Patent Application
20210269611
Various embodiments of the present disclosure relate to articles of manufacture comprising an extrusion-foamed polymeric composition. Other aspects concern processes for extrusion foaming polymeric compounds.
One embodiment is an article of manufacture, comprising:
Another embodiment is a method of making an extrusion-foamed polymer composition, the method comprising:
As noted above, various embodiments of the present disclosure concern an extrusion-foamed polymeric composition comprising an ethylene-based polymer and an olefin-based elastomer. The extrusion-foamed polymeric composition is prepared by an extrusion foaming process from a foamable polymeric composition comprising the ethylene-based polymer, the olefin-based elastomer, a nucleating agent, and a blowing agent. Optionally, the foamable polymeric composition and the resulting extrusion-foamed polymeric composition may contain one or more additives.
As noted above, one component of the extrusion-foamed polymeric compositions described herein is an ethylene-based polymer. As used herein, “ethylene-based” polymers are polymers prepared from ethylene monomers as the primary (i.e., greater than 50 weight percent (“wt %”)) monomer component, though other co-monomers may also be employed. “Polymer” means a macromolecular compound prepared by reacting (i.e., polymerizing) monomers of the same or different type, and includes homopolymers and interpolymers. “Interpolymer” means a polymer prepared by the polymerization of at least two different monomer types. This generic term includes copolymers (usually employed to refer to polymers prepared from two different monomer types), and polymers prepared from more than two different monomer types (e.g., terpolymers (three different monomer types) and quaterpolymers (four different monomer types)).
In various embodiments, the ethylene-based polymer can be an ethylene homopolymer. As used herein, “homopolymer” denotes a polymer comprising repeating units derived from a single monomer type, but does not exclude residual amounts of other components used in preparing the homopolymer, such as chain transfer agents.
In one or more embodiments, the ethylene-based polymer can be an ethylene/alpha-olefin (“a olefin”) interpolymer having an α-olefin content of at least 1 wt %, at least 5 wt %, at least 10 wt %, at least 15 wt %, at least 20 wt %, or at least 25 wt %/o based on the entire interpolymer weight. These interpolymers can have an α-olefin content of less than 50 wt %, less than 45 wt %, less than 40 wt %, or less than 35 wt % based on the entire interpolymer weight. When an α-olefin is employed, the α-olefin can be a C3-20 (i.e., having 3 to 20 carbon atoms) linear, branched or cyclic α-olefin. Examples of C3-20 α-olefins include propene, 1 butene, 4-methyl-1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, and 1-octadecene. The α-olefins can also have a cyclic structure such as cyclohexane or cyclopentane, resulting in an α-olefin such as 3 cyclohexyl-1-propene (allyl cyclohexane) and vinyl cyclohexane. Illustrative ethylene/α-olefin interpolymers include ethylene/propylene, ethylene/1-butene, ethylene/1-hexene, ethylene/1-octene, ethylene/propylene/1-octene, ethylene/propylene/1-butene, and ethylene/1-butene/1-octene.
In various embodiments, the ethylene-based polymer can be used alone or in combination with one or more other types of ethylene-based polymers (e.g., a blend of two or more ethylene-based polymers that differ from one another by monomer composition and content, catalytic method of preparation, etc). If a blend of ethylene-based polymers is employed, the polymers can be blended by any in-reactor or post-reactor process.
In an embodiment, the ethylene-based polymer can be a low-density polyethylene (“LDPE”). LDPEs are generally highly branched ethylene homopolymers, and can be prepared via high pressure processes (i.e., HP-LDPE). LDPEs suitable for use herein can have a density ranging from 0.91 to 0.94 g/cm3. In various embodiments, the ethylene-based polymer is a high-pressure LDPE having a density of at least 0.91 g/cm3, but less than 0.94 g/cm3, or less than 0.93 g/cm3. Polymer densities provided herein are determined according to ASTM International (“ASTM”) method D792. LDPEs suitable for use herein can have a melt index (I2) of less than 20 g/10 min., or ranging from 0.1 to 10 g/10 min., from 0.5 to 5 g/10 min., from 1 to 3 g/10 min., or an I2 of 2 g/10 min. Melt indices provided herein are determined according to ASTM method D1238. Unless otherwise noted, melt indices are determined at 190° C. and 2.16 Kg (i.e., I2). Generally, LDPEs have a broad molecular weight distribution (“MWD”) resulting in a relatively high polydispersity index (“PDI;” ratio of weight-average molecular weight to number-average molecular weight).
