CA2094253C

CA2094253C - Meltblowing die

Info

Publication number: CA2094253C
Application number: CA002094253A
Authority: CA
Inventors: Martin A. Allen; John T. Fetcko
Original assignee: Nordson Corp
Current assignee: Nordson Corp
Priority date: 1990-10-17
Filing date: 1991-10-11
Publication date: 2000-02-15
Anticipated expiration: 2011-10-11
Also published as: US5269670A; DE69126667T2; US5445509A; AU8862691A; WO1992007121A2; DE69126667D1; AU655441B2; JPH06502453A; US5605706A; EP0701010A1; JP2623169B2; CA2094253A1; KR930702562A; US5421941A; EP0553237A1; EP0553237B1; KR100192731B1; US5145689A; WO1992007121A3

Abstract

A melt-blowing die assembly features (a) intermittent operation, (b) modular valve actuator to selectively shut off polymer flow, (c) an in-line electric heater, and (d) melt-blowing units arranged in side-by-side relationship.

Description

1 ~~942~~
MELTBLOWING DIE

1 This invention re ates genera y to meltblowing and in particular to improved meltblowing dies. In one aspect the invention relates to a modular die construction featuring intermittent operation of individual modules thereby permitting the application of meltblown material in a predetermined pattern.
r In another aspect, the invention relates to an unproved heater/meltblowing die assembly. In a~specific aspect, the invention relates to a method of applying an adhesive or web to a diaper film:
, Meltblowing is a process in which high velocity hot air (normally referred to as "primary air") is used to blow molten fibers extruded from a die onto a collector to form a web or onto a substrate to form a coating or composite. The process employs a die provided with (a) a plurality of orifices formed in a tip of a triangular shaped die tip and (b) flanking air passages. As extruded strands of the polymer melt emerges from the orifices, the converging high velocity hot air from the air passages stretches and draws them down by drag forces forming ~nicrosized f i 1 aments.
The filaments are drawndown to their final diameter of 0.5 to 20 microns (avg.) in the case of polyolefin polymers such as polypropylene and to 10 to 200 microns in the case of polymers used in adhesives and spray coating. The strands extruded from the die may be continuous or discontinuous fibers. For the purpose of the present description, the term "filament" refers to both the continuous and discontinuous strands.
The meltblowing process grew out of laboratory research by the Naval Research Laboratory which was published in Naval Research Lahoratory Report 4364 "Manufacture of Superfine Organic Fibers", April 15, 1954. Exxon Chemical developed a variety of commercial meltblowing dies, processes, and end-use products as evidenced by U.S. Patents 3,650,866, 3,704,198, 3,755,527, 3,825,379., 3,849,241, 3,947,537, and 3,978,185, to name but a few.
Other die designs were developed by Beloit and Kimberly Clark.

