LIQUID-ABSORBENT ARTICLE AND METHOD AND APPARATUS FOR MANUFACTURING THE ABSORBENT ARTICLE

Abstract: A liquid-absorbent article having a high absorption capacity and a short fluid penetration time. The liquid-absorbent article has a porosity gradient along the Z direction (the thickness) established by superposing layers of absorbent material having different average pore sizes. In one embodiment the porous network of each absorbent layer is a combination of inter-particle and intra-particle interstices. In another embodiment the absorbent layers have different average particle sizes. The liquid-absorbent article is well-suited for use as an absorbent component of a disposable absorbent product, such as a sanitary napkin, a diaper, an incontinence pad, an adult brief, a wound dressing, a nursing pad, a tampon pledget, or as desiccant for packaging materials to keep goods dry during shipping or storage. The invention also extends to a novel method and apparatus for manufacturing the liquid-absorbent article.

Description: TITLE: LIQUID ABSORBENT ARTICLE AND METHOD AND APPARATUS FOR MANUFACTURING THE ABSORBENT ARTICLE FIELD OF THE INVENTION The Invention relates to the art of anufacturinq structures for absorbino body exudate. More specifically, the invention relates to a hiohlv absorbent article that has a porosity qradient alonq the direction of fluid miqration there throuqh. The Invention also extends to a method and apparatus for manufacturinq the absorbent article. BACKGROUND OF THE INVENTION Many disposable absorbent products use absorbent cores made primarily of cellulosic pulp fluff material. Such cores are generally soft, flexible and absorbent but tend to be bulky and thick and have poor wicking properties. In addition, cellulosic pulp fluff material has poor structural stability which may cause the absorbent core to collapse when saturated with liquid. An absorbent structure that has poor wickinq properties usually Increases the likelihood of failure of the absorbent product to hold and contain body liquids. Body exudate will be localized to a certain area of the poorly wicking absorbent medium, causing localized saturation whereby excess liquid may overflow throuoh an external surface of the absorbent product . This overflow may contact the user's qarment and cause stains or contact the user's body and cause wet discomfort or rash. It is therefore desirable to provide an absorbent core for disposable absorbent products which can wick away body liquids from the point of contact with the absorbent core and spread it throuqh the absorbent core. The improved wlckino properties of such an absorbent core provide the capacity for liquids to travel bv capillary pressure throuohout the entire absorbent volume. This permits the use of thinner cores, since more absorbent volume can be made available for absorbino body liquids by such wickinq action. Thinner absorbent cores may also prove to be more comfortable for the user and less unsiqhtlv or obvious when worn under clothes. Absorbent cores co prlsinα sphagnum moss are described, for example, in the followinq US patents, the subject matter of which is incorporated herein by reference, in their entirety: In accordance with the teachinα of these patents, an absorbent structure comprisino sphaqnu moss as a primary absorbent component is formed as a sheet by air or wet lavinq of particles. The sheet is calendered to obtain a relatively thin. i.e. from about 0.025 to about 0.25 centimeters (cm) thick and relatively dense, i.e. from about ø.l to about 1.0 qrams per cubic centimeter (g/cc) structure. Such absorbent sphaonum moss sheet may be processed to increase its flexibility for enhancino its comfort potential bv subjectinq the sheet to mechanical tenderlzinq such as a perf-embossinq or a micro-corruoatinq process. The sphaqnum moss sheet thus formed has a larqe proportion of extremely tiny pores and capillaries allowing the sheet to absorb and retain a very hiqh amount of liquid. The sphaqnum moss pores swell as they absorb liquid, however, this swelling does not cause a loss of capacity for further admittinq liquid. Rather, the swelling contributes to the ability of the absorbent medium to retain the liquid while qenerally maintaininq the structural integrity of the absorbent structure in use. The wickinq properties of the above-described sphaqnum moss sheet provide the ability for the sheet to be highly absorbent while remaining relatively thin. Although sphagnum moss has certain highly desirable liquid-absorption properties, It manifests less than ideal fluid-acquisition rates. To overcome this difficulty it is common practice to provide a highly permeable, fibrous, llguid transfer layer on the sphagnum moss layer, whose function is to quickly collect the body exudate and then meter the liguid to the sphagnum moss material. Liquid discharged on such composite absorbent structure will rapidly Ingress the transfer layer due to its highly porous network. From the transfer layer, liquid migrates toward the sphagnum moss layer by capillary pressure as a result of the substantial difference in wickino power between the different materials. The liquid mlqration is well-controlled, occurrinq at the rate of acceptance of the sphaqnum moss. Compound absorbent structures includinq transfer and reservoir layers are costly to produce because the raw material for manufacturlnq the transfer layer Is expensive. Another drawback is the undesirable bulk increase of the disposable absorbent article resultinq from the use of a thick transfer layer. Hence, there Is a need in the industry to provide a sphagnum moss absorbent core having a significantly improved liguid acquisition rate, thus allowinq to employ a thinner transfer layer and possibly eliminate the transfer layer altogether. SUMMARY OF THE INVENTION It is an object of this invention to provide an absorbent article having a high liquid-acquisition rate and a hiqh absorption capacity. Another object of this invention is to provide a disposable absorbent product, such as a sanitary napkin, a diaper, an incontinence pad, an adult brief, a wound dressing, a nursing pad, a tampon pledget, or a desiccant for packaging materials, which utilizes a sphagnum moss absorbent core having a significantly improved liquid acgulsition rate. Another object of this invention is to provide a novel method and apparatus for manufacturing a liquid-absorbent article which utilizes a sphaonum moss absorbent core havinα a sionifleantIv improved liquid acquisition rate. As embodied and broadly described herein, the present invention provides a liquid-absorbent article comprising absorbent particulate material and further comprislnα first and second zones in Intimate fluid communicative relationship, each zone having a multiplicity of inter-particle and intra-particle Interstices admitting passage of liquid, said first zone havinα a larger average interstice size than said second zone, whereby said second zone manifests a higher capillary attraction than said first zone. For purposes of the present invention, the terminology "particle" shall mean fibrous as well as non-fibrous materials, i.e., any small unit of material without limitations of shape. Thus, a fiber that is characterized as havinq a geometrical extension along a preferential direction will be considered a particle. Hence, "particulate material" includes materials made of fibers, particles having non-fibrous identity, or a combination of both. As used herein the terminology "inter-particle interstices" refers solely to the interstices defined between the particles, while "intra-particle interstices" refers to an open cellular structure inside the particles, such as the lumen in sphagnum moss leaves. The terminology "average interstice size" as used herein refers to both the intra-particle interstices and the inter-particle interstices. There exist many different porous materials which are capable of providing intra-particle interstices and thus are considered suitable for use in the manufacture of the liquid-absorbent article of the present invention. Suitable materials include, for example, sphaqnum, perlite, ver iculite, expanded clav, expanded rice, crushed foam, zeolite, and combinations thereof are suitable for use in the present invention. Sphaαnum, however, is the preferred material for use in the present invention due to its hiqhlv absorbent nature. As used herein the terminoloαy "intlmate fluid-communicativ relationship" refers to a condition in which liquid in one of the zones can easily mlorate toward the other zone. This condition is achieved when the zones are co-formed or when they have been formed as discrete elements and then joined to one another by means to create an interface providing a path of comparatively low resistance to the mlqration of liquid. Suitable means for joining the zones include, but are not limited to, adhesive, thermobondlnq, needle punchinq, and the like, and combinations thereof. It has now been discovered that absorbent structures havlnq a porosity qradient of the type broadly defined above, provide a