Apparatus and method of manufacturing synthetic boards including fire-retardant boards

Abstract: A method and apparatus for producing a synthetic board from cellulosic or lignocellulosic fibres is disclosed wherein a standard isocyanate binder is emulsified and immediately applied to the fibres before consolidation into a finished board product. The apparatus includes an emulsification and application nozzle comprising a diluent inlet, a binder inlet, a mixing section for emulsifying the diluent and the binder, and a spray nozzle for applying the binder/diluent emulsion to the fibres. The method includes supplying a binder stream, supplying a diluent stream, emulsifying the binder with the diluent and immediately applying the emulsion to the fibres. The method further includes flushing the binder/diluent emulsion using the diluent at the end of a binder application run to prevent curing of the emulsion and clogging of the apparatus. The present invention can be used to apply the binder/diluent emulsion to the fibres either in the blowline or downstream of the blowline, such as in the blender. The invention further includes a method and apparatus for producing fire-­ retardant boards in which a fire-retardant chemical such as an ammonium polyphosphate is applied to the fibres downstream of the refiner and upstream of the mat-former.

Description: The present invention relates to an apparatus and method of manufacturing synthetic boards and fire-retardant synthetic boards from cellulosic or lignocellulosic furnish materials using an organic binder. Such an apparatus and such a method are, for example, known from EP-A-0 118 659 Many synthetic board products are manufactured using a thermosetting binder, heat and pressure to reconsolidate refined cellulosic and/or lignocellulosic furnish materials into a unitary finished board product. Examples of board manufacturing processes are shown in US-A-2,757,115 and US-A-4,407,771. Basically, furnish material, such as wood, is reduced to fibres of the desired size by a refiner, mixed with a binder and other chemicals such as release and sizing agents, partially dewatered, formed into mats and compressed between heated platens in a hot press to form a board product of the desired thickness and density. In many current processes, the binder is applied to a rapidly moving stream of the fibres as it exits the refiner, in the so-called "blowline" of the process equipment. Alternatively, the binder may be added in the blender or elsewhere downstream of the refiner. A wide variety of binder systems have been utilized in the production of synthetic boards, including various thermosetting organic binders, such as isocyanates, polyisocyanates, urea formaldehydes, phenolics, melamines and various mixtures thereof. Isocyanate and polyisocyanate binders have advantages over urea formaldehyde binders in that boards with greatly improved weather resistance can be produced. Processing time can typically be substantially reduced using isocyanate and polyisocyanate binders rather than standard phenolic binders. Although specially formulated phenolic binders can decrease the processing time, the cost of these specialty binders makes their use less attractive. Additionally, urea formaldehyde binders tend to produce formaldehdyes, and phenolic binders tend to produce both formaldehydes and free phenols around the press area, which can cause significant health problems. Heretofore, successful application of isocyanate binders in fibreboard manufacture has been limited due to many factors. First, there is often difficulty in achieving adequate distribution at low dosage rates. Second, many systems require the use of an expensive release agent-containing binder or must utilize a caul plate system which allows external release agent application. These problems usually result in increased production costs and/or inferior finished board product quality. Many of the binder systems used today in board manufacture include an organic isocyanate binder which is specially mixed with a variety of diluent/extender agents to enhance binder distribution. These admixtures must also have a relatively long pot life to avoid premature curing, which can clog the binder delivery system. Unfortunately, even quite stable admixtures tend to deposit reaction products in process lines during use, and especially when use is interrupted. Both problems usually necessitate expensive machine downtime to unclog or replace components of the binder delivery system. In systems utilizing isocyanate binders, the binder is typically formulated into an aqueous emulsion long before application to the furnish. Since the binder is highly reactive, the temperature during and after emulsification must be kept relatively low to avoid prereaction of the binder before it is applied to the furnish materials. Water-cooled addition devices, such as the nozzle described in US-A-4,402,896 have been used, but require a constant supply of cooling water and are still subject to clogging. Another problem associated with specialty binders and their mixing equipment is that if the binder is not completely removed from the binder delivery system at the end of a production run, the binder will usually cure and clog the system. Therefore there is a need for a binder delivery system which assures that all of the binder is removed therefrom to avoid these problems. Additionally, release agents are often