Low viscosity functionalized ethylene copolymers

Abstract

The present disclosure provides embodiments of epoxy-functionalized ethylene-based polymers and processes for making the same, which may include extruding a reactive mixture to form the epoxy-functionalized ethylene-based polymer, the reactive mixture including: an ethylene-based polymer having a viscosity of 50,000 cP or less at 177° C.; an epoxy-functional monomer; a peroxide; and a vinyl-terminated multifunctional coagent having a functionality of 2 or greater.

Description

[Technical Field]

[0001] CROSS-REFERENCE TO RELATED APPLICATIONS This application claims the benefit of U.S. Provisional Application No. 63 / 402,764, filed August 31, 2023, the entire disclosure of which is incorporated herein by reference.

[0002] FIELD OF THE INVENTION The embodiments described herein generally relate to methods for grafting epoxy functional groups onto low viscosity ethylene-based copolymers. [Background technology]

[0003] Grafted or functionalized low viscosity ethylene-based copolymers are useful as recycle compatibilizers. Epoxy-functionalized ethylene-based copolymers are of interest for these applications due, at least in part, to the reaction between the epoxy groups of the epoxy-functionalized ethylene-based copolymer and the acid groups (e.g., in the polyester).

[0004] Common epoxy-functional monomers grafted onto polyolefins or polyolefin copolymers or block copolymers are glycidyl acrylate, glycidyl methacrylate (GMA), and allyl glycidyl ether (AGE). However, it is also possible to graft other epoxy-functional vinyl monomers onto polyolefins or polyolefin copolymers or block copolymers. Typically, grafting is performed using peroxide initiation. However, grafting epoxy functionality onto ethylene copolymers is difficult due to low grafting efficiency and the tendency of the monomer to homopolymerize (rather than graft) and participate in other side reactions. Furthermore, due to the low viscosity of ethylene copolymers (e.g., less than 50,000 cP at 177°C), an appropriate extruder and peroxide combination are required to achieve the proper graft structure and drive the reaction to completion.

[0005] Polyethylene containing GMA functionality can be produced by in-reactor copolymerization, but there is a lower limit to the resin viscosity (or upper limit to the melt index), which is problematic because low viscosity is needed to achieve good compatibilization in packaging recycling.

[0006] Therefore, there is a need for a more efficient method for grafting epoxy-functional monomers onto low viscosity polyolefins that avoids the low viscosity limitations present in copolymerization processes. Summary of the Invention

[0007]

[0006] Embodiments of the present disclosure fulfill the aforementioned needs by utilizing a coagent that improves the grafting reaction of epoxy-functional monomers onto low-viscosity polyolefins during the grafting process. It has been discovered that certain coagents containing vinyl groups aid in grafting epoxy-functional monomers onto low-viscosity polyolefins while improving grafting levels and grafting efficiency and minimizing homopolymer formation.

[0008] In one embodiment, a grafting process of the present disclosure involves producing an epoxy-functionalized ethylene-based polymer, the process comprising extruding a reactive mixture to form the epoxy-functionalized ethylene-based polymer, the reactive mixture comprising: an ethylene-based polymer having a viscosity of 50,000 cP or less at 177° C; an epoxy-functional monomer; a peroxide; and a vinyl-terminated multifunctional coagent having a functionality of 2 or greater.

[0009] These and other embodiments are described in more detail in the detailed description below. DETAILED DESCRIPTION OF THE INVENTION

[0010] Certain embodiments of the present application will now be described. These embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the subject matter to those skilled in the art.

[0011] As noted above, the present disclosure provides a process for producing an epoxy-functionalized ethylene-based polymer, comprising extruding a reactive mixture to form an epoxy-functionalized ethylene-based polymer, the reactive mixture comprising: an ethylene-based polymer having a viscosity of 50,000 cP or less at 177° C; an epoxy-functional monomer; a peroxide; and a vinyl-terminated multifunctional coagent having a functionality of 2 or greater.

[0012] Ethylene-based polymers In one embodiment, the ethylene-based polymer is an ethylene / α-olefin interpolymer, and the α-olefin is a C3 to C20 α-olefin, or a C3 to C10 α-olefin. In one embodiment, the ethylene-based polymer is an ethylene / α-olefin copolymer, and the α-olefin is a C3 to C20 α-olefin, or a C3 to C10 α-olefin.

[0013] In one embodiment, the reactive mixture comprises 80 to 97 weight percent ethylene-based polymer. In some embodiments, the reactive mixture comprises 83 to 97 weight percent ethylene-based polymer, 85 to 97 weight percent ethylene-based polymer, 85 to 96 weight percent ethylene-based polymer, 87 to 96 weight percent ethylene-based polymer, 88 to 96 weight percent ethylene-based polymer, 89 to 96 weight percent ethylene-based polymer, or 89.5 to 96 weight percent ethylene-based polymer. All individual values ​​and subranges from 80 to 97 weight percent ethylene-based polymer are included herein and disclosed herein.

