Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B13/00—Machines or plants for applying liquids or other fluent materials to surfaces of objects or other work by spraying, not covered by groups B05B1/00 - B05B11/00
  • B05B13/02—Means for supporting work; Arrangement or mounting of spray heads; Adaptation or arrangement of means for feeding work
  • B05B13/04—Means for supporting work; Arrangement or mounting of spray heads; Adaptation or arrangement of means for feeding work the spray heads being moved during spraying operation
  • B05B13/0463—Installation or apparatus for applying liquid or other fluent material to moving work of indefinite length
  • B05B13/0484—Installation or apparatus for applying liquid or other fluent material to moving work of indefinite length with spray heads having a circular motion, e.g. being attached to a rotating supporting element
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05D1/00—Processes for applying liquids or other fluent materials
  • B05D1/02—Processes for applying liquids or other fluent materials performed by spraying
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B13/00—Machines or plants for applying liquids or other fluent materials to surfaces of objects or other work by spraying, not covered by groups B05B1/00 - B05B11/00
  • B05B13/02—Means for supporting work; Arrangement or mounting of spray heads; Adaptation or arrangement of means for feeding work
  • B05B13/0221—Means for supporting work; Arrangement or mounting of spray heads; Adaptation or arrangement of means for feeding work characterised by the means for moving or conveying the objects or other work, e.g. conveyor belts
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B15/00—Details of spraying plant or spraying apparatus not otherwise provided for; Accessories
  • B05B15/60—Arrangements for mounting, supporting or holding spraying apparatus
  • B05B15/62—Arrangements for supporting spraying apparatus, e.g. suction cups
  • B05B15/628—Arrangements for supporting spraying apparatus, e.g. suction cups of variable length
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B7/00—Spraying apparatus for discharge of liquids or other fluent materials from two or more sources, e.g. of liquid and air, of powder and gas
  • B05B7/02—Spray pistols; Apparatus for discharge
  • B05B7/12—Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages
  • B05B7/1254—Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages the controlling means being fluid actuated
  • B05B7/1263—Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages the controlling means being fluid actuated pneumatically actuated
  • B05B7/1272—Spray pistols; Apparatus for discharge designed to control volume of flow, e.g. with adjustable passages the controlling means being fluid actuated pneumatically actuated actuated by gas involved in spraying, i.e. exiting the nozzle, e.g. as a spraying or jet shaping gas
• • 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
  • D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
  • D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
  • D21H23/22—Addition to the formed paper
  • D21H23/50—Spraying or projecting
• • 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
  • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
  • D21H27/18—Paper- or board-based structures for surface covering
  • D21H27/22—Structures being applied on the surface by special manufacturing processes, e.g. in presses
  • D21H27/26—Structures being applied on the surface by special manufacturing processes, e.g. in presses characterised by the overlay sheet or the top layers of the structures
  • D21H27/28—Structures being applied on the surface by special manufacturing processes, e.g. in presses characterised by the overlay sheet or the top layers of the structures treated to obtain specific resistance properties, e.g. against wear or weather
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
  • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
  • B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
  • B05B1/30—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to control volume of flow, e.g. with adjustable passages
  • B05B1/3033—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to control volume of flow, e.g. with adjustable passages the control being effected by relative coaxial longitudinal movement of the controlling element and the spray head
  • B05B1/304—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to control volume of flow, e.g. with adjustable passages the control being effected by relative coaxial longitudinal movement of the controlling element and the spray head the controlling element being a lift valve
  • B05B1/3046—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to control volume of flow, e.g. with adjustable passages the control being effected by relative coaxial longitudinal movement of the controlling element and the spray head the controlling element being a lift valve the valve element, e.g. a needle, co-operating with a valve seat located downstream of the valve element and its actuating means, generally in the proximity of the outlet orifice
  • B05B1/306—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to control volume of flow, e.g. with adjustable passages the control being effected by relative coaxial longitudinal movement of the controlling element and the spray head the controlling element being a lift valve the valve element, e.g. a needle, co-operating with a valve seat located downstream of the valve element and its actuating means, generally in the proximity of the outlet orifice the actuating means being a fluid

Definitions

• the present invention relates in general to impregnated laminates, and more particularly to a method and apparatus for applying abrasion-resistant particles to a surface sheet used in such laminates, and surface sheets produced thereby.