In an embodiment, the ethylene-based polymer can be a linear-low-density polyethylene (“LLDPE”). LLDPEs are generally ethylene-based polymers having a heterogeneous distribution of comonomer (e.g., α-olefin monomer), and are characterized by short-chain branching. For example, LLDPEs can be copolymers of ethylene and α-olefin monomers, such as those described above. LLDPEs suitable for use herein can have a density ranging from 0.916 to 0.925 g/cm3. LLDPEs suitable for use herein can have a melt index (I2) ranging from 1 to 20 g/10 min., or from 3 to 8 g/10 min.
Production processes used for preparing ethylene-based polymers are wide, varied, and known in the art. Any conventional or hereafter discovered production process for producing ethylene-based polymers having the properties described above may be employed for preparing the ethylene-based polymers described herein. In general, polymerization can be accomplished at conditions known in the art for Ziegler-Natta or Kaminsky-Sinn type polymerization reactions, that is, at temperatures from 0 to 250° C., or 30 or 200° C., and pressures from atmospheric to 10,000 atmospheres (1,013 megaPascal (“MPa”)). In most polymerization reactions, the molar ratio of catalyst to polymerizable compounds employed is from 10-12:1 to 10-1:1, or from 10-9:1 to 10-5:1.
In one or more embodiments, the ethylene-based polymer is a low-density polyethylene homopolymer having a density of at least 0.91 g/cm3, or in the range of from 0.91 to 0.93 g/cm3, from 0.915 to 0.925 g/cm3, or of about 0.92 g/cm3. Additionally, the low-density polyethylene can have a melt index (I2) in the range of from 0.1 to 10 g/10 min., from 0.2 to 9 g/10 min., or from 0.25 to 8 g/10 min.
Examples of suitable commercially available ethylene-based polymers include, but are not limited to, DOW™ LDPE 1321, commercially available from The Dow Chemical Company, Midland, Mich., USA, DOW AXELERON™ CX 1253 NT CPD, commercially available from The Dow Chemical Company, Midland, Mich., USA, and DOW AXELERON™ CX 1258 NT CPD, commercially available from The Dow Chemical Company, Midland, Mich., USA.
As noted above, the extrusion-foamed polymeric composition comprises an olefin-based elastomer. Olefin-based elastomers include both polyolefin homopolymers and interpolymers. Examples of polyolefin interpolymers are ethylene/α-olefin interpolymers and propylene/α-olefin interpolymers. In such embodiments, the α-olefin can be a C3-20 linear, branched or cyclic α-olefin (for the propylene/α-olefin interpolymers, ethylene is considered an α-olefin). Examples of C3-20 α-olefins include propene, 1-butene, 4-methyl-1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, and 1-octadecene. The α-olefins can also contain a cyclic structure such as cyclohexane or cyclopentane, resulting in an α-olefin such as 3-cyclohexyl-1-propene (allyl cyclohexane) and vinyl cyclohexane. Although not α-olefins in the classical sense of the term, for purposes of this invention certain cyclic olefins, such as norbornene and related olefins, are α-olefins and can be used in place of some or all of the α-olefins described above. Similarly, styrene and its related olefins (for example, α-methylstyrene, etc.) are α-olefins for purposes of this disclosure. Illustrative polyolefin copolymers include ethylene/propylene, ethylene/butene, ethylene/1-hexene, ethylene/1-octene, ethylene/styrene, and the like. Illustrative terpolymers include ethylene/propylene/1-octene, ethylene/propylene/butene, ethylene/butene/1-octene, and ethylene/butene/styrene. The interpolymers can be random or blocky.