[0014] In one embodiment, the ethylene-based polymer has a melt viscosity at 350°F (177°C) of 50,000 cP or less, or 45,000 cP or less, or 40,000 cP or less. In one embodiment, the ethylene-based polymer has a melt viscosity at 350°F (177°C) of 30,000 cP or less, or 25,000 cP or less, or 20,000 cP or less, or 15,000 cP or less. In one embodiment, the ethylene-based polymer has a melt viscosity at 350°F (177°C) of 1,000 cP or more, or 2,000 cP or more, or 3,000 cP or more, or 4,000 cP or more, or 5,000 cP or more. In one embodiment, the viscosity of the ethylene-based polymer is from 5,000 to 50,000 cP at 350°F (177°C). For purposes of this disclosure, a "low viscosity" ethylene-based polymer refers to an ethylene-based polymer having a melt viscosity of 50,000 cP or less at 350°F (177°C).

[0015] In one embodiment, the ethylene-based polymer has a density less than, or equal to, 0.900, less than, or equal to, 0.895, less than, or equal to, 0.890, less than, or equal to, 0.885, less than, or equal to, 0.880, or less than, or equal to, 0.875 g / cc (g / cc = g / cm 3 In one embodiment, the ethylene-based polymer has a density greater than, or equal to, 0.850, 0.855, 0.860, or 0.865 g / cc. In one embodiment, the ethylene-based polymer has a density from 0.850 to 0.900 g / cc.

[0016] Epoxy-functional monomers In one embodiment, the epoxy-functional monomer comprises one or more of glycidyl acrylate, glycidyl methacrylate (GMA), and allyl glycidyl ether (AGE). Other suitable epoxy-functional monomers include, but are not limited to, (3,4-epoxycyclohexyl)methyl acrylate, (3,4-epoxycyclohexyl)methyl acrylate, and 1,2-epoxy-4-vinylcyclohexane.

[0017] In one embodiment, the reactive mixture includes 0.3 wt% to 10.0 wt% epoxy-functional monomer, based on the total weight of the reactive mixture. In some embodiments, the reactive mixture may include 2.5 to 9.5 wt% epoxy-functional monomer, 2.5 to 9.0 wt% epoxy-functional monomer, 3.0 to 9.0 wt% epoxy-functional monomer, 3.0 to 8.5 wt% epoxy-functional monomer, or 3.0 to 8.0 wt% epoxy-functional monomer. All individual values ​​and subranges from 0.3% to 10.0 wt% epoxy-functional monomer are included herein and disclosed herein.

[0018] auxiliary agent In one embodiment, the reactive mixture comprises 0.1 to 5.0 weight percent vinyl-terminated multifunctional coagent. In some embodiments, the reactive mixture may comprise 0.6 to 4.6 weight percent vinyl-terminated multifunctional coagent, 0.7 to 4.2 weight percent vinyl-terminated multifunctional coagent, 0.8 to 3.8 weight percent vinyl-terminated multifunctional coagent, 0.9 to 3.4 weight percent vinyl-terminated multifunctional coagent, 1.0 to 3.0 weight percent vinyl-terminated multifunctional coagent, or 1.1 to 2.6 weight percent vinyl-terminated multifunctional coagent. All individual values ​​and subranges between 0.1 and 5.0 weight percent vinyl-terminated multifunctional coagent are included herein and disclosed herein.

[0019] In one embodiment, the vinyl-terminated multifunctional coagent comprises divinylbenzene. Other suitable vinyl-terminated multifunctional coagents include, but are not limited to, trivinylcyclohexane and diethylene glycol divinyl ether.

[0020] The molecular structure of the vinyl-terminated polyfunctional coagent can be represented by formula (I) where n≧2.

[0021] [ka]

[0022] In one embodiment, the molecular structure of the vinyl-terminated multifunctional coagent can be represented by formula (I) where n≧3.

[0023] In one embodiment, the vinyl-terminated multifunctional coagent comprises an acrylate-terminated multifunctional coagent, the molecular structure of which can be represented by formula (II) where n≧2.

[0024] [ka]

[0025] In one embodiment, the molecular structure of the acrylate-terminated multifunctional coagent can be represented by formula (II), where n≧3.

