AU3705802A - Method for producing sized glass fibres and resulting products - Google Patents

Method for producing sized glass fibres and resulting products Download PDF

Info

Publication number
AU3705802A
AU3705802A AU37058/02A AU3705802A AU3705802A AU 3705802 A AU3705802 A AU 3705802A AU 37058/02 A AU37058/02 A AU 37058/02A AU 3705802 A AU3705802 A AU 3705802A AU 3705802 A AU3705802 A AU 3705802A
Authority
AU
Australia
Prior art keywords
yarns
filaments
compositions
composition
mixture
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
AU37058/02A
Inventor
Bruno Gibello
Patrick Moireau
Marc Roubin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Saint Gobain Adfors SAS
Original Assignee
Saint Gobain Vetrotex France SA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Saint Gobain Vetrotex France SA filed Critical Saint Gobain Vetrotex France SA
Priority to AU37058/02A priority Critical patent/AU3705802A/en
Publication of AU3705802A publication Critical patent/AU3705802A/en
Abandoned legal-status Critical Current

Links

Landscapes

  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)

Description

AUSTRALIA
Patents Act 1990 COMPLETE SPECIFICATION STANDARD PATENT Applicant: SAINT-GOBAIN VETROTEX FRANCE S.A.
Invention Title: METHOD FOR PRODUCING SIZED GLASS FIBRES AND RESULTING
PRODUCTS.
The following statement is a full description of this invention, including the best method of performing it known to us: la PROCESS FOR THE PRODUCTION OF SIZED GLASS YARNS, AND PRODUCTS RESULTING THEREFROM In the field of reinforcing yarns and composites, the present invention relates to a process for the production of sized glass yarns, as well as to the yarns obtained and to the composites made from the said yarns.
Reinforcing glass yarns are manufactured, in a known manner, from molten glass threads flowing through die orifices. These threads are drawn in the form of continuous filaments and these filaments are then assembled as base yarns, which are then collected.
Before being assembled in the form of yarns, the filaments are usually coated with a sizing composition by passing them through a sizing member.
This deposition of sizing is very important: on the one hand, it allows the yarns to be obtained and, on the other hand, it allows these yarns to be used effectively in the production of composites. Sizing has the following usual functions: it protects the yarns from abrasion and thus prevents them from breaking during their manufacture and, possibly, during their use; it furthermore allows the combination of yarns made with organic and/or inorganic materials to be reinforced, by facilitating, in particular, the wetting and/or impregnation of the yarns by these materials. In most cases, sizing also enhances the adhesion between the glass and the material to be reinforced and allows composites to be obtained with improved mechanical properties.
It is thus important for the deposition of sizing to be carried out effectively and under the best possible conditions, so that the sizing can carry out its functions correctly.
The sizings most commonly used are aqueous sizings (containing more than 85% by weight of water) which are easy to deposit, the water then being removed by drying. Sizing compositions are normally chosen so 2 as not to undergo chemical reactions at room temperature (during storage) and at the die (for example polymerization of the sizing, thereby making it impossible to deposit). On the other hand, they can optionally be chosen to polymerize under the effect of a treatment subsequent to the deposition on the filaments. This is, in general, a heat treatment at a temperature above 100 0 C, carried out after collecting the yarns. This polymerization of the sizing makes it possible to obtain intact yarns (whose filaments are solidly attached to each other) and which are manipulable, this intact nature being especially desired in textile applications in which the yarns are subjected to high mechanical stresses.
Since each additional treatment of the sized yarns, in particular each energy-consuming treatment, results in additional cost with regard to the yarn manufacturing process and is liable to generate defects on the yarns obtained (problems of migration of the components of the sizing on a package of heat-treated yarns, for example), it is economically advantageous to find means for reducing the magnitude or number of these treatments.
However, no process currently exists which is both very cost-effective (especially insofar as it does not require an expensive energy treatment of the sized yarns during their manufacture) and which makes it possible to obtain, in good yields (in particular at high rates, with a reduced level of breakage and with no variation in the quality of the yarns, which would necessitate rejection of some of the products), an entire range of sized yarns for various applications, these sized yarns having a coating and uniform characteristics over their entire length.
The object of the present invention is thus to provide a process for the production of sized glass yarns of constant quality in favourable yield, this process being both cost-effective and affording the best possible yarn-coating conditions. The object of 3 the present invention is also to provide a process which makes it possible to obtain, with these same advantages, an entire range of glass yarns which can be used in various applications. The object of the present invention is also to obtain yarns which can be used and manipulated directly to prepare composites and which have a uniform coating over their entire length.
This object is achieved by the process according to the invention, in which the conditions necessary for obtaining the desired yarns with the advantages described above are defined.
According to the present invention, there is provided glass yarn coated with a sizing composition including at least one base system which is polymerizable at room temperature.
In this process, threads of molten glass are drawn, these threads coming from orifices located at the bottom of one or more dies, in the form of one or more sheets of continuous filaments, and the filaments are then assembled into one or more yarns which are collected on one or more moving support(s), this process consisting in depositing a first stable composition, having a viscosity of between 0.5 and 250 cP, onto the surface of the filaments, in depositing at least a second stable composition, supplied separately of the first and having a viscosity of between 0.5 and 300 cP, onto the surface of the filaments or of the yarn(s), at the very earliest during the deposition of the first composition and at the very latest during the collection of the yarn(s), the difference in viscosity between the compositions deposited being less than 150 cP, the mixture of the compositions deposited also having the functions of a sizing composition and being capable of polymerising at room temperature.
The process according to the invention has several advantages: firstly, it makes it possible to dispense with the treatments (heat treatments or \\melb-fils\hoe\PCarke\Keep\Retypes\P45725 Div of 77722-98 saint-gobaindoc 29/04/02 3a irradiation) usually used to polymerise sizing compositions on glass yarns, which represents a considerable economy. In the same way, it avoids the treatment of certain effluents, the release of effluents generally being associated with the polymerisation heat treatments carried out. The process THE REST OF THIS PAGE IS INTENTIONALLY BLANK \\melbfiles\homeS\PClarke\Keep\Retypes\P45725 Div of 77722-98 sainC-gobain.doc 29/04/02 4 according to the invention is of improved production efficiency, the yarns obtained especially being of uniform quality over their entire length. Furthermore, it allows better control over the sizing polymerization reactions carried out on the yarns and reduces the risks of these yarns breaking. This process also reduces the risks of irregular migration of sizing components on the yarn and/or the risks of coloration of the yarns or of deformation of the packages associated with certain yarn treatments (such as drying). In other respects, the process is applied with the same advantages to the preparation of different types of sized yarns for the purpose of various applications. It also makes it possible to obtain yarns coated with novel compositions, based on systems not existing in current sizings on account of their reactivity and instability. The process according to the invention thus makes it possible to broaden considerably the field of sizings and opens the way to novel products anTd novel applications.
