ¦
by the forced air flowing over the exterior surface. ' '~
¦i Referring now to Figure 5 there is illustrated a second !
¦ preferred embodiment of an apparatus Eor preventing melt back of ~j li molten material from the grid melter 12 in-to the bottom of the hopper 11. In this embodiment, the upper end of walls 32 of 11 , .
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Il hopper l:L is we:l(lccl or o~ erwise sup[~o:rtil-ly.l.y secure~ to the upper,l~ end of shroud 220. In this embodiment/ rather than utilizing l -the Ean 210 to Eorce a:ir throucJh the air flow chamber 221 between I
3 i ~ I
the interior surface oE the shroud and the exterior surface of the walls 32 of t}le hopper 11, exhaust air Erom the pneumatic motor j! 165 is supplled via a conduit 222 to the chamber 221. This ex-haust air then is caused ko move upwardly through the chamber over ~Z ~1 the exterior walls 32 of -the hopper and out through ports 223 in ll the shroud.
.`~ 10 ! Compxessed aix drives the motor 165. As the compressed !
. air is exhausted from the outlet of the air motor and the conduit ¦
¦ 222, it expands rapidly into the cooliny chamber 221 thereby cooling, generally to a temperature at or~below 32F. Therefore, exhaust air from -the air motor 165 continually chills or cools ¦
~ the sidewalls 32 of hopper 11 as it passes upwardly over the`~` j outer surfaces of walls 32.
Referring now to Figure 6 there is illustrated a third embodiment which is, a further modificatlon of the apparatus illus~
trated in Figure 5 of the drawings. In this embodiment, the 20 l~ exhaust air from motor 165 flows into the cooling chamber 221 and at least a portion of the air-from conduit 222 is directed into a , cooling tube 225. This tube 225 extends transversely between and is affixed to the side wall 32 of the hopper 11. It is located directly in the path of~the air stream emitted from the conduit ~ ;1 222 into the chamber 221 so that most of the cool exhaust air : ! 11 .from the conduit is forced to flow through the cooliny tube. In the course oE passing through the tube, the cool exhaùst air ~ extracts heat from the solid thermoplastic material disposed ~.
7 ¦I within the lower end of the hopper as well as from the tube and . 30 'Z the connecting hopper walls.
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' ~ ' , ' , ' , ` ' . . ' ' . , , . : , , , -~64~6~3i5 The primary advantage of this invention resid~s in its elimination of "brid~in~" or forming of a solid barrier across and between the inside surface of the walls of a feed hopper of a thermoplastic melting and dispensing apparatus.
The elimination of this melt back into the hopper eliminated the problem of the apparatus feed being temporarily disabled by a solid barrier of feedstock contained within the hopper when the apparatus is turned off and then subseguently re-started.
While I have disclosed only three embodiments of my -invention, persons skilled in the art to which this invention pertains will readily appreciate changes and modifications which may be made in the invention. Therefore, I do not intend to be limited except by the scope of the following ~ appended claims. ;
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~646915 In one r~rticular aspect the present i.nvent:Lon provides an al)parcl~us ror ~onvertillK ;o:l.:i.~l Lhermol):l.a~ti.c maLc~ria:l. to moltell -thermop].astic mater:ial and for dispensing the molten thermoplastic material., comprisLng a housing inc:l~ld:ing a hopper having side walls ?
for receiv:Lng solid thermoplast:Lc materi.al, a flow through grid melter having a continuo-ls side wall, a bottom wall, and an open top for receiving said solid thermoplastic material from said :.
hopper, said bottom wall comprising a plurality of spaced heating ,~ ' . ' ' ., sections, a plurality of discharge openings in said bottom wall of ;.~
: 10 said grid melter between said spaced heating sections, a reservoir .; . -mounted beneath the grid melter and adapted to receive molten material from said discharge openings of said grid melter, means for heating said bottom wall of said grid melter, a di.spenser operable to dispense said molten thermoplastic material, a pump for ;;~`
supplying said molten thermoplastic material from said reservoir .