[0026] In some embodiments, the acrylate-terminated multifunctional coagent comprises trimethylolpropane triacrylate (TMPTA SR351H, SR351HP). TMPTA is commercially available from Sartomer. Other suitable acrylate-terminated multifunctional coagents include, but are not limited to, cyclohexanedimethanol diacrylate (SR406), alkoxylated hexanediol diacrylate (SR561, SR562, SR563, SR564), alkoxylated neopentyl glycol diacrylate (SR9043), 1,3-butylene glycol diacrylate (SR212B), 1,4-butanediol diacrylate (SR213), diethylene glycol diacrylate (DEGDA, SR230), 1,6-Hexanediol diacrylate (HDDA, SR238, SR238B, SR238BTF), neopentyl glycol diacrylate, polyethylene glycol diacrylate (SR259, SR344, SR610), tetraethylene glycol diacrylate (SR268), tripropylene glycol diacrylate (TPGDA, SR306F, SR306FTF), ethoxylated bisphenol A diacrylate (SR349, SR601, SR602, SR9038, CN120A60), dipropylene glycol diacrylate (DPGDA), tricyclodecane dimethanol diacrylate (SR833S), neopentyl glycol diacrylate (SR9209A), propoxylated neopentyl glycol diacrylate (SR9003B), tris(2-hydroxyethyl) isocyanurate triacrylate (THEICTA SR368, SR368D), ethoxylated trimethylolpropane triacrylate (SR415, SR454, SR499, SR502, SR9035), pentaerythritol triacrylate (PETIA SR444), propoxylated trimethylolpropane triacrylate (SR492, SR501), propoxylated glyceryl triacrylate (GPTA, SR9020), pentaerythritol tetraacrylate (SR295), ditrimethylolpropane tetraacrylate (SR355), dipentaerythritol pentaacrylate (DiPEPA, SR399, SR399LV), ethoxylated pentaerythritol tetraacrylate (SR494), alkoxylated pentaerythritol tetraacrylate (LM5401), low viscosity diacrylate oligomer (CN132), low viscosity triacrylate oligomer (CN133US), and the like, which are commercially available from Sartomer.

[0027] In some embodiments, the reactive mixture includes a combination of two or more coagents.

[0028] peroxide Suitable peroxides include, but are not limited to, LUPEROX 101 (2,5-dimethyl-2,5-di(t-butylperoxy)hexane) CAS#78-63-7; LUPEROX DC (dicumyl peroxide) CAS#80-43-3; LUPEROX DTA (di(t-amyl) peroxide) CAS#10508-09-5; LUPEROX P (t-butylperoxybenzoate) CAS#614-45-9; LUPEROX TAP (t-amyl peroxybenzoate) CAS#4511-39-1; LUPEROX F (a,a'-bis(t-butylperoxy)-diisopropylbenzene) CAS#25155-25-3; and LUPEROX TBEC (OO-t-butyl O-(2-ethylhexyl) monoperoxycarbonate) CAS#34443-12-4. LUPEROX 101 is a preferred peroxide. The purpose of the peroxide is to function as a free radical initiator by generating radical species for radical reactions, particularly grafting reactions. The peroxide can decompose into at least one primary radical selected from the following radicals: (a) RCOO· (where R is alkyl); (b) RO· (where R is alkyl); or c) ROC(O)O· (where R is alkyl).

[0029] In some embodiments, the reactive mixture comprises a combination of two or more peroxides.

[0030] Extruder Examples of extruders that can be used to extrude the reactive mixture to form the epoxy-functionalized ethylene-based polymer include, but are not limited to, co-rotating intermeshing twin-screw extruders, counter-rotating twin-screw extruders, tangential twin-screw extruders, Buss kneading extruders, planetary extruders, and single-screw extruders. Further features of interest are design specifications, including the length / diameter ratio (L / D ratio) and mixing section (screw design). Typically, the maximum L / D ratio for a single extruder is about 60. For longer L / D ratios, two extruders are coupled together. Shaft (screw) designs include, but are not limited to, those comprised of mixing elements such as kneading disk blocks, left-handed screw elements, turbine mixing elements, gear mixing elements, and combinations thereof.

[0031] Grafting in a twin-screw extruder with an appropriate residence time (30 seconds to 3 minutes) to complete the reaction has been found to give the best results, although other extruders, including but not limited to those mentioned above, may be used. Longer residence times, while possible, will limit the speed and productivity of the grafting extruder. Additionally, it is important to use a peroxide with a half-life appropriate to the residence time in the extruder at the melt temperature. Suitable peroxides are discussed above.

[0032] Modern extruders, both modular and single barrel, feature temperature control over various sections. Thus, it is possible to set and control different barrel temperatures along the length of the barrel. The maximum barrel temperature is the maximum set temperature. Different barrel temperatures are desirable to control the energy input and melt temperature along the length of the extruder, and to control the extrudate temperature.

[0033] The extruder barrel houses the screw or rotor of the extruder. They serve to contain the polymer within the extruder and are designed to provide heating or cooling to the polymer as it is processed through heater and cooling channels. They are designed to withstand the high temperatures and pressures encountered during the extrusion operation.

[0034] The screw / rotor can rotate at various speeds, typically up to 1500 rpm. The rotation of the screw / rotor also inputs energy into the materials being processed within the extruder, raising their temperature and thereby promoting melting, mixing, and reaction.

[0035] Processing results In one embodiment, the process for producing the epoxy-functionalized ethylene-based polymer results in a grafting level of at least 0.4 wt%, at least 2 wt%, at least 3%, or at least 4%.

