WO1991013115A1 - Polyolefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom - Google Patents

Polyolefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom Download PDF

Info

Publication number
WO1991013115A1
WO1991013115A1 PCT/US1991/000743 US9100743W WO9113115A1 WO 1991013115 A1 WO1991013115 A1 WO 1991013115A1 US 9100743 W US9100743 W US 9100743W WO 9113115 A1 WO9113115 A1 WO 9113115A1
Authority
WO
WIPO (PCT)
Prior art keywords
foam
polyolefin
polyethylene
blowing agent
weight
Prior art date
Application number
PCT/US1991/000743
Other languages
English (en)
French (fr)
Inventor
Chung Poo Park
Original Assignee
The Dow Chemical Company
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=23925428&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=WO1991013115(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by The Dow Chemical Company filed Critical The Dow Chemical Company
Priority to FI923756A priority Critical patent/FI923756L/fi
Priority to CA002076872A priority patent/CA2076872C/en
Priority to EP91904592A priority patent/EP0517748B1/en
Priority to BR919106085A priority patent/BR9106085A/pt
Priority to KR1019920702033A priority patent/KR100198043B1/ko
Priority to DE69123734T priority patent/DE69123734T2/de
Publication of WO1991013115A1 publication Critical patent/WO1991013115A1/en

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • C08J9/12—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent
    • C08J9/14—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent by a physical blowing agent organic
    • C08J9/141—Hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0014—Use of organic additives
    • C08J9/0023—Use of organic additives containing oxygen
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00—Use of organic ingredients
    • C08K5/04—Oxygen-containing compounds
    • C08K5/10—Esters; Ether-esters
    • C08K5/101—Esters; Ether-esters of monocarboxylic acids
    • C08K5/103—Esters; Ether-esters of monocarboxylic acids with polyalcohols
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02—Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment

