US3851023A - Process for forming a web - Google Patents

Process for forming a web Download PDF

Info

Publication number
US3851023A
US3851023A US00303044A US30304472A US3851023A US 3851023 A US3851023 A US 3851023A US 00303044 A US00303044 A US 00303044A US 30304472 A US30304472 A US 30304472A US 3851023 A US3851023 A US 3851023A
Authority
US
United States
Prior art keywords
web
baffle
shield
radial directions
location
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US00303044A
Inventor
D Brethauer
J Prideaux
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US00303044A priority Critical patent/US3851023A/en
Priority to US447253A priority patent/US3860369A/en
Application granted granted Critical
Publication of US3851023A publication Critical patent/US3851023A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04HMAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
    • D04H3/00Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
    • D04H3/08Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating
    • D04H3/16Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of strengthening or consolidating with bonds between thermoplastic filaments produced in association with filament formation, e.g. immediately following extrusion
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/11Flash-spinning

Definitions

  • An improved apparatus for use in making nonwoven fibrous sheets of organic synthetic polymers includes a spinneret orifice through which a polymer solution is flash spun to form a plexifilamentary strand directed in a generally horizontal direction toward a rotating 'bafiie whose axis of rotation is generally parallel to but spaced from the axis of the extrusion orifice and whose surface is contoured so as to simultaneously spread said strand into a planar web, direct the web into a generally vertical plane downward toward a collecting surface, and cause said web to oscillate in the plane as the baffle rotates.
  • the improvement consists of an aerodynamic shield of specified configuration.
  • the shield terminates at an edge which lies substantially along an arc of a circle whose center lies on the axis of rotation of the baflie. Since the plexifilamentary' strand impinges on the bafiie at a point near its axis of rotation and is deflected as a web which therefore oscillates through various radial directions within the plane substantially perpendicular to the rotation axis, only the specified shield configuration will provide flow paths of approximately equal impedance, independent of the instantaneous radial direction at which the web leaves the baffle.
  • This invention relates to a process and apparatus used in the preparation of nonwoven fibrous sheets of synthetic organic polymers. More particularly, it is directed to a process and apparatus for spreading a plexifllamentary strand into a planar web, directing the web toward a surface, charging the web and collecting the web in the form of a nonwoven fibrous swath.
  • the three-dimensional network is spread into a wide web by causing it to be swept along a smooth path past a curved surface baflie whereupon the expanding solvent gas spreads the material.
  • the web can be directed to various areas across the width of a moving collecting belt where it is deposited in the form of swaths.
  • the web can be electrostatically charged to both further increase its width through mutual electrostatic repulsion between fibrils and also attract the swath to the belt and immobilize the deposit. A fibrous nonwoven sheet is thereby obtained.
  • the oscillating baflle can be replaced by a rotating baffle, having specially contoured surfaces, which simultaneously spreads and oscillates the web as it is directed through an electrostatic device to apply uniform electrostatic charge on the web and promote uniform deposition of the web on a moving collecting surface.
  • a suitable charging apparatus is described in Kilby and Smith, US. Pat. No. 3,456,156.
  • the apparatus consists of an annular disc target electrode which is concentric with the rotating baflle and rotates independently of said bafiie.
  • a multineedle ion gun is positioned opposite the target plate, the needles being aimed at a portion of the target electrode to provide a corona discharge zone.
  • the fibrous material moving in a planar path between the target electrode and the ion gun needles is electrostatically charged before being deposited on the moving collecting surface.
  • An apparatus for forming a fibrous web that includes means for flash spinning a polymer solution to form a plexifilamentary strand entrained in a gaseous stream, means at one location (e.g., a rotating baflle) for spreading the strand to form a web and oscillating the web in a generally vertical plane in a plurality of downward radial directions toward a collecting surface and means positioned below said spreading and oscillating means for charging said web.
  • the improvement comprises an aerodynamic shield having front and rear members disposed on each side of said plane below said spreading and oscillating means.
  • the members have surfaces facing said plane, said surfaces terminate in edges equispaced from each other that lie along arcs of equal radius extending from a horizontal axis proximate to said one location.
  • the surface of the rear member facing said plane is substantialy parallel thereto and is a stepped surface, stepped away from said plane in the downward direction along one or more arcs concentric with the terminating edge of the rear member.
  • the surface of the front member facing said plane is a section of a surface of revolution about said horizontal axis that converges downwardly toward said plane.
  • the surface of the front member facing the vertical plane preferably is a segment of a right circular cone converging downwardly toward said plane at an angle of about degrees.
  • the front and rear members extend downward for a distance of from about 30 percent to about 60 percent of the distance from said one location to said collecting surface.
  • the invention concerns an improved process that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal path toward one location, directing and oscillating said web and said stream from said one location in a plurality of downward radial directions in a substantially vertical plane through ambient gas toward a collecting means, and collecting said web on said collecting means as a fibrous sheet, the improvement comprising: converging said stream in said downward radial directions within a shield presenting substantially equal flow impedances in said radial directions.
  • the process may include the step of aspirating said ambient gas into said shield generally in said downward radial directions.
  • the primary function of the shield is not to diffuse the gas stream but rather to protect it and the entrained web as shaped by the rotating baffle and prevent premature mixing with the ambient gas.
  • the exit gap 'width between front and rear shield members is selected such that there is neutral gas pressure on the members, i.e., the average internal and external gas pressures are equal.
  • the actual gap width required is, of course, a function of the rate of gas generation by flash vaporization, the quantity of gas entrained and aspirated into the shield, the dimensions of the shield, etc. However, under any given set of spinning conditions the required gap width is readily determined by the neutral pressure condition.
  • FIG. 1 is a cross-sectional elevation indicating schematically the arrangement of various elements of an apparatus which can be used in the practice of the invention.
  • FIG. 2 is a more detailed cross-sectional view of a portion of a preferred embodiment of the aerodynamic shield of the present invention.
  • FIG. 3 is a view of the web facing surface of the front shield member of FIG. 2.
  • FIG. 4 is a graph presentation of data showing the improved machine direction sheet uniformity provided by the apparatus and process of the present invention.
  • a spinneret device 1 is shown connected to a polymer solution supply source.
  • Polymer solution 2 under pressure is fed through an orifice 3 into intermediate pressure or letdown pressure zone 4 and then through spinning orifice 5 into web forming chamber 6.
  • the extrudate from spinning orifice 5 is a plexifilamentary strand 7.
  • baffle 8 Due to the pressure drop at spinning orifice 5 and the high temperature of the spinning solution, vaporization of solvent creates a vapor blast which, by passage along the surface of baffle 8 concomitantly with plexifilament 7, generally follows the path of advance from spinning orifice 5 to collecting surface 9, thereby creating a flow pattern within chamber 6 as indicated by the ar rows in FIG. 1.
  • Baffle 8 is mounted on shaft 10 which is mounted in bearing 11 and is rotated by means not shown.
  • the surface of bafile 8 is so contoured that the plexifilamentary strand 7 issuing from orifice 5 is deflected into a generally vertical plane and simultaneously spread laterally to form a plexifilamentary web 21 which oscillates from side-to-side as baffle 8 is rotated.
  • the plexifilamentary web 21 passes from bafile 8 directly into the aerodynamic shield of this invention.
  • the shield is comprised of front member 18 and a rear member comprising elements 13 and 17.
  • Multineedle ion gun 14- is mounted on the interior surface of front member 18, and is connected to constant current power source 35 which supplies a potential of approximately 50-60 kilovolts.
  • a corona discharge occurs between needles 14 and target plate 13 which is disposed so that the vapor blast originating at 5 and deflected by bafile 8 carries the plexifilament web along its charging surface.
  • Target plate 13 is connected via commutating ring and brushes to ground by wire 15 and microammeter 16 which indicates target plate current.
  • Target plate 13 is an annular metal disc electrode, and is preferably covered with a dielectric insulating surface as disclosed in US. Pat. No. 3,578,739.
  • Target plate 13 together with concentric annular segment 17 comprise the rear member of the aerodynamic shield, and are adapted to be rotated concentrically with, but independent of, bafiie S by means not shown.
  • its interior surface passes by rotating brush 20, driven by means not shown, so that the surface of target plate 13 and adjacent parts may be cleared of any debris, thereby furnishing a continuously cleaned surface for optimum operation of the corona discharge.
  • the rear shield member is pierced by ports 19 through which ambient gas may be aspirated into the step region between concentric disc segments 13 and 17.
  • plexifilament web 21 is deposited upon a collecting surface 9.
  • the surface illustrated is a continuous electrically conductive belt forwarded by drive roll 36.
