US20080047548A1 - Solar collector - Google Patents

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US20080047548A1
US20080047548A1 US11/843,484 US84348407A US2008047548A1 US 20080047548 A1 US20080047548 A1 US 20080047548A1 US 84348407 A US84348407 A US 84348407A US 2008047548 A1 US2008047548 A1 US 2008047548A1
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solar collector
acid
formaldehyde
anhydride
mineral wool
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US11/843,484
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Thomas KONIETZNY
Erling Hansen
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Rockwool AS
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Rockwool International AS
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Assigned to ROCKWOOL INTERNATIONAL A/S reassignment ROCKWOOL INTERNATIONAL A/S ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: KONIETZNY, THOMAS MAREK, HANSEN, ERLING LENNART
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    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C25/00Surface treatment of fibres or filaments made from glass, minerals or slags
    • C03C25/10Coating
    • C03C25/24Coatings containing organic materials
    • C03C25/26Macromolecular compounds or prepolymers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24SSOLAR HEAT COLLECTORS; SOLAR HEAT SYSTEMS
    • F24S80/00Details, accessories or component parts of solar heat collectors not provided for in groups F24S10/00-F24S70/00
    • F24S80/60Thermal insulation
    • F24S80/65Thermal insulation characterised by the material
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B10/00Integration of renewable energy sources in buildings
    • Y02B10/20Solar thermal
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/40Solar thermal energy, e.g. solar towers

Abstract

A solar collector which comprises a mineral wool insulation based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system. This Abstract is not intended to define the invention disclosed in the specification, nor intended to limit the scope of the invention in any way.

Description

    CROSS-REFERENCE TO RELATED APPLICATIONS
  • The present application claims priority under 35 U.S.C. §119 of European Patent Application No. 06017564.3, filed Aug. 23, 2006, and of U.S. Provisional Application No. 60/859,498, filed Nov. 17, 2006. The disclosures of these applications are expressly incorporated by reference herein in their entireties.
  • BACKGROUND OF THE INVENTION
  • 1. Field of the Invention
  • The present invention relates to a solar collector, in particular, a flat-plate collector, having a mineral wool insulation based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system.
  • 2. Discussion of Background Information
  • Solar collectors transform solar radiation into heat and transfer that heat to a medium (water, solar fluid, or air). The solar heat can, for instance, be used for heating water, to back up heating systems or for heating swimming pools.
  • Solar collectors can be classified into two major categories based on the working fluid used to cool them. These two are “liquid” and “air”. Each of the two categories can then be sub-classified according to average temperature range over which they are intended to be used, and can be used effectively. These classifications are: “low temperature”, “medium temperature” and “high temperature”, with some overlap among the classifications depending on the construction of the individual collector model.
  • Low-Temperature Collectors
  • Plastic low-temperature collectors have been used widely for swimming pool heating. However, because of the deteriorating effects of ultraviolet radiation and stagnation temperatures on some plastic solar collectors, metal collectors are being more widely utilized. Unglazed collectors with aluminum absorber plates and copper water passages appear to be most cost effective over the typical metal collector life time of 20 years or more. All-copper collectors for swimming pool heating also work well, but are generally more expensive for the same performance characteristics. Copper is preferred over any other metal for water passages because of its high conductivity and compatibility with water. Almost all other metals must be separated from direct contact with the water being heated by a heat exchanger, which seriously reduces the collector efficiency.
  • Medium-Temperature Collectors
  • Medium temperature collectors typically are flat-plate collectors, enclosed in an insulated case, with one or two glazings. The intended temperature range of operation is from about 10° C. to 100° C. above ambient temperature. For the lower end of this range, single-glazed collectors with non-selective absorber plates are most cost effective. In the middle and high end of the range, selective collectors with one or two glazings become more cost effective. Typical applications include water heating, space heating and some medium temperature industrial heating uses.
  • High Temperature Collectors
  • High temperature collectors include some overlap from flat plate collectors in the medium temperature range, with selective absorber plates and heavy insulation, and may have temperature capabilities enhanced in installation by being mounted in a sun-tracking system. Many other variations of high temperature collectors include evacuated-tube flat plate types, parabolic dish reflector types, parabolic trough types and modified parabola types. Most high temperature collectors depend on some type of sun tracking, in one or two axes, for effective operation. Tracking collectors are used to a small extent for domestic water heating and space heating, but are limited in cost effectiveness and reliability by the complexities of the tracking mechanisms, where used. Other uses are highly specialized, such as in absorption cooling systems, and applications where steam must be generated, or very high temperatures are required with sacrifice of efficiency. While parabolic and other types of focusing collectors do not respond to indirect solar radiation, and collect little, if any heat when the sun is obscured enough to prevent a clear shadow from being thrown, flat plate collectors respond to radiation from all directions, and will collect diffuse radiation energy of as much as 30% of normal direct energy when there is no visible shadow.
  • Flat Plate Collectors
  • The design of a typical flat-plate collector is illustrated in the attached FIGURE and consists essentially of an absorber, a transparent cover, a housing, and an insulation. A plurality of pipes or tubes may be used for carrying a heat transfer medium. The flat plate collector shown in the FIGURE is but one of many examples of suitable solar collector designs, and the present invention is not limited to flat plate collectors or to the specific embodiment shown.
  • The heart of a solar collector is the absorber, which is usually composed of several narrow metal strips. A carrier fluid for heat transfer flows through heat-carrying pipes or tubes, which are connected to the absorber strip. In plate-type absorbers, two sheets are sandwiched together, allowing the medium to flow between the two sheets. Absorbers are typically made of copper or aluminum.
  • Swimming pool absorbers, on the other hand, are usually made of plastic (mostly EPDM, but also of polypropylene and polyethylene), as the lower temperatures involved do not require greater heat capacity.
  • Usually low-iron solar safety glass is used as a transparent cover, as it transmits a great amount of the short-wave light spectrum. Simultaneously, only very little of the heat emitted by the absorber escapes the cover (greenhouse effect). In addition, the transparent cover prevents the collected heat of being carried away by wind or convection. Together with the housing, the cover protects the absorber from adverse weather conditions. Typical housing (case) materials include aluminum and galvanized steel; sometimes fiberglass-reinforced plastic is used.
  • Case insulation is not the only important thermal insulation in a quality collector. The absorber plate and connecting tubing penetrating the housing must be thermally insulated from the case at all points of support. Heat losses can be severe if either the absorber or tubing touches the case or is supported through heat-conducting materials to the case.
  • As an insulation material, polyurethane or polyisocyanurate foam has become popular for solar collectors because it has a high insulation value and is very easy to handle. However, its use is associated with certain disadvantages. An otherwise well-designed solar collector will experience stagnation temperatures of up to 260° C. that will cause the insulation of this type to outgas and rapidly destroy the effectiveness of the collector by condensation of volatile organic components and formation of visible deposits on the transparent cover (so-called “fogging effect”). Furthermore, urethane and related products may be prohibited in collectors in fire hazard areas, because of their toxic fume production.
  • Similarly, insulating materials based on mineral fibers bonded with conventional phenol/formaldehyde resins have the disadvantage of undesired toxic formaldehyde emission at the high working temperatures of solar collectors, in particular, during stagnation periods.
  • Accordingly, there exists a need for improved insulating materials which are suitable for use in solar collectors.
  • It would be desirable to have available a solar collector which has a mineral wool insulation that avoids or at least reduces the detrimental effect of condensation or deposition of volatile binder components or binder decomposition products (“fogging”) on performance and efficiency of the solar collector.
  • It would also be desirable to have available a solar collector which has an mineral wool insulation that is not associated with the health hazards of prior art insulation materials.
  • SUMMARY OF THE INVENTION
  • The present invention provides a solar collector which has a mineral wool insulation based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system.
  • In one aspect of the collector, the MMVF may comprise one or more fibers selected from glass wool, glass filaments, ceramic fibers, basalt fibers, slag wool, stone wool and rock wool.
  • In another aspect, the insulation may comprise black mineral wool.
  • In yet another aspect, the formaldehyde-free polymeric binder system may comprise a water-soluble reaction product of an alkanolamine with a carboxylic anhydride which is obtainable by reacting at least one alkanolamine with at least one carboxylic anhydride and, optionally, treating the reaction product with a base.
