HYDROLYSIS STABLE COMPOSITIONS FOR FILMS IN SOLAR CELLS
20230112640 · 2023-04-13
Assignee
Inventors
Cpc classification
C08L79/08
CHEMISTRY; METALLURGY
Y02E10/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C08J2367/02
CHEMISTRY; METALLURGY
C08L79/00
CHEMISTRY; METALLURGY
C08L67/04
CHEMISTRY; METALLURGY
C08L67/02
CHEMISTRY; METALLURGY
C08L67/02
CHEMISTRY; METALLURGY
C08K5/29
CHEMISTRY; METALLURGY
C08L67/04
CHEMISTRY; METALLURGY
C08L79/08
CHEMISTRY; METALLURGY
C08J2367/04
CHEMISTRY; METALLURGY
International classification
C08K5/29
CHEMISTRY; METALLURGY
C08L67/02
CHEMISTRY; METALLURGY
C08L67/04
CHEMISTRY; METALLURGY
Abstract
The present invention relates to polyester and carbodiimide containing transparent films for solar cells, which are characterized by improved resistance to hydrolysis, and also to the solar cells comprising these films. The carbodiimides have a number-average molar mass M.sub.n of >1000 to <2000 g/mol, determined by GPC, measured in tetrahydrofuran (THF) against polystyrene as standard.
Claims
1. A film comprising at least one polyester and at least one polymeric carbodiimide according to formula (I) ##STR00003## where: R.sup.1 may be identical or different and is selected from the group comprising NHCONHR.sup.3, —NHCONR.sup.3R.sup.4 or —NHCOOR.sup.5, wherein: R.sup.3 and R.sup.4 are identical or different and represent a C.sub.1-C.sub.12-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.7-C.sub.18-aralkyl radical or aryl radical, and R.sup.5 represents a C.sub.1-C.sub.22-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.6-C.sub.18-aryl or C.sub.7-C.sub.18-aralkyl radical, an unsaturated alkyl radical having 2-22 carbon atoms, or an alkoxypolyoxy- C.sub.1-C.sub.12-alkylene radical, R.sup.6, R.sup.7 and R.sup.8 are each independently methyl or ethyl, but only a maximum of one of the radicals R.sup.6, R.sup.7 and R.sup.8 is methyl, and n denotes 1 to 5, and the carbodiimides have a number-average molar mass M.sub.n of >1000 to <2000 g/mol, determined by GPC, measured in tetrahydrofuran (THF) against polystyrene as standard wherein the film is transparent and stable to hydrolysis.
2. The film according to claim 1, wherein the polyester is selected from the group consisting of polyethylene terephthalate (PET), polyethylene naphthalate (PEN), polybutylene terephthalate (PBT), polytrimethylene terephthalate (PTT), polycyclohexanedimethanol terephthalate (PCT), ester-based thermoplastic elastomers, and biobased and/or biodegradable or compostable polyesters, and mixtures thereof.
3. The film according to claim 1, wherein the film is biaxially oriented.
4. The film according to claim 1, wherein the film comprises 0.5-2.5% by weight of the at least one polymeric carbodiimide of the formula (I), based on the polyester.
5. The film according to claim 1, wherein the film comprises 1.0-2.0% by weight of the at least one polymeric carbodiimide of the formula (I), based on the polyester.
6. The film according to claim 1, wherein: n=3; R.sup.1═—NHCOOR.sup.5 where R.sup.5=cyclohexyl, and R.sup.6, R.sup.7 and R.sup.8 are methyl or ethyl, with the proviso that a maximum of only one of the radicals R.sup.6, R.sup.7 and R.sup.8 is methyl.
7. The film according to claim 6, wherein the polyester is selected from the group consisting of polyethylene terephthalate (PET), polyethylene naphthalate (PEN), polybutylene terephthalate (PBT), polytrimethylene terephthalate (PTT), polycyclohexanedimethanol terephthalate (PCT), thermoplastic urethane elastomers (TPE U), thermoplastic copolyester elastomer (TPE E), polybutylene adipate therephthalate PBAT, polylactides (PLA), and polyhydroxyalkoxides (PHA), and mixtures thereof.
8. The film according to claim 6, wherein the at least one polyester comprises a mixture of polyethylene terephthalate (PET) and polyethylene naphthalate (PEN) or a mixture of polyethylene terephthalate (PET) and polylactide (PLA).