• Laminated materials such as those formed of paper and impregnated melami ⁇ e-formaldehyde resins and the like, find uses as surfacing materials in countertops, table tops, wails and the like. These laminates typically consist of a stack of several impregnated paper webs. A top or surface sheet of the stacked laminate most often contains a pleasing design and/or color. It is desirable to impart abrasion resistance to this top sheet so that it will not be worn away to expose the u ⁇ decorative kraft paper laminations underneath it.
• One way to impart abrasion resistance to the top or surface sheet is to coat or otherwise apply abrasion-resistant particles to the sheet. The particles can, for example, be any of several hard minerals such as alumina or silica.
• U.S. Patent No. 4,940,503 issued to Li ⁇ dgren et al. illustrates a method of applying small, dry, hard particles directly on to the surface of a wet impregnated paper web through a doctor-roll.
• abrasion-resistant paniculate matter such as alumina is applied electrostatically to a wet, impregnated web and the web then dried.
• hard particulate matter such as alumina is deposited on the surface of a dry web using a binder such as microcrystalli ⁇ e cellulose.
• micr ⁇ crystalline cellulose as a binder has drawbacks when particular visual effects, such as peariescent or opalescent effects, are desired.
• the highly refractive nature of microcrystalline cellulose defeats this visual characteristic.
• the application of the grit at an early stage causes increased wear on the web rollers because of the presence of abrasive particles. The need therefore exists in the industry for an improved method and apparatus for applying abrasion-resistant particles to a surface sheet web.
• a method for manufacturing abrasion-resistant surface sheets for laminates includes the steps of impregnating the web with a thermosetting resin; prior to drying the web, spraying the impregnated web with a slurry including abrasion- resistant materials; thereafter drying the impregnated web; and cutting the web into sheets of predetermined length.
• the step of spraying the slurry of abrasion-resistant materials is performed by a rotary head which is disposed above the impregnated web.
• a preselected number of spray arms are affixed to the rotary head so as to radially and downwardly extend from the rotary head.
• a spray pistol is mounted on a remote end of each of the spray arms.
• a pressurized air pipeline and a slurry pipeline are connected to each of the spray pistols.
• the rotary head rotates and the spray pistols spray a slurry of abrasion- resistant particles onto the surface of the web. This provides a more uniform coverage than has heretofore been obtained with such methods as dropping dry particles onto a web or electrostatic adherence.
• a station for partially drying the web occurs immediately after the spray station. Then, a coating of thermosetting resin is applied to the partially dried web at a coating station placed after the first drying station. The web is then further dried in a second drying station. The dried web is then cut into surface sheets.
• Top sheets produced by the invention have a paper web impregnated with a thermosetting resin selecting from the group consisting of melamine-formaldehyde, phenol-formaldehyde, phenol-urea- formaidehyde, melamine-urea-formaldehyde, urea-formaidehyde and polyester, and having a resin content between 30 and 80% by weight.
• the abrasion-resistant particles are sprayed onto the upper surface of the web before drying at a concentration of 1 to 40 grams per square meter.
• the particles preferably have a size falling within a Gaussian distribution centered around 9 microns, and are selected from the group consisting of alumina, silica, silicon carbide, boron nitride, diamond and mixtures of the foregoing.
• the use of abrasion-resistant particles of this size provides good abrasion resistance, but does not detract from a peariescent or opalescent effect contributed by the design of the top sheet.
• the present invention provides several technical advantages.
• the claimed method can be put into practice by merely incorporating the slu ⁇ y-spraying step into a conventional laminate-producing installation. This allows existing equipment to be used. Applying the abrasion-resistant material through spraying allows the process to be highly controlled and to be controlled independently from the initial impregnation step. Cylinders which come into contact with the impregnated web prior to the abrasion- resistant particle application step do not experience any wear from such particles, which tend to be abrasive themselves. The method and apparatus of the invention also avoid the use of special papers. BRIEF DESCRIPTION OF THE DRAWINGS
• FIGURE 1 is a schematic diagram of a process for fabricating abrasion-resistant surface sheets, diagrammaticaUy illustrating several successive steps in the process;
• FIGURE 2 is a detail of FIGURE 1 showing the beginning stages of the process
• FIGURE 3 is a schematic elevatio ⁇ ai view of a rotary spray head according to the invention.