siqnifleant advantage to absorbent products. The first zone has an open network that rapidly admits the discharge of body exudate into the absorbent structure. The second zone has a less open network which provides a strong capillary attraction differential between the two zones, whereby the liguid is preferentially drawn toward the second zone where it is permanently entrapped. The increase in the fluid take-up rate of the provided bv the absorbent structure of the present invention permits a disposable absorbent product to utilize a thinner transfer layer without increasing the risk of failure by overflow leakage. For some applications, the transfer layer may even be dispensed with. The average interstice size of a given zone of the liquid-absorbent article mav be controlled v one or more of the followinq expedients-. A) adjusting the proportion between inter-particle interstices and intra-part icle interstices In the liquid-absorbent material. For example, an increase in the relative amount of particles having intra-part icle interstices in the liguid-absorbent material, wherein the intra-part icle interstices are smaller than the inter-particle interstices, will cause the average interstice size of the liquid-absorbent material to diminish. For example, sphaqnum moss has lumen (i.e. intra-part icle interstice) whose average size is typically below 66 microns. Accordingly, a relative Increase m the amount of sphagnum moss in the liguid-absorbent material will result in a reduction in the average interstice size. Conversely, a relative decrease in the ratio intra-part icle interstices/inter-particle interstices, results In an increase in the average Interstice size. B) adjusting the size of the inter-particle interstices of the material. In general, the size of inter-particle interstices is proportional to the size of the particles. Hence, the incorporation of coarse particles into a liquid- absorbent material will result in a liquid-absorbent article having larger interstices than would be obtained by the use of fine particles. This allows one to regulate the average interstice size by varying the average particle size of the material. C) combininα steps A and B. For example, the averaoe Interstice size of a material mav be increased bv introducing in the absorbent material non-porous particles that are relatively larqe. The non-porous character of the particles increases the ratio inter-particle interstices/intra-particles interstices while the coarseness of the particles augments the average inter- particle size. D) applyinq mechanical compression to brlnq the particles closer to one another, thus decreasing the average interstice size. The compression may affect both the inter-particle interstice and the intra-particle interstice sizes . Thus, anyone of the steps A to D applied alone or in combination can be used to control the average interstice size of individual zones of the liguid-absorbent to optimize the porosity gradient in the liguid-absorbent product. Under one exemplary embodiment, the liquid-absorbent product includes a lower layer made of sphagnum moss material on top of which is inteqrally formed an upper layer that combines sphaqnum moss and debonding component . The purpose of the debondlng component is to increase the average Interstice size In the sphagnum moss network and provide therein interstices that are significantly larger than the interstices of the lower layer. For the purpose of this specification "debonding component" shall mean any material which is capable of reducing the cohesivenesε of a given particulate liguid- absorbent material, such as an agent acting chemically to reduce the bonds unit inq the particle- * . of the material to one another, or a physical separator that forcibly maintains the particles in a spaced apart relationship, hence increasing the average interstice size of the network. One example of a suitable debonding component manifestinα a physical separator activity is cross-linked cellulosic fibers. Suitable cross-linked cellulosic fibers for use in this invention are disclosed in US patent 4,853,086, assigned to Weyerhaeuser Company, dated August 1, 1989, which describes a method for manufacturing cross-linked cellulosic fibers which consists of sprayinq a wet or partially dry web of cellulosic fibers with an aqueous solution of glycol and dialdehyde. The disclosure of this patent is incorporated herein by reference in its entirety. Under another exemplary embodiment, the porosity gradient is obtained by forming the various layers of the liquid-absorbent sheet from sphagnum moss particles having different dimensions. More particularly, the upper layer is formed of sphagnum moss particles that are relatively coarse i.e. larger than the particles in the lower layer. When those particles are amalgamated together during the formation process of the absorbent sheet, large inter-particle interstices remain between them. In contrast, the lower layer is formed primarily of fine sphagnum moss particles that, due to their smaller size, fit closer to one another to provide inter-particle interstices of lesser dimensions. A hybrid structure combining the features of the two previously described embodiments is the most preferred. The characterizing feature of this variant is the inclusion of debonding component into the upper laver of coarse sphaonum moss particles. Again, the debonding component may be a chemical aqent or a physical separator such as cross-linked fibers. Preferably, the layer of coarse sphagnum moss particles has a particle size median value in the range from about 2øøø microns to about 5øø microns. Preferably, the fine layer of sphaqnum moss particles has a particle size median value in the range from about 5øø microns to about 150 microns. The layer of coarse sphagnum moss particles having a median particle of about 2000 microns has significantly more inter-particle interstices in the size range from about 6øø microns to about 120 microns, by comparison to a fine layer of sphagnum moss where no separation has been made between coarse and fine sphagnum moss particles, and thus has a lesser amount of inter-particle interstices in the size range from about 6øø microns to about 120 microns than the coarse sphagnum layer. In a preferred embodiment, the coarse layer of sphagnum moss has at least about 55% of inter-particle Interstices (in term of interstice count rather than Interstice volume) having a size in the range from about 6øø microns to about 120 microns, more preferably at least about 60% of inter-particle interstices In that range and most preferably at least about 63% of inter-particle Interstices in that range. For purposes of this specification, any interstice in sphagnum moss material having a size in excess of 66 microns is considered to be an inter-particle interstice rather than an intra-particle interstice, since the intra-particle interstices (lumen) on the sphagnum leaves are substantially smaller than 66 microns. As embodied and broadly described herein, the invention also lø provides a liguid-absorbent article including first and second zones in fluid-communicative relationship, said first zone and said second zone including sphagnum moss particles, said first zone having a larqer proportion of inter-particle interstices (in terms of interstice count rather than interstice volume) in a size ranqe from about 600 microns to about 12ø microns than said second zone. Under this embo i ent, the absorbent article is not necessarily an inteqrally formed structure. The various zones which preferably form individual layers of the article may be discrete elements that are united with adhesive or by another suitable means. As embodied and broadly described herein, the Invention also provides a liquid-absorbent article including first and second zones in fluid-communica ive relationship, said first zone including sphagnum moss particles having a first particle size median value, said second zone having a second particle size median value. As embodied and broadly described herein, the invention also provides a disposable absorbent product, comprising! - an absorbent component of particulate material, said absorbent component including upper and lower layers in Intimate fluid communicative relationship, each zone havinq a multiplicity of inter-particle and intra-particle interstices admitting passage of liguid, said first zone having a larger averaoe interstice size than said second zone, whereby said lower zone manifests a higher capillary attraction than said upper laver in order to induce liguid absorbed in said upper laver to mlorate toward said lower layer-, and - a body contacting, liguid-pervious cover layer superposed to said absorbent component . As embodied and broadly described herein, the invention further provides a method for manufacturing a liquid absorbent component, said method comprising the steps of: - provldlnq a first zone of particulate material havinα a multiplicity of inter-partIcle and intra-particle interstices, said first zone havinq a first averaαe interstice size; - providing a second