  • the belt may either be grounded or charged to a positive or negative potential by power source 37. Due to differences in their electrostatic charge, the plexifilament web 21 is attracted to surface 9 and clings to it in its arranged condition as a swath 38 with sufficient force to overcome the disruptive influences of whatever vapor blast may reach this area. Since high rates of production can generate high turbulence in chamber 6, auxiliary corona devices 43 stationed just above the surface of belt 9 may be employed to place even higher electrostatic charge on swath 38, thereby pinning it even more tightly to belt 9.
  • Wide sheets are produced by blending and overlapping the output from several spinning positions placed in an appropriate manner across the width of a receiving surface such as the belt '9.
  • the degree of uniformity of the web deposits tends to increase as the aerodynamic shield is extended to protect a greater fraction of the vertical distance from the baffle to the receiving surface.
  • the web fibril orientation is biased too heavily in the cross machine direction.
  • too extensive a shield can lead to nonuniform deposits and hang-up due to electrostatic attraction and erratic clinging of the charged web to the internal shield surfaces.
  • Applicants have discovered that a preferred balance in sheet uniformity and fibril directionality is attained when the aerodynamic shield extends over about 30-60% of the vertical distance from the edge of the baffle to the collecting surface.
  • the sheet is then lightly compacted by roll 41 and is collected on windup roll 42 after passing through port 39 and flexible elements (or rolls) 40 which assist in retention of vapor within chamber 6.
  • a conventional solvent recovery unit 44 may be beneficially employed to improve economic operation.
  • FIG. 2 is an enlarged cross-sectional view of a portion of the aerodynamic shield depicted in FIG. 1.
  • Front member 18 is constructed of Lucite (trademark for Du Pont acrylic resin), its exit lip 22 lies along a semicircle centered on rotating baffle axis 23 and the angle of convergence 24 is 5.
  • Multineedle corona charging electrode 14 consists of 17 needles smoothly graduated in length, spaced at intervals along conductor 25 to provide a varying needle-to-needle target spacing. The needle electrode is recessed in channel 31 cut into the web facing surface of front member 18.
  • the needles lie along an arc of a circle centered on axis 23, and the angle subtended by the end needles as viewed from the center of the circle is 140, which is sufiicient to overlap the plexifilamentary web envelope throughout its period of oscillation. (The angle subtended by channel 31, viewed from the center of the circle is 166.)
  • the 17 needles pass through a curved strip of Lexan 26 whose width is tapered to allow each needle point to protrude the same distance.
  • This strip thus bridges the gap between adjacent needles and prevents plexifilamentary debris from building up from the base of the individual needles during spinning, which debris could alter the shape and intensity of the electrical field and thereby lead to nonuniform corona generation and consequent erratic web charging and sheet nonuniformities.
  • the rear shield member is comprised of metallic annular target plate 13, covered by a dielectric surface 27 having a volume resistivity between l0 and 1 10 ohm centimeters, and annular target plate extension 28 constructed of Lucite plus concentric annular segment 17, also constructed of Lucite.
  • These rear shield members elements are assembled by means of annular Lexan (General Electrics polycarbonate resin) support member 30 and thereby adapted to be rotated as a unit about axis 23, i.e., concentrically with baffle 8. (Baffle 8 is rotated at much higher speeds than the rear shield unit.)
  • the step height between elements 28 and 17 is designated 19a, and support member 30 is perforated at intervals by aspiration ports 19.
  • the provision of access ports in the rear member near the step permits a suitable quantity of ambient gas to be aspirated into the aerodynamic shield to form a protective cushion of gas which flows toward the exit lip along the internal surface of the rear member.
  • FIG. 3 is a view of the web facing surface of front shield member 18 showing the needle electrode unit 14, channel 31, Lexan strip 26, and also indicating support members 29a and 2%.
  • Front shield member 18 is suspended from pivot points (not shown) inside members 29a and 2%, both located on a common horizontal axis, which thus permits front shield member 18 to swing farther away from the rear shield member momentarily whenever a mass of plexifilarnentary material may begin to plug the shield passageway.
  • metal spring elements (not shown) urging front member 18 back intonormal operating position as soon as the plug mass is expelled.
  • Adjustable stops are provided such that the normal exit gap width 220.
  • the specific neutral pressure gap width may be established during spinning, for example, by temporarily releasing the front member from the spring biasing means and allowing it to swing free on its pivots and seek a position such that pressure on the web side (or inside) is in balance with the ambient gas pressure on the opposite side (outside). Of course, appropriate allowance or correction may need to be made should the center of gravity of the front shield member not lie directly beneath the pivot points. As may be noted from FIGS.
  • the entrance edge of front member 18 has a configuration approximating a section of a toroid, thus surrounding a portion of baffle 8 and extending backward to a point close to the spinneret housing in order to restrict entrainment of ambient gas while still providing suflicient clearance for the occasional swinging motion required to relieve adventitious plugs.
  • the web facing surface of the front member of the aerodynamic shield must satisfy two requirements: (1) it should present approximately equal gas flow impedance at all radial directions at which the web may leave the rotary baffle in the vertical plane, and (2) the spacing between confronting surfaces of front and rear members should decrease on the average as the web moves radially through the shield from entrance to exit.
  • This decreasing separation between shield members partially compensates for the increase in width of the gas stream as it flows along diverging radial directions within the vertical plane as directed by the contoured surface of the rotating baffie, and thereby keeps the cross-sectional area of the gas stream taken at right angles to its direction of flow from increasing so rapidly that excessive deceleration and sticking of the web to the shield can occur.
  • the equal impedance criterion is met by a front shield member whose web facing surface is a section of a surface of revolution about the rotation axis of the battle; and since the rear member's surface is approximately flat (apart from the annular steps), the convergence criterion can simultaneously be satisfied most simply by choosing the surface of the front member to be a segment of a right circular cone.
  • the optimum angle of convergence i.e., the angle between the vertical and a straight line tangent to the web-facing surface of the front member at two points proximate its entrance and exit edges, respectively, measured on a vertical cross section perpendicular to the web oscillation plane
  • the optimum angle of convergence is a function of the detailed contour of the baffle surface, the number and size of the steps in the rear shield member, etc.
  • PERCENT CV OF BASIS WEIGHT UNIFORMITY A sheet of material about 500 inches long and at least 8 inches wide is used. Eighty l-inch diameter circles are cut from the sheet along each of three rows, the centercenter distances of these circles being about 3 inches in the width direction of the sheet and 6 inches in the length direction. The coeflicient of variation (percent CV) of the weights of these 1 inch circles in each row is calculated and the average percent CV for the three rows is used as a measure of the sheet uniformity.
  • Linear polyethylene having a density of 0.95 g./cc. and a melt fiow rate of 0.9 gram/ 10 minutes as determined by ASTM method D123857T, condition E, is flash spun from a hot trichlorofluorornethane solution.
  • the solution is continuously pumped to the spinneret assembly under high pressure.
  • the solution then passes into a small chamber through a first orifice to reduce the pressure to the desired value for flash spinning, and is then immediately extruded into a region at substantially atmospheric pressure through a second (spin) orifice.
  • Initial flash vaporization occurs inside a short cylindrical tunnel immediately downstream and coaxial with the spin orifice, which serves to shape the resulting high velocity gas and entrained strand,
  • the resulting plexifilamentary strand passes along the surface of a rotating baffle which simultaneously spreads it, imparts lateral oscillation and directs it vertically downwards through a corona charging zone between a multineedle corona discharge electrode and a grounded 7 target plate toward a moving belt, where it is collected in overlapping layers.
  • the sheet is then lightly consolidated by passage between a pair of rolls under a pressure of 8. of less variable swath width from run-torun and day-today, and substantially decreases sensitivity to other process variables such as equipment alignment, web charge, etc.
  • Set A is prepared employing the aerodynamic shield of the present invention, using the preferred embodiment detailed in FIGS. 2 and 3, and having exit and entrance radii of 9 /2 and 2% inches, respectively, with a step height of inch.
  • set B is prepared employing the best available prior art apparatus, namely, the scoop diffuser disclosed in US. Pat. No. 3,593,074 and in particular the embodiment described in Example 4 of the patout.
  • the optimum available bafile designs are employed, together with the appropriate bailleto-belt distance required to obtain a :2' /2 inch swath Width for the plexifilamentary deposits on the belt.
  • a process for forming fibrous sheets that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal-path toward one location on a bafile, directing and oscillating said Web and said stream from said one location in a plurality of downward radial directions in a substantially vertical plane through ambient gas toward a collecting means, electrostatically charging the 'web, and collecting said Web on said collecting means as a fibrous sheet, the improvement comprising: c0nverging said stream below said bafile in said downward radial directions within a shield presenting substantially equal tflOW impedances in said radial directions for a distance of from 30 to 60 percent of the distance from said one location to said collecting means thereby maintaining the stream entrained web substantially as formed by said bafile and preventing premature mixing with said ambient gas.

