IP Library Granted Patent US 12,606,686
Granted Patent B2
US 12,606,686 · App. 17/788,812 · Granted Apr 21, 2026

Crosslinked polyolefin foam and process for producing same

Inventors: Bharat I. Chaudhary (Princeton, NJ); Jian Yang (Pearland, TX)
Assignee: Dow Global Technologies LLC
C08J9/141C08L23/06C08L23/08C08L23/26C08J2201/026C08J2201/03C08J2203/14C08J2300/108C08J2323/06C08J2323/08
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Quick Facts
Patent No.
US 12,606,686
App. No.
17/788,812
Granted
Apr 21, 2026
Kind
B2
Abstract

The process disclosed includes an extruder under extrusion conditions at a temperature from 50° C. to 250° C., and a polymer composition. The polymer composition includes (A) greater than or equal to 5 wt % of a silane functionalized olefin-based polymer with first melting temperature, Tm1, (B) optionally, a nonsilane functionalized polyolefin, with second melting temperature, Tm2, (C) a highly effective silanol condensation catalyst (HEC), (D) a permeability modifier, and (E) optionally, a scorch inhibitor. The process includes introducing a physical blowing agent into the polymer composition to form a foamable composition. The foamable composition is cooled to a foaming temperature from 10° C. less than to 10° C. greater than Tm1. The foamable composition from an extruder exit die to form a foam composition. The foam composition is moisture cured to form a crosslinked foam composition having a density from 0.010 g/cc to 0.200 g/cc, and a gel content from 5% to 100%.

Claims (12)

1 . A process comprising:

providing, an extruder under extrusion conditions at a temperature from 50° C. to 250° C., and a polymer composition comprising

(A) from 5 wt % to 10 wt % ethylene/silane copolymer having a first melting temperature Tm1, from 106° C. to 110° C.,

(B) from 80 wt % to 90 wt % nonsilane functionalized polyolefin that is LDPE, having a second melting temperature, Tm2, from 111° C. to 120° C.,

(C) from 0.03 wt % to 0.2 wt % of a highly effective silanol condensation catalyst (HEC) that is an aromatic sulfonic acid catalyst, wherein wt % is based on total weight of the polymer composition,

(D) from 0.1 wt % to 2.0 wt % of a permeability modifier that is an ester of a C 10 to C 24 fatty acid, and

(E) a scorch inhibitor;

introducing, under the extrusion conditions, a physical blowing agent into the polymer composition to form a foamable composition;

cooling the foamable composition to a foaming temperature that is from 106.1° C. to 116.1° C.;

propelling the foamable composition from an exit die of the extruder to form a foam composition; and

moisture curing of the foam composition to form a crosslinked foam composition having a density from 0.015 g/cc to 0.100 g/cc and a gel content from 10% to 95%.

2 . The process of claim 1 wherein the ester of the C 10 to C 24 fatty acid is selected from the group consisting of glycerol monostearate, glycerol monobehenate, sorbitol monostearate, and combinations thereof.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 21, 2023
From: CHAUDHARY, BHARAT I.; YANG, JIAN
To: DOW GLOBAL TECHNOLOGIES LLC
Reel/Frame 065638/0789 →
Continuity (2)
Provisional Application 62953751 · Dec 26, 2019
Related Publication 20230046463A1 · Feb 16, 2023
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