added to the binder system to avoid sticking of the board to platens or caul plates during processing. However, these specially formulated binders are typically proprietary to a particular manufacturer and are prohibitively expensive for large-scale fibreboard manufacturing operations. Accordingly, there is a need for a process and apparatus which can utilize basic non-proprietary isocyanate and other binder compounds and release agents. US-A-3,874,990 discloses a method for producing a flame retardant particle-board or chip-board in which the flame retardant chemicals are added during production of the particle board, prior to mat-forming, and comprise alkaline borate chemicals and flame retardant phosphoric acid-dicyandiamide-formaldehyde resin. The flame retardant chemicals are added to the wood chips as a dry powder. Such a method does not lend itself to applications in the field of fibreboard production as it would be extremely difficult to achieve a good dispersion of a powder with the fine fibre used. Therefore, there is a need for an apparatus and method for producing a fire-retardant fibreboard in which the fire-retardant compound is incorporated into the board during its production and the product board has the desirable physical characteristics of standard fibreboard as well as excellent fire-retardant characteristics. It is therefore an object of the present invention to provide a method of producing a synthetic board from cellulosic or lignocellulosic materials wherein standard, nonproprietary, inexpensive and readily available isocyanate, polyisocyanate and similar binders can be utilized, thus obviating the need for expensive specialty chemical formulations. It is also an object of the present invention to provide an apparatus for producing a synthetic board wherein standard binders and release agents can be utilized. It is a further object of the present invention to provide a method and an apparatus for forming a binder emulsion immediately upstream from the point of application to the wood fibres, thus allowing the use of isocyanates or polyisocyanates which do not form emulsions having extended stabilities or pot life. It is also an object of the present invention to provide a method and apparatus for binder application wherein the emulsion is cooled by the diluent. It is an object of the present invention to provide a method and apparatus for applying the binder which would avoid periodic plugging of the process equipment and the binder system. It is also an object of the present invention to provide a method and apparatus for flushing the binder from the nozzle at the end of a production run so that the binder does not cure within the nozzle and clog the same. Another object of the invention is to provide a method and apparatus as aforesaid which includes a new and improved method and apparatus for producing a fibreboard that is fire-retardant. Still another object of the invention is to provide a method and apparatus as aforesaid which produces a fire-retardant fibreboard having size, strength, water-resistance and other characteristics comparable to those of standard fibreboard. Another object is to provide a method and apparatus as aforesaid capable of producing an exterior grade fibreboard that is fire-retardant. The invention accordingly provides an apparatus adapted for mixing a binder stream and a diluent stream and applying the product stream to the fibres in the production of synthetic boards, the apparatus comprising binder inlet means for receiving a first stream containing a binder; diluent inlet means for receiving a second stream containing a diluent; mixing means fluidly connected to the binder inlet means and the diluent inlet means for mixing the first stream and the second stream to produce a fourth stream comprising a product stream containing a mixture of the binder and the diluent; and outlet means positioned proximate the mixing means and fluidly connected to the mixing means for immediately applying the product stream to the fibres; characterised by a flush means for flushing the mixing means with the second stream after flow of the first stream is stopped. The invention further provides a method of blending a binder with cellulosic fibres in the manufacture of synthetic boards from cellulosic fibres, the method comprising conveying cellulosic fibres in a first stream; conveying a binder in second stream; conveying a diluent in a third stream; merging the second stream and the third stream to produce a fourth stream; emulsifying the binder/diluent mixture of the fourth stream proximate to the first stream; and immediately thereafter merging the fourth stream and the first stream to apply the binder and the diluent to the fibres; characterised by flushing the fourth stream at the end of a production run, using the third stream. Further preferred features of the invention are disclosed in the following description and are defined in the claims. The invention will now be described more particularly with reference to the accompanying drawings. In the drawings: Figure 1 is a schematic diagram showing the process and apparatus in accordance with the present invention. Figure 2 is a side view of a nozzle in accordance with the present invention mounted on a blowline of a fibreboard manufacturing process. Figure 3 is a schematic view of the nozzle in accordance with the present invention. Figure 4 is a schematic drawing