Patent Publication Number: US-2009233049-A1

Title: Coform Nonwoven Web Formed from Propylene/Alpha-Olefin Meltblown Fibers

Description:
BACKGROUND OF THE INVENTION 
     Coform nonwoven webs, which are composites of a matrix of meltblown fibers and an absorbent material (e.g., pulp fibers), have been used as an absorbent layer in a wide variety of applications, including absorbent articles, absorbent dry wipes, wet wipes, and mops. Most conventional coform webs employ meltblown fibers formed from polypropylene homopolymers. One problem sometimes experienced with such coform materials, however, is that the polypropylene meltblown fibers do not readily bond to the absorbent material. Thus, to ensure that the resulting web is sufficiently strong, a relatively high percentage of meltblown fibers are typically employed to enhance the degree of bonding at the crossover points of the meltblown fibers. Unfortunately, the use of such a high percentage of meltblown fibers may have an adverse affect on the resulting absorbency of the coform web. Another problem sometimes experienced with conventional coform webs relates to the ability to form a textured surface. For example, a textured surface may be formed by contacting the meltblown fibers with a foraminous surface having three-dimensional surface contours. With conventional coform webs, however, it is sometimes difficult to achieve the desired texture due to the relative inability of the meltblown fibers to conform to the three-dimensional contours of the foraminous surface. 
     As such, a need currently exists for an improved coform nonwoven web for use in a variety of applications. 
     SUMMARY OF THE INVENTION 
     In accordance with one embodiment of the present invention, a coform nonwoven web is disclosed that comprises a matrix of meltblown fibers and an absorbent material. The meltblown fibers are formed from a thermoplastic composition that contains at least one propylene/α-olefin copolymer having a propylene content of from about 60 mole % to about 99.5 mole % and an α-olefin content of from about 0.5 mole % to about 40 mole %. The copolymer further has a density of from about 0.87 to about 0.94 grams per cubic centimeter and a melt flow rate of from about 200 to about 6000 grams per 10 minutes, determined at 230° C. in accordance with ASTM Test Method D1238-E. 
     In accordance with another embodiment of the present invention, a method of forming a coform nonwoven web is disclosed that comprises merging together a stream of an absorbent material with a stream of meltblown fibers to form a composite stream. Thereafter, the composite stream is collected on a forming surface to form a coform nonwoven web. The meltblown fibers are formed from a thermoplastic composition such as described above. 
     Other features and aspects of the present invention are described in more detail below. 
    
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
       A full and enabling disclosure of the present invention, including the best mode thereof, directed to one of ordinary skill in the art, is set forth more particularly in the remainder of the specification, which makes reference to the appended figures in which: 
         FIG. 1  is a schematic illustration one embodiment of a method for forming the coform web of the present invention; 
         FIG. 2  is an illustration of certain features of the apparatus shown in  FIG. 1 ; and 
         FIG. 3  is a cross-sectional view of one embodiment of a textured coform nonwoven web formed according to the present invention. 
     
    
    