: to said dispenser, and cooling means for maintaining said hopper .. ;~ -~
: side walls below the solidification temperature of said molten material so as to prevent the melt back of molten material from . said grid melter into said hopper, sald cooling means comprising 20 a shroud surrounding at least the lower portion of said hopper, .
said shroud defining an air chamber between the inner walls of . `~
said shroud and the outer walls of said hopper, and air flow means ~: for supplying a flow of forced air through said air chamber so as ~ to cool the lower portion of said hopper. .;~
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llese alld o~her aspects of tl~is inve~ntion will be more ~¦ readily apparerl~ from the followiny description of the drawings ¦ in which:
Fi~ure L is a pers~ective view oE one embodiment of a thermoplastic material melting and dispensing apparatus incor- ¦
porating the invention of this application.
¦ Figure 2 is an exploded perspective view of a portion ¦ of the apparatus of Figure 1.
Figure 3 is a side elevational view, partially broken 'I away, of a portion of the apparatus of Figure 1.
Figure 4 is a cross sectional view taken on line 4-4 of ¦
Figure 3.
' Figure 5 is a cross sectional view, similar to Figure ', 4, but illustrating a second embodiment of the inven-tion.
Figure 6 is a fragmentary view in section, similar to t 11 Figure 5, but illus-trating a third embodiment of the invention.
¦¦ Figure 7 is a cross sectional view taken on line 7-7 , ~ ;
of Figure 6.
j Referring first to Figures 1 and 2, it will be seen ' that the thermoplastic material melting and dispensing apparatus 5 of this invention comprises a housing 10 within which there is located a hopper 11, a grid melter 12, a reservoir 13, a gear ¦ 1! pump 14, and a manifold block 15. Solid thermoplastic material 6~1 ,1 in the form of chunks ~Fig. 4), pelle-ts (Fig. 6), or blocks 1, are placed in *he top of the hopper 11 from which they flow ¦ through the open bottom into contact with the top surface of the grid mel-ter 12. The grid melter 12 is heated so that surface contact of the solid thermoplastic material wi-th the top surface !~ f the grid causes the solid thermoplastic material to be melted ', il and converted to a molten state. The molten thermoplastic material ¦ 7 then flows downwardly through bottom passageways 16 in the grid ~
. . . .
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, ' ' ,: ,'.,, . ' :' 10~i46~5 , ' ' rnel~er into tllc rcservoir 13 locaLed irnmedi~tcly beneath the melter 12. The reservoir has sloping bottom walls 17, 18 and 19 which direc~ the molten material toward the inlet 20 of -the pump 14. The pump -then moves the molten rnaterial into the Manifold block 15 from whence it is directed to one or more conventional applicators or dispensers 22 via hoses or conduits 21.
~ 11 , .
Housing, Hopper The housing 10 comprises a shee-t metal base pla-te 25 and a cover 26 mounted atop the base plate. The cover 26 encloses ~, 10 ¦¦ two sections of the applicator, the melt section 27 and the con-¦ trol section 28. The two sections are separated by an insulative barrier (not ShOWll). Within the control section 28 are all of ¦¦ the electrical components for controlling the temperature of the ¦I components throughout the system. These controls form no part of !
the invention of this application and are conventional in commer-cially available equipment, as for example equipment of the type ¦~
jl shown in U. S. Patent No~ 3,792,901, issued February 19, 1974 and ¦
j 1' assigned to the assignee of this application.
~ The top 30 of the cover has an opening 31 into which ;¦~ 20 Ij there is fitted the hopper 11 and a surrounding shroud 29. The hopper comprises a vertical tube 32, the bottom 33 of which is ii open ~and the top of which is closed by a lid 34. Around the periphery of the hopper there is a flange 35 which is welded or ¦ j fixed to the exterior of the hopper and which in turn functions as the at;tachment for the hopper surrounding shroud 29, as is 1 1l explained more fully hereinafter.