[0036] In one embodiment, the process for producing the epoxy-functionalized ethylene-based polymer results in a grafting efficiency of 30% or greater, 40% or greater, or 50% or greater.

[0037] In one or more embodiments, grafting levels of at least 5% and grafting efficiencies of at least 65% were achieved without significant crosslinking with glycidyl methacrylate (GMA) as the epoxy-functional monomer and trimethylolpropane triacrylate (TMPTA) as the crosslinking coagent.

[0038] Epoxy-functionalized ethylene-based polymers Also provided are epoxy-functionalized ethylene-based polymers formed from any embodiment, or combination of embodiments, described herein.

[0039] In one embodiment, the epoxy-functionalized ethylene-based polymer has a melt viscosity at 350°F (177°C) of 50,000 cP or less, 40,000 cP or less, 30,000 cP or less, 20,000 cP or less, or 15,000 cP or less. In one embodiment, the epoxy-functionalized ethylene-based polymer has a melt viscosity at 350°F (177°C) of 6,500 to 50,000 cP, 65,000 to 30,000 cP or less, or 10,000 to 30,000 cP. It is important that the epoxy-functionalized ethylene-based polymer have a melt viscosity at 350°F (177°C) of 50,000 cP or less because this demonstrates that unacceptable levels of crosslinking have been avoided. Excessive amounts of crosslinking can hinder grafting efficiency. Additionally, as discussed above, it is important that the epoxy-functionalized ethylene-based polymer have a low viscosity to achieve good compatibilization in packaging recycling.

[0040] Also provided are compatibilized formulations comprising epoxy-functionalized ethylene-based polymers formed from any embodiment, or combination of embodiments, described herein.

[0041] In some embodiments, the compatibilizing formulation can include 1 to 10 weight percent epoxy-functionalized ethylene-based polymer, 2 to 10 weight percent epoxy-functionalized ethylene-based polymer, 4 to 10 weight percent epoxy-functionalized ethylene-based polymer, 5 to 8 weight percent epoxy-functionalized ethylene-based polymer, 5 to 7 weight percent epoxy-functionalized ethylene-based polymer, In one embodiment, the compatibilizing formulation includes 6 weight percent epoxy-functionalized ethylene-based polymer.

[0042] Compatibilized formulations incorporating epoxy-functionalized ethylene-based polymers produced according to the present disclosure may have an Izod impact strength (at ambient temperature) of 200 J / m or greater, 250 J / m or greater, 300 J / m or greater, or 335 J / m or greater, as measured by ASTM D256 Method A, as described in the Test Methods section of this disclosure.

[0043] Compatibilized formulations incorporating epoxy-functionalized ethylene-based polymers produced according to the present disclosure may have an elongation at break of 50% or greater, 60% or greater, 70% or greater, or 75% or greater, as measured by ASTM D4703, Appendix A.1 (Procedure C), as described in the Test Methods section of this disclosure.

[0044] Compatibilized formulations incorporating epoxy-functionalized ethylene-based polymers produced according to the present disclosure may have a stress at break of 1000 psi or greater, 1100 psi or greater, 1200 psi or greater, or 1300 psi or greater, as measured by ASTM D4703 as per Appendix A.1 (Procedure C), as described in the Test Methods section of this disclosure.

[0045] Compatibilized formulations incorporating the epoxy-functionalized ethylene-based polymers produced according to the present disclosure may have a low shear viscosity at 275°C and a frequency of 0.1 rad / s of 10,000 Pa·s or greater, 10,500 Pa·s or greater, 11,500 Pa·s or greater, or 12,500 Pa·s or greater, as measured according to the Dynamic Mechanical Spectroscopy (DMS) method, as described in the Test Methods section of this disclosure.

[0046] definition As used herein, the term "composition" includes the material or mixture of materials that comprise the composition, as well as reaction products and decomposition products formed from the materials of the composition. Typically, any reaction products and / or decomposition products are present in trace amounts.

[0047] The term "polymer" refers to a polymeric compound prepared by polymerizing monomers, whether of the same or different types. Thus, the general term polymer generally encompasses the term "homopolymer," which refers to a polymer prepared from only one type of monomer, as well as the term "copolymer," which refers to a polymer prepared from two or more different monomers. As used herein, the term "interpolymer" refers to a polymer prepared by polymerization of at least two different types of monomers. Thus, the general term interpolymer includes copolymers or polymers prepared from more than two different types of monomers, such as terpolymers.

[0048] "Polyethylene" or "ethylene-based polymer" means a polymer containing 50 mole percent or more of units derived from ethylene monomers. This includes ethylene-based homopolymers or copolymers (meaning the units are derived from two or more comonomers). Common forms of ethylene-based polymers known in the art include low-density polyethylene (LDPE), linear low-density polyethylene (LLDPE), ultra-low-density polyethylene (ULDPE), very low-density polyethylene (VLDPE), single-site catalyzed linear low-density polyethylene (m-LLDPE), including both linear and substantially linear low-density resins, medium-density polyethylene (MDPE), and high-density polyethylene (HDPE).

