 Autoclave film and bag
专利摘要:
A film and autoclave pouch discloses a polymeric composition here. the polymeric composition includes: (a) a propylene / α-olefin interpolymer; (b) an ethylene-based polymer; (c) a block composite comprising: (i) a propylene-based crystalline polymer; (ii) an ethylene / α-olefin polymer; and (iii) a block copolymer comprising a propylene-based crystalline block and an ethylene / α-olefin block. the polymeric composition provides improved thermal seals when molded in film, film layer, or flexible containers such as autoclave pouch. 公开号:BR112013007286B1 申请号:R112013007286-5 申请日:2011-09-29 公开日:2020-03-31 发明作者:Wenbin Liang；Kim L. Walton；R. Marchand Gary 申请人:Dow Global Technologies Llc； IPC主号:
专利说明:
"FILM AND AUTOCLAVE BAG History [0001] Plastic films find use in a wide variety of packaging applications such as bags, containers, cups, bags, tubes, and trays. Laminates, single layer films, and multilayer films having a heat sealable layer are often used in forming, filling, and sealing (FFS) machines. FFS machines create a continuous stream of film packages, packages capable of being closed by film-to-film seals. [0002] Film-to-film heat seal closures are formed by placing the film between heat seal clamps that apply pressure and also apply heat above the start temperature of the film seal. Prepared heat seal closures are often the strongest after the seal has cooled to room temperature. In order to increase production capacity, the packages are filled with product before the thermal seal has time to cool completely. Consequently, it is necessary for the thermal seal to provide sufficient strength very quickly without the need to cool the package to room temperature. Otherwise, the thermal seal will be compromised resulting in rejected product, disposal, and increased expense. [0003] In addition, films used in autoclave packaging need to form thermal seals that can withstand the high temperature required for sterilization. Typically, autoclave packs are exposed to temperatures greater than 121 ° C, or greater than 130 ° C, for Petition 870190115675, of 11/11/2019, p. 11/72 2/58 extended period of time in order to sterilize the contents inside. [0004] Therefore, the technique recognizes the continuing need to develop improved films for FFS applications. In particular, there is a need for films having a low heat seal start temperature and a strong thermal stickiness resistance over a wide temperature range in order to increase the production efficiency of packaging procedures, such as FFS procedures. There is still a need for films having sealing resistance at high temperature in addition to the aforementioned film properties. Summary [0005] The present disclosure provides a polymeric composition and films produced with it. When molded into a film (or film layer), the present polymeric composition exhibits (I) low heat seal initiation temperature, (II) strong hot tackiness over a wide temperature window, and (III) high tackity resistance the hot. In addition, the composite film of the present polymeric composition has a high temperature sealing resistance suitable for use as a film in autoclave packaging. [0006] The present disclosure provides a polymeric composition. In an embodiment, a polymeric composition is provided including: (A) a propylene / aolefin interpolymer; (B) an ethylene-based polymer; (C) a block composite comprising: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin polymer; and (III) a block copolymer comprising a crystalline block based on Petition 870190115675, of 11/11/2019, p. 12/72 3/58 propylene and an ethylene / a-olefin block. [0007] The present disclosure provides a film. In an embodiment, a film is provided that includes at least one layer formed by a polymeric composition comprising: (A) a propylene / α-olefin interpolymer; (B) an ethylene-based polymer; (C) a block composite comprising: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin polymer; and (III) a block copolymer comprising a propylene-based crystalline block and an ethylene / α-olefin block. [0008] In an embodiment, the film provides a second layer. The second layer is composed of an olefin-based polymer. [0009] The present disclosure provides an article. In an embodiment, an autoclave pouch is provided that includes a first layer, a second layer, and an optional third layer. The first layer is composed of a polymeric composition comprising: (A) a propylene / α-olefin interpolymer; (B) an ethylene-based polymer; (C) a block composite comprising: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin polymer; and (III) a block copolymer understanding a crystalline block the base propylene it is a block of ethylene / a-olefin. [0010] In incorporation, The Monday layer can to be composed on one polymer based in olefin. [0011] An advantage of gift disclosure is an improved polymeric composition that provides improved thermal sealing properties when molded into a film or film layer such as low start temperature Petition 870190115675, of 11/11/2019, p. 13/72 4/58 thermal sealing and / or strong resistance to hot tackiness over a wide temperature window, and / or high resistance to hot tackiness. [0012] An advantage of the present disclosure is an improved film for thermal sealing applications. Brief description of the drawings [0013] A Figure 1 is an View in plan an purse of autoclave according with an incorporation gives gift disclosure; [0014] A Figure 2 is an View lateral elevation of a multilayer film according to an embodiment of the present disclosure; [0015] Figure 3 is a side elevation view of a multilayer film according to an embodiment of the present disclosure; [0016] Figure 4 is a graph showing resistance to hot tackiness and temperature for comparative samples and incorporations of the present disclosure; [0017] Figure 5 is a graph showing the hot stickiness temperature window for comparative samples and incorporations of the present disclosure; [0018] Figure 6 is a graph showing thermal sealing resistance and sealing temperature for comparative samples and incorporations of the present disclosure; [0019] Figure 7 is a graph showing friction coefficients for comparative samples and incorporations of the present disclosure; [0020] Figure 8 is a graph showing the clarity for comparative samples and incorporations of the present disclosure; and Petition 870190115675, of 11/11/2019, p. 14/72 5/58 [0021] Figure 9 is a graph showing resistance to hot tackiness at 150 ° C for comparative samples and incorporations of the present disclosure. Detailed Description 1. Composition [0022] The present disclosure provides a polymeric composition. In an embodiment, a polymeric composition is provided including: (A) a propylene / aolefin interpolymer; (B) an ethylene-based polymer; (C) a block composite comprising: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin polymer; and (III) a block copolymer comprising a propylene-based crystalline block and an ethylene / α-olefin block. [0023] Optionally, the polymeric composition can include (D) an olefin-based polymer and / or (E) additives. In an embodiment, the polymeric composition contains from 50% by weight to 95% by weight of component (A), from 1% by weight to 30% by weight of component (B), and 1% by weight to 30% by weight of component (C). Weight percentages are based on the total weight of the composition. It is understood that the amount of each component (A) - (E) can be adjusted to produce 100% of a polymeric composition. (A) Propylene / α-olefin interpolymer [0024] The present composition contains a component (A) propylene / α-olefin interpolymer. For the purposes of this disclosure, ethylene is considered an a-olefin. Non-limiting examples of suitable comonomers include ethylene, C4-20 α-olefins, such as 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-heptene, 1-octene, 1-decene , 1-dodecene, 1-tetradecene, 1-hexadecene, and 1-octadecene; diolefins Petition 870190115675, of 11/11/2019, p. 15/72 6/58 C 4-20 , such as 1,3-butadiene, 1,3-pentadiene, norbornadiene, 5-ethylidene-2-norbornene (ENB) and dicyclopentadiene; aromatic C 8-40 vinyl compounds including styrene, o-, m-, and pmethyl styrene, divinyl-benzene, vinyl biphenyl, vinyl naphthalene; and aromatic vinyl compounds of C 8-40 substituted with halogen such as styrene chlorine and styrene fluorine. 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. [0025] In an embodiment, the propylene / αolefin interpolymer is a propylene / ethylene copolymer. The propylene / ethylene copolymer contains from 1% by weight to 40% by weight of ethylene-derived units (based on the total weight of the propylene / ethylene copolymer). In an additional embodiment, the propylene / ethylene copolymer has a density of 0.86 g / cm 3 to 0.90 g / cm 3 , and / or a melt flow rate (MFR) of 0.5 g / 10 min at 10 g / 10 min, and / or a total crystallinity of 10% to 40%, and / or a melting temperature (T m ) of 70 ° C or 80 ° C to 90 ° C or 95 ° C. Non-limiting examples of propylene / ethylene copolymers are propylene / ethylene copolymers sold under the trade name VERSIFY (such as VERSIFY 2200 and VERSIFY 3200) obtainable from The Dow Chemical Company, Midland, Michigan, and propylene / ethylene copolymers sold with trade name VISTAMAXX obtainable from ExxonMobil Corporation, Irving, Texas. [0026] In incorporation, the copolymer in propylene / ethylene has a density of 0.8 6 g / cm 3 a 0.89 g / cm 3 , and / or a MFR 1 g / 10 min at 3 g / 10 min, and / or Petition 870190115675, of 11/11/2019, p. 16/72 7/58 crystallinity in 20% by weight to 25% in weight, and / or a Tm in 80 ° C to 85 ° C. [0027] In aincorporation, the copolymer in propylene / ethylene has a density of 0.86 g / cm3 to 0, 88 g / cm 3 , and / or a 5 g / 10 min MFR at 10 g / 10 min, and / or crystallinity in 25% by weight to 35% in weight, and / or a Tm in 80 ° C to 90 ° C. [0028] In aincorporation, the copolymer in propylene / ethylene is a copolymer of propylene / ethylene in single phase. In other words, the copolymer in propylene / ethylene excludes heterophasic copolymers such as propylene impact copolymer. [0029] In an embodiment, the propylene / aolefin copolymer has a molecular weight distribution (MWD) of 2.0 or 2.5 to 4.0 or 4.5. In a further embodiment, the propylene / a-olefin interpolymer is a propylene / ethylene copolymer with a MWD greater than 2.0 or 2.5 to 3.5 or 4.0. [0030] The propylene-based polymer may comprise two or more incorporations disclosed herein. (B) Ethylene-based polymer [0031] The present polymeric composition contains an ethylene-based polymer, component (B). The ethylene-based polymer can be an ethylene homopolymer or an ethylene copolymer. The comonomer can be an α-olefin such as a linear, branched or cyclic C 3-20 α-olefin. Non-limiting examples of suitable C 3-20 α-olefins include propene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, and 1-octadecene. Α-olefins may also contain a cyclic structure such as cyclohexane or cyclopentane, resulting in Petition 870190115675, of 11/11/2019, p. 17/72 8/58 in an α-olefin such as 3-cyclohexyl-1-propene (allyl cyclohexane) and vinyl cyclohexane. Although not α-olefins in the classic sense of the term, for the purposes of this disclosure certain cyclic olefins, such as norbornene and related olefins, particularly 5-ethylidene-2norbornene, are α-olefins and can be used in place of some or all α-olefins described above. Similarly, styrene and its related olefins (for example, α-methyl-styrene, etc.) are α-olefins for the purposes of this disclosure. Illustrative ethylene polymers include copolymers of ethylene / propylene, ethylene / butene, ethylene / 1hexene, ethylene / 1-octene, ethylene / styrene, and the like. Illustrative terpolymers include ethylene / propylene / butene, ethylene / butene / 1-octene, ethylene / propylene / diene monomer (EPDM) and ethylene / butene / styrene terpolymers. Copolymers can be random or in blocks. [0032] In an embodiment, the ethylene-based polymer is a high density polyethylene. When used here, the term “high density polyethylene (or HDPE) is an ethylene-based polymer having a density greater than or equal to 0.941 g / cm 3 . A non-limiting example of an appropriate HDPE is 1245N obtainable from The Dow Chemical Company, Midland, Michigan. [0033] In