Definitions

  • This invention relates to novel polyolefin compositions, to a process for making foamed or expanded articles therefrom and to foams of these polyolefin compositions which are characterized, in fresh or non- fully cured form, by improved elevated temperature distortion characteristics.
  • foamed products prepared from the present compositions possess improved electrostatic dissipation properties.
  • 25 products may, during transport, in enclosed vehicles particularly in war climates or during hot weather, be subjected to prolonged exposure at relatively high temperatures. Moreover, this concern is even further
  • CFC-I42b and isobutane permeate faster through ethylenic polymers than air resulting in foam collapse.
  • stability control agents to retard the permeation rate of these halocarbon or hydrocarbon blowing agents.
  • polyolefin foams having, in fresh foam form, good elevated temperature distortion properties as well as to provide polyolefin compositions which are expandable to form such improved polymer -it-
  • Another object of this invention is to provide polyolefin foams having increased electrostatic dissipation properties. Other objects and advantages of the present invention will be apparent from the description thereof which follows.
  • polyolefin composition comprising an polyolefin and from about 0.1 to about 10 weight percent based upon the polyolefin of glycerol monoesters of C20--24 fatty acids.
  • the present invention is the above-noted type of polyolefin composition which further comprises a volatile organic blowing agent and which is thereby expandable to form an expanded article (that is, a polymer foam) of said polyolefin composition.
  • a particularly beneficial aspect of the present invention resides in a method for substantially improving the elevated temperature distortion characteristics (for example, dimensional stability at elevated temperatures such as, for example, 66°C, the maximum heat distortion temperature, etc.) of relatively fresh polyolefin foams by incorporating therein (for example, during extrusion foaming thereof) from about 0.1 to about 10 weight percent, based upon the polyolefin, of the above described fatty acid monoesters.
  • the features of the present invention are particularly beneficial when practiced with a blowing agent comprising CFC-I42b, or similar soft chlorofluorocarbon; isobutane, or similar hydrocarbon; or mixtures thereof.
  • Polyolefins suitable for use in the practice of the present invention include homopolymers of ethylene as well as copolymers thereof with other monomers such as propylene, butene-1, 1-octene and other polyolefins, especially ⁇ -polyolefins of carbon atoms,
  • linear low density polyethylene vinyl esters of saturated carboxylic acids such as vinyl acetate and vinyl propionate; alkyl esters of mono- ethylenically unsaturated carboxylic acids such as methyl acrylate or methacrylate, ethyl acrylate or methacrylate, propyl acrylate or methacrylate, the several butyl- and isobutyl acrylate and methacrylates, 2-ethylhexyl acrylate, dimethyl maleate; the various monoethylenically unsaturated carboxylic acids themselves such as, for example, acrylic acid, methacrylic acid, ethacrylic acid, crotonic acid, mesaconic acid, etc.
  • Polymers of particular interest for use herein are polyethylene, linear low density polyethylene, ethylene-vinyl acetate copolymers and ethylene acrylic acid copolymers. Naturally, blends of 2 or more of the above-noted polyolefin can also be suitably employed.
  • a key feature of the present invention resides in the use of a small amount of a glycerol monoester of a C20-24 fatty acid in conjunction with the above-described polyolefin to provide polyolefin foams having, in fresh foam form, improved distortion and stability characteristics at elevated temperatures.
  • a preferred stability control agent is glycerol monobehenate.
  • the glycerol monoester of C20-24 fatty acid may be present in mixture with other fatty acid esters depending on the purity of fatty acid used to manufacture the same.
  • monobehenic acid is a hydrogenated rape seed oil containing by weight about 60 percent C22 fatty acids, 38 percent C- j g fatty acids and 2 percent C g_- j fatty acids.
  • as much as •40 percent by weight of the ester mixture may constitute diesters and 15 percent by weight triacid esters in the mixture.
  • fatty acid monoesters there may also be employed, as auxiliary stability control agents, certain other compounds such as, for example, the higher alkyl amines, the fatty acid esters, the fatty acid amides or N-substituted fatty acids which are described in U.S. Pat. No. -4,21*4,054, U.S. Pat. No. 3,644,230 or U.S. Pat. No. 4,368,276.
  • Such additives may be employed in order to obtain an advantageous balance of both ambient temperature and elevated temperature dimensional stability characteristics in the polyolefin foams prepared therewith.
  • a static dissipation agent may be included in the present composition.
  • antistatic agents include alkyl amines, ethoxylated alkyl amines, and alkenyl amines and quaternary ammonium compounds which surprisingly do not adversely affect the stability control properties of the present compositions.
  • Other additives such as nucleation aids (for example, talcum powder, sodium bicarbonate, calcium silicate, etc.), colorants, antioxidants, etc. may also be included.
  • the above-described fatty acid monoesters are preferably employed in an amount of from 0.15 to 5 weight percent based upon the weight of the polyolefin.
  • the total level of such additives combined will typically not be in excess of 10 weight percent based upon the polyolefin weight and the minimum amount of the compound employed will preferably be an amount sufficient to prevent the fresh foam prepared therewith from shrinking more than 10 percent in volume during prolonged exposure at 66°C.