     Repeat use of reference characters in the present specification and drawings is intended to represent same or analogous features or elements of the invention. 
     DETAILED DESCRIPTION OF REPRESENTATIVE EMBODIMENTS 
     Definitions 
     As used herein the term “nonwoven web” generally refers to a web having a structure of individual fibers or threads which are interlaid, but not in an identifiable manner as in a knitted fabric. Examples of suitable nonwoven fabrics or webs include, but are not limited to, meltblown webs, spunbond webs, bonded carded webs, airlaid webs, coform webs, hydraulically entangled webs, and so forth. 
     As used herein, the term “meltblown web” generally refers to a nonwoven web that is formed by a process in which a molten thermoplastic material is extruded through a plurality of fine, usually circular, die capillaries as molten fibers into converging high velocity gas (e.g., air) streams that attenuate the fibers of molten thermoplastic material to reduce their diameter, which may be to microfiber diameter. Thereafter, the meltblown fibers are carried by the high velocity gas stream and are deposited on a collecting surface to form a web of randomly dispersed meltblown fibers. Such a process is disclosed, for example, in U.S. Pat. No. 3,849,241 to Butin, et al., which is incorporated herein in its entirety by reference thereto for all purposes. Generally speaking, meltblown fibers may be microfibers that are substantially continuous or discontinuous, generally smaller than 10 micrometers in diameter, and generally tacky when deposited onto a collecting surface. 
     As used herein, the term “spunbond web” generally refers to a web containing small diameter substantially continuous fibers. The fibers are formed by extruding a molten thermoplastic material from a plurality of fine, usually circular, capillaries of a spinnerette with the diameter of the extruded fibers then being rapidly reduced as by, for example, eductive drawing and/or other well-known spunbonding mechanisms. The production of spunbond webs is described and illustrated, for example, in U.S. Pat. Nos. 4,340,563 to Appel, et al., 3,692,618 to Dorschner, et al., 3,802,817 to Matsuki, et al., 3,338,992 to Kinney, 3,341,394 to Kinney, 3,502,763 to Hartman, 3,502,538 to Levy, 3,542,615 to Dobo, et al., and 5,382,400 to Pike, et al., which are incorporated herein in their entirety by reference thereto for all purposes. Spunbond fibers are generally not tacky when they are deposited onto a collecting surface. Spunbond fibers may sometimes have diameters less than about 40 micrometers, and are often between about 5 to about 20 micrometers. 
     DETAILED DESCRIPTION 
     Reference now will be made in detail to various embodiments of the invention, one or more examples of which are set forth below. Each example is provided by way of explanation, not limitation of the invention. In fact, it will be apparent to those skilled in the art that various modifications and variations may be made in the present invention without departing from the scope or spirit of the invention. For instance, features illustrated or described as part of one embodiment, may be used on another embodiment to yield a still further embodiment. Thus, it is intended that the present invention cover such modifications and variations. 
     Generally speaking, the present invention is directed to a coform nonwoven web that contains a matrix of meltblown fibers and an absorbent material. The meltblown fibers are formed from a thermoplastic composition that contains at least one propylene/ 60  -olefin copolymer of a certain monomer content, density, melt flow rate, etc. The selection of a specific type of propylene/α-olefin copolymer provides the resulting composition with improved thermal properties for forming a coform web. For example, the thermoplastic composition crystallizes at a relatively slow rate, thereby allowing the fibers to remain slightly tacky during formation. This tackiness may provide a variety of benefits, such as enhancing the ability of the meltblown fibers to adhere to the absorbent material during web formation. Due in part to its enhanced bonding capacity, a lower amount of meltblown fibers may also be employed than previously thought needed to form a coherent and self-supporting coform structure. For example, the meltblown fibers may constitute from about 2 wt. % to about 40 wt. %, in some embodiments from 4 wt. % to about 30 wt. %, and in some embodiments, from about 5 wt. % to about 20 wt. % of the coform web. Likewise, the absorbent material may constitute from about 60 wt. % to about 98 wt. %, in some embodiments from 70 wt. % to about 96 wt. %, and in some embodiments, from about 80 wt. % to about 95 wt. % of the coform web. 
     In addition to enhancing the bonding capacity of the meltblown fibers, the thermoplastic composition of the present invention may also impart other benefits to the resulting coform structure. In certain embodiments, for example, the coform web may be imparted with texture using a three-dimensional forming surface. In such embodiments, the relatively slow rate of crystallization of the meltblown fibers may increase their ability to conform to the contours of the three-dimensional forming surface. Once the fibers crystallize, however, the meltblown fibers may achieve a degree of stiffness similar to conventional polypropylene, thereby allowing them to retain their three-dimensional shape and form a highly textured surface on the coform web. 
     Various embodiments of the present invention will now be described in more detail. 
     I. Thermoplastic Composition 
     The thermoplastic composition of the present invention contains at least one copolymer of propylene and an α-olefin, such as a C 2 -C 20  α-olefin, C 2 -C 12  α-olefin, or C 2 -C 8  α-olefin. Suitable α-olefins may be linear or branched (e.g., one or more C 1 -C 3  alkyl branches, or an aryl group). Specific examples include ethylene, butene; 3-methyl-1-butene; 3,3-dimethyl-1-butene; pentene; pentene with one or more methyl, ethyl or propyl substituents; hexene with one or more methyl, ethyl or propyl substituents; heptene with one or more methyl, ethyl or propyl substituents; octene with one or more methyl, ethyl or propyl substituents; nonene with one or more methyl, ethyl or propyl substituents; ethyl, methyl or dimethyl-substituted decene; dodecene; styrene; and so forth. Particularly desired α-olefin comonomers are ethylene, butene (e.g., 1-butene), hexene, and octene (e.g., 1-octene or 2-octene). The propylene content of such copolymers may be from about 60 mole % to about 99.5 mole %, in some embodiments from about 80 mole % to about 99 mole %, and in some embodiments, from about 85 mole % to about 98 mole %. The α-olefin content may likewise range from about 0.5 mole % to about 40 mole %, in some embodiments from about 1 mole % to about 20 mole %, and in some embodiments, from about 2 mole % to about 15 mole %. The distribution of the α-olefin comonomer is typically random and uniform among the differing molecular weight fractions forming the propylene copolymer. 
     The density of the propylene/α-olefin copolymer may be a function of both the length and amount of the α-olefin. That is, the greater the length of the α-olefin and the greater the amount of α-olefin present, the lower the density of the copolymer. Generally speaking, copolymers with a higher density are better able to retain a three-dimensional structure, while those with a lower density possess better elastomeric properties. Thus, to achieve an optimum balance between texture and stretchability, the propylene/α-olefin copolymer is normally selected to have a density of about 0.87 grams per cubic centimeter (g/cm 3 ) to about 0.94 g/cm 3 , in some embodiments from about 0.88 to about 0.92 g/cm 3 , and in some embodiments, from about 0.88 g/cm 3  to about 0.90 g/cm 3 . 
