Patent Application
20230294386
The invention relates to the use of special polymers as barrier layers, in particular as barrier layers in composite materials. These barrier layers exhibit a selective barrier effect with respect to different gases, the barrier effect being especially effective with respect to HFOs. On account of these properties, such barrier layers can positively affect insulation properties, for example in thermally insulated pipes.
Foams for insulation are known materials. Such foams have numerous applications, in particular for thermal insulation, and are therefore important components in a large number of applications. The insulating properties of foams are dependent on several parameters, inter alia on the composition of the cell gases.
A known class of foams is polyurethane foams (PU), which consist of a polyol and an isocyanate. In order to produce these foams, another physical foaming agent is usually also added and is typically stirred into the polyol component, which is then mixed with the isocyanate in a high-pressure mixing head immediately before the two-component mixture (2C) is metered. This physical foaming agent is a first component of cell gases in PU foams. The polyol component typically contains a certain amount of water, with a typical range being 0.5 to 1.5 wt. %. This water results in the following reactions: a) reaction with the isocyanate to form carbamic acid, which is, however, unstable and, when carbon dioxide splits off, immediately disintegrates to form the corresponding amine; b) reaction of the amine thus produced with another isocyanate molecule to form the corresponding urea.
This reaction leads to the formation of further cell gases in PU foams and thus assists with the foaming process. The urea produced is advantageous for the thermal stability of the foam produced. Details relating thereto are described in Oertel et al (Polyurethane, editor Günter Oertel, 3rd edition 1993, Hanser Verlag, p. 13; p. 94).
In stark contrast to chlorofluorocarbons (HFCs), hydrofluoroolefins (HFOs) are a known class of compounds that are known for their low global warming potential (GWP). Since HFOs are not combustible either, they are used as foaming agents, as is mentioned in WO2016/094762, for example. HFOs positively affect the insulating properties of foams.
Polymer materials generally have a certain degree of permeability to all types of permeants (gaseous or liquid). However, polymers differ markedly by the amount of a specific permeant that migrates through a given material per unit of time in each case. The use of polymer materials as barrier layers for the gases in the air, in particular nitrogen (N2), oxygen (O2), carbon dioxide (CO2) and water (H2O) is known per se. EP 1355103 thus describes a barrier based on EVOH or PVDC, which reduces diffusion of the CO2, N2 and O2 gases but is simultaneously permeable to water. EP2340929 describes an EVOH layer as a barrier with respect to O2 and CO2. WO92/13716 describes EVOH layers as barriers with respect to HFCs. As set out above, HFCs have in principle different properties when compared with HFOs.
In light of this, it appears to be desirable to provide foams having improved insulating properties.
It also appears to be desirable to provide materials having barrier properties, in particular having selective barrier properties.
The objects outlined above are solved according to the independent claims. The dependent claims constitute advantageous embodiments. Additional advantageous embodiments can be found in the description and the FIGURES. Any of the general, preferred and particularly preferred embodiments, ranges, etc. given in connection with the present invention can be combined with one another. Likewise, individual definitions, embodiments, etc. may be omitted or may not be relevant.
The present invention, which relates to a composite article comprising a barrier layer and a lagging, is described in detail below such as in
The terms used in the present invention are used in the usual sense, with which a person skilled in the art is familiar. Provided the direct connection does not have another meaning, the following terms have in particular the meaning/definitions given here.
The present invention is also illustrated by the FIGURES; in addition to the following description, further embodiments of the invention can be found in these FIGURES.
The invention therefore relates to the use of a polymer layer as a barrier (1) for gases, the polymer of the polymer layer comprising a copolymer consisting of ethylene and vinyl alcohol or a copolymer consisting of ethylene and carbon monoxide or a copolymer consisting of ethylene and carbon monoxide and propylene; and said gas being selected from the group of hydrofluoroolefins.
It has been found that hydrofluoroolefins HFO, in particular as a cell gas (21) in a foam (22), are held back by said polymer layer (1) very effectively. As a result, the loss over time of these cell gases in a foam, for example, can be minimized in order to preserve the thermal insulating effect of this foam for a long period of time.