According to the invention, the term "glass yarns" is understood to refer to yarns based on glass, i.e. not only yarns formed solely of glass filaments but also yarns formed of glass filaments and of organic filaments, in particular thermoplastic filaments. In the latter case, during the drawing of the glass filaments, the organic filaments are extruded and entrained simultaneously (or the organic yarns obtained, for example, from packages are supplied simultaneously), the paths followed by the glass filaments and the organic filaments (or yarns) converging on one another before the said filaments are assembled into at least one mechanically-entrained composite yarn.
The glass filaments can be drawn in the form of a sheet from a die or in the form of several sheets from one or more dies and can be assembled into one or more yarns. The draw rate of the glass filaments in the process according to the invention is generally between 5 8 and 75 m/s, usually between 10 and 60 m/s. In general and preferably according to the invention, the compositions (in particular the first composition) are deposited on the filaments which are cooled to a temperature below 90 0 C, advantageously below 75 0 C, in order to avoid any risk of selective evaporation of components of the compositions deposited and to afford better control over what is deposited on the filaments.
Optionally, the cooling of the filaments can be accelerated using a device for spraying a coolant fluid. If necessary, this fluid can be removed before the first composition is deposited.
The first composition is deposited during the drawing, at the very latest, when the filaments are assembled into yarn(s) and preferably before the filaments are assembled into yarn(s), so as to avoid any breakage of the filaments rubbing against the assembly member and in order to obtain distribution of the first composition over all of the filaments. The coating can be carried out, for example, using a roller, using a sprayer, using a device which also acts as an assembly member, etc. or can also be carried out by means of other yarns or filaments coated with the first composition and placed in contact with the glass yarns in the case, for example, of the preparation of composite yarns.
Preferably, the second composition is also deposited on the filaments at the very latest during assembly of the filaments into yarns. This composition can also be deposited using a roller, using a sprayer, using a device which also acts as an assembly member, etc. or can be carried out by means of other yarns or filaments coated with this composition and placed in contact with the glass filaments, in which case the first composition is preferably deposited directly on the glass filaments at least, before being combined with the other yarns or filaments.
According to the invention, the expression "at the very earliest during the deposition of the first 6 composition" is understood to mean that the compositions are mixed immediately before (within a few seconds of, or even in the second preceding, the deposition) their joint deposition onto the filaments or are mixed onto the filaments or yarn(s). In the latter case, each composition is generally deposited on the filaments or yarn(s) using a deposition means which is specific for it (at least two separate deposition means being necessary in this case, these two means being placed on the same side of the filaments or yarn(s) or on either side of the filaments or yarn(s)) and the compositions are mixed by interdiffusion (diffusion of the compositions into each other) at the surface of the filaments. It can also be advantageous to use only one device to deposit the two compositions, the two compositions then being supplied separately and being mixed, in this case, in the device, optionally on the filaments, or even immediately before (within a few seconds of, or even in the second before) introduction into the deposition device. This single deposition device can be a remote-application device (sprayer) or a contact device, the latter type of device having the advantage of allowing better control over the amounts deposited onto the filaments. In the latter case, it is important- for the compositions to be fully deposited on the filaments after they have been placed in contact in the device, this being made possible especially by the choice of the amounts of composition deposited (these amounts being specified later in a preferred embodiment of the invention).
It is clear that the present invention is described on the basis of the deposition of two separate compositions, but it also applies in the case of the deposition of a larger number of compositions.
In this case, each additional composition is preferably defined on the model of the second composition, i.e.
each composition is stable and supplied separately, each additional composition has a viscosity of between and 300 cP and each additional composition is 7 deposited at the very earliest during the deposition of the first composition and at the very latest during the collection of the yarn(s). Furthermore, in accordance with the general definition, the difference in viscosity between the compositions (for example between the first and each of the subsequent compositions deposited before collection) must be less than 150 cP, the mixture of the compositions also having the functions of a sizing composition and being capable of polymerizing at room temperature. It is worth pointing out, in this respect, that, in the general definition, the "mixture of the compositions" refers to the mixture of all of the compositions deposited on the yarn(s) before collection (and not necessarily to the mixture -of the first two compositions deposited in the case of the deposition of a number of compositions which is greater than two).
The term "stable composition" is understood to refer mainly to a "composition which does not polymerize without supplying at least one other component", it being possible in many cases for this composition to be stored for many days, at storage temperatures which can be up to 40 or 50 0
C.
Each of the compositions deposited can be chosen from compositions which are aqueous, anhydrous or which have a low content of solvent. Preferably, compositions comprising less than 5% by weight of solvent of compounds acting solely as solvent), or even totally free of solvent, are used. The optional solvents are essentially organic solvents required to dissolve certain compounds. The absence or the limited presence of solvents makes it possible to avoid all the problems associated with the presence of water (drying problems) or of organic solvents (problems of toxicity of the solvents in particular) on the yarns. The compositions are generally in the form of at least partially miscible and preferably miscible solutions (it is possible, however, for certain specific applications, for at least one of the compositions 8 forming the mixture to be in the form of a dispersion emulsion, suspension or not to be miscible with one or other of the compositions forming the mixture) The viscosity of the compositions is particularly high, in order to guarantee good deposition of the compositions, and most particularly the difference in viscosity between the compositions. If the difference in viscosity exceeds 150 cP, the yarns obtained have an insufficiently uniform coating.
Preferably and as a general rule, if the difference in viscosity is large, the first composition deposited has the lowest viscosity among the compositions deposited.
The difference in viscosity is preferably less than 135 cP and can be zero. The difference in viscosity is preferably proportionately lower the less miscible the compositions mixed together. The viscosity is equal to the composition deposition temperature, this temperature generally being between 20 and 70 0 C, and usually between 30 and 60 0
C.
Preferably, the first composition has a viscosity (at the time of deposition) of between 1 and 200 cP (in a particularly preferred manner between 1 and 150 cP) and the second composition (or the subsequent ones) has(have) a viscosity (at the time of deposition) of between 1 and 250 cP (in a particularly preferred manner between 1 and 200 cP) Preferably, when one or more of the compositions used has(have) a solvent content of less than the viscosity of this(these) composition(s) is between 10 and 250 cP (preferably between 20 and 150 cP) for the first composition and between 10 and 300 cP (preferably between and 200 cP) for the subsequent compositions. In the case of the use of one or more aqueous compositions, the viscosity is between 1 and 25 cP for the first composition and is between 1 and 50 cP for the subsequent compositions.