1 Representative meltblowing patents of these two companies include 3,942,723, 4,100,324, and 4,526,733. kecent meltblowing die improvements are disclosed in U.S. Patents 4,889,476, 4,818,463 and 4,889,476.
A key component in the meltblowing die assembly is the die tip which is a machined steel member having a triangular nose-piece through which the orifices are formed. In the die assembly, air Massages are formed on opposite sides of the~converging tri-angular nose piece, meeting at the apex where the polymer melt .
emerges from the orifices. Most of the melt blowing prior art dies employ a long die tip (typically from 10 to 120 inches and longer) having evenly-spaced, side-by-side orifices. In order to provide the desired air drag forces by the primary air on the filaments, the included angle of the nosepiece (which determines the direction of the air flow has been about 60' so that the primary air has a major velocity component parallel to filament spinning.
Also, the meltblowing die assemblies are operated .
continuously. Interrupting polymer flow presents two problems:
ZO (a) polymer continues to dribble out of the polymer orifices, and (b) the air tends to aspirate polymer from the die tips causing undesired afterflow. At the present, when a rneltblowing die is shut down, it continues to flow out polymer until the residual polymer in the distribution manifold, the screen pack section and 25~ the die tip has emptied itself due to gravitational and aspira-tional forces. This can be as much as 5 lbs. of melt for conventional dies.
Another feature cacmon to most, if not all, meltblowing dies is the air heating system. Energy used to heat the air is 30 one of the most expensive operational items of meltblowing systems. Generally, the air is compressed and flowed through a furnace and conducted through large insulated conduits to air distribution manifolds on the die assembly. The use of a single furnace fnr the system not only presents prablerns in design 35 (because.large space must be provided to house the furnace and 2i1.~~1~~3 1 large conduits) but it also is energy inefficient (because of thermal loss between the furnace and the die assembly). Even small improvements in thermal efficiency can produce large savings in energy costs.
Summarizing the state of prior meltblowing dies, there is a need (a) to provide intermittent polymer discharge from the dies, and (b) to improve the..air.heater facilities.
SUMMARY OF THE INVENTION
The present invention provides a die assembly which features (a) intermittent operation for controlled meltblowing polymer deposition, (b) a modular u~eltblowing die assembly, (c) an improved air heating system, and (d) a plurality of separate meltblowing die un its operable in parallel to permit the use of different resins or different patterns.
A novel feature of the meltblowing die constructed according to the present invention is its internal valve with external actuator. By prograrnning the valve actuator, the valve can be opened or closed to control the flow of polymer melt through the die. It has been discovered that by designing the polymer flow passage to limit the volume of polymer melt between the valve and the die outlet, the polymer flow can be interrupted;
or shut off, with none or only negligible polymer afterflow or dribbling, even with continued operation of the meltblowing air.
In a preferred embodiment, the valve in the die includes a valve seat and a stem having one end sized to mate with valve seat and the other end operatively connected to the valve actuator. The valve seat and stem end are designed to create a pressure or rate pulse attendant to actuation of the stem. The high pulse flow through the die aids in removing or preventing the buildup of polymer residue on or in the orifices.
In another embodiment of the invention, the die comprises a series of side-by-side melt blowing units which are separately and independently operable (except for the air flow).
The units may be fed with separate resin or operated under different conditions (e.g. flow rate) to produce a variety of WO 92/07121 1'Lf/US91/07525 ,~~9 4~Z5~3 1 patterns. When the die asse;nbly is provided witn internal valves, each valve (one for each unit) is operatively connected to a modular valve actuator. The valve actuators may be programmed to interrupt the flow of polymer through certain units while continuing polymer flow through other units. This selectivity is particularly useful in applying adhesives or polymer melt to a substrate of predetermined shape.(e.g. diaper backsheet).
Still another novel feature of the present invention is the in-line electric heater connected directly to the die assembly for heating the air. The high-efficiency electric heater permits the use of much smaller diameter air feed lines. Moreover, the feed lines need not be insulated. Perhaps most important, radiant heat losses are ;minimized since the air is heated immediately upstream of the die assembly.
BRIEF OESCRIPTION-OF THE DRAWINGS
Figure 1 is a perspective view illustrating a die assembly constructed according to the present invention.
Figure 2 is a front elevational view of a die assembly constructed according to the present invention, with portions cut away.
Figure 3 is a side eieyational view of the die assembly shown in Figure 1 showing details thereof.
Figure 4 is a top plan view of one pattern of product made by the die assembly of Figure 1.
Figure 5 is a sectional view of the assembly shown in Figure 3 illustrating internal details thereof.
Figure 6 is an enlarged view of the die tip shown in Figure 5.
Figure 7 is a sectional view of the assembly shown i.n Figure 5 with the cutting plane taken along line 7-7 thereof.
Figure 8 is a sectional view of the die assembly shown in Figure 5 with the .cutting plane taken along line 8-8 thereof.
Figure 9 is a sectional view of the die tip shown in Figure 6 with the cutting plane taken along line 9-9 thereof.

~~J~42~3 1 Figure 10 is a persNective sectional, sectional view of . the die tip shown in assembly of Figure s 1-3, 5, and 6.
Figure 11 is a perspective view of a heater useably in the assembly shown in Figures 1 and 3 with portions cut away to illustrate internal parts.
Figures 12 - 14 illustrates an alternate valve assembly useable in the intermittently operated ,neltblowing die.
DESCRIPTItIN OF THE PREFERRED EMBODIMENTS
With reference to Figures 1-3 and 5, a die assembly 10 of ,the present invention comprises a die body 11, valve assembly 12 comprising a plurality of 'valve actuators 15 (shown as 15A-150 in Figure 2), die tip assembly 13, air delivery line I4 including in-line air heater 16 and polymer delivery line l7.
As will be described in detail below, polymer melt is delivered to body 11 and extruded through orifices in the die tip I3 forming filaments (or fibers) 18. Hot air is delivered to each side of the row of filaments l8 to stretch and attenuate the filaments. The filaments 18 are deposited on a suitable substrate 19 or collector; such as a rotating screen or conveyor.
Operation of the valve assembly l2 provides for selective inter-mittent polymer flow so that various patterns may be formed and collected on the substrate or collector 19. The form and type of pattern may be varied by programming the valve operation.
When using small orifices (typically in the size range 't5 of 0.010" to 0:020" for meltblowing polymers) the collection of microsized filaments may be in the fonn of a nonwoven web. When the die assembly 10 is operated to me~ltbtown adhesive polymers, the collection may be as an adhesive layer 20 on substrate 19 as illustrated in Figure 1. The die,assembly 10 may also be used in other meltblowing polymer applications such as coating. Other collection devices such as filter cylinders, composites, etc. are , possible.
Details of the present invention will be described with reference to its four main components: (1) die body 11, (2) valve assernbly 12, (3) die tip assembly 13, and (4) air heater 16.