     Any of a variety of known techniques may generally be employed to form the propylene/α-olefin copolymer used in the meltblown fibers. For instance, olefin polymers may be formed using a free radical or a coordination catalyst (e.g., Ziegler-Natta). Preferably, the copolymer is formed from a single-site coordination catalyst, such as a metallocene catalyst. Such a catalyst system produces propylene copolymers in which the comonomer is randomly distributed within a molecular chain and uniformly distributed across the different molecular weight fractions. Metallocene-catalyzed propylene copolymers are described, for instance, in U.S. Pat. Nos. 7,105,609 to Datta, et al.; 6,500,563 to Datta, et al.; 5,539,056 to Yang, et al.; and 5,596,052 to Resconi, et al., which are incorporated herein in their entirety by reference thereto for all purposes. Examples of metallocene catalysts include bis(n-butylcyclopentadienyl)titanium dichloride, bis(n-butylcyclopentadienyl)zirconium dichloride, bis(cyclopentadienyl)scandium chloride, bis(indenyl)zirconium dichloride, bis(methylcyclopentadienyl)titanium dichloride, bis(methylcyclopentadienyl)zirconium dichloride, cobaltocene, cyclopentadienyltitanium trichloride, ferrocene, hafnocene dichloride, isopropyl(cyclopentadienyl-1-flourenyl)zirconium dichloride, molybdocene dichloride, nickelocene, niobocene dichloride, ruthenocene, titanocene dichloride, zirconocene chloride hydride, zirconocene dichloride, and so forth. Polymers made using metallocene catalysts typically have a narrow molecular weight range. For instance, metallocene-catalyzed polymers may have polydispersity numbers (M w /M n ) of below 4, controlled short chain branching distribution, and controlled isotacticity. 
     The propylene/α-olefin copolymer typically constitutes about 50 wt. % or more, in some embodiments about from 60 wt. % or more, and in some embodiments, about 75 wt. % or more of the thermoplastic composition used to form the meltblown fibers. Of course, other thermoplastic polymers may also be used to form the meltblown fibers so long as they do not adversely affect the desired properties of the composite. For example, the meltblown fibers may contain other polyolefins (e.g., polypropylene, polyethylene, etc.), polyesters, polyurethanes, polyamides, block copolymers, and so forth. In one embodiment, the meltblown fibers may contain an additional propylene polymer, such as homopolypropylene or a copolymer of propylene. The additional propylene polymer may, for instance, be formed from a substantially isotactic polypropylene homopolymer or a copolymer containing equal to or less than about 10 weight percent of other monomer, i.e., at least about 90% by weight propylene. Such a polypropylene may be present in the form of a graft, random, or block copolymer and may be predominantly crystalline in that it has a sharp melting point above about 110° C., in some embodiments about above 115° C., and in some embodiments, above about 130° C. Examples of such additional polypropylenes are described in U.S. Pat. No. 6,992,159 to Datta, et al., which is incorporated herein in its entirety by reference thereto for all purposes. 
     When employed, additional polymer(s) may constitute from about 0.1 wt. % to about 50 wt. %, in some embodiments from about 0.5 wt. % to about 40 wt. %, and in some embodiments, from about 1 wt. % to about 30 wt. % of the thermoplastic composition. Likewise, the above-described propylene/α-olefin copolymer may constitute from about 50 wt. % to about 99.9 wt. %, in some embodiments from about 60 wt. % to about 99.5 wt. %, and in some embodiments, from about 75 wt. % to about 99 wt. % of the thermoplastic composition. 
     The thermoplastic composition used to form the meltblown fibers may also contain other additives as is known in the art, such as melt stabilizers, processing stabilizers, heat stabilizers, light stabilizers, antioxidants, heat aging stabilizers, whitening agents, etc. Phosphite stabilizers (e.g., IRGAFOS available from Ciba Specialty Chemicals of Terrytown, N.Y. and DOVERPHOS available from Dover Chemical Corp. of Dover, Ohio) are exemplary melt stabilizers. In addition, hindered amine stabilizers (e.g., CHIMASSORB available from Ciba Specialty Chemicals) are exemplary heat and light stabilizers. Further, hindered phenols are commonly used as an antioxidant. Some suitable hindered phenols include those available from Ciba Specialty Chemicals of under the trade name “Irganox®”, such as Irganox® 1076, 1010, or E  201 . When employed, such additives (e.g., antioxidant, stabilizer, etc.) may each be present in an amount from about 0.001 wt. % to about 15 wt. %, in some embodiments, from about 0.005 wt. % to about 10 wt. %, and in some embodiments, from 0.01 wt. % to about 5 wt. % of the thermoplastic composition used to form the meltblown fibers. 
     Through the selection of certain polymers and their content, the resulting thermoplastic composition may possess thermal properties superior to polypropylene homopolymers conventionally employed in meltblown webs. For example, the thermoplastic composition is generally more amorphous in nature than polypropylene homopolymers conventionally employed in meltblown webs. For this reason, the rate of crystallization of the thermoplastic composition is slower, as measured by its “crystallization half-time”—i.e., the time required for one-half of the material to become crystalline. For example, the thermoplastic composition typically has a crystallization half-time of greater than about 5 minutes, in some embodiments from about 5.25 minutes to about 20 minutes, and in some embodiments, from about 5.5 minutes to about 12 minutes, determined at a temperature of 125° C. To the contrary, conventional polypropylene homopolymers often have a crystallization half-time of 5 minutes or less. Further, the thermoplastic composition may have a melting temperature (“T m ”) of from about 100° C. to about 250° C., in some embodiments from about 110° C. to about 200° C., and in some embodiments, from about 140° C. to about 180° C. The thermoplastic composition may also have a crystallization temperature (“T c ”) (determined at a cooling rate of 10° C./min) of from about 50° C. to about 150° C., in some embodiments from about 80° C. to about 140° C., and in some embodiments, from about 100° C. to about 120° C. The crystallization half-time, melting temperature, and crystallization temperature may be determined using differential scanning calorimetry (“DSC”) as is well known to those skilled in the art and described in more detail below. 
     The melt flow rate of the thermoplastic composition may also be selected within a certain range to optimize the properties of the resulting meltblown fibers. The melt flow rate is the weight of a polymer (in grams) that may be forced through an extrusion rheometer orifice (0.0825-inch diameter) when subjected to a force of 2160 grams in 10 minutes at 230° C. Generally speaking, the melt flow rate is high enough to improve melt processability, but not so high as to adversely interfere with the binding properties of the fibers to the absorbent material. Thus, in most embodiments of the present invention, the thermoplastic composition has a melt flow rate of from about 200 to about 6000 grams per 10 minutes, in some embodiments from about 300 to about 3000 grams per 10 minutes, and in some embodiments, from about 400 to about 1500 grams per 10 minutes, measured in accordance with ASTM Test Method D1238-E. 