9. The film according to claim 8, comprising 1-2% by weight, based on the polyester, of the carbodiimide.
10. A solar cell module comprising the film according to claim 1.
11. The solar cell module according to claim 10 having a backing film comprising the film according to claim 1.
12. A method for isolating solar cells from ambient environment, the method comprising enclosing at least a portion of the solar cells within the film according to claim 1 for sealing of the solar cell.
13. A transparent film comprising polylactide (PLA), polyethylene terephthalate (PET), or a combination thereof; and about 0.05 to about 2.5% by weight of at least one polymeric carbodiimide according to formula (I) ##STR00004## where: R.sup.1 may be identical or different and is selected from the group comprising NHCONHR.sup.3, —NHCONR.sup.3R.sup.4 or —NHCOOR.sup.5, wherein: R.sup.3 and R.sup.4 are identical or different and represent a C.sub.1-C.sub.12-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.7-C.sub.18-aralkyl radical or aryl radical, and R.sup.5 represents a C.sub.1-C.sub.22-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.6-C.sub.18-aryl or C.sub.7-C.sub.18-aralkyl radical, an unsaturated alkyl radical having 2-22 carbon atoms, or an alkoxypolyoxy- C.sub.1-C.sub.12-alkylene radical, R.sup.6, R.sup.7 and R.sup.8 are each independently methyl or ethyl, but only a maximum of one of the radicals R.sup.6, R.sup.7 and R.sup.8 is methyl, and n denotes 1 to 5, and the carbodiimides have a number-average molar mass M.sub.n of >1000 to <2000 g/mol, determined by GPC, measured in tetrahydrofuran (THF) against polystyrene as standard wherein the film is stable to hydrolysis.
13. The film according to claim 12, comprising 1-2% by weight, based on the polylactide (PLA), polyethylene terephthalate (PET), or a combination thereof, of the carbodiimide.
14. A solar cell module comprising the film according to claim 12.
Description
DETAILED DESCRIPTION
[0012] The present invention therefore relates to compositions comprising at least one polyester and at least one polymeric carbodiimide according to formula (I)
##STR00002##
[0013] where R.sup.1 may be identical or different and is selected from the group comprising NHCONHR.sup.3, —NHCONR.sup.3R.sup.4 or —NHCOOR.sup.5,
[0014] wherein R.sup.3 and R.sup.4 are identical or different and represent a C.sub.1-C.sub.12-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.7-C.sub.18-aralkyl radical or aryl radical,
[0015] R.sup.5 represents a C.sub.1-C.sub.22-alkyl, C.sub.6-C.sub.12-cycloalkyl, C.sub.6-C.sub.18-aryl or C.sub.7-C.sub.18-aralkyl radical, and an unsaturated alkyl radical having 2-22 carbon atoms, preferably 12-20, particularly preferably 16-18 carbon atoms, or an alkoxypolyoxy- C.sub.1-C.sub.12-alkylene radical,
[0016] R.sup.6, R.sup.7 and R.sup.8 are each independently methyl or ethyl, but only a maximum of one of the radicals R.sup.6, R.sup.7 and R.sup.8 is methyl and n denotes 1 to 5, having a number-average molar mass M.sub.n of >1000 to <2000 g/mol, determined by GPC, measured in tetrahydrofuran (THF) against polystyrene as standard.
[0017] The measurements of the number-average molar mass were evaluated using a combination of RI detector (refractive index) and viscosity detector (universal calibration).
[0018] In a particularly preferred embodiment of the invention are the polymeric aromatic carbodiimide of the formula (I) where n=3 and R.sup.1═—NHCOOR.sup.5 where R.sup.5=cyclohexyl, and where R.sup.6, R.sup.7 and R.sup.8 are methyl or ethyl, with the proviso that a maximum of only one of the radicals R.sup.6, R.sup.7 and R.sup.8 is methyl. It is furthermore preferred that n=3 is an arithmetic mean value of the measurements.
[0019] In one embodiment of the invention, the numerical values specified for n in formula (I) are arithmetic mean values.
[0020] The number-average molar masses were determined by GPC (gel permeation chromatography), measured in tetrahydrofuran (THF) against polystyrene as standard. This was evaluated using a combination of RI detector (refractive index) and viscosity detector (universal calibration). The calibration with polystyrene was carried out using reference polystyrenes of different molar masses from PSS Polymer Standards Service GmbH.