Olefin-based elastomers can also comprise one or more functional groups such as an unsaturated ester or acid or silane, and these elastomers are well known and can be prepared by conventional high-pressure techniques. The unsaturated esters can be alkyl acrylates, alkyl methacrylates, or vinyl carboxylates. The alkyl groups can have 1 to 8 carbon atoms and preferably have 1 to 4 carbon atoms. The carboxylate groups can have 2 to 8 carbon atoms and preferably have 2 to 5 carbon atoms. The portion of the copolymer attributed to the ester comonomer can be in the range of 1 up to 50 percent by weight based on the weight of the copolymer. Examples of the acrylates and methacrylates are ethyl acrylate, methyl acrylate, methyl methacrylate, t-butyl acrylate, n-butyl acrylate, n-butyl methacrylate, and 2-ethylhexyl acrylate. Examples of the vinyl carboxylates are vinyl acetate, vinyl propionate, and vinyl butanoate. Examples of the unsaturated acids include acrylic acids or maleic acids. One example of an unsaturated silane is vinyl trialkoxysilane.
Functional groups can also be included in the olefin-based elastomer through grafting which can be accomplished as is commonly known in the art. In one embodiment, grafting may occur by way of free radical functionalization which typically includes melt blending an olefin polymer, a free radical initiator (such as a peroxide or the like), and a compound containing a functional group. During melt blending, the free radical initiator reacts (reactive melt blending) with the olefin polymer to form polymer radicals. The compound containing a functional group bonds to the backbone of the polymer radicals to form a functionalized polymer. Exemplary compounds containing functional groups include but are not limited to alkoxysilanes, e.g., vinyl trimethoxysilane, vinyl triethoxysilane, and vinyl carboxylic acids and anhydrides. e.g., maleic anhydride.
Olefin-based elastomers suitable for use herein have a density of less than 0.91 g/cm3, or in the range of from 0.85 to 0.90 g/cm3, from 0.85 to 0.88 g/cm3, or from 0.855 to 0.875 g/cm3. Additionally, the olefin-based elastomers can have a melt index (I2) in the range of from 0.5 to 10 g/10 min., or from 0.7 to 5.0 g/10 min.
More specific examples of the olefin-based elastomers useful herein include very-low-density polyethylene (“VLDPE”) (e.g., FLEXOMER™ ethylene/1-hexene polyethylene made by The Dow Chemical Company), homogeneously branched, linear ethylene/α-olefin copolymers (e.g. TAFMER™ by Mitsui Petrochemicals Company Limited and EXACT™ by Exxon Chemical Company), and homogeneously branched, substantially linear ethylene/α-olefin polymers (e.g., AFFINITY™ and ENGAGE™ polyethylene available from The Dow Chemical Company). Specific examples of ENGAGE™ elastomers suitable for use include, but are not limited to, ENGAGE™ 8207, ENGAGE™ 7447, and ENGAGE™ 8842, all available from The Dow Chemical Company.
The olefin-based elastomers useful herein also include propylene, butene, and other alkene-based copolymers, e.g., copolymers comprising a majority of units derived from propylene and a minority of units derived from another α-olefin (including ethylene). Exemplary propylene polymers useful herein include VERSIFY™ polymers available from The Dow Chemical Company, and VISTAMAXX™ polymers available from ExxonMobil Chemical Company.
Olefin-based elastomers can also include ethylene-propylene-diene monomer (“EPDM”) elastomers and chlorinated polyethylenes (“CPE”). Commercial examples of suitable EPDMs include NORDEL™ EPDMs, available from The Dow Chemical Company. A specific example of an EPDM suitable for use is NORDEL™ IP 3722P EL, available from The Dow Chemical Company.
Other suitable olefin-based elastomers include olefin block copolymers (such as those commercially available under the trade name INFUSE™ from The Dow Chemical Company, Midland, Mich., USA), mesophase-separated olefin multi-block interpolymers (such as described in U.S. Pat. No. 7,947,793), and olefin block composites (such as those described in U.S. Pat. Nos. 8,822,598, 8,686,087, and 8,716,400; and PCT Published Application Nos. WO 2017/044547 and WO 2014/043522).