. Il Grid Melter ; ;1 1 .
i' Referring to Figures 2, 3 and 4, i-t will be seen that 1 the grid melter 12 comprises a receptacle into which solid !l `........... I --5--':1 1, . I
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46'9S
-thermoplastic rnaterial flows from the hopper 11. '~'his receptacle Il comprises four side walls 37, 38, 39 and ~0 and a bottom flange ¦l ~1. The bo-ttom itself comprises a plurality of vertical pro~
¦ trusions or heater elements 43, each one of which is hexagonal ¦ in cross section at the base ~2 and has an upper end shaped as jl a truncated cone. The protrusions are arranyed in longitudinal ¦¦ rows 44 with -the base 42 of each protrusion 45 interconnected and integral with the adjacent protrusions 45 of the same row ¦1 44. The pro-trusions 45 of adjacent rows 44 are longitudinally ; 10 ~ offset from each of the protrusions of the adjacent rows such that when viewed in top plan -the protrusions create a staggered I pattern or rows and columns, but with the protrusions of the I ~ j', columns spaced apart and separated by~an intermediate row of ! protrusions. There are open passageways 16 located on opposite , I~ sides of each row and extending for the length of the row. These ~ passageways 16 open into the top of the reservoir 13.
`' ¦ In the melting of thermoplastic materials it is critical ~ that the melter have a large surface area in contact with the : i l ~
poor heat conductive blocks or pellets of thermoplastic material.
~; 20 il Prior to this inventlon attempts have been made to increase the surface area by forming ribs on the bottom of the grid melter as ln U. S. Patent No. 3,531,023. The grid melter 12 of this , invention incorporating~the truncated cone shaped heater elements ~ j has been Lound to increase the throughput of the grid melter over :!~ ¦ rib type grids by as much as 30 or 40~ while maintaining the same surface temperature of the grid so as to avoid degrading of the ¦ material.
¦~ The protrusions are formed as truncated cones or pyra-¦¦ mids having flat or blunt -topmost end surfaces 50. As used ~l throughout this application and in the claims the term "cone"
is used in the generic sense to include pyramids which have ~' 1, , ..... , ~
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~L064695 Il anywhere frolll three to an infinite nurnber of sides. When the ¦¦ pyramid has an infinite nul~er of sides it is of course circular ¦
in cross sec-tion. The truncation or bluntiny of the topmost sur-¦
'¦ face 50 of the "cone" increases the area in contact with the solid thermoplastic ma-terial and enables the surface temperature of the complete "cone" to be evenly main-tainecl with a minimal power input.
Ii In one preferred embodiment the grid melter 12 is I ! formed as an integral casting. This casting has three lugs 52 I formed on each end wall and a pair of lugs 53 formed on each of the front and rear walls. Each lug is vertically bored to accommol-¦ date bolts (not shown) for mounting the grid melter upon the top !
¦¦ of the reservoir 13 and securement of a gasket hold-down plate 55 1 to the top of the grid melter. A gasket 56 is clamped between the top of the grid melter and the hold-down plate 55. It extends inwardly into contact with the side walls of the hopper tube 32 so l '~ as to form a seal to prevent gases from escaping around the edge ¦l of the hopper to the atmosphere. The gasket 56 also enables the hopper ll to be evacuated or to maintain a blanket of inert gas 2Q l over the top of the thermoplastic material. Such evacuation of the hopper or maintenance of an inert blanket are employed in ~ , some applications to retard or minimize degradation of the molten !
,' ! l material.
,~ I In the illustrated embodlment the grid melter has an integral annular boss 54 extending forwardly frorn its front wall.
I 1I The boss 54 also has three lugs 57 equidistantly spaced about its outer wall and bored as illustrated at 58 to accommodate bolts (not shown) ~or mounting the grid melter atop the reservoir.
¦¦ There are nine horizontal bores 60 which extend through 30 1¦ the front wall and through the base portions of each row of heater , . . .
ll 7_ - ' 101i4695 element pro~.~us LOnS 45. ~n electrica:l resistance hea-ter 61 is mountcd within e~ach of these bores 60 so that one heater extends in-to and through the bases o~ each row of frustoconicaL heater ll elements. I'here is~also a bore 63 which ex-tends through the rear : ll wall of the rnel-ter within which a temperature sensor device (not ll shown) is mounted. This device is used to control and maintain : ¦¦ the temperature of -the hea-ter elements 61 at a preset temperature.;
.' , There is also a transverse bore 64 formed in the rear wall of ; I the grid melter block. This transverse bore accommodates a con-ll ventional temperature measuring gauge 65, the front face 66 of .~ Il ; I which is located upon the control panel of the housing 26. 1 Reservoir ~¦ The reservoir 13 comprises an open top, closed bottom ~¦ receptacle which is fixedly secured to the bottom of the grid I li melter. Preferably there is an insulative gasket 67 located be-','2:~ ij tween the top of the reservoir 13 and the bottom of the grid melter 12. The reservolr has shallow side walls 70, 71 and a ;
shallow rear wall 72.: The front wall 73 is slightly deeper such ¦
that the bottom of the reservoir slopes downwardly from the front I
20 1 and side walls toward a front opening 75 in the front wall 73. ~ 1 This openlng 75 functions as the entrance Eor molten material into a blind recess 76 formed in a pump mounting boss 77 of the reser-boir. The blind recess 76 of the pump mounting boss 77 is inter- il sected by a vertical bore 83 which extends from the bottom :of the ¦
~ boss 77 into the recess 76. The:pump 14 is located within this f 1I bore 83 and bolted to the manifold block 15.