showing the positions of entry of binder, diluent, and other agents to the fibre flow-path. The present invention is intended for use in the production of reconstituted products made from cellulosic or lignocellulosic materials, and in particular, the production of fibreboard from wood fibres. The invention is also intended for use in the production of fibreboard having fire-retardant characteristics. As shown in Figure 1, pieces of wood, such as chips, are fed into a plug feeder 10 for delivery to a digester 12, where they are subjected to steam and high pressure to soften the chips and break down the lignin therein. The cooked chips are transferred to a refiner 14 where they are separated into their constituent fibres, such as between uni- or bi- directional rotating discs. The hot and wet fibres exit refiner 14 with steam in a rapidly moving continuous stream which is transported through a so-called "blowline" 16, where the binder and other desired compounds, such as release and sizing agents, are typically added. The binder is preferably a material selected from the group consisting of monomeric isocyanates, oligomeric isocyanates, and mixtures thereof having a functionality of at least 2. In addition, other conventional thermosetting binders may be used. Aqueous emulsions of the binder and other additives are well-suited to blowline injection for several reasons. First, a large portion of the heat energy available in the blowline is absorbed in raising the temperature of the applied emulsions since the specific heat of water is higher than many of the other substances being added. Second, the water-to-water solvent compatibility between the wood fibres and the additive emulsion is excellent and helps assure good flow and distribution of the binder. Third, deposits of the additive emulsion on the wall of the blowline are minimized due to the presence of a continuous film of water condensate, with which the additive emulsions are also compatible. Fourth, the great turbulence within the blowline results in a scouring action which tends to keep the blowline wall clean, providing those adhering substances are also water compatible. Lastly, the residence time in the blowline is so short that most chemical reactions, such as curing of the binder, have insufficient time and energy to move very far toward reaction products. In the preferred embodiment of the present invention, a binder emulsion and application nozzle assembly 18 in accordance with the present invention is connected to blowline 16 for emulsifying the isocyanate binder with a diluent and applying the resulting emulsion to the fibres as they pass through blowline 16. In the preferred embodiment, conventional nozzles 20 and 22 are also plumbed to blowline 16 for applying release and sizing agents to the fibres. Alternatively, the isocyanate binder, release agent and sizing agents may be added at other locations in the process, as will be described below. Upon entering blowline 16, the steam and the fibres undergo a rapid drop in pressure and temperature, but travel therethrough in less than about 1 second. The velocity of the fibres through a typical blowline has been reported to be approximately 100m (325 feet) per second. There is extreme turbulence in blowline 16, which provides excellent mixing of additives, such as the binder, with the fibres. After exiting blowline 16, the fibres enter a dryer 24 where they are partially dewatered. A first cyclone 26 and an air lock 28 are provided to separate the fibre from the dryer airstream. The fibres next pass to a blender 30 wherein the isocyanate binder, sizing, release agents or other desired materials can be mixed with the fibres, if desired. If all desired compounds have already been added, the fibres can be directed through a bypass chute 32 and go directly to a second cyclone 34 with an air lock 36 and then into a fibre storage bin 38. Fibre storage bin 38 provides fibres to one or more forming head apparatuses 40 which are used to dispense a forming mat of fibres 41 onto a forming belt 42. Forming mat 41 is deaerated by one or more prepresses 44 and then compressed to the final pressed thickness by a hot press 46 wherein the binder is cured to form the desired board product. In general, the binder can be added to the fibres in any suitable location in the board forming apparatus upstream of forming mat 41. Alternative locations where the binder can be added to the fibres are designated by dashed arrows 17a-d in Figure 1. For example, the binder may be added using the nozzle assembly of the present invention in any of the following locations: refiner 14; blender 30; bypass chute 32 or forming head apparatuses 40. Similarly, the sizing and release agents can be added, separately or together, in the various locations in the board forming apparatus, including: plug feeder 10, digester 12, refiner 14, blowline 16, blender 30 or bypass chute 32. Referring to Figures 2 and 3, nozzle assembly 18 comprises a diluent inlet 52, a binder inlet 54, a mix section 56 for emulsifying diluent and binder and a spray nozzle 58 adapted for connection to a blow line 16 for spraying the emulsion on the fibres. A stream of water or other diluent is introduced through diluent inlet 52, and a stream of a binder, which can be isocyanate, polyisocyanate or other suitable thermosetting binder, is introduced through binder inlet 54. Diluent inlet 52 includes a coupling 62, such