  • In a still further aspect, the formaldehyde-free polymeric binder system may comprise:
  • (a) a polyacid component having acid groups, or anhydride or salt derivatives thereof; and
  • (b) a polyhydroxy component having hydroxyl groups.
  • The pH of the binder composition may be greater than about 7 and/or not greater than about 10. Further, the ratio of the number of molar equivalents of acid groups, or anhydride or salt derivatives thereof, present on the polyacid component to the number of molar equivalents of hydroxyl groups present on the polyhydroxy component may be from about 0.6:1 to about 1.2:1.
  • In another aspect, the formaldehyde-free polymeric binder system may comprise a heat-curable aqueous composition comprising
  • (a) at least one carboxyl-containing addition copolymer synthesized from
      • from about 50% to about 99.5% by weight of at least one ethylenically unsaturated mono- and/or dicarboxylic acid,
      • from about 0.5% to about 50% by weight of at least one ethylenically unsaturated compound selected from esters of ethylenically unsaturated monocarboxylic acids and monoesters and diesters of ethylenically unsaturated dicarboxylic acids with an amine having at least one hydroxyl group,
        (b) up to about 20% by weight of at least one monomer,
        (c) at least one β-hydroxyalkylamine of relatively high functionality, and
        (d) optionally, at least one surfactant.
  • In another aspect of the solar collector of the present invention, the polymeric binder system may be present in an amount of from about 0.1% to about 10% by weight of the bonded mineral wool insulation in a dry state.
  • In another aspect, the polymeric binder system may be present in a concentration gradient over a thickness of the mineral wool insulation such that a concentration of the binder system is lowest in an upper region next to the absorber of the collector and is higher in a lower region adjacent to the housing of the collector.
  • In another aspect of the collector, the mineral wool insulation may have a thermal conductivity of ≦about 0.040 W/mK and/or a bulk density of from about 10 to about 120 kg/m3.
  • The present invention also provides a solar heating system which comprises the solar collector of the present invention as set forth above, including the various aspects thereof.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The present invention is further described in the detailed description which follows, in reference to the drawings by way of non-limiting examples of exemplary embodiments of the present invention, wherein the only FIGURE is a schematic representation of a typical flat plate collector.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The particulars shown herein are by way of example and for purposes of illustrative discussion of the embodiments of the present invention only and are presented in the cause of providing what is believed to be the most useful and readily understood description of the principles and conceptual aspects of the present invention. In this regard, no attempt is made to show structural details of the present invention in more detail than is necessary for the fundamental understanding of the present invention, the description in combination with the drawing making apparent to those skilled in the art how the several forms of the present invention may be embodied in practice.
  • The present inventors have found that when using a formaldehyde-free polymeric binder system, “fogging” of the solar collector can effectively be prevented. For instance, usually there is no significant reduction of transmittancy of the transparent cover of a flat plate collector within the critical wavelength range of between about 0.2 μm and about 2.5 μm. The solar collectors according to the present invention may therefore be produced in an economical manner without requiring means for avoiding or removing any hazardous emissions. Furthermore, it has been found that the mineral wool solar collector insulation according to the present invention exhibits superior dimensional stability as compared to a needle-punched or stitched mineral wool mats.
  • The solar collector according to the present invention comprises a mineral wool insulation based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system. The other elements of the solar collector and its design and construction features are the same as with the conventional solar collectors described herein-above.
  • Absorber
  • For instance, the preferred absorbers are made of copper or aluminum. Absorbers are usually black, as dark surfaces exhibit a particularly high degree of light absorption. In order to reduce energy loss through heat emission, the most efficient absorbers have a selective surface coating. This coating enables the conversion of a high proportion of the solar radiation into heat, simultaneously reducing the emission of heat.
  • The absorber coating on both unglazed and glazed solar collector absorber plates must be stable and durable to withstand the weather exposure of unglazed collectors and the stagnation temperatures of glazed collectors without outgassing. For either type, the paint and primer should be baked, and must be a top quality coating material such as polyceram or epoxy. The most secure paint and primer bonding is obtained by using an electrostatic painting process. For collectors intended to operate in the upper end of the medium temperature range and in the high temperature range, selective absorber coating is worthwhile, because it reduces radiation losses significantly. The most effective selective coating is black chrome, applied by an electroplating process over a nickel base. If applied on a material other than copper, the plating must be applied to both sides to avoid corrosion. Other galvanically applied selective coatings include black nickel, and aluminum oxide with nickel. Another example of a suitable coating is a titanium-nitride-oxide layer, which is applied via steam in a vacuum process.
  • The tubes carrying the heat transfer medium (e.g. water or an anti-freeze solution such as water/glycol) may be soldered, brazed, snapped into grooves or inserted into spring-loaded extrusions. Wide spacing of tubes reduces collector cost, while close spacing increases cost, but improves efficiency. Cost effective collectors have sufficient spacing typically of no more than about 10 cm, preferably in a parallel grid arrangement of tubes. Another highly desirable design and construction feature is secure attachment of headers to water tubes. High quality collectors have the tubes brazed or welded to the headers and supported mechanically by insertion into sockets extracted directly from the header metal. In addition to high level insurance against leaks, and breakage at joints and from wind vibration, this method of attachment provides smooth easily balanced flow and reduces the possibility of corrosion.
  • Transparent Cover
  • The most preferred glazing material for the transparent cover in terms of service life and maintained transmissivity is tempered plate glass, borosilicate glass or Pyrex®. Of the various grades of tempered plate glass, low-iron glass has the highest transmission and lowest reflection of sunlight. These properties result in significant increases in collector efficiency.
  • The glazing material may also comprise glass having a structured surface. The structured glass surface will prevent direct reflections (of sunlight, for example), thereby suppressing an undesired mirror effect. Additionally, a structured glass surface will obscure direct view of the interior of the collector.
  • Housing
  • The housing is used to contain the insulation, provide support for the absorber and glazing, and to protect the collector from heat loss due to wind, plus the important function of keeping moisture out of the insulation from rain and dew. The housing may be made of a broad variety of materials and designs, including wood cases, aluminum extrusions with sheet aluminum back, galvanized steel, welded or formed, and even collectors without back covers. Whatever the case material and construction, it must be weather resistant, fireproof, durable, dimensionally stable, strong and completely and permanently sealed against moisture intrusion. Steel should be both galvanized and primed before painting and baking and paint should be tough and scratch-resistant. Aluminum should be used with caution in areas exposed to salt air or industrial pollution and smog in the air. Top-quality collectors use cases or frames of architectural anodized aluminum similar to those used for exterior windows.
  • Insulation
  • The mineral wool insulation of the solar collector according to the present invention is based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system.
  • Suitable MMVF comprise, for instance, glass wool, glass filaments, ceramic fibers, basalt fibers, slag wool, stone wool, rock wool and other types of man-made vitreous fibers. Black (e.g. iron-containing) mineral wool is also useful for the purposes of the present invention.
  • The term “formaldehyde-free” as used in connection with the binder system, is meant to indicate that the binder composition is substantially free of formaldehyde, and does not liberate substantial amounts of formaldehyde as a result of drying and/or curing. Typically, less than about 1 ppm formaldehyde, based on the weight of the composition, is present in a formaldehyde-free composition.
  • FIRST EMBODIMENT OF MMVF BINDER
  • In a first embodiment of the present invention, the formaldehyde-free polymeric binder system comprises the water-soluble reaction product of an alkanolamine with a carboxylic anhydride obtainable by reacting at least one alkanolamine with at least one carboxylic anhydride and, optionally, treating the reaction product with a base.
  • Preferred examples of alkanolamines for use in the preparation of this binder system include alkanolamines having at least two hydroxy groups such as, for instance, alkanolamines represented by the formula
    Figure US20080047548A1-20080228-C00001

    wherein R1 is hydrogen, a C1-10 alkyl group or a C1-10 hydroxyalkyl group; and R2 and R3 independently are C1-10 hydroxyalkyl groups.
  • Preferably, R2 and R3 independently are C2-5 hydroxyalkyl groups, and R1 is hydrogen, a C1-5 alkyl group or a C2-5 hydroxyalkyl group. Particularly preferred hydroxyalkyl groups include β-hydroxyalkyl groups.