The boss 77 has a base portion 78, the bottom flat ~i ¦ surface of which rests atop and is supported by the manifold ;¦ block 15. The manifold block in turn rests upon and is supported ¦ from the base 25 of the housing. The maniEold block 15 and pump ! l ,i! , .
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rnountinc;~ boss 77 of ihe reservoir are secl~rcd tocJether by bolts (not shown) WhiCIl exterld throuyh and are thread~d into aligned ver-tical bores ;, In the preferred embodiment there are two identical l "U" shaped resistance heaters 85 molded within ~he bottom walls ¦ 17, 18 and 19 of the reservoir. There is also a tube 87 molded I within the bottom wall 18. A temperature sensor is inserted into the tube 87 and is u-tilized to control the flow of electrical current to the hea-ters 85 so as to maintain the bottom wall at a I preset temperature. There is also a transverse bore 82 located ¦
¦j beneath the side wall of the reservoir. The bore 82 accommodates ¦
¦ a conventional temperature measuring gauge 89, the front face 90 ¦
of which is located on the control panel of the housing 26. The I heaters 85, as shown in Figure S, aré positioned~on opposite sidesl of the pump 14 to insure uniform heating of the pump 14 and mani- ¦
fold 15.
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, ; The pump 14 has a top surface 92 which;is co-planar , wlth and forms a cont1nuation of the sloping surface 93 of the i' reservoir bottom wall 18. In the preferred ernbodiment lt slopes at an angle of approximately 5 to the horizontal plane. The slope is such~that the natural flow of moltenlmaterial~over the j bottom wall of the reservoir~is toward the pump inlet 20. 1 ~;
The pump 14 comprises a pair of counter-rotating shafts ! 94, 95 which extend;above the top surface 92 of the pump and which tend because of their rota-tion to force material between the two : . ~ i :
il toward an overhanyiny re~ar wall 97 formed on the~inside of an ¦1 overhanying hood 98. The wall 97 overhanys the entrance port 20 ¦
!! o the pump and slopes toward the entrance port so that material i,', .
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contacl:in~.l tl~e walL 97 is caused to ELow toward the inlet port 20 of the pump.
The rema:inder of the pump, other than the end plate : l 96 and the associa-ted infeed mechanism comprises a pair of interconnected gears 103, 104 which are drivingly keyed to a ¦I drive shaft 94 and idler shaft 95. These gears rotate within a ¦ generally four leaved clover-shaped recess 105 of the gear stator ¦j 106. One "leaf" 107 of the clover-shaped opening in the stator ,1 106 is open to communicate with the inlet port 20 and the opposite ~-I "leaf" 108 of the recess communicates with an outlet port 109 of a lower end plate 110. The other "leaves" 111 and 112 of the 1 ! clover-shaped recess 105 accommodate -the counter-rotating inter-~ ~ engaged gears. . I ~:
¦I. The lower end plate 110 includes in addition to the ~ out]et por-t 109, a pressure balancing port 115 which extends :J~ . ¦ through the end plate 110 and communicates with a pressure bal~
ancing port 116 of the maniEold block 15. Additionally, the end plate 110 includes a pair of vertical apertures 117 and 118 which :~
.: i .
accommodate the lower ends of the shafts 94, 95 and function as ~:l 20 ,I bearings or journals for those lower ends. Between the bottom surface 120 of the end plate 110 and the top surface of the mani- ¦
: j !
