IP Library Granted Patent US 8,110,612
Granted Patent B2
US 8,110,612 · App. 11/702,282 · Granted Feb 7, 2012

Process for preparing adhesive using planetary extruder

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Quick Facts
Patent No.
US 8,110,612
App. No.
11/702,282
Granted
Feb 7, 2012
Kind
B2
Abstract

A process for preparing a pressure sensitive adhesive using a modified planetary roller extruder is described. The process in accordance with one aspect of the invention includes introducing primary raw materials including a non-thermoplastic elastomer into a feeding section of the modified planetary roller extruder, conveying the raw materials from the feeding section to a compounding section of the modified planetary roller extruder, continuously mixing the primary raw materials in the compounding section to produce a homogeneous adhesive composition. The adhesive composition may be applied to a web-form material. The compounding section of the modified planetary roller extruder includes a main spindle surrounded by and intermeshed with a plurality of planetary spindles at least one of which is a double transversal mixing spindle having a plurality of back-cut helical flights.

Claims (52)

1. An adhesive composition made according to a process comprising:

introducing primary raw materials comprising a non-thermoplastic elastomer into a feeding section of a planetary roller extruder;

conveying the primary raw materials from the feeding section to a compounding section of the planetary roller extruder;

mixing the primary raw materials in the compounding section;

providing a first means of crosslinking by adding a heat-activatable crosslinker to the compounding section;

providing a second means of crosslinking by adding an ionizing radiation crosslinker to the compounding section;

continuously producing a homogeneous adhesive composition while maintaining the temperature of the adhesive composition between about 25° C. and 100° C.;

applying the homogeneous adhesive composition to a web-form material; and

exposing the web-form material with the applied composition to ionizing radiation thereby crosslinking the adhesive composition with the ionizing radiation crosslinker;

wherein the non-thermoplastic elastomer is masticated during mixing in the compounding section such that its M w is reduced by about 50% to about 80% and the heat-activatable chemical crosslinker remains generally unactivated such that it is a residual latent curing agent available for later activation.

2. The adhesive composition of claim 1 wherein the ionizing radiation is electron beam radiation.

3. The adhesive composition of claim 2 wherein the non-thermoplastic elastomer includes natural rubber, synthetic rubber, or blends thereof.

4. The adhesive composition of claim 3 wherein the synthetic rubber includes styrene-butadiene rubbers, butadiene rubbers, synthetic polyisoprenes, butyl rubbers, polyisobutylene rubber, halogenated butyl rubbers, acrylate rubbers, ethylene vinyl acetate copolymers, polyurethanes, and blends thereof.

5. The adhesive composition of claim 1 wherein the heat-activatable crosslinker is selected from the group consisting of an accelerated sulphur or sulphur donor system, an isocyanate system, a reactive melamine resin, a formaldehyde resin, a phenol-formaldehyde resin, a reactive phenolic resin, a diisocyanate system, an epoxidized polyester resin, and combinations thereof.

6. The adhesive composition of claim 5 wherein the heat-activatable crosslinker includes an isocyanate system or a diisocyanate system.

7. The adhesive composition of claim 1 wherein the non-thermoplastic elastomer is masticated such that its M w is reduced to less than 1,000,000 as measured by GPC.

8. The adhesive composition of claim 1 wherein the step of applying includes slot-die coating, reverse roll, roll-over-roll coating, or knife-over-roll coating.

9. The adhesive composition of claim 1 wherein the planetary roller extruder contains adhesive at a temperature of about 29° C., 33° C., 52° C., 53° C., 57° C., 59° C., 60° C., 62° C., 64° C., or 72° C. in at least one barrel cylinder thereof.

10. The adhesive composition of claim 1 wherein the residence time of the homogeneous adhesive composition in the extruder does not exceed about three minutes.

11. The adhesive composition of claim 5 wherein the activation temperature of the heat-activatable crosslinker is about 110° C. to about 140° C.

12. The adhesive composition of claim 3 further comprising mixing a thermoplastic elastomer with the non-thermoplastic elastomer; wherein the thermoplastic elastomer is selected from the group consisting of styrene-isoprene-styrene, styrene-butadiene-styrene, styrene-isoprene-butadiene-styrene, styrene-ethylene-butadiene-styrene, styrene-ethylene-propylene-styrene, and combinations thereof.