An example of a commercially available olefin block copolymer suitable for use herein includes, but is not limited to, INFUSE™ 9107, available from The Dow Chemical Company, Midland, Mich., USA.
As noted above, the extrusion-foamed polymeric composition can be prepared from a foamable polymeric composition containing a nucleating agent. A “nucleator” or “nucleating agent” is a substance, typically a small particle, that provides a nucleation site or location for bubble formation within a polymer melt. Nucleating agents are used to enhance the cell structure of foamed polymers. Non-limiting examples of suitable nucleating agents include fluororesins, boron nitride, alumina, silica, poly(4-methyl pentene), zirconia, talc, azodicarbonamide (“ADCA”), and 4,4′-oxybisbenzenesulfonylhydrazide (“OBSH”). In an embodiment, the nucleating agent is selected from a fluororesin, boron nitride, ADCA, silica, poly(4-methyl pentene), and combinations or two or more thereof. In various embodiments, the nucleating agent is ADCA.
The fluororesin may be various polymers inclusive of a homopolymer and a copolymer of fluorine-containing monomers. Non-limiting examples of suitable fluororesins include polytetrafluoroethylene (“PTFE”), tetrafluoroethylene-perfluoroalkyl vinyl ether copolymer (“PFA”), ethylene tetrafluoroethylene copolymer (“ETFE”), tetrafluoroethylene-hexafluoropropylene copolymer (“FEP”), tetrafluoroethylene-ethylene copolymer, polyvinylidene fluoride (“PVdF”), polychlorotrifluoroethylene (“PCTFE”), chlorotrifluoroethylene-ethylene copolymer (“ECTFE”), and the like. In an embodiment, the nucleating agent is a fluororesin selected from PTFE, PFA, ETFE, and combinations thereof. In another embodiment, the nucleating agent is PTFE.
In various embodiments, the nucleating agent can be incorporated into the foamable polymeric composition as a nucleating masterbatch that includes the nucleating agent and a polymeric component (e.g., LDPE). An example of a commercial nucleating masterbatch includes AXELERON™ CX A-0012 NT CPD, available from The Dow Chemical Company, Midland, Mich., USA.
In an embodiment, extrusion-foamed polymeric composition is prepared using a blowing agent. The blowing agent is one or more suitable for the extrusion temperature, foaming conditions, foam forming method, and the like. Suitable blowing agents include, for example, an inert gas such as nitrogen, a carbon gas (e.g., CO, CO2, etc.), helium, argon, and the like; hydrocarbon such as methane, propane, butane, pentane, and the like; and halogenated hydrocarbons such as dichlorodifluoromethane, dichloromonofluoromethane, monochlorodifluoromethane, trichloromonofluoromethane, monochloropentafluoroethane, trichlorotrifluoroethane, and the like.
In an embodiment, the extrusion-foamed polymeric composition includes one or more additives. Representative additives include but are not limited to, processing aids, lubricants, stabilizers (antioxidants), foaming aids, surfactants, flow aids, viscosity control agents, coloring agents, copper inhibitors and the like. These additives can be added to the ethylene-based polymer and olefin-based elastomer either before or during processing. The amount of any particular additive in the composition is typically from 0.01 to 1 wt %, more typically from 0.01 to 0.5 wt % and even more typically from 0.01 to 0.3 wt %, and the total amount of additives in the composition, if present at all, is typically from 0.01 to 5 wt %, more typically from 0.01 to 2 wt % and even more typically from 0.01 to 1 wt %, based on the total weight of the composition.
As noted above, the extrusion-foamed polymeric composition can be prepared from a foamable polymeric composition containing the ethylene-based polymer, the olefin-based elastomer, the nucleating agent, the blowing agent, and optionally one or more additives.
The foamable polymeric composition, as well as the extrusion-foamed polymeric composition, can contain the ethylene-based polymer in an amount ranging from 10 to 90 wt %, from 20 to 80 wt %, or from 30 to 70 wt %, based on the entire weight of the foamable polymeric composition or the extrusion-foamed polymeric composition, respectively. In some embodiments, the ethylene-based polymer can be present in the foamable polymeric composition, as well as the extrusion-foamed polymeric composition, in an amount ranging from 30 to 50 wt %, based on the entire weight of the foamable polymeric composition or extrusion-foamed polymeric composition, respectively.