: ~ ! fold block 15 there is a conventional O-ring 121 which fits with- ¦
in a semi-circular cross~ sectional annular ring 122 in the top ¦I surface of the manifold block. This O-ring 121 functions as a ~¦ seal between the bottom surface of the reservoir 13 and the top .:~ !! surface of the manifold 15. Except for this seal between the ~ ¦! manifold and the reservoir 13 there are no gaskets or seals.
.. iI While leakage does occur around the periphery of the shafts 94, 'I jl 95 with.in -the pump that leakaye is accommodated by permitting .~ 30 ¦~ it to flow through a T-shaped slot 123 in the -top surface of the i 1~ manifold block back to the inlet or suc-tion side of the pump.
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I Witll reference to ii<Jure 2 it will be seen that the Il T-shapcd slot 123 interconnects -the vertical bores 117, 118 of ¦¦ the lower elld plate as well as the vertical por-t 115 of the end plate. Consequelltly, leakage of mol-ten material flowing between - jl the rotating shafts 94, 95 and the inside surface of the bores 117, 118 is simply routed -through -the T-shaped slot 123 back to !I the suction side of the pump through the connecting bore 115 of the pump end plate 110.
The pump 14 is secured to the top of the manifold o !¦ block by bol-ts (not shown) which extend vertically -through verti-! cal bores 126, 127. In the preferred embodiment of the pump, I spacer sleeves (not shown) are located within the bores 126, 127 between the bolts and the inner surfaces of the bores 126, 127.
Manifold Block ~`~ I The manifold block 15 is ported such that the molten material flowing from the outlet port 109 of the pump flows into the vertical inlet port 130 of the mani~old. This inlet port ¦ communicates with a longitudinal passage 131, a transverse pass-age 132, a longitudInal passage 133 on the front side of the l, block and ou-tlet ports 134 and 135. Conventional dispensers, as for example conventional hot melt applicator guns or dispensers of the~type shown ln United tates Reissue Patent No. 27,865 or United States Patent No. 3,690,518 may be attached to the outlet ports 134, 135 of the mani~old block, either directly or by con- I
ventional heated hoses. The number of outlet ports and connected j I dispensers will vary depending upon the particular applicati.on to ¦, whlch -the system is applied.
Intersecting the longitudinal passageway 131 and extending coaxially with it there is a filter mounting bore 137.
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1~4~Cj This bore accommodates a conventional filter, one end of which comprises a plug 138 threaded into a threaded end section 139 of the bore 137. A complete description of the filter assembly may be found in United States Patent No. ~:
3,224,590 which issued Dec~mber 21, 1965. :
Intersecting the longitudinal passage 133 there is a one-way check valve mounting bore 149 which extends in~
wardly rom the front surface 150 of the manifold block into communication with the pressure balancing port 116. This . .- -check valve mounting bore also intersects the longitudinal passage 133 in the front of the manifold. Threaded i~to the .~.-bore 149 there is a conventional pressure relief one-way check valve (not shown).
Pum~ Drive Svstem -The pump 14 may be driven in rotation by any con, ventional type of drive motor 165 and ïnterconnected drive ~ :
shaft 166. In the preferred embodiment illustrated in Figures 1-4, the motor drive shaft has a key 168 on its .
outer end which fits within a key-way slot 169 at the upper end o~ the pump drive shaft 94. The motor 165 is mounted . atop the cover 26 of the housing, and is a rotary pneumatic motor driven by conventional shop air pressure and operative .
. ,.~ .
to effect rotation of the shaft 166 at a predetermined speed through a conventional gear reduction unit mounted interiorly .
.;~ of :the motor housing.
..... .. ............ ..... , ................. . ~ , . Hopper Melt Back Prevention ~
The thermoplastic material melting and dispensing ~ :
:: .
~ appara-tus heretofore described except for the shroud 29 is ., ~
completely disclosed in aforementioned co-pending application .- ;
Serial No. 24S~72. The invention of this application re- -~
sides in the provision of means for ') : ~, ' : .
r~
Il prevcnkincJ moLten material melted by the gri~ melter 12 from ¦¦ backiny up into the hopper 11. If khe feedstock material is I¦ rneltecl by the grid melter 12 ak a faste.r rate than it is dispensed : through -the dispensèr 22, this condition can occur. To prevent such melt back the shroud 29 is loca-ted over and spaced from , the bo-tt.om ex-terior walls of the hopper so as to provide an air ~ ¦I chamber 200 through which forced air may be continually moved i ¦ when the appara-tus 5 is in use. That air flow is operative.to ~; ¦ dissipate or carry heat away from the exterior walls of tube 32 ¦ of the hopper 11 at a faster rate than heat may be imparted to l. ~ those walls by incoming molten thermoplastic material from the ::` melter 12. Consequently, the cool walls 32 of the hopper act as a thermal barrier to prevent back-up of molten material into the ::
1~ I hopper.