The amount of compositions deposited is also, in many cases, an important factor in combination with the other characteristics of the process according to 9 the invention. By keeping to the amounts indicated below, it is possible in particular, in certain cases, to avoid an uncontrolled and/or possibly non-uniform polymerization of the mixture on the yarns and to avoid phenomena of pollution of the composition deposition means by another composition when contact-deposition devices placed one after the other are used, these phenomena leading in particular to breaking of the yarns (such phenomena being proportionately larger in magnitude the higher the draw rate, and being inevitable at larger amounts when, for example, it is desired to make prepregs directly). Thus, preferably and as a general rule according to the invention, the amount of each composition deposited represents, by weight, excluding solvent if possible solvents are removed), from 0.1 to 2% of the weight of the filaments, in a particularly preferred manner from 0.3 to 1.5% of the weight of the filaments. Also preferably, the loss on ignition of the yarns obtained (coated with the assembly of compositions) is less than 3% by weight.
As a general rule, when one (or more) composition(s) containing less than 5% by weight of solvent is(are) used, the amount of this(these) composition(s) (solvent(s) included) deposited on the filaments is approximately between 0.1 and 2% by weight of the filaments, and in the case of one or more aqueous compositions, the amount of this(these) composition(s) (solvent(s) included) is, rather, between 1 and 15% by weight of the filaments.
When the mixture coating the yarns according to the invention consists solely of a first composition and of a second composition, the ratio of the two amounts by weight of each of these compositions on the filaments or yarns (the possible solvent(s) being taken into account in this case to evaluate the amounts) is also, preferably, between 1/10 and 10 the first composition represents approximately from 9 to 91% by weight of the mixture deposited on the filaments). In a 10 particularly preferred manner, mainly in the case in which the compositions contain less than 5% by weight of solvent, this ratio is between 1/3 and 3 the first composition represents from 25 to 75% by weight of the mixture deposited on the filaments) to allow good interdiffusion of the compositions with each other. More generally, irrespective of the number of compositions deposited on the filaments, these compositions are preferably deposited in similar amounts to each other.
The compositions are chosen so as to polymerize, after they have been mixed together, on the filaments or yarns and are preferably chosen. such that the polymerization of the mixture the reactive part of the mixture) at room temperature takes place to at least 80% to at least 80% of the expected conversion rate) in less than 80 hours, and preferably in less than 50 hours, after deposition and mixing of the compositions, in particular of the reactive compositions (which are liable to be involved in the polymerization reaction of the mixture), on the filaments. The yarns thus obtained are easy to manipulate and pose no problems of subsequent implementation.
In the present invention, the terms "polymerization", "polymerize" etc. are understood to mean "polymerization and/or crosslinking", "polymerize and/or crosslink", etc. Moreover, the term "room temperature" also means, in the process according to the invention, "without any additional supply of energy" and covers a temperature range below 600C, generally from 15 to 450C.
Polymerization of the mixture is initiated at the very earliest during the mixing of at least two reactive compositions, and at the very latest during the collection of the yarns.
The compositions are also chosen such that their mixture has the characteristics and functions essential of a sizing composition (protection of the 11 yarns against abrasion, enhancement of the wetting and/or impregnation of the yarns by the material to be reinforced and/or of the adhesion of glass to this material, etc.). The "mixture" formed of at least two compositions mentioned in the present invention can thus also be denoted by the term "sizing composition".
The mixture of compositions present on the sized yarns comprises at least one base system which is polymerizable at room temperature. According to the invention, the terms "mixture comprising" and "composition comprising" are understood to refer to the "mixture (or composition, respectively) one of whose initial constituents is independently of the change of this constituent within the mixture (or the composition, respectively) The term "base system" is understood to refer to the compound(s) which is(are) essential for the sizing and which form part of the structure of the polymerized sizing. As a general rule, the base system represents between 55 and 100% by weight, mainly between 60 and 98% by weight, and in most cases between 65 and 96% by weight, of the "solids" of the mixture (or of the mixture from which the possible solvent(s) has(have) been removed). The proportion of the base system generally increases as the desired integrity increases.
The base system comprises at least one group of component(s) capable of homopolymerizing at room temperature and/or comprises at least two groups of component(s), the components of the two groups being capable of copolymerizing at room temperature.
According to the invention, the expression "group of component(s)" is understood by extension to refer to one or more components of the same reactivity. The term "same reactivity" is understood to mean "the same ability to polymerize with or in the presence of certain components (of the mixture) or in the presence of certain functions (of component(s) of the mixture). The components of the same reactivity can be subdivided into one or more subgroups, the component(s) 12 of each subgroup having at least one reactive function (capable of taking part in the polymerization reaction of the mixture) which is common (in common).
Preferably, the base system essentially consists of a group of component(s) capable of homopolymerizing at room temperature or of two groups of component(s) capable of polymerizing (homopolymerizing or copolymerizing) at room temperature, this(these) group(s) representing at least 60% by weight, preferably at least 80% by weight and up to 100% by weight in most cases, of the base system.
Preferably, the base system comprises at least two groups of component(s) (capable of homopolymerizing or of copolymerizing), the two groups being derived respectively from different compositions deposited on the yarn.
Moreover, in a preferr.d manner according to the invention, mainly in the case in which the mixture comprises less than 5% by weight of solvent, the base system comprises at least 60% by weight (in a particularly preferred manner at least 75% by weight and up to 100% by weight in most cases) of component(s) with a molecular mass of less than 750 (in a particularly preferred manner less than 500) In most cases according to the invention, and in a preferred manner, these components with a molecular mass of less than 750 are monomers (mono- or polyfunctional monomers), but the base system can also comprise one (or more) component(s) with a molecular mass of less than 750 in the form of oligomer(s) or polymer(s) containing partially polymerized functions.
According to one embodiment of the invention, the mixture of compositions deposited on the filaments comprises, in addition to the base system, at least one catalyst (or accelerator or initiator) which promotes the polymerization of all or part of the component(s) of the base system. The amount of catalyst(s) in the mixture of the compositions is generally less than 13 by weight of the mixture, and is preferably less than 3% by weight of the'mixture.
As a general rule, each reactive component of the mixture is supplied by a composition different from the one (those) supplying the component(s) capable of reacting with the said component or giving rise to the reaction of the said component. It is possible, however, to envisage supplying, to the same composition, components which need to react together or part of which need to react together in the presence of the other part, if one part of the components is blocked so as to prevent the spontaneous reaction. In this case, at least one deblocking agent which allows the polymerization reaction to be triggered is supplied to another composition.