zone of particulate material having a multiplicity of inter-particle and intra-particle interstices, said second zone having a second average interstice size, said first interstice size being larger than said second Interstice size; and - establishing an intimate fluid communicative relationship between said zones to allow liguid in said first zone to migrate toward said second zone. In a most preferred exemplary embodiment, the first and the second zones include sphagnum moss and are manufactured by a co-forming process which includes the following steps: A) laying in a superposed relationship and in physical contact a first slurry layer of particulate material and a second slurry layer of particulate material to form a laminated composite slurry laver, the first and the second slurry layers includinq [effective amounts of) sphaqnum moss particles, I) the first slurrv layer constitutinq a precursor phase of a the first zone; II) the second slurry layer constitutinq a precursor phase of the second zone; B) extractinq fluidizing medium from the laminated composite slurry layer to form a laminated composite web including the first zone and the second zone in a superposed condition and intimately united to one another. The co-forming process broadly described above greatly simplifies the manufacture of the liquid-absorbent article in accordance with the Invention because the formation and bonding of the layers is accomplished In a single operation. A further advantage of this method resides in the strength of the bond between the layers which is highly resistant to delamination. As a result, the liquid-absorbent article can withstand vlqorous mechanical working without loosing its structural Integrity. Further, the bond is such as to establish the desirable Intimate fluid-communicative relationship allowing fluid to easily migrate from the upper layer towards the lower layer. In a most preferred embodiment, the slurries forming the respective layers of the liguid-absorbent article are laid in a superposed relationship on a continuously advancing Fourdrinier wire to form the laminated composite slurry layer. The Fourdrinier wire is passed over a vacuum slot establishing a pressure differential across the laminated composite slurrv laver to extract water therefrom. The resulting web is dried, calendered and cut into discrete absorbent components. If desired, the web may be subjected to mechanical working, such as perf-embossing or micro-corrugating, in order to increase its flexibility for a better comfort potential. The composition of the individual slurry layers determines the final structure of the liguid-absorbent sheet. When the porosity qradient Is achieved solely bv the inclusion of debonding component in the upper layer, the selected debonding component Is added to the slurry before laying the slurry on the Fourdrinier wire. Under the embodiment that reguires separation of the sphagnum moss In coarse particles and fine particles, the manufacturing process begins by preparing a mother slurry containing sphagnum moss particles of varying sizes. The slurry is then subjected to a classification step to separate the mother slurry in at least two slurry fractions according to the size of the sphagnum moss particles. The slurry fractions are then laid in a superposed relationship on a Fourdrinier wire as described above. Under the hybrid embodiment the sphaqnum moss particle separation is followed by the addition of debonding component in the slurry fraction containing the coarse sphagnum moss particles. In a possible variant, the layers of the absorbent article are formed as discrete elements that are ultimately united bv adhesive bonding or by any other suitable agency to form a laminated structure having strata of different average interstice sizes. In an exemplary embodiment the layers are manufactured bv separating a mother slurry of sphagnum moss into coarse and fine fractions, and then laying the fractions separately to form the individual layers. After the usual post-formation treatments, such as drylnq, pressing, calendering, etc., the layers are united to one another In a superposed relationship. Objectively, the manufacture of the liguid absorbent article conducted by assembling together discrete absorbent layers is perhaps less desirable than the lnteqral formation approach, primarily because additional manipulations are required to complete the manufacture of the absorbent article. In addition, the interface between the discrete layers provides a liquid path of somewhat hlqher resistance than when the layers are inteqrally formed. Still, this embodiment exhibits significantly improved liquid-absorbent properties by comparison to prior art structures and it thus suitable for many applications. As embodied and broadly described herein, the invention further provides a method for manufacturing a laminated liquid-absorbent article, comprising the steps of: - providing a body of particles suspended in fluid, such as liguid or gas, said particles havinq varying dimensions; separating said body of particles in at least two fractions, referenced as a first fraction and a second fraction, said first fraction having a higher particle size median value than said second fraction: - extracting fluidizing medium from said fractions to form a first absorbent layer and a second absorbent layer respectively, said first absorbent layer havinq a hlqher averaαe inter-particle Interstice size than said second absorbent layer, whereby said second absorbent layer manifests a higher capillary attraction than said first absorbent layer; - establishing a liguid-communlcatlve relationship between said layers, whereby liguid introduced in said first layer is induced to migrate toward said second layer under the effect of capillary attraction. In the most preferred embodiment, the liguid communicative relationship between the absorbent layers is created by co-formation, such as wet laying the slurry fractions in a superposed relationship, as described earlier. This approach produces an integrally formed liguid-absorbent article. In a variant, the absorbent layers may be formed separately from one another and then assembled by adhesive bonding or the like to establish the liquid-communicative relationship between them. As embodied and broadly described herein, the invention also provides an apparatus for manufacturing a highly absorbent structurally integral article having superposed liguid-absorbent layers united In an intimate fluid-communicative relationship, said apparatus comprising: a classifier for separating particles suspended in fluidizing medium into at least two slurry fractions in accordance to size of said particles, a first slurrv fraction having a larger particle size median than a second slurrv fraction, said classifier having first and second outlets for discharging said first and second slurry fractions, respectively; - a foramlnous member; - first and second headboxes in a fluid communica ive relationship with said firs and second outlets respectively for discharging said first and second slurry fractions in a superposed relationship on said foraminous member to form a laminated composite slurry layer-, and - means for establishing a pressure differential across said laminated composite slurry layer to extract fluidizing medium from said first and second slurry fractions in order to form respective first and second porous networks intimately united to one another, said second porous network manifesting a higher capillary attraction than said first porous network to induce liquid absorbed in said first porous network to migrate toward said second porous network. The fluid absorbent article In accordance with the present invention is suitable for use in disposable absorbent products Including, but not limited to sanitary napkins, diapers, urinary pads, adult briefs, wound dressing, nursing pads, tampon pledgets, or as desiccants for packaging materials to keep goods dry during shipping or storage. BRIEF DESCRIPTION OF THE DRAWINGS - Figure 1 is a fragmentary, perspective view of a sanitary napkin incorporating the liαuid-absorbent article accordmα to the invention: - Figure 2 is a fragmentary perspective view of the liquid- absorbent article according to the present invention that is characterized by a non-uniform porositv distribution; - Figure 3 is a schematic representation of an apparatus for manufacturing the compound, structurally inteqral, liquid-absorbent article in accordance with the invention; - Fiαure 4 is a flowchart of the process for manufacturing the liquid-absorbent article In accordance with the invention; - Fiqure 5 is a flowchart of the process for manufacturing the liguid-absorbent article in accordance with a variant; - Figure 6 is a flowchart of the process for manufacturing the liguid-absorbent article in accordance with a further variant ; - Figure 7 is a perspective view of a liguid-absorbent article manufactured by assembling in a superposed relationship separately formed discrete absorbent layers; and Figure 8 is a porosity distribution graph of