: l I The shroud 29 comprises a base section 201 and an upper ~ I section 202. The base section consists of four interconnected ; ¦I side walls which are spaced ou-twardly from the vertical walls 32 ¦ of the hopper, a lower flange 203, and an upper flange 204. The lower flange 203 extends outwardly from the bottom surface~of the ¦I base section 201 and rests atop the gasket hold-down plate 55.
~ The upper.section 202 of the shroud also has four ! ¦I vertical walls spaced outwardly from the walls 32 of the hopper,a lower flange 205, and an upper flange 206. The lower flange ~¦ 1 of the upper section 202 extends inwardly from the four side walls `! ¦ of the upper section 202 and rests atop the outwardly extending flange 204 of the bottom section 201. The top flange 206 of the -top section 202 extends inwardly inko contact with the exterior ~i !surface of the side walls 32 of the hopper. In the preferred ! ¦ embodiment, the lower sec-tion 201 of the shroud is bolted or 1 1, 1 6~69S i, !
I otherwise fi~ecl to the top section 202 and i.o the -top of the grid¦
¦l melter by corlveni;onal connectors (not shown). ~rhe hopper 11 is ¦
¦ simply inse~t:ed into thc shroud an~ forced downwardly until the flanye 35 of the ~lopuer abuts the top flange 20f, of the shroud.
, ,li The flange 35 is generall~ not bolted or o-therwise Eixed to the ¦¦ shroud so that the hopper can easily be removed by simply pulling it upwardly through the top of the shroud. I
¦l In the embodiment of Fic3ures 1-4, a conventional elect- !
¦ rical motor driven fan 210 is mounted within one side wall 211 of ' 10 j the upper section 202 of the shroud 29. This fan is operative to blow a continuous stream of forced air through the interior of the shroud and out through orifices 212 in the bottom section i ,~
¦~ j; 201 of the shroud so long as the melting and dispensing apparatus~
i 5 is in use. I
I have found that the side walls 32 of the hopper 11 are preferably made from aluminum so as -to facilitate heat trans-¦
fer away from and out of the hopper side walls by the continuously ~, moving air stream from the fan 210. If the air stream is to pre- ¦ ' .i ;, . , , vent bridging of molten material within the hopper resulting from~
,I the molten material freezing therein, the air flow through the j II chamber 200 must be capable of dissipating heat at a faster rate j, l~ than it may be imparted to the side walls 32 by,incoming molten "~ ~ jl material. Construction of the side walls of the hopper from ! aluminum'facilitates this dissipation of heat from the side walls ¦
by the forced air flowing over the exterior surface. ' '~
¦i Referring now to Figure 5 there is illustrated a second !
¦ preferred embodiment of an apparatus Eor preventing melt back of ~j li molten material from the grid melter 12 in-to the bottom of the hopper 11. In this embodiment, the upper end of walls 32 of 11 , .
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Il hopper l:L is we:l(lccl or o~ erwise sup[~o:rtil-ly.l.y secure~ to the upper,l~ end of shroud 220. In this embodiment/ rather than utilizing l -the Ean 210 to Eorce a:ir throucJh the air flow chamber 221 between I
3 i ~ I
the interior surface oE the shroud and the exterior surface of the walls 32 of t}le hopper 11, exhaust air Erom the pneumatic motor j! 165 is supplled via a conduit 222 to the chamber 221. This ex-haust air then is caused ko move upwardly through the chamber over ~Z ~1 the exterior walls 32 of -the hopper and out through ports 223 in ll the shroud.
.`~ 10 ! Compxessed aix drives the motor 165. As the compressed !