as a quick disconnect coupling shown, for connection to a diluent supply line 64 with an appropriate coupling 66 through which water or other suitable diluent is delivered to nozzle assembly 18. A pressure relief check valve 68 for diluent inlet 52 is operated by a control spring 70 and is threadedly connected to coupling 62. Diluent check valve 68 prevents backflow from mix section 56 into diluent supply line 64. In addition, diluent check valve 68 will only open to allow diluent into mix section 56 when the pressure of the water stream is above a certain minimum pressure, for example, 1.03 bar (15 psi). This assures that there will be no admixing of water and binder until the water stream has achieved proper operating pressure, such as by the use of an appropriate metering pump (not shown). It also assures that the flow of diluent into nozzle assembly 18 will stop immediately upon stopping the flow of the diluent stream or upon a drop in the prssure of the stream. Suitable check valves are available from the NuPro Company of Willoughby, Ohio. Although alternative diluents, such as propylene carbonate or furfural, can be used under various conditions, water has long been used to reduce the viscosity of binders and thus improve distribution. The water also serves as a thermal buffer for the binder. This is particularly significant for those applications utilizing blowline addition of isocyanates. Since there is a constant flow of relatively cool (less than ambient temperature) diluent water through nozzle assembly 18, the temperature to which the binder is subjected during emulsification is also less than ambient, which prevents precuring. No additional cooling of the emulsion, such as provided by a cooling water jacket, is required. Binder inlet 54 similarly includes a coupling 72 for connection to a binder supply line 74 with a coupling 76 through which binder is delivered to nozzle assembly 18. In the preferred embodiment, the binder is standard technical grade isocyanate or polyisocyanate. A pressure relief check valve 78 for binder inlet 54 includes a control spring 80 and is threadedly connected to coupling 72. Binder check valve 78 operates as above to prevent backflow from mix section 56 into binder supply line 74. Binder check valve 78 also prevents the admixing of water and binder before the binder stream has achieved its proper operating pressure, or if the flow of the binder stream has been stopped or if the pressure of the binder stream drops below a proper operating pressure. Additional compounds, such as release agents, sizing agents, etc., may be applied to the fibres, if desired. Referring to Figure 4, release agents and sizing agents may be added, separately or together, to diluent stream 81a, binder stream 81b, combined binder/diluent stream 81c or directly to fibre stream 81d, as shown by dashed lines 82a - 82d, respectively. If the additional compounds are to be added to combined binder/diluent stream 81c, a third inlet 83 (shown by dashed lines in Figure 2) can be plumbed to mix section 56 of nozzle assembley 18 for introducing such compounds into mix section 56. In this way, the additional compound will be merged with the binder/diluent immediately before application to the fibres. Mix section 56 includes an intersection tee 84 which is threadedly attached to the outlets of diluent check valve 68 and binder check valve 78 for receiving the binder stream and the diluent stream. Tee 84 is also threadedly connected to an in-line mix section 85 equipped with a plurality of interior baffles 86 which cause mixing and emulsion of the binder with the diluent. The exact number and configuration of baffles 86 has not been found to be critical, as long as sufficient mixing results. A plastic baffled-style motionless mixer insert sized for insertion into in-line mix section 85 and sold by TAH Industries of Imalyston, New Jersey under the name Kinetic Mixer has been found to give good results. Spray nozzle 58 is threadedly attached to in-line mix section 85 for applying the diluent-binder emulsion to the fibres passing through blowline 16. Spray nozzle 58 is provided with external threads 90 for attachment to mating internal threads 92 in wall 94 of blowline 16. Spray nozzle 58 is mounted so that only a small tip portion 96 of the nozzle 90 extends into blowline 16 and is subjected to the abrasive atmosphere therein. Due to the abrasive atmosphere of blowline 16 and to avoid any possible interaction with the emulsion, it has been determined that spray nozzle 58 should be constructed out of stainless steel or other suitable material. It has also been determined that a spray nozzle obtained from Spraying Systems Company of Wheaton, Illinois and sold under the trademark FULLJET gives good results. This nozzle tip includes an integral interior spiral vane mixer which produces a full cone spray pattern for good distribution of the emulsion on the fibres. It has also been determined that a nozzle I.D. of 6.2 mm (0.245 inches) is preferred to maintain proper backpressure in nozzle assembly 18. Nozzle assembly 18 is typically operated at an emulsion flow rate of approximately 23 litres (5 gallons) per minute and a pressure of between 5.5 and 8.6 bar (80 and 125 psi), although some applications may require other application rates and parameters. In the preferred embodiment, blowline 16 has an interior diameter of about 150 mm (6 inches). Thus, the distance