N0~42~

1 Die Body (Figures 2, 5, 7; and 8) As shown in Figure 2, the die body 11 is a relativaly large, elongate steel body which supports the other components.
Although integral in structure, the body 11 may be viewed as a plurality of separate functional units 11A, 118, 11C, and 11D, each unit being independent; of the other units: The embodiment illustrated in Figure I contains four side; by-side units 11A-11D, but it should be emphasized that the body may consist of from 1 to 100 units. Note that Figure l discloses a die assembly 10 compris-ing 9 actuators 15 which means the die body 11 is provided with 9 units.
Only one (unit 11A) of the units 11A-11D will be descri-bed in detail, it being understood that the polymer and air passages formed in all of the units 11A-11D will be generally the same. The description with reference to Figures 5 and 6 of Unit 11A and its associated actuator 15A will be without letter designation. However, each of the other units 11B-150 will have corresponding parts. The description with reference to Figures depicting more than one unit will include the letter designation to denote the separate units.
Referring first to Figure 5, die body 11 has formed therein intersecting polymer passages 23 and 24. Passage 23 connects to polymer feed line l7 through header manifold 22, and passage 24 is vertically aligned with valve actuator 15 and die tip assembly 13. In Figure 1, the polymers.feed line 17 is illustrated as entering manifold 22 from the vertical. (For simplicity of description, the feed line 17 in Figures 3, 5, and 7 is illustrated as entering manifold 22 in the horizontal.) Also formed in die body ll is an opening 25 extending upwardly from passage 24 and terminating in threaded counterbore 27.
The lower end of passage 24 is threaded for receiving insert 28 having port 29 formed therein. The inlet to port 29 is shaped to provide a valve seat 30, as described in detail below.
As best seen in Figure 8, each polymer passage 23A-D is fed by a manifold 22 having a balancing header 25 in the 1 form of a clothes hanger spanning the four inlets of passages 23A-23D. Returning to Figure 5, polymer flow through the body 11 is from line 17,~through header 25, through flow passages 23 and 24 of each unit in parallel flow pattern, discharging through port 29 of each unit. The flow through each unit preferably is at the scone rate. , As shown in Figure 7, the bottom side of die body li has a machined out section which defines elongate air chamber 39.
The circular inserts 28A-280 mounted on the die body 11 as previously described separate the air chamoer 39 from polymer flow passages. The air chamber 39 defined by end walls 34, 35 and side walls 36, 37 is continuous throughout the die body 11 and surrounds the unit inserts 28A-280.
Referring to Figures 5 and 7, a plurality of air pas-sages 32 extend through die body 11 into chamber 39. The air passages 32 are distributed along wall 36 of the die body 11 to provide generally uniform flow of air into chamber 39. Air is fed by header 33 which may be formed in block 22.
The electric in-line heater 16 is connected to the inlet of air block immediately upstream of header 33. Air thus flows from air line l4 through heater 16, through air header 33, through air passages 32, in parallel flow, into chamber 39.
Oie Tip Assembly (Figures 6, 9, and lOj The die tip assembly 13 is mounted to the underside of the die body ll and covers air charier 39. This assembly comprises a stack up of three members: a transfer plate 41, a die tip 42, ' and air plates 43 and 44. The transfer plate 41 extends substan-tially the full length of die body 11 and is secured thereto by bolts 46 through countersunk holes 47. Pairs of air holes 48 and 49 convergingly extend through the thickness of plate 41. Tne pairs of_air holes 48 and 49 (as best seen in Figure 9j are pro-vided for each of the units IlA=110. The inlets of air holes 48 and 49, communicate with the air chamber 39 on opposite sides of the row of inserts 28. As best seen in Figure 6, each pair of holes 48 and 49 tapers convergingly inwardly toward one another.