Abstract

1.In a process for forming fibrous sheets that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal path toward one location on a baffle, directing and oscillating said web and aid stream from said one location in a plurality of downward radial directions in a vertical plane through ambient gas toward a collecting means, electrostatically charging the web, and collecting said web on said collecting means as a fibrous sheet, the improvement comprising: converging said stream below said steam below said baffle in said downward radial directions within a shield presenting substantially equal flow impedances in said radial directions for a distance of from 30 to 60 percent of the distance from said one location to said collecting means thereby maintaining the steam entrained web substantially as formed by said baffle and preventing premature with said ambient gas.

Description

N07. 26, 1974 MBRETHAUER ETAL 3,851,023
PROCESS FOR FORMING A WEB Filed .Nov 2, 1972 l 3 Sheets-Sheet 1 20 TO SOLVENT F I G- v fly g RECOVERY :0 s 5 A I x 7 POLYMER t SOLUTIONI I 3 -"I"m S U P PLY I5 I9 :34 ST PO I'VE l7 OR /35 ,l NEGATIVE 0c 16 SOURCE l 7 GROUNDED M6 35 SOURCE 40 E 38 9/ i /39 42 k $40 F I G- 3 7 29b Nov. 26, 1974 o. M. BRETHAUER ETAL 3,851,023
PROCESS FOR FORMING A WEB 3 Sheets-Sheet 2 Filed Nov. 2, 1972 NOV. 26, 1974 BRETHAUER I ET AL 3,851,023
PROCESS FOR FORMING A WEB Filed Nov. 2, 1972 3 Sheets-Sheet 3 FIG. 4
IZO-
II.O-
i SETS 75pph (scoo 2 [I O L: 9.0- 2 O '5 U SET A IOOpph (AERODYNAMIC SHIELD) 6'0 I l 1 l 0.8 L0 1.2 L4 L6 1.8 2.0 2.2
SHEET BASIS WEIGHT United States Patent O U.S. Cl. 264-24 3 Claims ABSTRACT OF THE DISCLOSURE An improved apparatus for use in making nonwoven fibrous sheets of organic synthetic polymers includes a spinneret orifice through which a polymer solution is flash spun to form a plexifilamentary strand directed in a generally horizontal direction toward a rotating 'bafiie whose axis of rotation is generally parallel to but spaced from the axis of the extrusion orifice and whose surface is contoured so as to simultaneously spread said strand into a planar web, direct the web into a generally vertical plane downward toward a collecting surface, and cause said web to oscillate in the plane as the baffle rotates. The improvement consists of an aerodynamic shield of specified configuration.
The shield terminates at an edge which lies substantially along an arc of a circle whose center lies on the axis of rotation of the baflie. Since the plexifilamentary' strand impinges on the bafiie at a point near its axis of rotation and is deflected as a web which therefore oscillates through various radial directions within the plane substantially perpendicular to the rotation axis, only the specified shield configuration will provide flow paths of approximately equal impedance, independent of the instantaneous radial direction at which the web leaves the baffle.
BACKGROUND OF THE INVENTION This invention relates to a process and apparatus used in the preparation of nonwoven fibrous sheets of synthetic organic polymers. More particularly, it is directed to a process and apparatus for spreading a plexifllamentary strand into a planar web, directing the web toward a surface, charging the web and collecting the web in the form of a nonwoven fibrous swath.
Steuber, US. Pat. No. 3,169,899 describes a process for making a nonwoven sheet from flash-spun fibrous materials. In the flash spinning technique, a solution of an organic polymer which is under pressure and at a temperature far above the boiling point of the solvent is extruded into an area of substantially atmospheric pressure. As the material issues from the orifice, the solvent flash evaporates and a plexifilamentary strand is formed. The plexifilmentary strand is composed of very thin film fibril elements which are interconnected in a three-dimensional network as described in detail in Blades and White, U .8. Pat. No. 3,081,519. The three-dimensional network is spread into a wide web by causing it to be swept along a smooth path past a curved surface baflie whereupon the expanding solvent gas spreads the material. By oscillating the deflecting baflie, the web can be directed to various areas across the width of a moving collecting belt where it is deposited in the form of swaths. The web can be electrostatically charged to both further increase its width through mutual electrostatic repulsion between fibrils and also attract the swath to the belt and immobilize the deposit. A fibrous nonwoven sheet is thereby obtained.
In an alternative process described in Pollock and Smith, US. Pat. No. 3,497,918, the oscillating baflle can be replaced by a rotating baffle, having specially contoured surfaces, which simultaneously spreads and oscillates the web as it is directed through an electrostatic device to apply uniform electrostatic charge on the web and promote uniform deposition of the web on a moving collecting surface. A suitable charging apparatus is described in Kilby and Smith, US. Pat. No. 3,456,156. The apparatus consists of an annular disc target electrode which is concentric with the rotating baflle and rotates independently of said bafiie. A multineedle ion gun is positioned opposite the target plate, the needles being aimed at a portion of the target electrode to provide a corona discharge zone. The fibrous material moving in a planar path between the target electrode and the ion gun needles is electrostatically charged before being deposited on the moving collecting surface.
A number of requirements must be satisfied in order to obtain wide, fibrous, nonwoven sheets having a uniform appearance and a uniform basis weight. In general, wide nonwovens are obtained by blending and overlapping the swaths from several spinning positions. Smith, US. Pat. No. 3,549,453, describes a mechanism for making fine adjustments and varying the weight distribution of the swaths deposited on the collection surface. Tests have shown that optimum basis weight uniformity in the cross machine direction (i.e., the direction at right angles to the direction of movement of the receiving surface) is obtained when the width of the swaths at this surface is within certain limits which depend on the shape of the cross machine direction basis weight profile of each swath. This width is a function of the amplitude of the oscillation imparted to the web by the baflie, the amount of electrostatic charge on the web and the distance between the baffle and the receiving surface.
Isakoff, US. Pat. No. 3,593,074, describes a short diffuser device, termed a scoop, which squeezes the gaseous stream to increase its width, thereby also increasing the width of the entrained web. This scoop is situated between the baflle and the corona charging station, and leads to improvements in sheet uniformity by permitting shorter baflle-to-receiving surface distances for a given swath width. However, as spinning throughputs are increased, the larger volumes and velocities of gas produced in the flash spinning operation create an undesirable increase in turbulence. This increases the random oscillation of the web producing a nonwoven sheet having less than the desired uniformity.
SUMMARY OF THE INVENTION An apparatus is provided for forming a fibrous web that includes means for flash spinning a polymer solution to form a plexifilamentary strand entrained in a gaseous stream, means at one location (e.g., a rotating baflle) for spreading the strand to form a web and oscillating the web in a generally vertical plane in a plurality of downward radial directions toward a collecting surface and means positioned below said spreading and oscillating means for charging said web. The improvement comprises an aerodynamic shield having front and rear members disposed on each side of said plane below said spreading and oscillating means. The members have surfaces facing said plane, said surfaces terminate in edges equispaced from each other that lie along arcs of equal radius extending from a horizontal axis proximate to said one location. The surface of the rear member facing said plane is substantialy parallel thereto and is a stepped surface, stepped away from said plane in the downward direction along one or more arcs concentric with the terminating edge of the rear member. The surface of the front member facing said plane is a section of a surface of revolution about said horizontal axis that converges downwardly toward said plane.
The surface of the front member facing the vertical plane preferably is a segment of a right circular cone converging downwardly toward said plane at an angle of about degrees.
' The front and rear members extend downward for a distance of from about 30 percent to about 60 percent of the distance from said one location to said collecting surface.
There are ports in said rear member at the location the surface of the rear member facing the vertical plane is stepped away from said plane.
The invention concerns an improved process that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal path toward one location, directing and oscillating said web and said stream from said one location in a plurality of downward radial directions in a substantially vertical plane through ambient gas toward a collecting means, and collecting said web on said collecting means as a fibrous sheet, the improvement comprising: converging said stream in said downward radial directions within a shield presenting substantially equal flow impedances in said radial directions. The process may include the step of aspirating said ambient gas into said shield generally in said downward radial directions.
Although some web deceleration can be tolerated within the aerodynamic shield of this invention, the primary function of the shield is not to diffuse the gas stream but rather to protect it and the entrained web as shaped by the rotating baffle and prevent premature mixing with the ambient gas. Accordingly, the exit gap 'width between front and rear shield members is selected such that there is neutral gas pressure on the members, i.e., the average internal and external gas pressures are equal. The actual gap width required is, of course, a function of the rate of gas generation by flash vaporization, the quantity of gas entrained and aspirated into the shield, the dimensions of the shield, etc. However, under any given set of spinning conditions the required gap width is readily determined by the neutral pressure condition.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cross-sectional elevation indicating schematically the arrangement of various elements of an apparatus which can be used in the practice of the invention.
FIG. 2 is a more detailed cross-sectional view of a portion of a preferred embodiment of the aerodynamic shield of the present invention.
FIG. 3 is a view of the web facing surface of the front shield member of FIG. 2.
FIG. 4 is a graph presentation of data showing the improved machine direction sheet uniformity provided by the apparatus and process of the present invention.
DETAILED DESCRIPTION OF THE ILLUSTRATED EMBODIMENTS Referring to FIG. 1, a spinneret device 1 is shown connected to a polymer solution supply source. Polymer solution 2 under pressure is fed through an orifice 3 into intermediate pressure or letdown pressure zone 4 and then through spinning orifice 5 into web forming chamber 6. The extrudate from spinning orifice 5 is a plexifilamentary strand 7. Due to the pressure drop at spinning orifice 5 and the high temperature of the spinning solution, vaporization of solvent creates a vapor blast which, by passage along the surface of baffle 8 concomitantly with plexifilament 7, generally follows the path of advance from spinning orifice 5 to collecting surface 9, thereby creating a flow pattern within chamber 6 as indicated by the ar rows in FIG. 1. Baffle 8 is mounted on shaft 10 which is mounted in bearing 11 and is rotated by means not shown. The surface of bafile 8 is so contoured that the plexifilamentary strand 7 issuing from orifice 5 is deflected into a generally vertical plane and simultaneously spread laterally to form a plexifilamentary web 21 which oscillates from side-to-side as baffle 8 is rotated.
The plexifilamentary web 21 passes from bafile 8 directly into the aerodynamic shield of this invention. The shield is comprised of front member 18 and a rear member comprising elements 13 and 17. Multineedle ion gun 14- is mounted on the interior surface of front member 18, and is connected to constant current power source 35 which supplies a potential of approximately 50-60 kilovolts. A corona discharge occurs between needles 14 and target plate 13 which is disposed so that the vapor blast originating at 5 and deflected by bafile 8 carries the plexifilament web along its charging surface. Target plate 13 is connected via commutating ring and brushes to ground by wire 15 and microammeter 16 which indicates target plate current.
Target plate 13 is an annular metal disc electrode, and is preferably covered with a dielectric insulating surface as disclosed in US. Pat. No. 3,578,739. Target plate 13 together with concentric annular segment 17 comprise the rear member of the aerodynamic shield, and are adapted to be rotated concentrically with, but independent of, bafiie S by means not shown. During rotation of the rear member, its interior surface passes by rotating brush 20, driven by means not shown, so that the surface of target plate 13 and adjacent parts may be cleared of any debris, thereby furnishing a continuously cleaned surface for optimum operation of the corona discharge. At intervals, in a circular pattern, the rear shield member is pierced by ports 19 through which ambient gas may be aspirated into the step region between concentric disc segments 13 and 17.