an embodiment, HDPE has a density of 0.941 g / cm 3 to 0.970 g / cm 3 , and / or a crystallinity of at least 55%, and / or a melting temperature of at least 125 ° C , and / or a melt index (MI) of 1.0 g / 10 min at 20.0 g / 10 min. [0034] In an embodiment, HDPE has a density of 0.950 g / cm 3 , and a melt index (MI) of 12.0 g / 10 min. Petition 870190115675, of 11/11/2019, p. 18/72 9/58 [0035] When used here, the sum weight is the combined weight of component (A) plus the weight of component (B). The sum-weight is a measure to evaluate component (A) with respect to component (B) and vice versa. In other words, the sum-weight excludes component (C) and optional components (D) and (E). In an embodiment, the sum-weight contains more than 50% by weight, or more than 60% by weight, or more than 70% by weight of component (A). [0036] The ethylene-based polymer may comprise two or more incorporations disclosed herein. (C) Block composite [0037] The present polymeric composition contains a block composite. The block composite includes: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin based polymer; and (III) a block copolymer comprising a propylene-based crystalline block and an ethylene / α-olefin block. [0038] The term block copolymer or segmented copolymer refers to a polymer comprising two or more chemically distinct regions or segments (referred to as blocks) preferably joined in a linear fashion, that is, a polymer comprising chemically differentiated units that end up together -to-extreme with respect to polymerized ethylene functionality, rather than in pendant or grafted mode. In an incorporation, the blocks differ in the amount or type of comonomer incorporated in each of them, density, amount of crystallinity, size of crystallite attributable to a polymer of such composition, the type or degree of tacticity (isotactic or syndiotactic), regularity or regality -regularity, the amount of Petition 870190115675, of 11/11/2019, p. 19/72 10/58 branching, including long chain branching or hyper-branching, homogeneity, or any other chemical or physical property. The block copolymers of the present disclosure are characterized by unique polymer polydispersion distributions (PDI or Mw / Mn), block length distribution, and / or distribution of number from bl hollow due, in a preferred embodiment, to It is made From exchange agents in combination with the catalysts . [0039] a block composite is a new polymer understanding a soft copolymer, a hard copolymer and one block copolymer having a soft segment and a hard segment, the hard segment of the block copolymer having the same composition as the hard polymer in the block composite and the soft segment of the block copolymer having the same composition as the soft copolymer of the composite composite blocks. The block copolymer can be linear or branched. More specifically, when produced in a continuous process, the block composite desirably has a PDI of 1.7 to 15, or 1.8 to 3.5, or 1.8 to 2.2, or 1.8 to 2.1. When produced in a batch or semi-batch process, the block composite has PDI of 1.0 to 2.9, or 1.3 to 2.5, or 1.4 to 2.0, or 1, 4 to 1.8. [0040] Hard segments refer to very crystalline blocks of polymerized units in which the monomer is present in an amount greater than 95 percent by weight, and preferably greater than 98 percent by weight. In other words, the comonomer content in the hard segments is less than 5 weight percent, and preferably less than 2 weight percent. In some incorporations, the hard segments Petition 870190115675, of 11/11/2019, p. 20/72 11/58 comprise all or substantially all of the propylene units. On the other hand, soft segments refer to amorphous, substantially amorphous or elastomeric blocks of polymerized units in which the comonomer content is greater than 10 mol%. Block composite index [0041] The present examples (Tables 3 and 4) show that insoluble fractions contain an appreciable amount of ethylene which would not otherwise be present if the polymer were simply a mixture of iPP homopolymer and EP copolymer. To explain this extra ethylene, a mass balance calculation can be performed to estimate a block composite index of the amount of soluble and insoluble fractions in xylene and the percentage by weight of ethylene present in each of the fractions. [0042] A sum of the ethylene weight percentage of each fraction according to equation 1 results in an overall ethylene weight percentage (in the polymer). This mass balance equation can also be used to quantify the quantity of each component in a binary mixture or extended to a ternary mixture or mixture of n components. % On total weight insoluble C2 W (% by weight insoluble C2) + w soluble (wt% C2-soluble) Eq. 1 [0043] Applying equations 2 to 4, the quantity of the soft block (providing the source of extra ethylene) present in the insoluble fraction is calculated. By substituting the% by weight of C 2 of the insoluble fraction in the member to the left of equation 2, one can calculate the% by weight of hard iPP and the% by weight of soft EP using equations 3 and 4. Note that the% in ethylene weight Petition 870190115675, of 11/11/2019, p. 21/72 12/58 in the soft EP is adjusted to be equal to the% by weight of ethylene in the xylene-soluble fraction. The% by weight of ethylene in the iPP block is set to zero or if differently known from your DSC melting point or other composition measure, the value can be put in place. % by weight of global C2 or insoluble in xylene w iPP hard (% by weight of C2 opp) + soft wep (% by weight of C2ep mole) Eq. 2 1. W iPP hard p e s O of global C2 or insoluble in xylene% by weight of soft C2EP % by weight of C 2 Hard iPP -% by weight of C 2EP soft Eq. 3 W soft EP = 1 - w hard IPP Eq. 4 [0044] After explaining the additional ethylene present in the fraction insoluble, the only way to have one EP copolymer present in the insoluble fraction, the polymeric EP chain must be connected in an ipp polymer block (or else it would have been extracted in the xylene insoluble fraction). Therefore, when the ipp block crystallizes, it prevents the Ep block from solubilizing. [0045] To estimate the composite index in blocks, the relative quantity of each block must be taken into account. To approach this, the ratio between the soft EP and the hard iPP is used. The ratio of the soft EP polymer and the hard iPP polymer can be calculated using Equation 2 of the total ethylene mass balance measured in the polymer. Alternatively, it can also be estimated from a mass balance of monomer and comonomer consumption during polymerization. Table 3 refers to the estimated ratio of iPP and EP present in the diblock copolymer for all experiments. It is calculated Petition 870190115675, of 11/11/2019, p. 22/72 13/58 the weight fraction of the hard iPP and the weight fraction of the soft EP using Equation 2 and it is assumed that the hard iPP does not contain any xylene. The% by weight of ethylene in the soft EP is the amount of ethylene present in the fraction soluble in xiiene. [0046] For example, if a block composite of the invention (C) composed of iPP (C) (I), EP (C) (II) and iPP / EP (C) (III) diblock contains a total of 47 % by weight of C 2 and is prepared under conditions to produce a soft EP polymer with 67% by weight of C2 and an iPP homopolymer containing zero ethylene, the amount of soft EP and hard iPP will be, respectively, 70% by weight and 30% by weight (calculated using Equations 3 and 4). If the percentage of EP is 70% by weight and that of iPP is 30% by weight, the relative ratio of the EP: iPP blocks can be expressed as 2.33: 1. [0047] Hence, if someone skilled in the art performs an xylene extraction of the polymer and recovers 40% by weight of insoluble and 60% by weight of soluble, this will be an unexpected result and this would lead to the conclusion that a fraction of block copolymer inventive was present. If the ethylene content of the insoluble fraction is subsequently measured to be 25% by weight of C2, Equations 2 to 4 can be solved to explain this additional ethylene and will result in 37.3% by weight of soft EP polymer and 62 , 7% by weight of hard iPP polymer. [0048] Since the insoluble fraction contains 37.3 wt% EP copolymer, it can be linked to an additional 16 wt% iPP polymer, based on the EP: iPP block ratio of 2, 33: 1. This leads to the estimated amount of diblocks in the insoluble fraction to be 53.3% by weight. For the entire polymer (unfractionated), the composition Petition 870190115675, of 11/11/2019, p. 23/72 14/58 as being 21.3% by weight of iPP / EP diblocks, 18.7% by weight of iPP polymer, and 60% by weight of EP polymer. Since the compositions of these polymers are new, the term “composite composite index (or“ BCI) is defined here as equal to the percentage of diblock weight divided by 100% (ie, weight fraction). The value of the composite index in diblocks can vary from 0 to 1, where 1 would equal 100% of inventive diblocks and zero would be a material such as a random copolymer or traditional mixture. For the example described above, the block composite index for the block composite is 0.213. For the insoluble fraction, the BCI is 0.533, and for the soluble fraction the BCI is zero. [0049] Depending on the estimates made of the total polymeric composition and the error in the analytical measures that are used to calculate the composition of the hard and soft blocks, an error between 5 and 10% in the computed value of the composite composite index is possible. Such estimates include the% by weight of C2 in the hard iPP block measured from the DSC melting point, NMR analysis, or process condition; the estimated% by weight of C2 in the soft block estimated from the composition of the soluble in xylene, either by NMR, or by DSC melting point of the soft block (if detected). But in general, calculating the composite composite index reasonably explains the unexpected amount of “additional ethylene present in the insoluble fraction, the only way to have a EP copolymer present in the insoluble fraction, the EP polymer chain must be linked to a iPP polymer block (or else s would have been extracted in the xylene-soluble fraction). [0050] The block composite polymers of the present disclosure are prepared by a process comprising Petition 870190115675, of 11/11/2019, p. 24/72 Contacting a monomer polymerizable by addition or mixing of monomers under conditions of addition polymerization with a composition comprising at least one addition polymerization catalyst, a cocatalyst and a chain exchange agent, said process being characterized by formation of at least part of the growing polymer chains in different process conditions in two or bad reactors operating under steady state polymerization conditions or in two or more zones of a reactor operating under continuous polymerization conditions. [0051] In an embodiment, the block composite comprises a fraction of the block polymer that has a very likely distribution of block lengths. Preferred polymers according to the present disclosure are block copolymers containing 2 or 3 blocks or segments. In a polymer containing three or more segments (i.e., blocks separated by a distinguishable block) each can be chemically the same or different and generally characterized by a distribution of properties. In a process to prepare the polymers, exchange agent is used as a way to extend the average life of a polymer chain such that a substantial fraction of the polymer chains leave at least the first reactor in a series of multiple reactors or the first zone in a multizone reactor operating substantially under continuous flow conditions in the form of polymer terminated with a chain exchange agent, and the polymeric chain experiences different polymerization conditions in the polymerization zone or in the next reactor. Different polymerization conditions in the respective reactors or zones include the use of different monomers, Petition 870190115675, of 11/11/2019, p. 25/72 16/58 comonomer, or monomer / comonomer ratios, different polymerization temperatures, pressures or partial pressures of various monomers, different catalysts, different monomer gradients, or any other difference that leads to the formation of a distinguishable polymeric segment. Thus, at least a portion of the polymer comprises two, three or more, preferably two