~~J94'~53 1 A central pol~nner passage 51 is aligned with port 29 and polymer passage 24 of the die body 11. Formed in the lower surface of the plate 41 are longitudinal channels 52 (shown as 52A-52D in Figure 9). Each channel 52 penetrates a short distance into the thickness of the transfer plate 41 and extends substantially the width of the unit but is separated frorn its adjacent channels. As shown in Figure 9, the channels 52A-52D are longitudinally aligned and in combination extend substantially the entire length of the plate 41. The ends of channels 52 are preferably closely spaced apart so that the orifices spacing along the die tip are equally spaced substantially along its entire die tip length. Also formed is the transfer plate 41 are bolt holes 50 for securing the die tip 42 and air plates 43 and 44 as described below.
As best seen in Figure 10, the die tip 42 comprises a tapered nose piece 53 of triangular cross section flanked by flanges 54. Returning to Figure 6, the base 58 of die tip 42 opposite the nose piece 53 is substantially flat and is sized to fit on the exposed lower side of transfer plate 41. The tapered nose piece 53 comprises tapered and intersecting surfaces 57a and 57b. A plurality of air passages 55 and 56 (Figure 5) extend through the die tip 42. Each flow passage comprises portion 55a aligned with an air passage 48 of the plate 41 and portion 55b which discharges at a mid section of surface 57a and passage likewise comprises portion 56a aligned with a flow passage 49 of plate 41, and 56b discharging at a midsection on surface 57b.
The flat surface 58 of the die tip 42 has formed therein a plurality of channels 59 of the sane size and shape as channels 52 of the transfer plate 41. The channels 59 and 52 form elongate polymer flow distribution chambers 60 for the orifices 61 as shown in Figures 2 and 5. Extending through the die tip 42 are a plurality of flow passages terminating in orifices 61.
The outlet of each air passage 55b or 56b forms an angle with its associated surface 57 or 58, respectively. The axis of the outlets of passages 55b or 55b define,an angle (B) with surface 57a or 51b, of between 75' and 90'; preferably between 80' 20~4~a3 _ g _ 1 and 9U°. Preferably the axes of passages 55h, 55a, 48, 49, 56c, and 56b, fall in the same vertical plane. From about 5 to 20 pairs of air passages are provided for each unit chamber 60A-60D, or about;2 to 15 pairs per inch of die.
The flanges 54 of die tip 42 are provided with threaded holes 62 permitting the t,ransf~er plate 4I to be bolted thereto by bolts 63. doles 64 formed in the flanges 54 permit the insertion of bolts 46 to secure the transfer plate 41 to body 11. The ai r plates 43 and 44 are provided with holes (not shown) aligned with holes 64 for the same purpose.
The air plates 43 and 44 are bolted to each side of the nose piece 42 by bolts 66 through countersunk holes 67 provided near the base of the nose piece 53. Flat portion 68 of each air plate 43 and 44 fits on the outer surface of each flange 54, Each plate 43 and 44 is secured to the flanges by bolts 63.
Each air plate 43 and 44 has a surface 69a or ti9b tapered about the same angle as the taper of nose piece surfaces 57a or 57b. The bolts 66 extend angularly through holes 67 in plate 43 or 44 and screw into nose piece 53 securing the air plates 43 and 44 to the die tip 42. In assembled condition plate , surface 69a abuts tapered surfaces 57a and plate surface 69b abuts tapered surface 57b. Threader holes are also provided on the underside of each plate 43 and 44 for receiving bolts 63.
Adjacent the flat surface 69a or 69b of each air plate 43 and 44 and positioned opposite the apex region of the nose-piece is a surface 71a and 71b spaced respectively from surf ace 57a for air plate 43 and surf ace 57b for air plate 44. Between surfaces 69a and 71a is a curved groove 72a which extends substan-tially the. full. length of the nosepiece 53. Likewise between surface 69b and 71b of plate 44 is a second groove 72b. Each groove 72a and 72b is aligned with air holes 55b or 56b respec-tively so that air discharging therefrom enters groove 72a or 72b.
The space between confronting surfaces lla and 57a for air plate 43 and 71 and 57b for air plate 44 eonducts air to each side of the row of orifices 6l generally in the form of ~~9425'3 -lo-1 converging sheets. This space referred to "air gap" typically ranges from 0.0007" to 0.020". The air plate edges 73a and 73b confront one anothar furring the air passage outlet 70. The set back of the edges 73a and 73b as measured axially along orifices S 6I ranges from -0.020" to ~O.OCO". The included angle A of the nose piece 53 at the apex rangrs from 70 to 120, preferable 80 to 100' and most preferably 35 to 95'. The purpose of the grooves 72a and 72b is to balance the flow of air 'through the air gap.
Each groove 72a, 72b should have a volume at least 5 times larger (preferably 5 to 20 times larger) than the volume between con-fronting surfaces 71a and 57a.
Valve Assembly (Figure 5) The valve assembly 12 imparts intermittent flow of polymer through the die body 11 and the die tip assembly 13 for each unit~llA-11D. Depending on the valve stem construction, the intermittent flow is off-on or pulsating which can be programmed :( to produce the desired web or adhesive pattern.
The mechanism for actuating the valve for either the on-off or pulse operations is the same and is shown in Figure 5.
The assembly; comprises a pneumatic valve actuator module 15 , a stem 82, having a valve tip 83 designed to cooperate with valve seat 30 of insert 28. Each actuator module 15A-150 is bolted to the top surface of the die body 11 for its particular unit 11A-11D
as shown in Figures 1 and 2.
The valve actuator module 15 comprises piston 81 which .,i reciprocates within cylindrical chamber 84 defined. by intercon-nected housing members 86 and 87. A fluid seal 88 is provided at the interface of members 86 and 87: The piston 81 comprises a metal disc 89 with raised or gnbossed surface 91, outer 0-ring 92 sized to sealingly engage the walls of chamber 84, and a nut 93.
A compression spring 94 interposed between disc 89 (encircling embossed surface 91) and the top of chamber 84 biases the piston 81 downwardly against the bottom surface of chamber 84.
Mounted on the top of housing member 86 is an elbow connector 96 connected to tubing 97. The elbow 96 is in fluid communication with chamber 84 and serves to conduct air to and from chamber 84 above piston 81.
The lower housing member 87 has a side port 98 extending therethrough. Tubing 99 is connected to port 98 and serves to introduce and withdraw air frU,n chamber 84 below piston 81.
The stem 82 has its upper end secured to nut, 93 of piston 81 and extends downwardly through hole 101 formed the bottom of housing member 87. A~pair of opposed bushings 102 and 103 interconnect housing member 87 and die body 11. Bushing 102 is threaded to housing 37 as at 104 with fluid seal 106 provided therebetween. Bushing 103 is threaded to counterbore 27 with seal 107 provided therebetween. The bushings 102 and 103 have central openings 108 through which stem 82 is slidingly mounted. The assembly of housing members 86 and 87, and bushings 102 and 103 are maintained in stacked relation and secured to die body 11 by , bolts 111. This modular construction permits the convenient installation and removal of the valve assembly modules 15.
In order to permit adjustment of the piston stroke within chamber 84, an adjustment knob 112 is provided. Knob 112 is threaded to a stationary portion 115 and is keyed to a rod 113 which passes through hole 114 in connector 96. The end of rod 33 engages surface 91. Turning the knob 112 in one direction moves the knob 11?. and rod 113 upwardly increasing the length of the piston stroke. Turning the knob 112 in the other direction lowers the.knob 112 and the rod 113 decreasing the length of the piston stroke.
The piston 81 is actuated by control valve which may be a solenoid, 4-way, two position valve 116 fed by air supply.
Electrical controls 117 aetivates and deactivates solenoid of the control valve 116. To open the valve, the solenoid is energized causing air flow from. control valve 116 through line 99 into chamber 84 below piston 81, while air in the upper chamber 84 exhausts through line 97 and valve 116. The piston 81 moves upwardly against spring 94 until piston surface 91 contacts rod 113.