the liquid-absorbent article and some of its component layers. DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS Referring now to Figure 1 of the annexed drawings, the reference numeral lø deslonates comprehensively a sanitary napkin constructed in accordance with the principles of the present invention. The sanitary napkin lø comprises an envelope 12 defining an internal space receiving an absorbent component 56 that includes sphagnum moss. The envelope 12 includes a liquid permeable cover layer 16 made of a non-woven fabric or any other suitable porous web or apertured film, and a liguid impervious backing layer 18, made of polyethylene film for example. The cover and backing layers 16 and 18 are heat-sealed to one another along their marginal portions. To attach the sanltarv napkin 10 to the wearer's underpants, the liquid impervious backing layer 18 may be provided with adhesive zones covered with a peelable backing (not shown in the drawings). The absorbent component 56 is a dual-layer structure featuring a porosity gradient along the Z direction. Preferably, a transfer layer (not shown in the drawings) of known construction is provided over the absorbent component with a view of further enhancing the liguid acquisition rate of the sanitary napkin. The structure of the absorbent component 56 is shown in Figure 2. It comprises a central core 58 containing primarily sphagnum moss and having a porosity gradient along the Z direction (the thickness). The central core 58 is constituted by an upper layer 60a and a lower layer 60b intermixed at the interface to provide an intimate liguid-communlcative relationship between them. Layer 60a has a larger average interstice size than layer 60b. The central core 58 is confined between reinforcing layers 62 and 64 of fibrous material. The purpose of the reinforcing layers Is twofold. First, they strengthen the core 58, thereby providing a unitlzed absorbent structure capable of maintaininα its integrity even when saturated with liguid. Second, the layers 62 and 64 reduce dusting by preventing free sphagnum moss particles within the absorbent structure from being released outside. Kraft wood pulp material has been found hlqhly satisfactory for manufacturinq the reinforcing layers 62 and 64. It is also possible to use other materials, such cotton linters or ground wood among others, in admixture with or In substitution to the Kraft wood pulp material. The detailed composition of the liquid-absorbent component 56 will be best understood from the following description of the apparatus and the process for manufacturing such absorbent component. Referring to Figure 3, the apparatus designated comprehensively by the reference numeral 18, comprises an endless, fluid-pervious Fourdrinier wire 26 which is mounted on rollers 28 to provide a horizontally extending run 30 that is continuously advanced forward to support and convey a slurry of sphagnum moss and cellulosic fibers through various processing stations. Headboxes 32, 34, 66 and 36 arranged in a spaced apart relationship along the path of travel of the wire 26 are provided to lay on the wire 26 slurry in sheeted form. The headbox bank deposits on the wire 26 four (4) layers of slurry in a superposed relationship to form a laminated slurry web. More specifically, the headboxes 34 and 66 lay slurries containing sphagnum moss while the headboxes 32 and 36 deliver slurries of fibrous material such as Kraft wood pulp or any other suitable substance. The preparation of the sphagnum moss slurry layers supplied to headboxes 34 and 66 is illustrated by the flowchart of Figure 4. The mother slurry prepared by dispersing raw sphagnum moss material in water is wet classified at steps 68 and 7ø to retain only the particles having a size in the range from about 74 microns to about 2ø0ø microns. The screened fraction is diluted with water to render the slurry more manageable and supplied to a dual-stage classifier station 72 in order to separate the sphagnum moss particles in a fine fraction and a coarse fraction. The classifier station 72 comprises a primary centrifugal classifier 74 to perform an initial separation of the sphagnum moss particles on the basis of size. A centrifugal classifier available from Hymac Limited under any one of commercial designations RB 200, RB 150XC or RB 8øX has been found satisfactory. The centrifugal classifier 74 is calibrated to produce a reject stream having a particle size median in the range from about 2øøø microns (lø mesh) to about 5øø microns(35 mesh) that is directed at headbox 66. The particle size median value is defined as the size of the particles having the highest freguency when the sphagnum moss particles are classified according to size. It is preferred to add a fibrous component, such as polyester fibers and/or Kraft wood pulp at step 76 prior to supplying the slurry to headbox 66 that forms the layer 6øa of the central core 58. Suitable fibrous components may include such materials as Kraft wood pulp, cross-linked cellulosic fibers, mechanical wood pulp, natural or synthetic textile fibers such as rayon, polyester, nylon, acrylic and the like, and mixtures thereof. The fibrous components are generally added to t h e headbox In an amount from 2 to 20% by weight of the absorbent sheet 10, preferably from 2% to 6%. As used herein, the term mechanical wood pulp is meant to include ground wood pu l p, thermo-mechanlcal pulp and refiner wood pulp. Ground wood pu l p is essentially trees and branches which have been debarked, cleaned and ground into particulate matter. Refiner wood pulp differs from ground wood pulp only in that the grindinq step utilizes a refiner, i.e. a disc-like device well-known in the art and having metallic ribs at the peripheral sections thereof which last contact the wood particles and help separate the wood fibers without excessively damaging them. Thermo-mechanical wood pulp is similar to refiner pulp with the exception that the wood particles are heated in the refiner, usually with steam, to aid in separating the wood fibers. The common characteristic of these mechanical pulps is that no attempt has been made to separate the fibers by chemical means although they may later, after being reduced to fine particulate matter, be subjected to a desired chemical treatment, such as bleaching. Preferably, when mechanical wood pulp is used in a sphagnum moss slurry, such mechanical pulp has a Canadian Standard Freeness (TAPPI test method T-227), in a range of from about 60 to 750 and preferably from about 40ø to 600. The Kraft wood pulp, also usable in combination with sphagnum moss, is essentially chemically treated, long fibred wood pulp such as sulphite and sulphate wood pulps. Preferably, a debonding component Is added to the slurry supplied to headbox 66 in an amount which is effective to increase the inter-particle interstices in the liquid-absorbent product. Suitable debondinq agents Include, but are not limited to fibrous materials which are effective for reducing the coheslveness of the particles in the liguid-absorbent product. These fibrous materials preferablv have a length of from about 0.6 cm to about 1.9 cm, preferably about 1.3 cm and a denier of from about 1.0 to 5.0. Preferred debonding components which have been found to be particularly effective in opening-up a sphagnum moss network in order to allow a faster liguid acquisition are cross-linked cellulosic fibers. In a preferred embodiment, cross-linked cellulosic fibers are incorporated Into the slurry in an amount effective to reduce the cohesiveness of the sphagnum moss particles in the liguid-absorbent product, i.e., open-up the sphagnum moss network. The exact amount of cross-linked fibers can vary widely, depending on the nature and particle size of the sphagnum moss particles, and is preferably in the range from about 5% to about 75% based on the weight of solids in the slurry. The slurry of coarse sphagnum moss particles may also contain an effective amount of a chemical debonding agent, of a type known in the art, which can be used either In combination or in substitution to the cross-linked cellulosic fibers. The accepts stream of the centrifugal classifier 74 that contains sphagnum moss particles of smaller size is supplied to a 60 mesh stationary screen 78 of the type described in Canadian patent application 2,057,654 assigned to Johnson & Johnson Inc. laid open on June 14, 1993 which is incorporated herein by reference in its entirety. The screen 78 features a system of jets directed at the screen plate to prevent the screen apertures from clogging. The rejects stream that contains particles larger than about 15ø microns (løø mesh) are discarded. The accepts having an average particle size in the range from about 50ø microns (35 mesh) to about 150 microns (løø mesh) are directed to headbox 34 to form layer 6øb of the central core 58. It is preferred that a stationary screen operating on the principle of a sieve be used in the second stage 78 than a centrifugal classifier because it allows a better process control. Similarly, a stationary screen, may