Patent Grant
9680141
The invention relates to a process for producing a separator comprising the steps of: providing a sheetlike porous substrate, a solvent, ceramic particles and an adhesion promoter; preparing a slip by mixing the solvent, the adhesion promoter and the ceramic particles; coating the substrate with the slip and thermally drying the coated substrate to obtain the separator.
Separators for the purpose of this invention are porous layered articles used for separating fluids in chemical engineering or for insulating electrodes of an electric energy store or of an electrochemical cell.
EP 1478451 B1 discloses separators comprising an organic supporting substrate having a ceramic coating. In their production process, the supporting substrate is provided in the form of a nonwoven web of organic fibres which is coated with a slip containing ceramic particles and thermally cured. A metal oxide sol is employed as an adhesion promoter. The separators thus obtained have mostly outstanding technical properties, but the metal oxide adhesion promoter of the ceramic particles limits the flexibility of the layers to a specified maximum bending radius.
A desirable separator in view of this prior art has, for example through deployment of organic adhesion promoters, an increased maximum bending radius whilst retaining the supreme technical properties of the separators described in EP 1478451 B1 and being obtainable in a process performed similarly to this prior art.
A water-based process for producing a ceramic separator with organic adhesion promoter is known from EP 2034540 A1. The layered article disclosed therein comprises an organic fibrous nonwoven web as supporting substrate having a coating of ceramic particles. The ceramic particles are bonded with an organic polymer to the fibres of the fibrous nonwoven web.
For production, a slip in the form of an aqueous dispersion containing the ceramic particles and also the dissolved binder is applied to the fibrous nonwoven web and dried. The solids content of the slip is supposed to be up to 70 wt %.
This teaching is disadvantageous because of the low ceramic content of the slip, which after coating the organic substrate leads to a low ceramic content of the separator. The separator thus obtained is therefore overwhelmingly organic and hence scarcely able to resist high thermal stresses.
The problem addressed by the invention in view of this prior art is that of specifying a process useful for producing separators having a higher ceramic content.
The problem is solved when in the process mentioned in the introduction the solvent used is a mixture of water and at least one organic component; the adhesion promoter used is a mixture of silanes and at least one thermally crosslinkable acrylic polymer; the slip is mixed with a carboxylic acid preparation and with a defoamer component free from silicone oil.
A carboxylic acid preparation for the purposes of the invention is a mixture of fatty, oily and/or polymeric carboxylic acids too weak to catalyze hydrolytic condensation of silanes. The mixture has a melting point below 80° C., preferably a melting point below 45° C. and more preferably a melting point below 25° C., melting point being defined as the lowest temperature at which the carboxylic acid preparation is free from solid constituents.
The fatty and/or oily acids may have branched or unbranched chains of in each case from 8 to 20 carbon atoms and preferably from 10 to 18 carbon atoms each.
The polymeric carboxylic acids are selected from poly(acrylic acid), poly(methacrylic acid), and/or co-polymers selected from poly(acrylic acid-methacrylic acid), or salts thereof. Carboxylic acids of this type are commercially available and familiar to a person skilled in the art under the product family name of Dolapix, obtainable for example from Zschimmer & Schwarz, or Darvan R.T. Vanderbilt Company Inc.
The carboxylic acid preparation used according to the invention contains no silicon-containing compounds.
The invention accordingly provides a process for producing a separator comprising the steps of:
The invention rests on the surprising realization that the separator obtained in this way has improved mechanical properties due to the acrylic polymer in the adhesion promoter whilst the silane content of the adhesion promoter works to provide a significant increase over the prior art in the ceramic content and hence in thermal stability.
Tests show that industrial production of the organic/inorganic adhesion promoter mixture would be impossible without admixing the carboxylic acid composition and the silicone oil-free defoamer component. It is only the use of these two processing auxiliaries which makes possible the first production of a both organically and inorganically bound separator.
The both organically and inorganically bound separator combines the advantages of purely organically bound separators with those where purely inorganic binders are employed.
Preferably, the step of thermally curing the coated substrate to obtain the separator cures the silanes and crosslinks the acrylic polymer and is carried out at a temperature below the glass transition temperature TG of the acrylic polymer. As long as the glass transition temperature of the acrylic polymer is not exceeded, embrittlement thereof is unlikely. As a result, the separator retains the preferred flexural stiffness.
Preferably, the acrylic polymer used swells little or preferably not at all in the solvent used and is infusible after crosslinking. Swelling is to be understood as meaning a volume increase on the part of the polymer due to penetration by solvent molecules.
Self-crosslinking acrylic polymers based on ethyl acrylate and methyl methacrylate which are commercially available as an aqueous dispersion are particularly suitable. Plextol BV 595 from SYNTHOMER Deutschland GmbH, Werrastr. 10, DE-45768 Marl, is one example of an aqueous dispersion of a self-crosslinking acrylic polymer based on ethyl acrylate and methyl methacrylate.