wo 92iomxi rcrius9vo~s~s 12 _ 1 In the normal deactivated position of the system, spring 94 forces piston 81 and stem 82 downwardly until stem tip 83 seats on valve seat 30 shutting off the polymer flow through port 29 to the die tip assembly 13. Energization of the control valve 116 causes the piston 81 and stem 82 to move upwardly opening port 29, permitting polymer to flow tordie tip assembly 13.
In the valve assembly embodiment illustrated in Figure 5, the valve stem closes port 29 thereby effecting on-off polymer flow. An alternate valve assembly is illustrated in Figures 12-14.
In this embodiment, the valve insert 128 and the tip 183 of stem 182 (corresponding respectively to insert 28, seat 83, and stem 82) will be in the form shown in Figure 12: The seat 128 has formed therein a large opening 120 which reduces to an intermediate cylindrically shaped opening 121 immediately above insert seat 129.
I5 Port 130 leads to transfer plate passage 51. The diameter of stem 182 is sized to fit in close conformity in opening 121, but allow reciprocal movement of the stem 182 into and out of opening 121.
Clearances of .002" to .005" are satisfactory for most applications.
In operation, the stem tip 183 with the valve open, is positioned in opening 120 as shown in Figure 12. When it is desired to pulse flow through the die tip polymer flow passages of a particular unit, the valve actuator 15 of that unit is energized causing the stem tip 183 to pass through opening 121 until stem tip 183 seats or nearly seats on seat 129. Thus the stem tip 183 acts as a plunger within cylinder 121 forcing polymer through port 130.
This action is fast and thus produces a pressure surge or pulse to clear any polymer flow passages or die tip orifices. The stroke of stem tip 183 may vary, but generally will be about 0.2 inches. The plunger action increases polymer flow through the cylinder 121 by at least 5 times normal flow, and preferably 10 to 50U times, and most preferably 20 to 100 times.
Air Heater (Figure 11) An inline electrical heater 16 is secured directly to the manifold 22, by short nipple 118 (as shown in Figure 3). Air ambient temperatures from line 14 flows through the heater 16 where it is heated to a temperature ranging from 300 to 10U0'F at 1 pressure drops of 1 to 20 psi at normal air flow rates (0.5 to 30 SCFM per inch of die length (e. g. length of the row or orifices 61).
As shown in Figure 11, the heater 16 comprises a casing 73 and serpentine heater elements 74. The elements 74 are con-tinuous and are mounted on a core 75 of insulator material such as ceramics. The core 25 extends' axially im casing 73 and has a diameter of 0.1 to 0.3 of the inside diameter of the housing. The .
interior of casing 73 is preferably provided with an insulated ' Liner 76. The inside diameter of the housing ranges from 1/4 to 3" with 1l2 to 3" being preferred.
The core 75 is ribbed or of spiral shape to maintain the elements 74 axially spaced apart. The elements 74 are continuous serpentine coils extending radially outwardly from the core 75 and have their outer tips spaced a short distance from the inside wall 76. The coil 74 is in the form of outwardly extending thin loops from the core 75 with each loop being angularly offset from its adjacent loops. The angular displacement may vary widely but from 10 to 45' is satisfactory. The ratio of the major axis of each loop extend radially outwardly and is 2 to 5 times larger than the minor axis of each loop. Electric conductor 77 connects the coils 74 to a power source (220 VAC) and the return lead 78 may be through the core 75 and connected .to the power source. Loop spacings of 0.02 to 0.25 per linear inch of the core are normally used. The electrical coils 74 may be made of tungsten, having a diameter of .010" to .080". An in-line heater useable in the present invention are manufactured by Sylvania GTE Co. In order to minimize heat losses, it is preferred that the heater 16 be mounted directly on the die assembly or within 12 inches, preferable 6 inches, therefran.
Oaeration The components of the die assembly 10 are assembled as illustrated in Figure 3: The die tip 13 is secured to the die body 11 and the valve actuator adjusted to. provide the desired stroke. The controls are set to program the valve actuators 15 thereby producing the desired pattern.