or three differentiated polymer segments arranged in an intermolecular manner. [0052] The following mathematical treatment of the resulting polymers is based on the theoretically derived parameters that are believed to apply and demonstrate that, especially in two or more stationary states, continuous reactors or zones connected in series, having different polymerization conditions to which they are exposed the growing polymer, the polymer block lengths being formed in each reactor or zone will be in accordance with a very likely distribution derived from the following way, in which pi (π) is the probability of polymer propagation in a reactor with respect to the sequences of catalyst blocks i. The theoretical treatment is based on standardized methods and hypotheses known in the art and used to predict the effects of polymerization kinetics on molecular architecture, including the use of mass reaction rate expressions that are not affected by block lengths or chains, and the hypothesis that polymeric chain growth is completed in a very short time compared to the average reactor dwell time. Such methods were previously disclosed in W.H. Ray, J. Macromol. Sci., Rev. Macromol. Chem., C8, 1 (1972) and in A.E. Hamielec and J.F. MacGregor, “Polymer Reaction Engineering, Petition 870190115675, of 11/11/2019, p. 26/72 17/58 K.H. Reichert and W. Geisler, Eds., Hanser, Munich, 1983. Furthermore, it is assumed that each incidence of the chain exchange reaction in a given reactor results in the formation of a single polymeric block, while the transfer of the polymer terminated by chain exchange agent for a different reactor or zone and exposure to different polymerization conditions results in the formation of a different block. For the catalyst i, The fraction of strings in length n being produced at the reactor is given by Xi [n] , where n it is a number all in 1 to infinity representing the number total of monomeric units in the block. Xi [n] = (1-pi) pi (n-1) very likely distribution of block lengths Ni = 1/1-pi numerical average block length [0053] If more than one catalyst is present in a reactor or zone, each catalyst will have a propagation probability (pi) and therefore will have a single average block length and distribution for polymer being made in that reactor or zone. In a most preferred embodiment, the probability of propagation is defined as: pi = Rp [i] / Rp [i] + Rt [i] + Rs [i] + [Ci] for each catalyst i = {1,2, ...}, where Rp [i] = local consumption rate monomer by catalyst i, (mol / L / time); Rt [i] = total chain transfer and termination rate for catalyst i, (mol / L / time); and Rs [i] = local rate of chain transfer with inactive polymer (mol / L / time). [0054] For a given reactor, the polymer propagation rate, Rp [i], is defined using an apparent rate constant, Petition 870190115675, of 11/11/2019, p. 27/72 18/58 kpi, multiplied by a total concentration of monomers, [M], and multiplied by the local concentration of catalyst i, [C i ] as follows: Rp [i] = kpi [M] [Ci] [0055] The chain transfer, termination, and exchange rate is determined as a function of chain transfer to hydrogen (H2), beta hydride elimination, and transfer of chain to chain exchange agent (CSA). The quantities [H2] and [CSA] are concentrations molars and each heat k subscribed is rate constant to reactor or zone: Rt [i] = kH 2 i [H 2 ] [Ci] + kpi [Ci] + kai [CSA] [Ci] [0056] Chains are created polymeric inactive when a polymer portion is transferred to a CSA and all reacting CSA portions are supposed to each be paired with an inactive polymer chain. The transfer rate of inactive polymer chain with catalyst i is given as follows, where [CSAf] is the feed concentration of CSA, and the amount ([CSAf] - [CSA]) represents the concentration of inactive polymer chains : Rs [i] = kai [Ci] ([CSAf] - [CSA]) [0057] As a result of the previous theoretical treatment, it can be seen that the overall block length distribution of the resulting block copolymer is the sum of the distribution block length given previously by Xi [n], influenced by the rate of local polymer production for catalyst i. This means that a polymer prepared in at least two different polymer forming conditions will have at least two distinguishable blocks or segments, each having a very Petition 870190115675, of 11/11/2019, p. 28/72 Likely 19/58 block length. [0058] Catalysts and catalyst precursors suitable for producing the composite in blocks (C) include metal complexes as disclosed in WO2005 / 090426, in particular those disclosed starting on page 20, line 30 through page 53, line 20, which here it is incorporated by reference. Suitable catalysts are also disclosed in US 2006/0199930, US 2007/0167578, US 2008/0311812, US 7,355,089, or WO 2009/012215, which are incorporated herein by reference with respect to catalysts. Suitable cocatalysts are those disclosed in WO 2005/090426, in particular those disclosed on page 19, line 21 through page 20, line 12, which is incorporated herein by reference. Particularly preferred chain exchange agents are dialkyl zinc compounds. [0059] The block polymers of the block composite comprise in polymerized form propylene and ethylene and / or one or more comonomers of C 4-20 α-olefins, and / or one or more additional copolymerizable comonomers or they comprise 4methyl-1 -pentene and ethylene and / or one or more C4-20 αolefin comonomers, or they comprise 1-butene and ethylene, propylene and / or one or more C 5-20 α-olefin comonomers and / or one or more additional copolymerizable comonomers. Additional suitable comonomers are selected from diolefins, cyclic olefins, and cyclic diolefins, halogenated vinyl compounds, and aromatic vinylidene compounds. [0060] The comonomer content in the resulting composite block polymers can be measured using any appropriate technique, with techniques based on spectroscopy being preferred. Petition 870190115675, of 11/11/2019, p. 29/72 20/58 nuclear magnetic resonance (NMR). It is highly desirable that some or all of the polymeric blocks comprise amorphous or relatively amorphous polymers such as copolymers of propylene, 1-butene or 4-methyl-1-pentene and a comonomer, especially random copolymers of propylene, 1-butene or 4-methyl -1-pentene with ethylene, and any remaining polymeric blocks (hard segments), if any, comprise predominantly propylene, 1-butene or 4-methyl1-pentene in polymerized form. Preferably such segments are of very crystalline or stereospecific polypropylene, polybutene or poly (4-methyl-1-pentene), especially isotactic homopolymers. [0061] Preferably still, the block copolymers of the present disclosure comprise 10 to 90 percent crystalline or relatively hard segments and 90 to 10 percent amorphous or relatively amorphous segments (soft segments), preferably 20 to 80 percent percent crystalline or relatively hard segments and 80 to 20 percent amorphous or relatively amorphous segments (soft segments), most preferably 30 to 70 percent crystalline or relatively hard segments and 70 to 30 percent amorphous or relatively amorphous (soft segments). Within the soft segments, the molar percentage of comonomer can vary from 10 to 90 molar percent, preferably from 20 to 80 molar percent, most preferably from 33 to 75 molar percent. In the case where the comonomer is ethylene, preferably it is present in an amount of 10 molar percent to 90 molar percent, more preferably 20 molar percent to 80 molar percent, and most preferably 33 molar percent to 75 percent Petition 870190115675, of 11/11/2019, p. 30/72 21/58 molar. Preferably, the copolymers comprise hard segments that are from 90 mol% to 100 mol% of propylene. The segments can be more than 90 mole percent, preferably more than 93 mole percent and more preferably more than 95 mole percent propylene, and much preferably more that 98 per percent mol air of propylene. Such segments hard have points in Fusion corresponding with values bigger or equals The 80 ° C, preferably greater or equal to 100 ° C, more preferably bigger or equal to 115 ° C, and much preferably greater than or equal to 120 ° C. Preferably, the block copolymers of the present disclosure comprise 10 to 90 percent crystalline or relatively hard segments and 90 to 10 percent amorphous or relatively amorphous segments (soft segments). Within the soft segments, the molar percentage of comonomer can vary from 5 to 90 mole percent, preferably from 10 to 60 mole percent. In the case where the comonomer is ethylene, it is preferably present in an amount of 10% by weight to 75% by weight, more preferably from 30% by weight to 70% by weight. [0062] Preferably, the copolymers comprise hard segments that are from 80% by weight to 100% by weight of propylene. The hard segments can be more than 90% by weight, preferably more than 95% by weight and more preferably more than 98% by weight of propylene. [0063] The block composite polymers of the present disclosure can be differentiated from conventional random copolymers, physical mixtures of polymers, and from block copolymers prepared via sequential addition of Petition 870190115675, of 11/11/2019, p. 31/72 22/58 monomers. Block composites can be differentiated from random copolymers by characteristics such as higher melting temperatures for a comparable amount of comonomer, block index and block composite index, as described below; of a physical mixture for characteristics such as block index, block composite index, better tensile strength, improved fracture resistance, finer morphology, improved optics, and greater impact resistance at lower temperature; block copolymers prepared by sequential addition of monomers by molecular weight distribution, rheology, shear decrease, rheology ratio, and the fact that there is block polydispersity. [0064] In some embodiments, the block composites of the present disclosure have a block composite index (BCI), defined below, which is greater than zero, but less than about 0.4 or about 0.1 to about 0.3. In other incorporations, BCI is greater than about 0.4 and even about 1.0. In addition, the BCI can be in the range of about 0.4 to about 0.7, about 0.5 to about 0.7, or about 0.6 to about 0.9. In some incorporations, BCI is in range in fence in 0.3 to fence 0.9, about of 0.3 about 0, 8, or of about 0.3 The about 0.7, from fence from 0.3 to about 0.6, in fence in 0, 3 to about 0.5, or of about 0.3 The fence in 0.4. In other incorporations, BCI is in range in fence in 0.4 to fence 1.0, about of 0.5 about 1, 0, or of about 0.6 The about 1.0 of fence from 0.7 to about 1.0, in fence in 0, 8 to about 1.0, or of about 0.9 to about 1.0. [0065] Other desirable compositions according to Petition 870190115675, of 11/11/2019, p. 32/72 The present disclosure is elastomeric copolymers in blocks of propylene, 1-butene or 4-methyl-1-pentene with ethylene, and optionally one or more α-olefins or diene monomers. The preferred α-olefins for use in this embodiment of the present disclosure are designated by the formula CH2 = CHR *, where R * is a linear or branched alkyl group of 1 to 12 carbon atoms. Examples of suitable α-olefins include, but are not limited to, isobutylene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene (when copolymerized with propylene), and 1-octene. Dienes suitable for use in the preparation of such polymers, especially polymers of the EPDM type in multiblocks include conjugated and unconjugated, normal or branched chain, cyclic or polycyclic dienes containing from 4 to 20 carbon atoms. Preferred dienes include 1,4-pentadiene, 1,4-hexadiene, 5-ethylidene-2-norbornene, dicyclopentadiene, cyclohexadiene, and 5-butylidene-2-norbornene. A particularly preferred diene is 5-ethylidene-2-norbornene. The resulting product may comprise segments of isotactic homopolymer alternating with segments of elastomeric copolymer, prepared at the site during polymerization. Preferably, the product may comprise only the elastomeric block copolymer of propylene, 1-butene or 4-methyl-1-pentene with one or more comonomers, especially ethylene. [0066] Since polymers containing diene contain alternating segments or blocks containing greater or lesser amounts of diene (including no amount) and olefin (including none), the total amount of diene and α-olefin can be reduced without loss of properties subsequent polymeric reactions. That is, like