The foamable polymeric composition, as well as the extrusion-foamed polymeric composition, can contain the olefin-based elastomer in an amount ranging from 10 to 90 wt %, from 20 to 80 wt %, or from 30 to 70 wt %, based on the entire weight of the foamable polymeric composition or the extrusion-foamed polymeric composition, respectively. In some embodiments, the olefin-based elastomer can be present in the foamable polymeric composition, as well as the extrusion-foamed polymeric composition, in an amount ranging from 50 to 70 wt %, based on the entire weight of the foamable polymeric composition or extrusion-foamed polymeric composition, respectively.
The combined weight of the ethylene-based polymer and the olefin-based elastomer can constitute at least 50, at least 55, at least 60, at least 65, at least 70, at least 75, at least 80, at least 85, at least 90, or at least 95 wt % of the entire foamable polymeric composition or the extrusion-foamed polymeric composition, respectively.
In various embodiments, the ethylene-based polymer and olefin-based elastomer can be present in the foamable polymeric composition, and the extrusion-foamed polymeric composition, in a weight ratio (ethylene-based polymer to olefin-based elastomer) ranging from 9:1 to 1:9, from 4:1 to 1:4, or from 7:3 to 3:7. In other embodiments, the ethylene-based polymer and olefin-based elastomer can be present in the foamable polymeric composition, and the extrusion-foamed polymeric composition, in a weight ratio (ethylene-based polymer to olefin-based elastomer) in the range of from 1:1 to 3:7.
The foamable polymeric composition can contain the nucleating agent in an amount ranging from 0.05 to 1 wt %, from 0.1 to 0.5 wt %, or from 0.2 to 0.4 wt % based on the entire weight of the foamable polymeric composition. If present as a masterbatch, the foamable polymeric composition can contain the nucleating masterbatch in an amount ranging from 0.5 to 10 wt %, from 1 to 5 wt %, or from 2 to 4 wt %, based on the total weight of the foamable polymeric composition.
The foamable polymeric composition can be prepared by any methods known or hereafter discovered in the art. For instance, the ethylene-based polymer and the olefin-based elastomer can be pre-blended, which can be accomplished, for example, by extruder, BUSS™ kneader, and the like. The nucleating agent can be compounded simultaneously while making the pre-blend, or may be added during the extrusion foaming process. The nucleator can be added neat, in combination with one or more other additives, e.g., antioxidant, cell stabilizer, etc., or as part of a masterbatch. In various embodiments, the nucleating agent can be mixed with the ethylene-based polymer and olefin-based elastomer to achieve an essentially homogeneous dispersion of nucleating agent in the polymer blend and to this end, batch mixing, e.g., through the use of a BUSS™ kneader, is typically preferred to mixing in an extruder. If the nucleator is first mixed with the ethylene-based polymer and olefin-based elastomer in an extruder, then it is typically added prior to injection of the blowing agent for foaming.
The amount of blowing agent to be used can vary. In an embodiment, the blowing agent is present in an amount of 0.0014.1 part by weight, or 0.0050.05 part by weight, per 100 parts by weight of the foamable polymer composition. The blowing agent may be mixed prior to extrusion or may be supplied into an extruder from a blowing agent supply opening formed on the barrel of the extruder.
The foamable composition can be foamed via extrusion foaming using any known or hereafter discovered extrusion foaming methods. In various embodiments, the extrusion foaming process can be performed at a rate of at least 1 meter per minute (“m/min.”), or at least 1.25 m/min. Extrusion speed can vary depending on the application, process, and thickness of the desired foamed product. In various embodiments, the extrusion foaming process can be performed at rates of up to 1,000 m/min. or more.