be substituted to the centrifugal classifier 74. Such stationary screen is identical to screen 78 described above with the exception that screening apertures of 6.35 mm could be used rather than 6ø mesh perforations. At the completion of the classification stage, a fibrous component may be added to the slurry, as shown as step 80. In a variant, the slurry fractions supplied to the headboxes 34 and 66 are prepared on the production line illustrated in Figure 5. The difference with the set-up of Figure 4 resides in that no cross-linked cellulosic fibers are added to the flow of coarse sphagnum moss particles. In a further variant shown in Figure 6, no separation of the sphagnum moss particles is made. The slurry from the screening system 68 and 70 is split in two parts having approximately the same sphagnum moss particle size distribution. To create the porosity gradient in the final product, cross-linked fibers or another debonding component is added to one of the slurry fractions from which the layer 6øa is made. In a first embodiment of the present invention, as illustrated in Figure 3, a slurry of Kraft wood pulp layer havinα a consistency of about 0.2% by weight of solids is first laid down on the wire 26 from the headbox 32 In order to form the bottom Kraft reinforcing layer 64. The slurry flow rate is selected to deliver on the wire 26, 15 grams of solids per square meter. The Kraft slurry passes under the headbox 34 which delivers on top of the Kraft layer a slurry of fine sphaqnum moss particles prepared with the installation of Fiqure 4. The slurry has a sphaqnum moss content in the range from about 80% to løø% by weight of solids in the slurry and contains polyester fibers up to 2ø% by weight. A specific formulation that has been found satisfactorv is reproduced belo : The consistency of the sphagnum moss slurry fraction is set at 0.5% by weight of solids. The flow rate of the slurry fraction is selected to deliver 178 grams of solids per sguare meter on the wire 26. The headbox 66 delivers the slurry fraction of coarse sphagnum moss particles intermixed with cellulosic cross-linked fibers. This slurry fraction has a consistency of 0.5% by welqht of solids, a flow rate to deliver 182 grams of solids per sguare meter on the wire 20. The coarse particles slurry contains sphaqnum moss in the ranoe from about 20% to 60% by weloht o f solids in the slurry, cross-linked cellulosic fibers in the ranqe from about 5% to about 75% by weiqht and polyester fibers up to 20% by weight . Example 1. A liguid absorbent article was manufactured havinq the following formulation and porosity distribution profile as described below: For comparison purposes, the porosity distribution of the individual layers of the liguid-absorbent article of this example was determined and provided in the following tables. The method for measuring the porosity distribution profiles is discussed hereinafter in the section entitled "Test procedures". For layer 6øa (containing the coarse sphaqnum moss particles, the interstice size and percentage of interstices are as follows: For layer 60b (containing the fine sphagnum moss particles), the interstice size and percentage of interstices are as follows: The porosity distribution profiles for the entire liguid-absorbent article and its individual layers are also reported in a chart shown in Figure 8. It is particularly interesting to note that the layer 6øa (coarse sphagnum particles) had a significant amount of interstices in the size range from about 6øø microns to about 120 microns. In a preferred embodiment, layer 6øa should have at least about 50% of interstices in the range 600 - 12ø microns, more preferably at least about 60% and most preferably (in the embodiment shown) at least about 63%. In contrast, the layer 60b had less interstices in this size range (41% in the embodiment shown). Example 2. A second example of a formulation for the sphagnum moss slurry layers delivered from the headboxes 34 and 66 is as follows. This formulation was prepared in accordance with the manufacturing process shown in Figure 5 and contained sphagnum moss in the range from about 68% to løø% by weight of solids in the slurry, polyester fibers up to 2ø% by weight and Kraft wood pulp fibers up to 30% by weight. The slurry fractions coarse/fine differed primarily by the particle size of the sphagnum moss material. In this example, the slurry fraction of primarily fine sphagnum moss particles was as follows: The s lurry f ract ion of primari ly coarse sphagnum moss part icles was as fol lows : CONSTITUENT PROPORTION BY WEIGHT spr.aαr.um ac-εs ' .art icle si ze mediar: i . the ranqe f om 2.3. micron, tc 58. iicrons' colvester fibers 2 . η . '< F.raft wood culo fibers 5.55! Example 3. A third example of a formulation for the sphagnum moss slurry layers delivered from the headboxes 34 and 66 is as follows. This formulation was prepared in accordance with the manufacturing process shown in Figure 6. In this example, both slurry fractions have approximately the same sphagnum moss particle size distribution. The lower slurry layer delivered from the headbox 34 had a sphagnum moss content in the range from about 8ø% to løø% by weight of solids in the slurry and contained polyester fibers up to 20% by weight. The specific formulation is as follows: The upper slurry fraction delivered from the headbox 66 contains sphagnum moss in the range from about 2ø% to about 6ø% by weight of solids in the slurry, cross-linked cellulosic fibers in the range from about 5% to about 75% by weight and polyester fibers up to 20% by weight. A specific formulation is reproduced below: A final Kraft wood pulp slurry layer was laid from the headbox 36 on the sphagnum moss slurry in order to form the reinforcing top layer 62. This final layer was identical In terms of consistency and composition to the bottom Kraft wood pulp layer 64 previously deposited except that the flow rate was such as to deposit on a sguare meter of the wire 26 five grams of solids. The resulting laminated slurry layer Kraft/Sphaqnum/ Sphagnum/Kraft was then passed over a vacuum slot 5ø to extract water under the influence of a pressure differential established across the slurry layer. It was necessary to regulate the residence time of the slurry layer over the vacuum slot 50 and the vacuum intensity in order to control the density of the final product. Generally, decreased vacuum and increased speed will result In a less dense product. Conversely, increased vacuum and decreased speed will produce a denser product . The web leaving the dewatering station 50 passed through a drier 52 whose purpose was to elevate the temperature of the web to evaporate residual water. The drier 52 is of a well-known construction and does not reguire a detailed description herein. It may be envisaged to add between the drier 52 and the vacuum slot 50 a press section (not shown in the drawings) to mechanically express water from the web, as it is well-known to those skilled in the art, in order to reduce the water contents in the web as much as possible before it is processed in the drier 52. Downstream of the drier 52 a calendering station 54 is provided which mechanically compresses the dried product in order to densify the sphagnum moss material for enhancing Its drying powe . If desired, the calendering station 54 may be followed by a perf-embossing station (not shown in the drawings) provided to tenderize the web by mechanical working. This treatment softens the sphagnum moss structure for enhancing its comfort potential. The calendering operation is described in detail in the international application PCT/CA92/00308 filed on July 2ø, 1992 in the name of Johnson & Johnson Inc. The contents of this application is incorporated herein by reference. An alternative to the perf-embossing technigue is the micro-corrugating operation which is similar to the perf-embossing except that no perforations are performed. The liguid-absorbent structure is solely subjected to an embossing operation to create closely spaced hinge lines. The micro-corrugating operation is described in US patents granted to Personal Products Company 4,596,567 and 4,559,ø5ø issued on June 24, 1986 and December 17, 1988 respectively. The contents of these patents is incorporated herein by reference. If desired, the absorbent article under the second embodiment may be treated with re-wetting agent. Preferably, an RL Thorowet re-wetting agent (available from Clough Chemicals) is added to the mother slurry prior to the screening step in an amount of 0.3% by weight of solids In the absorbent article. Subsequently, a G-60 Thorowet re-wetting agent (available from Clough Chemicals) is delivered on the Kraft/Sphagnum/ Sphagnum/Kraft laminated slurry layers, prior the dewatering stage in an amount of 0.8% by weight of solids in the absorbent article. Most preferably, the G-60 Thorowet re-wetting agent is delivered on the top Kraft layer in a foamed condition, as described in the Canadian Patent application 2,057,693 in the name of Johnson & Johnson Inc. and laid open on June 14, 1993. The