It has also been found that the polymer layer (1) described here has a relatively high degree of permeability to carbon dioxide. The carbon dioxide generated when a polyurethane foam (PU) is formed, for example, can therefore leave the polymer layer (1) over time by means of diffusion.
It has also been found that production methods for the use described here can be implemented in a simple and cost-effective manner and can be integrated in a continuous process.
This use and the individual features shall be explained in the following.
Barrier (1): diffusion barriers are known in several fields of technology, for example in the field of conduit pipes/pipe systems.
According to the invention, the barrier (1) is in the form of a layer. According to the invention, the barrier can be provided as a single layer or as several separate layers.
The values for the permeability of polymer materials vary over very wide ranges; more than the factor 105. The criteria relating to the presence of a barrier effect are different for different permeants.
The measured values for O2, N2 and CO2 (determined according to ISO 15105-1) are usually given in cm3/m2*day*bar. If the values are smaller than 20, the barrier effect is good and the polymer is considered to be impermeable. If the values are greater than 100, a barrier effect is no longer provided and the polymer is considered to be permeable. For values therebetween, the polymer is considered to be semi-permeable.
The measured values for HFO (determined according to ISO 15105-1:2007-10), Cp (determined according to ISO 15105-2:2003-02) and water (determined according to ISO 15105-3:2003-01) are usually given in ml/m2*day. If the values are smaller than 3, the barrier effect is good and the polymer is considered to be impermeable. If the values are greater than 20, a barrier effect is no longer present and the polymer is considered to be permeable. For values therebetween, the polymer is considered to be semi-permeable.
The invention also relates to the use of a polymer layer as a selective barrier (1) for gases, the polymer of the polymer layer comprising a copolymer consisting of ethylene and vinyl alcohol or a copolymer consisting of ethylene and carbon monoxide or a copolymer consisting of ethylene and carbon monoxide and propylene as described here; and said barrier preferably being
said barrier preferably being
It has been found that the barriers (1) described here meet these requirements very well.
The polymer layer (1) advantageously has the following diffusion coefficients:
HFOs less than 3 ml/m2*day
H2O (gas) more than 3 ml/m2*day
CO2 more than 20 cm3/m2*day*bar
O2 less than 20 cm3/m2*day*bar
N2 less than 20 cm3/m2*day*bar
These values can be achieved in particular by selecting the polymers and/or the layer thickness. Such values have proven to be advantageous for numerous applications, in particular in the field of laggings, for example for conduit pipes.
Barrier effect with respect to HFOs: due to their low degree of thermal conductivity, HFOs are advantageous cell gases in laggings. It is accordingly advantageous to hold said gases back in the insulating material. The layer described here allows for the diffusion of HFOs through the layer (1) to be reduced. This property is important, for example in order to ensure the insulating capacity of a conduit pipe/pipe system over a long period of time.
Barrier effect with respect to water vapor: prevention of the diffusion of said water vapor should not too great, since this otherwise runs the risk of said water vapor accumulating in the lagging and therefore impairing the degree of thermal conductivity.
In addition, the accumulation of moisture in the lagging also risks damaging said lagging. In an advantageous embodiment, the layer described here also allows for water to diffuse out of the lagging. This property is particularly important for conduit pipes/pipe systems, the medium pipe of which is made of plastics material. If an aqueous medium is transported in such conduit pipes/pipe systems, water can be transferred from the medium, through the conduit pipe and into the lagging, and can therefore reduce the insulating capacity and damage the foam lagging.
Barrier effect with respect to carbon dioxide: in an advantageous embodiment, the layer described here also provides a certain degree of permeability to CO2. A particularly suitable value for the CO2 permeability is in the range of 0.5 to 100 cm3/m2*day*bar.
Barrier effect with respect to oxygen: O2 can lead to the oxidative damage of the insulating material, especially at high use temperatures, as in plastics jacketed pipes (PJP). Therefore, cell gases should not contain O2 and diffusion thereof into the lagging should be avoided.