[0021] In the context of the invention, the polymeric carbodiimides are preferably aromatic polymeric carbodiimides of the formula (I) having a number-average molar mass M.sub.n of >1000 to <2000 g/mol. These are commodity chemicals and are available, for example from Rhein Chemie Rheinau GmbH.
[0022] The carbodiimide content (NCN content measured by titration with oxalic acid) of the carbodiimides used according to the invention is preferably 2-12% by weight, preferably 4-8% by weight, particularly preferably 5-7% by weight.
[0023] In one embodiment of the present invention, the polyester is polyethylene terephthalate (PET), polyethylene naphthalate (PEN), polybutylene terephthalate (PBT), polytrimethylene terephthalate (PTT) and/or polycyclohexanedimethanol terephthalate (PCT), ester-based thermoplastic elastomers such as TPE-U or TPE-E and also biobased and/or biodegradable or compostable polyesters such as Ecoflex from BASF, polybutylene adipate therephthalate PBAT (Ecovio from BASF), polylactides (PLA, from Natureworks for example) or polyhydroxyalkoxides (PHA). In this case, particular preference is given to polyethylene terephthalate (PET), polybutylene adipate terephthalate (PBAT) and polylactide (PLA).
[0024] In a further embodiment of the invention, the polyester is a mixture of polyesters. In this connection, preference is given to a mixture of polyethylene terephthalate (PET) and polyethylene naphthalate (PEN) and also a mixture of polyethylene terephthalate (PET) and polylactide (PLA).
[0025] The polyesters are commodity substances obtainable, for example, from Invista, Novapet S. A., BASF, NatureWorks.
[0026] In a further preferred embodiment of the invention, the amount of polymeric carbodiimide of the formula (I), based on the polyester, is 0.5-2.5% by weight, preferably 1.0-2.0% by weight.
[0027] The present invention further relates to films comprising the composition according to the invention.
[0028] The films according to the invention may also comprise further additives such as, for example, pigments, dyes, fillers, stabilizers, antioxidants, plasticizers, processing aids, crosslinkers etc.
[0029] The film according to the invention is preferably produced according to the following method.
[0030] In one embodiment of the invention, the polymeric carbodiimide of the formula (I) having a number-average molar mass M.sub.n of >1000 to <2000 g/mol is incorporated into the polyester at the desired concentration by means of a kneader and/or extruder.
[0031] In a further embodiment of the invention, the polymeric carbodiimide of the formula (I) is incorporated into the polyester in the form of a polyester-containing master batch by means of a kneader and/or extruder. In this case, the concentration of the carbodiimide in the master batch is preferably 10-20% by weight. The following devices may preferably be employed for the production: single-screw, twin-screw or multi-screw extruders, planetary extruders, cascade extruders, continuous co-kneaders (Buss-type) and discontinuous kneaders, e.g. Banbury-type and other units customary in the polymer industry.
[0032] Optionally used additives, pigments, dyes, fillers, stabilizers, antioxidants, plasticizers, processing aids, crosslinkers, are preferably incorporated into the polyester with the polymeric carbodiimide in a mixing step. The sequence of addition of carbodiimide and additive can be selected arbitrarily in this case.
[0033] The film is preferably produced by mixing carbodiimide or carbodiimide master batch and polyester in a melt and subsequent melt extrusion, see also EP-A 2262000.
[0034] In a preferred embodiment of the invention, the film is oriented biaxially. In one embodiment of the invention, the biaxially oriented film is produced by applying a thin layer of the molten composition according to the invention, using PET as polyester for example, on a roller, firstly in the direction of the roller and then extending it orthogonally to the direction of rotation of the roller (BOPET).
[0035] In one embodiment of the invention, the biaxially oriented film is produced on a BOPET machine, which is partly or fully sealed in order to minimize the emission of toxic gases during preparation and/or is provided with special exhaust air extraction, that are commercially available for example.
[0036] The films may be produced in any desired thickness. However, film thicknesses between 25 and 300 micrometers are preferred.
[0037] The present invention also relates to the use of the films according to the invention in solar cells, where they are preferably used for sealing and thus for protecting from environmental influences, for example moisture and ingress of foreign objects.