  • the expanded polyolefin articles of the present invention can be conveniently prepared using conventional extrusion foaming principles by heat plastifying the desired polyolefin resin and incorporating into such heat plastified polymer at elevated temperature and pressure (a) a volatile organic blowing agent and (b) from 0.1 to 10 weight percent (based upon the polyolefin) of the above-discussed fatty acid monoester (or a mixture of such ester with one or more of the above-noted auxiliary stability control agents) to form a flowable gel of an expandable polyolefin composition and thereafter extruding said gel into a zone of lower pressure and temperature to form the desired substantially closed-cell polyolefin foam.
  • the volatile organic blowing agent is compounded into the starting polyolefin resin in proportions suitable to provide the desired degree of expansion in the resulting foamed cellular product, usually up to a 100-fold volume expansion to make products having aged foam densities down to 9.6 kilograms per cubic meter (kg/ ⁇ ).
  • the resulting foam products of this invention will typically have densities in the range of from 9.6 to 160 kg/ ⁇ .
  • the foam products of the invention are of relatively low density (for example, in the range of from 16 to 96 kg/m ⁇ and the practice of such invention is especially beneficial for polyolefin foams having densities in the range of from 16 to 48 kg/ ⁇ .
  • the amount of volatile organic blowing agent employed in preparing polyolefin foams in such density ranges will be in the range of from 0.02 to 0.35 gram mole thereof per 100 grams of the polyolefin employed.
  • the choice of the specific volatile organic blowing agent selected for use in the present invention is not particularly critical. Indeed, it is a particularly beneficial aspect of the instant invention that the use of the above-described fatty acid monoesters (or their mixtures with the above-noted auxiliary stability control agents) facilitates obtainment of low density polyolefin foams having commercially desirable properties (for example, ambient temperature dimensional stability and/or suitable fresh foam elevated temperature distortion characteristics, etc.) with a much broader range of volatile organic blowing agent systems than was heretofore possible.
  • volatile organic blowing agents can suitable be employed in the practice of the present invention either alone or in conjunction with thermally decomposable gas- releasing chemical blowing agents or auxiliary blowing agents such as water, carbon dioxide, etc., though such auxiliary blowing agents are also useful as blowing agents by themselves or as primary blowing agents.
  • auxiliary blowing agents are also useful as blowing agents by themselves or as primary blowing agents.
  • volatile organic blowing agents are employed which have an atmospheric boiling point below the melting point of the polyolefin employed.
  • suitable such volatile blowing agents include halogenated hydrocarbon compounds having from 1 to 4 carbon atoms (for example, trichlorofluoromethane, dichlorodifluoromethane, dichlorofluoromethane, chlorodifluoromethane, 1, 1 ,2-tri-chlorotrifluoroethane, 1 ,2-dichlorotetrafluoroethane, 1 , 1-dichloro-2,2,2 trifluoroethane, 1 , 1-dichloro-1-fluoroethane, 1-chloro- 1 ,2,2,2-tetrafluoroethane 1-chloro-1 , 1-difluoroethene 1 , 1 , 1,2-tetrafluoroethane, 1 , 1-difluoroethane, ethyl chloride, methyl chloride, methylene chloride, etc.) as well as volatile non-halogenated hydrocarbon compounds such as propane, butane, isot
  • mixtures of two or more of the foregoing blowing agents can also be suitably employed and, indeed, an especially preferred embodiment of the present invention involves the use of a mixed blowing agent system comprising from 40 to 90 weight percent of 1-chloro-1 , 1-difluoroethane and from 60 to 10 weight percent of ethyl chloride, both weight percentages being based upon the total weight of such mixed blowing agent system.
  • the blowing agent is compounded into the starting polyolefin in conventional fashion to make a flowable gel, preferably in a continuous manner, for example, in a mixing extruder, using heat to plastify the normally solid polymer, pressure to maintain the blowing agent in non-gaseous state, and mechanical working to obtain a thorough mixing of the polymer and blowing agent.
  • the resulting gel is then cooled if necessary and passed through a suitable die orifice into a zone of lower pressure, for example, normal ambient air pressure, where it expands to a lower density, cellular mass.
  • a suitable die orifice for example, normal ambient air pressure
  • the resulting polyolefin foam is comprised of substantially closed-cell structure and, even at low densities, that is, from 16 to 48 kg/m ⁇ and when in fresh foam form, is remarkably stable in dimension at ambient temperature as well as upon exposure to elevated temperatures.
  • the dimensional stability of the extrusion foamed products is measured by observing the changes in volume occurring in test specimens of the foam as a function of time of exposure under the environmental circumstances of concern.
  • the test specimens are obtained by quickly cutting, from the extrusion foamed product soon, for example, within about fifteen minutes, after emerging from the extrusion die orifice, test pieces of the desired dimensions (conveniently, samples 13 cm long, 1.3 em thick and 2.5 cm wide can be suitably employed) and accurately measuring their overall volume, for example, by cubic displacement of water.
  • the initial volume of each specimen is arbitrarily selected as the benchmark volume for the subsequent dimensional stability study.
  • the individual foam specimens are exposed to air at atmospheric pressure and ordinary room temperature (for example, 23°C) and their volumes are measured periodically to determine the minimum volume to which they shrink during the ambient temperature curing process (that is, "curing” referring to the phenomenon in which the gaseous blowing agent within the foam cells is gradually diffusing out thereof and during which air is gradually diffusing in to replace the escaping blowing agent).