  • Specific and non-limiting examples of suitable alkanolamines include diethanolamine, triethanolamine, diisopropanolamine, triisopropanolamine, methyldiethanolamine, ethyldiethanolamine, n-butyldiethanolamine, methyldiisopropanolamine, ethyl-isopropanolamine, ethyldiisopropanolamine, 3-amino-1,2-propanediol, 2-amino-1,3-propanediol and tris(hydroxymethyl)aminomethane. Diethanolamine is the currently preferred alkanolamine.
  • The carboxylic anhydride reactant may be selected from saturated or unsaturated aliphatic and cycloaliphatic anhydrides, aromatic anhydrides and mixtures thereof, saturated or unsaturated cycloaliphatic anhydrides, aromatic anhydrides and mixtures thereof being preferred. In a particularly preferred embodiment of the invention, two different anhydrides selected from cycloaliphatic and/or aromatic anhydrides are employed. These different anhydrides are preferably reacted in sequence.
  • Specific and non-limiting examples of suitable aliphatic carboxylic anhydrides include succinic anhydride, maleic anhydride and glutaric anhydride. Specific and non-limiting examples of suitable cycloaliphatic anhydrides include tetrahydrophthalic anhydride, hexahydrophthalic anhydride, methyltetrahydrophthalic anhydride and nadic anhydride, i.e. endo-cis-bicyclo[2.2.1]-5-heptene-2,3-dicarboxylic anhydride. Specific and non-limiting examples of suitable aromatic anhydrides include phthalic anhydride, methylphthalic anhydride, trimellitic anhydride and pyromellitic dianhydride.
  • If two different anhydrides are employed, a combination of cycloaliphatic anhydride and aromatic anhydride is particularly preferred, e.g. a combination of tetrahydrophthalic anhydride (THPA) and trimellitic anhydride (TMA). The molar ratio of cycloaliphatic anhydride to aromatic anhydride is preferably within the range of from about 0.1:1 to about 10:1, more preferably within the range of from about 0.5:1 to about 3:1. Curing tests with the system THPA/TMA have surprisingly shown that a lower molar ratio of THPA to TMA results in a higher curing speed.
  • In the preparation of the binder composition, the proportion of the alkanolamine and carboxylic anhydride reactants is preferably selected such that the ratio of equivalents of amine plus hydroxy groups (NH+OH) to equivalents of carboxy groups (COOH) is at least about 0.4, more preferably at least about 0.6. By employing these minimum ratios, too high an excess of free unreacted acid is avoided which under specific conditions might lead to a displacement of binder in the curing oven, i.e. to a non-uniform distribution in the amount of binder between the bottom and top of the mineral wool mat or web. Furthermore, high amounts of unreacted acid may increase corrosiveness.
  • On the other hand, the properties of the final binder composition, such as curing behaviour, durability and humidity resistance are determined by the total ratio of reactive groups present. Therefore, for optimum performance, the ratio of equivalents of amine plus hydroxy groups (NH+OH) to equivalents of carboxy groups (COOH) in the final binder composition is preferably adjusted to about 2.0 or less, more preferably to about 1.7 or less. In general, the final binder composition has an equivalent ratio of (NH+OH)/(COOH) within the range of from about 1.25 to about 1.55.
  • The reaction between the alkanolamine and carboxylic anhydride reactants is carried out in the usual manner, for instance, as described in WO 99/36368, WO 01/05725, WO 01/96460, WO 02/06178, WO 2004/007615 and WO 2006/061249, the entire disclosures whereof are incorporated by reference herein.
  • The reaction temperature is generally within the range of from about 50° C. to about 200° C. In a preferred embodiment and, in particular, when two different anhydrides are employed, the alkanolamine is first heated to a temperature of at least about 40° C., preferably at least about 60° C., whereafter the first anhydride is added and the reaction temperature is raised to at least about 70° C., preferably at least about 95° C. and more preferably at least about 125° C., at which temperature the second anhydride is added to the reaction mixture when substantially all the first anhydride has dissolved and/or reacted. Increasing the reaction temperature from about 70-95° C. to about 100-200° C. allows a higher conversion of monomers to oligomers. In this case, a preferred temperature range is about 105-170° C., more preferably about 110-150° C.
  • If water is added after the first anhydride has reacted, either together with the second anhydride or before addition of the second anhydride or at the end of the reaction, in an amount to make the binder easily pumpable, a binder having an increased molecular weight (compared to water addition from the start) is obtained which still has a desired pumpability, viscosity, and water dilutability and contains less unreacted monomers.
  • In order to improve the water solubility and dilutability of the binder, a base may be added up to a pH of about 8, preferably a pH of from about 5 to about 8, and more preferably a pH of about 6. Furthermore, the addition of a base will cause at least partial neutralization of unreacted acids and a concomitant reduction of corrosiveness. Normally, the base will be added in an amount sufficient to achieve the desired water solubility or dilutability. The base is preferably selected from volatile bases which will evaporate at or below curing temperature and hence will not influence curing. Specific and non-limiting examples of suitable bases include ammonia (NH3) and organic amines such as diethanolamine (DEA), triethanolamine (TEA) and dimethylethanolamine (DMEA). The base is preferably added to the reaction mixture after the reaction between the alkanol amine and the carboxylic anhydride has been actively stopped by adding water.
  • If appropriate, an additional acid monomer may be employed in the reaction and is preferably added to the reaction mixture before addition of the anhydride reactant. Specific and non-limiting examples of suitable acid monomers include di-, tri- and polycarboxylic acids such as adipic acid, citric acid, sebacic acid, azelaic acid, succinic acid, tartaric acid and trimellitic acid.
  • Furthermore, one or more polycarboxy crosslinking agents may be added after termination of the reaction and, optionally, together with the base. Suitable polycarboxy crosslinking agents include, e.g., homopolymers and copolymers of acidic monomers such as acrylic acid, alkylacrylic acid (e.g. methacrylic acid) and maleic acid, and copolymers of such acidic monomers and acrylates. The weight percentage of these polycarboxy crosslinking agents is at least about 0.5%, preferably at least about 10 wt. %, and up to about 50%, preferably up to about 30 wt. %, more preferably up to about 15 wt. %, based on the binder composition.
  • SECOND EMBODIMENT OF MMVF BINDER
  • In a second aspect of the present invention, the formaldehyde-free polymeric binder system comprises an aqueous binder composition comprising:
  • (a) a polyacid component having acid groups, or anhydride or salt derivatives thereof; and
  • (b) a polyhydroxy component having hydroxyl groups;
  • wherein the pH of the binder composition is greater than about 7 and is preferably within the range of from about 7 to about 10.
  • In an exemplary embodiment, the composition includes a polyacid component and a polyhydroxy component where the ratio of the number of molar equivalents of acid groups, or anhydride or salt derivatives thereof, present on the polyacid component to the number of molar equivalents of hydroxyl groups present on the polyhydroxy component is in the range of from about 0.6:1 to about 1.2:1.
  • In another exemplary embodiment, the composition includes a polyacid component that is a dicarboxylic acid, including, but not limited to, unsaturated aliphatic dicarboxylic acids, saturated aliphatic dicarboxylic acids, aromatic dicarboxylic acids, unsaturated cyclic dicarboxylic acids, saturated cyclic dicarboxylic acids, hydroxy-substituted derivatives thereof, and the like. In another exemplary embodiment, the composition includes a polyacid component that is a tricarboxylic acid, including, but not limited to, unsaturated aliphatic tricarboxylic acids, saturated aliphatic tricarboxylic acids, aromatic tricarboxylic acids, unsaturated cyclic tricarboxylic acids, saturated cyclic tricarboxylic acids, hydroxy-substituted derivatives thereof, and the like. In another exemplary embodiment, the composition includes a polyacid component that comprises one or more of tetracarboxylic, pentacarboxylic, and like polycarboxylic acids, and salts and anhydride derivatives thereof, and combinations thereof. It is to be appreciated that any of these polyacids may be optionally substituted, such as with hydroxy, halo, alkyl, alkoxy, and the like.