     II. Meltblown Fibers 
     The meltblown fibers may be monocomponent or multicomponent. Monocomponent fibers are generally formed from a polymer or blend of polymers extruded from a single extruder. Multicomponent fibers are generally formed from two or more polymers (e.g., bicomponent fibers) extruded from separate extruders. The polymers may be arranged in substantially constantly positioned distinct zones across the cross-section of the fibers. The components may be arranged in any desired configuration, such as sheath-core, side-by-side, pie, island-in-the-sea, three island, bull&#39;s eye, or various other arrangements known in the art. Various methods for forming multicomponent fibers are described in U.S. Pat. Nos. 4,789,592 to Taniguchi et al. and U.S. Pat. No. 5,336,552 to Strack et al., 5,108,820 to Kaneko, et al., 4,795,668 to Kruege, et al., 5,382,400 to Pike, et al., 5,336,552 to Strack, et al., and 6,200,669 to Marmon, et al., which are incorporated herein in their entirety by reference thereto for all purposes. Multicomponent fibers having various irregular shapes may also be formed, such as described in U.S. Pat. Nos. 5,277,976 to Hogle, et al., 5,162,074 to Hills, 5,466,410 to Hills, 5,069,970 to Largman, et al., and 5,057,368 to Largman, et al., which are incorporated herein in their entirety by reference thereto for all purposes. 
     III. Absorbent Material 
     Any absorbent material may generally be employed in the coform nonwoven web, such as absorbent fibers, particles, etc. In one embodiment, the absorbent material includes fibers formed by a variety of pulping processes, such as kraft pulp, sulfite pulp, thermomechanical pulp, etc. The pulp fibers may include softwood fibers having an average fiber length of greater than 1 mm and particularly from about 2 to 5 mm based on a length-weighted average. Such softwood fibers can include, but are not limited to, northern softwood, southern softwood, redwood, red cedar, hemlock, pine (e.g., southern pines), spruce (e.g., black spruce), combinations thereof, and so forth. Exemplary commercially available pulp fibers suitable for the present invention include those available from Weyerhaeuser Co. of Federal Way, Wash. under the designation “Weyco CF-405.” Hardwood fibers, such as eucalyptus, maple, birch, aspen, and so forth, can also be used. In certain instances, eucalyptus fibers may be particularly desired to increase the softness of the web. Eucalyptus fibers can also enhance the brightness, increase the opacity, and change the pore structure of the web to increase its wicking ability. Moreover, if desired, secondary fibers obtained from recycled materials may be used, such as fiber pulp from sources such as, for example, newsprint, reclaimed paperboard, and office waste. Further, other natural fibers can also be used in the present invention, such as abaca, sabai grass, milkweed floss, pineapple leaf, and so forth. In addition, in some instances, synthetic fibers can also be utilized. 
     Besides or in conjunction with pulp fibers, the absorbent material may also include a superabsorbent that is in the form fibers, particles, gels, etc. Generally speaking, superabsorbents are water-swellable materials capable of absorbing at least about 20 times its weight and, in some cases, at least about 30 times its weight in an aqueous solution containing 0.9 weight percent sodium chloride. The superabsorbent may be formed from natural, synthetic and modified natural polymers and materials. Examples of synthetic superabsorbent polymers include the alkali metal and ammonium salts of poly(acrylic acid) and poly(methacrylic acid), poly(acrylamides), poly(vinyl ethers), maleic anhydride copolymers with vinyl ethers and alpha-olefins, poly(vinyl pyrrolidone), poly(vinylmorpholinone), poly(vinyl alcohol), and mixtures and copolymers thereof. Further, superabsorbents include natural and modified natural polymers, such as hydrolyzed acrylonitrile-grafted starch, acrylic acid grafted starch, methyl cellulose, chitosan, carboxymethyl cellulose, hydroxypropyl cellulose, and the natural gums, such as alginates, xanthan gum, locust bean gum and so forth. Mixtures of natural and wholly or partially synthetic superabsorbent polymers may also be useful in the present invention. Particularly suitable superabsorbent polymers are HYSORB 8800AD (BASF of Charlotte, N.C. and FAVOR SXM 9300 (available from Degussa Superabsorber of Greensboro, N.C.). 
     IV. Coform Technique 
     The coform web of the present invention is generally made by a process in which at least one meltblown die head (e.g., two) is arranged near a chute through which the absorbent material is added while the web forms. Some examples of such coform techniques are disclosed in U.S. Pat. Nos. 4,100,324 to Anderson, et al.; 5,350,624 to Georger, et al.; and 5,508,102 to Georger, et al., as well as U.S. Patent Application Publication Nos. 2003/0200991 to Keck, et al. and 2007/0049153 to Dunbar, et al., all of which are incorporated herein in their entirety by reference thereto for all purposes. 
     Referring to  FIG. 1 , for example, one embodiment of an apparatus is shown for forming a coform web of the present invention. In this embodiment, the apparatus includes a pellet hopper  12  or  12 ′ of an extruder  14  or  14 ′, respectively, into which a propylene/α-olefin thermoplastic composition may be introduced. The extruders  14  and  14 ′ each have an extrusion screw (not shown), which is driven by a conventional drive motor (not shown). As the polymer advances through the extruders  14  and  14 ′, it is progressively heated to a molten state due to rotation of the extrusion screw by the drive motor. Heating may be accomplished in a plurality of discrete steps with its temperature being gradually elevated as it advances through discrete heating zones of the extruders  14  and  14 ′ toward two meltblowing dies  16  and  18 , respectively. The meltblowing dies  16  and  18  may be yet another heating zone where the temperature of the thermoplastic resin is maintained at an elevated level for extrusion. 
     When two or more meltblowing die heads are used, such as described above, it should be understood that the fibers produced from the individual die heads may be different types of fibers. That is, one or more of the size, shape, or polymeric composition may differ, and furthermore the fibers may be monocomponent or multicomponent fibers. For example, larger fibers may be produced by the first meltblowing die head, such as those having an average diameter of about 10 micrometers or more, in some embodiments about 15 micrometers or more, and in some embodiments, from about 20 to about 50 micrometers, while smaller fibers may be produced by the second die head, such as those having an average diameter of about 10 micrometers or less, in some embodiments about 7 micrometers or less, and in some embodiments, from about 2 to about 6 micrometers. In addition, it may be desirable that each die head extrude approximately the same amount of polymer such that the relative percentage of the basis weight of the coform nonwoven web material resulting from each meltblowing die head is substantially the same. Alternatively, it may also be desirable to have the relative basis weight production skewed, such that one die head or the other is responsible for the majority of the coform web in terms of basis weight. As a specific example, for a meltblown fibrous nonwoven web material having a basis weight of 1.0 ounces per square yard or “osy” (34 grams per square meter or “gsm”), it may be desirable for the first meltblowing die head to produce about 30 percent of the basis weight of the meltblown fibrous nonwoven web material, while one or more subsequent meltblowing die heads produce the remainder 70 percent of the basis weight of the meltblown fibrous nonwoven web material. Generally speaking, the overall basis weight of the coform nonwoven web is from about 10 gsm to about 350 gsm, and more particularly from about 17 gsm to about 200 gsm, and still more particularly from about 25 gsm to about 150 gsm. 