  • curing referring to the phenomenon in which the gaseous blowing agent within the foam cells is gradually diffusing out thereof and during which air is gradually diffusing in to replace the escaping blowing agent.
  • elevated temperature dimensional stability performance evaluation the above-described ambient temperature procedures are followed except that the specimen is exposed to atmospheric pressure air at elevated temperatures rather than at ambient temperature.
  • the polymer foams of the present invention preferably do not shrink by more than 20 percent and more preferably not more than from 15 percent from their original volume (measured 5 minutes after extrusion) after two weeks of aging under either ambient (for example, 23°C) or elevated temperature (ambient to 160°C) test conditions.
  • test methods include measuring both the surface resistivity (ASTM D-257) and static decay time (Federal Test Standard 101C Method 4046.1).
  • the equipment used in this example is a 1" screw type extruder having additional zones for mixing and cooling at the end of sequential zones for feeding, metering and mixing.
  • An opening for blowing agent addition is provided on the extruder barrel between the metering and mixing zones.
  • a die orifice having an opening of rectangular shape.
  • the height of the opening, hereinafter call die gap, is adjustable while its width is fixed at 3.68 mm.
  • One hundred parts of granular low density polyethylene (2.1 melt index, 0.923 g/cc density, was uniformly blended with 2.0 parts of glycerol mono- behenate (Kemaster 6500, Humko Chemcial Div.) in concentrate form and 0.25 parts of talcum powder.
  • the blend was fed into the extruder at a uniform rate of approximately 6 pounds per hour (2.7 kg/hr).
  • the temperatures maintained at the extruder zones were 95°C at the feeding zone, 150°C at the melting zone, 1 ⁇ 0°C at the metering zone and 200°C at the mixing zone.
  • CFC-I42b 1-chloro-1 , 1-difluoroethane
  • the temperature of the cooling zone was maintained so that the polymer/blowing agent mixture could reach an optimum foaming temperature which was in the range of 106°C ⁇ 1°C.
  • the die gap was adjusted in each test to provide a foam strand having smooth skin.
  • foam samples for determination of foam dimensional stability.
  • the foam strands were of oval shape with approximately 1.1 cm x 1.6 cm dimensions and cell sizes ranging from about 0.45 mm to 0.85 mm. From the strand, four 12.7 cm long pieces of foam specimens were cut out and their initial weight and volume were measured within about 5 minutes. Two pieces were aged at ambient temperature and one piece each at 54°C and 71°C, respectively. The weight and volume of the foam specimens were periodically determined, hourly for the first 6 hours and daily for the first week and then weekly.
  • the comparative samples were prepared in a similar manner excepting that no stability control agent was added to the polymer melt.
  • glycerol monobehenate provides foam dimensional stability at temperatures as high as 71°C.
  • Example 1 The same apparatus, temperature settings, polymer type, stability control agent amount, talc level and solid feed rate as used in Example 1 were employed in the tests of this example.
  • Run 3 1 percent by weight of an alkyl amine type antistatic agent (Atmer 163 made by ICI Americas) was included.
  • the blowing agent was selected from CFC-I42b or its mixture (55/45 mole ratio) with ethyl chloride (Run 4). The blowing agent was fed at a uniform rate of approximately 0.15 gram moles per 100 grams of polymer throughout the tests of this example. Die openings, foam cross-section sizes and cell sizes fell approximately in the same ranges as for the tests of Example 1.
  • Atmer 163 brand antistatic agent an alkyl amine type made by ICI Americas Inc.
  • Substantially the same resin blend as employed 5 in Example 1 is extruded and foamed by means of a 1 1/2" screw type extruder having essentially the same configuration as the equipment used in Example 1 operating at substantially the same extrusion conditions. There is attached a die orifice having a rectangular opening of 6.35 mm x 1.27 mm.
  • glycerol monobehenate a mixture of sodium bicarbonate and citric acid in polyethylene, Hydrocerol ® CF-20, available from Berlinger Ingelheim.
  • the blend was fed into the extruder at a uniform rate of 4.5 kilograms per hour.
  • Isobutane was injected into the extruder at a rate of 0.84 pounds 3.8 kilograms per hour.
  • foaming gel temperature 110°C, there was achieved a good quality foam having 33 kg/ ⁇ density, 1.5 mm cell size and 1 cm x 3.2 cm cross-section. From the foam strand, 10 cm long pieces were cut and subjected to similar dimensional stability tests as in the Example 1.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Emergency Medicine (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
PCT/US1991/000743 1990-02-26 1991-02-04 Polyolefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom WO1991013115A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
FI923756A FI923756L (fi) 1990-02-26 1991-02-04 Polyolefinkompositioner som omfattar glycerolmonoestrar av c20-24-fettsyror och daerav framstaellda skumprodukter
CA002076872A CA2076872C (en) 1990-02-26 1991-02-04 Polyolefin compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom
EP91904592A EP0517748B1 (en) 1990-02-26 1991-02-04 Polyolefin polymer compositions comprising glycerol monoesters of c 20-24 fatty acids and foamed articles prepared therefrom
BR919106085A BR9106085A (pt) 1990-02-26 1991-02-04 Composicoes de poliolefina que compreendem monoesteres de glicerol de acidos graxos de c20-24 e artigos em espuma preparadas a partir delas
KR1019920702033A KR100198043B1 (ko) 1990-02-26 1991-02-04 C20-24 지방산의 글리세롤 모노에스테르를 포함하는 폴리오레핀 조성물 및 이로부터 제조된 발포체
DE69123734T DE69123734T2 (de) 1990-02-26 1991-02-04 Glycerin-monoester von c20-24-fettsäuren umfassende polyolefin-polymerzusammensetzungen und geschäumte artikel daraus