Barrier effect with respect to nitrogen: first of all, N2 is not expected to have an adverse effect on the PU foam, but the degree of thermal conductivity of N2 of 26 mW/m*K is markedly higher than the other cell gases. As a result, its presence in the PU foam would also increase the degree of thermal conductivity thereof, which is not desirable.
The barrier layer can accordingly be adapted to the desired requirements profile. In order to produce foams having as low a degree of thermal conductivity as possible and to also maintain this low degree of thermal conductivity for a long period of time, said barrier layer aims to prevent the oxygen and nitrogen gases from diffusing into the foam, to allow for diffusion of the CO2 out of the foam, and to prevent diffusion of HFOs out of the foam. The more effective this is, the better the properties of the foam.
The combination of cell gases (21) from the group of HFOs and barrier layers (1) according to the formulas (II), (III) and (IV) described here leads to particularly good, superadditive insulating properties in thermally insulated conduit pipes. Such a positive interaction between these components is surprising. Without being tied to any theories, this superadditive effect can be attributed to the barrier properties of the materials according to formulas (II), (Ill) and (IV).
Polymer: as shown, the barrier comprises a copolymer consisting of ethylene with either carbon monoxide (so-called polyketones) or with vinyl alcohol (so-called ethylene vinyl alcohols).
Polyketones (PK): in an advantageous embodiment, the barrier comprises a polymer that contains or consists of polyketone(s). The polymer layer accordingly comprises polyketones and blends of polyketones. Polyketones are materials that are known per se and are characterized by the keto group (C═O) in the polymer chain.
In this embodiment, the polymer advantageously comprises 50 to 100 wt. %, preferably 80 to 100 wt. % structural units of formula (II) or formula (III).
where
o represents 1 or 2, preferably 1,
p represents 1 or 2, preferably 1,
q represents 1 to 20, and
r represents 1 to 20.
In one embodiment, the polymer contains 90 to 100 wt. % structural units of formula (II), where o and p represent 1.
In one embodiment, the polymer contains 90 to 100 wt. % structural units of formula (III), where q and r represent, independently of one another, 1 to 20.
In one embodiment, the polymer of formula (II) has a molecular weight Mw of more than 20,000, in particular of 50,000 to 500,000. In one embodiment, the polymer of formula (III) has a molecular weight Mw of more than 20,000, in particular of 50,000 to 500,000.
In one embodiment, the polymer of formula (II) or formula (III) has a melting temperature above 200° C. (measured using DSC, 10 K/min according to ISO 11357-1/3).
In one embodiment, the polymer of formula (II) or formula (III) has a low degree of water absorption, preferably of less than 3%, measured according to DIN EN ISO 62:2008-05 (saturation in water at 23° C.).
Polyketones can be obtained by the catalytic conversion of carbon monoxide with the corresponding alkenes, such as propene and/or ethene. Such polyketones are also referred to as aliphatic polyketones. These polymers are commercially available, for example as polyketone copolymers (formula II) or polyketone terpolymers (formula III) from Hyosung. Such polyketones are also commercially available under the trade name Akrotek® PK.
In comparison with EVOHs (IV), PKs (II, III) have worse barrier properties with respect to O2 and N2, and a worse barrier effect with respect to H2O and CO2. Accordingly, one of these barrier materials can be advantageous depending on the planned use. For example, if medium pipes made of plastics material are used, it is of greater importance to allow for the migration of moisture in order to prevent their accumulation in the PU foam. If medium pipes made of metal are used, the effect of the migration out of the warm water being transported and into the foam is not noticeable. In this case, it may be of greater importance for the degree of thermal conductivity of the foam to be kept as low as possible for long periods of time, since the KMR pipes that are typically used are preferably used in classic district heating, where large amounts of energy are transported and losses have to be minimized.
Ethylene vinyl alcohols (EVOH): in another advantageous embodiment, the barrier comprises a polymer containing or consisting of ethylene vinyl alcohol.
In this embodiment, the polymer comprises 50 to 100 wt. %, preferably 80 to 100 wt. % structural units of formula (IV),
where
m represents 1 to 10, and
n represents 2 to 20.
