AU638300B2 - Superabsorbent thermoplastic compositions and nonwoven webs prepared therefrom - Google Patents

Description

1"63WAft S F Ref: 46764D1 FORM COMMONWEALTH OF AUSTRALIA PATENTS ACT 1952 COMPLETE SPECIFICATION

(ORIGINAL)

FOR OFFICE USE: Class Int Class Complete Specification Lodged: Accepted: Published: Priority: Related Art: r U Name and Address of Applicant: Address for Service: Kimberly-Clark Corporation North Lake Street Neenah Wisconsin 54956 UNITED STATES OF AMERICA Spruson Ferguson, Patent Attorneys Level 33 St Martins Tower, 31 Market Street Sydney, New South Wales, 2000, Australia 0 4

S

Complete Specification for the invention entitled: Superabsorbent Thermoplastic Compositions and Nonwven Webs Prepared Therefrom The following statement is a full description of this invention, including the best method of performing it known to me/us 5845/3 SUPERABSORBENT THERMOPLASTIC COMPOSITIONS AND NONWOVEN WEBS PREPARED THEREFROM Background of the Invention The present invention relates to superabsorbent thermoplastic compositions, superabsorbent thermoplastic polymer blends, and to meltblown or spunbonded webs prepared therefrom.

Disposable absorbent products such as diapers, sanitary napkins, tampons, incontinence products, and the like typically are comprised of a batt or absorbent portion which is wrapped with a liner. The batt typically is .comprised primarily of cellulose fibers and the liner us-ally is a nonwoven web of a polyolefin such as polyethylene or polypropylene.

Meltblowing techniques for forming nonwoven webs or materials from the random deposition of relatively small diameter fibers from thermoplastic resins are well known in the art. For example, the production of fibers by meltblowing is described in an article by Van A. Wente, entitled, "Superfine Thermoplastic Fibers," which appeared too: t o in Industrial and Engineering Chemistry, Vol. 48, No. 8, pp. 1342-1346 (1956). The article was based on work done at the Naval Research Laboratories in Washington, D.C. See also Naval Research Laboratory Report 111437, dated April 1954. A more recent article of a general nature is Robert R. Butin and Dwight T. Lohkamp, "Melt Blowing A €0 One-Step Web Process for New Nonwoven Products", Journal of the Technical Association of the Pulp and Paper Industry, Vol. 56, No. 4, pp. 74-77 (1973).

In general, meltblowing techniques include heating a thermoplastic, fiber-forming resin to a molten state and extruding the molten resin as threads from a die having a plurality of linearly arranged small diameter capillaries.

The molten threads or filaments exit the die into a high velocity stream of a heated gas which usually is air. The heated gas serves to attenuate, or draw, the threads of molten resin to form fibers having diameters which are less than the diameter of the capillaries of the die. The fibers thus obtained usually are deposited in a random fashion on a moving porous collecting device, such as a screen or wire, thereby resulting in the formation of a nonwoven web. By way of illustration only, some specific examples of meltblowing techniques are described in U.S.

Patent Nos. 3,016,599, 3,755,527, 3,704,198, 3,84S,241 and 4,100,324.

In the past, significant efforts have been made to find ways to make disposable absorbent products more efficient or more appealing to the consumer. Much of such .J efforts have focused on increasing the absorbent capacity o of the product on a unit mass basis while at the same time increasing the ability of the product to retain absorbed 4* fluid. The ability of a product to remove and keep body fluids from the skin is perceived as a desirable attribute and is believed to be a factor in the reduction of such skin problems as diaper rash.

Such increased absorbent capacity and fluid retention 4* typically have been accomplished by incorporating a superabsorbent material into the absorbent batt. The '5 superabsorbent material usually is in particulate form.

Unfortunately, particulate superabsorbents often migrate in or fall out of the absorbent product and/or exhibit gel-blocking, a phenomenon which prevents the migration of fluid into the central portion of the superabsorbent particle. Moreover, the use of particulate superabsorbents complicates the manufacturing process and the particulate nature of the superabsorbents limits the applications for the superabsorbents.

It is expected that all of the foregoing difficulties encountered through the use of particulate superabsorbents in disposable absorbent products can be minimized or even 2 Seliminated if the superabsorbent were in the form of a nonwoven web. However, superabsorbent nonwoven webs are believed to be unknown prior to the present invention, even though there is a large body of literature relating to superabsorbents and to products into which superabsorbents have been incorporated.

Superabsorbent materials, also referred to as hydrogels, frequently are based on acrylate and methacrylate polymers and copolymers. Other hydrogels are based on starch or a modified starch. Hydrogels prepared from hydrolyzed croeslinked polyacrylamides and crosslinked a sulfonated polystyrenes or based on maleic anhydride (or 15" similar compornds) have been described. Finally, still other hydrogels are based on polyoxyalkylene glycols and include polyurethane hydrogels.

The known polyoxyalkylene glycol-based superabsorbents generally tend to come within one of the following classes, at least in so for as they are reasonably related to the present invention: crosslinked poly(oxyalkylene) glycols; crosslinked isocyanate-capped poly(oxyalkylene) glycols, polyurethanes or polyureas; polyurethanes prepared from polyfunctional prepolymers or resins and diisocyanates; polyurethanes prepared from isocyanate-capped Spolyesters or poly(oxyalkylene) glycols and difunctional extenders; polyurethanes prepared from poly(oxyalkylene) glycols, isocyanate-capped low molecular weight prepolymers, and polyfunctional low molecular weight components.

Class 1 Crosslinked Poly(oxyalkylene) Glycols U.S. Patent No. 3,783,872 describes absorbent pads containing insoluble hydrogels. The hydrogels can be 3 present in the pads as a powder or as a film. The hydrogels are comprised of crosslinked poly(alkylene oxide). Suitable materials are stated to include, by way of illustration, a poly(alkylene oxide), such as poly(ethylene oxide); poly(vinyl alcohol); poly(vinyl methyl ether); copolymers of maleic anhydride and ethylene; and copolymers of maleic anhydride and vinyl methyl ether.

The polymers are crosslinked by ionizing radiation.

An apparently preferred group of polymers includes poly(ethylene oxide), copolymers of ethylene oxide and propylene oxide, and alkyl-substituted phenyl ethers of ethylene oxide polymers in which the alkyl groups may be methyl and/or butyl.

S* The polymers which can be used also are described in terms of reduced viscosity, rather than by molecular weight. The polymers apparently can have average molecular weights of less than about 150,000 to more than about 10,000,000.

Class 2 Crosslinked Isocyanate-Capped Poly(oxyalkylene) Glycols, Polyurethanes or Polyureas U.S. Patent No. 3,939,105 describes microporous polyurethane hydrogels. The hydrogels are the reaction oe products of a poly(oxyalkylene) polyol having an average molecular weight of up to about 25,000 and organic diisocyanate which have been lightly crosslinked with water 6 or an organic amine. In practice, the polyol is reacted with the diisocyanate to give an isocyanate-capped polyol.

Before the isocyanate-capped polyol is crosslinked, a liquid nonsolvent is added thereto in an amount which will not result in precipitation. It is the addition of the nonsolvent which results in the production of the microporous hydrogel. The nonsolvent typically is an aliphatic hydrocarbon or a dialkyl ether.

4 The disclosure of U.S. Patent No. 3,939,123 is similar to that of the foregoing patent, except that a nonsolvent is not employed.

In a variation of the procedures disclosed in the two preceding patents, U.S. Patent No. 3,940,542 describes the extrusion of a solution of the isocyanate-capped poly(oxyalkylene) polyol of such preceding patents into a coagulant or crosslinking bath containing water or an organic polyamine as a crosslinking agent to produce water swellable, lightly crosslinked hydrogel polymer tapes or fibers. U.S. Patent No. 4,209,605 describes another variation in which hydrogels are produced by charging preselected feeds containing the poly(alkyleneoxy) polyol, S' diisocyanate, and catalyst to a reaction zone, extruding the resulting high viscosity polymer through a suitable die, and allowing crosslinking to take place by exposure to atmospheric humidity.

U.S. Patent No. 4,182,827 describes a method of increasing the wetting rates of the hydrogels disclosed in the above three patents. The wetting rates are enhanced by treating the surface of the solid hydrogel with certain ketones, alcohols, organic amines, aromatic hydrocarbons, or aqueous alkali metal hydroxide solutions.

e 2 Class 3 Polyurethanes Prepared from Polyfunctional Prepolymers or Resins and Diisocyanates Hydrophilic polyurethane polymers are described in U.S. Patent No. 3,822,238. They are prepared by reacting a diisocyanate with a polyfunctional prepolymer or resin.

The prepolymer or resin can be, among other things, an adduct of ethylene oxide, propylene oxide, ethylene imine, propylene amine, dioxolane, or a mixture thereof with a polyhydroxy compound; a hydroxy carboxylic acid; a low molecular weight, hydrolyzed poly(vinyl acetate), polyacrylic acid, or polymethacrylic acid; or mixtures 5 thereof. Examples of polyhydroxy compounds include ethylene glycol, propylene glycol, glycerol, trimethylolpropane, erythritol, pentaerythritol, anhydroenneaheptitol, sorbitol, mannitol, sucrose, and lactose. See also U.S. Patent No. 3,975,350 which describes a carrier system employing the hydrophilic polyurethane polymers of the first patent.

Class 4 Polyurethanes Prepared from Isocyanate-Capped Polyesters or Poly(oxyalkylene) Glycols and Difunctional Extenders Segmented urethane polymers are described in U.K.

Patent Application GB 2,154,886A. Briefly, a polyester or polyether glycol having a molecular weight of at least be** S. about 200 is reacted with an excess of organic diisocyanate to form an isocyanate-terminated prepolymer. The prepolymer then is reacted with a difunctional extender and, optionally, with a very small proportion of a monofunctional material which acts as a molecular weight regulator.

A polyether glycol apparently is preferred, such as a poly(tetramethylene ether) glycol having a molecular weight above about 600, from about 800 to about 5000.

2 The diisocyanate usually is an aromatic diisocyanate such as 4,4'-diphenylmethane diisocyanate and toluene diisocyanate. An excess of diisocyanate is employed, e.g., from about 1.2 to about 1.9 moles of diisocyanate per mole of glycol.

The difunctional extender h.as two groups which are reactive with isocyanates. The extender can be a diol, an amine having at least one amino hydrogen per amino group, or water. Examples of suitable extenders include water, 1,4-butanediol, diethylene glycol, ethylene glycol, ethylenediamine, diphenylmethane diamine, 1,3-cyclohexylene diamine, 1,4-cyclohexylene diamine, and the like.

6 Similar polymers are described in U.S. Patent Nos.

2,929,800, 2,929,804, 3,428,711, and 3,557,044.

Class 5 Polyurethanes Prepared from Poly(oxyalkylene) Glycols, Isocyanate-Capped Low Molecular Weight Prepolymers, and Polyfunctional Low Molecular Weight Components A poll .rethane similar to the polyurethane hydrogels described above is disclosed in U.K. Patent Application GB 2,157,703A. The material is described as useful for coating fabrics and clothing, with no mention of water-absorbing properties. According to the reference, the polyurethane is formed from a reaction mixture 6 comprising an isocyanate-terminated prepolymer, a polyol component containing at least 25 percent by weight of polyoxyethylene units based on the total weight of constituents, and a low molecular weight constituent having an active hydrogen functionality of at least two. If desired, the viscosity of the reaction mixture can be increased by adding one or more additional low molecular weight constituents having a functionality of at least two and preferably three; in the preferred case, it is clear that the additional constituent is functioning as a crosslinking agent.

The prepolymer is formed from the reaction product of >a polyisocyanate containing at least two isocyanate groups per molecule with a low molecular weight component having an active hydrogen functionality of at least two. Such component can be a diamine, dihydrazide, diamide, diol, dithiol, dicarboxylic acid, disulfonic acid, or a mixture thereof. Diols are preferred, with representatives examples including thiodiglycol, ethylene glycol, diethylene glycol, and 1,4-butanediol. Trifunctional compounds can be included, such as trimethylolpropane, diethylenetriamine, and compounds having two or more 7 ydifferent types of functional groups. Preferably, such low molecular weight component has a molecular weight of not more than 200.

The polyisocyanate used to prepare the prepolymer can S be any of those known to be useful for preparing polyurethanes. Examples include toluene-2,4-diisocyanate, toluene-2,6-diisocyanate, mixtures of the foregoing two compounds, 1,6-hexamethylenediisocyanate, diisocyanate, 4,4'-diphenylmethanediisocyanate, 1,4-cyclohexanediisocyanate, 1,4-phenylenediisocyanate, m- and p-tetramethylxylydiisocyanates and mixtures thereof, isophoronediisocyanate, and 4,4'dicyclohexylmethanediisocyanate. The last two compounds are preferred.

4 The polyol component contains at least 25 percent polyoxyethylene units. The preferred polyoxyethylene- 0e 6 containing compound is a polyethylene glycol having a Smolecular weight of from about 400 to about 2000. Other suitable compounds include block copolymers of ethylene oxide with other 1,2-alkylene oxides, such as propylene oxide and butylene oxide; and copolymers formed by reaction of ethylene oxide with polyols, polyamines, and polythiols.