. air is exhausted from the outlet of the air motor and the conduit ¦
¦ 222, it expands rapidly into the cooliny chamber 221 thereby cooling, generally to a temperature at or~below 32F. Therefore, exhaust air from -the air motor 165 continually chills or cools ¦
~ the sidewalls 32 of hopper 11 as it passes upwardly over the`~` j outer surfaces of walls 32.
Referring now to Figure 6 there is illustrated a third embodiment which is, a further modificatlon of the apparatus illus~
trated in Figure 5 of the drawings. In this embodiment, the 20 l~ exhaust air from motor 165 flows into the cooling chamber 221 and at least a portion of the air-from conduit 222 is directed into a , cooling tube 225. This tube 225 extends transversely between and is affixed to the side wall 32 of the hopper 11. It is located directly in the path of~the air stream emitted from the conduit ~ ;1 222 into the chamber 221 so that most of the cool exhaust air : ! 11 .from the conduit is forced to flow through the cooliny tube. In the course oE passing through the tube, the cool exhaùst air ~ extracts heat from the solid thermoplastic material disposed ~.
7 ¦I within the lower end of the hopper as well as from the tube and . 30 'Z the connecting hopper walls.
,j ~
, ~ 1' ' .
i!
: , -15-l l . , .
' ~ ' , ' , ' , ` ' . . ' ' . , , . : , , , -~64~6~3i5 The primary advantage of this invention resid~s in its elimination of "brid~in~" or forming of a solid barrier across and between the inside surface of the walls of a feed hopper of a thermoplastic melting and dispensing apparatus.
The elimination of this melt back into the hopper eliminated the problem of the apparatus feed being temporarily disabled by a solid barrier of feedstock contained within the hopper when the apparatus is turned off and then subseguently re-started.
While I have disclosed only three embodiments of my -invention, persons skilled in the art to which this invention pertains will readily appreciate changes and modifications which may be made in the invention. Therefore, I do not intend to be limited except by the scope of the following ~ appended claims. ;
',: ' ."' : ,,- .
. ;: .
' ' , ~ .
- ~, '~,, .
-16~
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~. f .. , ~` ` -, . . - ' ;
Claims (7)
PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. An apparatus for converting solid thermoplastic material to molten thermoplastic material and for dispensing the molten thermoplastic material, comprising a housing including a hopper having side walls for receiving solid thermoplastic material, a flow through grid melter having a continuous side wall, a bottom wall, and an open top for receiving said solid thermo-plastic material from said hopper, said bottom wall comprising a plurality of spaced heating sections, a plurality of discharge openings in said bottom wall of said grid melter between said spaced heating sections, a reservoir mounted beneath said grid melter and adapted to receive molten material from said discharge openings of said grid melter, means for heating said bottom wall of said grid melter, a dispenser operable to dispense said molten thermoplastic material, a pump for supplying said molten thermoplastic material from said reservoir to said dispenser, and cooling means for maintaining said hopper side walls below the solidification temperature of said molten material so as to prevent the melt back of molten material from said grid melter into said hopper, said cooling means comprising a shroud surrounding at least the lower portion of said hopper, said shroud defining an air chamber between the inner walls of said shroud and the outer walls of said hopper, and air flow means for supplying a flow of forced air through said air chamber so as to cool the lower portion of said hopper.
2. The apparatus of Claim 1 which further includes a flexible seal extending between the inside wall of said shroud and the outside wall of said hopepr, said flexible seal being located adjacent the bottom of said hopper.
3. The apparatus of Claim 1 in which said air flow means includes a motor driven fan mounted in the wall of said shroud.
4. The apparatus of Claim 1 which further includes a pneumatic motor for driving said pump, said pneumatic motor having an inlet adapted to be connected to a source of air pressure and an exhaust, and said air flow means for supplying a continuous flow of air through said air chamber comprising a conduit connecting said pneumatic motor exhaust to said air chamber.
5. The apparatus of Claim 4 which further includes conduit means disposed inside of said hopper, and said conduit means being located adjacent to and in the path of air from one end of said conduit connecting said pneumatic motor exhaust to said air chamber.