     Each meltblowing die  16  and  18  is configured so that two streams of attenuating gas per die converge to form a single stream of gas which entrains and attenuates molten threads  20  and  21  as they exit small holes or orifices  24  in each meltblowing die. The molten threads  20  and  21  are formed into fibers or, depending upon the degree of attenuation, microfibers, of a small diameter which is usually less than the diameter of the orifices  24 . Thus, each meltblowing die  16  and  18  has a corresponding single stream of gas  26  and  28  containing entrained thermoplastic polymer fibers. The gas streams  26  and  28  containing polymer fibers are aligned to converge at an impingement zone  30 . Typically, the meltblowing die heads  16  and  18  are arranged at a certain angle with respect to the forming surface, such as described in U.S. Pat. Nos. 5,508,102 and 5,350,624 to Georger et al. Referring to  FIG. 2 , for example, the meltblown dies  16  and  18  may be oriented at an angle α as measured from a plane “A” tangent to the two dies  16  and  18 . As shown, the plane “A” is generally parallel to the forming surface  58  ( FIG. 1 ). Typically, each die  16  and  18  is set at an angle ranging from about 30 to about 75 degrees, in some embodiments from about 35° to about 60°, and in some embodiments from about 45° to about 55°. The dies  16  and  18  may be oriented at the same or different angles. In fact, the texture of the coform web may actually be enhanced by orienting one die at an angle different than another die. 
     Referring again to  FIG. 1 , absorbent fibers  32  (e.g., pulp fibers) are added to the two streams  26  and  28  of thermoplastic polymer fibers  20  and  21 , respectively, and at the impingement zone  30 . Introduction of the absorbent fibers  32  into the two streams  26  and  28  of thermoplastic polymer fibers  20  and  21 , respectively, is designed to produce a graduated distribution of absorbent fibers  32  within the combined streams  26  and  28  of thermoplastic polymer fibers. This may be accomplished by merging a secondary gas stream  34  containing the absorbent fibers  32  between the two streams  26  and  28  of thermoplastic polymer fibers  20  and  21  so that all three gas streams converge in a controlled manner. Because they remain relatively tacky and semi-molten after formation, the meltblown fibers  20  and  21  may simultaneously adhere and entangle with the absorbent fibers  32  upon contact therewith to form a coherent nonwoven structure. 
     To accomplish the merger of the fibers, any conventional equipment may be employed, such as a picker roll  36  arrangement having a plurality of teeth  38  adapted to separate a mat or batt  40  of absorbent fibers into the individual absorbent fibers. When employed, the sheets or mats  40  of fibers  32  are fed to the picker roll  36  by a roller arrangement  42 . After the teeth  38  of the picker roll  36  have separated the mat of fibers into separate absorbent fibers  32 , the individual fibers are conveyed toward the stream of thermoplastic polymer fibers through a nozzle  44 . A housing  46  encloses the picker roll  36  and provides a passageway or gap  48  between the housing  46  and the surface of the teeth  38  of the picker roll  36 . A gas, for example, air, is supplied to the passageway or gap  46  between the surface of the picker roll  36  and the housing  48  by way of a gas duct  50 . The gas duct  50  may enter the passageway or gap  46  at the junction  52  of the nozzle  44  and the gap  48 . The gas is supplied in sufficient quantity to serve as a medium for conveying the absorbent fibers  32  through the nozzle  44 . The gas supplied from the duct  50  also serves as an aid in removing the absorbent fibers  32  from the teeth  38  of the picker roll  36 . The gas may be supplied by any conventional arrangement such as, for example, an air blower (not shown). It is contemplated that additives and/or other materials may be added to or entrained in the gas stream to treat the absorbent fibers. The individual absorbent fibers  32  are typically conveyed through the nozzle  44  at about the velocity at which the absorbent fibers  32  leave the teeth  38  of the picker roll  36 . In other words, the absorbent fibers  32 , upon leaving the teeth  38  of the picker roll  36  and entering the nozzle  44 , generally maintain their velocity in both magnitude and direction from the point where they left the teeth  38  of the picker roll  36 . Such an arrangement, which is discussed in more detail in U.S. Pat. No. 4,100,324 to Anderson, et al. 
     If desired, the velocity of the secondary gas stream  34  may be adjusted to achieve coform structures of different properties. For example, when the velocity of the secondary gas stream is adjusted so that it is greater than the velocity of each stream  26  and  28  of thermoplastic polymer fibers  20  and  21  upon contact at the impingement zone  30 , the absorbent fibers  32  are incorporated in the coform nonwoven web in a gradient structure. That is, the absorbent fibers  32  have a higher concentration between the outer surfaces of the coform nonwoven web than at the outer surfaces. On the other hand, when the velocity of the secondary gas stream  34  is less than the velocity of each stream  26  and  28  of thermoplastic polymer fibers  20  and  21  upon contact at the impingement zone  30 , the absorbent fibers  32  are incorporated in the coform nonwoven web in a substantially homogenous fashion. That is, the concentration of the absorbent fibers is substantially the same throughout the coform nonwoven web. This is because the low-speed stream of absorbent fibers is drawn into a high-speed stream of thermoplastic polymer fibers to enhance turbulent mixing which results in a consistent distribution of the absorbent fibers. 
     To convert the composite stream  56  of thermoplastic polymer fibers  20 ,  21  and absorbent fibers  32  into a coform nonwoven structure  54 , a collecting device is located in the path of the composite stream  56 . The collecting device may be a forming surface  58  (e.g., belt, drum, wire, fabric, etc.) driven by rollers  60  and that is rotating as indicated by the arrow  62  in  FIG. 1 . The merged streams of thermoplastic polymer fibers and absorbent fibers are collected as a coherent matrix of fibers on the surface of the forming surface  58  to form the coform nonwoven web  54 . If desired, a vacuum box (not shown) may be employed to assist in drawing the near molten meltblown fibers onto the forming surface  58 . The resulting textured coform structure  54  is coherent and may be removed from the forming surface  58  as a self-supporting nonwoven material. 