The polyol component may consist in part of substances which do not contain polyoxyethylene units, such as o. polyester polyols and polyether polyols. Examples of the 25 former include polycaprolactone diols and polyesters t prepared from a dicarboxylic acid such as oxalic, maleic, succinic, adipic, suberic, sebacic, and the isomeric phthalic acids and a polyol such as ethylene glycol, diethylene glycol, 1,4-butanediol, 1,6-hexanediol, mixtures thereof, glycerol, trimethylolpropane, pentaerythritol, sorbitol, and sucrose. An example of the latter, which is preferred, is polytetramethylene glycol.

The low molecular weight constituent in general can be the same type of compound as the low molecular weight component already described.

8 If desired, crosslinking agents such as trilsocyanates and melamine-formaldehyde resins also can be employed.

Summary of the Invention A method of preparing a superabsorbent, thermoplastic polymeric composition is provided. The method comprises: reacting a first compound with a second compound at a temperature of from 50 to 200 degrees C for a time sufficient to effect essentially complete reaction; and 4* 9 9 9.

9 99 99 4 o e t 9 rhk/0296E 10 reacting with the product from step A a third compound at a temperature of from 80 to 200 degrees C for a time sufficient to obtain a melt flow rate of less than 1,000 g per 10 minutes; in which said first compound is a difunctional poly(oxyethylene) having a weight average molecular weight of from 5,000 to 50,000; said second compound is an aliphatic, cycloaliphatic, aromatic, or heterocyclic compound having two functional groups which are reactive with the functional groups of said first compouid; the mole ratio of said second compound to said first compound is in the range of from 2 to 100; said .5

C

S

rhk/0296E 11 third compound is an aliphatic, cycloaliphatic, aromatic, heterocyclic, or polymeric compound having two functional groups which are reactive with the functional groups of said second compound; the reaction product of said first compound with said second compound, excluding excess second compound, is from 86 to 98 percent by weight of the final composition; and said third compound plus the excess of said second compound are from 2 to 14 percent by weight of the final composition; in which the functional groups of said second compound and said third

B..

compound independently are selected from the group consisting of hydroxy, .O carboxy, amino, epoxy, imino, and isocyanate groups, with the selection of a *0

B

B*

f ft Bo rhk/0296E 12 all such functional groups being such that said superabsorbent, thermoplastic polymeric composition contains linkages selected from the group consisting of urethane, amide, ester, and secondary urea linkages; and the melt flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2,0955 0.0051 mm.

There is also provided a method for forming a supe'absorbent article which comprises: *0 o 4 g.* 4 6 O 4

*S

rhk/0296E 13 heating a superabsorbent, thermoplastic polymeric composition to a temperature in the range from about the temperature at which the melt flow rate of the superabsorbent is at least 20 g per 10 minutes to the temperature at which significant degradation of K' composition begins to occur; and forming the heated composition; In which the melt flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2.0955 0.0051 mm.

e* e 0

*O

S

•8 rhk/0296E 14 In another embodiment of the invention, there is provided a method for making a nonwoven superabsorbent web which comprises: heating a superabsorbent, thermoplastic polymeric composition to a temperature in the range from about the temperature at which the melt flow rate of the superabsorbent is at least 20 g per 10 minutes to the temperature at which significant degradation of the composition begins to occur; and

'S

ee

*SS

S**

9.

S S 06 S 9 9

S

rhk/0296E 15 extruding the heated composition through a plurality of extrusion orifices into a gas stream to form a gas-borne stream of a plurality of substantially identically prepared monofilaments which are attenuated by the gas stream; and substantially randomly depositing the stream of monofilaments on a porous collecting screen to form a nonwoven web; in which the melt flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2,0955 0.0051 mm.

Q 4 b8 S

S.

O

4 6 00.

6 0 6 s t rhk/0296E Detailed Description of the Invontion Although the term "superabsorbent" has been used rather loosely in the prior art, the term is used herein to mean that the composition absorbs at least about 10 g of water per g of composition (10 g/g).

The superabsorbent articles of the present invention have broad application in the preparation of disposable absorbent products. The methods of the present invention have broad application in the forming of superabsorbent articles by any saitable method. Suitable methods include, by way of illustration only, molding, such as injection s molding; extrusion, such as continuous melt extrusion to form films or fibers; and the like. A particularly useful method is the meltblowing of a thermoplastic superabsorbent to form a superabsorbent nonwoven web.

In general, the nature of the superabsorbent, thermoplastic polymeric composition is not kncwn to be critical, provided that it otherwise meets the criteria set forth herein. Preferred compositions are those of the present invention described hereinafter. Especially preferred are the superabsorbent thermoplastic polyurethanes described herein. Such especially preferred polyurethanes were used in the examples of the present ,disclosure.

o The superabsorbent, thermoplastic polymeric composition of the present invention comprises a soft segment and a hard segment, each segment being described herein in terms of segment constituents or composition and by general formula.

The soft segment typically comprises from about 86 to about 98 percent by weight of the total composition.

Preferably, the soft segment comprises from about 90 to about 97 percent by weight, and most preferably from about 95 to about 97 percent by weight, of the total composition.

16 SIn general, the soft segment is based on a first compound having a weight average molecular weight of from about 5,000 to about 50,000. Preferably, the molecular weight *of th first compound will be in the range of from about 8,000 to about 50,000, more preferably from about 8,000 to about 30,000, and most preferably from about 8,000 to about 16,000.

More particularly, the first compound is a difunctional poly(oxyethylene). The functional groups can be any group which will react with a second compound to give urethane, amide, ester, or secondary urea linkages, with urethane linkages being preferred. Examples of suitable functional groups include hydroxy, carboxy, amino, 2. epoxy, imino, isocyanate, and the like. Preferably, both groups will be the same, and most preferably, both groups will be hydroxy groups.

10 When both functional groups of the first compound are hydroxy groups, the first compound will be a poly(oxyethylene) diol which is most preferred. Other functional groups can be present, however, either through e. direct synthesis or by reacting a poly(oxyethylene) diol Sa* 0*40 with a modifier, with the latter procedure being preferred.

e However, a modifier does not have to introduce functional o* groups other than hydroxy groups. By way of illustration, 5 a diol will be obtained upon reacting a poly(oxyethylene) diol with propylene oxide or a hydroxy-substituted carboxylic acid.

The use of a modifier involves procedures already known to those having ordinary skill in the art. To illustrate further, reacting a poly(oxyethylene) diol with ethylenimine will give a poly(oxyethylene) diamine. A diamine also will be obtained upon reacting the diol with an amino-substituted carboxylic acid. For convenience, a first compound obtained from the use of a modifier will be referred to herein as a modified poly(oxyethylene) diol, even though the functional groups present may not be 17 hydroxy groups. Such term also is meant to include a poly(oxyethylene) having two functional groups other than hydroxy which was prepared by means other than through the use of a modifier. Similarly, the term "poly(oxyethylene) diol" is not to be limited to a diol which is the polycondensation product of ethylene oxide; rather, the term includes any diol composed substantially of a plurality of oxyethylene units, including a diol prepared by covalently coupling together two or more molecules of a poly(oxyethylene) diol by means of a coupling reagent, such as a diisocyanate.

The soft segment comprises the reaction product of first compound with second compound; excess second compound which may he present is not a part of the soft segment.

Thus, the soft segment is a second compound-terminated o poly(oxyethylene). The linkages by which the first compound is covalently bound to the second compound will be selected independently from the group consisting of urethane, amide, ester, and secondary urea linkages.

Preferably, such linkages will be the same, and most preferably such linkages will be urethane linkages.

The second compound can be any compound having two .functional groups which are reactive with the functional groups of the first compound to give urethane, amide, .5 ester, and secondary urea linkages, provided only that the properties of the resulting soft segment are not significantly adversely affected by the choice of second compound. Thus, the second compound can be aliphatic.

cycloaliphatic, aromatic, or heterocyclic. Moreover, for any given first compound functional group, one having ordinary skill in the art will be able to select appropriate functional groups for the second compound.

As already noted, the reaction between the first compound and the second compound preferably will result in the formation of urethane linkages. Since the preferred functional groups of the first compound are hydroxy groups, 18 U it follows that the preferred functional groups of the second compound are isocyanate groups. Thus, the most preferred second compounds are diisocyanates.

By- way of illustration only, suitable diisocyanates which can be employed as the preferred second compound include toluene-2, 4-diisocyanate, toluene-2,6-diisocyanate, ethylidene diisocyanate, propylene-l, 2,-diisocyanate, cyclohexylene-1,2-diisocyanate, cyclohexylene-l, 4-diisocyanate, m-phenylene diisocyanate, 4,4' -biphenylene dilsocyanate, 3,3' -dichloro-4,4 '-biphenylene diisocyanate, 1, 4-tetramethylene diisocyarnate, 1, 6-hexamethylene diisocyanate, 1, 10-decamethylene diisocyanate, xylene diisocya- V* nate, chlorophenylene diisocyanate, diphenylmethane-4 0~ **.4'-diisocyanate, naphthalene-l 1,5-diisocyanate, cumene-2,4- 605 diisocyanate, 4-methoxy-1 ,3-phenylene diisocyanate, **too "4-chloro-l, 3-phenylerie diisocyanate, 4-brumo-l ,3-phenylene ".60066 diisocyanate, 4-ethoxy-l,3-phenylene diisocyanate, 2,4-di- 11000,isocyanatodiphenyl ether, 5,6-dimethyl-1,3-phenlylene *see diisocyanate, 2 ,4-dimethyl-l ,3-phenylene diisocyanete, 4,4' -diisocyanatodiphenyl ether, benzidine diisocyanate, xylene-alpha, alpha' -diisothiocyanate, 3,3' -diaet'byl-4, 4'biphenylene diisocyanate, 2,2' ,5,5 '-tetramethyl-4,4' -bi- ~:,phenylene diisocyanate, 4,4' -methylenebis (phenyliocyanate), 4,4'-'sulfonylbis(phenylisocyanate) 4,4'-methylene S di-o-tolylisocyanate, 1 ,4-bis (2-isocyanatoisopiropyl) benzene, ethylene diisocyanate, trimethylene diisocyanate, mixtures thereoZ, and the like.

The most preferred second Compounds are tolue-ne-2,- 4-diisocyanate, toluene-2 ,6-diisocyanate, mixtures of toluene-2 and toluene-2,E-diisocyanates, 4, 4'-methylenebis(phenylisocyanate), and 1,6-hexamethylene diisocyanate.

The hard segment generall.y comprises from about 2 to about 14 percent by weighti of the total composition.

Preferably, the hard segment comprises from about 3 to about 10 percent by weight and most preferably from about 3 to about 5 percent by weight, of the total composition.

19 The hard segment must have a melting point above ambient temperature and below the temperature at which decomposition of either the composition or the soft segment takes place. In addition, the hard segment must be essentially insoluble in water and must phase separate from the soft segment.

The hard segment is selected from the group consisting of polyurethanes, polyamides, polyesters, polyureas, and combinations thereof. The hard segment can be polymeric ab initio or prepared in situ by the reaction between second compound and a third compound. Regardless of how the nard segment is prepared, polyurethanes are preferred. Most preferably, the hard segment is obtained by reacting second compound with a third compound.

Stated differently, the third compound can be either polymeric or monomeric. In either case, it is the reaction between the functional groups of the third compound with those of the second compound which results in the covalent linkage joining the hard and soft segments together, When the third compound is monomeric, excess second compound should be present in order for a condensation polymerization reaction to occur between the third compound and the excess second compound; such polycondensation reaction often is desired in order to obtain the appropriate properties for the hard segment.

1 As already noted, monomeric third compounds are preferred. If desired, a mixture of two or more third compounds can be employed. In addition, mixtures of one or more monomeric third compounds with one or more polymeric third compounds also are contemplated and come within the scope of the present invention.

In general, the third compound can be any compound having two functional groups which are reactive with second compound to from urethane, amide, ester, or secondary urea linkages. Thus, the third compound can be aliphatic, cycloaliphatic, aromatic, or heterocyclic.

20 The functional groups of the third compound can be any of those listed for the first compound. Preferably, the functional groups of the third compound will be of the same type as those of the first compound. Thus, the preferred functional groups of the third compound are hydroxy groups.

The most preferred third compounds are aliphatic and aromatic diols having from 2 to about 24 carbon atoms.

Examples of suitable most preferred third compounds include, among others, ethylene glycol, 1,3-propanediol, 1,2-butanediol, 1,3-butanediol, 1,4-butanediol, 1,3-pentanediol, 1,5-pentanediol, 1,6-hexanediol, 1,6-heptanediol, 1,4-dodecanediol, 1,16-hexadecanediol, resorcinol, 4-hydroxymethylphenol, 1,4-bis(2-hydroxyethyl)benzene, 1,3-bis(2-hydroxyethyl)benzene, bis(2-hydroxyethyl) terephthalate, and the like.

The superabsorbent, thermoplastic polymeric composition of the present invention car be represented by the following general formula: n- (1) in which S represents S. S. z-Z -X (Y -P-Y -X )p-Z (2)

CC

and H represents CC

C

o Z 3

-X

3

(Y

3 -X 5

-Y

4

-X

4 mZ 4 (3) wherein P reoresents a poly(oxyethylene) moiety; each of

Y

1 Y2', Y3 and Y 4 independently represents a urethane, amide, ester, or secondary urea linkage; each of X 1

X

2

X

3

X

4 and X 5 independently represents a divalent aliphatic, cycloaliphatic, aromatic, or heterocyclic group; each of Z 1

Z

2

Z

3 and Z 4 independently represents a monovalent functional group which is reactive with another 21 functional group to give a urethane, amide, ester, or secondary urea linkage; m is an integer of from 0 to about n is an integer of from about 1 to about 20; p is an integer of from about 1 to about 10; S represents from about 86 to about 98 percent by weight of the total composition and has a weight average molecular weight of from about 5,000 to about 50,000; and H represents from about 2 to about 14 percent by weight of the total composition and has a melting point above ambient temperature and below the temperature at which decomposition of either the composition or the soft segment takes place, is essentially insoluble in water, and phase separates from the soft segment, said hard segment being selected from the group consisting of polyurethanes, polyamides, polyesters, polyureas, and combinations *a thereof.

