WO2007065222A1 - Pre-preg and laminate manufacture - Google Patents

Pre-preg and laminate manufacture Download PDF

Info

Publication number
WO2007065222A1
WO2007065222A1 PCT/AU2006/001864 AU2006001864W WO2007065222A1 WO 2007065222 A1 WO2007065222 A1 WO 2007065222A1 AU 2006001864 W AU2006001864 W AU 2006001864W WO 2007065222 A1 WO2007065222 A1 WO 2007065222A1
Authority
WO
WIPO (PCT)
Prior art keywords
resin
woven
preg
paper
nir
Prior art date
Application number
PCT/AU2006/001864
Other languages
French (fr)
Inventor
David Elwyn Price
Original Assignee
Depco-Trh Pty Ltd
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
Priority claimed from AU2005906886A external-priority patent/AU2005906886A0/en
Application filed by Depco-Trh Pty Ltd filed Critical Depco-Trh Pty Ltd
Priority to US12/096,162 priority Critical patent/US20090017223A1/en
Priority to AU2006322652A priority patent/AU2006322652B2/en
Priority to EP06817598A priority patent/EP1960598B1/en
Publication of WO2007065222A1 publication Critical patent/WO2007065222A1/en

Links

Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/04—Physical treatment, e.g. heating, irradiating
    • D21H25/06—Physical treatment, e.g. heating, irradiating of impregnated or coated paper
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
    • B29C70/04—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising reinforcements only, e.g. self-reinforcing plastics
    • B29C70/28—Shaping operations therefor
    • B29C70/40—Shaping or impregnating by compression not applied
    • B29C70/50—Shaping or impregnating by compression not applied for producing articles of indefinite length, e.g. prepregs, sheet moulding compounds [SMC] or cross moulding compounds [XMC]
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M10/00—Physical treatment of fibres, threads, yarns, fabrics, or fibrous goods made from such materials, e.g. ultrasonic, corona discharge, irradiation, electric currents, or magnetic fields; Physical treatment combined with treatment with chemical compounds or elements
    • D06M10/001—Treatment with visible light, infrared or ultraviolet, X-rays
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
    • D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
    • D06M15/37—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M15/39—Aldehyde resins; Ketone resins; Polyacetals
    • D06M15/423—Amino-aldehyde resins
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20—Macromolecular organic compounds
    • D21H17/33—Synthetic macromolecular compounds
    • D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/47—Condensation polymers of aldehydes or ketones
    • D21H17/49—Condensation polymers of aldehydes or ketones with compounds containing hydrogen bound to nitrogen
    • D21H17/51—Triazines, e.g. melamine