the diene monomers Petition 870190115675, of 11/11/2019, p. 33/72 24/58 and α-olefin are preferably incorporated into a type of polymer block rather than uniformly or randomly throughout the polymer, they are used more efficiently and subsequently the crosslinking density of the polymer can be better controlled. Such crosslinkable elastomers and cured products have advantageous properties, including greater tensile strength and better elastic recovery. [0067] In an embodiment, the block composite has an average molecular weight (M w ) from 10,000 to about 2,500,000, preferably from 35,000 to about 1,000,000 and more preferably from 50,000 to about 300,000, preferably from 50,000 to about 200,000. The block composite (C) is disclosed in the copending US patent application No. 61 / 248,160 filed on October 2, 2009, all the content of which is incorporated by reference. (II) Crystalline block composite [0068] The block composite (C) can be a crystalline block composite. The term “crystalline block composite (CBC) refers to a new polymer comprising a crystalline ethylene-based polymer (CEP), a crystalline alpha-olefin-based polymer (CAOP), and a block copolymer having a block crystalline ethylene (CEB) and a crystalline alpha-olefin block (CAOB), the CEB of the block copolymer having essentially the same composition as the CEP of the block composite and the CAOB of the block copolymer having essentially the same composition as the CAOP of the composite block. Block copolymers can be linear or branched. More specifically, each of the respective block segments may contain long chain branches of similar composition to the respective block, but the Petition 870190115675, of 11/11/2019, p. 34/72 25/58 block copolymer segment is substantially linear as opposed to containing grafted or branched blocks. When produced in a continuous process, crystalline block composites desirably have a PDI of 1.7 to 15, preferably 1.8 to 5, more preferably 1.8 to 3.5, and most preferably 1.8 to 2.5. [0069] CAOB refers to very crystalline blocks of polymerized alpha-olefin units in which the monomer is present in an amount greater than 90 mol%, preferably greater than 93 mol%, more preferably greater than 95 mol%, and preferably greater than 96 molar percent. In other words, the comonomer content in CAOBs is less than 10 molar percent, and preferably less than 7 molar percent, and more preferably less than 5 molar percent, and most preferably less than 4 molar percent. Such CAOBs have corresponding melting points that are greater than or equal to 80 ° C, preferably greater than or equal to 100 ° C, more preferably greater than or equal to 115 ° C, and most preferably greater than or equal to 120 ° C. In some incorporations, CAOB comprises all or substantially all of the propylene units. On the other hand, CEB refers to blocks of polymerized ethylene units in which the comonomer content is less than or equal to 10 mol%, preferably between 0 mol% and 10 mol%, more preferably between 0 mol% and 7 mol% and, most preferably, between 0 mol% and 5 mol%. Such CEB has corresponding melting points which are preferably greater than or equal to 75 ° C, more preferably greater than or equal to 90 ° C, and most preferably greater than or equal to 100 ° C. Petition 870190115675, of 11/11/2019, p. 35/72 26/58 [0070] Preferably, the crystal block composite polymers of the present disclosure comprise from 0.5 to 94% by weight of CEP, from 0.5 to 94% by weight of CAOP and from 5 to 99% by weight block copolymer. More preferably, crystalline block composite polymers comprise from 0.5 to 79% by weight of CEP, from 0.5 to 79% by weight of CAOP and from 20 to 99% by weight of block copolymer and more preferably, from 0.5 to 49% by weight of CEP, from 0.5 to 49% by weight of CAOP and from 50 to 99% by weight of block copolymer. [0071] Preferably, the block copolymers of the present disclosure comprise from 5 to 95% by weight of crystalline ethylene blocks (CEP) and from 95 to 5% by weight of crystalline alpha-olefin blocks (CAOB). They can comprise from 10% by weight to 90% by weight of CEB and from 90% by weight to 10% by weight of CAOB. More preferably, the block copolymers comprise from 25 to 75% by weight of CEB and from 75 to 25% by weight of CAOB, and even more preferably they comprise from 30 to 70% by weight of CEB and from 70 to 30% by weight. CAOB weight. [0072] In some embodiments, the block composites of this disclosure have a crystalline block composite index (CBCI), defined below, which is greater than zero, but less than about 0.4 or about 0.1 to about 0.3. In other incorporations, CBCI is greater than about 0.4 and even about 1.0. In addition, CBCI can be in the range of about 0.4 to about 0.7, about 0.5 to about 0.7, or about 0.6 to about 0.9. In some incorporations, CBCI is in the range of about 0.3 to about 0.9, about 0.3 to about 0.8, or about 0.3 to about 0.7, about from 0.3 to about 0.6, from about 0.3 to about 0.5, Petition 870190115675, of 11/11/2019, p. 36/72 27/58 or from about 0.3 to about 0.4. In other incorporations, CBCI is in the range of about 0.4 to about 1.0, about 0.5 to about 1.0, about 0.6 to about 1.0, about 0.7 to about 1.0, about 0.8 to about 1.0 or about 0.9 to about 1.0. [0073] Still preferably, crystalline block composites of this embodiment of the present disclosure have a weight average molecular weight (Mw) of 1,000 to about 2,500,000, preferably from 35,000 to about 1,000,000 and more preferably from 50,000 to 500,000, from 50,000 to about 300,000, and preferably from 50,000 to about 200,000. The crystalline block composite and the crystalline composite index index (CBCI) are disclosed in the copending US patent application No. 61 / 356,978 filed on June 21, 2010, all the content of which is incorporated by reference . [0074] In an embodiment, the block composite (C) includes isotactic crystalline propylene homopolymer, or iPP (C) (I), ethylene / propylene copolymer, or EP (C) (II), and block copolymer (C ) (III). The block copolymer subcomponent (C) (III) includes a diblock with the formula (1) below. (EP) - (iPP) (1) [0075] The term EP represents a segment of polymerized ethylene and propylene monomer units. The term iPP represents an isotactic propylene homopolymer segment or a substantially isotactic propylene homopolymer segment with minimal (<1%) atactic or syndiotatic defects. Petition 870190115675, of 11/11/2019, p. 37/72 28/58 [0076] In an embodiment, the block composite (C) has an ethylene content greater than 20% by weight, or greater than 30% by weight, or greater than 35% by weight. The weight percentage of ethylene is based on the total weight of the block composite (C). [0077] In an embodiment, component (C) (III) is present in an amount greater than 15% by weight, or greater than 20% by weight, or greater than 25% by weight, or greater than 30% by weight, or greater than 50% by weight to about 80% by weight, based on the total weight of component (C). [0078] In an embodiment, the block composite (component C) has a density of 0.865 to 0.90 g / cm3, or 0.897 g / cm 3 and / or a melting index (I2) of 1 to 50 g / 10 min [0079] In an embodiment, the C block composite has a melt index of about 1, or about 2, or about 3, or about 4, or about 5, or about 6 at about 40, or about 35, or about 20, or about 15, or about 13 g / 10 min. [0080] In an embodiment, the C block composite has I10 / I2 of about 6, or about 7, or from about 8 to about 20, or about 19, or about 17, or about 17, or about 15, or about 13, or about 12, or about 11. D. Olefin-based polymer [0081] The present polymeric composition can optionally include an olefin-based polymer. Non-limiting examples of suitable olefin-based polymers include propylene-based polymer and ethylene-based polymer. Non-limiting examples of suitable ethylene-based polymer include linear low density polyethylene (LLDPE), low density polyethylene (LDPE), Petition 870190115675, of 11/11/2019, p. 38/72 29/58 HDPE, homogeneously branched polyethylene (non-limiting examples include polymers sold under the trade name EXXACT by ExxonMobil and under the trade name TAFMER by Mitsui), substantially linear ethylene polymer (non-limiting examples include polymers sold under the trade names AFFINITY and ENGAGE de The Dow Chemical Company), functionalized olefin-based polymer, and any combination thereof. [0082] A substantially linear ethylene / α-olefin interpolymer (SLEP) is a homogeneously branched polymer and is described in US Patent Nos. 5,272,236, 5,278,272, 6,054,544, 6,335,410 and 6,723,810, each of which is incorporated by reference. The substantially linear ethylene / α-olefin interpolymers have long chain branching. The long chain branches have the same comonomer distribution as the polymeric main chain, and can be approximately the same length as the length of the polymeric main chain. Typically, substantially linear refers to a polymer that is replaced, on average, with 0.01 long chain branch per 1000 carbons to 3 long chain branch per 1000 carbons. The length of a long chain branch is greater than the length of carbons of a short chain branch, formed by the incorporation of a comonomer in the polymeric main chain. [0083] Some polymers can be substituted with 0.01 long chain branch per 1000 total carbons to 3 long carved branches per 1000 total carbons, more preferably from 0.05 long chain branch by 1000 total carbons to 2 carved branches long per 1000 Petition 870190115675, of 11/11/2019, p. 39/72 30/58 total carbons, and especially from 0.3 long chain branch per 1000 total carbons to 1 long branch branch per 1000 total carbons. [0084] The substantially linear ethylene / α-olefin interpolymers form a unique class of homogeneously branched ethylene polymers. They differ substantially from the well-known homogeneously conventional branched linear ethylene / α-olefin interpolymers class, as discussed above, and furthermore, they are not in the same class as the linear heterogeneous “ethylene polymers polymerized by conventional heterogeneous Ziegler-Natta catalyst. (for example, ultra low density polyethylene (ULDPE), linear low density polyethylene (LLDPE) or high density polyethylene (HLDPE), prepared, for example, using the technique disclosed by Anderson et al., in US patent no. 4,076,698); nor are they in the same class as highly branched polyethylene initiated via free radicals, high pressure, such as, for example, low density polyethylene (LDPE), ethylene / acrylic acid (EAA) copolymers and ethylene / vinyl acetate copolymers (EVE). [0085] The substantially linear homogeneously branched ethylene / α-olefin interpolymers useful in the invention have excellent processability, although they have a relatively narrow molecular weight distribution. Surprisingly, the melt flow rate (Ii 0 / I 2 ) according to ASTM D 1238, of the substantially linear ethylene interpolymers can vary widely, and is essential and regardless of the molecular weight distribution (M w / M n or MWD) . This surprising behavior is contrary to that of Petition 870190115675, of 11/11/2019, p. 40/72 31/58 homogeneously conventional branched linear ethylene interpolymers, such as those described, for example, by Elston in US 3,645,992, and the linear polyethylene interpolymers "polymerized by heterogeneously branched Ziegler-Natta, such as those described by Anderson et at US 4,076,698. Unlike substantially linear ethylene interpolymers, linear ethylene interpolymers (whether homogeneously or heterogeneously branched) have rheological properties, such that when the molecular weight distribution increases, the I10 / I2 value also increases. [0086] One can determine long chain branching using nuclear magnetic resonance spectroscopy 13 C (13 C NMR), and it can be quantified using the method of Randall (Rev. Micromol. Chem Phys., 1989, C29 (2 & 3), pages 285-297), The dissemination of which one on here incorporates per reference . Two others methods are chromatography in permeation in gel, coupled with a detector spreading in laser light in low angle (GPC-LALLS), and chromatography in gel permeation, coupled with a differential viscosimetric detector (GPC-DV). The use of these techniques for detecting long chain branching, and the underlying theories, are well documented in the literature. See, for example, Zimm B. H. and Stockmayer, W. H., J. Chem. Phys., 17, 1301 (1949) and Rudin, A., Modern Methods of Polymer Characterization, John Wiley & Sons, New York (1991), pages 103-112. [0087] The olefin-based polymer can include a functionalized olefin-based polymer. Non-limiting examples of suitable functionalized olefin-based polymers include anhydride-grafted polyethylene Petition 870190115675, of 11/11/2019, p. 41/72 32/58 maleic, polypropylene grafted with maleic anhydride, ethylene / acrylic acid copolymer, ethylene / methacrylate copolymer, and any combination thereof. E. Additives [0088] The present polymeric composition may optionally comprise one or more additives. Known additives can be incorporated into the resin composition as long as they do not compromise the objectives of the disclosure. Non-limiting examples of such additives include nucleating agents, antioxidants, acid purgers, thermal stabilizers, light stabilizers, ultraviolet light absorbers, lubricants, antistatic agents, pigments, dyes, dispersing agents, inhibitors, neutralizing agents, foaming agents, plasticizers , fluidity enhancers, nonstick agents, slip additives, and weld strength enhancers. [0089] The aforementioned additives can be used in any combination and each of them can be contained in the respective polymeric compositions in quantities of 0.0001 to 10 percent by weight (or any individual value or subrange of the same) or in an amount from 0.001 to 1.0 per percent in Weight. [0090] The composition polymeric can understand two or more incorporations here disclosed. 