[0049] The term "LLDPE" includes resins made using Ziegler-Natta catalyst systems, as well as resins made using single-site catalysts, including but not limited to bismetallocene catalysts (sometimes referred to as "m-LLDPE"), phosphinimine, and constrained geometry catalysts, and post-metallocene catalysts, including but not limited to bis(biphenylphenoxy) catalysts (also referred to as polyaryloxy ether catalysts). LLDPE includes linear, substantially linear, or heterogeneous ethylene-based copolymers or homopolymers. LLDPE contains less long chain branching than LDPE and includes substantially linear ethylene polymers as further defined in U.S. Patent Nos. 5,272,236, 5,278,272, 5,582,923, and 5,733,155, homogeneously branched linear ethylene polymer compositions such as those in U.S. Patent No. 3,645,992, heterogeneously branched ethylene polymers such as those prepared according to the process disclosed in U.S. Patent No. 4,076,698, and blends thereof (such as those disclosed in U.S. Patent No. 3,914,342 or U.S. Patent No. 5,854,045). LLDPE resins may be made by gas phase, solution phase, or slurry polymerization, or any combination thereof, using any type of reactor or reactor configuration known in the art.

[0050] The term "HDPE" refers to ethylene-based polymers having a density greater than about 0.940 g / cc, and are generally prepared with Ziegler-Natta, chromium, or even metallocene catalysts.

[0051] "Polypropylene" or "propylene-based polymer" shall mean a polymer containing 50 mole percent or more of units derived from propylene monomers. This includes propylene-based homopolymers or copolymers (meaning units derived from two or more comonomers). Common forms of ethylene-based polymers known in the art include, but are not limited to, impact polypropylene copolymers (icPP), random copolymers (rcPP), polypropylene homopolymers (hPP), propylene / ethylene copolymers (POE plastomers), and polypropylene reactor blends.

[0052] As used herein, the term "olefin-based polymer" refers to a polymer that, in polymerized form, comprises 50% by weight or a majority amount of an olefin monomer, e.g., ethylene or propylene, based on the weight of the polymer, and may optionally comprise one or more comonomers. In one embodiment, an olefin-based polymer comprises a majority amount of an olefin monomer (based on the weight of the polymer) and may optionally comprise one or more comonomers. Olefin-based polymers are also referred to herein as "polyolefins."

[0053] As used herein, the term "ethylene / α-olefin interpolymer" refers to an interpolymer comprising, in polymerized form, at least 50% by weight or a majority amount of ethylene monomer (based on the weight of the interpolymer) and at least one α-olefin. In one embodiment, the ethylene / α-olefin interpolymer comprises a majority amount of ethylene monomer (based on the weight of the ethylene-based interpolymer) and at least one α-olefin.

[0054] As used herein, the term "ethylene / α-olefin copolymer" refers to a copolymer that, in polymerized form, comprises at least 50% by weight or a majority amount of ethylene monomer (based on the weight of the copolymer) and an α-olefin, as the only two monomer types. In one embodiment, the ethylene / α-olefin copolymer comprises, as the only monomer types, a majority amount of ethylene monomer (based on the weight of the ethylene-based copolymer) and an α-olefin.

[0055] The term "multifunctional," when used in conjunction with a functional group as a descriptor of a coagent, indicates that the coagent is terminated in at least two positions with the corresponding functional group. For example, the phrase "vinyl-terminated multifunctional coagent" refers to a coagent that includes molecules that are terminated in at least two positions with vinyl functionality. Similarly, the phrase "acrylate-terminated multifunctional coagent" refers to a coagent that includes molecules that are terminated in at least two positions with acrylate functionality. Furthermore, because the acrylate functionality contains a vinyl functionality, an acrylate-terminated multifunctional coagent represents one form of a vinyl-terminated multifunctional coagent.

[0056] The terms "comprising," "including," "having," and their derivatives are not intended to exclude the presence of any additional components, steps, or procedures, whether specifically disclosed or not. For the avoidance of doubt, all compositions claimed through the use of the term "comprising" may include any additional additives, adjuvants, or compounds, whether polymeric or otherwise, unless otherwise stated to the contrary. In contrast, the term "consisting essentially of" excludes from any subsequently recited scope any other component, step, or procedure, except those that are not essential to operability. The term "consisting of" excludes any component, step, or procedure not specifically delineated or listed.

[0057] It should be noted that for purposes of describing and defining the present invention, references herein to "at least one" component, element, etc. should not be used to create an inference that the alternative use of the article "a" or "an" is to be limited to a single component, element, etc. For example, reference to "a" component includes aspects having two or more such components, unless the context clearly dictates otherwise.