• FIGURE 4 is an elevational sectional detail of a slurry spray pistol according to the invention.
• FIGURE 1 a schematic representation of apparatus for the continuous manufacture of abrasion-resistant surface sheets is shown including a plurality of stations at which different process steps are performed. At point 100, a continuous paper web is fed into the process.
• the paper does not require any special characteristic with respect to the later application of the abrasion-resistant material.
• the paper will typically have a decorative printed design or the like, as is suitable for a top or surface sheet of a laminate.
• the web is fed through the various process stations by use of standard conveying equipment (only schematically shown).
• a first impregnation of the paper web occurs.
• the impregnation is performed in a conventional manner.
• the impregnation may be carried out with a vessel or bath of melamine- formaldehyde, phenol-formaldehyde, phenol-urea-formaldehyde, melamine- urea-formaldehyde, urea-formaldehyde or polyester, with a resin content of 30 to 80% and preferably between 40 and 60% by weight.
• the first impregnation step at station 101 is performed using a drip-and-squeeze process with a resin bath having a viscosity in the range of 20 to 100 centipoises, and with squeeze rollers 103.
• the impregnated web 102 next passes to a station 104, which includes an enclosed cabin or compartment 106.
• the web 102 is carried in a flat condition by a conveyor belt 107 or the like (see FIGURES 2 and 3).
• a slurry of hard paniculate matter is sprayed onto the surface of the web 102 using pressurized air.
• the siurry is formed through a continuous agitation of abrasive particles, water and/or adequate solvents or binders as well as a dispersion/suspension agent.
• the dispersion/suspension agent can be a polyacrylic acid or the like. The dispersion agent prevents the grit from settling down and keeps it dispersed in the slurry.
• the slurry contains an abrasive particle weight in the range of 5 to 40%.
• the slurry should have a final viscosity range in between 5 and 80 seconds No. 4 Ford cup (10-200 centipoises), and more preferably, between 10 and 30 seconds (15-100 centipoises).
• the surface of the paper web 102 is sprayed until it is uniformly covered with a weight of 1 to 40 grams per square meter and, more preferably, between 2 and 20 grams per square meter.
• the abrasive particles can be constituted by any of several materials, such as alumina, silica, silicon carbide, boron nitride, diamond or a mixture of any of the above.
• the particle size affects the characteristics of the finished laminate surface in that the greater the particle size, the greater the abrasion resistance.
• One advantage of the invention is that because the particle slurry is directly sprayed onto the wet impregnated web 102, no microcrystalline cellulose or other binder is necessary. However, where a binder is desired, any can be used as long as it is compatible with the impregnation resin applied to the web at station 101.
• binders such as modified caseins, acrylic compounds, polyvinyi alcohols, et cetera can be used in binder: grit weight ratios ranging from 1:5 to 1:15.
• the grit size In the instance where the design definition calls for a peariescent or opalescent effect in the final surface sheet, the grit size
• the average thickness of the abrasive particle coating on the web 102 is in the range of 1 to 8 microns.
• FIGURE 2 The beginning steps of the process are illustrated in more detail in FIGURE 2.
• a continuous paper web 112 is fed via rollers 114 between a photocell 116 and a light source 118.
• Photocell 116 and light source 118 coact such that when the end of the web 112 is reached, the photocell 116 will be activated.
• Photocell 116 is connected by a relay or the like (not shown) to each of a plurality of valves mounted in respective spray pistols of the slurry sprayer 108, all of which will be described below;
• Web 112 is then guided by rollers 120, 122, 124, 126, 128 and 130 through a vat or both 132 of meiamine formaldehyde resin or other impregnation resin.
• a novel rotary sprayer indicated generally at 108 includes a plurality of spray arms indicated schematically at 134, each arm 134 terminating in a spray pistol 136.
• the arms 134 are connected to a rotary spray head 138 which is driven to rotate about its axis indicated by the dashed line 140.
• the rotary spray head 138 may, for example, be belt- driven by an apparatus such as a drive belt indicated schematically at 142 and an electric motor indicated schematically at 144.
• the electric motor indicated schematically at 144.