2. Film [0091] The present disclosure provides films comprising the present polymeric composition. In other words, the present polymeric composition can be molded into a film. In an embodiment, a film is provided which includes: (A) from 50% by weight to 95% by weight of the interpolymer of Petition 870190115675, of 11/11/2019, p. 42/72 33/58 propylene / a-olefin; (B) from 1% by weight to 30% by weight of the ethylene-based polymer; and (C) from 1% by weight to 30% by weight of the block composite. [0092] Optionally, the film can include olefin-based polymer (D) and / or additives (E). Components (A) - (E) can be any respective components (A) - (E) disclosed above for the polymeric composition. In an embodiment, the film contains from 70% by weight to 80% by weight of component (A), from 10% by weight to 20% by weight of component (B), and from 5% by weight to 15% by weight of component (C). Weight percentages are based on the total weight of the film. The film exhibits one, some, or all of the following properties shown in Table 1 below. Petition 870190115675, of 11/11/2019, p. 43/72 34/58 Table 1 - Film properties Property unity Banner Film thickness thousand 0.3 to 5 Kinetic friction coefficient (F-F)0.15 to 1.2 Static friction coefficient (F-F)0.15 to 1.2 Opacity The % 0.5 to 15 Clarity The % 80 to 99.5 Maximum hot stickiness N / in 3 to 18 Hot tack start temperature (HTIT) ° C 70-150 Maximum hot tack temperature ° C 60 to 140 Hot tack temperature window ° C Wider than 50 ° C, or wider than 55 ° C Hot stickiness resistance N / in 1 to 8 [0093] In order to improve processing and / or to make packaging speed faster, a low coefficient of friction (COF) is desirable. The friction coefficient in Table 1 above is film-by-film friction coefficient. A large hot tack temperature window is advantageous for (I) decreasing the start sealing temperatures, (II) improving the sealing stability at autoclave temperatures (120 ° C to 130 ° C), and (III) making faster processing speeds. A high resistance to hot tackiness at 150 ° C is advantageous for autoclave applications. [0094] The applicant discovered a film with the following desirable combination of properties: low COF, wide hot tack temperature window, low hot tack start temperature, and high hot tack resistance at high temperature. [0095] Furthermore, the present film has properties Petition 870190115675, of 11/11/2019, p. 44/72 35/58 desirable optics: low opacity and high clarity. [0096] In an embodiment, the film of a hot tack temperature (HTIT) below 80 ° C, or below 75 ° C. [0097] The present film can be a single layer film. The present polymeric composition can be molded in one or more layers in a multilayer film. The structure of the mono / multilayer film can be laminated, extruded (casting / sheet), coextruded (casting / sheet), oriented (axially, biaxially, stretch structure, bubble, double bubble, trapped bubble), and a combination thereof. [0098] In an embodiment, the present film is free of crosslinking. When used here, a film is “free of crosslinking when it has a gel content of less than 5% measured according to Method A of ASTM D-2765-84. [0099] In an incorporation, the film has a thickness of about 0.3 mil (millipolch) to about 5.0 mil, or about 3.5 mil. (A) Multilayer film [0100] The present disclosure provides a multilayer film. In an embodiment, a multilayer film is provided that includes a first layer, a second layer, and an optional third layer. The first layer includes: (A) from 50% by weight to 95% by weight of the propylene / α-olefin interpolymer; (B) from 1% by weight to 30% by weight of the ethylene-based polymer; and (C) from 1% by weight to 30% by weight of the block composite. [0101] Weight percentages are based on the total weight of the first layer. Components (A), (B), and (C) can be Petition 870190115675, of 11/11/2019, p. 45/72 36/58 any respective component (A) - (C) disclosed for the present polymeric composition. In an embodiment, the first layer (A) includes a propylene / ethylene copolymer with a density of 0.89 g / cm 3 to 0.92 g / cm 3 and / or from 1 mol% to 12 mol% of units derived from ethylene. The first layer can include optional (D) and (E) components. [0102] In one embodiment, component (B) of the first layer is an HDPE having a density greater than 0.941 g / cm 3 and / or a melting index of 1.0 g / 10 min at 20.0 g / 10 min . [0103] In one embodiment, the first layer of component (C) of the multilayer film comprises (I) iPP, (II) ethylene / propylene copolymer, and (III) a diblock copolymer comprising an iPP block and a block of ethylene / propylene. The density of the block composition (C) is 0.87 g / cm 3 , or 0.875 g / cm 3 to 0.915 g / cm 3 , or 0.92 g / cm 3 . [0104] In an embodiment, the second layer of the multilayer film is composed of an olefin-based polymer. Non-limiting examples of suitable olefin-based polymers include LLDPE, LDPE, homogeneously branched polyethylene, SLEP, HDPE, propylene-based polymer, and any combination thereof. [0105] In an embodiment, the second layer includes from 70% by weight to 99% by weight of olefin-based polymer and from 30% by weight to 1% by weight of functionalized olefin-based polymer. Non-limiting examples of functionalized olefin-based polymers include polyethylene grafted with maleic anhydride, polypropylene grafted with maleic anhydride, ethylene / acrylic acid copolymer, ethylene / methacrylate copolymer, and any combination thereof. Weight percentages are based on the total weight of the second Petition 870190115675, of 11/11/2019, p. 46/72 37/58 layer. [0106] The optional third layer includes a material selected from nylon, poly (ethylene terephthalate) (PET), polypropylene, and any combination thereof. [0107] In an embodiment, the multilayer film is a three-layer film. The first layer is a sealing layer (containing the present polymeric composition), the second layer is a core layer (containing the olefin-based polymer), and the third layer is a lining layer (containing nylon, PET, and / or polypropylene). The sealing layer is an inner layer. The second layer is a core layer. A core layer is a layer located between at least two other layers. In other words, the core layer is not the innermost layer or the outermost layer. The lining layer is an outermost layer. [0108] In an incorporation, the three-layer film has a thickness of 0.3 mil, or 0.5 mil to 3 mil, or 5 mil (millipole). [0109] The present film may comprise two or more incorporations disclosed herein. 3. Articles [0110] The present disclosure provides articles comprising at least one component formed by the present polymeric composition. In other words, the present polymeric composition can be shaped into articles. The present polymeric composition and / or the present film can be molded into a finished article of manufacture by any of a number of conventional processes and apparatus. Illustrative processes include, but are not limited to, extrusion, calendering, injection molding, and / or compression molding. Per Petition 870190115675, of 11/11/2019, p. 47/72 For example, articles can be prepared by injection molding, extrusion, extrusion followed by thermoforming, low pressure molding, compression molding, and the like. Non-limiting examples of suitable articles include extruded profiles (single or multilayer films), foams, sealing strips, belts, hoses, wire and cable coatings, tubes, floor materials, gaskets, molded products, sheets, and parts extruded. Additional items include automotive parts (for example, instrument panels and window seals), computer parts, building materials, appliances, toys, shoe components, labels and tags, cardboard such as milk carton, sachets, bags, pouches, sealed bags or sausage and / or meat wrap, dry food packages such as for cereal, sugar, flour, etc., thermoformed multilayer films, blister packs, and pharmaceutical packaging films. (A) Autoclave pouch [0111] In an embodiment, the article is a flexible container containing the present polymeric composition. Referring to the drawings, and initially to Figure 1, an article form is an autoclave pouch and is shown and usually indicated by reference number 10. When used here, an autoclave pouch is a flexible packaging that can remain hermetically sealed after exposure at temperatures of 120 ° C135 ° C and pressure of up to 500 kPa for 30-80 minutes. The autoclave bag 10 includes two sheets 12A and 12B of a multilayer film, joined and sealed together in their respective peripheries by a thermal closure 14. The thermal closure 14 can Petition 870190115675, of 11/11/2019, p. 48/72 39/58 extend across the entire common periphery of sheets 12A, 12B. Alternatively, the thermal closure 14 can extend over a portion of the common leaf periphery 12A, 12B and within the thermal closure 14. The storage space 16 is isolated from the surrounding environment and contains the contents 18 of the autoclave pouch, for example, foodstuffs. Although the package is described as having two sheets 12A, 12B, it is understood that a single sheet can be used. The single sheet can be folded over itself to form the two layers. The three unconnected edges would then be heat sealed after the contents were placed between the folded layers. [0112] The sheets 12A, 12B of the retort pouch 10 can be manufactured with the two-layer film structure shown in Figure 2. An outer layer 20 is further from the packaging contents 18. In an embodiment, the outer layer corresponds to the second layer of film described above. [0113] A sealing layer 22 is immediately adjacent to the outer layer 20. Sealing layer 22 (or the innermost layer, or the contact layer with the contents of the autoclave bag) is composed of the present polymeric composition. The outer layer 20 and the sealing layer 22 can be coextruded directly with each other. Alternatively, an adhesive layer 24 can connect the outer layer 20 to the sealing layer 22 as shown in Figure 2. The film-to-film contact under heat and pressure of opposite sealing layers 24 forms a thermal seal 14. [0114] In an embodiment, the autoclave bag 10 is an autoclave bag that is free from folding or substantially free Petition 870190115675, of 11/11/2019, p. 49/72 40/58 bending. [0115] In one embodiment, an autoclave bag 100 is made with a three-layer film as shown in Figure 3. The autoclave bag 100 is similar to the autoclave bag 10 except that the retort bag 100 is made with a film three-layer, not with a two-layer film. The sealing layer 22 contacts the layer 20. A lining layer 26 contacts the layer 20. The contact between layers can be direct (intimate and / or immediate touch) or indirect (intermediate adhesive layer and / or intermediate structure between layers of film) . In this configuration, layer 20 (corresponding to the second film layer described above) becomes a core layer. Layer 26 is the outermost layer and corresponds to the third layer of the film described above. [0116] The thickness of the layers 22, 20, and 26 can to be at same or different.