Definitions

  • the invention relates to the manufacture of partially cured resin impregnated papers or non-wovens used for decorative and industrial laminates.
  • the impregnated and optionally coated paper or non-woven known as a b-stage pre-preg
  • a hot press to form a laminate.
  • the full and final curing of the laminate in a hot press while under pressure enables the b-stage pre-preg to bond with other b-stage pre-pregs, and/or a carrier substrate such as particleboard, fibreboard or oriented strand board.
  • the invention therefore also relates to laminate products manufactured using the partially cured resin impregnated papers or non-wovens formed according to the invention.
  • the optimal process technology for bringing impregnated papers or non-woven materials used in laminate manufacture to the so-called b-stage includes all of single bath, single bath and coating, and single bath and multiple coating options. "Single bath” also embraces multiple dipping in a single bath or split baths. Papers or non- wovens may be developed that only require coating of the resin onto a pretreated surface thereby avoiding the usual first bath saturation.
  • the basic option is to saturate the paper or non-woven in a bath of resin, usually urea formaldehyde (UF) resin, melamine formaldehyde (MF) resin, phenol formaldehyde (PF) resin or any combination of these, before controlling the resin pickup via a set of metering rollers.
  • the resin impregnated paper or non-woven is then passed through a set of ovens, each oven or zone set at temperatures that enable the solvent to volatilise and the resin to progress in the degree of cure.
  • the rate of progress of the paper or non-woven through the oven, and the temperature profile can be carefully controlled to prevent premature skinning of the surface through resin polymerisation in the outer layer.
  • the impregnated paper or non-woven at the end of the impregnation process has a known amount of remaining volatiles and a known degree of cure. This partially dried and partially cured impregnated paper or non-woven is known as a b-stage pre-preg.
  • First is the high cost of energy arising from the set of ovens.
  • Second is the large footprint in the form of the long series of drying ovens required to achieve high operating speed.
  • NIR irradiation eg applied from halogen-tube radiators
  • NIR irradiation is an effective mechanism for drying or curing a variety of systems: an early disclosure was in US patent 6,436,485 for the purpose of cross-linking and curing the powder in powder coating of thermally sensitive substrates.
  • Other disclosures of interest include WO 2004/106027 [post forming of thermosetting laminates using NIR radiation], and WO 03/000612 [curing adhesive or sealing agents using NIR radiation]. It is an object of the invention to at least in part alleviate the above-mentioned disadvantages.
  • NIR irradiation can be usefully applied to the production of pre-pregs with significant process advantages without incurring the skinning and consequent dusting problems that might have been expected to arise with the higher drying and curing rates that can be achieved with NIR irradiation.
  • the invention accordingly provides, in a first aspect, a method of manufacturing a b-stage pre-preg of resin impregnated paper or non-woven, characterised by irradiating a resin impregnated paper or non-woven with NIR radiation to at least partially remove solvent by vaporisation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg.
  • the invention further provides apparatus for manufacturing a fa- stage pre-preg of resin impregnated paper or non-woven, including a resin impregnation station for impregnating a paper or non-woven with resin carried by a solvent, a heating and curing station having irradiation means to irradiate the impregnated paper or non- woven with near infra-red (NIR) radiation to at least partially remove the solvent by evaporation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg.
  • NIR near infra-red
  • near infra-red is herein meant the wavelength range between the visible region and 2.5 ⁇ m, ie about 0.7 to 2.5 ⁇ m.
  • NIR radiation does not rely on thermal conduction to the interior as do conventional ovens and infra-red heating systems, but is directed immediately into the whole body of the wet resin to achieve simultaneous drying and curing. As drying occurs, simultaneously the rate of curing increases.
  • a significant facility arising from the invention is the ability, in a preferred embodiment of the invention, to achieve substantially uniform application of the NIR radiation through the impregnated paper or non-woven, an outcome not possible in current state of the art drying equipment.
  • a further advantage is the ability to apply the energy only across the width of the web rather than the width of the drying cabinet.
  • NIR radiation is thought to cause flash evaporation of the solvent, which is most often water, by agitation of the solvent molecules, and to advance curing as the solvent is driven off by agitating the aminoplast resin molecules. Radiant heat from the NIR apparatus also provides energy to advance the cure of the resin.
  • the invention allows for a considerable reduction in the number of drying ovens required to achieve the desired properties of the partially dried and partially cured b- stage pre-preg. NIR irradiation may be employed alone or in conjunction with conventional non-NIR drying/curing ovens to achieve a pre-determined drying and curing program.
  • the apparatus further includes means for conveying the paper or non- woven as an elongated web through the resin impregnation station and the heating and curing station.
  • the method includes controlling the amount of the resin outside the body or matrix of the paper or non-woven.
  • metering means may be provided between the resin impregnation station and the heating and curing station.
  • This controlling may comprise substantially removing resin outside the body or matrix of the paper or non-woven.
  • the dwell time using NIR irradiation may be able to be reduced to of the order of seconds or less.
  • the amount of NIR electromagnetic radiation will vary depending on the properties of the paper or non-woven being processed.
  • a black paper will absorb more energy than a white paper or clear overlay paper, and thus the parameters for the individual paper or non-woven need to be taken into consideration.