The inorganic adhesion promoter component used preferably comprises one or more silanes selected from the group comprising 3-aminopropyltriethoxysilane, 2-aminoethyl-3-aminopropyltrimethoxysilane, 3-glycidyloxy-trimethoxysilane, 3-methacryloyloxypropyltrimethoxysilane, vinyltriethoxysilane, vinyltrimethoxysilane and vinyltris(2-methoxy-ethoxy)silane, methyltriethoxysilane, 3-glycidyloxypropyltriethoxysilane.
The adhesion promoter used may preferably also be a mixture of silanes, at least one thermally crosslinkable acrylic polymer and at least one silicate, in particular tetraethyl orthosilicate. The silicate then is a second inorganic adhesion promoter component, in addition to the silane. This increases the ceramic content of the separator.
Preferably, in the mixture of silanes and acrylic polymer used as adhesion promoter silanes account for 25 to 45 wt % and acrylic polymer accounts for the remainder.
According to the invention, the ceramic fraction of solids is in the range from 45 to 60 wt % in the slip and below 90 wt % in the cured coating material. The fibrous nonwoven web coated therewith accordingly gives rise to a separator having a ceramic content of up to 80 wt %.
In one particularly preferred embodiment of the invention, the slip is admixed with a defoamer component free from silicone oil in the step of preparing the slip. This is because it was found that the silicone oils typically used as industrial defoamers—polyorganosiloxanes, that is—cause damaged areas in the coating. Admixing a silicone-free defoamer customary in the food sector makes it possible to process the acrylic polymer without having to accept the retention of gas-filled micelles in the separator.
Commercially available defoamers based on an organic supporting medium such as, in particular, paraffin oil which contain organic solids as additionally foam-breaking component are particularly useful as defoamer component. Suitable defoamers are disclosed in DE 19917186 C1 and EP 0878224 A1.
The proportion of defoamer component in the slip need not be more than 200 ppm to obtain the desired effect.
The solvent used is a mixture of water and an organic component. The organic component used can be any of the customary organic solvents. The simplest is to use an alcohol, in particular ethanol. Ethanol meets all the technical requirements, is less toxic compared with other organic solvents and is inexpensive.
Porous substrate used is preferably a fibrous nonwoven web. A fibrous nonwoven web is a textile sheet material composed of a multiplicity of randomly directed, mutually adherent fibres. It is preferable to use a fibrous nonwoven web composed of organic fibres, wherein the organic fibres are selected from polyacrylonitrile, polyester, polyimide, polyamide, polytetrafluoroethylene, polyethylene terephthalate or polyolefin.
In a preferred development of the invention, the ceramic particles have a non-spherical structure and are selected from oxides of the metals Al, Zr, Si, Ti and/or Y.
In a particularly preferred development of the invention, the acrylic polymer is introduced into the production process in the form of a dispersion. Plextol BV 595, useful as acrylic polymer, is supplied as an aqueous dispersion.
The slip is prepared by these steps in particular:
The invention also provides a separator obtainable/obtained in the process of the present invention.
A separator of this type is from 18 to 25 μm, preferably from 20 to 23 μm in thickness and has a porosity between 30 and 70%, preferably between 40 and 60%, reckoned as the quotient between the geometric density and the density measured by helium pycnometry. Its ceramic content should be up to 80 wt %.
The separator obtained according to the invention is particularly useful for insulating electrodes of an electric energy store or of an electrochemical cell, in particular in a double-layered capacitor or a rechargeable battery.
Since the organic-inorganic adhesion promoter is an essential aspect of the separator according to the invention, a mixture containing water, alcohol, silanes, at least one thermally crosslinkable acrylic polymer, a carboxylic acid preparation and a defoamer component free from silicone oil, wherefrom the adhesion promoter is derived, likewise forms part of the subject-matter of the invention.
This mixture is useful as an organic-inorganic adhesion promoter particularly in the production of separators.
The invention will now be more particularly described by means of examples.
Providing the fibrous nonwoven web:
The substrate used for producing the inventive separator is a fibrous nonwoven web composed of polyethylene terephthalate fibres. The fibres are between 1 and 15 μm in thickness, while the web has an overall thickness of 15 to 18 μm. The substrate of the inventive separator includes fibres having a softening temperature above 100° C. and a melting temperature above 110° C. Substrate porosity is in the range from 50 to 70%.
Preparing the slip:
To an initial charge of 13 kg of a 70:30 water/ethanol mixture is added 0.05 kg of a carboxylic acid composition which contains Dolapix CE 64 from Zschimmer & Schwarz GmbH & Co. KG Chemische Fabriken, DE-56112 Lahnstein, followed by the dispersal therein of 15 kg of ct1200 alumina from Almatis Inc, Leetsdale, Pa. 15065, USA. The resulting mixture has to be homogenized with a stirred motor for at least 16 hours. Thereto is added, after sufficient stirring time has elapsed, a sol composed of an initially charged 50:50 water/ethanol mixture (0.84 kg), tetraethyl orthosilicate (0.08 kg), methyltriethoxysilane (0.31 kg), 3-glycidyloxypropyltriethoxysilane (0.45 kg) and Plextol BV 595 self-crosslinking acrylic polymer from Synthomer (0.67 kg). The sol is externally prepared, stirred for at least 60 minutes and then introduced into the slip which then has to be homogenized for at least a further 16 hours. Before commencement of the coating operation, about 5 g of TEGO® Antifoam 2290 defoamer additive from Evonik Industries AG, Goldschmidtstr. 100, DE-45127 Essen, are introduced into the slip.