Advantageously, a majority of component(s) (at least 50%) of the base system supplied by one of the reactive compositions is at least partially miscible with the composition(s) comprising the component(s) which need to polymerize with this(these) component(s) and/or which need to promote the polymerization of this(these) component(s).
According to a preferred embodiment of the present invention, the mixture comprises at least one base system, this system comprising at least a first group of component(s) capable of homopolymerizing at room temperature and at least a second group of component(s) capable of homopolymerizing at room temperature, the mixture also comprising at least a first initiator which promotes the homopolymerization of the components of the first group and at least a second initiator which promotes the homopolymerization of the components of the second group. The first group of component(s) is supplied by at least one of the compositions, for example the first composition, and the second group of component(s) is preferably supplied by one or more compositions different from that(those) supplying the first group, for example supplied by the second composition. Similarly, the first initiator is 14 preferably supplied by one or more compositions which are different from that(those) supplying the first group, for example supplied by the second composition, and the second initiator is preferably supplied by one or more compositions which are different from that(those) supplying the second group, for example supplied by the first composition.
By way of non-exhaustive example, the first group can consist, in the above embodiment, of one or more components chosen from components having at least one epoxy reactive function, the second group can consist of one or more components chosen from components having at least one (meth)acrylic reactive function, the first initiator can consist of one or more components chosen from Lewis acids and Lewis bases and the second initiator can consist of one or more peroxides.
According to another particularly preferred embodiment of the present invention, the mixture comprises at least one base system, this system comprising at least a first group of component(s) and at least a second group of component(s) capable of copolymerizing at room temperature with the component(s) of the first group. The first group of component(s) is supplied by at least one of the compositions, for example the first composition, and the second group of component(s) is preferably supplied by one or more compositions different from that(those) supplying the first group, for example supplied by the second composition.
Optionally, the mixture also comprises at least one catalyst or initiator which promotes the copolymerization reaction, this catalyst being supplied by any one of the compositions.
By way of non-exhausting example, the first group can consist, in the above embodiment, of one or more components chosen from components having at least one epoxy reactive function, and the second group can consist of one or more components chosen from components having at least one amine reactive function or 15 from components having at least one anhydride reactive function, it being possible for the optional catalyst(s) to be chosen in particular from tertiary amines, etc.
The choice of the component(s) of the base system and the amount of this(these) component(s) depends in particular on the organic material which needs to be reinforced by the yarns according to the invention and on the application envisaged. In the case especially in which the base system of the mixture comprises at least a first and a second group of component(s) capable of copolymerizing, the respective amounts of these groups are chosen as a function of the desired polymerization (it may be advantageous, for example, to have an excess of component(s) of one of the groups in order to keep certain reactive functions free after polymerization for the purpose of combining them with certain organic materials). It is thus possible to obtain yarns coated with a sizing composition which is partially or fully polymerized. The process according to the invention allows, in this respect, better control of the polymerization processes than processes which use a polymerization heat treatment, since heat treatments promote the appearance of spurious reactions (for example uncontrolled and generally undesired oxidation-type reactions).
Besides the component(s) essentially forming part of the polymerized sizing structure and the optional catalyst(s), the mixture deposited on the yarns according to the invention can comprise one or more components (denoted hereinbelow as additives) supplied by one and/or other of the compositions and imparting specific properties to the mixture.
In particular, the mixture preferably comprises one or more coupling agents, as component(s) of the base system for the coupling agent(s) involved in the polymerization reaction and/or solely as additive(s) for the coupling agent(s) not involved in the polymerization reaction. The proportion of the coupling 16 agent(s) is between 0 and 25% by weight of the mixture, and preferably between 5 and 20% by weight of the mixture. These coupling agents are generally required for the mixture to have the functions of a sizing composition. They can be chosen, for example, from the following components: silanes such as gamma-glycidoxypropyltrimethoxysilane, gamma-methacryloxypropyltrimethoxysilane, polyethoxylated-propoxylated trimethoxysilane, gamma-acryloxypropyltrimethoxysilane, vinyltrimethoxysilane, phenylaminopropyltrimethoxysilane, styrylaminoethylaminopropyltrimethoxysilane, aminopropyltriethoxysilane, tert-butylcarbamoylpropyltrimethoxysilane, etc.; titanates, zirconates, siloxanes, etc.
The mixture can also comprise, generally as additive not involved in the polymerization reaction, at least one textile implementation agent acting essentially as a lubricant, in proportions of between 0 and by weight of the mixture, and preferably less than or equal to 20% by weight. Lubricant textile agents are necessary in many cases for the mixture to have the functions of a sizing composition. They can be chosen, for example, from the following components: fatty esters, glycol derivatives (in particular ethylene glycol or propylene glycol), such as an isopropyl or cetyl palmitate, an isobutyl stearate, a decyl laurate, an ethylene glycol adipate, a polyethylene glycol or a polypropylene glycol with a molecular weight of less than 2000, an isopropyl stearate, etc.
The mixture can also comprise at least one film-forming agent generally acting as a slip agent and facilitating the yield of yarn, in proportions of between 0 and 10% by weight of the mixture, and preferably less than or equal to 5% by weight. The presence of this(these) agent(s) prevents any appreciable rubbing of the filaments (for example on sizing devices) when the filaments are drawn at a high rate more than 40 m/s and/or when they are very thin, these agents, however, being expensive and 17 possibly resulting in a decrease in the mechanical properties of the composites. The film-forming agents can be chosen, for example, from the following components: silicones, siloxanes or polysiloxanes such as glycidyl(n)polydimethylsiloxane, alpha-omegaacryloxypolydimethylsiloxane, etc., silicone derivatives such as silicone oil, etc.
The mixture can also comprise at least one agent for adaptation to the materials to be reinforced, in the case of cement materials in particular.
The glass yarns obtained according to the process of the present invention are coated with a sizing composition comprising at least one base system which is polymerizable at room temperature, this base system comprising at least one group of component(s) capable of homopolymerizing at room temperature and/or comprising at least two groups of component(s), the components of the two groups being capable of copolymerizing at room temperature, the sizing composition also comprising, if necessary, at least one catalyst and/or at least one deblocking agent which is(are) capable of triggering the polymerization reaction.