  • Options to manage the process include controlling the speed at which the impregnated and/or coated paper or non-woven passes through the NIR radiation unit or units, controlling the power output of the NIR unit or units, choice of NIR emitter (eg 80Ow, 120Ow, 180Ow, 250Ow, 360Ow, 4000w and 440Ow) and whether the NIR radiation is applied from one side or both sides.
  • the method may include applying one or more successive thin coats of resin to the at least partially dried and at least partially cured b-stage pre-preg produced at the heating and curing station.
  • Such thin coats may be applied at a coverage in the range 2 to 10 g/m 2 , preferably 4 to 8 g/m 2 , most preferably 5 to 6 g/m 2 .
  • the invention provides apparatus for applying a thin coat or multiple thin coats of resin to an at least partially dried and at least partially cured b- stage pre-preg, disposed downstream of a heating and curing station or stations that produced the pre-preg.
  • the resin impregnating the paper or non-woven may be a thermosetting resin component consisting of UF, MF, PF, or any combination of these, whether or not modified with other compatible resin systems.
  • the invention extends, in a third aspect, to a method of manufacturing a decorative or industrial laminate, characterised by employing one or more b-stage pre- preg papers or non-wovens produced according to the first aspect of the invention.
  • this method may further employ in the laminate one or more pre-preg papers or non-wovens produced by drying and curing in conventional non-NIR ovens.
  • the final fully cured surface and surface characteristics may be obtained, for example, in a hot press.
  • Figure 1 is a schematic depiction of apparatus for manufacturing a b-stage pre- preg of resin impregnated paper or non-woven, according to an embodiment of the invention
  • Figure 2 shows a modified form of the apparatus depicted in Figure 1 , for additionally applying one or more thin coats to the pre-preg
  • Figure 3 is a diagrammatic plan view of one of the NIR irradiator units.
  • the illustrated apparatus includes a resin impregnation station 10, and a heating and curing station 20.
  • An elongated web 5 of paper or non-woven is drawn from a roll 6 through the successive stations 10, 20.
  • Resin impregnation station 10 comprises an aqueous or other solvent resin bath 12 in which web 5 is in contact twice with the resin 11 as illustrated to ensure paper saturation, a short contact against a pre-wet roll 13, followed by a longer dip 19. Web 5 then passes to metering means 14 comprising metering rollers 15 that are adjustable to control the amount of resin outside the body or matrix of the paper or non-woven web 5. It is found that best results are achieved downstream if the metering means is set to substantially remove resin outside the body or matrix of the paper and non-woven, i.e. there is left at most only a minimal surface coating of the resin on the paper or non- woven.
  • the resin is typically melamine formaldehyde (MF), urea formaldehyde (UF) or phenol formaldehyde (FF) resin, but these may be used in combination, or any other suitable or desired resin may be employed.
  • the impregnated paper or non-woven 5 r Downstream of metering rolls 15 the impregnated paper or non-woven 5 r optionally contacts a set of smoothing rolls 16 and is then passed into a treatment tunnel 22 of heating and curing station 20.
  • the impregnated paper or non-woven 5' is irradiated from both sides by respective NIR irradiator units 24, 25 for a period typically in the range 0.2 to 1.5 seconds.
  • This irradiation is effective to at least partially remove the resin solvent, typically water, by flash evaporation of the solvent, effected through agitation of the solvent molecules.
  • the NIR radiation is further effective to advance cure of the resin, for example by agitating aminoplast molecules of the resin.
  • Each NIR irradiator unit 24, 25 conveniently comprises a bank of elongate NIR emitters 26 ( Figure 3) preferably arranged in functional blocks 28 of six emitters each.
  • the bank extends as an upper or lower bridge across the web path with the emitters aligned in the direction of web travel.
  • Each block may, for example, extend 120mm laterally of the web, with each emitter, e.g., 250 mm long.
  • the NIR emitter 26, or at least the emitter blocks 28, that lie outside the impregnated web of paper or non-woven can be turned off, meaning that the radiation is only applied on the web and not significantly outside the web, thereby increasing energy productivity.
  • Examples of different web widths are annotated in Figure 3.
  • the distance from the web to the emitters 26 is adjustable according to other parameters such as type of emitter, web speed and grammage or colour of the paper or non-woven material.
  • successive NIR irradiations are effected, either with separate irradiators in the one unit or at separate spaced heating and curing stations.
  • the irradiation is managed so as to convert the impregnated paper or non-woven
  • the pre-preg 5" is successively treated by applying one or more thin coats of the resin at coating stations 30, and then partially drying and partially curing the respective coat at further NIR drying and curing stations 20' similar to station 20.
  • Coating stations 30 may apply the coats by spraying (32) or by means of gravure rolls (34), and a thin coat is typically applied to both sides of the pre-preg.
  • the number of thin coats can be as many as is required to obtain a desired amount of final resin uptake and coat weight.
  • a typical individual applied thin coat has a coverage of the order of 2 - 10 g/m 2 , preferably 4 - 8 g/m 2 most preferably 5 - 6 g/m 2 .
  • a web of white decor paper, of basis weight 80 gsm was impregnated with melamine formaldehyde resin in aqueous solvent, and then partially dried and partially cured by being passed twice between 4.4 kw NIR irradiators at 60 m/min. With the NIR irradiators operating at 80% power, the first pass exit temperature was measured as 75 0 C and the final exit temperature about 102°C. The end weight (paper, resin and water) was observed to be 165 gsm including about 11 % volatiles. Total residence time between the NIR irradiators was 0.5 seconds.
  • NIR radiation is an extremely effective method of removing the solvent from the impregnated paper or non- woven over a comparatively short distance and with a comparatively short exposure time to the NIR energy source.
  • a conventional set of drying ovens operating at the same or a similar web speed would remove similar amounts of solvent over a distance of 12 - 20 metres with a dwell time of 18 - 30 seconds.