  • Exemplary polyacid components include dicarboxylic acids, such as, for example, maleic acid. Other examples of suitable polyacid components include, but are not limited to, aconitic acid, adipic acid, azelaic acid, butane tetracarboxylic acid dihydride, butane tricarboxylic acid, chlorendic acid, citraconic acid, citric acid, dicyclopentadiene-maleic acid adducts, diethylenetriaminepentaacetic acid, adducts of dipentene and maleic acid, endomethylenehexachlorophthalic acid, ethylenediamine tetraacetic acid (EDTA), fully maleated rosin, maleated tall oil fatty acids, fumaric acid, glutaric acid, isophthalic acid, itaconic acid, maleated rosin-oxidize unsaturation with potassium peroxide to alcohol then carboxylic acid, malic acid, mesaconic acid, biphenol A or bisphenol F reacted via the KOLBE-Schmidt reaction with carbon dioxide to introduce 3-4 carboxyl groups, oxalic acid, phthalic acid, polylacetic acid, sebacic acid, succinic acid, tartaric acid, terephthalic acid, tetrabromophthalic acid, tetrachlorophthalic acid, tetrahydrophthalic acid, trimellitic acid, and trimesic acid, and anhydrides and salts thereof, and combinations thereof.
  • In an exemplary embodiment, the acid groups of the polyacid component of the formaldehyde-free, thermally curable, alkaline, aqueous binder composition are neutralized with a base, and thereby converted to acid salt groups, prior to their reaction with the hydroxyl groups of the polyhydroxy component to form the polyester resin. It is understood that complete neutralization, i.e., about 100% calculated on an equivalents basis, may eliminate any need to titrate or partially neutralize acid groups in the polyacid component prior to polyester formation, but it is anticipated that less-than-complete neutralization would not inhibit formation of the polyester.
  • The term “base” as used herein refers to a base which may be substantially volatile or non-volatile under conditions which are sufficient to promote a formation of the polyester. Illustratively, the base may be a volatile base, such as, for example, aqueous ammonia; alternatively, the base may be a non-volatile base, such as, for example, sodium carbonate, and other non-volatile bases, such as sodium hydroxide, potassium hydroxide, and the like. Neutralization may be carried out either before or after the polyacid component is mixed with the polyhydroxy component.
  • In one aspect, the composition may be an alkaline composition, where the polyacid component is neutralized by the addition of a base or where certain salts of the polyacid component are used. In another exemplary embodiment, the composition may include a polyacid component, such as succinic acid, citric acid, or fumaric acid and the like that has been neutralized by the addition of a base, or is a salt. In another exemplary embodiment, the polyacid component may be maleic acid neutralized with, for example, aqueous ammonia. In another exemplary embodiment, the polyacid component may be the ammonium salt of maleate.
  • The formaldehyde-free, thermally curable, alkaline, aqueous binder composition also includes a polyhydroxy component having hydroxyl groups. In one aspect, the polyhydroxy component is sufficiently nonvolatile to maximize its ability to remain available for reaction with the polyacid component. The polyhydroxy component may be a polyvinyl alcohol, a partially hydrolyzed polyvinyl acetate, such as, for example, an ELVANOL® (available from DuPont Packaging and Industrial Polymers; Wilmington, Del., USA), or a mixture thereof.
  • In an exemplary embodiment, the formaldehyde-free, thermally curable, alkaline, aqueous binder composition may also include a catalyst capable of increasing the rate of polyester formation during curing of the binder compositions described herein. Illustratively, the catalyst may be an ammonium salt, such as, for example, ammonium para-toluene sulfonate or ammonium naphthalene disulfonate. Other suitable catalysts are contemplated to include, but are not limited to, ammonium sulfate, ammonium chloride, sulfuric acid, lacetic acid, lead acetate, sodium acetate, calcium acetate, zinc acetate, organotin compounds, titanium esters, antimony trioxide, germanium salts, sodium hypophosphite, sodium phosphite, methanesulfonic acid and para-toluenesulfonic acid, and mixtures thereof.
  • In an exemplary embodiment, the formaldehyde-free, thermally curable, alkaline, aqueous binder composition may also include a silicon-containing coupling agent, e.g., an organosilicon oil, a silylether or alkylsilyl ether. In one aspect, the silicon-containing compound may be an amino-substituted silane, such as, for example, gamma-aminopropyltriethoxy silane.
  • As described in WO 2005/087837, the entire disclosure whereof is incorporated by reference herein, the formaldehyde-free, thermally curable, alkaline, aqueous binder composition according to the second embodiment may be prepared by admixing an about 10-50 weight percent aqueous solution of a polyacid component, already neutralized or neutralized in the presence of the polyhydroxy component, an about 10-30 weight percent aqueous solution of a polyhydroxy component, and, if desired, an aqueous solution of a catalyst capable of increasing the rate of polyester formation during curing, and also, if desired, a silicon-containing coupling agent. By varying the polyacid component, the polyhydroxy component, and optional catalyst and silicon-containing coupling agent compositions, the initial concentrations thereof, and the mixing ratio of solutions, a wide range of binder solution compositions can be prepared, wherein the pH of the binder composition is alkaline, and preferably in the range of from about 7 to about 10.
  • THIRD EMBODIMENT OF MMVF BINDER
  • In a third aspect of the present invention, the formaldehyde-free polymeric binder system comprises a binder composition comprising a polycarboxy polymer (especially a polyacrylic acid polymer), a polyhydroxy crosslinking agent, and a surfactant selected from cationic surfactants, amphoteric surfactants, nonionic surfactants, and mixtures thereof.
  • The binder composition is prepared by polymerization of monomers (preferably acrylic acid) emulsified in water using conventional emulsion polymerization procedures. Suitable surfactants are used for emulsification of the monomers, including cationic, amphoteric or nonionic surfactants, and mixtures thereof, with nonionic surfactants being preferred.
  • The binder composition comprises an organic polymer or oligomer containing a plurality of pendant carboxy groups which may be a homopolymer or copolymer prepared from unsaturated carboxylic acids including acrylic acid, methacrylic acid, crotonic acid, isocrotonic acid, maleic acid, cinnamic acid, 2-methylmaleic acid, itaconic acid, 2-methylitaconic acid, and the like. Alternatively, the polycarboxy polymer may be prepared from unsaturated anhydrides including maleic anhydride, itaconic anhydride, acrylic anhydride, methacrylic anhydride, and the like, as well as mixtures thereof.
  • The low molecular weight polycarboxy polymer produced in the first step of the process is reacted with a polyhydroxy crosslinking agent, such as triethanolamine, glycerol, trimethylolpropane, 1,2,4-butanetriol, ethyleneglycol, 1,3-propanediol, 1,4-butanediol, 1,6-hexanediol, pentaerythritol, sorbitol, and the like. No catalyst is necessary in this crosslinking step.
  • The polycarboxy polymer, polyhydroxy crosslinking agent and surfactant may be mixed in a conventional mixing device. The polycarboxy polymer may be present at a concentration of from about 5% to about 50% by weight, preferably of from about 10% to about 30% by weight, based on the total weight of the mixture. Water may be added to the solids mixture in any amount which would produce an aqueous binder having a viscosity and flow rate suitable for its application to a forming fibrous glass mat by any convenient method, such as by spraying. Conveniently, water may comprise up to about 98% by weight of the binder.
  • Non-limiting examples of useful cationic surfactants include alkylamine salts such as laurylamine acetate, quaternary ammonium salts such as lauryl trimethyl ammonium chloride and alkyl benzyl dimethylammonium chlorides, and polyoxyethylene-alkylamines. Non-limiting examples of the amphoteric surfactants include alkyl betaines such as lauryl betaine.
  • Non-limiting examples of suitable nonionic surfactants include polyethers, e.g., ethylene oxide and propylene oxide condensates which include straight and branched chain alkyl and alkaryl polyethylene glycol and polypropylene glycol ethers and thioethers; alkylphenoxypoly(ethyleneoxy)ethanols having alkyl groups containing from about 7 to about 18 carbon atoms and having from about 4 to about 240 ethyleneoxy units, such as heptylphenoxy poly(ethyleneoxy)ethanols, nonylphenoxy poly(ethyleneoxy)ethanols; the polyoxyalkylene derivatives of hexitol including sorbitans, sorbides, mannitans, and mannides; partial long-chain fatty acids esters, such as the polyoxyalkylene derivatives of sorbitan monolaurate, sorbitan monopalmitate, sorbitan monostearate, sorbitan tristearate, sorbitan monooleate, and sorbitan trioleate; the condensates of ethylene oxide with a hydrophobic base, said base being formed by condensing propylene oxide with propylene glycol; sulfur containing condensates, e.g., those prepared by condensing ethylene oxide with higher alkyl mercaptans, such as nonyl, dodecyl, or tetradecyl mercaptan, or with alkylthiophenols wherein the alkyl group contains from about 6 to about 15 carbon atoms; ethylene oxide derivatives of long-chain carboxylic acids, such as lauric, myristic, palmitic, or oleic acids or mixtures of acids, such as tall oil fatty acids; ethylene oxide derivatives of long-chain alcohols such as octyl, decyl, lauryl, or cetyl alcohols; and ethylene oxide/propylene oxide copolymers.