As indicated above, the yarns obtained have a coating which is partially or fully polymerized, this coating generally being uniform over its entire thickness. In certain very specific cases and with suitable deposition means, it is possible, however, to envisage having a polymerization only on a certain thickness of this coating (for example at the interface of the two compositions deposited).
These yarns are generally collected in the form of packages on rotating supports. Irrespective of the speed of the polymerization reaction, absence of excessive sticking together of the yarns on the packages is generally observed, this being the case even for low crossing angles of less than 1.50. The yarns obtained according to the invention are easy to unwind from packages and are easy to manipulate.
18 The yarns can also be collected on travelling receiver supports. They can, in fact, be sprayed by a member which also serves to draw them, towards the collection surface which moves transversely to the direction of the sprayed yarns, in order to obtain a sheet of interwoven continuous yarns known as a "mat".
They can also be chopped before collection by a member which also serves to draw them.
The yarns obtained according to the invention can thus be in different forms after collection, in particular in the form of bobbins of continuous yarns (roving, cakes, cops, etc.), in the form of chopped yarns, they can be assembled in the form of braiding, slivers, mats or networks, which may or may not be woven, etc. The glass filaments forming these yarns can have a diameter of between 5 and 30 microns and the glass used to make these filaments can be any type of glass known for the preparation of reinforcing yarns: E glass, AR (alkali-resistant) glass, etc.
The yarns according to the invention can advantageously be combined with various materials to be reinforced in order to make composite articles with good mechanical properties. The composites are advantageously obtained by combining at least some glass yarns according to the invention and at least one organic and/or inorganic material, the glass content within these composites being generally between 30 and by weight.
The examples which follow illustrate the present invention without, however, limiting it.
EXAMPLE 1 Filaments 14 microns in diameter, obtained by drawing molten glass threads, are coated with the following first stable composition, expressed as a weight percentage relative to the mixture of the first and second compositions deposited: Components (first group) of the base system with a molecular mass of less than 750: trimethylolpropane triglycidyl etherm 1 20.0% 19 diglycidyl ether of cyclohexanedimethanol 2 15.0% cresyl glycidyl ether' 3 18.0% The viscosity of this composition (as well as of the following compositions) is measured on a Sofraser-type machine (Mivi 4000) sold by the company Sofraser.
The viscosity obtained for this composition is 44 cP at 20 0 C (which corresponds to a viscosity of about 15 to 30 cP at the deposition temperature, which is about 40 to 60 0 C in this example).
The filaments are then coated with the following second stable composition, expressed as a weight percentage relative to the mixture of the first and second compositions deposited: Components (second group) of the base system with a molecular mass of less than 750: isophorone diamine 20.5% Catalyst: organometallic amine 4 Additives: lubricant textile agent based on fatty acid esters and surfactants 5 10.0% gamma-methacryloxypropyltrimethoxysilane coupling agent 6 3-4,5-dihydroxyimidazol-l-yl- (propyltriethoxysilane) coupling agent' 7 This composition has a viscosity of 58 cP at 0 C (which corresponds to a viscosity of about 13 to cP at the deposition temperature of about 40 to 60 0 C) The filaments are then assembled into yarns, which are wound in the form of roving. The yarns obtained have a yarn count (linear mass) of 300 tex (g/km) approximately and a loss on ignition of 0.6%.
The yarns obtained are easy to manipulate and have a uniform coating over their entire length, polymerization (in the present case this is a copolymerization) being carried out over approximately 18 h after mixing together the compositions on the filaments. These yarns have good abrasion resistance 20 and allow organic materials to be reinforced effectively.
EXAMPLE 2 Filaments 14 microns in diameter, obtained by drawing molten glass threads, are coated with the following first stable composition (weight percentages relative to the mixture of the first and second compositions): Components (first group) of the base system with a molecular mass of less than 750: diglycidyl ether of cyclohexanedimethanol 2 18.0% cresyl glycidyl ether 3 18.0% gamma-glycidoxypropyltrimethoxysilane coupling agent 9 10.0% Catalyst (for the second group): dibenzoyl peroxide 8 This composition has a viscosity of 32 cP at 0 C (which corresponds to a viscosity of about 15 to cP at the deposition temperature of about 40 to 60 0
C).
The filaments are then coated with the following second stable composition (weight percentages relative to the mixture of the first and second compositions): Components (second group) of the base system with a molecular mass of less than 750: ethoxylated trimethylolpropane triacrylate 1 0 15.0% hexanediol diacrylate 11 16.0% gamma-methacryloxypropyltrimethoxysilane coupling agent 6 10.0% Components (third group) of the base system with a molecular mass of less than 750 and catalyst (for the first group): 2-(4,6-dimethylaminomethyl)phenol 12 This composition has a viscosity of 24 cP at 0 C (which corresponds to a viscosity of about 12 to cP at the deposition temperature of about 40 to 0 C) The filaments are then assembled into yarns, which are wound in the form of roving. The yarns 21 obtained have a yarn count of about 150 tex and a loss on ignition of The yarns obtained are easy to manipulate and have a uniform coating over their entire length, polymerization (in the present case this is a copolymerization and crossed homopolymerizations) being carried out over about 72 h after mixing together the compositions on the filaments.
These yarns are extracted from the packages in order to measure their abrasion resistance. This resistance is evaluated by weighing the amount of flock formed after passing the yarns over a series of lifting rods. For different yarns obtained according to the present invention, the amount of flock weighed is about 1 mg of flock per kg of yarn tested. This shows that the yarns obtained have good abrasion resistance.
The tensile breaking force and tenacity of the yarns obtained are also measured under the conditions defined by ISO standard 3341. The tensile breaking force measured on 8 to 10 test pieces is about 5 kgf (standard deviation of 0.4 kgf) and the tensile breaking tenacity is about 34 g/tex (standard deviation of 3 g/tex) These yarns allow organic materials to be reinforced effectively.
EXAMPLE 3 Filaments 14 microns in diameter, obtained by drawing molten glass threads, are coated with the following first stable composition (weight percentages relative to the mixture of the first and second compositions): Components (first group) of the base system with a molecular mass of less than 750: trimethylolpropane triglycidyl ether'' 30.0% diglycidyl ether of 1,4-butanediol l13 15.0%
(C
12
-C
14 )alkyl monoglycidyl ether' 14 15.0% This composition has a viscosity of 68 cP at 200°C (which corresponds to a viscosity of about 20 to cP at the deposition temperature of about 40 to 600C).
22 The filaments are then coated with the following second stable composition (weight percentages relative to the mixture of the first and second compositions): Components (second group) of the base system with a molecular mass of less than 750: trimethoxysilylpropylaminopropyltrimethoxysilane coupling agent(15) 10.0% mixture of benzene-1,3-dimethanamine, trimethylhexaneethylenediamine and p-tert-butylphenol 1 12.0% Additives phenylaminopropyltrimethoxysilane coupling agent 17 lubricant textile agent based on fatty acid esters and surfactantss 5 10.0% This composition has a viscosity of 56 cP at 200C (which corresponds to a viscosity of about 15 to cP at the deposition temperature of about 40 to 600C) The filaments are then assembled into yarns, which are wound in the form of roving. The yarns obtained have a yarn count of about 307 tex and a loss on ignition of 0.6%.
The yarns obtained are easy to manipulate and have a uniform coating over their entire length, polymerization (in the present case,- this is a copolymerization) being carried out over about 36 h after mixing together the compositions on the filaments.