Abstract

A method and apparatus for manufacturing a b-stage pre-preg of resin impregnated paper or non-woven. The method includes irradiating a resin impregnated paper or non-woven with near infra-red (NIR) radiation to at least partially remove solvent by evaporation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg. The apparatus includes a resin impregnation station (10) for impregnating a paper or non-woven (5) with resin carried by a solvent, and a heating and curing station (20) having irradiation means (24, 25) to irradiate the impregnated paper or non-woven (5') with near infra-red (NIR) radiation.

Description

Pre-Preg and Laminate Manufacture
Field of the invention
The invention relates to the manufacture of partially cured resin impregnated papers or non-wovens used for decorative and industrial laminates. The impregnated and optionally coated paper or non-woven, known as a b-stage pre-preg, is subsequently fully cured under pressure in a hot press to form a laminate. The full and final curing of the laminate in a hot press while under pressure enables the b-stage pre-preg to bond with other b-stage pre-pregs, and/or a carrier substrate such as particleboard, fibreboard or oriented strand board. The invention therefore also relates to laminate products manufactured using the partially cured resin impregnated papers or non-wovens formed according to the invention.
Any reference herein to a prior document or other prior disclosure is not to be taken as an admission that the content of the document or the disclosure is common general knowledge, either in Australia or elsewhere.
Background of the invention
The optimal process technology for bringing impregnated papers or non-woven materials used in laminate manufacture to the so-called b-stage includes all of single bath, single bath and coating, and single bath and multiple coating options. "Single bath" also embraces multiple dipping in a single bath or split baths. Papers or non- wovens may be developed that only require coating of the resin onto a pretreated surface thereby avoiding the usual first bath saturation.
The basic option is to saturate the paper or non-woven in a bath of resin, usually urea formaldehyde (UF) resin, melamine formaldehyde (MF) resin, phenol formaldehyde (PF) resin or any combination of these, before controlling the resin pickup via a set of metering rollers. The resin impregnated paper or non-woven is then passed through a set of ovens, each oven or zone set at temperatures that enable the solvent to volatilise and the resin to progress in the degree of cure. The rate of progress of the paper or non-woven through the oven, and the temperature profile, can be carefully controlled to prevent premature skinning of the surface through resin polymerisation in the outer layer. If this occurs, remaining internal water has to force itself out through the skinned film which causes a problem with dusting arising from broken off particles of dried resin, and in some cases also filler particles. This is avoided by having a graduated drying profile over significant drying oven length - the productivity comes from line speed which is limited by the number of drying ovens and their temperatures.
It is important to avoid the dusting effect because this would present a significant occupational health and safety issue. Dusting can cover parts of equipment such as safety beams used as breakers if a worker enters a dangerous part of the machine, and a health issue inevitably arises from dust particles in the air. The impregnated paper or non-woven at the end of the impregnation process has a known amount of remaining volatiles and a known degree of cure. This partially dried and partially cured impregnated paper or non-woven is known as a b-stage pre-preg.
Among further options in the impregnation process to achieving the desired fa- stage pre-preg, there is the option to further coat the impregnated paper or non-woven before any partial drying and partial curing takes place, so-called wet-on-wet processing, before partial drying and partial curing in a set of heated ovens, whether gas fired, oil fired or heated by other means.
The state of the art is not limited to the abovementioned descriptions, as one skilled in the art would know. Numerous combinations of resin types, resin content, resin additives, additives for specific purposes, such as corundum for improved abrasion resistance, and remaining volatiles and degree of cure are preferred for different strategies in producing the final laminate. There are several aspects in the current method of manufacturing b-stage impregnated papers that are economically disadvantageous.
First is the high cost of energy arising from the set of ovens.
Second is the large footprint in the form of the long series of drying ovens required to achieve high operating speed.
Third is that the gas fired or oil fired drying ovens are always used at maximum operating width, a disadvantage when treating a paper or non-woven at a web width less than the maximum of the drying oven.
It is known per se that NIR irradiation, eg applied from halogen-tube radiators, is an effective mechanism for drying or curing a variety of systems: an early disclosure was in US patent 6,436,485 for the purpose of cross-linking and curing the powder in powder coating of thermally sensitive substrates. Other disclosures of interest include WO 2004/106027 [post forming of thermosetting laminates using NIR radiation], and WO 03/000612 [curing adhesive or sealing agents using NIR radiation]. It is an object of the invention to at least in part alleviate the above-mentioned disadvantages.
Summary of the invention
It has been realised, in accordance with the invention, that NIR irradiation can be usefully applied to the production of pre-pregs with significant process advantages without incurring the skinning and consequent dusting problems that might have been expected to arise with the higher drying and curing rates that can be achieved with NIR irradiation.
The invention accordingly provides, in a first aspect, a method of manufacturing a b-stage pre-preg of resin impregnated paper or non-woven, characterised by irradiating a resin impregnated paper or non-woven with NIR radiation to at least partially remove solvent by vaporisation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg.
In its first aspect, the invention further provides apparatus for manufacturing a fa- stage pre-preg of resin impregnated paper or non-woven, including a resin impregnation station for impregnating a paper or non-woven with resin carried by a solvent, a heating and curing station having irradiation means to irradiate the impregnated paper or non- woven with near infra-red (NIR) radiation to at least partially remove the solvent by evaporation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg. By "near infra-red" is herein meant the wavelength range between the visible region and 2.5 μm, ie about 0.7 to 2.5μm.
It is thought that the skinning and consequent dusting problems that might have been expected to arise with the higher drying and curing rates that can be achieved with NIR irradiation do not arise because NIR radiation does not rely on thermal conduction to the interior as do conventional ovens and infra-red heating systems, but is directed immediately into the whole body of the wet resin to achieve simultaneous drying and curing. As drying occurs, simultaneously the rate of curing increases.
A significant facility arising from the invention is the ability, in a preferred embodiment of the invention, to achieve substantially uniform application of the NIR radiation through the impregnated paper or non-woven, an outcome not possible in current state of the art drying equipment.
A further advantage is the ability to apply the energy only across the width of the web rather than the width of the drying cabinet.
The NIR radiation is thought to cause flash evaporation of the solvent, which is most often water, by agitation of the solvent molecules, and to advance curing as the solvent is driven off by agitating the aminoplast resin molecules. Radiant heat from the NIR apparatus also provides energy to advance the cure of the resin. The invention allows for a considerable reduction in the number of drying ovens required to achieve the desired properties of the partially dried and partially cured b- stage pre-preg. NIR irradiation may be employed alone or in conjunction with conventional non-NIR drying/curing ovens to achieve a pre-determined drying and curing program.
Typically, the apparatus further includes means for conveying the paper or non- woven as an elongated web through the resin impregnation station and the heating and curing station.