Suitable EVOHs are in particular statistical copolymers, in which the ratio m/n is 30/100 to 50/100.
Suitable EVOHs in particular have a molecular weight Mw of more than 20,000, in particular of 50,000 to 500,000.
EVOHs are commercially available, for example as EVAL FP series or EP series from Kuraray. These are characterized by good processability, in particular they are very easy to process together with the jacket material polyethylene (PE) that is normally used by means of coextrusion, since the melt viscosities and melting temperatures thereof lie in a similar range.
In comparison with PKs (II, III), EVOHs (IV) display better barrier properties with respect to O2 and N2 and a better barrier effect with respect to H2O and CO2. These materials are accordingly particularly suitable in uses where there is little H2O and/or CO2. The considerations presented in connection with PK correspondingly apply here.
Gas: as mentioned above, the gas is selected from the group of hydrofluoroolefins (HFOs). This gas can be the cell gas (21) of a foam, in particular of a foam lagging (20), for example. This gas can consist of or contain HFOs. Typical additional components of the gas are in particular (cyclo)alkanes, CO2, N2, O2 and H2O.
Hydroolefins: HFOs are known and are commercially available or can be produced using known methods. The term includes both compounds that only comprise carbon, hydrogen and fluorine and compounds that also contain chlorine (also referred to as HFCOs) and each contain at least one unsaturated bond in the molecule. HFOs can be a mixture of different components or a pure component. HFOs can also be isomeric mixtures, in particular E-isomers/Z-isomers, or isomerically pure compounds.
Within the context of the present invention, HFOs that are particularly suitable have a boiling point above 0° C.
Within the context of the present invention, HFOs that are particularly suitable are selected from the group comprising compounds of formula (I),
where R5 represents H, F, Cl, CF3, preferably CI, Cf3, and R6 represents H, F, Cl, CF3, preferably H.
Particularly suitable HFOs are 1233zd (for example Solstice LBA, from Honeywell) and 1336mzz (for example Formacel 1100, from DuPont).
It has surprisingly been found that thermally insulated conduit pipes have improved insulating behavior when the cell gases (21) of the lagging (20) contain at least 10 vol. %, preferably at least 30 vol. %, particularly preferably 50 vol. % HFO, and when this lagging is surrounded by a barrier (1), as described here.
(Cyclo)alkanes: these are known as the cell gas of the lagging in thermally insulated pipes. Said alkane or cycloalkane is advantageously selected from the group comprising propane, butanes, pentanes, cyclopentane, hexanes and cyclohexane. By combining (cyclo)alkane with HFO, the product properties can be finely adjusted and/or the producibility can be improved and/or the costs can be reduced together with a reasonable loss of quality. Said (cyclo)alkanes can be pure compounds or mixtures; the aliphatic alkanes can be isomerically pure compounds or isomeric mixtures. A particularly suitable (cyclo)alkane is cyclopentane (Cp).
Carbon dioxide (CO2): this is known as the cell gas of the lagging in thermally insulated pipes. It can be formed as a byproduct of the production process or can be added in a specific amount. The CO2 content of a cell gas is typically less than 50 vol. %.
Nitrogen (N2), oxygen (O2): the production process can cause components from the atmosphere/ambient air to enter the cell gas. These are substantially N2 and/or O2, for example air. The cell gas content is typically less than 5 vol. % at the time of production.
Water (H2O): this can be in the form of a gas or a liquid. H2O typically enters the lagging cell gas from the surrounding area by means of condensation or from an element carrying media by means of permeation.
In one embodiment, the invention therefore relates to the use described here, wherein the cell gas (21) is a mixture comprising 10 to 100 vol. % HFOs and 0 to 50 vol. % (cyclo)alkane and 0 to 50 vol. % CO2.
Foam: as mentioned above, the gas can be the cell gas (21) of a foam, in particular of a foam lagging (20).