[0117] In an incorporation, the layer sealant 22 is coextruded to core layer 20. The layer in lining 26 is coextruded to the core layer 20. Each of the sealing layer 22 and the lining layer 26 is in direct and intimate contact with the layer 20. In other words, there are no intermediate layers between the sealing layer 22 and the core layer 20. Similarly, there are no intermediate layers between the lining layer 26 and the core layer 20. [0118] In an embodiment, the autoclave bag 10 or the autoclave bag 100 includes a barrier layer. [0119] The 10/100 autoclave bag is designed to withstand a maximum temperature applied in the range of 120 to 135 ° C (or any individual value or sub-range thereof) by Petition 870190115675, of 11/11/2019, p. 50/72 41/58 to 90 minutes without significant degradation. [0120] The autoclave bag is used to secure, protect, or conserve non-limiting items such as food, spices, medicines and sterile solutions. The autoclave bag can be in the form of a pillow, or a flat-bottomed autoclave bag or nameplate. In form and fill packaging, they are formed in line by making bottom and side closures of two films joined in surface contact with each other, adding the material to be preserved, and forming the final closure to wrap the food or other substance to be packaged, all in continuous operation. In general, the resulting autoclave bag is a pillow-shaped bag. Alternatively, the processor may employ prefabricated pouches having a single open end, which are filled and closed or sealed after filling. This technique is best suited for nameplate autoclave bags. In a final step, the autoclave bag and its contents are usually heated to pasteurize, sterilize or cook the contents, such as using an oven or pressurized steam in an autoclave. [0121] The autoclave bag may comprise two or more incorporations disclosed herein. Definitions [0122] All references to the Periodic Table of Elements here will relate to the Periodic Table of Elements published and registered, by CRC Press, Inc., 2003. Likewise, any references to a Group or Groups will be to a Group or Groups shown in this Periodic Table of Elements using the IUPAC system to number groups. Saved Petition 870190115675, of 11/11/2019, p. 51/72 42/58 if stated otherwise, implicit in context, or customary in the technique, all parts and percentages are based on weight and all testing methods are current as of the filing date of this disclosure. For United States patent practice purposes, the contents of any patent, patent application, or publication referred to herein are hereby incorporated by reference in their entirety (or the equivalent US version thereof is also incorporated by reference) especially with respect to the dissemination of synthetic techniques, definitions (to the extent not inconsistent with any definitions provided herein) and general knowledge of the technique. [0123] Any numerical range mentioned here includes all values from the lower value to the upper value, in increments of one unit, as long as there is a separation of at least two units between any lower value and any higher value. As an example, if it is stated that the quantity of a component, or a value of a composition or physical property, such as, for example, quantity of a mixing component, softening temperature, melting index, etc., is between 1 and 100, it is intended that all individual values, such as, 1, 2, 3, etc., and sub-ranges, such as, 1 to 20, 55 to 70, 97 to 100, etc., are expressly listed in this report. For ranges containing values that are less than one, or containing fractional numbers greater than one (for example, 1.1, 1.5, etc.) a unit is considered to be 0.0001, 0.001, 0.01 or 0.1, when appropriate. For ranges containing single digit numbers less than ten (for example, 1 to 5), a unit is typically considered to be 0.1. These Petition 870190115675, of 11/11/2019, p. 52/72 43/58 are only examples of what is specifically intended, and all possible combinations of numerical values between the minimum and maximum values listed will be considered to be expressly established in this patent application. In other words, any numerical range mentioned here includes any value or sub-range within the declared range. Within this disclosure, numerical ranges are provided to, among other things, refer to melt index, melt flow rate, and other properties. [0124] When used herein, the terms mixture and “polymeric mixture mean a mixture of two or more polymers as well as mixtures of polymers with various additives. Such a mixture may or may not be miscible. Such a mixture may or may not be separated by phases. Such a mixture may or may not contain one or more domain configurations, determined from electronic transmission spectroscopy, light scattering, X-ray scattering, and any other method known in the art. [0125] When used herein, the term composition includes a mixture of materials comprising the composition, as well as reaction products and decomposition products formed from the materials of the composition. [0126] The term comprising and its derivatives is not intended to exclude the presence of any additional component, step or procedure, whether or not it is specifically disclosed. In order to avoid any doubt, all compositions claimed through the use of the term comprising may include any additive, adjuvant, or compound, polymeric or not, additional, unless otherwise stated. In contrast, the term, consisting of Petition 870190115675, of 11/11/2019, p. 53/72 44/58 essentially excludes any other component, step or procedure from the scope of any subsequent mention, except those that are not essential to operability. The term “consisting of excludes any component, step or procedure not specifically described or listed. Unless otherwise stated, the term “or refers to members listed individually as well as in any combination. [0127] When used herein, the term “ethylene-based polymer is a polymer that comprises a majority weight percentage of polymerized ethylene monomer (based on the weight of polymer) and, optionally, can comprise at least one polymerized comonomer. [0128] “Hot tack start temperature (HTIT) is the temperature at which hot tack reaches 4 N / inch when the sealing temperature increases. [0129] “Hot tack temperature window or“ delta T is the temperature range in which the hot tack resistance is greater than or equal to 5 N / inch. [0130] The term “olefin-based polymer is a polymer containing, in polymerized form, a majority weight percentage of an olefin, for example, ethylene or propylene, based on the weight of the polymer. Non-limiting examples of olefin-based polymers include ethylene-based polymers and propylene-based polymers. [0131] The term “polymer is a macromolecular compound prepared by polymerizing monomers of the same or different types. “Polymer includes homopolymers, copolymers, terpolymers, interpolymers, and so on. The term “interpolymer means a polymer prepared by polymerizing at least two types of monomers or Petition 870190115675, of 11/11/2019, p. 54/72 45/58 comonomers. It includes, but is not limited to, copolymers (which refers to polymers prepared from two different types of monomers or comonomers), terpolymers (which refers to polymers prepared from three different types of monomers or comonomers), tetrapolymers (which refers to polymers prepared from four different types of monomers or comonomers), and the like. [0132] When used herein, the term propylene-based polymer refers to a polymer that comprises a majority weight percentage of polymerized propylene monomer (based on the weight of the polymer), and optionally can comprise at least one polymerized comonomer . Testing methods [0133] Clarity Clarity is measured according ASTM D 1746. [0134] Friction coefficient is measured coefficient of friction (COF) of films coextruded between films with layer outer (seal) moved against the outer layer (seal) of the expanded film, measured according to ASTM D 1894 at room temperature (23 ° C). A piece of film is kept on a horizontal bed. Another piece of film (approximately 2.5 by 3 inches) is attached to the bottom of a sled, which has been placed over the top of the flat film bed. A TMI monitor / slip and friction analyzer, model 32-06-00, was used to measure COF. The drag speed is 6 inches / min. The forces required to initiate relative motion and to maintain constant motion are recorded and used to obtain coefficient of static friction and kinetic friction coefficient, respectively. Values are an average of 5 Petition 870190115675, of 11/11/2019, p. 55/72 46/58 readings. [0135] Crystallinity - Differential scanning calorimetry (DSC) is used to measure crystallinity of samples based on ethylene (PE) and samples based on propylene (PP). A sample is compressed into a thin film at a temperature of 190 ° C. Weigh about 5 to 8 mg of film sample and place it in a DSC pan. The lid is set into the pan to ensure a closed atmosphere. The sample pan is placed in a DSC cell, and then heated, at a rate of approximately 10 ° C / min, to a temperature of 180 ° C for PE (230 ° C for PP). The sample is kept at this temperature for three minutes. Then, the sample is cooled at a rate of 10 ° C / min to -60 ° C for PE (-40 ° C for PP), and maintained isothermally at that temperature for 3 minutes. Then, the sample is heated at a rate of 10 ° C / min until completely melted (second heating). The percentage of crystallinity is calculated by dividing the heat of fusion (Hf), determined by the second heating curve, by a theoretical heat of fusion of 292 J / g for PE (165 J / g for PP), and multiplying this amount by 100 (for example,% crystallinity = (Hf / 292 J / g) x 100 (for PE)). [0136] Density Density is measured according to ASTM D 792-08. [0137] Opacity is measured opacity according to ASTM D 1003. [0138] Thermal seal resistance thermal seal resistance is measured using Enepay's MAGMA thermal seal and hot tack test system. The films are sealed at specified temperatures, and allowed to cool completely to room temperature (23 ° C). The Petition 870190115675, of 11/11/2019, p. 56/72 47/58 specimens are conditioned at 23 ° C and 50% relative humidity for a minimum of 24 hours before the test. Sample films with thermal closures are prepared in the Examples section below. [0139] Hot tack test [0140] Sample films (prepared in the Examples section below) are measured using an Enepay MAGMA heat seal and tack test system (obtainable from Enepay Corporation, Raleigh, NC), based on ASTM F 1921, method B according to the following conditions: Table 2. Hot stickiness test conditions for coextruded films. Parameter unity Value Specimen width mm 25, 4 Sealing time s 1, 0 Sealing pressure N / mm 2 0. 