Preferably, the method includes controlling the amount of the resin outside the body or matrix of the paper or non-woven. For this purpose, metering means may be provided between the resin impregnation station and the heating and curing station.
This controlling may comprise substantially removing resin outside the body or matrix of the paper or non-woven.
Instead of the usual 40 or 50 metres or more of drying ovens and a line speed of 50 m/min, giving a dwell time of approximately one minute, the dwell time using NIR irradiation may be able to be reduced to of the order of seconds or less.
The amount of NIR electromagnetic radiation will vary depending on the properties of the paper or non-woven being processed. A black paper will absorb more energy than a white paper or clear overlay paper, and thus the parameters for the individual paper or non-woven need to be taken into consideration. Options to manage the process include controlling the speed at which the impregnated and/or coated paper or non-woven passes through the NIR radiation unit or units, controlling the power output of the NIR unit or units, choice of NIR emitter (eg 80Ow, 120Ow, 180Ow, 250Ow, 360Ow, 4000w and 440Ow) and whether the NIR radiation is applied from one side or both sides.
In an embodiment, the method may include applying one or more successive thin coats of resin to the at least partially dried and at least partially cured b-stage pre-preg produced at the heating and curing station. Such thin coats may be applied at a coverage in the range 2 to 10 g/m2, preferably 4 to 8 g/m2, most preferably 5 to 6 g/m2.
In a second aspect, the invention provides apparatus for applying a thin coat or multiple thin coats of resin to an at least partially dried and at least partially cured b- stage pre-preg, disposed downstream of a heating and curing station or stations that produced the pre-preg.
The resin impregnating the paper or non-woven may be a thermosetting resin component consisting of UF, MF, PF, or any combination of these, whether or not modified with other compatible resin systems. Downstream of the heating and curing station there may be a station for manufacturing a decorative or industrial laminate from one or more of the pre-pregs. Indeed, the invention extends, in a third aspect, to a method of manufacturing a decorative or industrial laminate, characterised by employing one or more b-stage pre- preg papers or non-wovens produced according to the first aspect of the invention. Optionally, this method may further employ in the laminate one or more pre-preg papers or non-wovens produced by drying and curing in conventional non-NIR ovens. The final fully cured surface and surface characteristics may be obtained, for example, in a hot press.
Brief description of the drawings
The invention will now be described, by way of example only, with reference to the accompanying drawings, in which:
Figure 1 is a schematic depiction of apparatus for manufacturing a b-stage pre- preg of resin impregnated paper or non-woven, according to an embodiment of the invention; Figure 2 shows a modified form of the apparatus depicted in Figure 1 , for additionally applying one or more thin coats to the pre-preg; and Figure 3 is a diagrammatic plan view of one of the NIR irradiator units.
Embodiments of the apparatus
The illustrated apparatus includes a resin impregnation station 10, and a heating and curing station 20. An elongated web 5 of paper or non-woven is drawn from a roll 6 through the successive stations 10, 20.
Resin impregnation station 10 comprises an aqueous or other solvent resin bath 12 in which web 5 is in contact twice with the resin 11 as illustrated to ensure paper saturation, a short contact against a pre-wet roll 13, followed by a longer dip 19. Web 5 then passes to metering means 14 comprising metering rollers 15 that are adjustable to control the amount of resin outside the body or matrix of the paper or non-woven web 5. It is found that best results are achieved downstream if the metering means is set to substantially remove resin outside the body or matrix of the paper and non-woven, i.e. there is left at most only a minimal surface coating of the resin on the paper or non- woven. The resin is typically melamine formaldehyde (MF), urea formaldehyde (UF) or phenol formaldehyde (FF) resin, but these may be used in combination, or any other suitable or desired resin may be employed.
Downstream of metering rolls 15 the impregnated paper or non-woven 5r optionally contacts a set of smoothing rolls 16 and is then passed into a treatment tunnel 22 of heating and curing station 20. Here, the impregnated paper or non-woven 5' is irradiated from both sides by respective NIR irradiator units 24, 25 for a period typically in the range 0.2 to 1.5 seconds. This irradiation is effective to at least partially remove the resin solvent, typically water, by flash evaporation of the solvent, effected through agitation of the solvent molecules. The NIR radiation is further effective to advance cure of the resin, for example by agitating aminoplast molecules of the resin.
The web 5 is moved through the successive units by a web conveying configuration of suitable form. This is not illustrated in detail but components are depicted diagrammatically at some turning points, e.g. at 17. Each NIR irradiator unit 24, 25 conveniently comprises a bank of elongate NIR emitters 26 (Figure 3) preferably arranged in functional blocks 28 of six emitters each. The bank extends as an upper or lower bridge across the web path with the emitters aligned in the direction of web travel. Each block may, for example, extend 120mm laterally of the web, with each emitter, e.g., 250 mm long. With this arrangement, the NIR emitter 26, or at least the emitter blocks 28, that lie outside the impregnated web of paper or non-woven can be turned off, meaning that the radiation is only applied on the web and not significantly outside the web, thereby increasing energy productivity. Examples of different web widths are annotated in Figure 3. The distance from the web to the emitters 26 is adjustable according to other parameters such as type of emitter, web speed and grammage or colour of the paper or non-woven material.
In a modified embodiment successive NIR irradiations are effected, either with separate irradiators in the one unit or at separate spaced heating and curing stations. The irradiation is managed so as to convert the impregnated paper or non-woven
5' to an at least partially dried and at least partially cured b-stage pre-preg 5".
In a further modification, illustrated in Figure 2, the pre-preg 5" is successively treated by applying one or more thin coats of the resin at coating stations 30, and then partially drying and partially curing the respective coat at further NIR drying and curing stations 20' similar to station 20. Coating stations 30 may apply the coats by spraying (32) or by means of gravure rolls (34), and a thin coat is typically applied to both sides of the pre-preg. The number of thin coats can be as many as is required to obtain a desired amount of final resin uptake and coat weight. A typical individual applied thin coat has a coverage of the order of 2 - 10 g/m2, preferably 4 - 8 g/m2 most preferably 5 - 6 g/m2.
Examples
A web of white decor paper, of basis weight 80 gsm was impregnated with melamine formaldehyde resin in aqueous solvent, and then partially dried and partially cured by being passed twice between 4.4 kw NIR irradiators at 60 m/min. With the NIR irradiators operating at 80% power, the first pass exit temperature was measured as 750C and the final exit temperature about 102°C. The end weight (paper, resin and water) was observed to be 165 gsm including about 11 % volatiles. Total residence time between the NIR irradiators was 0.5 seconds.
In a second trial, the same grade of MF impregnated white decor paper was passed once between similar NIR irradiators at a much slower speed, 37.5 m/min. The exit temperature was measured as about 960C and the end weight (paper, resin and water) 140 gsm. Volatiles comprised about 8%. Residence time between the NIR irradiators was 0.8 seconds.
In both trials, no significant skinning or dusting was observed.
These trials demonstrate that these trials demonstrate that NIR radiation is an extremely effective method of removing the solvent from the impregnated paper or non- woven over a comparatively short distance and with a comparatively short exposure time to the NIR energy source. A conventional set of drying ovens operating at the same or a similar web speed would remove similar amounts of solvent over a distance of 12 - 20 metres with a dwell time of 18 - 30 seconds.