Such foams are known per se. Foams that meet the following standards: DIN EN 253:2015-12 (in particular for PJP) and EN15632-1:2009/A1:2014, EN15632-2:2010/A1:2014 and EN15632-3:2010/A1:2014 (in particular for PMP) are particularly suitable. The term includes hard foams and soft foams. Foams can be closed-celled or open-celled, preferably closed-celled, in particular as shown in the standard DIN EN 253:2015-12, for example. Such foams are preferably selected from the group of polyurethanes (PU), polyisocyanurates (PIR), thermoplastic polyesters (in particular PET) and thermoplastic polyolefins (in particular PE and PP).
The invention therefore also relates to the use of a polymer layer as a barrier (1) for gases, as described here, the gas being the cell gas of a foam, characterized in that said foam (polymer (22) and cell gas (21)) meets the following criteria:
PU containing 50 to 100 vol. % 1233zd and 0 to 50 vol. % Cp;
PU containing 50 to 100 vol. % 1336mzz and 0 to 50 vol. % Cp;
PIR containing 50 to 100 vol. % 1233zd and 0 to 50 vol. % Cp;
PIR containing 50 to 100 vol. % 1336mzz and 0 to 50 vol. % Cp;
PET containing 50 to 100 vol. % 1233zd and 0 to 50 vol. % Cp;
PET containing 50 to 100 vol. % 1336mzz and 0 to 50 vol. % Cp;
PE containing 50 to 100 vol. % 1233zd and 0 to 50 vol. % Cp; and/or
PE containing 50 to 100 vol. % 1336mzz and 0 to 50 vol. % Cp.
In one embodiment, said cell gases complement one another up to 100 vol. %. In another embodiment, these cell gases are complementary together with CO2 and air up to 100%.
The invention also relates to the use described here, wherein said polymer layer (1) is a self-supporting structural element. The polymer layer (1) can therefore be a film or a molded body.
The invention also relates to the use described here, wherein said polymer layer (1) is part of a composite material (10). Such composite materials are known per se. For the use described here, said composite material (10) may have the following layered structure: thermoplastic polymer (3), optional adhesion promoter (2), polymer layer as a barrier (1) as described here, optional adhesion promoter (2′), optional thermoplastic polymer (3′). Components (2) and (3) are commercially available products known to a person skilled in the art.
Thermoplastic polymer (3): a wide range of thermoplastics can be used; these typically have a lesser barrier effect than the layer (1). Thermoplastic polymers (3, 3′) selected from the group comprising commercial types of PE, such as high-density PE (HDPE), low-density PE (LDPE), linear low-density PE (LLDPE) are advantageously used.
Adhesion promoters (2, 2′): a wide range of adhesion promoters can be used; these typically have a lesser barrier effect than the layer (1). Adhesion promoters (2, 2′) are advantageously selected from the group of PE graft copolymers, which have at least one other component, for example maleic anhydride. Such substances are commercially available under the brand name Amplify™ from Dow or under Admer™ from Mitsui, for example.
The thicknesses of said individual layers can vary over a wide range and depend on the desired barrier effect with respect to the individual permeants, on the material and lastly on production and cost considerations, inter alia. The following values have proven suitable: the layer thickness of the polymer layer (1) is advantageously in the range of 0.01 to 1 mm, preferably in the range of 0.03 to 0.5 mm, particularly preferably in the range of 0.05 to 0.3 mm. The layer thickness of the adhesion promoter layer (2, 2′) is advantageously in the range of 0.01 to 1 mm, preferably in the range of 0.05 to 0.5 mm, particularly preferably in the range of 0.1 to 0.3 mm in each case. The layer thickness of the thermoplastic polymer (3, 3′) is advantageously in the range of 0.01 to 1 mm, preferably in the range of 0.05 to 0.5 mm, particularly preferably in the range of 0.1 to 0.3 mm in each case.
The invention also relates to the use of a polymer layer as a barrier (1) or of a composite material (10) for gases, as described here, in numerous technological fields. The use according to the invention is not limited to one single use; instead, it can be used in all fields in which the barrier effect with respect to HFOs is useful or desirable.
The invention correspondingly relates to the use of a polymer layer (1) as described here or of a composite material (10) as described here
Laggings: the term includes in particular thermally insulated pipe systems from the group of plastics media pipe systems (PMP) and plastics jacketed pipe systems (PJP). These are used for transporting heated or cooled media, in particular water or aqueous solutions. However, they can also be used to transport other substances and chemicals.