[0058] It should be noted that, as used herein, terms such as "preferably," "generally," and "typically" are not used to limit the scope of the claimed invention or to imply that a particular feature is critical, essential, or even essential to the structure or function of the claimed invention. Rather, these terms are merely intended to identify particular aspects of embodiments of the present disclosure, or to highlight alternative or additional features that may or may not be utilized in a particular embodiment of the present disclosure.

[0059] It should be noted that one or more of the following claims utilize the term "wherein" as a transitional phrase. It should be noted that for purposes of defining the invention, this term is introduced in the claims as an open-ended transitional phrase used to introduce the recitation of a series of features of structure, and should be interpreted in a similar manner to the more commonly used open-ended preamble term "comprising."

[0060] Unless specifically and explicitly stated otherwise, it is in no way intended that any method described herein be construed as requiring its steps to be performed in a particular order, or as requiring a particular orientation of any apparatus. Thus, where a method claim does not actually recite the order in which its steps should be followed, or any apparatus claim does not actually recite an order or orientation for individual components, or unless it is specifically stated in the claim or specification that the steps are to be limited to a particular order, or no particular order or orientation for the apparatus components is recited, no order or orientation is intended to be inferred in any respect. This preserves any possible implicit basis for interpretation, including questions of logic regarding the sequencing of steps, operational flow, component order, or component orientation; plain meaning derived from grammatical constructions or punctuation; and the number or type of embodiments described herein.

[0061] Test Method Test methods used herein include the following: Epoxide content, Fourier transform infrared spectroscopy (FTIR) analysis The concentration of epoxide groups is determined by the ratio of the epoxide group peak height to the polymer reference peak (at the corresponding wavenumber); in the case of polyethylene, the wavenumber is 2751 cm -1 The epoxide content was calculated by multiplying this ratio by the appropriate calibration constant. -1 The formula used for GMA grafted polyolefins, represented by the peaks at 1, has the following form, as shown in Equation 1: GMA(weight%)=A * {[847cm -1 FTIR peak height at 2751 cm -1 FTIR peak height at ]-B (Equation 1)

[0062] The calibration constants A (12.403) and B (0.168) can be determined using known calibration standards. Actual calibration constants may vary slightly depending on the instrument and polymer.

[0063] The sample preparation procedure begins by pressing a sample, typically 0.05-0.15 mm thick, between two protective films in a heated press at 150-180°C for 1 hour. MYLAR and TEFLON are suitable protective films for protecting the sample from the platens. The platens must be under pressure (approximately 10 tons) for approximately 5 minutes. The sample is allowed to cool to room temperature and then vacuum stripped to remove any unreacted residual GMA. After stripping, the sample is placed in an appropriate sample holder and then scanned in the FTIR. A background scan should be performed before each sample scan or as needed. Test precision is good, with an inherent variation of less than ±5%.

[0064] Grafting efficiency Grafting efficiency was determined by normalizing the weight percent of GMA determined by FTIR with the weight percent provided in the formulation.

[0065] Melt Viscosity Melt viscosity was measured according to ASTM D 3236 (177°C, 350°F) using a Brookfield digital viscometer (Model DV-III, Version 3) and a disposable aluminum sample chamber. The spindle used was generally an SC-31 hot-melt spindle, suitable for measuring viscosities in the range of 10 to 100,000 centipoise. The sample was poured into the chamber, which was then inserted into a Brookfield Thermosel and secured in place. The sample chamber had a notch in the bottom that fit the bottom of the Brookfield Thermosel, ensuring that the chamber would not rotate when the spindle was inserted and rotating. The sample (approximately 8 to 10 grams of resin) was heated to the required temperature until the molten sample was 1 inch below the top of the sample chamber. The viscometer device was lowered, immersing the spindle in the sample chamber. The lowering continued until the viscometer bracket was flush with the Thermosel. The viscometer was turned on and set to operate at a shear rate that would result in a torque reading within the range of 40-60 percent of the total torque capacity, based on the rpm output of the viscometer. Readings were taken every minute for approximately 15 minutes or until the value stabilized, at which point a final reading was recorded.

[0066] low shear viscosity To prepare each test sample, it was first placed into a 3.10 mm thick, 1.5 inch diameter chase and compression molded at 25,000 lbs pressure at 190°C for 6.5 minutes using a Carver Hydraulic Press (Model #4095.4NE2003). After cooling to room temperature, the sample was removed and awaited rheological testing.

[0067] Dynamic mechanical spectroscopy (DMS) frequency sweeps were performed using 25 mm parallel plates over a frequency range of 0.1 to 100 rad / s. The test gap separating the plates was 1.8 mm, and a 10% strain was applied to satisfy the linear viscoelastic condition. Each test was performed under a nitrogen atmosphere and isothermal conditions at 275 °C. To begin the DMS test, the rheometer oven was first equilibrated at the desired test temperature for at least 30 minutes, after which the sample was loaded into the test geometry. The sample was then equilibrated in the oven with the door closed for 1 minute. The test gap was then set to 1.8 mm, and the sample was allowed 5 minutes to relax the resulting normal force. The oven was then quickly opened, and the sample was trimmed to ensure no bulging was present. The oven was then closed again, and the DMS measurement was initiated. During the test, the shear modulus (G'), viscous modulus (G''), and complex viscosity (η) were measured. * The complex viscosity measured at a frequency of η 0.1 rad / s is referred to herein as the low shear viscosity.