After exiting the aerodynamic shield, plexifilament web 21 is deposited upon a collecting surface 9. The surface illustrated is a continuous electrically conductive belt forwarded by drive roll 36. The belt may either be grounded or charged to a positive or negative potential by power source 37. Due to differences in their electrostatic charge, the plexifilament web 21 is attracted to surface 9 and clings to it in its arranged condition as a swath 38 with sufficient force to overcome the disruptive influences of whatever vapor blast may reach this area. Since high rates of production can generate high turbulence in chamber 6, auxiliary corona devices 43 stationed just above the surface of belt 9 may be employed to place even higher electrostatic charge on swath 38, thereby pinning it even more tightly to belt 9. Wide sheets are produced by blending and overlapping the output from several spinning positions placed in an appropriate manner across the width of a receiving surface such as the belt '9. The degree of uniformity of the web deposits tends to increase as the aerodynamic shield is extended to protect a greater fraction of the vertical distance from the baffle to the receiving surface. However, unless some free-fall is permitted, the web fibril orientation is biased too heavily in the cross machine direction. Furthermore, too extensive a shield can lead to nonuniform deposits and hang-up due to electrostatic attraction and erratic clinging of the charged web to the internal shield surfaces. Applicants have discovered that a preferred balance in sheet uniformity and fibril directionality is attained when the aerodynamic shield extends over about 30-60% of the vertical distance from the edge of the baffle to the collecting surface. The sheet is then lightly compacted by roll 41 and is collected on windup roll 42 after passing through port 39 and flexible elements (or rolls) 40 which assist in retention of vapor within chamber 6. A conventional solvent recovery unit 44 may be beneficially employed to improve economic operation.
FIG. 2 is an enlarged cross-sectional view of a portion of the aerodynamic shield depicted in FIG. 1. Front member 18 is constructed of Lucite (trademark for Du Pont acrylic resin), its exit lip 22 lies along a semicircle centered on rotating baffle axis 23 and the angle of convergence 24 is 5. Multineedle corona charging electrode 14 consists of 17 needles smoothly graduated in length, spaced at intervals along conductor 25 to provide a varying needle-to-needle target spacing. The needle electrode is recessed in channel 31 cut into the web facing surface of front member 18. The needles lie along an arc of a circle centered on axis 23, and the angle subtended by the end needles as viewed from the center of the circle is 140, which is sufiicient to overlap the plexifilamentary web envelope throughout its period of oscillation. (The angle subtended by channel 31, viewed from the center of the circle is 166.) The 17 needles pass through a curved strip of Lexan 26 whose width is tapered to allow each needle point to protrude the same distance. This strip thus bridges the gap between adjacent needles and prevents plexifilamentary debris from building up from the base of the individual needles during spinning, which debris could alter the shape and intensity of the electrical field and thereby lead to nonuniform corona generation and consequent erratic web charging and sheet nonuniformities.
The rear shield member is comprised of metallic annular target plate 13, covered by a dielectric surface 27 having a volume resistivity between l0 and 1 10 ohm centimeters, and annular target plate extension 28 constructed of Lucite plus concentric annular segment 17, also constructed of Lucite. These rear shield members elements are assembled by means of annular Lexan (General Electrics polycarbonate resin) support member 30 and thereby adapted to be rotated as a unit about axis 23, i.e., concentrically with baffle 8. (Baffle 8 is rotated at much higher speeds than the rear shield unit.) The step height between elements 28 and 17 is designated 19a, and support member 30 is perforated at intervals by aspiration ports 19. The provision of access ports in the rear member near the step permits a suitable quantity of ambient gas to be aspirated into the aerodynamic shield to form a protective cushion of gas which flows toward the exit lip along the internal surface of the rear member.
FIG. 3 is a view of the web facing surface of front shield member 18 showing the needle electrode unit 14, channel 31, Lexan strip 26, and also indicating support members 29a and 2%. Front shield member 18 is suspended from pivot points (not shown) inside members 29a and 2%, both located on a common horizontal axis, which thus permits front shield member 18 to swing farther away from the rear shield member momentarily whenever a mass of plexifilarnentary material may begin to plug the shield passageway. Also mounted within members 29a and 29b are metal spring elements (not shown) urging front member 18 back intonormal operating position as soon as the plug mass is expelled. Adjustable stops (not shown) are provided such that the normal exit gap width 220. is set in the range of from to inch, or the value at which no net gas pressure difference exists on front element 18 in a direction parallel to axis 23. The specific neutral pressure gap width may be established during spinning, for example, by temporarily releasing the front member from the spring biasing means and allowing it to swing free on its pivots and seek a position such that pressure on the web side (or inside) is in balance with the ambient gas pressure on the opposite side (outside). Of course, appropriate allowance or correction may need to be made should the center of gravity of the front shield member not lie directly beneath the pivot points. As may be noted from FIGS. 2 and 3, the entrance edge of front member 18 has a configuration approximating a section of a toroid, thus surrounding a portion of baffle 8 and extending backward to a point close to the spinneret housing in order to restrict entrainment of ambient gas while still providing suflicient clearance for the occasional swinging motion required to relieve adventitious plugs.
The web facing surface of the front member of the aerodynamic shield must satisfy two requirements: (1) it should present approximately equal gas flow impedance at all radial directions at which the web may leave the rotary baffle in the vertical plane, and (2) the spacing between confronting surfaces of front and rear members should decrease on the average as the web moves radially through the shield from entrance to exit. This decreasing separation between shield members partially compensates for the increase in width of the gas stream as it flows along diverging radial directions within the vertical plane as directed by the contoured surface of the rotating baffie, and thereby keeps the cross-sectional area of the gas stream taken at right angles to its direction of flow from increasing so rapidly that excessive deceleration and sticking of the web to the shield can occur. The equal impedance criterion is met by a front shield member whose web facing surface is a section of a surface of revolution about the rotation axis of the battle; and since the rear member's surface is approximately flat (apart from the annular steps), the convergence criterion can simultaneously be satisfied most simply by choosing the surface of the front member to be a segment of a right circular cone. The optimum angle of convergence (i.e., the angle between the vertical and a straight line tangent to the web-facing surface of the front member at two points proximate its entrance and exit edges, respectively, measured on a vertical cross section perpendicular to the web oscillation plane) is a function of the detailed contour of the baffle surface, the number and size of the steps in the rear shield member, etc. Fortunately, this convergence angle appears to be not too sensitive to variations in these parameters and a convergence angle of 5 has been found to be generally satisfactory. Various materials, e.g., Lucite, nylon, Teflon (trademark for Du Pont fluoro carbon resin), various filled nylons and Teflons, Nerna G (laminated glass/ epoxy insulating materials), Lexan, etc., can be used for members 17, 18, 26, 28 and 30, if desired.
In order to illustrate the improved uniformity of nonwoven sheets made possible by the present invention, particularly at higher productivities, a series of samples is prepared employing prior art apparatus and compared with a series of samples prepared with the present apparatus, using percent coefficient of variation of basis weight uniformity as the criterion.
PERCENT CV OF BASIS WEIGHT UNIFORMITY A sheet of material about 500 inches long and at least 8 inches wide is used. Eighty l-inch diameter circles are cut from the sheet along each of three rows, the centercenter distances of these circles being about 3 inches in the width direction of the sheet and 6 inches in the length direction. The coeflicient of variation (percent CV) of the weights of these 1 inch circles in each row is calculated and the average percent CV for the three rows is used as a measure of the sheet uniformity.
EXAMPLE Linear polyethylene having a density of 0.95 g./cc. and a melt fiow rate of 0.9 gram/ 10 minutes as determined by ASTM method D123857T, condition E, is flash spun from a hot trichlorofluorornethane solution. The solution is continuously pumped to the spinneret assembly under high pressure. The solution then passes into a small chamber through a first orifice to reduce the pressure to the desired value for flash spinning, and is then immediately extruded into a region at substantially atmospheric pressure through a second (spin) orifice. Initial flash vaporization occurs inside a short cylindrical tunnel immediately downstream and coaxial with the spin orifice, which serves to shape the resulting high velocity gas and entrained strand, The resulting plexifilamentary strand passes along the surface of a rotating baffle which simultaneously spreads it, imparts lateral oscillation and directs it vertically downwards through a corona charging zone between a multineedle corona discharge electrode and a grounded 7 target plate toward a moving belt, where it is collected in overlapping layers. The sheet is then lightly consolidated by passage between a pair of rolls under a pressure of 8. of less variable swath width from run-torun and day-today, and substantially decreases sensitivity to other process variables such as equipment alignment, web charge, etc.
TABLE 1 Set A.Aerodynamic shield, baffle edge to belt=l3% inches, spin rifice=52=i=% mils Solution Flow rate Swath Web charge Cone, Temp, Pres., (p. .h. width (micrecou- Basis wt. Percent; Sample percent; C. p.s.i.g. Tunnel, L/D polymer) (inches) lombs/gm.) (on/yd?) CV Set B.-Scoop, baffle edge to be1t=11% inches, spin orifice=44i2 mils about 45 lb./lineal inch. The speed of the laydown receiver is adjusted incrementally to obtain a set of nonwoven sheet samples of granduated basis weights.
Two sets of plexifilamentary sheet samples are prepared. Set A is prepared employing the aerodynamic shield of the present invention, using the preferred embodiment detailed in FIGS. 2 and 3, and having exit and entrance radii of 9 /2 and 2% inches, respectively, with a step height of inch. For comparison, set B is prepared employing the best available prior art apparatus, namely, the scoop diffuser disclosed in US. Pat. No. 3,593,074 and in particular the embodiment described in Example 4 of the patout. For each set of samples the optimum available bafile designs are employed, together with the appropriate bailleto-belt distance required to obtain a :2' /2 inch swath Width for the plexifilamentary deposits on the belt. In addition, maximum possible sheet uniformity is sought by applying the highest electrostatic charge level to the web which can be tolerated without causing web hangups, disruptive lightening discharges, etc. The specific parameters employed for each sample are listed in Table l. All samples in set A are prepared employing a spin orifice sized to yield a nominal polymer throughput of 100 lbs./ hr., while all samples in set B are prepared with a smaller orifice providing a nominal 75 lbs/hr. of polymer.
The percent coeflicient of variation of basis weight uniformity is determined for the sheet samples within each set, as listed in Table 1, and the data are presented graphically in FIG. 4. Low values of percent CV, corresponding to the greatest degree of uniformit are, of course, preferred. It is apparent on comparing the curves for sample sets A and B, that substantially superior sheet uniformity is provided by the apparatus and process of the present invention, than can be achieved by the best prior art technology. This has been accomplished even at' higher rates of productivity (100 versus 75 lbs/hr.) which, except for the benefits provided by the present invention, otherwise inherently lead to degradation in sheet uniformity. It has also been observed that the apparatus of the present invention provides the further advantages What is claimed is:
1. In a process for forming fibrous sheets that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal-path toward one location on a bafile, directing and oscillating said Web and said stream from said one location in a plurality of downward radial directions in a substantially vertical plane through ambient gas toward a collecting means, electrostatically charging the 'web, and collecting said Web on said collecting means as a fibrous sheet, the improvement comprising: c0nverging said stream below said bafile in said downward radial directions within a shield presenting substantially equal tflOW impedances in said radial directions for a distance of from 30 to 60 percent of the distance from said one location to said collecting means thereby maintaining the stream entrained web substantially as formed by said bafile and preventing premature mixing with said ambient gas.
2. The process as defined in claim 1, including the stepof aspirating said ambient gas into said shield generally in said downward radial directions through holes in said shield.
3. The process as defined in claim 1, the step of electrostatically charging the web being accomplished within-