Claims

1. A method of manufacturing a b-stage pre-preg of resin impregnated paper or non-woven, characterised by irradiating a resin impregnated paper or non-woven with near infra-red (NIR) radiation to at least partially remove solvent by evaporation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg.
2. A method according to claim 1 wherein the NIR radiation is applied substantially uniformly through the impregnated paper or non-woven.
3. A method according to claim 1 and 2 wherein said paper or non-woven is an elongated web conveyed through a heating and curing station at which said irradiation is effected.
4. A method according to claim 1 , 2 or 3, further including controlling the amount of said resin outside the body or matrix of the paper or non-woven.
5. A method according to claim 4 wherein said controlling comprises substantially removing resin outside the body or matrix of the paper or non-woven.
6. A method according to any one of claims 1 to 5 further including applying one or more successive thin coats of resin to the at least partially dried and at least partially cured b-stage pre-preg.
7. A method according to claim 6 where said individual thin coats are applied at a coverage of 2 to 10 g/m2.
8. A method according to any one of claims 1 to 7 wherein said evaporation of the solvent is flash evaporation of the solvent by agitation of the solvent molecules.
9. A method according to any one of claims 1 to 8 wherein said advance of resin cure comprises agitating aminoplast molecules of the resin.
10. A method according to any one of claims 1 to 9 wherein said resin-impregnated paper or non-woven is irradiated with NIR radiation to produce the at least partially dried and at least partially cured b-stage pre-preg, for a time period less than 10 seconds.
11. A method according to any one of claims 1 to 9 wherein said resin-impregnated paper or non-woven is irradiated with NIR radiation, to produce the at least partially dried and at least partially cured b-stage pre-preg, for a time period less than 5 seconds.
12. A method according to any one of claims 1 to 11 , wherein the resin-impregnated paper or non-woven is irradiated in conjunction with being heated by conventional non- NIR drying/curing ovens, to achieve a pre-determined drying and curing program.
13. A method of manufacturing a decorative or industrial laminate, characterised by employing one or more b-stage pre-preg papers or non-wovens produced according to any one of claims 1 to 12.
14. A method according to claim 13 further employing in the laminate one or more pre-preg papers or non-wovens produced by drying and curing in conventional non-NIR ovens.
15. A method according to claim 14 including fully curing the pre-preg papers or non- woven in a hot press.
16. Apparatus for manufacturing a b-stage pre-preg of resin impregnated paper or non-woven, including a resin impregnation station for impregnating a paper or non- woven with resin carried by a solvent, and a heating and curing station having irradiation means to irradiate the impregnated paper or non-woven with near infra-red (NIR) radiation to at least partially remove solvent by evaporation of the solvent, and to advance cure of the resin, whereby to produce an at least partially dried and at least partially cured b-stage pre-preg.
17. Apparatus according to claim 16 wherein said irradiation means is configured for applying the NIR radiation substantially uniformly through the impregnated paper or non-woven.
18. Apparatus according to claim 16 or 17, further including means for conveying said paper or non-woven as an elongated web through said resin impregnation station and said heating and curing station.
19. Apparatus according to claim 18, further including metering means between said stations for controlling the amount of said resin outside the body or matrix of the paper or non-woven.
20. Apparatus according to claim 19, wherein said metering means is operable to substantially remove resin outside the body or matrix of the paper or non-woven.
21. Apparatus according to any one of claims 16 to 20, further including means downstream of said heating and curing station for applying one or more successive thin coats of resin to the at least partially dried and at least partially cured b-stage pre-preg of resin impregnated paper or non-woven produced at the heating and curing station.
22. Apparatus for applying a thin coat or multiple thin coats of resin to an at least partially dried and at least partially cured b-stage pre-preg, disposed downstream of a heating and curing station or stations that produced the pre-preg.
23. Apparatus according to claim 22 wherein said heating and curing station or stations effect drying and curing of the resin impregnated paper or non-woven by irradiation with near infra-red (NIR) radiation.
24. Apparatus according to claim 22 or 23, including at least one NIR irradiator unit for at least partially drying and at least partially curing the thin coat or multiple thin coats of resin.
PCT/AU2006/001864 2005-12-07 2006-12-07 Pre-preg and laminate manufacture WO2007065222A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US12/096,162 US20090017223A1 (en) 2005-12-07 2006-12-07 Pre-preg and laminate manufacture
AU2006322652A AU2006322652B2 (en) 2005-12-07 2006-12-07 Pre-preg and laminate manufacture
EP06817598A EP1960598B1 (en) 2005-12-07 2006-12-07 Pre-preg and laminate manufacture