[0038] The present invention also relates to a solar cell module comprising at least one film according to the invention, preferably as a backing cover.
[0039] Solar cells generally consist of several layers of different materials, such as [0040] front glass, composed of windscreens for example or transparent substrates such as polycarbonate, [0041] silicon wafers, which are laminated in embedding films, generally consisting of ethylene vinyl acetate, [0042] a backing film of polyvinyl fluoride and/or polyester and [0043] an aluminium frame.
[0044] In addition, solar cells are also known in which transparent polymer layers are positioned between the front glass and the silicon wafer, for example composed of α-olefin-vinyl acetate copolymers with olefins selected from ethene, propene, butene, pentene, hexene, heptene and octene, such as described, for example, in EP-A 2031662.
[0045] In the present invention, the film according to the invention is used in solar cells as a backing film. In this case, the film can be used in all solar cells known from the prior art.
[0046] The solar cell in this case is produced according to the methods described in the prior art, starting from the standard methods for producing silicon via the casting process, Bridgeman method, EFG (edge-defined film-fed growth) process or the Czochralski process, and the subsequent production of the Si wafer and the laminating of the aforementioned material layers, wherein instead of the backing film used as standard, the film according to the invention is used. The individual layers of the solar cell can also be attached to one another in this case in laminating processes, see EP-A 2031662.
[0047] The scope of the invention encompasses all hereinabove and hereinbelow recited general or preferred definitions of radicals, indices, parameters and elucidations among themselves, i.e. including between the respective ranges and preferences in any combination.
[0048] The examples which follow serve to elucidate the invention but have no limiting effect.
Exemplary Embodiments
[0049] In the examples, the following substances were used:
[0050] PET=polyethylene terephthalate from Invista, used in Examples 1 to 5.
[0051] PLA=polylactide (polylactic acid) from NatureWorks in Examples 6 to 16.
[0052] In Examples No. 2 and 7, the aforementioned PET or PLA was extruded once in a laboratory twin screw extruder ZSK 25 from Werner & Pfleiderer prior to the measurement described below.
[0053] CDI 1 (comparitive)=Bis-2,6-diisopropylphenylcarbodiimide, a monomeric aromatic carbodiimide having a number-average molar mass of Mn=270 g/mol, and an NCN content of ca. 11% by weight, used in Examples 3, 8 and 13.
[0054] CDI 2 (comparative)=a polymeric aromatic carbodiimide of the formula
[0055] R.sup.10—R.sup.9—(—N═C=N—R.sup.9).sub.m—R.sup.10 where R.sup.9=triisopropylphenylene and R.sup.10═—NCNR.sup.9 having a number-average molar mass of Mn=1700 g/mol, and an NCN content of ca. 13% by weight, is used in Examples 4, 9 and 14.
[0056] CDI 3 (comparative)=a polymeric aromatic carbodiimide of the formula
[0057] R.sup.11—R.sup.9—(—N═C═N—R.sup.9—).sub.m—R.sup.11 where R.sup.9=triisopropylphenylene and R.sup.11═—NCO having a number-average molar mass of ca. Mn=5700 g/mol, and an NCN content of ca. 13.5% by weight, used in Examples 10 and 15.
[0058] CDI 4 (inventive)=polymeric aromatic carbodiimide of the formula (I) where n=3 as arithmetic mean value and R.sup.1═—NHCOOR.sup.5 where R.sup.5=cyclohexyl, and R.sup.6, R.sup.7=ethyl and R.sup.8=methyl, having a number-average molar mass: ca. 1400 g/mol, and an NCN content of ca. 11% by weight, used in Examples 5, 11 and 16.
[0059] CDI 5 (comparative)=polymeric aromatic carbodiimide of the formula (I) where n=2-3 as arithmetic mean value and R.sup.1═—NHCOOR.sup.5 where R.sup.5=cyclohexyl, and R.sup.6, R.sup.7=ethyl and R.sup.8=methyl, having a number-average molar mass: ca. 790 g/mol, and an NCN content of ca. 11% by weight, used in Examples 5, 11 and 16.
[0060] CDI 6 (comparative)=polymeric aromatic carbodiimide of the formula (I) where n=3-4 as arithmetic mean value and R.sup.1═—NHCOOR.sup.5 where R.sup.5=cyclohexyl, and R.sup.6, R.sup.7=ethyl and R.sup.8=methyl, having a number-average molar mass: ca. 2180 g/mol, and an NCN content of ca. 11% by weight, used in Examples 5, 11 and 16.