Claims (1)

1.In a process for forming fibrous sheets that includes the steps of entraining a web in a gaseous stream flowing in a generally horizontal path toward one location on a baffle, directing and oscillating said web and aid stream from said one location in a plurality of downward radial directions in a vertical plane through ambient gas toward a collecting means, electrostatically charging the web, and collecting said web on said collecting means as a fibrous sheet, the improvement comprising: converging said stream below said steam below said baffle in said downward radial directions within a shield presenting substantially equal flow impedances in said radial directions for a distance of from 30 to 60 percent of the distance from said one location to said collecting means thereby maintaining the steam entrained web substantially as formed by said baffle and preventing premature with said ambient gas.
US00303044A 1972-11-02 1972-11-02 Process for forming a web Expired - Lifetime US3851023A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US00303044A US3851023A (en) 1972-11-02 1972-11-02 Process for forming a web
US447253A US3860369A (en) 1972-11-02 1974-03-01 Apparatus for making non-woven fibrous sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US00303044A US3851023A (en) 1972-11-02 1972-11-02 Process for forming a web

Publications (1)

Publication Number Publication Date
US3851023A true US3851023A (en) 1974-11-26

Family

ID=23170305

Family Applications (1)

Application Number Title Priority Date Filing Date
US00303044A Expired - Lifetime US3851023A (en) 1972-11-02 1972-11-02 Process for forming a web

Country Status (1)

Country Link
US (1) US3851023A (en)