between the point of emulsification of the binder and the point of application to the fibres in blowline 16 is very small, approximately 100 mm (4 inches). This relatively short distance helps assure that the binder emulsion does not cure before application to the fibres. In accordance with the present invention, a method of and means for flushing binder and emulsion out of nozzle assembly 18 are also provided. This flushing is necessary to avoid leaving the emulsion in mix section 56 or spray nozzle 58 where it could quickly cure and plug nozzle assembly 18. To flush nozzle assembly 18 at the end of a production run, the binder pump should be turned off to stop the flow of binder. This causes binder check valve 78 to close. The water stream is allowed to continue to flow for a few seconds (3-5 seconds) to flush out any residual emulsion. Preferably, the binder stream should be shut off before fibre stream flow past spray nozzle 58 has ended to avoid buildup of binder in blowline 16. Application of the aqueous emulsions of standard isocyanate and polyisocyanate through nozzle assembly 18 into blowline 16 results in a practical and economical means of producing a superior fibreboard product, especially a medium density, water-resistant fibreboard suitable for exterior use. The ready availability of the binders are of great significance to a commercial fibreboard production facility. Fire-retardant fibreboard is advantageously produced by the above described method and apparatus, with the introduction of an additional step whereby a fire-retardant chemical in aqueous solution is added to the wood material. Ammonium polyphosphate has been found to be a suitable compound for this purpose when used with an isocyanate binder. Ammonium polyphosphate is known as a fire-retardant for the treatment by spraying, dipping, etc. of fabrics. However, it has not, to Applicants' knowledge, been used successfully as a fire-retardant in fibreboard. Attempts have been made by the Applicants to produce a fire-retardant fibreboard using urea-formaldehyde as the binder system, together with ammonium polyphosphate as the fire-retardant compound. The product was found to have poor internal bonding, probably due to chemical reaction between the binder and fire-retardant, resulting in inferior fire-retardancy, water resistance, strength and other characteristics. Applicants have now found that use of the same fire-retardant chemical with an isocyanate binder system gives a product board having superior physical characteristics and with water resistance and strength similar to comparable non-fire-retardant boards. It has been found that the fire-retardant compound may be added in the range of 7 - 15% solid ammonium polyphosphate to oven dry weight of wood where an isocyanate is used as the binder. Addition of higher amounts of the fire-retardant compound, when used with an isocyanate binder, has been found to result in a finished fibreboard whose tensile strength is unacceptably lowered. The preferred range is 7 - 10% solid ammonium polyphosphate to oven dry weight of wood. The fire-retardant chemical may be added to the wood chips or fibres at any suitable location in the board forming apparatus upstream of forming mat 41 (Figure 1). Suitable points are: plug feeder 10; digester 12; refiner 14, blowline 16 or blender 30. Introduction of the chemical is via a standard spray nozzle, for example a 25 mm (1 inch) FULLJET (Trademark) nozzle. The fire-retardant liquid may be added to the fibre stream either before or after addition of the isocyanate binder emulsion to the fibre stream. If desired, one of auxiliary nozzles 20, 22 may be used for this purpose. Alternatively, a stream of the fire-retardant liquid may be merged with the stream of emulsified isocyanate binder in nozzle assembly 18, for example by using inlet 83 to nozzle mix section 85. The fire-retardant liquid may also be added to either the diluent in inlet passage 64 or the binder in inlet passage 74 to the nozzle assembly 18. The fire-retardant fibreboard meets the same technical specifications, including size, strength, density and water-resistance characteristics, as the non fire-retardant fibreboard produced by the method and apparatus according to the invention. With respect to its fire-retardant properties, the fire retardant fibreboard described herein is certified to Class 1 surface spread of flame in accordance with the class definitions given in British Standard 476: Part 7: 1987. The test assesses ignition characteristics and the extent to which the product surface spreads flames laterally. Materials are classified according to performance as Classes 1 to 4 in descending order of performance. The fire-retardant fibreboard is suitable for use, but is not limited to use, in any of the following applications: ceilings, wall linings, partitioning in building and shopfitting, display panels for the shopfitting and exhibitions industry, shipbuilding applications, general purpose building panels where greater fire integrity is specified or required whilst still retaining a surface suitable for finishing. Although preferred embodiments of the present invention have been shown, it is obvious that many modifications and variations of the present invention are possible in the light of the above teachings. It is therefore to be understood that the present invention may be practiced otherwise than as specifically described.