     It should be understood that the present invention is by no means limited to the above-described embodiments. In an alternative embodiment, for example, first and second meltblowing die heads may be employed that extend substantially across a forming surface in a direction that is substantially transverse to the direction of movement of the forming surface. The die heads may likewise be arranged in a substantially vertical disposition, i.e., perpendicular to the forming surface, so that the thus-produced meltblown fibers are blown directly down onto the forming surface. Such a configuration is well known in the art and described in more detail in, for instance, U.S. Patent Application Publication No. 2007/0049153 to Dunbar, et al. Furthermore, although the above-described embodiments employ multiple meltblowing die heads to produce fibers of differing sizes, a single die head may also be employed. An example of such a process is described, for instance, in U.S. Patent Application Publication No. 2005/0136781 to Lassig, et al., which is incorporated herein in its entirety by reference thereto for all purposes. 
     As indicated above, it is desired in certain cases to form a coform web that is textured. Referring again to  FIG. 1 , for example, one embodiment of the present invention employs a forming surface  58  that is foraminous in nature so that the fibers may be drawn through the openings of the surface and form dimensional cloth-like tufts projecting from the surfaces of the material that correspond to the openings in the forming surface  58 . The foraminous surface may be provided by any material that provides sufficient openings for penetration by some of the fibers, such as a highly permeable forming wire. Wire weave geometry and processing conditions may be used to alter the texture or tufts of the material. The particular choice will depend on the desired peak size, shape, depth, surface tuft “density” (that is, the number of peaks or tufts per unit area), etc. In one embodiment, for example, the wire may have an open area of from about 35% and about 65%, in some embodiments from about 40% to about 60%, and in some embodiments, from about 45% to about 55%. One exemplary high open area forming surface is the forming wire FORMTECH™ 6 manufactured by Albany International Co. of Albany, N.Y. Such a wire has a “mesh count” of about six strands by six strands per square inch (about 2.4 by 2.4 strands per square centimeter), i.e., resulting in about 36 foramina or “holes” per square inch (about 5.6 per square centimeter), and therefore capable of forming about 36 tufts or peaks in the material per square inch (about 5.6 peaks per square centimeter). The FORMTECH™ 6 wire also has a warp diameter of about 1 millimeter polyester, a shute diameter of about 1.07 millimeters polyester, a nominal air permeability of approximately 41.8 m 3 /min (1475 ft 3 /min), a nominal caliper of about 0.2 centimeters (0.08 inch) and an open area of approximately 51%. Another exemplary forming surface available from the Albany International Co. is the forming wire FORMTECH™ 10, which has a mesh count of about 10 strands by 10 strands per square inch (about 4 by 4 strands per square centimeter), i.e., resulting in about 100 foramina or “holes” per square inch (about 15.5 per square centimeter), and therefore capable of forming about 100 tufts or peaks per square inch (about 15.5 peaks per square centimeter) in the material. Still another suitable forming wire is FORMTECH™ 8, which has an open area of 47% and is also available from Albany International. Of course, other forming wires and surfaces (e.g., drums, plates, etc.) may be employed. Also, surface variations may include, but are not limited to, alternate weave patterns, alternate strand dimensions, release coatings (e.g., silicones, fluorochemicals, etc.), static dissipation treatments, and the like. Still other suitable foraminous surfaces that may be employed are described in U.S. Patent Application Publication No. 2007/0049153 to Dunbar, et al. 
     Regardless of the particular texturing method employed, the tufts formed by the meltblown fibers of the present invention are better able to retain the desired shape and surface contour. Namely, because the meltblown fibers crystallize at a relatively slow rate, they are soft upon deposition onto the forming surface, which allows them to drape over and conform to the contours of the surface. After the fibers crystallize, they are then able to hold the shape and form tufts. The size and shape of the resulting tufts depends upon the type of forming surface used, the types of fibers deposited thereon, the volume of below wire air vacuum used to draw the fibers onto and into the forming surface, and other related factors. For example, the tufts may project from the surface of the material in the range of about 0.25 millimeters to at least about 5 millimeters, and in some embodiments, from about 0.5 millimeters to about 3 millimeters. Generally speaking, the tufts are filled with fibers and thus have desirable resiliency useful for wiping and scrubbing. 
       FIG. 3  shows an illustration of a cross section of a textured coform web  100  having a first exterior surface  122  and a second exterior surface  128 . At least one of the exterior surfaces has a three-dimensional surface texture. In  FIG. 3 , for instance, the first exterior surface  122  has a three-dimensional surface texture that includes tufts or peaks  124  extending upwardly from the plane of the coform material. One indication of the magnitude of three-dimensionality in the textured exterior surface(s) of the coform web is the peak to valley ratio, which is calculated as the ratio of the overall thickness “T” divided by the valley depth “D.” When textured in accordance with the present invention, the coform web typically has a peak to valley ratio of about 5 or less, in some embodiments from about 0.1 to about 4, and in some embodiments, from about 0.5 to about 3. The number and arrangement of the tufts  24  may vary widely depending on the desired end use. Generally, the textured coform web will have from about 2 and about 70 tufts per square centimeter, and in some embodiments, from about 5 and 50 tufts per square centimeter. The textured coform web may also exhibit a three-dimensional texture on the second surface of the web. This will especially be the case for lower basis weight materials, such as those having a basis weight of less than about 70 grams per square meter due to “mirroring”, wherein the second surface of the material exhibits peaks offset or between peaks on the first exterior surface of the material. In this case, the valley depth D is measured for both exterior surfaces as above and are then added together to determine an overall material valley depth. 
     V. Articles 
     The coform nonwoven web may be used in a wide variety of articles. For example, the web may be incorporated into an “absorbent article” that is capable of absorbing water or other fluids. Examples of some absorbent articles include, but are not limited to, personal care absorbent articles, such as diapers, training pants, absorbent underpants, incontinence articles, feminine hygiene products (e.g., sanitary napkins), swim wear, baby wipes, mitt wipe, and so forth; medical absorbent articles, such as garments, fenestration materials, underpads, bedpads, bandages, absorbent drapes, and medical wipes; food service wipers; clothing articles; pouches, and so forth. Materials and processes suitable for forming such articles are well known to those skilled in the art. 