The invention is explained in more detail on the basis of the following non-limiting examples.
In a foam from the class of polyurethanes, at the end of the production process numerous cell gases are present. A summary of possible cell gases and their essential properties is shown in the table. The stated amounts for the types of foam given as examples relate to the values for freshly produced foams that have not aged.
The diffusion of O2, N2, CO2, HFO1233zd, Cp and H2O through different polymer films has been experimentally determined in the manner described in the standards specified. The results are summarized in the table.
Cp: cyclopentane; PK: aliphatic polyketone; EVOH: copolymer consisting of ethylene and vinyl alcohol; PAN: polyacrylonitrile; LDPE: low-density polyethylene.
According to the above definition, EVOH is a good barrier for all permeants observed. LDPE has practically no barrier effect, and only has a partial barrier effect with respect to water. Aliphatic PK and PAN have a good barrier effect with respect to O2, N2, HFO and Cp and a partial barrier effect with respect to CO2 and H2O.
With regard to practical application, the fact that PAN is tough to process, is brittle and is poorly commercial available is disadvantageous. EVOH and PK can be easily processed and are commercially available.
Film webs having a width of 20 to 30 cm were welded to form bags, which have a volume of approximately eight liters. These bags were filled with a PU foam, which contained cyclopentane as the foaming agent. Once the foaming process had finished, the bags were also welded at the upper end.
Each bag was then first cut and the composition of the cell gases was determined (day 0). The other samples were aged in two climatic chambers; the temperature of one of the climatic chambers being 70° C. and the relative air humidity (RH) being 10%, and the temperature of the other chamber being 70° C. and the relative humidity (RH) being 90%.
The values for the individual gases in vol. % are set out in the table.
It can be clearly seen that, for the materials EVOH and PAN, the barrier effect is heavily dependent on the humidity of the surrounding area.
From the results of example 1, a similar result is expected for HFO and Cp. EVOH and PK are therefore reasonable barrier layers for these gases.
Whilst the present application describes preferred embodiments of the invention, including those embodiments enumerated below, it should be pointed out that the invention is not limited to these embodiments and can also have a different design within the scope of the claims that follow.
Embodiment 1. A composite article comprising a barrier layer and a lagging, wherein:
(a) the barrier layer comprises a copolymer of ethylene and vinyl alcohol that contains 50 to 100 wt. % structural units of formula (II) or (III) or (IV),
where m represents 1 to 10, n represents 2 to 20 and where the layer thickness of the barrier layer is in the range of 0.03 to 0.5 mm; and
(b) the lagging comprises a polymer foam and a cell gas comprises a hydrofluoroolefin having a boiling point above 0° C.
Embodiment 2. The composite article of embodiment 1 wherein (a) the barrier layer comprises a copolymer of ethylene and vinyl alcohol contains 50 to 100 wt. % structural units of formula (IV),
and (b) the hydrofluoroolefin is selected from the group consisting of HFO1233zd, HFO1336mzz and mixtures thereof.
Embodiment 3. The composite article of embodiment 2 wherein the copolymer of ethylene and vinyl alcohol contains 90 to 100 wt. % structural units of formula (IV),
and has a molecular weight Mw of more than 20,000.
Embodiment 4. The composite article of embodiment 2, wherein said cell gas comprises a mixture of 10 to 100 vol. % hydrofluoroolefin HFO1233zd, 0 to 50 vol. % (cyclo)alkane and 0 to 50 vol. % CO2.
Embodiment 5. The composite article of embodiment 2 wherein the cell gas optionally contains less than 5 vol % nitrogen and optionally contains less than 5 vol % oxygen.
Embodiment 6. The composite article according to embodiment 2, where the barrier layer has a layered structure comprising a thermoplastic polymer, an optional adhesion promoter, the barrier layer, an optional adhesion promoter, and an optional thermoplastic polymer.
