Process for producing a syntactically foamed polymer composition, preferably a pressure-sensitive adhesive composition, apparatus for carrying out the process, extrudate and self-adhesive tape
View Patent ↗Process for producing a syntactically foamed polymer composition, comprising a) introducing expandable microspheres into a matrix material and mixing in a mixing machine, b) expanding the microspheres, c) the temperature distribution in the mixing machine being inhomogeneous in a plane perpendicular to the transport direction of the machine, d) maintaining the temperature of a first surface bounding the mixing space of the mixing machine, in a plane perpendicular to the transport direction of the mixing machine, at a temperature sufficient for the polymer composition containing the microspheres coming into contact with such first bounding surface to reach a temperature sufficient for commencement and continuation of expansion, e) maintaining a second surface bonding the mixing space in the same plane at a temperature sufficiently low for the polymer composition containing the microspheres coming into contact with it, not to reach a temperature sufficient for commencement and continuation of expansion.
1. Process for producing a syntactically foamed polymer composition, where
a) at least a majority of closed foam voids are achieved by introduction of expandable microspheres into a matrix material and subsequent mixing in a mixing machine ( 1 ) and
b) the expansion of the expandable microspheres is carried out after they have been introduced into the matrix material,
c) where the temperature distribution in the mixing machine ( 1 ) is inhomogeneous in a plane perpendicular to a transport direction of this machine ( 1 ),
wherein
d) a first surface ( 3 ) bounding a mixing space ( 2 ) of the mixing machine ( 1 ) is, in a plane perpendicular to a transport direction of the mixing machine ( 1 ), maintained at a temperature which is sufficiently high for the polymer composition containing the microspheres, insofar as it comes into contact with this first bounding surface ( 3 ), to reach a temperature Te which is the minimum temperature that allows for commencement and continuation of expansion,
e) while in the same plane perpendicular to a transport direction of the mixing machine ( 1 ), a second surface ( 4 ) bounding the mixing space ( 2 ) of the mixing machine ( 1 ) is maintained at a temperature which is sufficiently low for polymer composition present in the microspheres, insofar as it comes into contact with this second bounding surface ( 4 ), not to reach a temperature Te which is the minimum temperature that allows for commencement and continuation of expansion.
2. Process according to claim 1 ,
f) wherein the mixing machine ( 1 ) is a planetary-gear extruder
c′) and an externally toothed central spindle ( 5 ) thereof and an internally toothed hollow gear ( 7 ) thereof are maintained at different temperatures in at least one cross-sectional plane in such a way
d′) that said temperature (Te) is reached in the polymer composition containing the microspheres insofar as it comes into contact with the first of these two components ( 5 or 7 ),
e′) while said temperature Te is not reached in the polymer composition containing the microspheres, insofar as it comes into contact with the second of these two components ( 7 or 5 ).
3. Process according to claim 2 ,
d′1) wherein the internally toothed hollow gear ( 7 ) of the planetary-gear extruder ( 1 ) is maintained at a temperature which is sufficiently high for a said temperature Te to be reached in the polymer composition containing the microspheres, insofar as it comes into contact with this hollow gear ( 7 ),
e′1) while the externally toothed central spindle ( 5 ) is maintained at a temperature which is sufficiently low for said temperature Te not to be reached in the polymer composition containing the microspheres, insofar as it comes into contact with this sun gear ( 5 ).
4. Process according to claim 3 , wherein the matrix base polymer is introduced onto the cool central spindle 5 in the intake region of the planetary-gear extruder ( 1 ).
5. Process according to claim 3 , wherein a coolant in the interior of the central spindle ( 5 ) flows counter to the polymer transport direction.
6. Process according to claim 2 ,
d′2) wherein the internally toothed hollow gear ( 7 ) of the planetary-gear extruder ( 1 ) is maintained at a temperature which is sufficiently low for said temperature Te not to be reached in polymer composition present in the microspheres, insofar as it comes into contact with this hollow gear ( 7 ),
e′2) while the externally toothed central spindle ( 5 ) is maintained at a temperature which is sufficiently high for said temperature Te to be reached in the polymer composition containing the microspheres, insofar as it comes into contact with this central spindle ( 5 ).
7. Process according to claim 6 , wherein the temperature difference between the cooler hollow gear and the central spindle is at least 50° C.
8. Process according to claim 7 , wherein polyethylene and/or polypropylene and/or polyethylene-vinyl acetate and/or polypropylene-vinyl acetate and/or copolymers of some or all of the monomers mentioned are used as matrix base polymer, optionally together with a tack-increasing resin.
9. Process according to claim 6 , wherein the matrix base polymer is introduced onto the hot central spindle 5 in the intake region of the planetary-gear extruder ( 1 ).
10. Process according to claim 6 , wherein a coolant in the hollow gear ( 7 ) flows counter to the polymer transport direction.
11. Process according to claim 1 , wherein the temperature difference between the first surface ( 3 ) bounding the mixing space ( 2 ) of the mixing machine and the second surface ( 4 ) bounding the mixing space ( 2 ) of the mixing machine is at least 50° C.
12. Process according to claim 1 , wherein the temperature difference between said first surface ( 3 ) and the said second surface ( 4 ) is at least 50° C.
13. Process according to claim 12 , wherein acrylates and/or methacrylates are used as matrix base polymer, optionally together with a tack-increasing resin.
14. Process according to claim 1 , wherein the expandable microspheres are firstly suspended in water before being introduced into the polymer composition and remain in this aqueous environment for at least 12 h before this water-microsphere suspension is introduced into and mixed with the matrix-forming polymer composition.
15. Process according to claim 14 , in which carbon black is mixed into the polymer composition, wherein the carbon black is firstly emulsified or suspended in water and the microspheres are then suspended in this carbon black-water emulsion or suspension before this carbon black-water-microsphere suspension is introduced into and mixed with the matrix-forming polymer composition.
16. Process according to claim 14 , wherein the expansion of the microspheres is started at at least 8° C. below the expansion start temperature thereof.
17. Process according to claim 14 , wherein the water content of the mixture is reduced further at any time after introduction of the aqueous microsphere suspension into the matrix material.
18. Process according to claim 17 , wherein the evaporation of the water is forced by application of subatmospheric pressure only after a homogeneous distribution of the microspheres in the matrix-forming composition has been attained.
19. Process according to claim 1 , wherein the polymer composition containing microspheres
f) is applied in a single layer to a support of a single-sided self-adhesive tape to be formed or
g) is applied in a single layer to each of the two sides of a support of a double-sided self-adhesive tape to be formed or
h) is applied in a single layer to a liner, after which this composite is either laminated with a composite or itself forms a double-sided, support-free self-adhesive tape.