'~~~~ ~~~~ - 14 _ 1 As indicated above, the die assembly 10 may be used in meltblowing adhesives, spray coating resins, and web for.miny resins. The adhesives include EVA's (e. g: 20-40 wt% VA). These polymers generally have lower viscosities than those used in meltblown webs. Conventional hot melt adhesives useable include those disclosed in U.S. Patents 4,497,941, 4,325,853., and 4,315,842, the disclosures of which are, incorporated herein uy reference. The above melt adhesives are by way of illustration only; other ~:~elt adhesives may also be used.
The typical meltblowing web forming resins include a wide range of polyolefins such as propylene and ethylene homopoly-mers and copolymers. Specific thermoplastics includes ethylene acrylic copolymers, nylon, polyamides, polyesters, polystyrene, poly(methyl methacrylate), palytrifluoro-chloroethylene, poly-urethanes, polycarbonates, silicone sulfide, and polyethylene terephthalate), pitch, and blends of the above. The preferred resin is polypropylene. The above list is not intended to b2 limiting, as new and improved meltblowing thermoplastic resins continue to be developed.
Polymers used in coating may be the same used in melt blowing webs but at somewhat lower viscosities. Meltblowing resins.for a particular application can readily be selected by those skilled in the art.
In meltblowing resins to form webs and composites, the die assanbly 10 is connected to a conventional extruder or polymer melt delivery system such as that disclosed in U.S. Patent Appli c ation Serial No. 447,930, filed December 8, 1989, the disclosure of which is incorporated herein by reference. With either system, a polymer by-pass circuit should be provided for intermittent operation.
The number of units in each die assembly 10 will depend on the application. The syst an shown in Figure 1 comprises nine units for applying adhesive to a diaper backsheet in the pattern shown in Figure 4. The adhesives used in the experiment was pressure sensitive adhesive. As best seen in Figures 1 and 3, 2Q'~~'~~~

