Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.
1068097
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This invention relates to a multiple pane
insulating panel for use in a window assembly comprising
two or more transparent or translucent sheets separated
` by an inter~edIate seal of plastic material between the
sheets around the periphery of the panel which seals the
air space between the sheets.
, In the course of the present description reference
will be made to sheets made of glass, but the invention is -i
,
not limited thereto.
In multiple pane panels the Joints or seals have a
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:,~ dual function. Firstly, they ensure seal tightness of the
inner air spaces situated between the sheets of glass by
- preventing the entry of vapors and dust from the outside 1 -
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air and, secondly, they keep the sheets of glass firmly
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fixed in proper poeition with respect to one another with
a given spacing therebetween.
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1068097
W'aen these joints or seals are made of plastic
material they comprise an inner filament consisting of a
first plastic material such as polyisobutylene, and an
outer mastic layer consisting of a second organic material
such as a silicone or polysulfide elastomer. This mastic
layer is in~ected between the filament and the edges of
the sheets and, by virtue of its excellent adhesive properties, ~ -
it keeps the sheets in correct position, while simultaneously
ensuring seal-tightness. The inner filament acts, inter
alia, as a spacer. To ensure that the moisture contained ;~
in the air space separating the two sheets of glass is
absorbed, a desiccant such as silica gel, levilite or a
material constituting a molecular sieve is incorporated j-~
in the inner filament.
The intermediate seals of multiple pane insulating ~;
panels may be produced from rods of thermofusible and self-
adhesive material known as "hot melt" and, with such material, -~
.
~/ it is possible to obtain relatively large spaces between the
; sheets of glass. However, it has not yet been possible to `
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7,." 20 render the manufacturing process entirely automatic. ~
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Extruded filaments have proved particularly suitable -~
for automated manufacture. Automatic apparatus designed for
applying the inner filament and the outer mastic layer have
been described in U.S. Patent 3,876,489, Canadian Appln.
Serial Nos. 237,354, 237,353 and 237,535, French Patent
~' Publication Nos. 2,195,566 and 2,207,799, all assigned to
l the assignee hereof.
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;:! When thick filaments are being deposited, for example
using machines such as those described in the aforementioned
- 30 French Patent Publication No. 2,207~799 it is necessary for
the plastic matèrial to have specific characteristics,
particularly with regard to its viscosity, thereby enabling
it to be extruded and providing it with good properties of
adhesion to glass.
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~0~8097
Plastic filaments have produced good results
in the case of air spaces of approximately 5-6 mm in
thickness, but above these thicknesses the known filaments
may be deformed and will no longer perform their spacing
and sealing functions in a satisfactory manner. Similarly
A to the thickness of the layer of air between the sheets, the
thickness of the intermediate seal refers to its dimension
measured perpendicularly to the glass sheets.
According to the present invention, there is
provided an apparatus for applying a plastic filament along
a line onto the periphery of a face of a glass sheet which
is adapted for use in the production of a multiple window
pane unit, the apparatus including an extrusion device having
an extrusion nozzle for extruding a plastic material on
the glass sheet and support means defining a surface for
supporting the glass sheet. The extrusion nozzle is `
situated in spaced relation above the supported glass ~
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sheet and disposed in a plane extending through the line
along which the plastic material is to be applied, and ~
the extrusion device includes a body portion and a head `
member disposed along a predetermined axis extending
transversely to the plane in which the nozzle is disposed.
; The head member is rotatably mounted on the body portion
for rotation about the predetermined axis for selectively
,
,~ positioning the nozzle at a variable angle with respect
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to the plane of the sheet. Means is operatively connected
to the body portion for vertically adjusting the body
portion, head member and nozzle relative to the plane of
;, the sheet onto which the plastic material is applied.
~' 30 According to a specific embodiment of the
'j~ invention, it is possible to obviate the disadvantages
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which are encountered in producing multiple pane panels
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106~097
havinc~ a very thick illtermediate seal by forming the
intermedi.ate seal from a materi.al which has a viscosity
in excess of 115 measured on a Mooney consistometer during
an 8 minute test at 40~C.