     In one particular embodiment of the present invention, the coform web is used to form a wipe. The wipe may be formed entirely from the coform web or it may contain other materials, such as films, nonwoven webs (e.g., spunbond webs, meltblown webs, carded web materials, other coform webs, airlaid webs, etc.), paper products, and so forth. In one embodiment, for example, two layers of a textured coform web may be laminated together to form the wipe, such as described in U.S. Patent Application Publication No. 2007/0065643 to Kopacz, which is incorporated herein in its entirety by reference thereto for all purposes. In such embodiments, one or both of the layers may be formed from the coform web of the present invention. In another embodiment, it may be desired to provide a certain amount of separation between a user&#39;s hands and a moistening or saturating liquid that has been applied to the wipe, or, where the wipe is provided as a dry wiper, to provide separation between the user&#39;s hands and a liquid spill that is being cleaned up by the user. In such cases, an additional nonwoven web or film may be laminated a surface of the coform web to provide physical separation and/or provide liquid barrier properties. Other fibrous webs may also be included to increase absorbent capacity, either for the purposes of absorbing larger liquid spills, or for the purpose of providing a wipe a greater liquid capacity. When employed, such additional materials may be attached to the coform web using any method known to one skilled in the art, such as by thermal or adhesive lamination or bonding with the individual materials placed in face to face contacting relation. Regardless of the materials or processes utilized to form the wipe, the basis weight of the wipe is typically from about 20 to about 200 grams per square meter (gsm), and in some embodiments, between about 35 to about 100 gsm. Lower basis weight products may be particularly well suited for use as light duty wipes, while higher basis weight products may be better adapted for use as industrial wipes. 
     The wipe may assume a variety of shapes, including but not limited to, generally circular, oval, square, rectangular, or irregularly shaped. Each individual wipe may be arranged in a folded configuration and stacked one on top of the other to provide a stack of wet wipes. Such folded configurations are well known to those skilled in the art and include c-folded, z-folded, quarter-folded configurations and so forth. For example, the wipe may have an unfolded length of from about 2.0 to about 80.0 centimeters, and in some embodiments, from about 10.0 to about 25.0 centimeters. The wipes may likewise have an unfolded width of from about 2.0 to about 80.0 centimeters, and in some embodiments, from about 10.0 to about 25.0 centimeters. The stack of folded wipes may be placed in the interior of a container, such as a plastic tub, to provide a package of wipes for eventual sale to the consumer. Alternatively, the wipes may include a continuous strip of material which has perforations between each wipe and which may be arranged in a stack or wound into a roll for dispensing. Various suitable dispensers, containers, and systems for delivering wipes are described in U.S. Pat. Nos. 5,785,179 to Buczwinski, et al.; 5,964,351 to Zander; 6,030,331 to Zander; 6,158,614 to Haynes, et al.; 6,269,969 to Huang, et al.; 6,269,970 to Huang, et al.; and 6,273,359 to Newman, et al., which are incorporated herein in their entirety by reference thereto for all purposes. 
     In certain embodiments of the present invention, the wipe is a “wet” or “premoistened” wipe in that it contains a liquid solution for cleaning, disinfecting, sanitizing, etc. The particular liquid solutions are not critical and are described in more detail in U.S. Pat. Nos. 6,440,437 to Krzvsik, et al.; 6,028,018 to Amundson, et al.; 5,888,524 to Cole; 5,667,635 to Win, et al.; and 5,540,332 to Kopacz, et al., which are incorporated herein in their entirety by reference thereto for all purposes. The amount of the liquid solution employed may depending upon the type of wipe material utilized, the type of container used to store the wipes, the nature of the cleaning formulation, and the desired end use of the wipes. Generally, each wipe contains from about 150 to about 600 wt. % and desirably from about 300 to about 500 wt. % of a liquid solution based on the dry weight of the wipe. 
     The present invention may be better understood with reference to the following examples. 
     Test Methods 
     Melt Flow Rate: 
     The melt flow rate (“MFR”) is the weight of a polymer (in grams) forced through an extrusion rheometer orifice (0.0825-inch diameter) when subjected to a load of 2160 grams in 10 minutes at 230° C. Unless otherwise indicated, the melt flow rate was measured in accordance with ASTM Test Method D1238-E. 
     Thermal Properties: 
     The melting temperature, crystallization temperature, and crystallization half time were determined by differential scanning calorimetry (DSC) in accordance with ASTM D-3417. The differential scanning calorimeter was a DSC Q100 Differential Scanning Calorimeter, which was outfitted with a liquid nitrogen cooling accessory and with a UNIVERSAL ANALYSIS 2000 (version 4.6.6) analysis software program, both of which are available from T.A. Instruments Inc. of New Castle, Del. To avoid directly handling the samples, tweezers or other tools were used. The samples were placed into an aluminum pan and weighed to an accuracy of 0.01 milligram on an analytical balance. A lid was crimped over the material sample onto the pan. Typically, the resin pellets were placed directly in the weighing pan, and the fibers were cut to accommodate placement on the weighing pan and covering by the lid. 
     The differential scanning calorimeter was calibrated using an indium metal standard and a baseline correction was performed, as described in the operating manual for the differential scanning calorimeter. A material sample was placed into the test chamber of the differential scanning calorimeter for testing, and an empty pan is used as a reference. All testing was run with a 55-cubic centimeter per minute nitrogen (industrial grade) purge on the test chamber. For resin pellet samples, the heating and cooling program was a 2-cycle test that began with an equilibration of the chamber to −25° C., followed by a first heating period at a heating rate of 10° C. per minute to a temperature of 200° C., followed by equilibration of the sample at 200° C. for 3 minutes, followed by a first cooling period at a cooling rate of 10° C. per minute to a temperature of −25° C., followed by equilibration of the sample at −25° C. for 3 minutes, and then a second heating period at a heating rate of 10° C. per minute to a temperature of 200° C. All testing was run with a 55-cubic centimeter per minute nitrogen (industrial grade) purge on the test chamber. The results were then evaluated using the UNIVERSAL ANALYSIS 2000 analysis software program, which identified and quantified the melting and crystallization temperatures. 
     The half time of crystallization was separately determined by melting the sample at 200° C. for 5 minutes, quenching the sample from the melt as rapidly as possible in the DSC to a preset temperature, maintaining the sample at that temperature, and allowing the sample to crystallize isothermally. Tests were performed at two different temperatures—i.e., 125° C. and 130° C. For each set of tests, heat generation was measured as a function of time while the sample crystallized. The area under the peak was measured and the time which divides the peak into two equal areas was defined as the half-time of crystallization. In other words, the area under the peak was measured and divided into two equal areas along the time scale. The elapsed time corresponding to the time at which half the area of the peak was reached was defined as the half-time of crystallization. The shorter the time, the faster the crystallization rate at a given crystallization temperature. 
     Example 1 
     Various grades of polypropylene were tested for their half crystallization time (t 1/2 ) at 125° C. and 130° C., crystallization temperature (T c ), and melting temperature (T m ) as described above. The results are shown below. 
     