6. The apparatus of Claim 4 which further includes conduit means disposed inside of and supported by said hopper.
7. The apparatus of Claim 6 in which said hopper and conduit means in said hopper are made from aluminum.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/583,586 US3981416A (en) | 1975-02-12 | 1975-06-04 | Apparatus for melting and dispensing thermoplastic material |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1064695A true CA1064695A (en) | 1979-10-23 |
Family
ID=24333710
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA251,814A Expired CA1064695A (en) | 1975-06-04 | 1976-05-05 | Apparatus for melting and dispensing thermoplastic material |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPS5953105B2 (en) |
CA (1) | CA1064695A (en) |
DE (1) | DE2624267A1 (en) |
FR (1) | FR2313184A2 (en) |
GB (1) | GB1544438A (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5488061U (en) * | 1977-12-01 | 1979-06-21 | ||
DE2836545C2 (en) * | 1978-08-21 | 1984-11-08 | Fa. Henning J. Claassen, 2120 Lüneburg | Device for liquefying hot melt masses, especially hot melt adhesives |
JPS5556865A (en) * | 1978-10-23 | 1980-04-26 | Sansei Riko Kk | Supplying method for hot melt adhesive and supplying adaptor |
US4328387A (en) * | 1980-03-19 | 1982-05-04 | Nordson Corporation | Fail-safe thermostatically controlled circuit for use in apparatus for melting and dispensing thermoplastic material |
US4485941A (en) * | 1981-09-14 | 1984-12-04 | Nordson Corporation | Apparatus for melting and dispensing thermoplastic material |
DE3522671A1 (en) * | 1985-06-25 | 1987-01-08 | Dittberner Gmbh | Device for liquefying thermoplastic material, in particular hot-melt adhesives |
DE4445291C1 (en) * | 1994-12-19 | 1996-04-25 | Wolfgang Puffe | Thermoplastic granulate heating unit |
US9499355B2 (en) * | 2012-10-26 | 2016-11-22 | Nordson Corporation | Pedestal for supporting an adhesive melter and related systems and methods |
US12031658B2 (en) | 2016-07-15 | 2024-07-09 | Nordson Corporation | Adhesive transfer hose having a barrier layer and method of use |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2300083A (en) * | 1938-08-09 | 1942-10-27 | Du Pont | Method and apparatus for the production of structures |
US2369506A (en) * | 1941-11-15 | 1945-02-13 | Irvington Varnish & Insulator | Producing filaments from molten organic compositions |
US2571975A (en) * | 1947-05-10 | 1951-10-16 | Du Pont | Melt spinning process |
GB694123A (en) * | 1949-10-05 | 1953-07-15 | Celanese Corp | Preparation of artificial filaments, yarns, ribbons and like filamentary materials |
CH279247A (en) * | 1949-10-29 | 1951-11-30 | Perfogit S P A | Process and device for melting down the polymers of super polyamides for the production of synthetic staple fibers. |
US2755506A (en) * | 1952-08-20 | 1956-07-24 | Celanese Corp | Band spinning |
FR1142081A (en) * | 1956-02-01 | 1957-09-13 | Method and device for continuous spinning, in particular of thermoplastic materials | |
NL256449A (en) * | 1959-10-01 | 1900-01-01 | ||
CH390455A (en) * | 1961-12-26 | 1965-04-15 | Thueringisches Kunstfaserwerk | Melting pot |
US3638673A (en) * | 1969-12-23 | 1972-02-01 | Lampcraft Tool & Mold Inc | Wax-conditioning apparatus |
US3810563A (en) * | 1972-07-14 | 1974-05-14 | Mers H | Plastic melting and feeding machine |
US3876105A (en) * | 1974-02-25 | 1975-04-08 | Possis Corp | Hot melt machine |
-
1976
- 1976-05-05 CA CA251,814A patent/CA1064695A/en not_active Expired
- 1976-05-24 GB GB2144676A patent/GB1544438A/en not_active Expired
- 1976-05-29 DE DE19762624267 patent/DE2624267A1/en not_active Withdrawn
- 1976-06-03 JP JP6510476A patent/JPS5953105B2/en not_active Expired
- 1976-06-03 FR FR7616830A patent/FR2313184A2/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS51148735A (en) | 1976-12-21 |
FR2313184B2 (en) | 1980-05-30 |
FR2313184A2 (en) | 1976-12-31 |
JPS5953105B2 (en) | 1984-12-22 |
GB1544438A (en) | 1979-04-19 |
DE2624267A1 (en) | 1976-12-23 |
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