The organic material constituting the filament
can advantageously comprise a mixture of polyisobutylene
and Butyl rubber (isobutylene isoprene copolymer), with
the ratio of the weight of the polyisobutylene to the
weight of the Butyl rubber between 4:1 and 8:1, and
preferably approximately 6:1.
In view of the physical characteristics of the
filament, particularly its viscosity and adherence to glass, .
it is necessary to extrude the filament at a defined angle .
~ with respect to the plane of the glass.
,. This process may be characterized in that a
. composition is extruded onto the sheet with the material
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being deposited in such a way that the axis of the extrusion .
' nozzle at the nozzle exit forms an angle of 15-45, and
- preferably 25-35, with respect to the sheet.
. 20 Other objects, features and advantages of the ;,
present invention will be made apparent in the following
description of a preferred embodiment thereof, with
; reference to the accompanying drawings, in which:
FIG. 1 is a partial sectional view of a double :.
.. pane window having a very thick intermediate filamentary . .
;, seal;
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~ FIG. 2 is a curve illustrating the variation
u in the Mooney viscosity of the material for forming the
:.1 intermediate seal, as a function of time and at 40C;
:~ 30 FIG. 3 is a curve illustrating the variation
`! in the Mooney viscosity of the material as a function
:,.,
~ of the temperature at the end of 8 minutes;
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- 1~68097
FIC. 4 is a front, partial sectional view of the
extrusion device used for applying the intermediate filament;
FIC. S is an axial section of the extrusion head
and a portion of the body portion of the device shown in
FIG. 4;
FIG. 6 is a transverse section along the line
VI-VI of FIG. 5; and
FIG. 7 is an elevational view of the apparatus for
adjusting the vertical position of the extrusion device.
Referring to FIG. 1, a double pane insulating panel
comprises sheets of glass 1 and 2 between which an inter- :, '
mediate filament 3 is interposed, the sheets being separated
by an air space 4. The sheets of glass are held in place
by an outer polysulfide layer 5. Double pane windows designed '~
; to ensure good thermal insulation should have a relatively
. thick layer of air 4. Accordingly, the filament 3 should . '
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, possess considerable thickness e with respect to its width h. ~:
,. In the automatic apparatus described in the above- ;-
mentioned patents and patent applications, the filament 3 ~,
'~; 20 is deposited by the extrusion nozzle of an extrusion machine '.
i, directly onto one of the sheets of gla8s~ for ex8mple onto
',' sheet 1. The second sheet 2 is then placed on the filament
.' 3 and the unit is pressed in order to adhere the sheets of ::
' glass in a tight and continuous manner against the filament :
;`, 3, thus producing a sealed joint. The outer layer 5 is then .`
;:',; deposited in situ between the two sheets of glass, in the `~.
space between the filament 3 and the edges 6 and 7 of the ;
, sheets, as well as on these edges.
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10680~7
It wlll be appreciated thatl in order for the
filament 3 to be automatically placed on a sheet 1, it will
be necessary for the material forming the filament to
possess good properties of adhesion to glass, and also
adequate viscosity. If the filament does not adhere well
to glass, it will be impossible to apply it automatically
as it will slide on the surface of the glass as the sheet ~ `,
moves beneath the extrusion nozzle. Similarly, if the
filament does not possess the requisite viscosity properties
for a given thickness, it will deform, sag or bend, so that
when the second sheet of glass is placed thereover it will -
be impossible to insure seal tightness by pressing.
The applicants have found that it is possible to
automatically apply a filament having a thickness in excess ;~
of 4 mm and preferably in excess of 12 mm, or even up to
,` 19 mm and higher, with compositions having a viscosity at -
the end of 8 minutes and at a temperature of 40C which is ~
1 higher than 115 expressed as Mooney degress in a test - ~-
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carried out according to the French Standard NFT 43005 using
a Mooney consistometer. Compositions of this type are
; formed, for example, of a mixture comprising polyisobutylene
and Butyl rubber. The ratio of the weight of polyisobutylene
to the weight of the Butyl rubber is between 4 and 8, and
preferably approximately 6. The quantities of the constitutents
in these compositions are, for example, within the following
ranges, expressed in terms of percent by weight:
. Polyisobutylene:40 - 70%
Butyl Rubber:5 - 17.5% ~ .