Claims: An apparatus adapted for mixing a binder stream and a diluent stream and applying the product stream to the fibres in the production of synthetic boards, the apparatus comprising binder inlet means (54) for receiving a first stream containing a binder; diluent inlet means (52) for receiving a second stream containing a diluent; mixing means (56) fluidly connected to the binder inlet means and the diluent inlet means for mixing the first stream and the second stream to produce a fourth stream comprising a product stream containing a mixture of the binder and the diluent; and outlet means (58) positioned proximate the mixing means and fluidly connected to the mixing means (56) for immediately applying the product stream to the fibres; characterised by a flush means for flushing the mixing means with the second stream after flow of the first stream is stopped. Apparatus according to Claim 1, wherein the binder inlet means (54) comprises binder control valve means (78) for automatically stopping the flow of the first stream upon a decrease in application pressure thereof. Apparatus according to Claim 1, wherein the diluent inlet means (52) comprises diluent control valve means (68) for automatically stopping the flow of the second stream upon a decrease in application pressure thereof. Apparatus according to Claims 1, 2 or 3, wherein the mixing means (56) emulsifies the binder and the diluent in forming the fourth stream. Apparatus according to any one of Claims 1 to 4, wherein the mixing means (56) comprises a plurality of baffles (86). Apparatus according to any one of Claims 1 to 5, wherein the mixing means (56) comprises an in-line mixer. Apparatus according to any one of Claims 1 to 6, wherein the outlet means (58) comprises a spray nozzle. Apparatus according to any one of Claims 1 to 7, wherein the flush means comprises means for first stopping flow of the first stream and thereafter stopping flow of the second stream when flushing of the mixing means has been completed. Apparatus according to any one of Claims 1 to 8, further comprising supplemental inlet means (83) fluidly connected to the mixing means (56) for receiving a third stream, wherein the third stream is mixed with the first stream and the second stream in forming the product stream. Apparatus according to any preceding claim, and further comprising refining means (12,14) for extracting fibres from a cellulosic material; conduit means (16) connected to the refining means for conveying the fibres along a fibre flow path; dryer means (24) for partially dewatering the fibre/binder mixture; forming means (40) for creating a mat of the dewatered fibre/binder mixture; and heated pressing means (46) for compressing the fibres and curing the binder in the mat for forming a consolidated board product. Apparatus according to Claim 10, wherein the binder/diluent mixture is mixed with the fibres upstream of the forming means. Apparatus according to Claim 10 or 11, wherein the conduit means (16) comprises a blender means (30) positioned along the fibre flow path for receiving and mixing the fibres, and the outlet means (58) is plumbed to the blender means for applying binder/diluent mixture to the fibres therein. Apparatus according to Claim 10 or 11, wherein the conduit means (16) comprises a blow line means and said outlet means (58) is plumbed to the blowline means for applying binder/diluent mixture to the fibres therein. Apparatus according to any preceding claim and further comprising a liquid fire-retardant application means (20,22 or 83) for introducing fire-retardant liquid onto the fibres. Apparatus according to Claim 14, wherein the liquid fire retardant application means (20,22) is located along the fibre flow path. Apparatus according to Claim 15, wherein the liquid fire retardant application means is located along the fibre/binder mixture flow path. Apparatus according to any one of Claims 14 to 16, wherein the liquid fire retardant application means includes a spray nozzle for introducing the liquid onto the fibres. A method of blending a binder with cellulosic fibres in the manufacture of synthetic boards from cellulosic fibres, the method comprising conveying cellulosic fibres in a first stream; conveying a binder in second stream; conveying a diluent in a third stream; merging the second stream and the third stream to produce a fourth