Coating the fibrous nonwoven web with the slip:
A fibrous nonwoven polyethylene terephthalate web 18 μm in thickness and 6 g/m2 in basis weight is coated with the above-described slip in a continuous roll-on process (linear web speed about 150 m/h, T=150° C.). The result is a separator having a thickness of 25 μm, a basis weight of 28 g/m2 and a porosity of about 55%.
Drying the fibrous nonwoven web:
The cure following the coating step takes place in-line in a circulating air oven at T≦200° C. It may be advantageous for the separator thus obtained to be subsequently heat-treated for 24 hours at T≧110° C.
Providing the fibrous nonwoven web:
A fibrous nonwoven web composed of polyethylene terephthalate fibres is provided as substrate. The fibres are from 2 to 15 μm in thickness, while the overall substrate (fibrous nonwoven web) is from 15 to 18 μm in thickness. The substrate preferably includes fibres having a softening temperature above 100° C. and a melting temperature above 110° C. Substrate porosity is in the range from 50 to 70%.
Preparing the slip:
In an initial charge of 13 kg of a 70:30 water/ethanol mixture are dispersed 15 kg of ct1200 alumina. The resulting mixture has to be homogenized with a stirred motor for at least 16 hours. Thereto is added, after sufficient stirring time has elapsed, a sol composed of an initially charged 50:50 water/ethanol mixture (0.84 kg), tetraethyl orthosilicate (0.08 kg), methyltriethoxysilane (0.31 kg), 3-glycidyloxypropyltriethoxysilane (0.45 kg) and Plextol BV 595 self-crosslinking acrylic polymer (0.67 kg). The sol is externally prepared, stirred for at least 60 minutes and then introduced into the slip which then has to be homogenized for at least a further 16 hours. Before commencement of the coating operation, about 5 g of TEGO® Antifoam 2290 defoamer additive are introduced into the slip.
The addition of Dolapix CE 64 carboxylic acid composition is eschewed in this case.
Coating the fibrous nonwoven web with the slip:
In the absence of the carboxylic acid composition, it is impossible to adjust the viscosity of the slip. Owing to the excessive viscosity, the dispersion cannot be coated in a continuous roll-on process, and therefore the inventive production of a ceramic separator is impossible in this way.
Providing the fibrous nonwoven web:
A fibrous nonwoven web substrate composed of polyethylene terephthalate fibres is provided. The fibres are from 2 to 15 μm in thickness, while the overall substrate is from 15 to 18 μm in thickness. The substrate preferably includes fibres having a softening temperature above 100° C. and a melting temperature above 110° C. Substrate porosity is in the range from 50 to 70%.
Preparing the slip:
To an initial charge of 13 kg of a 70:30 water/ethanol mixture is added 0.05 kg of Dolapix CE 64 carboxylic acid composition followed by the dispersal therein of 15 kg of ct1200 alumina. The resulting mixture has to be homogenized with a stirred motor for at least 16 hours. Thereto is added, after sufficient stirring time has elapsed, a sol composed of an initially charged 50:50 water/ethanol mixture (0.84 kg), tetraethyl orthosilicate (0.08 kg), methyltriethoxysilane (0.31 kg), 3-glycidyloxypropyltriethoxysilane (0.45 kg) and Plextol BV 595 self-crosslinking acrylic polymer (0.67 kg). The sol is externally prepared, stirred for at least 60 minutes and then introduced into the slip which then has to be homogenized for at least a further 16 hours. The addition of defoamer before commencing the coating operation is eschewed in this case.
Coating the fibrous nonwoven web with the slip:
A fibrous nonwoven polyethylene terephthalate web 18 μm in thickness and 6 g/m2 in basis weight is coated with the above-described slip in a continuous roll-on process (linear web speed about 150 m/h, T=150° C.). The resulting separator with a thickness of 25 μm, a basis weight of 28 g/m2 and a porosity of about 55% corresponds to the inventive separator, but coating quality is impaired by defects due to blistering during production.
Drying the fibrous nonwoven web:
The cure following the coating step takes place in-line in a circulating air oven at T≧200° C.
Comparison of Examples 1, 2 and 3 shows that the organically/inorganically bound separator is obtainable in the quality needed for the intended service by using the carboxylic acid composition and the defoamer.
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| 10 2012 201 251 | Jan 2012 | DE | national |
| 10 2013 200 722 | Jan 2013 | DE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2013/051626 | 1/29/2013 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2013/113673 | 8/8/2013 | WO | A |
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