13. An adhesive composition made according to a process comprising:

introducing a natural rubber, a synthetic rubber, or blends thereof into a planetary roller extruder, the natural rubber, the synthetic rubber, or the blend thereof having an initial molecular weight;

masticating the natural rubber, the synthetic rubber, or the blends thereof in the planetary roller extruder such that the initial molecular weight thereof is reduced by about 50% to about 80%;

adding a combination of an ionizing radiation crosslinker and a heat-activatable chemical crosslinker to the natural rubber, the synthetic rubber, or the blends thereof;

continuously producing a homogeneous adhesive composition while maintaining the temperature of the adhesive composition between about 25° C. and 100° C.;

applying the homogeneous adhesive composition to a web-form material; and

activating the ionizing radiation crosslinker to crosslink the adhesive composition;

wherein the heat-activatable chemical crosslinker remains generally unactivated such that it is a residual latent curing agent available for later activation.

14. The adhesive composition of claim 13 , further comprising introducing a solvent into the planetary roller extruder.

15. The adhesive composition of claim 13 wherein the heat-activatable crosslinker is the isocyanate system or the diisocyanate system.

16. The adhesive composition of claim 15 wherein the ionizing radiation crosslinker includes an acrylate resin.

17. The adhesive composition of claim 13 wherein activating the ionizing radiation crosslinker includes applying electron beam radiation.

18. The adhesive composition of claim 13 wherein the synthetic rubber includes styrene-butadiene rubbers, butadiene rubbers, synthetic polyisoprenes, butyl rubbers, polyisobutylene rubber, halogenated butyl rubbers, acrylate rubbers, ethylene vinyl acetate copolymers, polyurethanes, and blends thereof.

19. The adhesive composition of claim 13 wherein the heat-activatable crosslinker is selected from the group consisting of an accelerated sulphur or sulphur donor system, an isocyanate system, a reactive melamine resin, a formaldehyde resin, a phenol-formaldehyde resin, a reactive phenolic resin, a diisocyanate system, an epoxidized polyester resin, and combinations thereof.

20. The adhesive composition of claim 13 wherein the temperature of the adhesive composition within the planetary roller extruder is about 29° C., 33° C., 52° C., 53° C., 57° C., 59° C., 60° C., 62° C., 64° C., or 72° C.

21. The adhesive composition of claim 13 further comprising mixing a thermoplastic elastomer is selected from the group consisting of styrene-isoprene-styrene, styrene-butadiene-styrene, styrene-isoprene-butadiene-styrene, styrene-ethylene-butadiene-styrene, styrene-ethylene-propylene-styrene, and combinations thereof with the natural rubber, the synthetic rubber, or the blends thereof.

22. A process for preparing an adhesive comprising the steps of:

introducing primary raw materials comprising a non-thermoplastic elastomer into a feeding section of a planetary roller extruder;

conveying the primary raw materials from the feeding section to a compounding section of the planetary roller extruder;

mixing the primary raw materials in the compounding section;

providing a first means of crosslinking by adding a heat-activatable crosslinker to the compounding section;

providing a second means of crosslinking by adding an ionizing radiation crosslinker to the compounding section;

continuously producing a homogeneous adhesive composition while maintaining the temperature of the adhesive composition between about 25° C. and 100° C.;

applying the homogeneous adhesive composition to a web-form material; and

g) exposing the web-form material with the applied composition to ionizing radiation thereby crosslinking the adhesive composition with the ionizing radiation crosslinker;

wherein the non-thermoplastic elastomer is masticated during mixing in the compounding section such that its M w is reduced by about 50% to about 80% and the heat-activatable chemical crosslinker remains generally unactivated such that it is a residual latent curing agent available for later activation.