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AU2005906886 2005-12-07
AU2005906886A AU2005906886A0 (en) 2005-12-07 Pre-preg and laminate manufacture

Publications (1)

Publication Number Publication Date
WO2007065222A1 true WO2007065222A1 (en) 2007-06-14

Family

ID=38122416

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/AU2006/001864 WO2007065222A1 (en) 2005-12-07 2006-12-07 Pre-preg and laminate manufacture

Country Status (3)

Country Link
US (1) US20090017223A1 (en)
EP (1) EP1960598B1 (en)
WO (1) WO2007065222A1 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008134823A1 (en) 2007-05-07 2008-11-13 Depco-Trh Pty Ltd Improvements in the manufacture of b-stage resin impregnated papers or non-wovens
DE102008021477A1 (en) 2008-04-29 2009-11-12 Kronotec Ag Preparing impregnate comprises providing liquid duroplastic synthetic resin on a fiber substrate and non-contact drying of the substrate, where the drying is carried out simultaneously/sequentially with infrared radiation and warm air
WO2010003982A2 (en) * 2008-07-08 2010-01-14 Kaindl Decor Gmbh Method and device for drying and precondensing impregnation products which are constituted of a resin-bonded film-type web material; melamine-free impregnation product
EP2837737A1 (en) 2013-08-13 2015-02-18 Flooring Technologies Ltd. Method for drying of aqueous coatings using near-infrared radiation

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL2808636T3 (en) * 2013-05-30 2016-07-29 Flooring Technologies Ltd Method for determining the moisture content of a resin layer on a support plate
US9144955B2 (en) * 2013-09-04 2015-09-29 Johns Manville Blended thermoplastic and thermoset materials and methods

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4278733A (en) 1979-07-23 1981-07-14 Spaulding Fibre Company, Inc. Epoxy modified aniline-phenolic laminate
JPS5823790A (en) * 1981-08-04 1983-02-12 Denki Kagaku Kogyo Kk Production of l-threonine
JPS5846182A (en) * 1981-09-16 1983-03-17 凸版印刷株式会社 Wash-and-wear processing treatment of cellulose fiber
US4687685A (en) 1984-06-22 1987-08-18 Isovolta Oesterreichische Isolierstoffwerke Aktiengesellschaft Process for impregnating a planar compressible carrier material with synthetic resin, as well as device for working this process
JPS6312766A (en) * 1986-07-04 1988-01-20 株式会社　松村石油研究所 Method for preventing surface napping of felt
US4738868A (en) 1985-07-24 1988-04-19 Basf Aktiengesellschaft Process and device for the preparation of fiber composite materials
WO1992009645A1 (en) * 1990-11-27 1992-06-11 Weyerhaeuser Company Isocyanate modified cellulose products and method for their manufacture
WO1999010589A1 (en) * 1997-08-22 1999-03-04 Hiroharu Okamoto Moisture-controlled curing durable press process
US6436485B1 (en) 1998-03-16 2002-08-20 Advanced Photonics Method for powder-coating
EP1264930A1 (en) * 2001-06-08 2002-12-11 The Procter & Gamble Company Cellulose fibers comprising radiation activatable resins
WO2003000612A1 (en) 2001-06-20 2003-01-03 Henkel Teroson Gmbh Method for gluing a pane
WO2004106027A1 (en) 2003-05-28 2004-12-09 Dsm Ip Assets B.V. Thermosetting material; process and apparatus for forming thermosetting material

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63275790A (en) * 1987-04-30 1988-11-14 神崎製紙株式会社 Production of cast coated paper
JP3446291B2 (en) * 1993-10-29 2003-09-16 信越化学工業株式会社 Method for producing hexamethylcyclotrisilazane
DE19710549C2 (en) * 1997-03-14 1999-01-28 Vits Maschinenbau Gmbh Process and plant for impregnating and drying a continuous web
DE19807643C2 (en) * 1998-02-23 2000-01-05 Industrieservis Ges Fuer Innov Method and device for drying a material to be dried on the surface of a rapidly conveyed carrier material, in particular for drying printing inks
DE19901525C2 (en) * 1999-01-16 2001-02-08 Vits Maschinenbau Gmbh Plant for impregnating and coating paper
DE10004488A1 (en) * 2000-02-02 2001-08-09 Basf Ag Process for the production of coatings, adhesive layers or seals for primed or unprimed substrates

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4278733A (en) 1979-07-23 1981-07-14 Spaulding Fibre Company, Inc. Epoxy modified aniline-phenolic laminate
JPS5823790A (en) * 1981-08-04 1983-02-12 Denki Kagaku Kogyo Kk Production of l-threonine
JPS5846182A (en) * 1981-09-16 1983-03-17 凸版印刷株式会社 Wash-and-wear processing treatment of cellulose fiber
US4687685A (en) 1984-06-22 1987-08-18 Isovolta Oesterreichische Isolierstoffwerke Aktiengesellschaft Process for impregnating a planar compressible carrier material with synthetic resin, as well as device for working this process
US4738868A (en) 1985-07-24 1988-04-19 Basf Aktiengesellschaft Process and device for the preparation of fiber composite materials
JPS6312766A (en) * 1986-07-04 1988-01-20 株式会社　松村石油研究所 Method for preventing surface napping of felt
WO1992009645A1 (en) * 1990-11-27 1992-06-11 Weyerhaeuser Company Isocyanate modified cellulose products and method for their manufacture
WO1999010589A1 (en) * 1997-08-22 1999-03-04 Hiroharu Okamoto Moisture-controlled curing durable press process
US6436485B1 (en) 1998-03-16 2002-08-20 Advanced Photonics Method for powder-coating
EP1264930A1 (en) * 2001-06-08 2002-12-11 The Procter & Gamble Company Cellulose fibers comprising radiation activatable resins
WO2003000612A1 (en) 2001-06-20 2003-01-03 Henkel Teroson Gmbh Method for gluing a pane
WO2004106027A1 (en) 2003-05-28 2004-12-09 Dsm Ip Assets B.V. Thermosetting material; process and apparatus for forming thermosetting material