Embodiment 7. The composite article according to embodiment 6, wherein the thermoplastic polymer is selected from the group consisting of high-density PE (HDPE), low-density PE (LDPE), linear low-density PE (LLDPE) and has a layer thickness of 0.01 to 1 mm; and/or the adhesion promoter is a PE graft copolymer, which has at least one other component, and has a layer thickness of 0.01 to 1 mm.
Embodiment 8. A composite article comprising a barrier layer and a lagging, wherein:
(a) the barrier layer comprises a copolymer of ethylene and vinyl alcohol that contains 50 to 100 wt. % structural units of formula (IV),
where m represents 1 to 10, n represents 2 to 20 and where the layer thickness of the barrier layer is in the range of 0.03 to 0.5 mm; and
(b) the lagging comprises a polyurethane foam and a cell gas wherein the cell comprises a mixture of:
i. 10 to 100 vol. % hydrofluoroolefin HFO1233zd,
ii. 0 to 50 vol. % (cyclo)alkane, and
iii. 0 to 50 vol. % CO2.
Embodiment 9. The composite article of embodiment 8 where the cell gases complement one another up to 100%.
Embodiment 10. The composite article of embodiment 9 wherein the cell gas optionally contains less than 5 vol % nitrogen and optionally contains less than 5 vol % oxygen.
Embodiment 11. The composite article of embodiment 2 or of embodiment 8 which is part of a pipe system.
Embodiment 12. The composite article according to embodiment 11, where the pipe system is selected from the group consisting of pipe systems for local and district heating, pipe systems for cooling buildings, pipe systems for transporting cooled media, pipe systems in industrial applications, and pipe systems for transporting gases, liquids or solids.
Embodiment 13. The composite article according to embodiment 12 for pipe systems selected from the group consisting of plastics medium pipe systems (PMP) and plastics jacketed pipe systems (PJP).
Embodiment 14. The composite article according to embodiment 1, wherein said barrier layer is a self-supporting structural element.
Embodiment 15. The composite article of embodiment 14 which is part of a pipe system.
Embodiment 16. The composite article of embodiment 15, wherein the pipe system is selected from the group consisting of pipe systems for local and district heating, pipe systems for cooling buildings, pipe systems for transporting cooled media, pipe systems in industrial applications, and pipe systems for transporting gases, liquids or solids.
Embodiment 17. The composite article of embodiment 16 for pipe systems selected from the group of plastics medium pipe systems (PMP) and plastics jacketed pipe systems (PJP).
Embodiment 18. A method for improving thermal insulation of a PMP, comprising applying a composite article to a pipe, wherein the composite article comprises a barrier layer and insulation lagging, wherein:
(a) the barrier layer comprises a copolymer of ethylene and vinyl alcohol that contains 50 to 100 wt. % structural units of formula (IV),
where m represents 1 to 10, n represents 2 to 20 and where the layer thickness of the barrier layer is in the range of 0.03 to 0.5 mm; and
(b) the lagging comprises a polyurethane foam and a cell gas comprising a hydrofluoroolefin selected from HFO1233zd, HFO1336mzz and mixtures thereof,
Embodiment 19. The method of embodiment 18 wherein the copolymer of ethylene and vinyl alcohol contains 90 to 100 wt. % structural units of formula (IV),
and has a molecular weight Mw of more than 20,000.
Embodiment 20. The method of embodiment 19, wherein said cell gas comprises a mixture of 10 to 100 vol. % hydrofluoroolefin HFO1233zd, 0 to 50 vol. % (cyclo)alkane and 0 to 50 vol. % CO2.
| Number | Date | Country | Kind |
|---|---|---|---|
| 00936/16 | Jul 2016 | CH | national |
This application is a continuation-in-part of U.S. patent application Ser. No. 16/310,089, which is the National Stage application of International Patent Application No. PCT/EP2017/067413, filed on Jul. 11, 2017, which claims priority to Swiss Patent Application No. 00936/16, filed on Jul. 20, 2016, each of which is hereby incorporated by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 20220402253 A1 | Dec 2022 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 16310089 | Dec 2018 | US |
| Child | 17892369 | US |
