Note: Descriptions are shown in the official language in which they were submitted.
` ~o646~5 ~
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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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~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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~0646~3,S
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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., , ., : .
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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
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'
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1~ S
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
1 1
¦ 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.
!
~
, ; 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
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064695
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.
I, !
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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.
,., I, I
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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
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1064695
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
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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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j, I
l Ii , ,
!
1064695
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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