  • The amounts of surfactants employed in the emulsion polymerization process will range from about 0.01 to about 10 weight percent, preferably about 0.2 to about 5 weight percent based on the total weight of monomers and water.
  • As described in US Patent No. 2004/0152824, the entire disclosure whereof is incorporated by reference herein, the polyacrylic acid and the polyhydroxy crosslinking agent may be mixed with water in a conventional mixing device. Water may be added to the mixture of acrylic acid monomer and polyhydroxy crosslinking agent in any amount which produces an aqueous binder mixture having a viscosity and flow rate suitable for application to a forming fibrous glass mat by any convenient method, e.g., spraying.
  • FOURTH EMBODIMENT OF MMVF BINDER
  • In a fourth aspect of the present invention, the formaldeyhde-free polymeric binder system comprises a heat-curable aqueous composition comprising
  • at least one carboxyl-containing addition copolymer synthesized from
  • from about 50% to about 99.5% by weight of at least one ethylenically unsaturated mono- and/or dicarboxylic acid,
  • from about 0.5% to about 50% by weight of at least one ethylenically unsaturated compound selected from esters of ethylenically unsaturated monocarboxylic acids and monoesters and diesters of ethylenically unsaturated dicarboxylic acids with an amine having at least one hydroxyl group,
  • up to about 20% by weight of at least one further monomer,
  • at least one β-hydroxyalkylamine of relatively high functionality, and
  • if desired, at least one surfactant.
  • The carboxyl-containing copolymers used in these binder compositions therefore incorporate from about 50% to about 99.5% by weight, preferably from about 70% to about 99% by weight, of structural units derived from ethylenically unsaturated monocarboxylic acids, ethylenically unsaturated dicarboxylic acids and/or their monoesters with C1 to C22 alkanols. In the copolymer, these acids may be wholly or partly in the form of a salt. The acidic form is preferred.
  • In the preparation of the carboxyl-containing copolymer, it is possible to use not only the above-mentioned monomers but also the anhydrides of the ethylenically unsaturated monocarboxylic acids and the anhydrides of the ethylenically unsaturated dicarboxylic acids.
  • Particularly preferred monomers for preparing the carboxyl-containing copolymers include maleic acid, maleic anhydride, acrylic acid, methacrylic acid, acrylic anhydride, methacrylic anhydride, itaconic acid, tetrahydrophthalic acid and the anhydrides thereof, and also the alkali metal salts and ammonium salts or mixtures thereof.
  • With particular preference, the copolymer incorporates structural elements derived from acrylic acid or of a mixture of acrylic acid and maleic acid in a ratio of from about 95:5 to about 40:60, in particular in a ratio of from about 90:10 to about 50:50.
  • The copolymer used in the compositions further contains from about 0.5% to about 50% by weight, preferably from about 1% to about 30% by weight, of at least one ethylenically unsaturated compound selected from esters of ethylenically unsaturated monocarboxylic acids and monoesters and diesters of ethylenically unsaturated dicarboxylic acids with at least one hydroxyl-containing amine, in copolymerized form.
  • Examples of monocarboxylic acids which are suitable as components of the esters include the above-mentioned C3 to C10 monocarboxylic acids, especially acrylic acid, methacrylic acid, crotonic acid and mixtures thereof.
  • Examples of dicarboxylic acids which are suitable as components of the monoesters and diesters include the above-mentioned C4 to C8 dicarboxylic acids, especially fumaric acid, maleic acid, 2-methylmaleic acid, itaconic acid, and mixtures thereof.
  • The amine having at least one hydroxyl group is preferably selected from secondary and tertiary amines containing at least one C6 to C22 alkyl, C6 to C22 alkenyl, aryl-C6 to C22 alkyl or aryl-C6 to C22 alkenyl radical, it being possible for the alkenyl group to have 1, 2 or 3 nonadjacent double bonds.
  • The amine is preferably hydroxyalkylated and/or alkoxylated. Alkoxylated amines preferably have one or two alkylene oxide residues with terminal hydroxyl groups. Preferably, the alkylene oxide residues each have from about 1 to about 100, preferably from about 1 to about 50, identical or different alkylene oxide units, distributed randomly or in the form of blocks. Preferred alkylene oxides are ethylene oxide, propylene oxide and/or butylene oxide. Ethylene oxide is particularly preferred.
  • The polymer preferably comprises an unsaturated compound based on an amine component incorporating at least one amine of the formula
    RcNRaRb
  • where
  • Rc is C6 to C22 alkyl, C6 to C22 alkenyl, aryl-C6-C22 alkyl or aryl-C6-C22 alkenyl, it being possible for the alkenyl radical to have 1, 2 or 3 nonadjacent double bonds,
  • Ra is hydroxy-C1-C6 alkyl or a radical of the formula II
    —(CH2CH2O)x(CH2CH(CH3)O)y—H  (II)
  • where
  • in the formula II the sequence of the alkylene oxide units is arbitrary and x and y independently of one another are integers from 0 to about 100, preferably from 0 to about 50, the sum of x and y being >1,
  • Rb is hydrogen, C1 to C22 alkyl, hydroxy-C1-C6 alkyl, C6 to C22 alkenyl, aryl-C6-C22 alkyl, aryl-C6-C22 alkenyl or C5 to C8 cycloalkyl, it being possible for the alkenyl radical to have 1, 2 or 3 nonadjacent double bonds,
  • or Rb is a radical of the formula III
    —(CH2CH2O)v(CH2CH(CH3)O)w—H  (III)
  • where
  • in the formula III the sequence of the alkylene oxide units is arbitrary and v and w independently of one another are integers from 0 to about 100, preferably from 0 to about 50.
  • Preferably Rc is C8 to C20 alkyl or C8 to C20 alkenyl, it being possible for the alkenyl radical to have 1, 2 or 3 nonadjacent double bonds. Rc is preferably the hydrocarbon radical of a saturated or mono- or polyunsaturated fatty acid. Preferred radicals Rc include, for example, n-octyl, ethylhexyl, undecyl, lauryl, tridecyl, myristyl, pentadecyl, palmityl, margarinyl, stearyl, palmitoleinyl, oleyl and linolyl.
  • With particular preference, the amine component comprises an alkoxylated fatty amine or an alkoxylated fatty amine mixture. The ethoxylates are particularly preferred. Use is made in particular of alkoxylates of amines based on naturally occurring fatty acids, such as tallow fatty amines, for example, which contain predominantly saturated and unsaturated C14, C16 and C18 alkylamines, or cocoamines, containing saturated, mono- and diunsaturated C6-C22, preferably C12-C14 alkylamines.
  • Copolymerization of the above-mentioned esters, monoesters and diesters generally brings about a reduction in the surface tension of the compositions.
  • The esterification reaction for preparing the above-described esters, monoesters and diesters takes place in accordance with customary techniques. To prepare esters of unsaturated monocarboxylic acids, the free acids or suitable derivatives, such as anhydrides, halides, e.g., chlorides, and C1 to C4 alkyl esters may be used. The preparation of monoesters of unsaturated dicarboxylic acids takes place preferably starting from the corresponding dicarboxylic anhydrides. The reaction is preferably effected in the presence of a catalyst, such as a dialkyl titanate or an acid, such as sulfuric acid, toluenesulfonic acid, or methanesulfonic acid, for example. The reaction takes place generally at reaction temperatures from about 60 to about 200° C. In accordance with one suitable embodiment, the reaction takes place in the presence of an inert gas, such as nitrogen. Water formed during the reaction may be removed from the reaction mixture by means of appropriate measures, such as distillation. The reaction may take place if desired in the presence of customary polymerization inhibitors. Essentially, the esterification reaction may be conducted to completion or just to a partial conversion. If desired, one of the ester components, preferably the hydroxyl-containing amine, may be used in excess. The extent of esterification may be determined by means of infrared spectroscopy.