Formulas 1-3, above, necessarily represent the ideal.

For example, formula 1 does not include the terminal moieties. In addition, because not all of the polymer molecules have the same length (or molecular weight), the values for m, n, and p rarely are whole numbers; such values typically are expressed as decimal fractions which represent average values. Consequently, the term "integer" as used herein is meant to include both whole numbers and decimal fractions.

According to formulas 2 and 3, each of the first, second, and third compounds can have two different functional groups. As a practical matter, however, this rarely will be the case Consequently, typically X 1

X

2

Y

1

Y

2

Z

1 X2 3 Y Y 4 and Z 3

Z

4 Moreover, usually X 5

X

1 and Y3 Under these circumstances, 22 formulas 2 and 3 can be rewritten as formulas 4 and respectively: Z 1 -(Y1-P-Y 1 1)p-Z 1 (4)

Z

3

-X

3 -X -Y-X 3 )m-Z 3 It should be apparent to one having ordinary skill in the art that the terminal moieties of the polymeric composition can be either soft segment or hard segment.

When the terminal moieties are soft segment, formulas 4 and can be combined to give formula 6: *9 Sz-[ (P-YI-X-Y p-X (Y-X1-Y-X3 mn 1 1-P-Y-X1 1(6 Similarly, formula 7 results when the terminal moieties are hard segment: a see Z 3 3 (YI-X-Y -X 3 m- [Y 1 (P-Y-X-Y p-X 3

(Y

1 -X -Y 1 3 )m]n-Z 3 (7) There necessarily is a relationship between the molecular weight of the soft segment (or first compound) and the amount of hard segment which is present in the .25 composition. The amount of hard segment present in turn is partly a function of the value of Tm, the number of repeating units in the hard segment. The amount of hard segment present in the composition also is a function of e"'e the mole ratio of soft segment to hard segment. Thus, the mole ratio of soft segment to hard segment can vary from 2 to 0.5. Mole ratios of 2 and 0.5 will result in compositions represented by formulas 6 and 7, respectively.

Mole ratios greater than 2 or less than 0.5 will result in the presence in the composition of unreacted soft segment or unreacted hard segment, respectively.

23 M These relationships are illustrated for compositions based on a poly(oxyethylene) diol, 4,4'-methylenebis- (phenylisocyanate), and 1,4-butanediol, compositions representative of those prepared in the examples. The relationships are summarized in Tables 1-6, inclusive, which show the percent hard segment present in the composition for a soft segment of a given molecular weight and different values of m at each of three soft segment hard segment mole ratios. The soft segment and hard segment molecular weights were calculated from formulas 2 and 3, respectively.

Table 1 *9 Percent Hard Segment in Compositions Based on 8,500 M.W. Soft Segment Percent Hard Segment S:H Mole Ratio Value of m 2 1 0 0.5 1.0 2.1 1 2.5 4.8 9.2 2 4,3 8.3 15.3 :25 3 6.1 11.6 20.7 s.

4 7.9 14.6 25.4 9.5 17.4 29.6 6 11.1 20.0 33.4 7 12.7 22.5 36.8 8 14.2 24.8 39.8 24 Table 2 Percent Hard Segment in Compositions -Based on 14,500 M.W. Soft Segment Percent

S:H

Value of m eq 4Se Sq Sq Spq *Osq 5

C

*5

S.

S. 0..q 2 0.3 2.6 3.7 4.8 5.8 6.8 7.8 10.7 14.3 Hard Segment Mole Ratio -1 0.6 2.9 5.0 7.1 9.1 11.0 12.8 14.6 19.4 25.1 1.2 5.6 9.6 13.3 16.7 19.8 22.7 25.4 3 2. 40.1 s *egq

S

SI Table 3 Percent Hard Segment in Compositions Based on 16,750 M.W. Soft Segment Percent Hard Segment S:H Mole Ratio SO 55 5

S

*Ssesq 5 5 Value of m 0 1 2 3 2 0.3 1.3 2.2 3.2 4.1 5.1 0.5 2.5 4.4 6.2 8.0 9.7 11.3 1. 1 4.9 8.4 11.7 14.*8 17.6 20.3 25 -0 6.9 7.7 11. 1 14.2 12.9 14.4 19.9 24.8 22.8 25.1 33.2 39.8 Table 4 Percent Hardi Segment in Compositions Based on 28,750 M.W. Soft Segment 2 fees $solo.

6: 98 309 359 Value of m.

0.2 0.7 1 .3 1. 9 2. 5 3.,0 3.6 4.1 5.7 7.8 12.5 14.3 Percent Hard Segment S:H Mole Ratio -1 0.3 1.5 2.6 3.7 4.8 5.9 6.9 7.9 10.8 14.4 22.3 25.1 2.9 5.1 7.2 9.2 11 .1 12.9 14.7 19.5 25.2 36.5 40.1 26 4 Table Percent Hard Segment in Compositions -Based on 33,250 M.W. Soft Segment Per cent

S:H

't v O R

O

Value of m 0 1 2 3 4 6 8 12 16 33 2 0.1 0.6 1.1 1.6 2.1 3.1 4.1 5.9 7.7 13.4 14.5 Hard Segment Mole Ratio -1 0.3 :1.3 2.3 3.2 4.2 6.0 7.8 11.1 14.3 23.6 25.4 4.4 6.2 11.4 14.5 20.1 25.0 38.2 40.5 0 0~ Table 6 Percent Hard Segment in Compositions Based on 50,500 M.W. Soft Segment 0* 66 4

S

*9@ee* S Percent Hard Segment S:H Mole Ratio Value of m 2 0.1 0.4 0.8 1.4 2.1 2.7 -1 0.2 0.8 1.5C 2.,8 4.0 5.3 0.4 1.7 5.4 7.8 10.0 27 W 24.0 7.6 14.2 6.4 12.0 21.4 24 7.6 14.0 24.6 11.9 21.3 35.2 50 14.4 25.2 40.2 To the extent desired, simil.ar calculations can be made for any combination of soft segment or first compound, second and third compounds, value of m, and mole ratio of soft segment to hard segment, thereby enabling one having ordinary skill in the art to, readily determine the mole ratios of first, second, and third compounds, and, :04, consequently, the amounts of such materials necessary to prepare a composition coming within the scope of the present invention.' By way of illustration, suppose m is selected to be three; each mole of hard segment then must contain three 96:96% moles of second compound and four moles of third compound.

Suppose further that a mole ratio of soft segment to hard segment of 1.5:1 is selected. Since each mole of soft segment must contain two moles of second compound and. one I'v 4*00 mole of first compound, the 1.5:1 S:H mole ratio requires 3 0 moles of second compound and 1.5 moles of first compound per mole of hard segment. Consequently, the reaction will *2 5 require 1.5 moles of first compound, 6 moles of second co~mpound, and four moles of third compound. It then becomes a simple matter to calculate the amounts of each .4 compounid required, based on the scale desired and the molecu~lar weights of thie compounds to be used. It may be noted at this point that the preferred mole ratio of soft segment to hard segment iF, about 1. Consequently, the preferred range for m~ is from 0 to about 24, From' the discussion thu far, it should be apparent that the mole ratio of soft segment to hard segment in the polymeric composition cannot be greater than 2 or less tha:a If the reaction mixture S:fl mole ratio is outside of 28 O this range, there necessarily must be present in the final reaction mixture unreacted soft or hard segment. Such a result comes within the scope of the present invention, but is not' preferred since such unreacted segments generally contribute to increased water solubility and decreased absorbence of the final reaction product which typically is not purified to remove unreacted materials and/or unwanted by-products of the reaction.

As a practical matter, the permissible molecular weight ranges of the first compound and the soft segment are essentially the same since the molecular weight of the second compound is relatively small when compared with that of the first compound. Consequently, the same range is used herein for both the first compound and the soft S segment as a matter of convenience, it being understood that the range is approximate only and in reality,

S.

the range of the soft segment is slightly greater than that of the first compound as a result of the reaction between first compound and second compound.

From the discussion thus far, it should be apparent that X 1

X

2 and X 5 represent the nonfunctional group portions of second compounds and that they typically will be the same since only one second compound usually is employed. Similarly, X 3 and X 4 represent the nonfunctional 25 group portions of third compounds and X 3 and X 4 typically will be the same since only one third compound usually is employed. In addition, Z 1 and Z 2 and Z 3 and Z 4 represent the functional group portions of the second and third compounds, respectively. Furthermore, Y 1 and Y2 and Y3 and

Y

4 represent linkages which result from the reaction of the functional groups of second compounds with those of the first and third compounds, respectively. Typically, all of such linkages will be the same.

As already stated, the superabsorbent, thermoplastic polymeric composition of the present invention can be prepared by the method which comprises: 29 reacting a first compound with a second compound at a temperature of from about 50 to about 200 degrees C for a time sufficient to effect essentially complete reaction; and reacting with the product from step A a third compound at a temperature of from about 80 to about 200 degrees C for a time sufficient to obt;ain a melt index of less than about 1,000 g per 10 minutes under the test conditions described hereinafter; in which said first compound is a difunctional poly(oxyethylene) having a weight average molecular weight of from about 5,000 to about 50,000; said second compound is an aliphatic, cycloaliphatic, aromatic, or heterocyclic compound having two functional groups which are reactive with the functional groups of said first compound; t mole ratio of said second compound to said first compound is in the range of from about 2 to about 100; said third compound is an aliphatic, cycloaliphatic, aromatic, heterocyclic, or polymeric compound having two functional groups which are reactive with the functional groups of said second compound; the reaction product of said first compound with said second compound, excluding excess second compound, is N* from about 86 to about 98 percent by weight of the final o. 2 composition; and said third compound plus the excess of 25 said second compound are from about 2 to about 14 percent by weight of the final composition.

In the first step of the above method, first compound S* is reacted with second compound at a temperature in the range of fzom about 50 to about 200 degrees C for a time sufficient to effect essentially complete reaction. The reaction temperature preferably will be in the range of from about 80 to about 150 degrees C and most preferably will be in the range of from about 95 to about 120 degrees C. While reaction time is not critical, typically the reaction time will be in the range of from about 20 minutes 30 to about 3 hours when the reaction is carried out in the most preferred temperature range.

The mole ratio cf second compound to first compound should be in the range of from about 2 to about 100.

Because the hard segment must be polymeric, a larger excess of second compound relative to first compound is required when the third compound is a monomer; in such cases, the polymeric hard segment is formed in situ. If desired, however, the third compound can be a polymer. All that is required in this case is to provide sufficient second compound to covalently link first compound with third compound to give the composition of the present invention, *0 Thus, when the third compound is a monomer, the preferred mole ratio of second compound to first compound is from about 2-5 to about 50; the most preferred mole ratio is from about 2.5 to about 26. When the third compound is polymeric, the preferred mole ratio of second compound to first compound is from about 2 to about Preferably, the first compound will have a weight average molecular weight of from about 8,000 to about 50,000, more preferably from about 8,000 to about 30,000, and most preferably from about 8,000 to about 16, 000.

As already noted, the first compound most preferably is a poly(oxyethylene) diol. When such a compound is employed, the second compound most preferably is a diisocyanate and the third compound most preferably is a diol. In preferred embodiments, the first compound is a S"poly(oxyethylene) diol having a weight average molecular *as weight of from about 8,000 to about 16,000, the second compound is 4,4'-methylenebis(phenylisocyanate), the third compound is 1,4-butanediol, and the percent hard segment in the composition is in the range of from about 3 to about percent by weight of the total composition.

The second step of the method of the present invention involves reacting the product from the first step with a third compound at a temperature of from about 80 to about 31 qW 200 degrees C for a time sufficient to obtain a melt flow rate of less than about 1,000 g per 10 minutes.

Preferably, the reaction temperature will be from about to about 150 degrees C, :nd most preferably from about 110 to about 130 degrees C.

Although the use of a solvent usually is not necessary, one or more solvents may be employed in either or both steps, if desired. For example, the use of a solvent may be convenient if the viscosity of the reaction mixture in the first step is too high to allow satisfactory mixing.

In general, any solvent can be used which is not reactive with any of the components of the reaction mixture and in which the reactants are sufficiently soluble.

5 Examples of suitable solvents include, by way of illustration only, aliphatic ketones, such as acetone, I, methyl ethyl ketone, methyl propyl ketone, and the like; aliphatic esters of the lower aliphatic carboxylic acids, such as ethyl acetate, methyl propionate, butyl acetate, and the like; aliphatic ethers, such as diethyl ether, methyl propyl ether, and the like; aromatic hydrocarbons, such as benzene, toluene, the xylenes, and the like; halogenated aliphatic hydrocarbons, such as methylene chloride and the like; dioxane; tetrahydrofuran; o. dimethylformamide; N-methylpyrrolidone; and the like. The amount of solvent used is not known to be critical.

C

However, a substantial amount of solvent preferably will .not be present in the reaction mixture at the conclusion of the second step.