The abrasion resistance of the yarns is measured as in Example 2. For different yarns according to the present example, the amount of flock weighed is about 8 mg of flock per kg of yarn tested. This shows that the yarns obtained have good abrasion resistance.
The tensile breaking force and tenacity of the yarns obtained are also measured as in Example 2. The tensile breaking force measured is about 16 kgf (standard deviation of 0.9 kgf) and the tensile breaking tenacity is about 50 g/tex (standard deviation 23 of 3 g/tex). These yarns allow organic materials to be reinforced effectively.
EXAMPLE 4 Filaments 14 microns in diameter, obtained by drawing molten glass threads, are coated with the following first stable composition (weight percentages relative to the mixture of the first and second compositions): Components (first group) of the base system with a molecular mass of less than 750: trimethylolpropane triglycidyl ether' 18 30.0% diglycidyl ether of 1,4-butanediol 13 10.0%
(C
12
-C
14 )alkyl monoglycidyl ether' 14 10.0% This composition has a viscosity of 68 cP at 20 0 C (which corresponds to a viscosity of about 20 to cP at the deposition temperature of about 40 to 0
C).
The filaments are then coated with the following second stable composition (weight percentages relative to the mixture of the first and second compositions): Components (second group) of the base system with a molecular mass of less than 750: trimethoxysilylpropylaminopropyltrimethoxysilane coupling agent' 15 mixture of benzene-1,3-dimethanamine, trimethylhexaneethylenediamine and p-tert-butylphenol 16) 12.0% N-aminoethylpiperazine 10.0% Catalyst: 2-(4,6-dimethylaminomethyl)phenol 12 Additives: gamma-methacryloxypropyltrimethoxysilane coupling agent 6 12.0% lubricant textile agent based on mineral oil and surfactant 19 This composition has a viscosity of 36 cP at 0 C (which corresponds to a viscosity of about 15 to cP at the deposition temperature of about 40 to 24 0 C) The filaments are assembled into yarns, which are wound in the form of roving. The yarns obtained have a yarn count of about 300 tex and a loss on ignition of 0.6%.
The yarns obtained are easy to manipulate and have a uniform coating over their entire length, polymerization (in the present case, this is a copolymerization) being carried out over about 12 h after mixing together the compositions on the filaments.
The abrasion resistance of the yarns is measured as in Example 2. The amount of flock weighed is about 3 mg of flock per kg of yarn tested. This shows that the yarns obtained have good abrasion resistance.
The tensile breaking force and tenacity of the yarns obtained are also measured as in Example 2. The tensile breaking force measured is about 11 kgf (standard deviation of 0.8 kgf) and the tensile breaking tenacity is about 38 g/tex (standard deviation of 3 g/tex). These yarns allow organic materials to be reinforced effectively.
EXAMPLE Filaments 14 microns in diameter, obtained by drawing molten glass threads, are coated with the following first stable composition (weight percentages relative to the mixture of the first and second compositions): Components (first group) of the base system with a molecular mass of less than 750: diglycidyl ether of 1,4-butanediol 13 40.0%
(C,
2
-C
14 )alkyl monoglycidyl ether' 14 15.0% This composition has a viscosity of 40 cP at 0 C (which corresponds to a viscosity of about 15 to 30 cP at the deposition temperature of about 40 to 0
C).
The filaments are then coated with the following second stable composition (weight percentages 25 relative to the mixture of the first and second compositions): Components (second group) of the base system with a molecular mass of less than 750: mixture of benzene-1,3-dimethanamine, trimethylhexaneethylenediamine and p-tert-butylphenol' 16 10.0% Catalyst: 2-(4,6-dimethylaminomethyl)phenol'12 Additives: gamma-methacryloxypropyltrimethoxysilane coupling agent 6 19.0% lubricant textile agent based on mineral oil and surfactant 19 lubricant textile agent based on paraffinic derivatives and surfactants 20 This composition has a viscosity of 38 cP at 200C (which corresponds to a viscosity of about 25 to cP at the deposition temperature of about 40 to 60 0 C) The filaments are assembled into yarns, which are wound in the form of roving. The yarns obtained have a yarn count of about 316 tex and a loss on ignition of 0.55%.
The yarns obtained are easy to manipulate and have a uniform coating over their entire length, polymerization (in the present case, this is a copolymerization) being carried out over about 48 h after mixing together the compositions on the filaments.
The abrasion resistance of the yarns is measured as in Example 2. The amount of flock weighed is about 0 mg of flock per kg of yarn tested. This shows that the yarns obtained have good abrasion resistance.
The tensile breaking force and tenacity of the yarns obtained are also measured as in Example 2. The tensile breaking force is about 14 kgf (standard deviation of 0.4 kgf) and the tensile breaking tenacity is about 42 g/tex (standard deviation of 1 g/tex).
26 These yarns allow organic materials to be reinforced effectively.
Composite plates with parallel yarns are made from the yarns, in accordance with the standard NF 57152. The reinforced resin is a polyester resin.
The mechanical properties presented by these plates, in terms of flexion and shear, are respectively measured according to ISO standards 178 and 4585, before maturation and after immersion of these plates in water at 98 0 C for 24 h. The flexural breaking strain, for a glass content in the composite of about 69.% by weight, is about 1256 MPa (standard deviation of 44 MPa) before maturation and about 785 MPa (standard deviation of 27 MPa) after maturation, the flexural breaking strain, for a glass content brought to 100% by weight, is about 2346 MPa (standard deviation of 82 MPa) before maturation and about 1465 MPa (standard deviation of 51 MPa) after maturation and the shear breaking strain, for a glass content in the composite of about 69% by weight, is about 67.5 MPa (standard deviation of MPa) before maturation and about 33 MPa (standard deviation of 1 MPa) after maturation. Such mechanical properties are particularly good.
The glass yarns according to the invention can be used in various applications, for example in textile applications such as the manufacture of chains by warping, or directly in reinforcement applications such as the reinforcement of organic materials (for example plastics) or inorganic materials (for example cement materials in order to obtain composite products).
Sold under the reference "Heloxy 5048" by the company Shell Sold under the reference "Heloxy 107" by the company Shell Sold under the reference "Heloxy 62" by the company Shell Sold under the reference "DY 071" by the company Ciba-Geigy 27 Sold under the reference "Nopcostat FT 504" by the company Henkel Sold under the reference "Silquest A 174" by the company OSi Sold under the reference "Dynasilan IMEO" by the company Hils Sold under the reference "Lucidol CH. 50" by the company Akzo Sold under the reference "Silquest A 187" by the company OSi Sold under the reference "SR 454" by the company Cray-Valley (11) Sold under the reference "HDDA" by the company
U.C.B.
(12) Sold under the reference "Actiron NX 3" by the company Protex (13) Sold under the reference "Heloxy 67" by the company Shell (14) Sold under the reference "DY 0391" by the company Ciba-Geigy Sold under the reference "Silquest A 1170" by the -company OSi (16) Sold under the reference "Ancamine 2089 M" by the company Air Products (17) Sold under the reference "Silauest Y 9669" by the company OSi (18) Sold under the reference "DY0396" by the company Ciba-Geigy (19) Sold under the reference "Lubronyl GF" by the company Rhone-Poulenc Bevaloid Sold under the reference "Rocoll 80" by the company Lamberti 28 For the purposes of this specification it will be clearly understood that the word "comprising" means "including but not limited to", and that the words "comprise" and "comprises" have a corresponding meaning.
It will be clearly understood that, although a number of prior art publications are referred to herein, this reference does not constitute an admission that any of these documents forms part of the common general knowledge in the art, in Australia or in any other country.
\\melb_files\homeS\PClarke\Keep\Retypes\P45725 Div of 77722-98 saint-gobain.doc 29/04/02