Cited By (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3892506A (en) * 1973-06-28 1975-07-01 Fred M Dann Projection forming of three-dimensional metal objects
US3971911A (en) * 1973-06-28 1976-07-27 Dann Fred M Projection forming of three-dimensional metal objects
US5296172A (en) * 1992-07-31 1994-03-22 E. I. Du Pont De Nemours And Company Electrostatic field enhancing process and apparatus for improved web pinning
WO1994023097A1 (en) * 1993-03-26 1994-10-13 E.I. Du Pont De Nemours And Company Process for improving electrostatic charging of plexifilaments
WO1996017117A1 (en) * 1994-12-02 1996-06-06 E.I. Du Pont De Nemours And Company Wand purging for electrostatic charging system in flash spinning process
US5603885A (en) * 1995-07-06 1997-02-18 E. I. Du Pont De Nemours And Company Process for the preparation of nonwoven fibrous sheets
US5672307A (en) * 1996-03-08 1997-09-30 E. I. Du Pont De Nemours And Company Flash spinning process
WO1997041379A1 (en) * 1996-04-30 1997-11-06 E.I. Du Pont De Nemours And Company Lateral entry remotely operated coupling system
WO1997041282A1 (en) * 1996-04-30 1997-11-06 E.I. Du Pont De Nemours And Company Arrangement for sealing a closed production system
US5723084A (en) * 1996-03-08 1998-03-03 E. I. Du Pont De Nemours And Company Flash spinning process
US5833900A (en) * 1995-07-28 1998-11-10 E. I. Du Pont De Nemours And Company Process for modifying porosity in sheet made from flash spinning olefin polymer
US5863639A (en) * 1995-09-13 1999-01-26 E. I. Du Pont De Nemours And Company Nonwoven sheet products made from plexifilamentary film fibril webs
US5874036A (en) * 1996-03-08 1999-02-23 E. I. Du Pont De Nemours And Company Flash-spinning process
US5977237A (en) * 1996-03-08 1999-11-02 E. I. Du Pont De Nemours And Company Flash-spinning solution
US5985196A (en) * 1998-01-20 1999-11-16 E. I. Du Pont De Nemours And Company Flash spinning process and flash spinning solution
US6004672A (en) * 1996-01-11 1999-12-21 E. I. Du Pont De Nemours And Company Fibers flash-spun from blends of polyolefin polymers
US6096421A (en) * 1996-01-11 2000-08-01 E. I. Du Pont De Nemours And Company Plexifilamentary strand of blended polymers
US6136911A (en) * 1996-01-11 2000-10-24 E.I. Du Pont De Nemours And Company Fibers flash-spun from partially fluorinated polymers
US6153134A (en) * 1998-12-15 2000-11-28 E. I. Du Pont De Nemours And Company Flash spinning process
US6218460B1 (en) 1997-01-09 2001-04-17 E. I. Du Pont De Nemours And Company Fibers flash-spun from fully halogenated polymers
US6270709B1 (en) 1998-12-15 2001-08-07 E. I. Du Pont De Nemours And Company Flash spinning polymethylpentene process and product
US20020046656A1 (en) * 2000-09-05 2002-04-25 Benson James D. Filter structure with two or more layers of fine fiber having extended useful service life
US6458304B1 (en) 2000-03-22 2002-10-01 E. I. Du Pont De Nemours And Company Flash spinning process and solutions of polyester
US20030010002A1 (en) * 2000-09-05 2003-01-16 Johnson Bruce A. Mist filtration arrangement utilizing fine fiber layer in contact with media having a pleated construction and floor method
US20030082978A1 (en) * 2001-05-18 2003-05-01 Lim Hyun Sung Dry wipe
US6673136B2 (en) 2000-09-05 2004-01-06 Donaldson Company, Inc. Air filtration arrangements having fluted media constructions and methods
US6716274B2 (en) 2000-09-05 2004-04-06 Donaldson Company, Inc. Air filter assembly for filtering an air stream to remove particulate matter entrained in the stream
US6740142B2 (en) 2000-09-05 2004-05-25 Donaldson Company, Inc. Industrial bag house elements
US6743273B2 (en) 2000-09-05 2004-06-01 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US20040119196A1 (en) * 2002-12-18 2004-06-24 Shin Hyunkook Flash spinning solution and flash spinning process using straight chain hydrofluorocarbon co-solvents
US6800117B2 (en) 2000-09-05 2004-10-05 Donaldson Company, Inc. Filtration arrangement utilizing pleated construction and method
US20040222568A1 (en) * 2003-04-03 2004-11-11 Armantrout Jack Eugene Process for forming uniformly distributed material
US20040226443A1 (en) * 2000-09-05 2004-11-18 Donaldson Company, Inc. Methods for filtering air for a gas turbine system
US20050139505A1 (en) * 2003-12-15 2005-06-30 Miller Mark R. Child-resistant blister package
US20050244639A1 (en) * 2004-04-01 2005-11-03 Marin Robert A Rotary process for forming uniform material
US20060040091A1 (en) * 2004-08-23 2006-02-23 Bletsos Ioannis V Breathable low-emissivity metalized sheets
US20060141084A1 (en) * 2003-04-03 2006-06-29 Armantrout Jack E Rotary process for forming uniform material
US20070037465A1 (en) * 2005-08-11 2007-02-15 Michel Nutz Porous metallized sheets coated with an inorganic layer having low emissivity and high moisture vapor permeability
US20070196610A1 (en) * 2006-02-21 2007-08-23 O'rourke Barbara K Durable metallized self-adhesive laminates
US20070202764A1 (en) * 2005-04-01 2007-08-30 Marin Robert A Rotary process for forming uniform material
US7270693B2 (en) 2000-09-05 2007-09-18 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US7316723B2 (en) 2001-05-31 2008-01-08 Donaldson Company, Inc. Air filter with fine fiber and spun bonded media
US20090075033A1 (en) * 2007-09-14 2009-03-19 Theresa Ann Weston Building wrap for use in external wall assemblies having wet-applied facades
US20090079216A1 (en) * 2007-09-21 2009-03-26 Ryo Kuroda Body assembly of a motor vehicle
US20090158683A1 (en) * 2007-12-20 2009-06-25 Theresa Ann Weston Multiple sheet building wrap for use in external wall assemblies having wet-applied facades
US20090162468A1 (en) * 2006-04-07 2009-06-25 Victor Barinov Controlled Electrospinning of Fibers
WO2010107989A1 (en) 2009-03-18 2010-09-23 E. I. Du Pont De Nemours And Company Metallized animal house curtain
US20100247855A1 (en) * 2004-08-23 2010-09-30 Bletsos Ioannis V Breathable low-emissivity metallized sheets
US20110018174A1 (en) * 2009-07-22 2011-01-27 Adra Smith Baca Electrospinning Process and Apparatus for Aligned Fiber Production
WO2014082014A1 (en) 2012-11-22 2014-05-30 E. I. Du Pont De Nemours And Company Thermally protective cover and method of manufacture thereof
US8741393B2 (en) 2011-12-28 2014-06-03 E I Du Pont De Nemours And Company Method for producing metalized fibrous composite sheet with olefin coating
US8778462B2 (en) 2011-11-10 2014-07-15 E I Du Pont De Nemours And Company Method for producing metalized fibrous composite sheet with olefin coating
US20150053086A1 (en) * 2011-08-15 2015-02-26 E I Du Pont De Nemours And Company Breathable product for protective mass transportation and cold chain applications
WO2016126591A1 (en) 2015-02-02 2016-08-11 E. I. Du Pont De Nemours And Company Root intrusion improvements in irrigation tubes
WO2016160733A1 (en) 2015-04-02 2016-10-06 E I Du Pont De Nemours And Company Dissipative system for safety garments
WO2017200831A1 (en) 2016-05-18 2017-11-23 E I Du Pont De Nemours And Company Composite comprising a nonwoven vapor permeable sheet
US9848543B2 (en) 2013-07-09 2017-12-26 E I Du Pont De Nemours And Company System and method for irrigation
WO2019135206A1 (en) 2018-01-08 2019-07-11 Low & Bonar Inc. Extruded rainscreen
WO2020033029A1 (en) 2018-08-10 2020-02-13 E. I. Du Pont De Nemours And Company Apparatus and method for protectively covering temperature sensitive products
WO2023039366A1 (en) 2021-09-07 2023-03-16 Dupont Safety & Construction, Inc. Hydroponic cultivation system