  • In one preferred embodiment, the unsaturated esters, monoesters or diesters are prepared and further reacted to the copolymers without isolation of the esters, the reactions preferably taking place in succession in the same reaction vesssel.
  • To prepare the copolymers it is preferred to use a reaction product of a dicarboxylic anhydride, preferably maleic anhydride, and one of the above-described hydroxyl-containing amines.
  • The polymers may advantageously also be prepared by means of polymer-analogous reaction. For this purpose a polymer incorporating from about 80% to about 100% by weight of at least one ethylenically unsaturated mono- and/or dicarboxylic acid may be reacted with at least one hydroxyl-containing amine.
  • Examples of suitable ethylenically unsaturated mono- and dicarboxylic acids include those mentioned above. Suitable amines having at least one hydroxyl group are likewise as mentioned above. In the polymer suitable for polymer-analogous reaction, the acids may, if desired, be present wholly or partly in the form of a derivative, preferably a C1 to C6 alkyl ester.
  • In one suitable embodiment, the copolymers incorporate as further monomer at least one compound selected from olefins, preferably ethylene, propene, n-butene, isobutene and/or diisobutene, vinylaromatic compounds, preferably styrene, esters of α,β-ethylenically unsaturated mono- and/or dicarboxylic acids with C1 to C22 alkanols, preferably (meth)acrylic esters, and mixtures thereof.
  • Preferred further monomers include
  • linear and branched-chain 1-olefins or cyclic olefins such as ethylene, propene, butene, isobutene, diisobutene, pentene, cyclopentene, hexene, cyclohexene, octene, and 2,4,4-trimethyl-1-pentene, alone or mixed with 2,4,4-trimethyl-2-pentene, C8 to C10 olefin, 1-dodecene, C12 to C14 olefin, octadecene, 1-eicosene (C20), C20 to C24 olefin; oligoolefins prepared with metallocene catalysis and having a terminal double bond, such as oligopropene, oligohexene and oligooctadecene; olefins prepared by cationic polymerization and having a high α-olefin content, such as polyisobutene, for example;
  • esters of preferably C3 to C6 α,β-monoethylenically unsaturated mono- or dicarboxylic acids, such as acrylic acid, methacrylic acid, maleic acid, fumaric acid, and itaconic acid, with C1-C12, preferably C1-C8 alkanols. Such esters are in particular methyl, ethyl, n-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl and 2-ethylhexyl acrylate and/or methacrylate;
  • vinylaromatic compounds, preferably styrene, α-methylstyrene, o-chloro-styrene, vinyltoluenes and mixtures thereof.
  • Particularly preferred further monomers include ethylene, propene, isobutene, diisobutene, styrene, methyl (meth)acrylate, ethyl (meth)acrylate, n-butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, and mixtures thereof. The copolymers are prepared preferably by free-radical addition polymerization in bulk or in solution.
  • Preparation by solution polymerization takes place generally in water as solvent. It is, however, also possible for water-miscible organic solvents, such as alcohols and ketones, e.g., methanol, ethanol, n-propanol, isopropanol, n-butanol, acetone or methyl ethyl ketone, to be present in a proportion of up to approximately 30% by volume.
  • The polymerization is preferably conducted in the presence of compounds which form free radicals (initiators). The amount required of these compounds is preferably from about 0.05% to about 10%, with particular preference from about 0.2% to 5% by weight, based on the monomers used in the polymerization.
  • Examples of suitable polymerization initiators include peroxides, hydroperoxides, peroxodisulfates, percarbonates, peroxo esters, hydrogen peroxide, and azo compounds. Examples of initiators, which can be soluble in water or else insoluble in water, include hydrogen peroxide, dibenzoyl peroxide, dicyclohexyl peroxodicarbonate, dilauroyl peroxide, methyl ethyl ketone peroxide, di-tert-butyl peroxide, acetylacetone peroxide, tert-butyl hydroperoxide, cumene hydroperoxide, tert-butyl pemeodecanoate, tert-amyl perpivalate, tert-butyl perpivalate, tert-butyl pemeohexanoate, tert-butyl per-2-ethylhexanoate, tert-butyl perbenzoate, lithium, sodium, potassium and ammonium peroxodisulfates, azodiisobutyronitrile, 2,2′-azobis(2-amidinopropane) dihydrochloride, 2-(carbamoylazo)isobutyronitrile, and 4,4′-azobis(4-cyanovaleric acid). The known redox initiator systems, such as, e.g., H2O2/ascorbic acid or tert-butyl hydroperoxide/sodium hydroxymethanesulfinate, can be used as polymerization initiators as well.
  • The initiators can be employed alone or in a mixture with one another, examples being mixtures of hydrogen peroxide and sodium peroxodisulfate. For polymerization in an aqueous medium it is preferred to use water-soluble initiators.
  • In addition to the above-described carboxyl-containing polymers, the heat-curable aqueous compositions according to the fourth embodiment further comprise at least one β-hydroxylamine of relatively high functionality. The weight ratio between copolymer and β-hydroxyalkylamine is preferably from about 1:1 to about 1:0.01, more preferably from about 1:1 to about 1:0.1.
  • Appropriate higher-functional β-hydroxyalkylamines include preferably compounds of the formula
    Figure US20080047548A1-20080228-C00002
  • where R1 is a hydrogen atom, a C1 to C10 alkyl group, a C1 to C10 hydroxyalkyl group, or a radical of the formula IV
    —(CH2CH2O)x(CH2CH(CH3)O)y—H  (IV)
  • where
  • in the formula IV the sequence of the alkylene oxide units is arbitrary and x and y independently of one another are integers from 0 to about 100, the sum of x and y being >1, and R2 and R3 independently of one another are a C1 to C10 hydroxyalkyl group.
  • With particular preference, R2 and R3 independently of one another are a C2 to C5 hydroxyalkyl group and R1 is a hydrogen atom, a C1 to C5 alkyl group or a C2 to C5 hydroxyalkyl group.
  • Particular preference is given to diethanolamine, triethanolamine, diisopropanolamine, trisopropanolamine, methyldiethanolamine, butyldiethanolamine and methyldiisopropanolamine, especially triethanolamine.
  • Further preferred β-hydroxyalkylamines are the amines disclosed as component A in DE-A-19621573, the entire disclosure whereof is incorporated by reference herein. They include preferably linear or branched aliphatic compounds containing per molecule at least two functional amino groups of type (a) or (b)
    Figure US20080047548A1-20080228-C00003
  • where R is hydroxyalkyl and R′ is alkyl, preferably a compound of formula I
    Figure US20080047548A1-20080228-C00004
  • where
  • A is C2-C18 alkylene substituted or unsubstituted by one or more groups selected independently of one another from alkyl, hydroxyalkyl, cycloalkyl, OH and NR6R7, R6 and R7 independently of one another being hydrogen, hydroxyalkyl or alkyl, and which is uninterrupted or interrupted by one or more oxygen atoms and/or NR5 groups, R5 being hydrogen, hydroxyalkyl, (CH2)nNR6R7 where n is from 2 to 5 and R6 and R7 are as defined above, or alkyl, which may in turn be interrupted by one or more NR5 groups, R5 possessing the above-mentioned definitions, and/or substituted by one or more NR6R7 groups, R6 and R7 possessing the above-mentioned definitions;
  • or A is a radical of the formula:
    Figure US20080047548A1-20080228-C00005
  • where
  • o, q and s independently of one another are 0 or an integer of from 1 to 6,
  • p and r independently of one another are 1 or 2, and
  • t is 0, 1 or 2,
  • it also being possible for the cycloaliphatic radicals to be substituted by 1, 2 or 3 alkyl radicals, and
  • R1, R2 and R3 and R4 independently of one another are hydrogen, hydroxyalkyl, alkyl or cycloalkyl.
  • Preferred β-hydroxyalkylamines of relatively high functionality include, in particular, at least doubly ethoxylated amines having a molar weight of less than about 1000 g/mol, such as diethanolamine, triethanolamine and ethoxylated diethylenetriamine, for example, preferably an ethoxylated diethylenetriamine, in which on average all nitrogen-attached hydrogen atoms are monoethoxylated.