[0068] All DMS frequency tests were performed on either an ARES-G2 or DHR-3 rheometer (both manufactured by TA Instruments). Data analysis was performed with TA Instruments TRIOS software.

[0069] Tensile properties Specimens were compression molded at 275°C to a nominal thickness of 0.125 inches according to ASTM D4703, Appendix A.1 (Procedure C). Type I specimens were die cut from the sheets and conditioned at 23 (±2)°C and 50 (±10)% relative humidity for at least 40 hours.

[0070] Type I specimens were tensile tested according to D638 (Standard Test Method for Tensile Properties of Plastics). The test speed was 2 inches / minute crosshead displacement. Strain was measured using an extensometer attached to the specimen with an initial gage length of 2 inches. Tensile tests were performed at 23 + / - 2°C.

[0071] Shock resistance Notched Izod impact strength testing was performed according to ASTM D4703 Method A. Specimens were machined to a nominal thickness of 0.125 inches from compression molded sheets prepared per ASTM D4703 Appendix A.1 (Procedure C).

[0072] Test specimens were cut from the sheets using an appropriate die to yield specimens 2.5 inches long and 0.5 inches wide. The specimens were notched on the long edge through the thickness using an automatic notcher to leave a ligament width of 0.4 inches. The notch half angle was 22.5° and the tip radius of curvature was 0.01 inches. The specimens were conditioned at 23 + / - 2°C and 50 + / - 10% relative humidity for at least 40 hours. Impact testing was performed at 23 + / - 2°C.

[0073] The specimen was loaded into the Izod tester per ASTM D256 Method A with the notch facing the impactor. The pendulum was released and the energy absorbed during the test was automatically recorded. The specimen was inspected after the test and the type of failure was recorded (full, hinge, partial failure, or no failure). Five replicates per sample were tested. [Example]

[0074] The following examples illustrate features of the present disclosure, but are not intended to limit the scope of the disclosure. The following experiments analyzed the performance of embodiments of the low viscosity functionalized ethylene copolymers described herein.

[0075] The materials used in this study are listed in Table 1.

[0076] [Table 1] * Density of 0.87 g / cc and melt viscosity of 6700 cP at 177°C (350°F)

[0077] Apparatus and experimental conditions To prepare the Examples and Comparative Examples described below, each grafting reaction was carried out in a 26 mm co-rotating twin-screw extruder (ZSK-26 manufactured by Coperion Corp.). The extruder was configured with 15 barrels (60 L / D). The maximum screw speed was 1200 rpm, and the maximum motor power was 40 HP. The extruder was equipped with a "loss-in-weight feeder." GMA and the GMA-coagent mixture were injected at barrel 3, and peroxide, soaked onto ethylene copolymer pellets, was fed through the main feed throat. Five standard cubic feet per hour (SCFH) of nitrogen was used to purge the first barrel section to maintain an inert atmosphere and minimize oxidation. A vacuum (approximately 15" Hg) was applied at barrel 13. A two-hole die was used to produce strands, which were then chopped into pellets with a strand cutter. The run rate was 8 lbs / hr, and a screw speed of 375 rpm was used. Barrel 1 was water-cooled, barrels 2-4 were maintained at 50-70°C, barrels 6-11 were maintained at 220°C, and barrels 12-15 were maintained at 160°C.

[0078] The compositions of the examples and comparative examples are shown in Table 2, along with the grafting level (GMA wt%), grafting efficiency (%), and viscosity, each determined according to the test methods described above.

[0079] [Table 2]

[0080] [Table 3]

[0081] [Table 4] * 1cP=0.001Pa·s

[0082] The results shown in Table 2 demonstrate the low grafting levels and efficiency when no coagent is used during the grafting process. In other words, the grafting reaction of epoxide groups (in this case, GMA) onto low-viscosity polyolefins can be improved when a coagent is used. The results in Table 2 further demonstrate the effect of various coagents. In particular, when comparing the results of the Examples with the Comparative Examples, it becomes clear that when a multifunctional vinyl or multifunctional acrylate coagent is used, the grafting efficiency is at least 30%. However, when no coagent is used or when a multifunctional methacrylate-terminated coagent is used, the grafting efficiency is consistently less than 20%. Furthermore, the epoxy-functionalized ethylene-based polymers exhibit minimal viscosity increase with the preferred coagents, thereby indicating a lack of crosslinking. The relatively high viscosities of Examples 2 and 11 are expected, as both of these Examples have high levels of peroxide and coagent, resulting in high grafting levels.