disclosure of this patent application is incorporated herein by reference. A variant of the liquid-absorbent article is illustrated in Figure 7. This variant Is characterized in that the layers 60a and 6øb are formed as discrete entities and then united to form a compound liguid-absorbent structure, rather than being integrally formed. The layers are manufactured by following the process steps illustrated in Figure 4 with the exception that headboxes 34 and 66 deposit the fine and the coarse slurry fractions on separate Fourdrinier wires (not shown in the drawings). Each slurry fraction is then subjected to independent post-formation treatments, such as pressing, drying, calendering, etc. The resulting absorbent layers are then united to one another in a superposed relationship by adhesive or any other suitable agency. Sanitary napkins constructed with the liguid-absorbent article 56 as the absorbent core are found to possess a very high liguid-absorption capacity and a comparatively high liquid-penet ation rate which reduces the risk of failure when a large quantity of body exudate is suddenly released on the sanitary napkin. The properties of the liquid-absorbent article 56 and of the sanitary napkin manufactured with such absorbent article are compared to control samples in a series of tests. LIQUID- BSORBENT ARTICLE CONTROL The control Is an integrally formed sheet containing a central core of sphagnum moss having a uniform porosity distribution and united to two outer layers of Kraft wood pulp. The central core contains 76.92% by weight of solids in the control sheet of sphagnum moss, 3.69% of polyester fibers and 7.38% of Kraft wood pulp. Each of the top and bottom Kraft layers represent 4.61% of the control by weight of solids. The control sheet also contains 0.92% by weight of solids of G-6ø Thorowet re-wetting agent and 0.4% by weight of solids of RL Thorowet re-wetting agent that are applied as discussed earlier. The basis weight of the control sheet is of 325 grams per meter sguared. SANITARY NAPKIN CONTROL The sanitary napkin control is manufactured by placing on the absorbent article as described above cut in the form of a lø centimeter (cm) by lø cm sguare, a transfer layer of identical dimensions. The specific transfer layer used has a basis weight of 120 grams per meter sguared and it is available from James River Corporation under the brand designation Alrtex 397. Finally, a lø cm by lø cm embossed hydrophillic apertured film is placed over the transfer layer. The apertured film is known in the trade as wettable Retlculon and it is used to manufacture the cover layer of a sanitary napkin commercialized by Johnson & Johnson in Germany under the trademark Silhouette Ultra. In a first set of tests the liguid-absorbent article prepared by the process of Figure 4 is tested against the liquid absorbent article control to assess the following characteristics (test procedures are described in detail later) : a) Capacity; b) Capillary pressure (1st load); c) Capillary pressure (2nd load); d) Penetration time (synthetic menstrual test liquid with protein having a viscosity of 25 centipoise (cps) ; e) Penetration time (synthetic menstrual test liguid with protein having a viscosity of 100 cps); and f) Stain area In a second set of tests the liquid absorbent article prepared by the process of Figure 4 is incorporated in a sanitary napkin construction as the absorbent core. This consists of placing on the liquid absorbent article the transfer layer and the cover layer used In the sanitary napkin control. The resulting product is then tested against the sanitary napkin control to assess the following characteristics (test procedures are described in detail later) : g) Penetration time (menstrual test liguid with protein having a viscosity of løø cps); h) Re-wet/wet back; and i) Liquid distribution; EXPERIMENTAL DATA FROM TESTS A TO F EXPERIKERTAL DATA FROH TEST I TEST PROCEDURES CAPACITY Purpose: to determine the absorption capacity of an absorbent material . Test procedure: a disk of 90 mm diameter is cut from a sheet of the material to be tested. The dry weiαht of the disk is measured and recorded. The disk is deposited on the porous plate of a GATS (Gravimetric Absorbency Test System) instrument (a "coarse" or "medium" fritted disk having 9ø mm diameter available from CanadaWide Inc., has been found satisfactory). Test fluid is allowed to ingress the sample through the porous plate for a period of 15 minutes. The wetted sample is removed from the porous plate and weighted to determine the amount of test fluid uptake. The absorption capacity is expressed in terms of volume of fluid absorbed (cubic centimeters (cc) or mllliliters (ml)) per gram of absorbent material. For ease of reference, however, the absorption capacity is reported in the above test results in mllliliters per pad of absorbent material in the form of a sheet of 20 cm X 5 cm having a weight of 4 grams (g). Test fluid-. 1% NaCl solution CAPILLARY PRESSURE Purpose: to determine the capillary attraction developed by an absorbent material on a fluid. Test procedure: the instrument disclosed in the US patent 5,361,627 assigned to Johnson & Johnson Inc that was issued on November 8, 1994 is used for this purpose. A sample of the material to be tested in the form of a rectangle 5 cm bv 2 0 cm is laid on a horizontal support surface. For a first l oa d test, 3 cc of test fluid is deposited on the virgin sample an d the sensor of the Instrument Is placed in contact wit h t h e absorbing surface of the sample. After 30 minutes from t h e fluid discharge the pressure readinq in millimeters of mercury (mmHg) is recorded. • For a second test load, the sensor is removed, an additional load of 3 cc of test fluid is discharged and the sensor is placed again In contact with the absorbing surface of the sample. The pressure reading is taken 3ø minutes after the second 3 cc fluid discharge. Test fluid; synthetic menstrual liguid with protein havinq a viscosity of 25 cps. STAIN AREA Purpose: to determine fluid migration profile of test fluid in a sample material. Test procedure: a sample of the absorbent material in the form of a rectangle lø cm X lø cm is laid on a flat surface and 1 cc of test fluid is discharged in the center of the absorbent surface. After the liguid has disappeared the surface area of the stain Is measured and recorded. A comparatively small surface area indicates that the absorbent material has a good wicking power in the Z direction (vertical). Test fluid: synthetic menstrual fluid with protein having a viscosity of 25 cps. PENETRATION TIME Purpose; to determine the penetration time of an absorbent material by measuring the time regulred to completely absorb a finite amount of fluid. Test procedure: the time required for a 5 cm X 2ø cm sample to absorb 5 cc of test fluid fed to the sample from an overhanqinq burette at 1.5 cm from the absorbinq surface of the sample. The penetration time is recorded when all free liquid has disappeared from the surface of the sample. Test fluid: synthetic menstrual fluid with protein havinα a viscosity of either 25 cps or løø cps. RE-WET/WETBACK Purpose: the purpose of this test is to assess the propensity of a fluid present in an absorbent material under pressure to wet back an adjacent surface in contact therewith. Test Procedure: the sample material to which has been delivered lø cubic centimeters of test fluid is allowed to rest 15 minutes and it is covered with a NuGauze brand pad. A pressure of 10.48 kPa is applied over the NuGauze pad. After 3 minutes, the amount of fluid (mass) captured by the pad is measured and reported in percentage on the basis of the dry weight of the pad. Test Fluid synthetic menstrual fluid with protein having a viscosity of løø cps. LIQUID DISTRIBUTION Purpose to determine the fluid distribution profile in a mult1-layered absorbent structure. Test procedure: the dry weight of each layer of the absorbent structure is recorded. The absorbent structure is then assembled and laid on a flat surface. 