Cited By (119)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3892506A (en) * 1973-06-28 1975-07-01 Fred M Dann Projection forming of three-dimensional metal objects
US3971911A (en) * 1973-06-28 1976-07-27 Dann Fred M Projection forming of three-dimensional metal objects
US5296172A (en) * 1992-07-31 1994-03-22 E. I. Du Pont De Nemours And Company Electrostatic field enhancing process and apparatus for improved web pinning
WO1994023097A1 (en) * 1993-03-26 1994-10-13 E.I. Du Pont De Nemours And Company Process for improving electrostatic charging of plexifilaments
WO1996017117A1 (en) * 1994-12-02 1996-06-06 E.I. Du Pont De Nemours And Company Wand purging for electrostatic charging system in flash spinning process
US5750152A (en) * 1994-12-02 1998-05-12 E. I. Du Pont De Nemours And Company Wand purging for electrostatic charging system in flash spinning apparatus
US5558830A (en) * 1994-12-02 1996-09-24 E. I. Du Pont De Nemours And Company Wand purging for electrostatic charging system in flash spinning process
US5603885A (en) * 1995-07-06 1997-02-18 E. I. Du Pont De Nemours And Company Process for the preparation of nonwoven fibrous sheets
US5833900A (en) * 1995-07-28 1998-11-10 E. I. Du Pont De Nemours And Company Process for modifying porosity in sheet made from flash spinning olefin polymer
US6070635A (en) * 1995-09-13 2000-06-06 E. I. Du Pont De Nemours And Company Nonwoven sheet products made from plexifilamentary film fibril webs
US5863639A (en) * 1995-09-13 1999-01-26 E. I. Du Pont De Nemours And Company Nonwoven sheet products made from plexifilamentary film fibril webs
US6136911A (en) * 1996-01-11 2000-10-24 E.I. Du Pont De Nemours And Company Fibers flash-spun from partially fluorinated polymers
US6096421A (en) * 1996-01-11 2000-08-01 E. I. Du Pont De Nemours And Company Plexifilamentary strand of blended polymers
US6004672A (en) * 1996-01-11 1999-12-21 E. I. Du Pont De Nemours And Company Fibers flash-spun from blends of polyolefin polymers
US5723084A (en) * 1996-03-08 1998-03-03 E. I. Du Pont De Nemours And Company Flash spinning process
US5672307A (en) * 1996-03-08 1997-09-30 E. I. Du Pont De Nemours And Company Flash spinning process
US5874036A (en) * 1996-03-08 1999-02-23 E. I. Du Pont De Nemours And Company Flash-spinning process
US5925442A (en) * 1996-03-08 1999-07-20 E. I. Du Pont De Nemours And Company Plexifilament and nonwoven made of alternating ethylene/carbon monoxide copolymer
US5977237A (en) * 1996-03-08 1999-11-02 E. I. Du Pont De Nemours And Company Flash-spinning solution
WO1997041379A1 (en) * 1996-04-30 1997-11-06 E.I. Du Pont De Nemours And Company Lateral entry remotely operated coupling system
WO1997041282A1 (en) * 1996-04-30 1997-11-06 E.I. Du Pont De Nemours And Company Arrangement for sealing a closed production system
US6364317B1 (en) 1996-04-30 2002-04-02 E. I. Du Pont De Nemours And Company Arrangement for sealing a closed production system
US6059318A (en) * 1996-04-30 2000-05-09 E. I. Du Pont De Nemours And Company Lateral entry remotely operated coupling system
US6218460B1 (en) 1997-01-09 2001-04-17 E. I. Du Pont De Nemours And Company Fibers flash-spun from fully halogenated polymers
US6303682B1 (en) 1998-01-20 2001-10-16 E. I. Du Pont De Nemours And Company Flash spinning solution
US5985196A (en) * 1998-01-20 1999-11-16 E. I. Du Pont De Nemours And Company Flash spinning process and flash spinning solution
US6162379A (en) * 1998-01-20 2000-12-19 E. I. Du Pont De Nemours And Company Flash spinning process and flash spinning solution
US6270709B1 (en) 1998-12-15 2001-08-07 E. I. Du Pont De Nemours And Company Flash spinning polymethylpentene process and product
US6319970B1 (en) 1998-12-15 2001-11-20 E. I. Du Pont De Nemours And Company Flash spinning process and flash spinning solution with azeotropes
US6352773B2 (en) 1998-12-15 2002-03-05 E. I. Du Pont De Nemours And Company Flash spinning polymethylpentene process and product
US6153134A (en) * 1998-12-15 2000-11-28 E. I. Du Pont De Nemours And Company Flash spinning process
US6692826B2 (en) 2000-03-22 2004-02-17 E. I. Du Pont De Nemours And Company Plexifilamentary strands of polyester
US6458304B1 (en) 2000-03-22 2002-10-01 E. I. Du Pont De Nemours And Company Flash spinning process and solutions of polyester
US20020177649A1 (en) * 2000-03-22 2002-11-28 Hyunkook Shin Solutions for flash spinning of polyester
US7090715B2 (en) 2000-09-05 2006-08-15 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US7090712B2 (en) 2000-09-05 2006-08-15 Donaldson Company, Inc. Air filtration arrangements having fluted media construction and methods
US6673136B2 (en) 2000-09-05 2004-01-06 Donaldson Company, Inc. Air filtration arrangements having fluted media constructions and methods
US20030010002A1 (en) * 2000-09-05 2003-01-16 Johnson Bruce A. Mist filtration arrangement utilizing fine fiber layer in contact with media having a pleated construction and floor method
US6716274B2 (en) 2000-09-05 2004-04-06 Donaldson Company, Inc. Air filter assembly for filtering an air stream to remove particulate matter entrained in the stream
US6740142B2 (en) 2000-09-05 2004-05-25 Donaldson Company, Inc. Industrial bag house elements
US6743273B2 (en) 2000-09-05 2004-06-01 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US6746517B2 (en) 2000-09-05 2004-06-08 Donaldson Company, Inc. Filter structure with two or more layers of fine fiber having extended useful service life
US8029588B2 (en) 2000-09-05 2011-10-04 Donaldson Company, Inc. Fine fiber media layer
US6800117B2 (en) 2000-09-05 2004-10-05 Donaldson Company, Inc. Filtration arrangement utilizing pleated construction and method
US20040200354A1 (en) * 2000-09-05 2004-10-14 Donaldson Company, Inc. Filtration arrangement utilizing pleated construction and method
US8118901B2 (en) 2000-09-05 2012-02-21 Donaldson Company, Inc. Fine fiber media layer
US20040226443A1 (en) * 2000-09-05 2004-11-18 Donaldson Company, Inc. Methods for filtering air for a gas turbine system
US6875256B2 (en) 2000-09-05 2005-04-05 Donaldson Company, Inc. Methods for filtering air for a gas turbine system
US8366797B2 (en) 2000-09-05 2013-02-05 Donaldson Company, Inc. Fine fiber media layer
US6955775B2 (en) 2000-09-05 2005-10-18 Donaldson Company, Inc. Process if making fine fiber material
US8512431B2 (en) 2000-09-05 2013-08-20 Donaldson Company, Inc. Fine fiber media layer
US6974490B2 (en) 2000-09-05 2005-12-13 Donaldson Company, Inc. Air filtration arrangements having fluted media constructions and methods
US6994742B2 (en) 2000-09-05 2006-02-07 Donaldson Company, Inc. Filtration arrangement utilizing pleated construction and method
US10967315B2 (en) 2000-09-05 2021-04-06 Donaldson Company, Inc. Fine fiber media layer
US7318853B2 (en) 2000-09-05 2008-01-15 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US7070640B2 (en) 2000-09-05 2006-07-04 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US7318852B2 (en) 2000-09-05 2008-01-15 Donaldson Company, Inc. Bag house filter with fine fiber and spun bonded media
US7270692B2 (en) 2000-09-05 2007-09-18 Donaldson Company, Inc. Air filtration arrangements having fluted media constructions and methods
US20020046656A1 (en) * 2000-09-05 2002-04-25 Benson James D. Filter structure with two or more layers of fine fiber having extended useful service life
US7115150B2 (en) 2000-09-05 2006-10-03 Donaldson Company, Inc. Mist filtration arrangement utilizing fine fiber layer in contact with media having a pleated construction and floor filter method
US7270693B2 (en) 2000-09-05 2007-09-18 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US10272374B2 (en) 2000-09-05 2019-04-30 Donaldson Company, Inc. Fine fiber media layer
US7179317B2 (en) 2000-09-05 2007-02-20 Donaldson Company, Inc. Polymer, polymer microfiber, polymer nanofiber and applications including filter structures
US9718012B2 (en) 2000-09-05 2017-08-01 Donaldson Company, Inc. Fine fiber media layer
US8709118B2 (en) 2000-09-05 2014-04-29 Donaldson Company, Inc. Fine fiber media layer
US20030082978A1 (en) * 2001-05-18 2003-05-01 Lim Hyun Sung Dry wipe
US7316723B2 (en) 2001-05-31 2008-01-08 Donaldson Company, Inc. Air filter with fine fiber and spun bonded media
US20040119196A1 (en) * 2002-12-18 2004-06-24 Shin Hyunkook Flash spinning solution and flash spinning process using straight chain hydrofluorocarbon co-solvents
US7300968B2 (en) 2002-12-18 2007-11-27 E.I. Du Pont De Nemours And Company Flash spinning solution and flash spinning process using straight chain hydrofluorocarbon co-solvents
US20060154549A1 (en) * 2003-04-03 2006-07-13 Armantrout Jack E Rotary process for forming uniform material
US20060141084A1 (en) * 2003-04-03 2006-06-29 Armantrout Jack E Rotary process for forming uniform material
US7118698B2 (en) 2003-04-03 2006-10-10 E. I. Du Pont De Nemours And Company Rotary process for forming uniform material
US20080284055A1 (en) * 2003-04-03 2008-11-20 Jack Eugene Armantrout Process for forming uniformly distributed material
US20040222568A1 (en) * 2003-04-03 2004-11-11 Armantrout Jack Eugene Process for forming uniformly distributed material
US8114325B2 (en) * 2003-04-03 2012-02-14 E.I. Du Pont De Nemours And Company Process for forming uniformly distributed material
US7786034B2 (en) 2003-04-03 2010-08-31 E.I. Du Pont De Nemours And Company Rotary process for forming uniform material
EP2264230A2 (en) 2003-04-03 2010-12-22 E. I. du Pont de Nemours and Company Rotary process for forming uniform material
US7621731B2 (en) 2003-04-03 2009-11-24 E.I. Du Pont De Nemours And Company Rotary process for forming uniform material
US20050139505A1 (en) * 2003-12-15 2005-06-30 Miller Mark R. Child-resistant blister package
US20050244639A1 (en) * 2004-04-01 2005-11-03 Marin Robert A Rotary process for forming uniform material
US7582240B2 (en) 2004-04-01 2009-09-01 E. I. Du Pont De Nemours And Company Rotary process for forming uniform material
US8431209B2 (en) 2004-08-23 2013-04-30 E I Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US8497010B2 (en) 2004-08-23 2013-07-30 E I Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US20060040091A1 (en) * 2004-08-23 2006-02-23 Bletsos Ioannis V Breathable low-emissivity metalized sheets
US20080060302A1 (en) * 2004-08-23 2008-03-13 E. I. Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US20100247855A1 (en) * 2004-08-23 2010-09-30 Bletsos Ioannis V Breathable low-emissivity metallized sheets
US7805907B2 (en) 2004-08-23 2010-10-05 E.I. Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US8404330B2 (en) 2004-08-23 2013-03-26 E I Du Pont De Nemours And Company Breathable low-emissivity metallized sheets
US20080187740A1 (en) * 2004-08-23 2008-08-07 E. I. Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US20080057292A1 (en) * 2004-08-23 2008-03-06 E. I. Du Pont De Nemours And Company Breathable low-emissivity metalized sheets
US20070202764A1 (en) * 2005-04-01 2007-08-30 Marin Robert A Rotary process for forming uniform material
US8025985B2 (en) 2005-08-11 2011-09-27 E. I. Du Pont De Nemours And Company Porous metallized sheets coated with an inorganic layer having low emissivity and high moisture vapor permeability
US20070037465A1 (en) * 2005-08-11 2007-02-15 Michel Nutz Porous metallized sheets coated with an inorganic layer having low emissivity and high moisture vapor permeability
US7641952B2 (en) 2006-02-21 2010-01-05 E.I. Du Pont De Nemours And Company Durable metallized self-adhesive laminates
US20070196610A1 (en) * 2006-02-21 2007-08-23 O'rourke Barbara K Durable metallized self-adhesive laminates
US8342831B2 (en) 2006-04-07 2013-01-01 Victor Barinov Controlled electrospinning of fibers
US20090162468A1 (en) * 2006-04-07 2009-06-25 Victor Barinov Controlled Electrospinning of Fibers
US20090075033A1 (en) * 2007-09-14 2009-03-19 Theresa Ann Weston Building wrap for use in external wall assemblies having wet-applied facades
US20090079216A1 (en) * 2007-09-21 2009-03-26 Ryo Kuroda Body assembly of a motor vehicle
US20090158683A1 (en) * 2007-12-20 2009-06-25 Theresa Ann Weston Multiple sheet building wrap for use in external wall assemblies having wet-applied facades
WO2010107989A1 (en) 2009-03-18 2010-09-23 E. I. Du Pont De Nemours And Company Metallized animal house curtain
US20100236492A1 (en) * 2009-03-18 2010-09-23 E.I. Du Pont De Nemours And Company Metallized animal house curtain
US20110018174A1 (en) * 2009-07-22 2011-01-27 Adra Smith Baca Electrospinning Process and Apparatus for Aligned Fiber Production
US8211352B2 (en) * 2009-07-22 2012-07-03 Corning Incorporated Electrospinning process for aligned fiber production
US9827529B2 (en) * 2011-08-15 2017-11-28 E I Du Pont De Nemours And Company Breathable product for protective mass transportation and cold chain applications
US20150053086A1 (en) * 2011-08-15 2015-02-26 E I Du Pont De Nemours And Company Breathable product for protective mass transportation and cold chain applications
US8778462B2 (en) 2011-11-10 2014-07-15 E I Du Pont De Nemours And Company Method for producing metalized fibrous composite sheet with olefin coating
US8741393B2 (en) 2011-12-28 2014-06-03 E I Du Pont De Nemours And Company Method for producing metalized fibrous composite sheet with olefin coating
WO2014082014A1 (en) 2012-11-22 2014-05-30 E. I. Du Pont De Nemours And Company Thermally protective cover and method of manufacture thereof
US9848543B2 (en) 2013-07-09 2017-12-26 E I Du Pont De Nemours And Company System and method for irrigation
EP3019000B1 (en) 2013-07-09 2018-12-19 E. I. du Pont de Nemours and Company System and method for irrigation
WO2016126591A1 (en) 2015-02-02 2016-08-11 E. I. Du Pont De Nemours And Company Root intrusion improvements in irrigation tubes
WO2016160733A1 (en) 2015-04-02 2016-10-06 E I Du Pont De Nemours And Company Dissipative system for safety garments
US9955747B2 (en) 2015-04-02 2018-05-01 E I Du Pont De Nemours And Company Dissipative system for safety garments
WO2017200831A1 (en) 2016-05-18 2017-11-23 E I Du Pont De Nemours And Company Composite comprising a nonwoven vapor permeable sheet
US10895036B2 (en) 2016-05-18 2021-01-19 Dupont Safety & Construction, Inc. Composite comprising a nonwoven vapor permeable sheet
WO2019135206A1 (en) 2018-01-08 2019-07-11 Low & Bonar Inc. Extruded rainscreen
WO2020033029A1 (en) 2018-08-10 2020-02-13 E. I. Du Pont De Nemours And Company Apparatus and method for protectively covering temperature sensitive products
WO2023039366A1 (en) 2021-09-07 2023-03-16 Dupont Safety & Construction, Inc. Hydroponic cultivation system