275 Lag time s 0, 1 Drag speed mm / s 200 [0141] Hot tackiness data is collected in 10 ° C temperature increments. [0142] Melt flow rate (MFR) is measured MFR according to the test method of ASTM D 1238 at 230 ° C with a weight of 2.16 kg. [0143] Melting index (MI) M is measured according to the test method of ASTM D 1238 at 190 ° C with a weight of 2.16 kg. [0144] Melting temperature (Tm) Tm of polymeric samples is measured using differential scanning calorimetry (DSC). A sample is compressed into a thin film at a temperature of 190 ° C. Weigh about 5 to 8 mg of film sample and place it in a DSC pan. The lid is set into the pan to ensure a closed atmosphere. The pot of Petition 870190115675, of 11/11/2019, p. 57/72 The sample is placed in a DSC cell, and then heated, at a rate of approximately 10 ° C / min, to a temperature of 180 ° C for PE (230 ° C for PP). The sample is kept at this temperature for three minutes. Then, the sample is cooled at a rate of 10 ° C / min to -60 ° C for PE (-40 ° C for PP), and maintained isothermally at that temperature for 3 minutes. Then, the sample is heated at a rate of 10 ° C / min until completely melted (second heating). The melting point of a substance is the temperature at which the material changes from a solid to a liquid state. A melting point of a polymer is defined here as the temperature at which the heat of fusion reaches its maximum. [0145] As an illustration and not as a limitation, examples of the present disclosure will now be provided. Examples 1. Polymeric composition [0146] The block composite, component (C) described in paragraphs 82-91 of the copending US patent application No. 61 / 248,160, filed on October 2, 2009, is prepared, all content of which is here is incorporated by reference. [0147] The polymerization conditions are provided for the production of composite examples in blocks 02, 03 and 14 in Table 3 below. Table 4 shows the physical properties of the resulting block composites 02, 03 and 14. [0148] The catalytic system includes catalyst ([[rel2 ', 2' - [(1R, 2R) -1,2-cyclohexanediyl bis (methylene oxikO)] bis [3- (9H-carbazol-9-yl) -5-methyl [1.1'-biphenyl] -2-olatoKO]] hafnium dimethyl) cocatalyst and a mixture of methyl salts of di (alkyl C 8 4- i) borate, ammonium tetrakis (pentafluoro phenyl) prepared by reaction of a Petition 870190115675, of 11/11/2019, p. 58/72 49/58 long-chain trialkylamine (ARMEEN ™ M2HT, obtainable from Akzo-Nobel, Inc.), HCl and Li [B (C6F 5 ) 4 ] as substantially disclosed in USP 5,919,983, Example 2, are purchased from Boulder Scientific and used without further purification. [0149] The catalytic system also includes CSA (diethyl zinc or TEN) and modified methyl aluminoxane purchased from Akzo-Nobel and used without further purification. The solvent for the polymerization reactions is a hydrocarbon mixture (SBP 100/140) obtainable from Shell Chemical Company and purified through 13-X molecular sieve beds before use. Petition 870190115675, of 11/11/2019, p. 59/72 50/58 Table 3A. Process conditions for the production of block composites, Examples 02 and 03. Ex. Food. solvent kg / h Food. propylene, kg / h Food. inethylene, kg / h Food. H2, cm 3 Temp° C Conc.Cat., Ppm Hf Sun stream. of cat., kg / h Conc. of cocat.kg / h Sun stream. cocat., kg / h Flow ofCSA, g of Zn / h Flow ofMMAO, g / h of Al Conv. propyleneThe% Div calculated o% Eff. of cat (g of polim / g of M) * 10 6 Process conditions of the first reactor 02 166, 4 6, 2 9, 8 13 95 19, 9 0. 164 199 0. 136 10.4 0.43 91 70 4.72 03 104.1 3, 6 6, 0 13 95 9, 9 0.109 199 0.045 6, 1 0.25 90 42 8.74 Second reactor process conditions 02 83.6 7.410 95 59, 9 0.59 1000 0.360 900.26 03 156, 0 14.410 93 59, 9 0.55 1000 0.320 900.42 50/58 Table 3B. Physical properties of Examples 02 and 03 of composite blocks Ex. % by weight of extraction MFR @230 ° C Mw, kg / mol Mw / Mn % by weight of C2 Tm (° C) Tc (° C) Fusion enthalpy (J / g) T g (° C) % by weight of HTLC separation PP 02 62.3 7.6 132 2.31 42.4 128 74.5 52 -46 13.0 03 29, 1 1.7 202 2.53 26, 9 134 91 67 -47 32.5 Petition 870190115675, of 11/11/2019, p. 60/72 51/58 Table 3C. Process conditions for the production of block composites, Example 14. Ex. Reactor control temp (° C) Food.Of solvent (lb / h) Food. Propylene (lb / h) Food.Ethylene (lb / h) Conc. propylene in the reactor (g / L) Eff. of cat (g of polim / g of M) * 106 Cat flow(lb / h) Conc. cat. (ppm) Cocat flow 1 (lb / h) Cocat flow 2 (lb / h) TEN flow (lb / h) Production rate (lb / h) Process conditions of the first reactor 14 105 229 2 18 1.08 2.40 0.28 29 0.44 0.45 0.73 11 Second reactor process conditions 14 93 343 32 0 1.97 0.44 0.66 100 0.66 34 51/58 3D table. Physical properties of Block Composite Example 14 Ex. MFR @ 230 ° C M w , kg / mol Mw / Mn % by weight of C2 Tm (° C) peak 1 (peak 2) T c (° C) Fusion enthalpy (J / g) Tg (° C) % by weight of HTLC separation PP 14 5.8 151 2.9 37.5 127(110) 95 97 -24 28 Petition 870190115675, of 11/11/2019, p. 61/72 52/58 [0150] Each block composite of Examples 02, 03 and 14, contains: (I) crystalline isotactic propylene homopolymer (iPP); (II) ethylene / propylene (EP) polymer; and (III) block copolymer (diblocks) composed of an iPP block and an EP block. [0151] Table 4 provides an analytical summary of the block composites of Examples 02, 03 and 14. Unless otherwise indicated, the properties in Table 4 are for the block composite (C). Petition 870190115675, of 11/11/2019, p. 62/72 53/58 Table 4. Analytical summary of the block composites of Examples 02, 03 and 14. Ex. Densid. (g / cm 3 ) MFR @ 230 ° C(g / 10 min) Mw kg / mol Mw / Mn % by weight of C2 Estimated fraction weight of iPP (hard) (C) (I) Estimated fraction weight ofEP (soft)(C) (II) Estimated composite composite index Rend. estimated dibloco(C) (III),% by weight 02 0.8688 7.6 132 2.31 42.4 0.30 0.70 0, 19 19 03 0.8804 1.7 202 2.53 26, 9 0.60 0.40 0.32 32 14 0.8997 5.8 151 2.9 37.5 0.60 0.40 0.55 55 53/58 Petition 870190115675, of 11/11/2019, p. 63/72 54/58 The. Films [0152] The polymeric composition composed of (A) propylene / a-olefin interpolymer, (B) ethylene-based polymer and (C) block composite is coextruded in film structures. Components (A), (B), and (C) are mixed dry prior to addition to the extruder feed hopper. [0153] Three-layer coextruded films are manufactured using a Colin extrusion expanded film line with three extruders. Table 5 shows the conditions for making films. ULTRAMID C33L01 nylon is used as a lining layer (inside the bubble). As the core layer a mixture of 90% by weight of ATTANE 4201 (a commercial grade ultra-low density ethylene / octene copolymer, obtainable from The Dow Chemical Company) and 10% by weight of AMPLIFY GR 205 (polymer of HDPE grafted with maleic anhydride, obtainable from The Dow Chemical Company). Table 6 shows the conditions of the sealing layer and the respective properties of the three-layer film. Petition 870190115675, of 11/11/2019, p. 64/72 55/58 Table 5. Extrusion conditions of 3 coextruded layers. Parameter unity Value Matrix opening mm 2.0 BUR2.5 Thickness millipole 3, 5 Horizontal width cm 23-24 Drag speed m / min 5.0-5.2 Actual rate Kg / h 10.4-13, 1 Ex. 25-A Ex. 30-A Ex. 25-B Layer configurationLining (inside the bubble) Core Sealant (outer layer) Layer ratio The % 25 50 25 Melting temperature ° C 223-225 191-196 187-194 Motor load Amp (A) 1.3-2.1 6, 1-6, 5 1.7-4.0 Spindle speed rpm 57-63 70-74 61-65 Petition 870190115675, of 11/11/2019, p. 65/72 56/58 Table 6. Sealing layer compositions and three-layer film properties. Component In. MI / MFR Dens. in. unity CS-1 CS-V1 CS-V2 ExV1 ExV2 1 12 13 15 14 (B) AFFINITY PL1880G 1, 0 0.902100 (A) H110-02N 2.0 0.902 (A) DS6D81 **(5.1% C2) 5.0 0.900 (A) VERSIFY 2200 2.0 0. 876 10075(A) VERSIFY 3200 8, 0 0. 876 10075 (C) Block composite (14 of Tables 3,4) 5, 8 0.8997 10 10 (B) HDPE 12450N 12 0.950 15 15 Kinetic COF (F-M) 1, 20 1, 37 1, 11 1.00 0.98 Static COF (F-M) 1, 37 1.54 1, 30 1, 15 1, 12 Opacity The0 0.63 0.76 1.66 2.38 1.83 Clarity The0 98, 2 98, 1 97, 1 96, 0 97.3 Maximum hot stickiness (N / in) 8, 14 7, 11 9, 72 8, 73 9, 52 HTIT(° C, 4 N / in) ° C 97 67 72 67 69 Maximum HT temperature ° C 120 120 100 80 110 Delta T (HT> 6 N / in) ° C 29 47 48 77 68 HT at 150 ° C N / in 4.3 4, 9 4, 1 5, 9 5.0 ** MFR measured @ 230 ° C. CS = Comparative Sample. Ex = Example of the present disclosure. Hot tackiness temperature window [0154] With specified film structure, coextruded films prepared with the present polymeric composition exhibit hot tackiness greater than 5 N / in over a temperature range of at least 40 ° C, or at least at least 45 ° C, or at least 50 ° C (Table 6) based on ASTM F 1921, method B with a thermal contact time of 1.0 second Petition 870190115675, of 11/11/2019, p. 66/72 57/58 and cooling time of 0.1 second. Figure 5 shows the hot tack temperature window data. Hot tack start temperature (HTIT) [0155] Coextruded films prepared with the present polymeric composition in the sealing layer exhibit a comparable or lower hot tack start temperature compared to comparative samples. In general, a lower hot tack temperature is desirable to improve the processing and production rate of the packaging operation. Coextruded films containing the present polymeric composition in the sealing layer exhibit lower HTIT than that of films containing an SLEP in the sealing layer. Table 6 lists the HTIT data. Friction coefficient (COF) [0156] In general, a lower COF is desirable to improve processing and / or speed up the packaging speed. Table 6 and Figure 7 show the COF data. Extruded films with a sealing layer prepared with the present polymeric composition exhibit less COF, compared to comparative samples prepared with SLEP and propylene-based polymers. Hot tack resistance at high temperatures [0157] Another very useful aspect of the present examples is their hot tack resistance at high temperatures, such as at 150 ° C. Higher resistance to hot tackiness at elevated temperatures allows packaging and / or processing of contents at elevated temperatures, such as sterilization via boiling water or other heating mechanisms, for use in autoclave applications. As shown in Figures 4 and 6, and in Table 6, the values of Petition 870190115675, of 11/11/2019, p. 67/72 58/58 hot tackiness of the present examples at 150 ° C is greater than that of the corresponding comparative samples. Optical properties [0158] The present examples exhibit very good optical properties, as shown in Table 6 and Figures 8 and 9. The opacity values of the sealant films of the comparative examples and the present examples are all below 2.5, and the clarity of these films is greater than 96%. [0159] Specifically, it is intended that the present disclosure is not limited to the embodiments and illustrations contained therein, but include modified forms of those incorporations including portions of the incorporations and combinations of elements from different embodiments as being within the limits of the scope of the following claims.
权利要求:
Claims (13) [1] 1. Film, characterized by the fact that it comprises a first layer comprising a polymeric composition comprising: (A) a propylene / α-olefin interpolymer; (B) an ethylene-based polymer; (C) a block composite comprising: (I) a crystalline polymer based on propylene; (II) an ethylene / α-olefin polymer; and (III) a block copolymer comprising a propylene-based crystalline block and an ethylene / aolefin block; and a second layer comprising an olefin-based polymer. [2] 2. Film according to claim 1, characterized in that component (A) comprises a propylene / ethylene copolymer having a density of 0.85 g / cm 3 to 0.90 g / cm 3 . [3] Film according to either of claims 1 or 2, characterized in that the component (A) has a melt flow rate of 0.5 g / 10 min to 10 g / 10 min. [4] 4. Film, according to any of the claims of 1 to 3, characterized in that component (B) comprises an ethylene-based polymer having a density greater than 0.941 g / cm 3 . [5] 5. Film, according to any of the claims of 1 to 4, characterized by the fact that component (B) has a melting index of 1.0 g / 10 min at 20.0 g / 10 min. [6] 6. Film, according to any of the claims of 1 to 5, characterized by the fact that the block copolymer (C) Petition 870190115675, of 11/11/2019, p. 69/72 2/3 (III) comprise a diblock with the formula (1) below: (EP) - (iPP) (1) in which EP represents a segment of polymerized ethylene and propylene monomer units, and iPP represents a segment of isotactic propylene homopolymer. [7] 7. Film according to any one of claims 1 to 6, characterized in that the block composite (C) comprises more than 15% by weight of C (III), based on the total weight of the block composite ( Ç). [8] 8. Film, according to any of the claims of 1 to 7, characterized by the fact that the block composite (C) has a density of 0.88 g / cm 3 to 0.90 g / cm 3 and a melting index of 1 g / 10 min at 50 g / 10 min. [9] Film according to any one of claims 1 to 8, characterized in that the polymeric composition further comprises an olefin-based polymer. [10] 10. Film according to claim 1, characterized in that the second layer comprises an olefin-based polymer and optionally a functionalized olefin-based polymer. [11] 11. Autoclave bag, characterized by the fact that it comprises: the film as defined in any one of claims 1 to 9; and an optional third layer. [12] Autoclave pouch according to claim 11, characterized in that the first layer is a sealing layer and the second layer comprises from 70% by weight to 99% by weight of an olefin-based polymer and 30% by weight at 1% by weight of a functionalized olefin-based polymer. [13] 13. Autoclave bag, according to any of claims 11 or 12, characterized by the fact that the