5 cc of test fluid is deposited on the absorbent surface of the structure. After 20 minutes following the test fluid discharge each layer of the absorbent structure is weighted to determine the individual amount of fluid take-uc. Test fluid; synthetic menstrual fluid with protein having viscosity of løø cps. POROSITY DISTRIBUTION Purpose: to determine the porositv distribution profile in an absorbent structure. Test procedure: A GATS (Gravimetric Absorbencv Test Rvst i is used to determine the amount of liquid retained .in the samplp at different hydrostatic negative pressures. The results are then converted to int rr-.t jre size value-- using a known formula. The GATS apparatus uses a "medium" fritted disc (CANADAWIDR) havinq a 90 mm diameter. The fritted disc is in liguid communication with a vertical burette containing test liquid. The vertical distance between the meniscus in the burette and the top surface of the fritted disc on which the sample is deposited defines the hydrostatic pressure exerted on the sample. To maintain the hydrostatic pressure constant during the entire test procedure the burette is continuously replenished with liquid at the same rate at which the liquid is beinq absorbed by the sample. Prior to initiating the test procedure the weight of the sample which is in the form of a 90 mm disc is corrected at 12% relative humidity (RH). This is effected by first measuring the dry weight of the sample (after drylno the sample at 150 degrees Celsius for 15 minutes) and then its weight when humid (after allowlnq the sample to reach equilibrium) to determine its level of humidity . P . -> Corrected weioht at 12% RH P . - * > weioht of humid sample P - Drv weiqht _^„-P..lOO R11-- The corrected weiαht at 12% RH is : The amount of liquid absorbed bv the sample is then measured for the followinq neqat ive hydrostatic pressures: -45 cm, -4ø cm, -35 cm, -25 cm, -15 cm, -5 cm and -1 cm. For the -45 cm measurement the sample is placed on the fritted disc under a 50 g compressive weight. The sample remains on the fritted disc for 15 minutes. The amount of test liguid pick-up is measured bv subtracting P. from the weioht. of the wet sample (P,_ ) . The height of the liquid in the burette lε raised to -40 cm and the sample placed back on the fritted disc for another 15 min. The amount of additional liquid pick-up is calculated by subtractinq from P ., rr the weiqht of the sample at -4ø cm. The same procedure is followed for the remaining hydrostatic pressures. The proportion of liguid pick-up at each hydrostatic pressure is translated in percentage of interstices by usinq the following table which establishes a correspondence between the hydrostatic pressure and Interstice size: -1 cm -> 298ø microns -5 cm -> 596 microns -15 cm -> 199 microns -25 cm -> 119 microns -35 cm -> 85 microns -4ø cm -> 74 microns -45 cm -> 66 microns By "interstice sizes" is meant the egulvalent interstice diameter. The above table establishing the relationship between the hydrostatic pressure and the Interstice size is obtained from the following formula; ._ 2y. cosA T . d. g. Where: h -> hydrostatic pressure height (cm) a -> 73 dynes/cm cosA -> assumed to be 1 r -> interstice radius (micron) d -> density of test liguid (l.OOg/cc) g -> gravity (980cm/ms ' ) ; and The test results clearly demonstrate the advantages of the liguid absorbent article in accordance with the invention. Note particularly the dramatic improvement in penetration time and capillary pressure over the control. The ability of such liquid absorbent article to manifest a powerful capillary attraction is particularly useful in sanitary napkin constructions for the purpose of desorbing the adjacent liguid absorbing layers. For instance, the results of test I (liguid distribution) show that the liguid absorbent article in accordance with the Invention collects virtually all the liquid discharqed on the sanitary napkin, totally desorbinα the cover layer and leaving only a small amount of liguid in the transfer layer. In contrast, the control has a less favorable fluid distribution pattern, with only 48 % of the total liguid discharge being contained in the absorbent core. Another interesting point is the significant reduction of wet-back in light of the penetration time improvement. These two parameters are usually considered by the prior art as incompatible objectives in that an improvement of one entails a negative effect on the other. Much to the contrary, the present invention demonstrates the possibility of improving both parameters without creating any significant drawbacks. Applications of the product and methods of the present invention for sanitary and other health-care uses can be accomplished by any sanitary protection, incontinence, medical and absorbent methods and techniques as are presently or prospectively known to those skilled in the art. Thus, it is intended that the present application covers the modifications and variations of this invention provided that they come within the scope of the appended claims and their equivalents.

Claims: WE CLAIM : 1. A liguid-absorbent article of particulate material Including first and second zones in intimate fluid communicative relationship, each zone having a multiplicity of inter-particle and intra-particle interstices admitting passage of liguid, said first zone having a larger averaαe interstice size than said second zone, whereby said second zone manifests a hlqher capillary attraction than said first zone. 2. A liquid-absorbent article as defined in claim 1, wherein said second zone incudes sphagnum moss. 3. A liquid-absorbent article as defined in claim 2, wherein said first zone Includes sphagnum moss. 4. A liguid-absorbent article as defined in claim 3, wherein said first zone has a larger sphagnum moss particle size median than said second zone. 5. A liguid-absorbent article as defined in claim 4, wherein said first zone has a sphagnum moss particle size median in the range from about 2000 microns to about 500 microns. 6. A liguid-absorbent article as defined in claim 5, wherein said second zone has a sphagnum moss particle size median in the range from about 5øø microns to about 150 microns. 7. A liquid-absorbent article as defined in claim 1, wherein said article is in the form of a sheet. 8. A liquid-absorbent article as defined in claim 7, wherein said zones constitute superposed layers of said sheet. 9. A liquid-absorbent article as defined in claim 3, wherein said first zone includes debonding component. 10. A liguid-absorbent article as defined In claim 9, wherein said debonding component constitutes a physical separator for maintaining sphagnum moss particles In a spaced apart relationshlp. 11. A liquid-absorbent article as defined in claim 10, wherein said debonding component has a fibrous identity. 12. A liguid-absorbent article as defined in claim 9, wherein said first zone includes cross-linked cellulosic fibers in the range from about 5% to about 75% by weight of solids in said first zone. 13. A liguid-absorbent article as defined in claim 1, further comprising a fibrous component selected from the group consisting of rayon, polyester, nylon, acrylic, Kraft wood pulp, mechanical wood pulp, cotton liners and mixtures thereof . 14. A liguid-absorbent article as defined in claim 1, wherein said article is mechanically tenderized for increasing a softness and flexibility of said article. 15. A liquid-absorbent article as defined in claim 1, wherein said article is mechanically tenderized by a method selected from the group consisting of perf-embossing and micro-corrugating. 16. A liguid-absorbent article as defined in claim 7 , comprising a reinforcing layer. 17. A liguid-absorbent article as defined in claim 16, wherein said reinforcing layer provides an outer surface o f said article. 18. A liguid-absorbent article as defined in claim 17, wherein said article includes a pair of reinforcing layers in a spaced apart relationship providing respective main outer surfaces of said article, said first and second zones being located between said reinforcing layers. 19. A liguid-absorbent article as defined in claim 16, wherein said reinforcing layer includes Kraft wood pulp fibers. 20. A liguid-absorbent article as defined in claim 3, wherein said first zone has a higher proportion of inter-particle interstices in a size range from about 6øø microns to about 12ø microns than said second zone. 21. A liguid-absorbent article as defined in claim 3, wherein said first layer has at least about 55% inter-particle interstices having a size In the ranoe from about 6øø microns to about 12ø microns. 22. A liguid-absorbent article as defined In claim 3, wherein said first layer has at least about 60% inter-partIcle interstices having a size in the range from about 600 microns to about 12ø microns. 23. A liguid-absorbent article as defined in claim 3, wherein said first layer has at least about 63% lnter-particle interstices having a size in the range from about 6øø microns to about 120 microns. 24. A liguid-absorbent article as defined in claim 1, wherein said article is integrally formed. 25. A liguid-absorbent article as defined in claim 1, wherein said zones are discrete entities united in a face-to-face relationship. 26. A liquid-absorbent article including first and second zones in fluid-communicative relationship, said first zone and said second zone including sphagnum moss particles, said first zone having a larger proportion of inter-particle interstices in a size range from about 60ø microns to about 120 microns than said second zone. 27. A liquid-absorbent article as defined in claim 26, wherein said zones are integrally formed. 28. A liguid-absorbent article as defined in claim 27, wherein said zones constitute superposed layers of said article. 29. A liguid-absorbent article including first and second zones in fluid-communicative relationship, said first zone including sphagnum moss particles having a first particle size median value, said second zone including sphagnum moss particles having a second particle size median value, said first particle size median value being larger than said second particle size median value. 