  • In one suitable embodiment, the heat-curable aqueous composition of the invention comprises at least one surfactant which may, but need not necessarily be, identical with the above-described hydroxy-containing amine.
  • If the compositions according to the fourth embodiment comprise as at least one additional surfactant at least one amine which corresponds to the hydroxyl-containing amines used above to prepare the esters and monoesters, then this amine may if desired be added separately to the compositions or may be used in an appropriate excess during the preparation of said esters.
  • As additional surfactants, the compositions preferably comprise from 0% to about 50% by weight, preferably from about 0.1% to about 40% by weight, based on the copolymer, of at least one surface-active, alkoxylated, preferably ethoxylated or propoxylated, alkylamine. Preferred alkylamines are the alkylamines of the formula RcNRaRb, as defined above, which are also present in the copolymer, particular preference being given to alkylamines of the formula
    Figure US20080047548A1-20080228-C00006
  • where R is an alkyl, alkenyl or alkylvinyl radical having at least 6 carbon atoms and m and n independently of one another are ≧1. Preferred radicals R have from about 8 to about 22 carbon atoms.
  • Further suitable long-chain amines are also for example the ethoxylated amines sold by AKZO as ETHOMEEN®, such as ETHOMEEN® C/15, a poly-oxyethylene-(5)-cocoamine, or ETHOMEEN® S/12, an oleylbis(2-hydroxyethyl)amine, or ETHOMEEN® T/25, a polyoxyethylene-(15)-tallowamine.
  • Preferred additional surfactants include ethoxylated long-chain mono- and diamines. To prepare the novel compositions use may also be made, however, of other long-chain primary, secondary or tertiary aliphatic amines. Examples are the AKZO products ARMEEN® DMOD (oleyldimethylamine), ARMEEN® M2C (dicocomethylamine), ARMEEN® NCMD (N-cocomorpholine), ARMEEN® 2C (Dicocoamine) or ARMEEN® 12D (n-dodecylamine).
  • If desired, the compositions according to the fourth embodiment may further comprise at least one additional crosslinker. Preference is given to amine or amide crosslinkers which contain at least two hydroxyl groups. Preferred crosslinkers are the alkanolamines described in DE-A-19729161, the entire disclosure whereof is incorporated by reference herein, especially the β-hydroxy-alkylamides described in U.S. Pat. No. 5,143,582, the entire disclosure whereof is incorporated by reference herein, of the formula
    Figure US20080047548A1-20080228-C00007
  • Particularly preferred β-hydroxyalkylamides are those in which R1 is hydrogen, a lower alkyl, or HO(R3)2C(R2)2C—, n and n′ are each 1, -A- is —(CH2)m—, m is from 0 to 8, preferably from 2 to 8, R2 both are hydrogen, and in each case one of the R3 groups is hydrogen and the other is hydrogen or a C1-C5 alkyl.
  • As described in DE-A-19949591, the entire disclosure whereof is incorporated by reference herein, the compositions are prepared preferably by solution polymerization in order to obtain a carboxyl-containing copolymer, followed by addition of the other components of the composition. The solution polymerization preferably takes place in water. Alternatively, it is possible to use water-miscible organic solvents, such as alcohols and ketones, e.g., methanol, ethanol, acetone, and their mixtures with water.
  • A typical process for preparing the compositions comprises
  • i) reacting at least one ethylenically unsaturated monocarboxylic acid or derivative thereof and/or at least one ethylenically unsaturated dicarboxylic acid or a derivative thereof with at least one hydroxyl-containing amine in an esterification reaction,
  • ii) reacting the reaction product(s) from step i) with at least one ethylenically unsaturated mono- and/or dicarboxylic acid and/or anhydride thereof and, if desired, at least one further monomer, to give a carboxyl-containing copolymer, and
  • iii) mixing the copolymer from step ii) with at least one β-hydroxyalkylamine of relatively high functionality, if desired, at least one surfactant, and, if desired, further additives.
  • Among the four types of MMVF binders described above, the binder according to the first embodiment is particularly preferred owing to its excellent properties.
  • Other Components of Binder Composition
  • The binder compositions according to all four embodiments of present invention may additionally comprise one or more conventional binder additives. These include, for instance, curing accelerators such as, e.g., β-hydroxyalkylamides; the free acid and salt forms of phosphoric acid, hypophosphorous acid, phosphonic acid, phosphinic acid, citric acid and adipic acid. Other strong acids such as boric acid, sulphuric acid, nitric acid and p-toluenesulphonic acid may also be used, either alone or in combination with the just mentioned acids, in particular with phosphoric, hypophosphorous acid, phosphonic or phosphinic acid. Other suitable binder additives include silane coupling agents such as γ-aminopropyltriethoxysilane; thermal stabilizers; UV stabilizers; emulsifiers; surface active agents, particularly nonionic surfactants; biocides; plasticizers; anti-migration aids; coalescents; fillers and extenders such as carbohydrates, clay, silicates and magnesium sulfate; pigments such as titanium dioxide; hydrophobizing agents such as fluorinated compounds, mineral oils and silicone oils; flame retardants; corrosion inhibitors such as thiourea; urea; antifoaming agents; antioxidants; and others.
  • These binder additives and adjuvants may be used in conventional amounts generally not exceeding about 20 wt. % of the binder solids. The amount of curing accelerator in the binder composition is generally between about 0.05% and about 5 wt. %, based on solids.
  • Final Binder Composition
  • The binder according to the present invention preferably has a solids content of from about 10% to about 40 wt. %. This is often the concentration range of the binder in storage containers before use. In a form ready for application, the aqueous binder composition preferably has a solids content of from about 1% to about 20 wt. %. In order to achieve adequate application properties and, in particular, spraying properties, the viscosity of the binder composition may be adjusted. This is accomplished, for instance, by controlling the type and concentration of binder components in the aqueous binder system. Viscosity may be kept within the desired ranges e.g. by controlling the molecular weight of the polymeric binder component (lower reaction temperature, stopping the reaction by adding water at an earlier reaction stage, etc.), and by properly adjusting the relative amounts of the binder components and water solvent.
  • Insulation Product
  • For producing the mineral wool solar collector insulation, the formaldehyde-free aqueous binder composition according to the present invention may be applied to the mineral fibers or mineral fiber products by conventional techniques such as, e.g., air or airless spraying, rotating disc atomization, padding, saturating, roll coating, curtain coating, beater deposition, or the like.
  • The mineral fibers may be any of man-made vitreous fibers (MMVF), glass fibers, ceramic fibers, basalt fibers, slag wool, rock wool, stone wool and others. The mineral fiber products include, for instance, woven and nonwoven fabrics, mats, batts, slabs, sheets and other shaped articles.
  • For the manufacture of solar collector insulation parts, the polymeric binder is normally applied in an amount of from about 0.1% to 10%, preferably from about 0.2% to about 5% by weight, of the bonded mineral wool product on a dry basis. It is also possible to establish a concentration gradient of binder over the thickness of the mineral wool insulation such that the binder concentration is lowest in the (hot) upper region next to the absorber whereas it is higher in the lower region adjacent to the housing.
  • In general, the binder composition is applied, normally by spraying, immediately after fiberization of the mineral melt whereupon the coated mineral wool is cured in a curing oven wherein heated air is passed through the mineral wool web to cure the binder. Typically, the curing oven is operated at a temperature of from about 200° C. to about 400° C. Preferably, the curing temperature ranges from about 225° C. to about 300° C. Generally, the curing oven residence time is from about 30 seconds to about 20 minutes, depending on, for instance, the product density.
  • Besides thermal curing (e.g. using heated air) other curing methods may be employed, for example curing with microwave or infrared radiation. If desired, the mineral wool web may also be subjected to a shaping process before curing.
  • The bonded mineral wool product emerging from the curing oven in the form of a bat may be cut to a desired format in accordance with the dimensions of the solar collector. The mineral wool insulation according to the present invention may, for instance, have the form of a sheet, plate, mat or strip and can be used for insulating the back and/or the side walls of the solar collector housing.
  • The mineral wool insulation according to the present invention preferably has a thermal conductivity of ≦about 0.040 W/mK and a bulk density of from about 10 to about 120 kg/m3. The thickness of the mineral wool insulation typically is from about 10 to about 80 mm.