[0061] The carbodiimide was incorporated into the PET and the PLA by means of a laboratory twin screw extruder ZSK 25 from Werner & Pfleiderer.
[0062] The nature and amount of the carbodiimide used are presented in Table 1, and the measurement results in relation to the stability to hydrolysis.
[0063] F3 standard test specimens used for measuring elongation at break were then created on an Arburg Allrounder 320 S 150-500 injection moulding machine.
[0064] For the hydrolysis test, these F3 standard test specimens were then stored for several days at a temperature of 110° C. in steam in the case of PET and at 65° C. in water in the case of PLA and the elongation at break thereof was measured after 0, 1, 3 and 5 days in the case of PET and 0, 1, 2, 3 and 6 days in the case of PLA.
[0065] The number-average molar masses were determined by GPC (gel permeation chromatography), measured in THF against polystyrene as standard, evaluated using a combination of RI detector (refractive index) and viscosity detector (universal calibration). For this purpose, a measuring instrument from Thermo Scientific was used. The calibration with polystyrene was carried out using reference polystyrenes of different molar masses from PSS Polymer Standards Service GmbH.
[0066] The values stated in Tables 1 and 2 for the elongation at break are derived from the following calculation:
Elongation at break[%]=(elongation at break after X days/elongation at break after 0days)×100
TABLE-US-00001 TABLE 1 Ex. No 1 2 3 4 5 C C C C I Amount of CDI [%] 0 0 1.5 1.5 1.5 CDI — — CDI 1 CDI 2 CDI 4 Elongation at break 80 69 100 88 100 [%] (X = 1 day) Elongation at break 30 0 61 37 95 [%] (X = 3 days) Elongation at break 0 0 40 0 52 [%] (X = 5 days) C = comparative experiment, I = inventive
TABLE-US-00002 TABLE 2 Ex. No 6 7 8 9 10 11 C C C C C I Amount of CDI [%] 0 0 1.5 1.5 1.5 1.5 CDI — — CDI 1 CDI 2 CDI 3 CDI 4 Elongation at 64 55 100 100 100 100 break [%] (X = 1 day) Elongation at 12 0 100 100 90 100 break [%] (X = 2 days) Elongation at 0 0 61 100 28 100 break [%] (X = 3 days) Elongation at 0 0 0 0 0 89 break [%] (X = 6 days) C = comparative experiment, I = inventive
[0067] It is apparent that by using the carbodiimide according to the invention, despite the low number-average molar mass, the highest stability to hydrolysis can be achieved.
[0068] Measurement of Emissions (Off-Gassing)
[0069] The exhaust air measurement for determining the isocyanate emissions was effected during the incorporation of the carbodiimide into the polylactide (PLA) by means of a laboratory twin screw extruder ZSK 25 from Werner & Pfleiderer.
[0070] For this purpose, a portion of the exhaust air flow was passed directly at the nozzle at 21/min for 30 min through a tube impregnated with a derivatizing agent. The amount of isocyanate was then determined by HPLC (duplicate determination).
[0071] The emission values using various carbodiimides are compiled in Table 3:
TABLE-US-00003 TABLE 3 Ex. No 12 13 14 15 16 C C C C I Amount of CDI [%] 0 1.5 1.5 1.5 1.5 CDI — CDI 1 CDI 2 CDI 3 CDI 4 Isocyanate — 3440/3450 960/950 480/480 240/230 concentration [ppm]
[0072] It is apparent that the polymeric carbodiimides of the composition according to the invention exhibit extremely improved emissions characteristics.
[0073] The influence of the number-average molecular weight on the processability and properties thereof in the film production is evident from Table 4 below.
TABLE-US-00004 TABLE 4 Ability to CDI Mn pelletize Film production CDI 5 (C)) 790 g/mol not pelletable, very good homo- soft, sticky geneous film, transparent CDI 4 1400 g/mol very good, good homogeneous brittle film, transparent CDI 6 (C)) 2180 g/mol good, brittle, non-homogeneous slight threads film, haze drawn formation
[0074] Only the carbodiimide according to the invention having a number-average molecular weight between 1000 and 2000 g/mol shows a very good ability to pelletize and affords homogeneous and transparent films.