• FIG. 144 has a speed variator which is coupled to the general motor (not shown) of the apparatus 10.
• This general motor regulates the speed of the paper web 112 so as to synchronize rotation speed of the head 138 and of the paper in the apparatus 10.
• the rotary sprayer 108 and associated equipment are illustrated in more detail in FIGURE 3.
• FIGURE 3 two spray arms 134 are shown instead of the three arms 134 that are shown in FIGURE 2. The number of spray arms may be varied according to the application.
• the number of spray arms may be varied according to the application.
• spray arms 134 are radially displaced from the axis 140 and are angularly disposed around the circumference of the spray head 138 preferably to be equally separated from each other.
• Each spray arm 134 includes an arm segment 146 which is directly affixed to the spray head 138.
• the arm segment 146 distally terminates in an adjustment sleeve 148.
• a second arm segment 150 has a first proximal end fitted into the adjustment sle&ve 148 and a second distal end terminating in a sprayer carrier holder 151.
• the adjustment sleeve 148 includes fasteners for adjustably holding the arm segment 150 in place, such as a screw or screws 154 or the like.
• a spray carrier 152 is fitted into the carrier holder 151.
• the carrier holder 151 likewise is an adjustment fitting, and includes a screw or screws 156 or the like. Carrier holder 151 allows the distance from the pistol 136 to the web being treated 158 to be adjusted.
• Each sprayer carrier 152 terminates in at least one spray pistol
• the radial distance of the pistol 136 from 5 the axis 140 can be adjusted.
• the radial arms 134 are adjusted in order to take into account the differing widths of the impregnated web 158 which - might be treated, which for example may range from 1240 to 1700 mm.
• Each spray pistol 136 receives pressurized air in a respective air pipeline 160 and liquid slurry in a respective slurry pipeline 162. Air
• 10 and slurry pipelines 160 and 162 are preferably sized to be at least 5 mm. in interior diameter.
• the air inside air pipe 160 is compressed, as by a compressor schematically illustrated at 164, to a pressure in a range of 2 to 10 kg/cm 2 in order to impart suitable spraying force to the slurry emitting from pistols
• a slurry pump schematically illustrated at 166 may be used to provide slurry under pressure to pipes 162.
• a slurry feed pressure in the range of 1.5 to 4 kg/cm 2 has been found suitable for operating the spray pistols 136, with a preferred slurry pressure of 1.5 to 2 kg/cm 2 .
• the spray pistols 136 each produce a conical spray or haze
• a single pipe or a line 170 be used to convey the pressurized .. air into the spray head 138, at which point air pipe 170 branches into a plurality of pipes or lines 160.
• a single pipe 172 carries the
• '-5 pressurized slurry from the siurry pump 166 into the rotary head 138, where it branches into a plurality of slurry pipelines 162 equal in number to the number of spray pistols 136.
• FIGURE 4 is a detailed elevatio ⁇ al sectional view of a single spray pistol 136.
• a body 174 of the pistol 136 has formed therein a central bore 176 which is formed around a pistol axis 178.
• the bore 176 has a tapered lower orifice 180.
• Received into the bore 176 is a needle 182 having a frusto-conical end surface 184 adaptable to seat on the tapered surface of orifice 180.
• the elongate needle 182 extends into a top portion 186 of the pistol 136 having relatively thin sidewalls 188.
• Sidewalls 188 define a lower chamber 190 and an upper chamber 192.
• a spring 194 is operable to exert force between a needle flange 196, affixed to needle 182, and a pistol cap 198.
• the cap 198 includes a central bore 200 adaptable to slidably receive a top end 202 of the needle 182 when the needle 182 is in an upward or open position.
• the flange 196 slides in close registry with the sidewalls 188 of top portion 186.
• a sealing gasket or ring 204 allows a coaxial up-and- down sliding motion " of the needle 182, but nevertheless substantially hermetically separates the lower chamber 190 from the bore 176.
• the air pipe 160 branches into a first length 206 regulated by a remotely controlled valve 208, and a second branch 212. Extending from the remotely controlled valve 208 to the lower chamber 190 is a pipe segment 210. When the valve 208 is open, pressurized air from pipe 160 flows into the lower chamber 190, urging the needle flange 188 in an upward direction against the bias exerted by the spring 194. The upward urging of the needle 182 will cause frustoconical surface 184 to unseat itself from the tapered surface of orifice 180, causing sloped orifice 180 to open.