Carbon Black10 - 40%
*Levilite: 0 - 20%
Molecular sieve:0 - 5%. `
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* - a colloidal silica for painting.
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~ 106~097
1 The molecular sieve used as a desiccant preferably con-
2 sists of a mixture of molecular sieves having absorption pore
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3 dimensions of a~out 4 A and 10 A, respectively~ The proportions
4 by weight of the sieves in the mixture are 0-4% and 0-1% ',
~f the total weight of the filament for 4 A and 10 A pores, re-
6lspectively
7¦¦ For example, a filament having the following com-
8¦1 position -
9~1 Polyisobutylene: 50'~
iO, Butyl Rubber: 10%'
i'l Carbon Black: 17.5
'~' Levilite: 20~
~ Molecular sieve: 2.5%
; I when subjected to shearing tests according to the aforementioned
"French Standard NFT 43005, by means of a Mooney consistometer,
¦yielded the viscosity curves as a function of temperature
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i 17land time shown in FIGS. 2 and 3. It was found that at 40 C, after
8 minutes, the viscosity of this composition is even higher than
Mooney.
20! A filament of this type can be,automatically deposited
21 ¦on a plate of glass at a speed of at least 30 cm~s by virtue of
22 the fact that it adheres sufficiently well to glass and that it
, ' 23 is not subject to deformation at thicknesses up to 19 mm and
',l 24 even higher.
-, 25 The filament'may be deposited by means of the
~i process according to the present invention. 'l'his process consists
' 2, 11 in applying the filament onto one of tne sheets of glass in such
~- 2~ija way that its axis forms an initial angle :~ of 15-45, and
~ 29¦~preferably 25-35, with respect to the line of application.
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10680~7
FIG. 4 is a front, partially sectional view of
the head of the extrusion device and of the extrusion nozzle.
It shows their position with respect to the glass sheet
onto which the filament is extruded. The head 11 of the
device carries on its side an extrusion nozzle 12, the axis ;
ZZ of which is also the axis of the filament 13 at the exit
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end of the nozzle, and it forms with the plane of the sheet ~--
; of glass 14 an angle ~ . On the same side of the head, a
support 15 carries a jack 16 which actuates a blade 17 -
designed to cut the filament when the latter has been
deposited on the four sides of the sheet of glass 14. The
sheet is carried by a conveyor (not shown in this figure) and
moves beneath the extrusion nozzle 12 in the direction of
arrow f. A pivoting device (not shown) makes it possible
to move the four sides of the sheet of glass in turn beneath
the nozzle.
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`l The angle ~ can vary between 15 and 45 to insure ~
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correct placement and adhesion of the filament to the sheet
of glass, and is a function of a number of parameters such as
the temperature, the state of the surface of the glass, the
rate of movement, etc. The angle can be adjusted by means
which enables the extrusion head 11 to be rotated about its
longitudinal axis.
` As shown in FIG. 5, the extrusion head 11 and the
body portion 18 of the extrusion device each have a collar or
flange 19 and 20. The outer surfaces of the flanges are
''"`,! tapered in conical configuration. Inside the head 11 and the
~i body 18 is disposed the extrusion screw 21 which compresses
the plastic material for the filament and thus supplies the
extrusion channel 22. The extrusion nozzle 12 (not shown in
this figure) is disposed at the discharge end of the
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extrusion channel 22. The extrusion
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. ~0680~5~7
head 11 and the body portion 18 are maintained in contact with
2 one another by means of a collar or clamp 23.
3 As shown in FIG. 6, the collar or clamp 23 consists
4 of two halves 24 and 25 pivoted at 26 and 27 to a bar 28. 1 -
5 A bolt 29 clamps the halves together. As shown in FIG. 5, each of
6 ¦the half collars has an inner arcuate channel in the form of
7 la double cone mating with the sides of flanges 19 and 20.
8 ! It is readily apparent that by releasing the bolt 29
I ~ lit will be possible to rotate the extrusion head 11 and thereby
10;, adjust the angle ~ (FIG. 4) and that by tightening the bolt 29
1 the head will be fixed in/~djusted position, at the same time
~,providing seal-tightness between the head and the body 18
i~ of the device.