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US07/484,745 US5089533A (en) 1990-02-26 1990-02-26 Olefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom
US484,745 1990-02-26

Publications (1)

Publication Number Publication Date
WO1991013115A1 true WO1991013115A1 (en) 1991-09-05

Family

ID=23925428

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1991/000743 WO1991013115A1 (en) 1990-02-26 1991-02-04 Polyolefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom

Country Status (11)

Country Link
US (1) US5089533A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
EP (1) EP0517748B1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
JP (1) JP3198334B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
KR (1) KR100198043B1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
BR (1) BR9106085A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
CA (1) CA2076872C (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
DE (1) DE69123734T2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
FI (1) FI923756L (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
HU (1) HU212810B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
TW (1) TW249813B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)
WO (1) WO1991013115A1 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5225451A (en) * 1992-08-27 1993-07-06 Astro-Valcour, Inc. Ultra low density polyolefin foam, foamable polyolefin compositions and process for making same
US5290822A (en) * 1992-08-27 1994-03-01 Astro-Valcour, Inc. Ultra low density polyolefin foam, foamable polyolefin compositions and process for making same
US5895614A (en) * 1995-08-22 1999-04-20 Tenneco Protective Packaging Inc. Method of forming a microcellular foam plank
US6245823B1 (en) * 1995-10-20 2001-06-12 Free-Flow Packaging International, Inc. Composition and blowing agent for making foamed polyethylene material
RU2174991C2 (ru) * 1996-02-01 2001-10-20 Деннис А. Кнаус Вспениваемая полиолефиновая композиция (варианты), композиция стабилизирующего реагента для пенополиолефинов, изделие из вспененного полиолефина и способ приготовления пенополиолефина
US5776389A (en) * 1996-06-20 1998-07-07 The Dow Chemical Company Process for making an alkenyl aromatic polymer foam having enlarged cell size
KR19980025674A (ko) * 1996-10-04 1998-07-15 김인환 고대전방지성 폴리프로필렌의 제조방법
US6225363B1 (en) 1998-04-07 2001-05-01 Pactiv Corporation Foamable composition using high density polyethylene
US6114025A (en) * 1998-06-15 2000-09-05 Tenneco Protective Packaging, Inc. Foam and film/foam laminates using linear low density polyethylene
US6582817B2 (en) 1999-11-19 2003-06-24 Wellman, Inc. Nonwoven fabrics formed from polyethylene glycol modified polyester fibers and method for making the same
US6454982B1 (en) 1999-11-19 2002-09-24 Wellman, Inc. Method of preparing polyethylene glycol modified polyester filaments
US6623853B2 (en) 1998-08-28 2003-09-23 Wellman, Inc. Polyethylene glycol modified polyester fibers and method for making the same
US6509091B2 (en) 1999-11-19 2003-01-21 Wellman, Inc. Polyethylene glycol modified polyester fibers
US6583190B2 (en) 2000-12-27 2003-06-24 Sealed Air Corporation (U.S.) Expandable composition, blowing agent, and process for extruded thermoplastic foams
US7045556B2 (en) * 2002-07-02 2006-05-16 Pactiv Corporation Polyolefin foams made with isopentane-based blowing agents
GB2395948A (en) * 2002-12-06 2004-06-09 Pactiv Europ B V Polyolefin foam
US7166248B2 (en) * 2003-01-03 2007-01-23 Pactiv Corporation Reduced VOC emission alkenyl aromatic polymer foams and processes
US7358282B2 (en) 2003-12-05 2008-04-15 Kimberly-Clark Worldwide, Inc. Low-density, open-cell, soft, flexible, thermoplastic, absorbent foam and method of making foam
US7291382B2 (en) 2004-09-24 2007-11-06 Kimberly-Clark Worldwide, Inc. Low density flexible resilient absorbent open-cell thermoplastic foam
US8158689B2 (en) 2005-12-22 2012-04-17 Kimberly-Clark Worldwide, Inc. Hybrid absorbent foam and articles containing it
KR100830093B1 (ko) 2007-02-23 2008-05-19 한국과학기술연구원 우수한 성형성을 갖는 폴리올레핀계 발포 입자의 제조방법
US7858681B2 (en) * 2007-08-21 2010-12-28 E. I. Du Pont De Nemours And Company Product comprising ionomer and plasticizer
US8648122B2 (en) * 2011-12-01 2014-02-11 Sealed Air Corporation (Us) Method of foaming polyolefin using acrylated epoxidized fatty acid and foam produced therefrom