• branch 212 communicates the air pipe 160 with an annular outiet 214. Air flowing out of the outlet 214 imparts downward spray force to the slurry.
• the slurry is fed by slurry pipe 162, and enters into bore 176 and out through the orifice 180.
• the spring 194 forces the needle 182 into registry with the sloped walls of the orifice 180, thus cutting off the spraying of slurry from pipe 162.
• Remotely controlled valve 208 preferably is controlled by the photocell 116 (FIGURE 2). When the photocell 116 senses that the end of the web 112 has passed it, it will cut off the spraying of slurry from each of the pistols 136 by closing the respective remotely controlled valves 208.
• the cap 198 may be removed for servicing of the spray pistol interior.
• the web 158 is passed to a first drying oven station 216.
• a coating station 218 at which a second coating of meiamine or other thermosetting resin is applied to the surface of the web. It is preferred that this be performed by a roller-coating operation as indicated by roller 220.
• the meiamine or other thermosetting resin used at station 218 can have a viscosity in the range of 30 to 300 centipoises.
• the additional coating provides the surface of the web with various special characteristics as desired.
• other additives may be added to the web at this point, such as finer abrasive particles, peariescent pigments, and other materials.
• a web 222 is produced which is passed to a second drying stage or oven 224.
• the dried web 226 is subsequently passed to a cutting stage 228 at which the web 226 is cut into surface sheets 230 having a desired length.
• TTiese may be subsequently used in a laminating process to create laminates for use in countertops, walls, partitions and the like.
• the surface sheets 230 may be subjected to laminating temperatures and pressures that are normally used in higher pressure laminates, such as a temperature in the range of 120 to 160° C, depending upon the type of resin used, and pressure of 70 to 120 kilograms per square centimeter.
• the present invention provides several technical advantages. It may be put into practice by merely incorporating the innovative spray step shown at 104 into an installation having otherwise conventional process steps.
• the abrasive coating is applied in a direct and very controllable fashion in a step which is independent from the initial dip-a ⁇ d-squeeze impregnation which takes place at step 101.
• the squeeze cylinders 103 do not suffer from abrasion due to abrasive particles, as the abrasive slurry is sprayed onto the surface of the web only after excess resin is squeezed out of the web in the first impregnation step. This, in turn, reduces the number of failures and increases the lifetime of the process equipment.
• the present invention also avoids the use of special papers where abrasion resistance is desired.
• the surface sheets 230 finally produced are therefore based on a web that is first impregnated with a first resin at a dip-and-squeeze 101.
• a layer of abrasion-resistant particles is applied to the web at station 104.
• the web is completed with the application of a second thermosetting resin, which may be the same or different from the resin initially applied at step 101. This allows additional materials to be placed on the surface of the surface sheet, such as finely divided abrasive particles and the like.

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• 1992
  • 1992-02-27 ES ES09200439A patent/ES2050598B1/es not_active Expired - Fee Related
• 1993
  • 1993-02-26 NZ NZ247012A patent/NZ247012A/en unknown
  • 1993-02-26 KR KR1019930002975A patent/KR100243722B1/ko not_active IP Right Cessation
  • 1993-02-26 CA CA002090553A patent/CA2090553A1/en not_active Abandoned
  • 1993-02-26 WO PCT/EP1993/000456 patent/WO1993017182A1/en not_active Application Discontinuation
  • 1993-02-26 EP EP93906472A patent/EP0583463A1/en not_active Withdrawn
  • 1993-02-26 AU AU33840/93A patent/AU3384093A/en not_active Abandoned
  • 1993-02-27 CN CN93103588A patent/CN1084786A/zh active Pending
  • 1993-03-01 JP JP5080001A patent/JP2653746B2/ja not_active Expired - Lifetime
  • 1993-03-04 TW TW082101599A patent/TW254891B/zh not_active IP Right Cessation
  • 1993-10-26 NO NO933851A patent/NO933851L/no unknown
  • 1993-10-26 FI FI934726A patent/FI934726A/fi not_active Application Discontinuation

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