1 the diaper backsheet (substrate 19) is fed onto a conveyor roller and passes under the die assembly 10. The assembly was operated at polymer temperatures' of 30U'F and air temperature 325'F.
By intermittent operation of the various units, the adhesive pattern of Figure 4 is obtained. , Initially, alt of the units are operated with valves open. As the sheet l9 approaches the diaper leg cut away areas 122 and 123, the outer two modules on each side of the row of modules are actuated closing the polymer flow valves of their corresponding units. Polymer flow is interrupted in areas and 123 while polymer continues in the central region 124.
Note that the die is constructed to leave strips 125 and 126 blank.
At the end of cutaway regions 122 and 123, operation of all units is resumed. At the end of the diaper, all valves are shut off for a short period of time to leave a space between that diaper and the next one. The die assembly manufactured 400 diapers per minute. A diaper sheet is applied to the adhesives.

In another embodiment, the units of the die assembly 10 are provided with pulsating valves (Figures 12-14) to ensure polymer passage cleanup. An experiment using a meltblowing polymer (PP,MFR of 35) to form a web was tarried out.

A total of 8 units were used providing a die width of 12". The die assembly was operated at 300'F (polymer) and 325'F

(air). The polymer and air flow rates were 100 grams per minute and 1 SCFM per inch of die. The die assembly produced a web having a web of 3 grams per m2 basis weight. During operation, , an orifice becarne plugged with polymer residue. The actuator of the problem unit was manually actuated sending a polymer flow surge through the orifices by operation of the valve shown in Figure 12.

The single pulse unplugged the orifice.

,~~1~~253 _ 16 _ 1 Important dimensions each as follows of die assembly are Broad PreferredBest Range Range Mode Die Assembly Number of units 1 - 50 2 - 40 2 -Length of units (inches)1 - 10 1 - 5 1.5 Orifice (61) diameter (inches) .010-.080.010-.04U.015 Orifice/inch:

Polymer (MB) 10 - 15 - 2U -Adhesives 5 - 40 10 - 12 -Air Holes (55, 56) Diameter (inches) .020-.080.040-.070.059 Balancing groove (72) volume (cc/inch) .005-.5 ~.05-.015.09 An important feature of the die assembly constructed according to the present invention is the intermittent operation.
To minimiie polymer after flow with the valve shut, it is preferred that the volume between the valve seat and the orifice discharge be 0.3 cc per inch of die, preferably between 0.2 to 0.3 cc per inch.
Alternative Uses The die assembly 10 constructed according to the present invention as demonstrated by the above examples is quite versatile. In addition to the meltblowing of adhesives for diapers and manufacture of webs, the die assembly can meltblow under coating polymers onto metals, it can meltblow composites layers) in a selected pattern onto a substrate; it can meltblow adhesives into or onto nonwovens (e. g. spunbond fibers) to bond the fibers together; it can meltblow polyfner additives onto or into other nonwoven materials; it can also employ different resins in each unit by merely using different polymer feed system into die inlet passages 23. Other uses will occur to those skilled in the art.

2~~~:~~~
1 Summary The meltblowing die assembly 10 constructed to the present invention embodies the following features:
(a) intermittent polymer flow;
(b) a plurality of separate side-by-side units;
(c) internal va~Tves with modular actuators;
(d) air flow passages in the die tip providing simplified construction; and (e) an air heater connected to the die.