Claims (6)

1. Glass yarn coated with a sizing composition including at least one base system which is polymerisable at room temperature.
2. Glass yarn according to claim 1, in which the base system includes at least one group of component(s) which is(are) capable of homopolymerising at room temperature and/or includes at least two groups of component(s), the components of the two groups being capable of copolymerising at room temperature.
3. Composite including at least one organic and/or inorganic material and sized glass yarns, including at least partly, sized glass yarns according to claim 1 or 2.
4. Glass yarn coated with a sizing composition substantially as herein before described with reference to any one of the foregoing examples.
Composite including at least one organic and/or inorganic material and sized glass yarns substantially as herein before described with reference to any one of the foregoing examples.
6. Every novel feature as hereinbefore described or defined either alone or in combination with any other feature whether novel or not. Dated this 29th day of April 2002 SAINT-GOBAIN VETROTEX FRANCE S.A. By their Patent Attorneys GRIFFITH HACK Fellows Institute of Patent and Trade Mark Attorneys of Australia \\melbfiles\home$\PC arke\Keep\Retypes\P45725 Div of 77722-98 saint-gobain.doc 29/04/02
AU37058/02A 1997-05-14 2002-04-29 Method for producing sized glass fibres and resulting products Abandoned AU3705802A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU37058/02A AU3705802A (en) 1997-05-14 2002-04-29 Method for producing sized glass fibres and resulting products