stream; emulsifying the binder/diluent mixture of the fourth stream proximate to the first stream; and immediately thereafter merging the fourth stream and the first stream to apply the binder and the diluent to the fibres; characterised by flushing the fourth stream at the end of a production run, using the third stream. A method according to Claim 18, wherein the binder/diluent mixture in the fourth stream is emulsified by forcing said stream through a plurality of baffles. A method according to Claim 18 or 19, wherein the second stream further comprises a sizing agent. A method according to Claim 18 or 19, wherein the second stream further comprises a release agent. A method according to Claim 18 or 19, wherein the third stream further comprises a sizing agent. A method according to Claim 18 or 19, wherein the third stream further comprises a release agent. A method according to Claim 18 or 19, further comprising the step of conveying a sizing agent in a fifth stream; and merging the fifth stream with the second and third streams immediately before merging the fourth stream and the first stream. A method according to Claim 18 or 19 further comprising the step of conveying a release agent in a fifth stream and merging the fifth stream with the second and third streams immediately before merging the fourth stream and the first stream. A method according to any one of Claims 18 to 25, wherein the binder comprises a thermosetting binder. A method according to any one of Claims 18 to 26, wherein the binder comprises a material selected from the group consisting of monomeric isocyanates, oligomeric isocyanates and mixtures thereof having a functionality of at least 2. A method according to any one of Claims 18 to 27, wherein the diluent comprises water. A method according to any one of Claims 18 to 28, further comprising the steps of extracting hot and wet fibres from a cellulosic material, transporting the hot and wet fibres in a first stream; partially dewatering the hot and wet fibres; forming the partially dewatered fibres into a mat; and compressing the mat in a heated press to cure the binder to form a consolidated board product. A method according to any one of Claims 18 to 29, further comprising the step of introducing fire-retardant liquid onto the cellulosic fibres. A method according to Claim 30, wherein the fire-retardant liquid is introduced to the fibres in a fibre flow path. A method according to Claim 31, wherein the fire-retardant liquid is introduced to the fibres following a merger of said first and fourth streams. A method according to Claim 30, 31 or 32, wherein the fire retardant liquid is introduced to the cellulosic fibres by means of a spray nozzle. A method according to any one of Claims 30 to 33, wherein the fire retardant liquid comprises an aqueous solution of a fire-retardant compound. A method according to Claim 34, wherein the fire-retardant liquid comprises an aqueous solution of ammonium polysulphate. A method according to any one of Claims 30 to 35, wherein the fire-retardant liquid is added in the range of 7 - 15% solid fire retardant compound to oven dry weight of cellulosic fibre. A method according to Claims 35 and 36, wherein the first stream is a stream of wood fibres and the solution of ammonium polysulphate is added to the wood fibre stream at a rate in the range of 7 - 15% by weight solid ammonium polysulphate to oven dry weight of wood. A method according to Claim 37, wherein the ammonium polysulphate is added to the wood fibre stream at a rate in the range of 7 - 10% by weight of solid ammonium polysulphate to oven dry weight of wood. A method according to Claim 29, further comprising mixing the stream of hot and wet cellulosic fibres with (1) an isocyanate binder emulsified with a diluent and (2) an aqueous solution of ammonium polysulphate, before forming the mixture into a mat. A method according to Claim 39, wherein the weight of solid ammonium polysulphate in the mixture comprises 7 - 15% of the oven dry weight of cellulosic fibres in the mixture.

Inventors: BAUER TED J, HARMON DAVID M, KIRWAN RORY GERARD, TRELIVING GORDON, BAUER, TED J, HARMON, DAVID M, KIRWAN, RORY GERARD, TRELIVING, GORDON
Applicants: MEDITE CORP, MEDITE EUROP, MEDITE CORPORATION, MEDITE OF EUROPE LIMITED
Application year: 1990
Main classification: B27N1
IPC codes: B01F3, B01F5, B27N9, B27N1, B27D1, E04B1