As already stated, the melt flow rate of the reaction mixture at the end of the second step should be less than about 1,000 g per 10 minutes. The melt flow rate value is for a solvent-free reaction mixture. The target value for the melt flow rate is largely dependent upon the use intended for the resulting composition. For example, if the composition is to be converted into a nonwoven web or 32 W fabric, the melt flow rate should be from about 20 to about 500 g per 10 minutes, preferably from about 50 to about 400 g per 10 minutes, and most preferably from about 80 to about 300 g per 10 minutes. On the other hand, if the composition is to be extruded as a film, the melt flow rate of the final reaction mixture probably should be from about to about 30 g per 10 minutes.

The melt flow rate was determined in accordance with a slightly modified version of ASTM Test Method D1238-82, "Standard Test Method for Flow Rates of Thermoplastics by Extrusion Plastometer," using a Model VE 4-78 Extrusion Plastometer (Tinius Olsen Testing Machine Co., Willow i. Grove, Pennsylvania). The modifications were as follows: the sample was predried at ambient temperature under reduced pressure prior to loading; the piston was not preheated; the sample was loaded in 2-3 minutes; and the loaded sample was preheated for 5 minutes. In every case, a 2.16 kg load was employed and the orifice diameter was 2.0955 0.0051 mm.

As already noted, the stable, nonreactive, thermoplastic polymer blend comprises from about 10 to eoe* about 95 percent by weight of a superabsorbent, thermoplastic polymeric composition and from about 90 to 6 about 5 percent by weight of at least one thermoplastic "25 polymer. The level of polymeric composition present in the blend preferably will be in the range of from about 30 to about 90 percent by weight, and most preferably will be in the range of from about 40 to about 75 percent by weight.

As used herein, the phrase "stable, nonreactive thermoplastic polymer blend" means that: the blend is stable at temperatures ranging from ambient temperature to the maximum temperature at which the blend may be melt processed; the components of the blend do not react to a significant extent with each other; and the blend is capable of being melt processed without significant decomposition or other deleterious effects. The term 33 W "stable" has reference primarily to chemical stability; it excludes phase separation in so far as any phase separation which may occur does not have a significant deleterious effect on the melt processability of the blend.

Stated differently, phase separation is permissible if it does not have a significant deleterious effect on the melt processability of the blend. Phase separation can occur at the melt processing temperature or at lower temperatures. In fact, the components of the blend need not form a homogeneous mixture at any stage of melt processing.

In addition to a superabsorbent, thermoplastic polymeric composition, the blend also contains at least one thermoplastic polymer. The thermoplastic polymer can be any thermoplastic polymer which will result in a stable, nonreactive, thermoplastic polymer blend.

Examples of thermoplastic polymers include, by way of illustration only, end-capped polyacetals, such as poly- (oxymethylene) or polyformaldehyde, poly(trichloroacetaldehyde), poly(n-valeraldehyde), poly(acetaldehyde), poly(propionaldehyde), and the like; acrylic polymers, such *oo* as polyacrylamide, poly(acrylic acid), poly(methacrylic acid), poly(ethyl acrylate), poly(methyl metha(rylate), and 0O the like; fluorocarbon polymers, such as poly(tetrafluoro- *25 ethylene), perfluorinated ethylene-propylene copolymer, ethylene-tetrafluoroethylene copolymer, poly(chlorotrifluoroethylene), ethylene-chlorotrifluoroethylene 0* copolymer, poly(vinylidene fluoride), poly(vinyl fluoride), and the like; polyamidez, such as poly(6-aminocaprioc acid) or poly( -caprolactam), poly(hexamethylene adipamide), poly(hexamethylone sebacamide), poly(ll-aminoundecanoic acid), and the like; pplyaramides, such as poly(imino-1,3phenyleneiminoisophthaloyl) or poly(m-phenylene isophthalamide), and the like; parylenes, such as poly-p-xylylene, poly(chloro-p-xylylene), and the like; polyaryl ethers, such as poly(oxy-2,6-dimethyl-1,4-phenylene) or poly(p- 34 phenylene oxide), and the like; polyaryl sulfones, such as poly(oxy-1,4-phenylenesulfonyl-1,4-phenyleneoxy-1,4-phenylene-isopropylidene-1,4-phenylene), poly(sulfonyl-1,4phenyleneoxy-1,4-phenylenesulfonyl-4,4'-biphenylene), and the like; polycarbonates, such as poly(bisphenol A) or poly(carbonyldioxy-1,4-phenyleneisopropylidene-1,4-phenylene), and the like; polyesters, such as poly(ethylene terephthalate), poly(tetramethylene terephthalate), poly(cyclohexylene-1,4-dimethylene terephthalate) or poly(oxymethylene-1,4-cyclohexylenemethyleneoxyterephthaloyl), and the like; polyaryl sulfides, such as poly(Ephenylene sulfide) or poly(thio-1,4-phenylene), and the like; polyimides, such as poly(pyromellitimido-1,4g phenylene), and the like; polyolefins, such as polyethylene, polypropylene, poly(1-butene), poly(2-butene), poly(1-pentene), poly(2-pentene), poly(3-methyl-1-pentene), poly(4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly- 1,3-butadiene, polyisoprene, polychloroprene, polyacrylonitrile, poly(vinyl acetate), poly(vinylidene chloride), polystyrene, and the like; copolymers of the foregoing, such as acrylonitrile-butadiene-styrene (ABS) copolymers, 90*4 e and the like; and the like.

*The preferred thermoplastic polymers are polyolefins, with polyethylene and polypropylene being most preferred.

'Y *35 It should be apparent to those having ordinary skill in the art that the present invention contemplates blends containing two or more superabsorbent, thermoplastic 9s C.

S' polymeric compositions and/or two or more thermoplastic polymers. Furthermore, the blends of the present invention are readily obtained by known procedures.

While the blends contain at least one superabsorbent, thermoplastic polymeric composition, such blends may or may not be superabsorbent, depending upon the level and absorbency of the superabsorbent, thermoplastic polymeric composition in the blend and the availability of the polymeric composition to aqueous media.

35 W Because the composition and blend of the present invention are thermoplastic, they can be melt processed to give films, fibers, nonwoven webs, molded articles, powders, particles, rods, tubes, and the like. Such compositions are especially useful for the preparation of ncnwoven webs by meltblowing and spunbonding processes, such as those described in U.S. Patent Nos. 3,016,599, 3,755,527, 3,704,198, 3,849,241, 3,341,394, 3,692,618, and 4,340,563. Such compositions also can be used in variations thereof. For example, the compositions can be used to prepare a coformed nonwoven material as described generally in U.S. Patent No. 4,100,324. Each of the foregoing patents is incorporated herein by reference.

Thus, the formation of fibers from the compositions of the present invention by melt spinning techniques represents the area of greatest interest. As used herein, however, the term "fiber" includes not only fibers which consist solely of c composition of the present invention, but also polycomponent fibers, at least one component of which is a composition of the present invention.

Polycomponent fibers are, of course, well known in the art, the two most common examples being sheath-core fibers and side-by-side bicomponent fibc-s. By way of illustration, a sheath-core fiber could have a S .25 polypropylene core and a sheath of a composition of the present invention. Alternatively, the sheath and core polymers could be two different compositions of the present invention. In the alternative case, the core perhaps would be a higher molecular weight polymer having an absorbency lower than that of the sheath composition. Similar polymer selections also are possible with a side-by-side bicomponent fiber.

Tricomponent, and higher polycomponent, fibers are known. In such cases, one or more of the components can be a composition of the present invention.

36 SAlthough the compositions of the present invention are particularly well-suited for the formation of nonwoven webs by meltblowing and coforming, the preparation of nonwovens by other methods is contemplated and comes within the scope of the present invention. For example, continuous filaments can be produced by melt spinning techniques, collected as a tow, and converted to staple fibers.

Nonwovens then can be prepared by carding, air forming, or the like. Variations in the production of the staple fibers, such as false twisting, crimping, and the like, can be practiced, if desired.

The present invention is further described by the following examples which illustrate specific embodiments.

Such examples are not to be construed as in any way 5 limiting either the spirit or scope of the present invention. In the examples, all temperatures are in degrees Celsius and all amounts are in parts by weight, unless specified otherwise. In every case, the poly(oxyethylene) diol was dried overnight at 95 degrees C under reduced pressure in order to reduce water content to 0.01 percent by weight or less and the assembled resin kettle was heat-dried by passing a portable butane burner flame over the external kettle surfaces while purging the vessel with nitrogen.

A. Preparation of Thermoplastic Superabsorbent.

S* Example 1 A 500-ml, wide mouth, two piece resin kettle with ground glass flanges and a four-necked cover was charged with 203 g (0.025 mole) of a poly(oxyethylene) diol having a molecular weight of 8,000 (CARBOWAX® PEG-8,000, Union Carbide Corporation, South Charleston, West Virginia) and 19.5 g (0.078 mole) of 4,4'-methylenebis(phenylisocyanate) (Eastman Kodak Co., Rochester, New York). The cover was 37 W attached and fitted with a nitrogen inlet, thermometer, condenser, and high torque mechanical stirrer (Caframa, Type RZR50, CSA® Wiarton, Ontario, Canada; Fisher Catalog No. 14-500, Fisher Scientific, Pittsburgh, Pennsylvania).

The kettle was flushed with nitrogen and maintained under a nitrogen atmosphere. The reaction mixture was heated to 100 degrees over a onr-hour period an'i maintained at that temperature with stiiring for one hour. The kettle then was charged with 4.8 g (0.053 mole) of 1,4-butanediol T. Baker Chemical Co., Phillipsburg, New Jersey).

Stirring and heating at 100 degrees were continued for about 15 minutes, during which time the viscosity of the reaction mixture increased to the point where the mixture began to climb up the shaft of the stirrer. The reaction mixture was cooled, removed from the kettle, and stored.

The resulting composition consisted of 94.8 percent by weight soft segment and 5.2 percent by weight hard segment, calculated as follows: from formula it is seen that o the weight of soft segment is approximately equal to the 2.0 amount of first compound or poly(oxyethylene) diol plus an amount of second compound or diisocyanate which is equal to twice the molar amount of first compound. The remaining amount of second compound plus third compound or 1,4-butanediol constitutes the weight of hard segment.

Since 0.025 mole of first compound was employed, the weight of second compound which must be added to the weight of @0 first compound is 0.05 mole x 250 g/mole or 12.5 g. Thus, the weight of soft segment is 203 g plus 12.5 g, or 215.5 g, while the weight of the composition must equal the sum 2* *3 of the weights of the components, or 227.3 g.

Consequently, the percent of soft segment present in the composition is equal to (215.5 x 100)/227.3, or 94.8 percent. The remainder, of course, is hard segment.

38 Example 2 The procedure of Example 1 was repeated, except that the second stage or step B reaction time was 240 minutes.

The final reaction mixture viscosity was comparable to that of Example 1. As with Example 1, the composition consisted of 94.8 percent by weight soft segment and 5.2 percent by weight hard segment.

Example 3 The procedure of Example 1 was repeated, except that the initial kettle charge consisted of 214 g (0.015 mole) of a poly(oxyethylene) diol having a molecular weight of 14,000 (CARBOWAX® PEG-14,000, Union Carbide Corporation, South Charleston, West Virginia) and 10.5 g (0.042 mole) of the diisocyanate, the amount of 1,4-butanediol was 2.43 g (0.027 mole), and the second stage or step B reaction time was 83 minutes. The composition obtained consisted of 97.3 percent by weight soft segment and 2.7 percent by weight hard segment.

b e Example 4 The procedure of Example 3 was repeated, except that the amount of the poly(oxyethylene) diol was decreased slightly to 196 g (0.014 mole), the amount of diisocyanate was increased to 14.5 g (0.058 mole), the amount of 1,4-butanediol was increased to 4.21 g (0.044 mole), and 38 the second stage or step B reaction time was 96 minutes.

The composition thus obtained consisted of 94.7 percent by weight soft segment and 5.3 percent by weight hard segment.

39 Example The procedure of Example 3 was repeated eleven times, except that a 2-1 resin kettle was employed and the amounts of poly(oxyethylene) diol, diisocyanate, and 1,4-butanediol were increased four-fold to 857 g (0.061 mole), 42 g (0.168 mole), and 9.6 g (0.107 mole), respectively. In addition, the second stage or step B reaction was continued until the torque on the stirrer reached about 3.2 lb-in, at which time 10.5 g (0.14 mole) of n-butanol \as added as a molecular weight limiter. The eleven batches were labeled respectively. As with Example 3, the compositions consisted of 97.3 percent by weight soft segment and 2.7 percent by weight hard segment.

Because higher molecular weight poly(oxyethylene) diols were not available in sufficiently pure form, lower molecular weight poly(oxyethylene) diols were coupled by means of urethane linkages, the extent of coupling being controlled by the ratio of diol and diisocyanate. The H. coupling reaction in effect yields a soft segment.

*4 Consequently, the preparation of the final superabsorbent thermoplastic composition requires the addition of both second compound and third compound for the second stage or step B reaction. This coupling reaction and the subsequent formation of the final composition are illustrated by 60..

Examples 6-9, inclusive.