Claims

CLAIMS:

1. A method of depositing a hot melt adhesive onto a substrate which comprises:
(a) passing a substrate under a meltblowing die having a plurality of side-by-side units extending in a row transversely of the direction of substrate movement, each unit having (i) an elongate die tip adapted to discharge a row of adhesive filaments therefrom, (ii) converging air slits for delivering converging sheets of air to opposite sides of the row of filaments, (iii) a valve for closing flow through the die tip, and (iv) a valve actuator for opening and closing the valve;
(b) delivering the hot melt adhesive to each unit; and (c) while passing the substrate under the meltblowing die, selectively actuating the valve actuators in a predetermined order to permit flow through the die tip and to discharge the row of filaments of the adhesive from each unit, with the valve actuators actuated, into the converging sheets of air which deposits the filaments onto the substrate as a thin, uniform coating spanning the length of the unit, and to stop flow of adhesive through the units with the valves thereof closed, whereby a preselected pattern of the adhesive coating is formed on the substrate.

2. A method of applying a hot melt adhesive coating in the shape of a diaper onto backsheets, which comprises:
(a) passing a backsheet continuously under a meltblowing die provided with a plurality of melt blowing units arranged in side-by-side relationship, each unit having (i) an elongate die tip provided with a plurality of orifices arranged in a row and positioned transversely with respect to the direction of backsheet movement, (ii) elongate air plates flanking the row of orifices for delivering converging sheets of air onto each side of the orifices, and (iii) a valve for interrupting flow of adhesives therethrough;
(b) sequentially meltblowing the hot melt adhesive onto the substrate as follows:

(i) meltblowing a polymer from selected units in the row onto the backsheet moving thereunder to form an adhesive coating for a predetermined length of movement by opening the valves thereof whereby adhesive is discharged from the row of orifices as a row of filaments into the converging sheets of air and are randomly deposited on a portion of the backsheet opposite the selected units as a thin coating, (ii) discontinuing meltblowing of polymer from the selected units located at opposite ends of the row of units while continuing meltblowing from the remaining selected central units in the row to leave leg cutout areas uncoated and central portion coated for a predetermined length, (iii) resuming meltblowing from all the selected units to provide coating of the backsheet to full width defined by the selected units; and (c) repeating steps (b) (i)-(iii) to produce a series of diaper shaped coatings on the backsheet.

3. The method of claim 2 wherein each unit of the meltblowing die has from 10 to 50 orifices per inch whereby the steps (b) and (c) deposits adhesive onto the backsheet from to 50 orifices of each of the selected units.

4. A method of applying hot melt adhesive onto a substrate, which comprises:
(a) passing the substrate under a meltblowing die having a plurality of side-by-side units extending in a row transversely across the substrate, each unit having (i) an elongate die tip shaped to discharge a row of filaments therefrom, (ii) air slits flanking the die tip for discharging converging sheets of air on each side of the row of filaments, and (iii) a valve for interrupting flow of adhesive therethrough;
(b) sequentially meltblowing adhesive from each meltblowing unit as follows:
(i) meltblowing the adhesive from selected units by opening valves of the selected units whereby adhesive filaments discharge from the die tips of the selected units into the converging sheets of air and are blown onto the substrate as a thin coating across the substrate underlaying the selected units; and (ii) discontinuing adhesive flow through one or more of the selected units by closing the valve thereof while continuing the flow of adhesive through the other selected units whereby the adhesive is deposited on the substrate in a preselected pattern.

5. The method of Claim 4 wherein the die tip discharges from 10 to 50 filaments per inch of each unit.

6. A method of depositing an adhesive onto a substrate which comprises (a) passing a substrate under a segmented meltblowing die having a plurality of side-by-side units extending in a row transverse the direction of substrate moving;
(b) meltblowing adhesives from selected units by discharging from 10 to 50 filaments from each unit into converging air sheets which attenuate the filaments and deposit them as a thin coating onto the moving substrate opposite the selected units;
(c) following step (b) discontinuing the meltblowing of adhesive from one or more of the selected units while continuing the meltblowing from at least one of the selected units by discharging from 10 to 50 filaments from at least one of the selected units into converging air sheets which attenuates the filaments and deposits them as a thin coating onto the substrate opposite at least one unit whereby a preselected pattern of adhesives is deposited on the substrate.