[0083] Evaluation in PE-PET compatibilized blends The materials used to prepare the experimental compatibilized formulations are listed in Table 3 below.

[0084] To prepare the formulations, samples were mixed using an RS5000 batch mixer manufactured by Rheometers Services Inc. A bowl capable of mixing batches up to 250 g was used with a roller blade rotor. After a few minutes of initial fluidization of the base polymers (polyethylene and polyethylene terephthalate), the compatibilizer (GMA graft polymer) was charged into the mixer at low speed. After all other ingredients were incorporated, the batches were mixed using a rotor speed of 30-60 rpm and a bowl temperature of 275 °C. Mixing continued for an additional 10-15 minutes. After mixing, each batch was collected on a glass-reinforced Teflon sheet, pressed into a flat "putty" on a compression molder, and cooled to ambient temperature. Compression-molded specimens for mechanical testing were prepared from each flat "putty" using the procedures described above in the Test Methods section. Results of DMS measurements, Izod impact strength, and tensile testing are also shown in Table 3.

[0085] [Table 5] * Table values ​​are in weight percent (wt%) based on the total weight of the formulation †Measured at 275°C and 0.1 rad / s using the DMS method described in the Test Methods section (reported in Pa·s) DOWLEX™ 2045 is a linear low density polyethylene (LLDPE) available from Dow Inc. LDPE 501I is a low density polyethylene (LDPE) available from Dow Inc. ELVALOY™ PTW is a GMA-based ethylene terpolymer available from Dow Inc. PET is polyethylene terephthalate.

[0086] As can be seen from the results in Table 3, when the GMA-grafted ethylene-based polymers from Examples 3, 4, and 5 of the present invention are incorporated into the compatibilized formulations (RC2, RC3, and RC4), the resulting impact strength and ductility (elongation at break) are improved. The formulations without the GMA-grafted ethylene-based polymer exhibit significantly lower impact strength and elongation at break. When compared to the commercial compatibilizer (EVALOPTW; RC5), the inventive grafts in formulations RC2, RC3, and RC4 exhibit better flow properties (as indicated by lower viscosity).

[0087] It will be apparent that modifications and variations are possible without departing from the scope of the present disclosure, as defined in the appended claims. More specifically, while certain aspects of the present disclosure have been identified herein as preferred or particularly advantageous, it is not intended that the present disclosure be necessarily limited to these aspects.

Claims

1. 1. A process for the production of an epoxy-functionalized ethylene-based polymer, comprising: extruding a reactive mixture to form the epoxy-functionalized ethylene-based polymer, wherein the reactive mixture comprises: an ethylene-based polymer having a viscosity of 50,000 cP or less at 177°C; an epoxy-functional monomer; Peroxide and a vinyl-terminated multifunctional coagent having a functionality of 2 or greater.

2. 10. The process of claim 1, wherein the epoxy-functionalized ethylene-based polymer has a grafting efficiency of 30% or greater.

3. 3. The process of claim 1 or 2, wherein the epoxy-functional monomer comprises one or more of glycidyl acrylate, glycidyl methacrylate (GMA), and allyl glycidyl ether (AGE).

4. The process of any one of claims 1 to 3, wherein the reactive mixture comprises 0.3 to 10.0 weight percent epoxy-functional monomer and 80 to 97 weight percent ethylene-based polymer.

5. The process of any one of claims 1 to 4, wherein the reactive mixture comprises 0.1 to 5.0 wt% of a vinyl-terminated multifunctional coagent.

6. The process of any one of claims 1 to 5, wherein the vinyl-terminated multifunctional coagent comprises divinylbenzene.

7. The process of any one of claims 1 to 5, wherein the vinyl-terminated multifunctional coagent comprises an acrylate-terminated multifunctional coagent.

8. 8. The process of claim 7, wherein the acrylate-terminated multifunctional coagent comprises trimethylolpropane triacrylate (TMPTA).

9. 8. The process of claim 7, wherein the acrylate-terminated multifunctional coagent comprises an alkylene glycol diacrylate or a polyalkylene glycol diacrylate.

10. The process of any one of claims 1 to 9, wherein the ethylene-based polymer has a viscosity of 5,000 to 50,000 cP (@ 177°C).

11. The process of any one of claims 1 to 10, wherein the epoxy-functionalized ethylene-based polymer has a viscosity of 6,500 to 50,000 cP, or 66,500 to 30,000 cP (@ 177°C).

12. The process of any one of claims 1 to 11, wherein the ethylene-based polymer comprises an ethylene / alpha olefin copolymer having a density from 0.850 to 0.900 g / cc.

13. The process of any one of claims 1 to 12, wherein extruding the reactive mixture is carried out using a twin-screw extruder.

14. 14. An epoxy-functionalized ethylene-based polymer produced by the process of any one of claims 1 to 13.

15. A compatibilizer formulation comprising the epoxy-functionalized ethylene-based polymer of claim 14.

Images