Example 6 A 500-ml, wide mouth, two piece resin kettle with ground glass flanges and a four-necked cover was charged with 211 g (0.0264 mole) of the poly(oxyethylene) diol employed in Example 1 and 9.9 g (0.0396 mole) of 4,4'-methylenebis(phenylisocyanate) (a 3:2 mole ratio of diisocyanate to PEG). The cover was attached and fitted as 40 O described in Example 1. The kettle was flushed with nitrogen and maintained under a nitrogen atmosphere. The reaction mixture was heated to 100 degrees over a one-hour period and maintained at that temperature with stirring for one hour. The kettle then was charged with an additional 3.3 g (0.0132 mole) of the diisocyanate and 2.4 g (0.0266 mole) of 1,4-butanediol. Stirring and heating at 100 degrees were continued for about 134 minutes, during which time the viscosity of the reaction mixture increased to the point where the mixture began to climb up the shaft of the stirrer. The reaction mixture was cooled, removed from the kettle, and stored. The resulting composition consisted of 97.5 percent by weight soft segment and 2.5 percent by weight hard segment.

The modified poly(oxyethylene) diol obtained from the first stage or step A reaction, before carrying out the next step, was composed of two molecules of the poly(oxyethylene) diol linked together by the diisocyanate.

Such modified poly (oxyethylene) diol can be :epresented 0 schematically as follows: MDI-PEG-MDI-PEG-MDI in which MDI %so* represents the diisocyanate and PEG represents the I. poly(oxyethylene) diol. Such modified poly(oxyethylene) e** diol or soft segment had a molecular weight of about 16,750.

Example 7 The procedure of Example 6 was repeated two times, except that in each case a 2-1 resin kettle was employed, '3 the initial kettle charge consisted of 845 g (0.106 mole) of poly(oxyethylene) diol and 39.6 g (0.158 mole) of diisocyanate (a 3:2 mole ratio of diisocyanate to PEG), the subsequent kettle charge consisted of 13.2 g (0.053 mole) of diisocyanate and 9.6 g (0.107 mole) of 1,4-butanediol, and the second stage or step B reaction times for the two procedures were 113 minutes and 159 minutes, respectively.

41 The two batches of polymers were labeled 7A and 7B, respectively. As with Example 6, the compositions consisted of 97.5 percent by weight soft segment and percent by weight hard segment.

Example 8 The procedure of Example 6 was repeated, except that the initial kettle charge consisted of 240 g (0.017 mole) of the poly(oxyethylene) diol employed in Example 6 and 6.4 g (0.026 mole) of the diisocyanate (a 3:2 mole ratio of diisocyanate to PEG), the subsequent kettle charge consisted of 5.3 g (0.021 mole) of the diisocyanate and 2.7 g (0.030 mole) of 1,4-butanediol, and the second stage or step B reaction time was 124 minutes. The resulting composition consisted of 96.8 percent by weight soft segment and 3.2 percent by weight hard segment.

The modified poly(oxyethylene) diol obtained from the first stage or step A reaction was composed of two molecules of the poly(oxyethylene) diol linked together by the diisocyanate. Such modified poly(oxyethylene) diol can be represented schematically as follows: MDI-PEG-MDI-PEG- "0S* MDI. Such modified poly(oxyethylene) diol or soft segment had a molecular weight of about 28,750.

Example 9 *9* The procedure of Example 6 was repeated, except that the initial kettle charge consisted of 211 g (0.026 mole) fi of the poly(oxyethylene) diol employed in Example 3 and 8.3 g (0.033 mole) of the diisocyanate (a 5:4 mole ratio of diisocyanate to PEG), the subsequent kettle charge S* consisted of 5.0 g (0.020 mole) of the diisocyaaate and 2.4 g (0.027 mole) of 1,4-butanediol, and the second stage or step B reaction time was 200 minutes. The resulting 42 composition consisted of 96.8 percent by weight soft segment and 3.2 percent by weight hard segment.

The modified poly(oxyethylene) diol obtained from the first stage or step A reaction was composed of four molecules of the poly(oxyethylene) diol linked together by the diisocyanate. Such modified poly(oxyethylene) diol can be represented schematically as follows: MDI-PEG-MDI-PEG- MDI-PEG-MDI-PEG-MDI. Such modified poly(oxyethylene) diol or soft segment had a molecular weight of about 33,250.

As already noted, Examples 6-9, inclusive, detail the preparation of soft segment followed by the in situ preparation of hard segment with the concomitant formation of the desired composition. It is possible, of course, to prepare both the soft and hard segments separately and then combine them to obtain a superabsorbent thermoplastic composition. This procedure is illustrated by Example **e Example Preparation of Hard Segment a A 50-ml, wide mouth, two piece resin kettle with ground glass flanges and a three-necked cover was charged with 9.96 g (0.1107 mole) of 1,4-butanediol T. Baker Chemical Co., Phillipsburg, New Jersey) and 13.83 g (0.0553 mole) of 4,4'-methylenebis (phenylisocyanate) (Eastman Kodak Co., Rochester, New York). The cover was attached and fitted with a nitrogen inlet, condenser, and mechanical stirrer (T-line Laboratory Stirrer, Model No. 134-2, Talboys Engineering Corp., Emerson, New Jersey). The kettle was flushed with nitrogen and maintained under a nitrogen atmosphere. The reaction mixture was heated in an oil bath to 72 degrees over ten minutes, after which a solid material formed. The resulting hard segment melted over the range 175-185 degrees.

43 ^W The hard segment was characterized by hydroxyl number in order to estimate the molecular weight of the hard segment, or the extent of coupling of diol to diisocyanate.

The hydroxyl number, which is defined as the number of milliciams of potassium hydroxide equivalent to the hydroxyl content of 1 g of sample, was determined as follows: Duplicate approximately 1.5 g samples were weighed into tared single-necked round-bottomed flasks. To each flask was added exactly 25 ml of phthalating reagent which consisted of 42.0 g of phthalic anhydride in 300 ml of freshly distilled pyridine. Each flask was fitted with a condeiser and purged slowly with nitrogel. The flasks were placed in an oil bath at 115 degrees for one hour.

Using five drops of phenolphthalein solution as the indicator, the reaction solution of each flask was titrated while hot with 0.5 N aqueous sodium hydroxide to a faint pink end-point lasting for 15 seconds. Blank samples were r.un with only the phthalating reagent. The hydroxyl number then was calculated by dividing the milliequivalents of ,0 potassium hydroxide required (corrected for the blank) by the weight of the sample. The average hydroxyl number from the duplicate runs was 270. This number is equivalent to an apparent molecular weight for the hard segment of 416.

Since the theoretical hard sengent molecular weight is 430, the hydroxyl number indicates that there probably was a slight excess of 1,4-butanediol present in the hard segment reaction mixture.

Preparation of Soft Segment %5 0 A 500-ml, wide mouth, two piece resin kettle with ground glass flanges and a four-necked cover was charged with 391.5 g (0.028 mole) of the poly(oxyethylene) diol and 13.98 g (0.056 mole) of the diisocyanate employed in Example 3. The cover was att"T hed and fitted with a nitrogen inlet, thermometer, condenser, and high torque 44 mechanical stirrer (Caframa, Type RZR50, CSA®, Wiarton, Ontario, Canada; Fisher Catalog No. 14-500, Fisher Scientific, Pittsburgh, Pennsylvania). The kettle was flushed with nitrogen and maintained under a nitrogen atmosphere. The reaction mixture was heated to 100 degrees over a one-hour period and maintained at that temperature with stirring for 231 minutes.

Preparation of Superabsorbent Thermoplastic Composition To the resulting soft segment was added 11.63 g (0.027 mole) of hard segment dissolved in about 40 ml of dry N-methyl-2-pyrrolidinone. The resulting mixture was heated at 72-82 degrees for 158 minutes to give the desired composition, the last 15 minutes being under reduced pressure to remove the solvent. The resulting composition consisted of 97.2 percent soft segment and 2.8 percent hard segment.

S

The compositions prepared in the preceding examples all are polyether urethanes based on a poly(oxyethylene) diol and an aliphatic third compound, 1,4-butanediol.

41 Moreover, in cases where the poly(oxyethylene) diol was coupled to give a modified poly(oxyethylene) diol leading to a higher molecular weight soft segment, coupling employed a diisocyanate which resulted in the formation of urethane bonds. Consequently, all of such compositions a contain only ether and urethane linkages.

As already stated, however, the compositions of the present invention are not limited to aliphatic third compounds or only to ether and urethane linkages, as *demonstrated by the next five examples.

45 Example 11 Preparation of Polyether Urethane Ester Following the procedure of Example 1, the resin kettle was charged with 212.8 g (0.0266 mole) of the poly(oxyethylene) diol employed in Example 1. As the diol was being heated to 95 degrees, 2.70 g (0.0',33 mole) of terephthaloyl chloride (recrystallized from hexane) was added to the resin kettle. Unlike the use of a diisocyanate as a coupling agent, the use of terephthaloyl chloride does not result in the formation of soft segment.

The resulting reaction mixture was heated, with stirring and under a nitrogen atmosphere, at 95 degrees for about 1,5 hours. To the kettle then was added 10.0 g (0.040 mole) of the diisocyanate employed in Example 1; the temperature of the reaction mixture now was 104 degrees.

After an additional hour, 2.40 g (0.0267 mole) of e 1,4-butanediol was added. The reaction mixture was heated for one more hour, at which time 2.0 g (0.027 mole) of n-butanol was added as described in Example 5. The resulting composition contained 97.5 percent soft segment and 2.5 percent hard segment.

Example 12 Use of a Third Compound Containing an Aromatic Group 4 The procedure of Example 1 was repeated, except that 30 the initial kettle charge consisted of 305.6 g (0.0382 mole) of the poly(oxyethylene) diol and 19.1 g (0.0764 mole) of the diisocyanate, in the second stage reaction the 1,4-butanediol was replaced with 7.56 g (0.038 mole) of hydroquinone bis(2-hydroxyethyl) ether (Eastman Kodak Co., Kingsport, Tennessee), and the second state or step B reaction time was 47 minutes. It may be noted that the 46 first compound :.second compound third compound mole ratio was 1:2:1. The resulting composition contained 97.7 percent. soft segment and 2.3 percent hard segment.

Example 13 In order to evaluate the effect of replacing the third compound used in Example 12 with the aliphatic diol employed in Examples 1-10, inclusive, the procedure of Example 12 was repeated with the same 1:2:1 mole ratio of first compound second compound third compound. Thus, the initial kettle charge consisted of 208 g (0.026 mole) of the poly(oxyethylene) diol and 13.25 g (0.053 mole) of diisocyanate, the amount of 1,4-butanediol was 2.34 g (0.026 mole), and the second stage or step B reaction time was 280 minutes. The resulting composition consisted of 98.8 percent soft segment and 1.2 percent hard segment.

The decrease in the percent hard segment relative to the composition of Example 12 is a result of the lower molecular weight of .,4-butanediol.

9.

0

O*

Example 14 Preparation of Polyether Urethane Amide Following the procedure of Example 11, the resin kettle was charged with 63.81 g (0.00798 mcle) of the poly(oxyethylene) diol employed in Example 1 and 250 ml of dry N-methyl-2-pyrrolidinone. As the reaction mixture was being heated and after the diol had dissolved, 3.99 g (0.01596 mole) of the diisocyanate employed in Example 1 S" was added to the kettle. The reaction solution was heated at 65 degrees for one hour. To the resin kettle then were added 1.17 g (0.00798 mole) of adipic acid, 100 ml of N-methyl-2-pyrrolidinone, and a catalytic amount of sodium hydride. The resulting solution was' heated at 120 degrees 47 for one hour. Films were cast from the reaction solution and air dried, followed by drying under reduced pressure at degrees. The composition consisted of 98.3 percent soft segment and 1.7 percent hard segment.

Example Preparation of Polyether Urethane Amide Following the procedure of Example 14, the resin kettle was charged with 45.02 g (0.0032 mole) of the poly(oxyethylene) diol of Example 3, 4.89 g (0.0196 mole) of the diisocyanate, and 300 ml of dry N-methyl-2-pyrrolidinone. The reaction mixture was heated to 100 degrees over a one-half hour period and maintained at that temperature for 1.5 hours. To the kettle then were added 2.40 g (0.016 mole) of adipic acid and a catalytic amount of sodium hydride. Heating was continued for an additional hour. The composition consisted of 89.1 percent soft segment and 10.9 percent hard segment.

S

The next example briefly summarizes scale-up activities with respect to certain of the compositions prepared in the preceding examples.

So Example 16 The procedure of Example 6 was repeated a number of times in 50-lb. and 200-lb. batches using appropriate *0 multiples of reactants. The second step reaction was .carried out for four hours at 130 30 dagrees. In each case, zinc octoate was added with the 1,4-butanediol at a level of 8 g zinc octoate per 1,000 lbs. of polymer. Each composition, of course, consisted of 97.5 percent by Weight soft segment and 2.5 percent by weight hard segment.

48 The compositions obtained in the above examples were characterized by a number of methods: 1. Infrared analysis A sample of the composition was mulled in Nujol. The instrument was a Perkin-Elmer Model 710B Spectrophotometer (Perkin-Elmer Corporation, Norwalk, Connecticut).

2. Proton nuclear magnetic resonance analysis (NMR).

The sample was dissolved in chloroform at a concentration of 10 percent by weight. The instrument was an IBM Instruments Model NR/250AF 250 Megahertz Spectrophotometer (IBM Corporation, Armonk, New York).