类似技术:
公开号 | 公开日 | 专利标题 JP6373337B2|2018-08-15|Polymer composition and sealant layer using the same BR112013007274B1|2021-08-10|POLYMER COMPOSITION, FILM AND RETORT BAG BRPI0314479B1|2015-10-13|polymer composition, skin layer, manufactured article and film JPH10507786A|1998-07-28|Polyolefin composition exhibiting heat resistance, low hexane extraction and exhibiting adjustable tensile stress RU2565682C2|2015-10-20|Sandwiched film and bag made thereof KR20170093968A|2017-08-16|Polypropylene films with improved sealing behaviour, especially in view of improved sealing properties BRPI1009645B1|2019-12-10|coated substrate WO2011149886A1|2011-12-01|Heat-sealable polyolefin-based film comprising olefin block copolymer BR112014015813B1|2020-12-22|multilayer film JP2004249568A|2004-09-09|Heat sealable polypropylene film, laminated film and its application JP6545479B2|2019-07-17|Polypropylene resin composition and laminated film obtained therefrom JP5060828B2|2012-10-31|Heat sealable laminate JP2004243626A|2004-09-02|Heat-fusible propylene polymer laminated film and its use JP2004231919A|2004-08-19|PROPYLENE-alpha-OLEFIN COPOLYMER COMPOSITION, MOLDED PRODUCT AND USE OF THE SAME BR112019027184A2|2020-06-30|resins, multilayer films and packaging comprising the same WO2021059913A1|2021-04-01|Propylene-based resin composition and heat-seal film KR20210154981A|2021-12-21|Polypropylene composition for retort packaging applications KR101984820B1|2019-05-31|Film for medical application with higher flexibility and transparency JPH11165389A|1999-06-22|Stretched packaging film WO2014094090A1|2014-06-26|Polymeric compositions for sealable films and articles BR112021003478A2|2021-05-18|Propylene random copolymer for use in film applications KR20200077155A|2020-06-30|Polyolefin resin composition having excellent thermal adhesiveness and blocking resistance BR112020004338A2|2020-09-08|multilayer film with reversible turbidity BR112017026756B1|2021-12-21|METHOD OF PREPARING A PEELING LAYER SEALING, PEELING SEALING LAYER, MULTILAYER FILM AND METHOD OF PREPARING A MULTILAYER FILM JPH11138714A|1999-05-25|Heat-shrinkable film
同族专利:
公开号 | 公开日 BR112013007286A2|2016-06-14| JP6373337B2|2018-08-15| JP2013542284A|2013-11-21| PL2622014T3|2018-01-31| JP6069204B2|2017-02-01| US8916249B2|2014-12-23| RU2013119976A|2014-11-10| EP2622014B1|2017-08-16| CN103228723A|2013-07-31| MX2013003617A|2013-05-20| CN103228723B|2016-01-13| US20130183465A1|2013-07-18| MX340414B|2016-07-06| WO2012044730A1|2012-04-05| JP2017122218A|2017-07-13| EP2622014A1|2013-08-07| ES2642060T3|2017-11-15|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 US4076698B1|1956-03-01|1993-04-27|Du Pont| CA849081A|1967-03-02|1970-08-11|Du Pont Of Canada Limited|PRODUCTION OF ETHYLENE/.alpha.-OLEFIN COPOLYMERS OF IMPROVED PHYSICAL PROPERTIES| JPH0734378B2|1991-03-15|1995-04-12|山一電機株式会社|Mounting type contact| US5278272A|1991-10-15|1994-01-11|The Dow Chemical Company|Elastic substantialy linear olefin polymers| US5272236A|1991-10-15|1993-12-21|The Dow Chemical Company|Elastic substantially linear olefin polymers| US5462807A|1993-08-20|1995-10-31|Exxon Chemical Patents Inc.|Heat sealable films and articles| JPH09194646A|1996-01-17|1997-07-29|Mitsui Petrochem Ind Ltd|Polypropylene resin composition| ID16442A|1996-01-22|1997-10-02|Dow Chemical Co|WEIGHT POLYMER ETHYLENE ULTRA LOW MOLECULES| JP3905006B2|2001-09-20|2007-04-18|株式会社プライムポリマー|Heat-sealable film and use thereof| US20030211350A1|2002-05-10|2003-11-13|Migliorini Robert A.|Multilayer heat sealable polyolefin film comprising skin layer and transition layer of differing melting points| EP1364990B1|2002-05-20|2012-10-10|Mitsui Chemicals, Inc.|Resin composition for sealant, laminate, and container obtained therefrom| US20040081842A1|2002-10-29|2004-04-29|Peet Robert G.|Film with metallocene-catalyzed propylene copolymer heat-seal layer| JP4344997B2|2003-09-16|2009-10-14|Ｄｉｃ株式会社|Easy-open coextruded multilayer film and easy-open laminate film| US7858706B2|2004-03-17|2010-12-28|Dow Global Technologies Inc.|Catalyst composition comprising shuttling agent for ethylene multi-block copolymer formation| US7355089B2|2004-03-17|2008-04-08|Dow Global Technologies Inc.|Compositions of ethylene/α-olefin multi-block interpolymer for elastic films and laminates| AR053693A1|2004-03-17|2007-05-16|Dow Global Technologies Inc|COMPOSITIONS OF ETHYLENE / ALFA-OLEFINE INTERPOLIMERO MULTIBLOCK SUITABLE FOR FILMS| US7582716B2|2004-03-17|2009-09-01|Dow Global Technologies Inc.|Compositions of ethylene/α-olefin multi-block interpolymer for blown films with high hot tack| US7608668B2|2004-03-17|2009-10-27|Dow Global Technologies Inc.|Ethylene/α-olefins block interpolymers| AR048104A1|2004-03-17|2006-03-29|Dow Global Technologies Inc|CATALYZING COMPOSITION THAT INCLUDES A LINK AGENT FOR THE FORMATION OF OLEFIN'S TOP COPOLYMERS IN MULTIPLE BLOCKS| JP6138408B2|2005-09-15|2017-05-31|ダウ グローバル テクノロジーズ エルエルシー|Catalytic olefin block copolymer with controlled block sequence distribution| US8153243B2|2005-12-09|2012-04-10|Dow Global Technologies Llc|Interpolymers suitable for multilayer films| US8617717B2|2006-06-09|2013-12-31|Exxonmobil Chemical Patents Inc.|Heat sealable films from propylene and α-olefin units| BRPI0812643B1|2007-07-13|2019-01-15|Dow Global Technologies Inc|ethylene / α-olefin interpolymer| US8716400B2|2009-10-02|2014-05-06|Dow Global Technologies Llc|Block composites and impact modified compositions| US8802774B2|2009-10-02|2014-08-12|Dow Global Technologies Llc|Block composites and impact modified compositions| JP5968321B2|2010-09-30|2016-08-10|ダウ グローバル テクノロジーズ エルエルシー|Polymer composition and sealant layer using the same| WO2012044730A1|2010-09-30|2012-04-05|Dow Global Technologies Llc|Polymeric composition and sealant layer with same| US20140072743A1|2012-09-11|2014-03-13|Baxter Healthcare S.A.|Polymer films containing microspheres|US8802774B2|2009-10-02|2014-08-12|Dow Global Technologies Llc|Block composites and impact modified compositions| WO2012044730A1|2010-09-30|2012-04-05|Dow Global Technologies Llc|Polymeric composition and sealant layer with same| JP5968321B2|2010-09-30|2016-08-10|ダウ グローバル テクノロジーズ エルエルシー|Polymer composition and sealant layer using the same| BR112013032423A2|2011-06-17|2017-01-17|Berry Plastics Corp|insulating glove for a cup| WO2012174567A2|2011-06-17|2012-12-20|Berry Plastics Corporation|Process for forming an insulated container having artwork| WO2012174422A2|2011-06-17|2012-12-20|Berry Plastics Corporation|Insulated container with molded brim| WO2012173873A2|2011-06-17|2012-12-20|Berry Plastics Corporation|Insulated container| WO2013003541A1|2011-06-30|2013-01-03|Dow Global Technologies Llc|Multilayered polyolefin-based films having a layer comprising a crystalline block copolymer composite or a block copolymer composite resin| RU2605398C2|2011-08-31|2016-12-20|Берри Пластикс Корпорейшн|Polymer material for heat-insulated container| US9982122B2|2012-04-12|2018-05-29|Dow Global Technologies Llc|Polyolefin blend composition and articles made therefrom| CA2879564A1|2012-08-07|2014-02-13|Berry Plastics Corporation|Cup-forming process and machine| JP6254166B2|2012-09-14|2017-12-27|ダウ グローバル テクノロジーズ エルエルシー|Multilayer polyolefin film| DK2727724T3|2012-10-25|2021-03-08|Buergofol GmbH|SINGLE OR MULTI-LAYER FILM| JP2015532945A|2012-10-26|2015-11-16|ベリー プラスチックス コーポレイション|Polymer materials for insulated containers| AR093943A1|2012-12-14|2015-07-01|Berry Plastics Corp|EDGE OF A THERMAL PACK| AR093944A1|2012-12-14|2015-07-01|Berry Plastics Corp|PUNCHED FOR PACKAGING| US9840049B2|2012-12-14|2017-12-12|Berry Plastics Corporation|Cellular polymeric material| US9957365B2|2013-03-13|2018-05-01|Berry Plastics Corporation|Cellular polymeric material| BR112015022750A2|2013-03-14|2017-07-18|Berry Plastics Corp|container| CN105592997A|2013-08-16|2016-05-18|比瑞塑料公司|Polymeric material for an insulated container| BR112016007421B1|2013-10-15|2021-09-14|Dow Global Technologies Llc|COMPOSITION, ARTICLE AND ROTOMOLDED ARTICLE| SG11201605238UA|2013-12-31|2016-07-28|Dow Global Technologies Llc|Multilayered films, methods of manufacture thereof and articles comprising the same| WO2015123827A1|2014-02-19|2015-08-27|Dow Global Technologies Llc|High performance sealable co-extruded oriented film, methods of manufacture thereof and articles comprising the same| US20150231862A1|2014-02-19|2015-08-20|Dow Global Technologies Llc|Multilayered polyolefin films, methods of manufacture thereof and articles comprising the same| WO2015123829A1|2014-02-19|2015-08-27|Dow Global Technologies Llc|Multilayer film, methods of manufacture thereof and articles comprising the same| JP6292441B2|2014-03-07|2018-03-14|東レフィルム加工株式会社|Polypropylene composite film and laminate using the same| JP6331074B2|2014-03-07|2018-05-30|東レフィルム加工株式会社|Polypropylene composite film and laminate using the same| JP6292442B2|2014-03-12|2018-03-14|東レフィルム加工株式会社|Polypropylene composite film and laminate using the same| JP2017514926A|2014-03-21|2017-06-08|ボレアリス・アクチェンゲゼルシャフトＢｏｒｅａｌｉｓ Ａｇ|Heterophase propylene copolymer with high melting point| WO2016014230A1|2014-07-25|2016-01-28|Exxonmobil Chemical Patents Inc.|Footwear compositions comprising propylene-based elastomers| US10155861B2|2014-08-21|2018-12-18|Dow Global Technologies Llc|Nucleation with a block composite nucleator| EP3183317B1|2014-08-21|2018-06-06|Dow Global Technologies LLC|Hot melt adhesive composition including a crystalline block composite| WO2016026120A1|2014-08-21|2016-02-25|Dow Global Technologies Llc|Hot melt adhesive composition including crystalline block composite| BR112017003445A2|2014-08-21|2017-11-28|Dow Global Technologies Llc|hot melt adhesive composition including a block composite compatibilizer| US9758655B2|2014-09-18|2017-09-12|Berry Plastics Corporation|Cellular polymeric material| BR112017010971A2|2014-12-02|2018-02-14|Dow Global Technologies Llc|dynamic vulcanization of a blend composition, methods of manufacturing it and articles comprising the same| US10513589B2|2015-01-23|2019-12-24|Berry Plastics Corporation|Polymeric material for an insulated container| US10688775B2|2015-04-16|2020-06-23|Response Technologies, Llc|Method of manufacturing containment bladders| JP6823645B2|2015-09-10|2021-02-03|ダウ グローバル テクノロジーズ エルエルシー|Polyolefin blend with compatibility agent| US10526436B2|2016-03-31|2020-01-07|Dow Global Technologies Llc|Polyolefin blends including crystalline block composites for PVC-free wear layers| CN109476888A|2016-05-31|2019-03-15|陶氏环球技术有限责任公司|Thermoplastic polyolefin blend including ethylene-rich polymer| WO2018058354A1|2016-09-28|2018-04-05|Dow Global Technologies Llc|Multilayer film and pouch with same| EP3559108A4|2016-12-22|2020-09-02|Bemis Company, Inc.|Packaging films with improved hot-tack performance| ES2783948T3|2017-03-10|2020-09-21|Dow Global Technologies Llc|Multilayer films and methods of the same| BR112019027920A2|2017-06-29|2020-07-21|Dow Global Technologies Llc|built-in plastic hinges with block composite polymer| EP3645623B1|2017-06-29|2021-05-19|Dow Global Technologies LLC|Plastic living hinges with block composite polymer| US11091311B2|2017-08-08|2021-08-17|Berry Global, Inc.|Insulated container and method of making the same| US10973601B2|2018-11-16|2021-04-13|WEG Surgical Solutions, LLC|Sterile drape without air-trapping wrinkles for use in warming system| CN111825908A|2020-06-04|2020-10-27|江门普立菲新材料有限公司|Modified film for hot melt adhesive packaging and preparation method thereof|
法律状态:
2018-04-03| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law| 2019-08-13| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure| 2020-02-11| B09A| Decision: intention to grant| 2020-03-31| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 29/09/2011, OBSERVADAS AS CONDICOES LEGAIS. |
优先权:
[返回顶部]
申请号 | 申请日 | 专利标题 US38843910P| true| 2010-09-30|2010-09-30| US61/388,439|2010-09-30| PCT/US2011/053816|WO2012044730A1|2010-09-30|2011-09-29|Polymeric composition and sealant layer with same| 相关专利
Sulfonates, polymers, resist compositions and patterning process
Washing machine
Washing machine
Device for fixture finishing and tension adjusting of membrane
Structure for Equipping Band in a Plane Cathode Ray Tube
Process for preparation of 7 alpha-carboxyl 9, 11-epoxy steroids and intermediates useful therein an
国家/地区
|