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
DATABASE WPI Week 198312, Derwent World Patents Index; Class A87, AN 1983-28493K, XP003014340 *
DATABASE WPI Week 198317, Derwent World Patents Index; Class A87, AN 1983-40398K, XP003014341 *
DATABASE WPI Week 198809, Derwent World Patents Index; Class A82, AN 1988-059012, XP003014342 *
See also references of EP1960598A4 *

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008134823A1 (en) 2007-05-07 2008-11-13 Depco-Trh Pty Ltd Improvements in the manufacture of b-stage resin impregnated papers or non-wovens
AU2008247331B2 (en) * 2007-05-07 2013-06-20 Depco-Trh Pty Ltd Improvements in the manufacture of B-stage resin impregnated papers or non-wovens
DE102008021477A1 (en) 2008-04-29 2009-11-12 Kronotec Ag Preparing impregnate comprises providing liquid duroplastic synthetic resin on a fiber substrate and non-contact drying of the substrate, where the drying is carried out simultaneously/sequentially with infrared radiation and warm air
WO2010003982A2 (en) * 2008-07-08 2010-01-14 Kaindl Decor Gmbh Method and device for drying and precondensing impregnation products which are constituted of a resin-bonded film-type web material; melamine-free impregnation product
DE102008032053A1 (en) 2008-07-08 2010-01-14 Kaindl Decor Gmbh Method and apparatus for drying and precondensing impregnates formed from resin impregnated sheet-like sheet material; Melamine resin-free impregnate
DE102008032053A8 (en) * 2008-07-08 2010-04-29 Kaindl Decor Gmbh Method and apparatus for drying and precondensing impregnates formed from resin impregnated sheet-like sheet material; Melamine resin-free impregnate
WO2010003982A3 (en) * 2008-07-08 2010-11-18 Kaindl Decor Gmbh Method and device for drying and precondensing impregnation products which are constituted of a resin-bonded film-type web material; melamine-free impregnation product
CN102138049A (en) * 2008-07-08 2011-07-27 凯得装饰有限公司 Method and device for drying and precondensing impregnation products which are constituted of a resin-bonded film-type web material
RU2485422C2 (en) * 2008-07-08 2013-06-20 Кайндль Декор Гмбх Method and device for drying and preliminary condensing of impregnates and impregnates
EP2837737A1 (en) 2013-08-13 2015-02-18 Flooring Technologies Ltd. Method for drying of aqueous coatings using near-infrared radiation

Also Published As

Publication number Publication date
EP1960598A1 (en) 2008-08-27
EP1960598B1 (en) 2012-10-17
US20090017223A1 (en) 2009-01-15
EP1960598A4 (en) 2009-10-21

Similar Documents

Publication Publication Date Title
EP2147153B1 (en) Improvements in the manufacture of b-stage resin impregnated papers or non-wovens
EP1960598B1 (en) Pre-preg and laminate manufacture
RU2595712C2 (en) Powder mix and method for making structural panel
US6458250B1 (en) Process for the application of powder coatings to non-metallic substrates
JP5384748B2 (en) Manufacturing method and manufacturing apparatus for double-sided coating decoration board
CA2759360C (en) Process and apparatus for manufacturing decorative papers and/or panels for flooring or surfacing of furniture, walls, etc.
US20130228300A1 (en) Method and system for impregnating and drying a continuous paper web
US20080199666A1 (en) Manufacture of an Impregnated Paper or Non-Woven
AU2006322652B2 (en) Pre-preg and laminate manufacture
US20110192048A1 (en) Method and Device for Drying and Precondensing Impregnation Products which are Constituted of a Resin-Bonded Film-Type Web Material; Melamine-Free Impregnation Product
CA2293623C (en) Method of producing paper
AU2007204606A2 (en) Manufacture of decorative and industrial laminates
AU2013231137A1 (en) Improvements in the manufacture of b-stage resin impregnated papers or non-wovens
AU2011202474A1 (en) Laminate manufacture with novel solids application
AU2006255480B2 (en) Manufacture of an impregnated paper or non-woven

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
DPE1 Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101)
WWE Wipo information: entry into national phase

Ref document number: 2006322652

Country of ref document: AU

WWE Wipo information: entry into national phase

Ref document number: 12096162

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: 2006817598

Country of ref document: EP

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2006322652

Country of ref document: AU

Date of ref document: 20061207

Kind code of ref document: A

WWP Wipo information: published in national office

Ref document number: 2006322652

Country of ref document: AU

WWP Wipo information: published in national office

Ref document number: 2006817598

Country of ref document: EP