3. Elemental analysis Elemental analyses were carried out by Atlantic Microlabs, Atlanta, Georgia.

4. Inherent viscosity The apparatus employed was a Schotte Gerate KPG® Ubbelohde Viscometer (Jenaer Glasswerk Schott Gen., Mainz, Germany) with a suspended level bulb. The sample was dissolved in m-cresol at a concentration of 0.5 percent, weight per volume. The solution was filtered through a medium frit scintered glass .2 funnel and equilibrated 30 min at 30 degrees in a constant temperature bath (Canner Instrument Company, Boalsburg, Pennsylvania) before measuring the rate of flow.

5. Melting point The melting point range of the sample was determined by means of a hotbench Reichert Ag., Wien, Austria).

6. Melt flow rate (MFR) The melt flow rate was determined as described at page 31.

S* 7. Tensile strength (TS) (Ultimate Modulus).

Tensile strength was measured on film samples by means of 0 an Instron Model 1122 (Instron Corporation, Canton, S Massachusetts). Films were made in a Carver Laboratory Press, Model 2518 (Fred S. Carver, Inc., Menomonee Falls, Wisconsin) at 175 degrees and a pressure less than 100 pounds, the minimum gauge pressure reading. Since roughly 5 g of polymer was employed in each case and film thickness varied from 0.010 to 0.031 inch (0.25 to 0.79 mm), the 49 S estimated pressure range was from about 2 to about 10 psi.

The films were equilibrated at ambient temperature and humidity for at least one day. Rectangular film samples measuring 0.5 x 1.5 inch (12.7 x 38.1 mm) were cut from the films. The ends of the samples were wrapped with masking tape. The Instron grips had 1 x 1.5 inch (25.4 x 38.1 mm) smooth rubber faces. Gauge length was one inch (25.4 mm) and the crosshead speed was 2 inches (50.8 mm) per minute.

8. Thermal gravimetric analysis (TGA). Thermal gravimetric analysis employed a DuPont Model 1090 Thermal Analyzer with a Model 1091 Disc Memory and a Model 950 Thermal Gravimetric Analyzer (DuPont Instruments, Wilmington, Delaware). Each polymer sample (8-10 mg) was weighed in a tared platinum sample pan and heated to 550 degrees at 10 degrees/minute.

9. Differential scanning calorimetry (DSC). Each polymer was analyzed by differential scanning calorimetry using a DuPont Model 1090 Thermal Analyzer with a Model 1091 Disc Memory and a Model 910 Differential Scianing Calorimeter (DuPont Instruments, Wilmington, Delaware).

Polymer (about 4 mg) was weighed in a tared, non-hermetically sealed aluminum pan and cooled in the sample cell to -80 degrees with a liquid nitrogen jacket.

The sample then was heated at 10 degrees/minute to 550 degrees.

Centrifuge Absorbency and Solubility Absorbency was determined with either water (WA) or with synthetic urine (SUA). Briefly, a polymer sample was melt-pressed into a film essentially as described above in .0 method 7 (tensile strength). A film thickness of 0.0109 c*e: inch (0.28 mm) was achieved by using flat metal spacer strips and TEFLON®-coated foil. The film was cut into 1-cm squares which were weighed. Each square was placed in water or synthetic urine at ambient temperature and allowed to soak for four hours. The soaked sample was placed in a centrifuge tube adapter. The adapter had at the bottom a 50 O barrier to the sample which was permeable to the test liquid under the conditions of centrifugation. The sample then was centrifuged at 1,000 rpm (196 x G) for 30 minutes.

To the- extent possible, the sample was removed from the centrifuge tube adapter and placed in a tared aluminum weighing dish. The sample was weighed, dried for three hours at 90 degrees, and reweighed. The absorbency then was calculated in accordance with the following equation! A (wt. wet final wt. dry)/final wt. dry Thus, absorbency is the number of g of test liquid absorbed per g of sample, corrected for soluble sample. When synthetic urine was used, the final dry weight also was corrected for the solids present in the absorbed liquid.

The solubility of the test sample, expressed as a percentage, was calculated from the water absorbency data as follows: '20 S 100(initial wt. dry final wt. dry)/initial wt. dry 4 The synthetic urine test liquid contained the following compounds in the amounts shown, per liter of liquid: 0.309 g of Ca(H 2

PO

4 2

.H

2 0 0.681 g of KH 2

PO

4 0.477 g of MgSO 4 7H 0 1.333 g of KSO4 3.244 g of Na 3

P

O 4 .12H 2 0 :30 4.441 g of NaCI 3.161 g of KC1 0.400 g of NaN 3 8.560 g of urea *ee* The compounds were added in the order listed to 900 ml of distilled water in a well rinsed, chromic acid washed, 51 g-W 1000 ml volumetric flask; each compound was dissolved completely before the next one was added. Distilled water then was added to the mark. The total solids' content of the synthetic urine was 20.606 g/liter which is approximately equivalent to 2.01 percent by weight.

The IR and NMR analyses supported the structures described herein for the compositions of the present invention, as did the EA. The MP determinations gave broad ranges which were indicative of wide molecular weight distributions. The thermograms obtained by DSC showed endotherms at about 50-60 degrees and 410-430 degrees, indicating the presence of block copolymers. Finally, TGA demonstrated that the compositions are stable, at least in a nitrogen atmosphere, to about 260 degrees, in that they undergo less than one percent by weight degradation. Some of the other characterization results are summarized in Table 7; it perhaps should be noted that the preferred S' temperature for determining the melt flow rate is 195 degrees.

p Table 7 Summary of Melt Flow Rates and Absorbencies

'•I

Absorbency, g/g Water Melt Flow Example Water Syn. Urine Sol.a Rate/Temp.

1 2 14.2 12.2 23 300/1900 3 40.7 44 38 65/1400 4 39.2 48.2 45 294/1900 eo0 5A 33/1950 S* 5B 16/1950 20/1950 5D 47/195° 5E 27/1950 5F 48/1950 63/1950 52 41.9 31.7 103/195" 51 30/1950 130/1950 122/1900 6 33.7 27.7 27 90/1950 7A-- -64/1950 7B 300/1950 8 39.2 31 43 116/1950 9 50.6 41.3 49 119/1900 10 20.7 19.4 28.5 11 1 0 7 b 1 1 5 b 200/1900 12 17.7 14.6 36.2 91/1900 13 Diss. DiSs. 182/1900 14 74.7 Diss. 15 31.3 72.8 16 4314/90 0. a Percent. of sample soluble in water at ambient temperature.

b~ bMeasured with 0.5 cm or smaller chips of polymer which .9620 were soaked for approximately 24 hours.

se*0 Range of values obtained for multiple batches.

0000 Finally, the inherent viscosity and ultimate modulus were determined for each of the polymers of Examples 3 and 4. The values obtained are summarized in Table 8.

ego* Table 8 Summary of Inherent Viscosity JO and Ultimate Modulus Values Sa*Example inherent Viscosity Ultimate Modulus 3 0.572 2200 o 4 0.505 4000 53 Several of the compositions prepared in Examples 1-16, inclusive, were subjected to molecular weight determinations by means of gel permeation chromatography.

The apparatus consisted of a Beckman Model 112 Solvent Delivery System (Beckman Instruments, Inc., Fullerton, California), a Beckman Model 421 System Controller, and Waters 500, 103 and 104 Angstrom Styragel columns (Waters Chromatography Division, Millipore Corporation, Milford, Massachusetts) in chloroform, HPLC-grade (Burdick and Jackson La"--atories, Inc., a subsidiary of American Hosyital Supply Corporation, McGaw Park, Illinois), equilibrated at 30 degrees.

Sample injection consisted of 50 1 of a 0.5 percent, weight per volume, solution of the polymer in HPLC-grade l5 chloroform. The flow rate of eluant (chloroform) was maintained at 1 ml per minute. Sample peaks were detected by means of changes in the refractive index using a Waters Model 410 Differential Refractometer. The calibration curves were constructed through the use of narrow molecular weight range standards covering the range from 600 to 600,000; below about 18,000, the standards were polyethylene glycols from American Polymer Standards Corporation, Mentor, Ohio, and above about 18,000, the standards were poly(ethylene oxide) standards from Polymer *25 Laboratories, Inc., Stow, Ohio.

Data acquisition was performed with a Nelson Analytical Model 760 Interface and an IBM Personal Computer S' AT (IBM Corporation, Endicott, New York), in conjunction with Nelson Analytical GPC Software, Version 3.6 (Nelson Analytical, Cupertino, California).

In general, the manufacturers' instructions were followed. However, the most relevant data acquisition parameters were as follows: Minimum peak width 15.00 seconds Time for one sample 1.50 seconds Real time plot full scale for CH.O. 500 millivolts 54 Full scale range for A.D.C. 1 volt Area reject for reference peaks 1000.00 The results of the molecular weight determinations are summarized in Table 9.

Table 9 Summary of Results of Molecular Weight Determinationsa Ex. Peak Area Peak MW Mwb Mnc 0 0O *0*S 9O

OSS&

0 .5 0*0* 2 MPd

S

e 3 MP

S

5H MP

S

7A MP

S

8 MP

S

9 MP

S

13 MP

S

59.7 91.7 80.8 9.3 97.5 92.4 88.7 10.9 25,425 9,628 28,595 16 ,000f 34,570 16 ,000 f 37,764 10,621 32,806 16 ,000f 34,570 10,000 29,585 10,039 190,878 7,702 117,424 108,455 307,465 9,206 91,605 139,135 70,867 9..81 46,656 6,757 41,217 33,331 44,458 8,534 31,632 Mw/Mn 4.091 1.140 2.849 3.254 6.916 1.079 2.896 38,201 3.642 32,828 8,957 2.159 1.036 an each case, 0* .0

U

a main peak with a shoulder was obtained.

bWeight average molecular weight.

CNumber average molecular weight.

dMain peak.

eShoulder.

Approximate value.

Since the standards used to construct the calibration curves may not be the most appropriate standards for the 55 type of polymer studied, it can be stated only that the shoulder represents a relatively low molecular weight oligomer with a narrow polydispersity. The shoulder may represent either soft segment or hard segment which was not incorporated into the polymer. On the other hand, the main peak apparently represents a relatively high molecular weight polymer with moderate to broad polydispersity.

Because of the limited amount of data, correlation of polymer properties, such as water solubility and absorbency, with molecular weight and/or polydispersity is not possible.

B. Preparation of Meltblown Nonwoven Webs.

0@* Examples 17 22 p 0oe To determine the suitability of the compositions of S* the present invention for the formation of nonwoven webs, several of the compositions from the above examples were extruded by means of a bench-scale apparatus having a single orifice in the die tip. The apparatus consisted of a cylindrical steel reservoir having a capacity of about g. The reservoir was enclosed by an electrically heated steel jacket. The temperature of the reservoir was thermostatically controlled by means of a feedback thermocouple mounted in the body of the reservoir. The extrusion orifice had a diameter of 0.016 inch (0.41 mm) and a length of 0.060 inch (1.5 mm). A second thermocouple was mounted near the die tip. The exterior surface of the die tip was flush with the reservoir body. Polymer extrusion was accomplished by means of a compressed air piston in the reservoir. The extruded filament was surrounded and attenuated by a cylindrical air stream exiting a circular 0.075-inch (1.9-mm) gap. The forming distance was from 8 to 20 inches (20 to 51 cm). The attenuated extruded filament was collected on the clear 56 I plastic film of an 8.5 x 11 inch loose leaf protector having a black paper insert.

Examples 17-22, inclusive, consisted of six separate meltblowing experiments using the above-described bench-scale apparatus. Meltblowing conditions are summarized in Table 10. The table identifies the polymer employed (by reference to a previous Example), the temperatures of the reservoir, die tip, and air stream, the air pressure (in psig), and the forming distance in inches (cm).

Table Summary of Meltblowing Conditions Using Bench-Scale Apparatus Sb Polymer Res. Die Air Air Forming Example Example Temp. Temp. Temp. Press. Distance 17 5A 185 169 222 2 10 (25.4) 18 5B 183 173 221 1-2 10 (25.4) 19 5D&F 180 179 216 1-2 10 (25.4) 7A 164 157 192 1 10 (25.4) 21 11 227 209 264 10-15 10 (25.4) 22 12 191 196 157 7-8 17-18 25 (43.2-45.7) In each case, a coherent superabsorbent nonwoven web was obtained.

Examples 23 and 24 In'a variation of the procedures described in Examples 17-22, inclusive, two of the bench scale apparatus were oriented 90 degrees from each other. One apparatus was oriented vertically with the die tip in the downward direction and the other apparatus was oriented horizontally 57 a with the die tip facing the vertically oriented apparatus.

The straight-line distance between the two die tips was 5.75 inches (14.5 cm). Thus, the extruded filaments met at a point 4 inches (10.2 cm) from each die tip. The confluent filament stream was directed at a 45 degree angle from the vertical. The forming distance was either 4 or 12 inches (10.2 or 30.5 cm), measured from the point of confluence to the collecting arrangement. The collecting arrangement was a 400-openings/in 2 screen attached to a vacuum hose.

The vertical apparatus was charged with PF-011 polypropylene (Himont Inc. Wilmington, Delaware).

The horizontal apparatus was charged with the composition a* of Example 5 (specifically, a mixture of 5D and Two experiments were conducted. In Example 23, the 0 forming distance was 4 inches (10.2 cm) and the weight to* ratio of polypropylene to superabsorbent composition was approximately 60:40. In Example 24, the forming distance 0* S was 12 inches (30.5 cm) and the weight ratio of polypropylene to superabsorbent composition was approximately 70:30. The meltblowing conditions for these s two Examples are summarized in Tables 11 and 12, respectively.