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3644230A (en) * 1968-02-19 1972-02-22 Haskon Inc Extrusion process for polyolefin foam

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5481370A (en) * 1977-12-13 1979-06-28 Japan Styrene Paper Corp Method of making polyolefin foam
US4663361A (en) * 1985-12-24 1987-05-05 The Dow Chemical Company Expandable polyolefin compositions and preparation process utilizing isobutane blowing agent

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3644230A (en) * 1968-02-19 1972-02-22 Haskon Inc Extrusion process for polyolefin foam

Also Published As

Publication number Publication date
CA2076872C (en) 2002-09-03
EP0517748A4 (en) 1992-10-05
HUT62627A (en) 1993-05-28
KR100198043B1 (ko) 1999-06-15
FI923756A0 (fi) 1992-08-20
HU9202747D0 (en) 1992-12-28
EP0517748A1 (en) 1992-12-16
TW249813B (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) 1995-06-21
JP3198334B2 (ja) 2001-08-13
DE69123734D1 (de) 1997-01-30
HU212810B (en) 1996-11-28
FI923756A7 (fi) 1992-08-20
FI923756L (fi) 1992-08-20
DE69123734T2 (de) 1997-06-19
JPH05503545A (ja) 1993-06-10
US5089533A (en) 1992-02-18
KR927003704A (ko) 1992-12-18
CA2076872A1 (en) 1991-08-27
EP0517748B1 (en) 1996-12-18
BR9106085A (pt) 1993-02-02

Similar Documents

Publication Publication Date Title
US5089533A (en) Olefin polymer compositions comprising glycerol monoesters of c20-24 fatty acids and foamed articles prepared therefrom
AU594976B2 (en) Expandable polyolefin compositions and preparation process utilizing isobutane blowing agent
US4368276A (en) Novel olefin polymer compositions and foamed articles prepared therefrom having improved elevated temperature dimensional stability
US4694027A (en) Expandable polyolefin compositions and preparation process utilizing isobutane blowing agent
US4528300A (en) Process for producing dimensionally stable polyolefin foams using environmentally acceptable blowing agent systems
EP0041167B2 (en) Expandable polyolefin compositions and polyolefin foam preparation process
US4395510A (en) Novel olefin polymer compositions and foamed articles prepared therefrom having improved elevated temperature dimensional stability
EP0036560B1 (en) Foamable olefin polymer compositions stabilized with n-alkyl substituted amides, foaming process using them and foam article produced
EP0036562A2 (en) Foamable olefin polymer compositions stabilized with certain higher ethers, esters or anhydrides, foaming process using them and foam article produced
US4275168A (en) Polyolefin resin foam and process for continuously manufacturing the same
EP0219548B1 (en) Polyolefin foam compositions having improved dimensional stability utilizing certain unsaturated nitrogen-containing compounds andprocess for making same
US5405883A (en) Ethylene polymer foams blown with isobutane and 1,1-difluoroethane and a process for making
WO1987004445A1 (en) Expandable polyolefin compositions and polyolefin foam preparation process
EP0041234B1 (en) Novel olefin polymer compositions and foamed articles prepared therefrom having improved elevated temperature dimensional stability
KR850000112B1 (ko) 지방족 올레핀 중합체의 발포방법
KR840001491B1 (ko) 발포성 합성수지의 제조방법
JPS6245255B2 (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html)

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): BR CA FI HU JP KR

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB GR IT LU NL SE

CFP Corrected version of a pamphlet front page
CR1 Correction of entry in section i

Free format text: IN PAT.BUL.21/91,UNDER INID (54) TITLE REPLACE THE EXISTING TEXT BY "POLYOLEFIN COMPOSITIONS COMPRISING GLYCEROL MONOESTERS OF C20-24 FATTY ACIDS AND FOAMED ARTICLES PREPARED THEREFROM"

WWE Wipo information: entry into national phase

Ref document number: 1991904592

Country of ref document: EP

Ref document number: 923756

Country of ref document: FI

WWE Wipo information: entry into national phase

Ref document number: 2076872

Country of ref document: CA

WWP Wipo information: published in national office

Ref document number: 1991904592

Country of ref document: EP

WWG Wipo information: grant in national office

Ref document number: 1991904592

Country of ref document: EP