       
         
           
               
               
               
               
               
               
             
               
                   
                   
               
               
                   
                   
                 t 1/2  [min] 
                 t 1/2  [min] 
                 T c   
                 T m   
               
               
                   
                 Designation 
                 @ 125 C. 
                 @ 130 C. 
                 [° C.] 
                 [° C.] 
               
               
                   
                   
               
             
            
               
                   
               
            
           
           
               
               
               
               
               
               
            
               
                   
                 Basell 441 1   
                 2.5 
                 9.5 
                 111 
                 167 
               
               
                   
                 Metocene MF650X 2   
                 5.0 
                 17.0 
                 113 
                 156 
               
               
                   
                 Borflow HL512 3   
                 1.3 
                 4.0 
                 119 
                 160 
               
               
                   
                 VM 7001-3 4   
                 6.0 
                 20.0 
                 111 
                 158 
               
               
                   
                   
               
               
                   
                   1 Basell 441 is a propylene homopolymer having a density of 0.91 g/cm 3  and melt flow rate of 440 g/10 minute (230° C., 2.16 kg), which is available from Basell Polyolefins. 
               
               
                   
                   2 Metocene MF650X is a propylene homopolymer having a density of 0.91 g/cm 3  and melt flow rate of 1200 g/10 minute (230° C., 2.16 kg), which is available from Basell Polyolefins. 
               
               
                   
                   3 Borflow HL512 is a propylene homopolymer having a density of 0.91 g/cm 3  and melt flow rate of 1200 g/10 minute (230° C., 2.16 kg), which is available from Borealis A/S. 
               
               
                   
                   4 [VM 7001-3] is a propylene/ethylene copolymer having a density of 0.89 g/cm 3  and a melt flow rate of 540 g/10 minutes (230° C., 2.16 kg), which is available from ExxonMobil Corp. 
               
            
           
         
       
     
     Example 2 
     Various samples of coform webs were formed from two heated streams of meltblown fibers and a single stream of fiberized pulp fibers as described above and shown in  FIG. 1 . The meltblown fibers were formed from the polypropylene samples referenced in Example 1. The pulp fibers were fully treated southern softwood pulp obtained from the Weyerhaeuser Co. of Federal Way, Wash. under the designation “CF-405.” 
     The polypropylene of each stream was supplied to respective meltblown dies at a rate of 1.5 to 2.5 pounds of polymer per inch of die tip per hour to achieve a meltblown fiber content ranging from 25 wt. % to 40 wt. %. The distance from the impingement zone to the forming wire (i.e., the forming height) was approximately 8 inches and the distance between the tips of the meltblown dies was approximately 5 inches. The meltblown die positioned upstream from the pulp fiber stream was oriented at an angle of 50° relative to the pulp stream, while the other meltblown die (positioned downstream from the pulp stream) was oriented between 42 to 45° relative to the pulp stream. The forming wire was FORMTECH™ 8 (Albany International Co.). To achieve different types of tufts, rubber mats were disposed on the upper surface of the forming wire. One such mat had a thickness of approximately 0.95 centimeters and contained holes arranged in a hexagonal array. The holes had a diameter of approximately 0.64 centimeters and were spaced apart approximately 0.95 centimeters (center-to-center). Mats of other patterns (e.g., clouds) were also used. A vacuum box was positioned below the forming wire to aid in deposition of the web and was set to 30 inches of water. 
     While the invention has been described in detail with respect to the specific embodiments thereof, it will be appreciated that those skilled in the art, upon attaining an understanding of the foregoing, may readily conceive of alterations to, variations of, and equivalents to these embodiments. Accordingly, the scope of the present invention should be assessed as that of the appended claims and any equivalents thereto.