By way of non-limiting example, the extrusion foaming process of the present disclosure can be conducted using a single-screw extruder equipped with a gas injection system. The polymer(s) and nucleating agent masterbatch are first fed to the extruder. The gas (blowing agent) can be injected into the middle section along the length of the extruder. The polymer melt and injected gas (blowing agent) first co-exist as two separate phases. When the melt passes through the extruder, subsequent mixing occurs to dissolve the gas (blowing agent) into the melt. A static mixer can be employed toward the end of the extruder to attain a homogeneous temperature and melt flow. Before being discharged from the die, the melt is cooled to a suitable temperature for foaming. Examples of foaming extrusion equipment include a single screw extruder as described above or two single screw extruders in tandem where the first extruder is used to melt the polymer with gas injection at the end prior to entering the second extruder to distribute and cool the melt.
The resulting extrusion-foamed polymeric composition can have foaming ratio of at least 20 percent, or at least 22 percent. The “foaming ratio” of the extrusion-foamed polymeric composition is determined by the following equation:
In various embodiments, the extrusion-foamed polymeric composition can have a foaming ratio in the range of from 10 to 60 percent, or in the range of from 22 to 57 percent.
The extrusion-foamed polymeric composition can have a DMA storage modulus at 0° C. of less than 130 MPa, less than 100 MPa, or less than 75 MPa. DMA storage modulus is determined according to the procedure provided for in the Test Methods section, below. In various embodiments, the extrusion-foamed polymeric composition can have a DMA storage modulus at 0° C. in the range of from 10 to 130 MPa, from 15 to 100 MPa, or from 20 to 75 MPa.
The extrusion-foamed polymeric composition can have a DMA storage modulus at 23° C. of less than 71 MPa, less than 60 MPa, less than 50 MPa, or less than 41 MPa. In various embodiments, the extrusion-foamed polymeric composition can have a DMA storage modulus at 23° C. in the range of from 10 to 71 MPa, from 15 to 50 MPa, or from 16 to 41 MPa.
In various embodiments, the extrusion-foamed polymeric composition can have a DMA storage modulus at 23° C. that is at least 25 percent less, at least 30 percent less, at least 35 percent less, at least 40 percent less, at least 45 percent less, or at least 50 percent less than the DMA storage modulus at 23° C. of a non-foamed, but otherwise identical, polymeric composition.
The extrusion-foamed polymeric composition can have a density of less than 0.7 g/cm3, or less than 0.68 g/cm3. In various embodiments, the extrusion-foamed polymeric composition can have a density in the range of from 0.35 to 0.7 g/cm3, or from 0.39 to 0.68 g/cm3.
The above-described extrusion-foamed polymeric composition can be included as a part or the entirety of various articles of manufacture. Such articles of manufacture include, but are not limited to, footwear (e.g., shoe soles), pipes and tubing, mattresses, automotive applications, wire-and-cable applications (e.g., cable insulation), building and construction applications (e.g., insulating materials), and the like.
Density is determined according to ASTM D792.
Melt index, or I2, is measured in accordance with ASTM D1238, condition 190° C./2.16 kg, and is reported in grams eluted per 10 minutes.
For tensile, flexural modulus and dynamic mechanical analysis testing, the compositions are compression molded into solid (non-foamed) plaques. A 4 inch×4 inch×0.050 inch thick plaque is prepared. Pellets for each composition are pressed under low pressure (500 psi) at 125° C. for 3 min, raised to high pressure (2500 psi) for 3 min, then cooled to 30° C. while under high pressure. The molded plaques are removed, cut into pieces, and pressed a second time under the same conditions.
Dynamic mechanical analysis (DMA) is tested on solid samples (non-foamed) using an ARES rheometer to assess modulus of the compositions as a function of temperature. The DMA test conditions are 0.025% strain, temperature from −80° C. to 120° C. at a rate of 3° C./min, frequency of 1 Hz, and 3 minutes soaking time. Similarly, DMA is tested on the extruded foam samples using an ARES rheometer to assess modulus of the compositions as a function of temperature. The DMA test conditions for foamed samples are 0.025% strain, temperature from −50° C. to 120° C. at a rate of 3° C./min, frequency of 1 Hz and 3 minutes soaking time.