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR97/05926 1997-05-14
AU37058/02A AU3705802A (en) 1997-05-14 2002-04-29 Method for producing sized glass fibres and resulting products

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
AU77722/98A Division AU743686B2 (en) 1997-05-14 1998-05-14 Method for producing sized glass fibres and resulting products

Publications (1)

Publication Number Publication Date
AU3705802A true AU3705802A (en) 2002-06-27

Family

ID=3724213

Family Applications (1)

Application Number Title Priority Date Filing Date
AU37058/02A Abandoned AU3705802A (en) 1997-05-14 2002-04-29 Method for producing sized glass fibres and resulting products

Country Status (1)

Country Link
AU (1) AU3705802A (en)

Similar Documents

Publication Publication Date Title
AU743686B2 (en) Method for producing sized glass fibres and resulting products
US6514612B1 (en) Glass fibre coating composition, method using said composition and resulting product
US5116900A (en) Coating composition for fibers
KR100352544B1 (en) Compositions for making glass fibers, methods of using the same, and products manufactured therefrom
EP2626335B1 (en) Surfaces containing coupling activator compounds and reinforced composites produced therefrom
AU721464B2 (en) Sizing composition for glass strands, process using this composition and resulting products
US6780468B2 (en) String binders
US5961684A (en) Sizing composition for glass strands, process using this composition and resulting products
AU3705802A (en) Method for producing sized glass fibres and resulting products
FR2809102A1 (en) Glass yarn is coated with size comprising given amount of solvent and polymerizable components including reactive (meth)acrylate and primary and/or secondary amine of given molecular weight
MXPA99000589A (en) Procedure to produce ensimated glass threads and products result
CA2406486A1 (en) String binders and method for making same
CZ20002263A3 (en) Lubricating composition for glass yarns, method of using such composition and products resulting therefrom

Legal Events

Date Code Title Description
MK1 Application lapsed section 142(2)(a) - no request for examination in relevant period