  • In accordance with the present invention it is also possible to produce composite materials by combining the bonded mineral wool product with suitable composite layers or laminate layers formed of a heat-resistant material such as metal, glass surfacing mats and other woven or non-woven materials. In practice, the mineral wool insulation of the solar collector is often combined with a cover layer of aluminum foil or coated with a silicate paint.
  • The mineral wool insulation according to the present invention usually sustains the high temperatures (up to about 260° C.) that occur during operation of the solar collector, particularly during stagnation periods, without any harmful emissions that could cause undesired fogging of the transparent cover. The bonded mineral wool insulation usually is also substantially resistant to ageing and exhibits good moisture resistance.
  • Solar Heating Systems
  • The solar collector of the present invention may be used in solar heating systems which typically comprise the collector; a heat transfer circuit that includes the fluid and the means to circulate it; and a storage system including a heat exchanger (if the fluid circulating through the collector is not the same liquid being used to heat the object of the system). The system may or may not include secondary distribution of heat among different storage reservoirs or users of the heat. The system can be used in a variety of ways, including warming domestic hot water, heating swimming pools, heating water for a radiator or floor-coil heating circuit, heating an industrial dryer, or providing input energy for a cooling system, among others. The heat is normally stored in insulated water storage tanks.
  • It is noted that while the present invention has been described with reference to exemplary embodiments, it is understood that the words that have been used are words of description and illustration, rather than words of limitation. Changes may be made, within the purview of the appended claims, as presently stated and as amended, without departing from the scope and spirit of the present invention in its aspects. Although the invention has been described herein with reference to particular means, materials and embodiments, the invention is not intended to be limited to the particulars disclosed herein. Instead, the invention extends to all functionally equivalent structures, methods and uses, such as are within the scope of the appended claims.
  • The entire disclosures of the provisional patent application Nos. 60/859,500, 60/859,524, 60/859,525 and 60/859,526, all filed Nov. 17, 2006 are incorporated by reference herein.

Claims (20)

1. A solar collector, wherein the collector comprises a mineral wool insulation based on man-made vitreous fibers (MMVF) which are bonded by a formaldehyde-free polymeric binder system.
2. The solar collector of claim 1, wherein the MMVF comprise one or more fibers selected from glass wool, glass filaments, ceramic fibers, basalt fibers, slag wool, stone wool and rock wool.
3. The solar collector of claim 1, wherein the insulation comprises black mineral wool.
4. The solar collector of claim 1, wherein the formaldehyde-free polymeric binder system comprises a water-soluble reaction product of an alkanolamine with a carboxylic anhydride which is obtainable by reacting at least one alkanolamine with at least one carboxylic anhydride and, optionally, treating the reaction product with a base.
5. The solar collector of claim 1, wherein the formaldehyde-free polymeric binder system comprises:
(a) a polyacid component having acid groups, or anhydride or salt derivatives thereof; and
(b) a polyhydroxy component having hydroxyl groups;
wherein a pH of the binder composition is greater than about 7.
6. The solar collector of claim 5, wherein the pH of the binder composition is up to about 10.
7. The solar collector of claim 5, wherein a ratio of the number of molar equivalents of acid groups, or anhydride or salt derivatives thereof, present on the polyacid component to the number of molar equivalents of hydroxyl groups present on the polyhydroxy component is from about 0.6:1 to about 1.2:1.
8. The solar collector of claim 1, wherein the formaldehyde-free polymeric binder system comprises a heat-curable aqueous composition comprising
(a) at least one carboxyl-containing addition copolymer synthesized from
from about 50% to about 99.5% by weight of at least one ethylenically unsaturated mono- and/or dicarboxylic acid,
from about 0.5% to about 50% by weight of at least one ethylenically unsaturated compound selected from esters of ethylenically unsaturated monocarboxylic acids and monoesters and diesters of ethylenically unsaturated dicarboxylic acids with an amine having at least one hydroxyl group,
(b) up to about 20% by weight of at least one monomer,
(c) at least one β-hydroxyalkylamine of relatively high functionality, and
(d) optionally, at least one surfactant.
9. The solar collector of claim 1, wherein the polymeric binder system is present in an amount of from about 0.1% to about 10% by weight of the bonded mineral wool insulation in a dry state.
10. The solar collector of claim 1, wherein the collector comprises an absorber and a housing and wherein the polymeric binder system is present in a concentration gradient over a thickness of the mineral wool insulation such that a concentration of the binder system is lowest in an upper region next to the absorber and is higher in a lower region adjacent to the housing.
11. The solar collector of claim 1, wherein the mineral wool insulation has a thermal conductivity of ≦about 0.040 W/mK.
12. The solar collector of claim 1, wherein the mineral wool insulation has a bulk density of from about 10 to about 120 kg/m3.
13. A solar collector, wherein the collector comprises a mineral wool insulation based on man-made vitreous fibers (MMVF) which comprise one or more fibers selected from glass wool, glass filaments, ceramic fibers, basalt fibers, slag wool, stone wool and rock wool and which are bonded by a formaldehyde-free polymeric binder system which is present in an amount of from about 0.2% to about 5% by weight of the bonded mineral wool insulation in a dry state.
14. The solar collector of claim 13, wherein the insulation comprises black mineral wool.
15. The solar collector of claim 13, wherein the mineral wool insulation has a thermal conductivity of ≦about 0.040 W/mK and a bulk density of from about 10 to about 120 kg/m3.
16. The solar collector of claim 13, wherein the formaldehyde-free polymeric binder system comprises a water-soluble reaction product of an alkanolamine with a carboxylic anhydride which is obtainable by reacting at least one alkanolamine with at least one carboxylic anhydride and, optionally, treating the reaction product with a base.
17. The solar collector of claim 13, wherein the formaldehyde-free polymeric binder system comprises:
(a) a polyacid component having acid groups, or anhydride or salt derivatives thereof; and
(b) a polyhydroxy component having hydroxyl groups;
wherein a pH of the binder composition is from greater than about 7 to about 10.
18. The solar collector of claim 17, wherein a ratio of the number of molar equivalents of acid groups, or anhydride or salt derivatives thereof, present on the polyacid component to the number of molar equivalents of hydroxyl groups present on the polyhydroxy component is from about 0.6:1 to about 1.2:1.
19. The solar collector of claim 17, wherein the formaldehyde-free polymeric binder system comprises a heat-curable aqueous composition comprising
(a) at least one carboxyl-containing addition copolymer synthesized from
from about 50% to about 99.5% by weight of at least one ethylenically unsaturated mono- and/or dicarboxylic acid,
from about 0.5% to about 50% by weight of at least one ethylenically unsaturated compound selected from esters of ethylenically unsaturated monocarboxylic acids and monoesters and diesters of ethylenically unsaturated dicarboxylic acids with an amine having at least one hydroxyl group,
(b) up to about 20% by weight of at least one monomer,
(c) at least one β-hydroxyalkylamine of relatively high functionality, and
(d) optionally, at least one surfactant.
20. A solar heating system, wherein the system comprises the solar collector of claim 1.
US11/843,484 2006-08-23 2007-08-22 Solar collector Abandoned US20080047548A1 (en)

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US20100206296A1 (en) * 2009-02-13 2010-08-19 Matalon Energy, Llc Parabolic solar collector
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US20130239572A1 (en) * 2011-10-03 2013-09-19 Uv Solar Power Inc. Dual energy solar thermal power plant
WO2014053633A1 (en) * 2012-10-05 2014-04-10 Maike Brabenec Photovoltaic-thermal hybrid solar system
US20140349048A1 (en) * 2004-12-07 2014-11-27 E I Du Pont De Nemours And Company Multilayer composite films and articles prepared therefrom
US20150233606A1 (en) * 2014-02-17 2015-08-20 Savo-Solar Oy Solar thermal absorber element
US20170082302A1 (en) * 2015-09-22 2017-03-23 Ribe Jern Holding A/S Radiator with heat insulation plate and radiator arrangement
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US11136451B2 (en) 2017-10-09 2021-10-05 Owens Corning Intellectual Capital, Llc Aqueous binder compositions
US11813833B2 (en) 2019-12-09 2023-11-14 Owens Corning Intellectual Capital, Llc Fiberglass insulation product

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