Similar Documents

Publication Publication Date Title
US3851023A (en) Process for forming a web
US3860369A (en) Apparatus for making non-woven fibrous sheet
US3689608A (en) Process for forming a nonwoven web
EP0635077B1 (en) Apparatus and method for producing a web of thermoplastic filaments
US4904174A (en) Apparatus for electrically charging meltblown webs (B-001)
US2273105A (en) Method and apparatus for the production of artificial structures
US5296172A (en) Electrostatic field enhancing process and apparatus for improved web pinning
EP2264230A2 (en) Rotary process for forming uniform material
US3593074A (en) Apparatus and process
GB1335216A (en) Process and apparatus for the manufacture of webs of non-woven fibrous material from melt-spun monofilaments
JP2005146502A (en) Stabilized filament drawing device for meltspinning apparatus
EP1432861B2 (en) Apparatus and method for producing a nonwoven web of filaments
CA1155264A (en) System and method for dispersing filaments
US3497918A (en) Apparatus for making a nonwoven fibrous sheet
US6979186B2 (en) Installation for producing a spunbonded fabric web with filament diffuser and separation by electrostatic process
US4666395A (en) Apparatus for making nonwoven sheet
US3296678A (en) Method and apparatus for producing nonwoven webs
US4172307A (en) Process and apparatus for the manufacture of non-wovens
JP2020045591A (en) Electrospinning apparatus and manufacturing method of nanofiber aggregates
EP0472208B1 (en) Gas management system for closely-spaced laydown jets
US3713590A (en) Apparatus for spreading filaments
US7008205B2 (en) Installation for producing a spunbonded fabric web whereof the diffuser is distant from the drawing slot device
US3655305A (en) Electrostatic repelling cylinders for filament flyback control
KR0142862B1 (en) Nonwoven fadric prodocing apparatus and air gun for the production of non-woven fadric
JP3518607B2 (en) Apparatus and method for forming fibrous sheet