30. A liguid-absorbent article as defined in claim 29, wherein said first zone has a sphagnum moss particle size median in the range from about 20øø microns to about 500 microns . 31. A liguid-absorbent article as defined in claim 30, wherein said second zone has a sphagnum moss particle size median in the range from about 500 microns to about 15ø microns. 32. A liguid-absorbent article as defined in claim 29, wherein said article is in a configuration of a sheet, said zones constituting superposed layers of said sheet. 33. A disposable absorbent product, comprising: - an absorbent component of particulate material, said absorbent component including upper and lower layers in intimate fluid communicative relationship, each zone havinq a multiplicity of inter-particle and intra-particle interstices admitting passage of liguid, said first zone having a larger average interstice size than said second zone, whereby said lower zone manifests a higher capillary attraction than said upper layer in order to induce liguid absorbed In said upper layer to migrate toward said lower layer; and - a body contacting, liguld-pervious cover layer superposed to said absorbent component . 34. A disposable absorbent product as defined in claim 33. further comprising a liguid-impervious layer underneath said absorbent component for preventing liquid captured by said absorbent component to egress said disposable absorbent product . 35. A disposable absorbent product as defined in claim 33, wherein said product is selected from the group consisting of sanitary napkin, diaper, adult incontinence brief, urinary pad, wound dressing, nursing pad and desiccant for packaging materials. 36. A method for manufacturing a liguid absorbent component, said method comprising the steps of: - providing a first zone of particulate material having a multiplicity of lnter-partlcle and intra-particle interstices, said first zone having a first average interstice size; - providing a second zone of particulate material having a multiplicity of lnter-particle and intra-particle interstices, said second zone having a second average interstice size, said first interstice size being larger than said second interstice size; and - establishing an intimate fluid communicative relationship between said zones to allow liguid in said first zone to migrate toward said second zone. 37. A method for manufacturinq a highly absorbent structurally integral sheet having superposed liguid-absorbent layers united in an intimate fluid-communicative relationship, said method comprising the steps of: - laying in a superposed relationship and in physical contact a first slurry layer of particulate material and a second slurry layer of particulate material to form a laminated composite slurry layer, said first and second slurry layers including effective amounts of sphagnum moss particles, i) said first slurry layer constituting a precursor phase of a first porous network having a multiplicity of lnter-particle Interstices and intra-particle Interstices admitting passage of liguid, said first porous network having a first average interstice size, 11 ) said second slurry layer constituting a precursor phase of a second porous network having a multiplicity of lnter-particle interstices and intra-particle interstices admitting passage of liguid, said second porous network having a second average interstice size, said first average interstice size being larger than said second average interstice size,- - extracting fluidizing medium from said laminated composite slurry layer to form a laminated composite web including superposed layers of said first porous network and said second porous network which are intimately united to one another, said second porous network manifesting a higher capillary attraction than said first porous network to induce liguid absorbed in said first porous network to migrate toward said second porous network. 38. A method as defined in claim 37, wherein said first slurrv layer has a larger sphaqnum moss particle size median than said second slurry layer. 39. A method as defined in claim 38, wherein said first slurry layer has a sphagnum moss particle size median in the range from about 2øøø microns to about 5øø microns. 40. A method as defined in claim 38, wherein said second slurry layer has a sphagnum moss particle size median in the range from about 500 microns to about 15ø microns. 41. A method as defined in claim 37, comprising the step of incorporating in said first porous network an effective amount of debonding component . 42. A method as defined in claim 41, comprising the step of Incorporating said debonding component in said first slurry layer. 43. A method as defined in claim 42, wherein said debonding component has a fibrous identity. 44. A method as defined in claim 43, comprising the step of incorporating in said first slurry layer cross-linked cellulosic fibers in the range from about 5% to about 75% by weight of solids in said first slurry layer. 45. A method as defined in claim 37, further comprising the step of incorporating in said laminated composite slurry layer a fibrous component selected from the group consistlno of rayon, polyester, nylon acrylic, Kraft wood pulp, mechanical wood pulp, cotton linters and mixtures thereof. 46. A method as defined in claim 37, comprising the steps of: - laying one of said slurries on a foramlnous member; - laying the other of said slurries on said one slurry to form said laminated composite slurry layer,- and - establishing a pressure differential across said laminated composite slurry layer to extract fluidizing medium therefrom. 47. A method as defined in claim 37, comprising the steps of: - providing a mother slurry of sphagnum moss particles; and - classifying the sphagnum moss particles in said mother slurry in fractions according to size to provide said first and second slurrv layers. 48. A method for manufacturing a laminated liquid-absorbent article, comprlslnq the steps of: - providing a body of particles suspended in fluid, such as liguid or gas, said particles having varying dimensions; - separating said body of particles in at least two fractions, referenced as a first fraction and a second fraction, said first fraction having a higher particle size median value than said second fraction; - extracting fluidizing medium from said fractions to form a first absorbent layer and a second absorbent layer respectively, said first absorbent layer having a higher average inter-particle interstice size than said second absorbent laver, wherebv said second absorbent layer manifests a higher capillary attraction than said first absorbent layer; - establishing a liguld-communicative relationship between said layers, whereby liguid introduced in said first layer is Induced to migrate toward said second layer under the effect of capillary attraction. 49. An apparatus for manufacturing a hiqhly absorbent structurally inteqral article havinq superposed liquid-absorbent layers united in an intimate fluid-communicative relationship, said apparatus comprising: - a classifier for separating particles suspended In fluidizing medium into at least two slurry fractions in accordance to size of said particles, a first slurry fraction having a larger particle size median than a second slurry fraction, said classifier having first and second outlets for discharging said first and second slurry fractions, respectively; - a foramlnous member; - first and second headboxes in a fluid communicative relationship with said first and second outlets respectively for discharging said first and second slurry fractions in a superposed relationship on said foramlnous member to form a laminated composite slurry layer; and - means for establishing a pressure differential across said laminated composite slurry layer to extract fluidizing medium from said first and second slurry fractions in order to form respective first and second porous networks intimately united to one another, said second porous network manifesting a higher capillary attraction than said first porous network to Induce liguid absorbed in said first porous network to migrate toward said second porous network. 50. An apparatus as defined in claim 49, wherein said particles include sphagnum moss, said classifier station producing the first slurrv fraction with sphagnum moss particle size median in the range from about 2000 microns from about 50ø microns. 51. An apparatus as defined In claim 49, wherein said particles include sphagnum moss, said classifier station producing the second slurry fraction with a sphagnum moss particle size median in the range from about 5øø microns to about 15ø microns. 52. A liguid-absorbent article as defined in claim l, wherein said zones include material selected from the group consisting of perlite, vermiculite, expanded clay, expanded rice, crushed foam, zeolite and sphagnum moss.

Inventors: CANUEL LOUIS, ROY MARTIN, CANUEL, LOUIS, ROY, MARTIN
Applicants: JOHNSON & JOHNSON INC, JOHNSON & JOHNSON INC.
Application year: 1996
Main classification: A61F13
IPC codes: A61F13