1~! When adjusting the angle~ , the distance between
15~l the sheet of glass 14 and the end of the extrusion nozzle 12
will be varied. To ensure that optimum work conditions are
17ll always obtained,it is also an advantage to be able to adjust
and maintain this spacing in order to obtain the desired value.
, 11 '
19 ¦ This is rendered possible by the arrangement shown in FIG. 7.
In FIG. 7 the extrusion unit 30 is supported by a
21 platform 31 mounted in a pivotal manner on the axle 32 through
22 the intermediary of the beam 33. The axle 32 is supported by
23 the stationary frame 32 . Motor 34 drives the device which
24 comprises, inter alia, the body portion 18 and the extrusion
251 head 11 bearing at its end the extrusion nozzle 12.
2*1 The right half of FIG. 7 shows a conveyor generally
27 designated as 35 which is designed to move the glass sheet
28 beneath the extrusion nozzle and to rotate it 90 each time the
29 filament has been deposit ~ articular edge~ This unit
is described in copending~application Serial ~o. ~ L
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~06809q
filed con~urrently her~with and entitled "Process and
Apparatus for Applying Plastic Filaments to Sheets for ~ ;
Multiple Pane Windows", and assigned to the assignee hereof.
Accordingly it will now be described here in detail.
In this figure a threaded shaft 37 has a vertically ~ ;
ad~ustable abutment 38 fixed in position by two nuts 39 and
40. The shaft is mounted in vertical bearings (not shown)
carried by the frame 36. An abutment 41 integral with the
extrusion unit 30 comes to rest against abutment 38, the ~:~
platform 31 being pivoted in the direction of the arrow g ~ -
by the action of the compression spring 42. It will be
noted that in order to adjust the distance between the
extrusion nozzle 12 and a sheet of glass carried by the --~
conveyor 35, not shown in this figure, it is only necessary -~
to adjust nuts 39 and 40 to raise or lower the abutment 38.
As will be understood from the foregoing, the -
present invention provides, in the production of a multiple
pane insulating panel for window assemblies, a process for
applying a plastic filament on the periphery of a face of
a transparent or translucent sheet which comprises extruding . .
a plastic material from an extrusion nozzle onto the face
of said sheet at an angle at the nozzle exit which is
between 15 and 45 with respect to the plane of the face of
the sheet, said plastic material having a viscosity greater
than 115 Mooney at the end of an 8 minute test at 40C as
measured by a Mooney consistometer. Preferably the angle
is between 25 and 35. Further spec~fic features are
given in the above description of specific embodiments thereof.
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10680~7
1 The invention also provides apparatus for carrying
2 out the above process comprising an extrusion device for
3 extruding a plastic material having a viscosity greater than
4 115 Mooney at the end o~ an 8 minute test at 40 C, as measured
by a Mooney consistometer, said extrusion device having an
6 extrusion nozzle for extruding said plastic material onto the
7 face of a said sheet at an angle at the nozzle exit which is
8 between 15 and 45 with respect to the plane of the face of
9 the sheet, support means for supporting a said sheet ~eneath
~0 said nozzle exit, said extrusion device having a body portion
1'i and a head car~ying said nozzle and rotatably adjustably mounted
~¦1 on the body portion, and means for vertically adjusting said
-~j body portion with respect to the plane of the face of the sheet
i !l onto which the plastic material is applied. Advantageously the
angle is between 25 and 35. Further features of the apparatus
~ 3j ~re described above in connection with the specific embodiment~.
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l The invention also provides a multiple pane w~k~
!
18 comprising a pair of transparent or translucent sheets with a
1~ j filamentary seal between the sheets around the periphery of the
20 ¦ window, said filamentary seal being formed of a plastic material
21 I having a viscosity greater than 115 Mooney at the end of an
22 8 minute test at 40 C as measured by a Mooney consistometer.
2~ Preferred mixtures for the plastic material, and preferred
24 mixtures for the molecular sieve, and other features are set
forth in the foregoing description.
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