Tensile and elongation (T&E) testing is conducted on solid samples (non-foamed) according to ASTM D638 Standard Test Method for Tensile Properties of Plastics on an Instru-Met model 4201 tensile testing machine. The T&E is tested at 20 inches per minute crosshead speed, 2.5 inch jaw span with a 100 pound load cell. Each specimen is cut per ASTM D638 Standard to a Type IV dogbone with nominal 0.075 inch thickness.
Flexural Modulus is tested on solid samples (non-foamed) according to ASTM D790 Standard Test Methods for Flexural Properties of Unreinforced and Reinforced Plastics and Electrical Insulating Materials.
The following materials are employed in the Examples, below.
DOW™ LDPE 1321 is a low-density polyethylene having a density of 0.92 g/cm3 and a melt index (I2) of 0.25 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
ENGAGE™ 8207 is a polyolefin elastomer having a density of 0.870 g/cm3 and a melt index (I2) of 5.0 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
ENGAGE™ 7447 is a polyolefin elastomer having a density of 0.865 g/cm3 and a melt index (I2) of 5.0 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
ENGAGE™ 8842 is a polyolefin elastomer having a density of 0.856 g/cm3 and a melt index (I2) of 1.0 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
INFUSE™ 9107 is an olefin block copolymer having a density of 0.866 g/cm3 and a melt index (I2) of 1.0 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
NORDEL™ IP 3722P EL is an EPDM having a density of 0.872 g/cm3 and a melt index (I2) of 0.7 g/10 min., which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
IRGANOX™ 1010 is pentaerythritol tetrakis [3-[3,5-di-tert-butyl-4-hydroxyphenyl]propionate, which is a sterically hindered phenolic antioxidant, and is commercially available from BASF, Ludwigshafen, Germany.
AXELERON™ CX A-0012 NT CPD is a nucleating masterbatch containing 10 weight percent of a nucleating agent in a high-pressure low-density polyethylene (“HP LDPE”), which is commercially available from The Dow Chemical Company, Midland, Mich., USA.
Prepare eight non-foamed inventive samples (S1-S8) and one non-foamed comparative sample (CS1) using the formulations provided in Table 1, below. The compositions are prepared on a twin-screw extruder. The polymer pellets are pre-mixed prior to being fed to the twin-screw extruder. The compositions are compounded at a melt temperature of around 200° C. and 40 lb/hr. Prepare specimens of the samples for analysis according to the preparation methods described above in the Test Methods section. Analyze S1-S8 and CS1 for density, DMA storage modulus, flexural modulus, and tensile modulus according to the Test Methods described above. The results are provided in Table 1, below.
Prepare foamed samples from S1-S8 and CS1 according to the formulations in Table 2 using a single screw extrusion line equipped with a CO2 gas injection system. The CO2 is injected into the middle barrel section of the extruder. The CO2 gas injection flow rate is 1.0 ml/min. The nucleating masterbatch is added during extrusion of the foam samples. The foam is extruded at a line speed of 1.25 in/mf with screw speed of 25 rpm. Analyze the foamed S1-S8 and CS1 for density and DMA storage modulus according to the Test Methods described above. The results are provided in Table 2, below.
The compositions and test results for the solid (non-foamed) samples are given in Table 1. The compositions and test results for the foamed samples are given in Table 2. The comparative example (CS1) has a high foaming ratio of >48%, but has an undesirably high modulus. The non-foamed CS1 storage modulus is over 2199 MPa and 544 MPa at −40° C. and 23° C., respectively.
Unlike CS1, the inventive samples (S1 to S8) exhibit a balance of sufficiently high foaming ratio and low modulus. The inventive compositions, particularly the blends, yield a foaming ratio >22% (sufficiently low density for lightweight), DMA storage modulus reduction of over 30% at all temperatures (<1620 MPa at −40° C., <500 MPa at 0° C., <285 at 23° C.), 2% secant flexural modulus reduction of over 46%, and tensile modulus reduction of over 40%, <90 MPa (for improved flexibility) compared CS1.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2018/116896 | 11/22/2018 | WO | 00 |