23. The process of claim 22 wherein the ionizing radiation is electron beam radiation.

24. The process of claim 22 wherein the primary raw materials comprise natural rubber and a tackifying resin.

25. The process of claim 22 wherein the heat-activatable crosslinker is an isocyanate.

26. The process of claim 25 wherein the isocyanate is a polyisocyanate.

27. A tape coated with the adhesive made according to the process of claim 22 .

Assignments (12)
SECURITY INTEREST Recorded Jul 1, 2022
From: BETTER PACKAGES, INC.; INTERTAPE POLYMER CORP.; IPG (US) HOLDINGS INC.; POLYAIR CORPORATION
To: WELLS FARGO BANK, NATIONAL ASSOCIATION
Reel/Frame 060558/0531 →
FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Jun 29, 2022
From: INTERTAPE POLYMER CORP.; IPG (US) HOLDINGS INC.; POLYAIR CORPORATION; BETTER PACKAGES, INC.
To: CREDIT SUISSE AG, NEW YORK BRANCH, AS COLLATERAL AGENT
Reel/Frame 060541/0448 →
RELEASE OF SECURITY INTEREST Recorded Jun 28, 2022
From: BANK OF AMERICA, N.A., AS ADMINISTRATIVE AGENT
To: INTERTAPE POLYMER CORP.; IPG (US) HOLDINGS INC.; IPG (US) INC.; CANTECH INDUSTRIES, INC.; BP ACQUISITION CORPORATION; BETTER PACKAGES, INC.; INTERTAPE POLYMER GROUP INC.; INTERTAPE POLYMER INC.; IPG LUXEMBOURG FINANCE S.A R.L.
Reel/Frame 060448/0488 →
RELEASE OF PATENT SECURITY INTEREST Recorded Jun 15, 2018
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: INTERTAPE POLYMER CORP.; BETTER PACKAGES, INC.
Reel/Frame 047225/0249 →
SECURITY INTEREST Recorded Jun 14, 2018
From: INTERTAPE POLYMER CORP.; IPG (US) HOLDINGS INC.; IPG (US) INC.; CANTECH INDUSTRIES, INC.; BP ACQUISITION CORPORATION; BETTER PACKAGES, INC.; INTERTAPE POLYMER GROUP INC.; INTERTAPE POLYMER INC.; IPG LUXEMBOURG FINANCE S.A. R.L.
To: BANK OF AMERICA, N.A., AS AGENT
Reel/Frame 046368/0196 →
SECURITY INTEREST Recorded Nov 22, 2014
From: INTERTAPE POLYMER CORP.; IPG (US) HOLDINGS INC.; IPG (US) INC.; INTERTAPE POLYMER GROUP INC.; INTERTAPE POLYMER INC.; SPUNTECH FABRICS INC.; INTERTAPE POLYMER US INC.; IPG LUXEMBOURG FINANCE S.A.R.L.
To: WELLS FARGO BANK, NATIONAL ASSOCIATION
Reel/Frame 034415/0682 →
RELEASE OF SECURITY INTEREST Recorded Nov 19, 2014
From: BANK OF AMERICA, N.A., AS AGENT
To: INTERTAPE POLYMER CORP.; IPG (US) INC.; IPG (US) HOLDINGS, INC.; IPG HOLDINGS LP; INTERTAPE POLYMER US INC.; POLYMER INTERNATIONAL CORP.; IPG FINANCIAL SERVICES INC.
Reel/Frame 034298/0705 →
SECURITY AGREEMENT Recorded Apr 3, 2008
From: INTERTAPE POLYMER CORP.; IPG (US) INC.; IPG (US) HOLDINGS INC.; IPG HOLDINGS LP; INTERTAPE POLYMER US INC.; POLYMER INTERNATIONAL CORP.; IPG FINANCIAL SERVICES INC.
To: BANK OF AMERICA, N.A., AS AGENT
Reel/Frame 020753/0044 →
MERGER Recorded Oct 19, 2007
From: INTERTAPE INC.
To: CENTRAL PRODUCTS COMPANY
Reel/Frame 019984/0352 →
MERGER Recorded Oct 19, 2007
From: IPG TECHNOLOGIES INC.
To: INTERTAPE INC.
Reel/Frame 019991/0087 →
MERGER Recorded Oct 19, 2007
From: CENTRAL PRODUCTS COMPANY
To: INTERTAPE POLYMER CORP.
Reel/Frame 019991/0421 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 3, 2007
From: TYNAN, JOHN KINCH, JR.; ST. COEUR, RICHARD WALTER; KOVACH, DAVID MICHAEL; LOMBARDO, THOMAS
To: IPG TECHNOLOGIES, INC.
Reel/Frame 019243/0764 →