0* 56 Table 11 Summary of Meltblowing Conditions for Example 23 Res. Die Air Air Temp_ Temp. Temp. Press.

Vertical apparatus a 173 178 226 Horizontal apparatus 156 153 157,223 b 4,12 c aThe extrusion orifice diameter was 0.010 inch (0.25 mm).

bThe air temperatu initially was 157 degrees, but was changed to 223 degrees about halfway through the experiment.

CThe air pressure initially was 4 psig, but was changed to 12 psig about one-fifth of the way through the experiment.

U Table 12 Summary of Meltblowing Conditions for Example 24 Res. Die Air Air 5 Temp. Temp. Temp. Press.

U.

Vertical apparatus a 173 177 226 Horizontal apparatus 156 158 207 12 S0 aThe extrusion orifice diameter was 0.010 inch (0.25 mm).

In each case, a coherent superabsorbent nonwoven web was obtained.

59 SExamples 25-41 Since the above bench-scale meltblowing trials were successful, many of the compositions from the examples were meltblown on a pilot-scale meltblowing apparatus, essentially as described in U.S. Patent No. 4,663,220, which is incorporated herein by reference. Meltblowing of various of the thermoplastic superabsorbent polymers of Examples 1-16 was accomplished by extruding polymer through a 0.75-inch (19-mm) diameter Brabender extruder and through a meltblowing die having nine extrusion capillaries per linear inch (approximately 3.5 capillaries per linear cm) of die tip. Each capillary had a diameter of about 0.0145 So inch (about 0.37 mm) and a length of about 0.113 inch "'1S (about 2.9 mm). The process variables in general were as follows: calculated polymer viscosity in the capillaries (in poise), polymer extrusion rate (g per capillary per min) and temperature, extrusion pressure (psig), die tip configuration which was either negative (recessed) or positive (protruding), perpendicular die tip distance, air passageway width, attenuo "Ir temperature and pressure (psig), and forming di ent' These meltblowing process variables are summarir Examples 25-41 in Tables 13-15, inclusive.

Table 13 Summary of Polymer Characteristics Using Brabender Extruder Example Polymer Example Polymer Viscositya 5D&5F 1960 26 5D&5F 2110 27 7A 1110 28 5J 698 29 5J 620 60 64 1 6A 1 6B 5K 5H&7Bb 1 6C 16GD 16E 16F 16G 16H1 605 904 241 301 243 429 738 525 219 214 939 320 In poise at the extrusion temperature.

A mixture consisting of 25 percent by weight percent by weight of 11B.

of 511 and Table 14 Suimmary of Extrusion Variables Using Brabender Extruder

S

S S S. S Example 26 27 28 29 31 32 33 34 36 Polymer Extrusion Rate Temp. Press.

0.16 186 430 0.14 187 406 0.14 178 214 0.47 189 450 0.47 188 400 0.47 188 390 0.22 188 273 0.45 190 149 0.29 190 120 0.49 190 165 0.49 190 290 0.27 190 275 Die Tip Config. Dist 0.11,0 0.110 0.110 0.110 0.110 0.110 0.110 0.110 0.110 0.110 0.010 c 61 0.50 0.35 0.51 0 .27 0.36 190 193 193 193 193 360 104 149 350 160 0.010 0.010 0.010 0.010 0.110 Perpendicular distance in inches from the plane of the air plate lips, or perpendicular die tip distance.

Or 2.8 mm.

Or 0.25 mm.

'C

C

C..

Cs a ego

C

C'

S

a eg 0u I C ~ep, Table Summary of Attenuation Variables Using Brabender Extruder Example 26 27 28 29 31 32 33 34 35 36 37 38 39 APW a 0.090Oc 0.090 0.090 0.090 0.090 0 .090 0.090 0 .090 0.090 0.090 0.090 0.060Of 0.060 0.060 0 .060 Attenuating Air Temp. Press.

412 1 412 5 427 2 432 1 432 2 420 4 430 437 0.75 435 442 433 430 0.75 427 1 428 418 1.25 Forming Distanceb 3 8 d 38 a. a.

*4 5

S

Sb *4CC C C 62 0.060 419 1.25 41 0.090 419 2.25 a a Air passageway width, in inches.

b In inches.

c Or 2.3 mm.

d Or 96.5 cm.

e e Or 63.5 cm.

Or 1.5 mm.

The collecting arrangement consisted of a rotating six-inch (15.2-cm) wide drum having a diameter of 30 inches (76.2 cm). The surface of the drum was a screen which had Sbeen coated with spunbonded polypropylene to prevent sticking of the meltblown web to the screen. The nonwoven webs were allowed to stay on the forming screen for at *e* least ten seconds to assure sufficient web integrity for removal and subsequent handling. Well formed, coherent, superabsorbent nonwoven webs were obtained.

The synthetic urine absorbencies of the meltblown webs obtained in Examples 28-39, inclusive, and Example 41 were determined by means of a saturated capacity test. The apparatus consisted of a stainless steel vacuum tank which was 28 cm high, 60 cm long, and 35 cm wide. The top of the 5 tank was a removable stainless steel grid. The grid was approximately 59.5 x 34 cm and contained approximately 84 S 2 4-mm diameter holes per 100 cm A latex rubber dam was attached to the top edge of one of the longer sides of the tank and was of a size to easily cover the grid without stretching, Evacuation of the tank was accomplished by a combination pressure/vacuum pump (Gast Manufacturing, Fisher Catalog No. 01-094, Fisher Scientific, Pittsburgh, Pennsylvania). The pump was gaged to provide a reading of the achieved pressure reduction in inches of water which was converted to pounds per square inch (psi).

63 To carry oUt the test, at least three 3-inch (7.6-cm) square samples were cut from each meltblown web; the spunbonded carrier was removed from each sample. Each sample then was dried for at least one hour at ambient temperature under reduced pressure. For each sample, two 4-inch (10.2-cm) squares were cut from a polypropylene meltblown web having a nominal basis weight of 25-34 g/m 2 Each sample and the accompanying two squares of polypropylene meltblown web were v >'ed separately.

The sample was placed on one polypropylene square and immersed, with the sample underneath the polypropylene square, for 30 minutes in a bath of synthetic urine at 37 degrees (98.6 degrees The sample was removed carefully from the bath and placed on the second polypropylene square which was on the vacuum tank grid, the sample being e sandwiched between the two polypropylene squares. After draining for one minute, the sample sandwich was weighed.

9* The sample sandwich was placed on the grid. The grid was covered completely with the rubber dam and the pressure in the tank was reduced to 0.5 psi less than atmospheric pressure; the pressure differential from one side of the sample sandwich to the other was 0.5 psi. This pressure differential was maintained for 5 minutes, after which time the sample sandwich was weighed. This procedure was repeated three additional times at pressure differentials of 1.0, 2.0, and 3.0 psi. After the sample sandwich weighing at the 3.0-psi differential, the sample was removed from the sandwich and weighed separately.

In order to calculate an absorbence at each pressure differential, it was necessary to correct each sandwich weight for the weight of the wet polypropylene squares (WPPS). This was done by subtracting the sample weight at the 3.0-psi pressure differential from the sandwich weight at the same pressure differential. The absorbence for each sample at each pressure differential then was 64 calculated as follows: A (wt. sandwich wt. WPPS wt. dry sample)/wt. dry sample Thus, the absorbence value at each pressure differential is the number of g of synthetic urine absorbed per g of sample.

The results of the saturated capacity test are summarized in Table 16. The absorbencies reported are averages of at least three samples.

Table 16 Summary of Saturated Capacity Test on Meltblown Webs from Examples 28-39, 41 a,' Vo s a.

a

S

a.

Example 0.5 psi

S..

Selli

I

r s S 2

I

19.91 23.00 25.65 25.43 9.56 11.16 11.16 7.68 15.77 17.92 12.39 15.70 17.69 Absorbency, g Syn.

1.0 psi 17.09 19.36 21.42 22.36 9.40 10.91 10.94 7.60 13.82 16.82 11.90 14.62 16.16 Urine/g 2.0 psi 15.52 18.06 19.02 19.61 9.14 10.64 10.54 7.45 12.69 16.33 11.59 13.82 14.45 14.17 16.46 16.86 17.76 8.92 10.37 10.13 7.33 11.91 15.75 11.30 13.20 13.26 3.0 psi It should be noted that the data in Tables 7 and 16, respectively, were obtained by two different test 65 procedures. Moreover, the data in Ti 7 were obtained with polymer films, whereas the data in Table 16 were obtained with meltblown webs.

Larger scale meltblowing runs were carried out, primarily to prepare coformed webs essentially as described in U.S. Patent No. 4,663,220, supra. These larger scale runs are described in Examples 42-66, inclusive, below. In each case the superabsorbent thermoplastic composition employed was that of Example 16.

Example 42 A fibrous coformed nonwoven web was formed by

W*O

meltblowing a superabsorbent thermoplastic composition of i5 the present invention and incorporating polyester staple fibers therein.

Meltblowing of the superabsorbent thermoplastic composition was accomplished by extruding the composition from a 1.5-inch (3.75-cm) Johnson extruder and through a meltblowing die having 15 extrusion capillaries per linear inch (about 5.9 extrusion capillaries per linear cm) of die tip. Each capillary had a diameter of about 0.018 inch (about 0.46 mm) and a length of about 0.14 inch (about 3.6 mm). The composition was extruded through the capillaries '2 at a rate of about 0.50 g per capillary per minute at a temperature of about 184 degrees. The extrusion pressure exerted on the composition in the die tip was in the range of from about 180 to 200 psig. The composition viscosity in the die tip under these conditions was about 500 poise.

The die tip configuration was adjusted to have a positive perpendicular die tip distance of about 0.010 inch (about 0.25 mm). The air gaps of the two attenuating air passageways were adjusted to be about 0.060 inch (about 0.15 mm). Forming air for meltblowing the composition was supplied to the air passageways at a temperature of acout 209 degrees and a pressure -f about 2 psig. The fibers 66 W thus formed were deposited on a forming screen drum which was approximately 18 inches (46 cm) below and 20 inches (51 cm) back from the die tip.

Following the procedure illustrated by Figure 5 of said U.S. Patent No. 4,663,220 and described therein, (3.75-cm) long, 15 denier per filament polyester staple was incorporated into the stream of meltblown fibers prior to deposition upon the forming drum. The polyester fibers were first formed by a Rando Webber mat-forming apparatus into e mat having a basis weight of about 100 2 g/m2. The mat was fed to the picker roll by a feed roll which was positioned about 0.007 inch (about C.18 mm) from S. the picker roll surface. The picker roll was rotating at a rate of about 3,000 revolutions per minute and fiber *1'5 transporting air was supplied to the picker roll at a pressure of about 3 psig. While actual measurement of the position of the nozzle of the coform apparatus with respect to the stream of meltblown fiber was not made, it was estimated to be about 2 inches (about 5.1 cm) below and about 2 inches (5.1 cm) away from the die tip of the meltblowing die.

A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 25 percent by weight of the :25 meltblown fibers and about 75 percent by weight of the *o* polyester fibers. The web had a basis weight of about 200 2 g/m Example 43 The procedure of Example 42 was repeated, except that the coformed web was composed of about 50 percent by weight of the meltblown fibers and about 50 percent by weight of the polyester fibers.

67 Example 44 The procedure of Example 43 was repeated, except that the basis weight of the coformed web was about 400 g/m 2 Example The procedure of Example 42 was repeated, except that the coformed web was composed of about 75 percent by weight of the meltblown fibers and about 25 percent by weight of the polyester fibers.

Example 46 4 The procedure of Example 45 was repeated, except that the staple was 2-inch (5.1-cm) long, 5.5 denier per filament polyester staple.

Example 47 The procedure of Example 46 was repeated, except that the coformed web was composed of about 50 percent by weight of the meltblown fibers and about 50 percent by weight of the polyester fibers.

4 Example 46 S 4 The procedure of Example 46 was repeated, except that the coformed web was compoied of about 25 percent by weight of the meltblown fibers and about 75 percent by weight of the polyester fibers.

68 4^ Example 49 The procedure of Example 42 was repeated, except that the polyester fiber was replaced with International Paper Super Soft pulp fibers. The pulp mat had a basis weight of about 200 g/m 2 and the mat feed roll was about 0.030 inch (about 0.76 mm) from the picker roll surface.

A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about percent by weight of the meltblown fibers and about 50 percent by weight of the pulp fibers. The web had a basis weight of about 200 g/m 2 Example The procedure web was composed of about 75 percent by 2 about 400 g/m 0* The procedure web was composed of about 50 percent by 9.

of Example 49 was repeated, except that the coformed about 25 percent by weight of the meltblown fibers and weight of the pulp fibers and had a basis weight of Example 51 of Example 50 was repeated, except that the coformA about 50 percent by weight of the meltblown fibers and weight of the pulp fibers.

Example K The procedure of Example 51 was repeated, except that the basis weight of the coformed web was about 200 g/m 2

S

0 05* S S SO SO

S

69 rhk/0311E 4 Example 53 The procedure of Example 42 was repeated, except that the meltblowing throughput was at a rate of about 0.25 g per capillary per hour at a temperature of about 181 degrees, the extrusion pressure at the die tip was 282 psig, composition viscosity was about 1500 poise, the forming air was at a temperature of about 197 degrees and a pressure of about 3 psig, the forming screen drum was about 7.5 inches (19 cm) from the die tip, and secondary fibers were not added to the meltblown stream.

A nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and a basis weight of about 60 9g/m 2 Example 54 The procedure of Example 53 was repeated, except that the forming air for meltblowing was supplied at a pressure of about 6 psig and the forming screen drum was about 17 inches (about 43.2 cm) from the die tip.

Example t\ The procedure of Example 42 was repeated, except that the meltblowing conditions of Example 53 were employed and the mat feed roll was about 0.005 inch (about 0.13 mm) from the picker roll surface.

4g;: A coformed nonwoven web was fcrmed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 30 percent by weight of the meltblown fibers and about 70 percent by weight of the polyester fibers. The web had a basis weight of about 200 g/m 2

S

S

rhk/0311E Example 56 The procedure of Example 55 was repeated, except that the forming air for meltblowing was supplied at a pressure of about 6 psig, the forming screen drum was about 17 inches (about 43.2 cm) from the die cip, and the fiber transporting air was supplied to the picker roll at a pressure of about 2 psig.

Example 57 The procedure of Example 56 was repeated, except that the coformed web was composed of about 60 percent by weight of meltblown fibers and about 40 percent by weight of the 1"15 polyester fibers and the basis weight of the web was about 160 g/m 2 Example 58 The procedure of Example 42 was repeated, except that the meltblowing throughput was at a rate of about 0.40 g *4 per capillary per minute at a temperature of about 204 degrees, the extrusion pressure at the die tip was about 288 psig, composition viscosity was about 950 poise, 25 forming air was at a temperature of about 231 degrees and a pressure of about 3 psig, the forming screen drum was about 17 inches (about 43.2 m) from the die tip, and the ev S* secondary fiber process parameters were the same as those of Example 55, except that the fiber transporting air pressure was 2 psig.

A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 60 percent by weight of the meltblown fibers and about 40 percent by weight of the polyester fibers. The web had a basis weight of about 200 g/m 2 71 Example 59 The procedure of Example 49 was repeated, except that the meltblowing throughput was at a rate of about 0.35 g pe capillary per minute at a temperature of about 194 degrees, the extrusion pressure at the die tip was about 273 psig, the composition viscosity was about 1030 poise, and the forming air was at a temperature of about 206 degrees.

A coformed nonwoven web was formed which had a width (cross-machine direction)_ of about 20 inches (about 51 cm) and which was composed of about 30 percent by weight of the meltblown fibers and about 70 percent by weight of the pulp 2 fibers. The web had a basis weight of about 200 g/m 2 Example The procedure of Example 59 was repeated, except that the forming air for meltblowing was supplied at a pressure ~2,4Q, of about 6 psig and the forming screen drum was about 17 inches (about 43.2 cm) from the die tip.

i Example 61 The procedure of Example 59 was repeated, except that the melt temperature was about 196 degrees, the extrusion pressure of the die tip was about 253 psig, the composition viscosity was about 960 poise, and the forming air pressure S was 6 psig.

A coformed nonwoven web was formed which had a width 3 (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 30 percent by weight of the meltblown fibers and about 70 percent by weight of the pulo 2 fibers. The web had a basis weight of about 200 g/m 2 72 Example 62 The procedure of Example 61 was repeated, except that the forming air pressure was about 3 psig.

A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 30 percent by weight of the meltblown fibers and about 70 percent by weight of the pulp fibers. The web had a basis weight of about 250 g/m 2 Example 63 fee The procedure of Example 62 was repeated, except that Sthe fiber transporting air was supplied to the picker roll at a pressure of about 2 psig, the coformed web was composed of about 40 percent by weight of the meltblown fibers and about 60 percent of the pulp fibers, and the web basis weight was about 216 g/m 2 Example 64 The procedure of Example 62 was repeated, except that the pulp fibers were Weyerhauser XB-309 pulp fibers and the fiber transporting air pressure was about 2 psig.

A cof,^ 'ed nonwoven web was formed which had a width (cross-machi.d direction) of about 20 inches (about 51 cm) and which was composed of about 44 percent by weight of the meltblown fibers and about 56 percent by weight of the pulp ofibers. The web had a basis weight of about 250 g/m 2 Example The procedure of Example 64 was repeated, except that the forming air pressure was about 6 psig.

73 A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of abcut 44 percent by weight of the meltblown fibers and about 56 percent by weight of the pulp fibers. The web had a basis weight of about 250 g/m 2 Example 66 The procedure of Example 65 was repeated.

A coformed nonwoven web was formed which had a width (cross-machine direction) of about 20 inches (about 51 cm) and which was composed of about 30 percent by weight of the meltblown fibers and about 70 percent by weight of the pulp fibers. The web had a basis weight of about 200 g/m 2 The nonwovenr webs obtained in Examples 43-50 and 53-66, inclusive, were subjected to the saturated capacity test to determine synthetic urine absorbencies. The results are summarized in Table 17; the absorbency values reported are averages of at least three samples. It perhaps should be noted that the test procedure this time did not require the removal of a spunbonded carrier since such carrier was not employed.

*e 74 Table 17 Summary of Saturated Capacity Test on Nonwoven Webs from Examples 42-50 and 53-66 Absorbency, g Syn. tUrine/g Example .0.5 psi 1.0 psi 2.0 psi 3.0 psi 42 9.0 6.8 5.9 5.3 43 11.8 9.8 8.9 8.4 44 8.9 7.7 7.4 7.2 45 12.8 12.0 11.7 11.5 46 11.3 10.2 9.7 1547 10.5 9.0 8.6 8.3 sees G 0:048 9.2 8.5 7.9 7.2 0 .0 49 7.3 6.0 5.0 4.8 7.4 5.8 4.8 4.7 53 9.5 9.3 9.0 8.7 54 13.8 13.1 12.3 11.3 10.4 8.1 6.9 6.2 Goe 56 9.4 8.0 6.5 5.6 10:057 10.8 8.3 7.2 59 9.0 7.2 5.7 4.9 *se:60 7.9 6.3 5.0 4.3 0 61 8.3 6.5 5,3 4.8 .62 8.5 7.0 6.1 5.6 **o:63 9.0 7.4 6.2 5.7 64 9.8 7.2 6.2 5.6 8.4 7.0 C-5 66 7.7 6.2 5.7 5.2 75 Example 67 The procedure of Example 31 was repeated, except that the polymeric composition of Example 5J was replaced with a blend consisting of 67 percent by weight of the polymeric composition of Example 5J and 33 percent by weight of low density polyethylene (PETROTHENE T NA 601, U.S.I. Chemicals, National Distillers Chemical Corporation, New York, New York). According to the manufacturer, the polyethylene has a density of 0.903 g/cc, a Brookfield viscosity at 190 degrees of 3300 centipoise (ASTM D 3236), and an equivalent melt index of 2000 g per 10 minutes (ASTM D 1238).

The extrusion throughput was estimated to be about 0.47 g per capillary per minute at a temperature of about 188 degrees. The extrusion pressure at the die tip was 220 psig. The viscosity of the blend in the capillaries was calculated to be 340 poise.

g* As before, a well-formed, coherent nonwoven web was formed. This time, though, the web exhibited considerable wet trength in the presence of excess water. The web had a water absorbency by the centrifuge method of 16.2 g per g of web (average of two samples) which is equivalent to 24,3 g per g of superabsorbent, thermoplastic polymeric composition in the blend. Two additional samples gave an i25 average value of 24 g per g of web, equivalent to 37 g per g of polymeric composition. The average water absorbency of these two samples by the centrifuge method was 52 0 percent by weight.

Having thus described the invention, numerous changes and modifications thereto will be apparent to those having ordinary skill in the art without departing from the spirit and scope of the present invention.

76

Claims (30)

1. A method of preparing a superabsorbent, thermoplastic polymeric composition which comprises: reacting a first compound with a second compound at a temperature of from 50 to 200 degrees C for a time sufficient to effect essentially complete reaction; and reacting with the product from step A a third compound at a temperature of from 80 to 200 degrees C for a time sufficient to obtain a melt flow rate of less than 1,000 g per 10 minutes; in which said first compound is a difunctional poly(oxyethylene) having a weight average molecular weight of from 5,000 to 50,000; said second compound is an aliphatic, cycloaliphatic, aromatic, or heterocyclic compound having two functional groups which are reactive with the functional groups of said first compound; the mole ratio of said second S compound to said first compound is in the range of from 2 to 100; said third compound is an aliphatic, cycloaliphatic, aromatic, heterocyclic, or polymeric compound having two functional groups which are reactive with the functional groups of said second compound; the reaction product of said first compound with said second compound, excluding excess second compound, is from 86 to 98 percent by weight of the final composition; and said third compound plus the excess of said second compound are from 2 to 14 percent by weight of the final composition; in which the functional groups of said second compound and said third compound independently are selected from the group consisting of hydroxy, carboxy, amino, epoxy, imino, and isocyanate groups, with the selection of all such functional groups being such that said superabsorbent, thermoplastic polymeric composition contains linkages selected from the group consisting of urethane, amide, ester, and secondary urea linkages; and the melt flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2.0955 t 0.0051 mm.

2. The method of claim 1, in which the weight average molecular weight of said first compound is in the range of from 8,000 to 50,000.

3. The method of claim 2, in which the weight average molecular weight of said first compound is in the range of from 8,000 to 30,000. rhk/0296E *t S- 78-

4. The method of claim 3, in which the weight average molecular weight of said first compound is in the range of from 8,000 to 16,000, The method of claim 1, in which the reaction product of said first compound with said second compound, excluding excess second compound, is in the range of from 90 to 97 percent by weight.

6. The method of claim 5, In which the reaction product of said first compound with said second compound, excluding excess second compound, is in the range of from 95 to 97 percent by weight.

7. The method of claim 1, in which said third compound plus the excess of said second compound is in the range of from 3 to 10 percent by weight.

8. The method of claim 7, in which said third compound plus the S excess of said second compound is in the range of from 3 to 5 percent by i. weight.

9. The method of claim 1, in which said first compound is a poly(oxyethylene) diol.

10. The method of claim 9, in which said second compound is allphatic or aromatic.

11. The method of claim 10, in which said second compound is a diisocyanate.

12. The method of claim 11, in which said second compound is toluene-2,4-diisocyanate, toluene-2,6-diisocyanate, or a mixture thereof.

13. The method of claim 11, In which said second compound is 4,4'-methylenebis(phenylisocyanate).

14. The method of claim 11, in which said second compound is 1,6-hexamethylene diisocyanate.

15. The method of claim 1, in which said third compound is monomeric. @*sob: 16. The method of claim 15, in which the mole ratio of said second compound to said first compound is from 2.5 to

17. The method of claim 16, in which the mole ratio of said second compound to said first compound is from 2.5 to 26.

18. The method of claim 15, in which said third compound is an aliphatic or aromatic compound having from 2 to 24 carbon atoms.

19. The method of claim 18, in which said third compound Is a diol. The method of claim 19, in which said third compound is 1,4-butanediol. rhk/0296E 79

21. The method of claim 19, in which said third compound is 1,3-propanediol.

22. The method of claim 19, in which said third compound is 1,4-bis(2-hydroxyethoxy)benzene.

23. The method of claim 19, in which said third compound is 1,3-bis(2-hydroxyethoxy)benzene.

24. The The compound to sai

26. The temperature of

27. The temperature of

28. The temperature of

29. The temperature of

30. The method method d first of claim 1, In which said third compound is polymeric. of claim 24, in which the mole ratio of said second Scompound is from 2 to method of claim 1, in which step A is carried out at a from 80 to 150 degrees C. method of claim 26, in which step A is carried out at a from 95 to 120 degrees C. method of claim 1, in which step B is carried out at a from 90 to 150 degrees C. method of claim 28, in which step B is carried out at a from 110 to 130 degrees C, method of claim 1, in which step B Is carried out to a melt *.0 646* *6* 6 6 66 6 *6 6 6 6666 6 6 6666 40r 0#00 flow rate 20 31. flow rate

32. flow rate

33. flow rate

34. of from 30 to 500 g per 10 minutes. The method of claim 30, in which step B is carried out to a melt of from 50 to 170 g per 10 minutes. The method of claim 31, in which step B is carried out to a melt of from about 80 to about 150 g per 10 minutes. The method of claim 1, in which step B is carried out to a melt of from about 10 to about 30 g per 10 minutes. A method for forming a superabsorbent article which comprises: heating a superabsorbent, thermoplastic polymeric composition made according to the method of any one of claims 1-33 to a temperature in the range from about the temperature at which the melt flow rate of 30 the superabsorbent is at least 20 g per 10 minutes to the temperature at which significant degradation of the composition begins to occur; and forming the heated composition; in which the melt flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2.0955 0.0051 mm. /LMM/296E 80 A method for making a nonwoven superabsorbent web which comprises: heating a superabsorbent, thermoplastic polymeric composition made according to the method of any one of claims 1-33 to a temperature in the range from about the temperature at which the melt flow.rate of the superabsorbent is at least 20 g per 10 minutes to the temperatur& at which significant degradation of the composition begins to occur; and extrudlng the heated composition through a plurality of extrusion orifices into a gas stream to form a gas-borne stream of a plurality of substantially identically prepared monofilaments which are attenuated by the gas stream; and e substantially randomly depositing the stream of monofilaments on a porous collecting screen to form a nonwoven web; in which the melt 15 flow rate is determined at a temperature of 195 degrees C, under a 2.16 kg load, and with an orifice diameter of 2.0955 0.0051 mm.

36. A method for forming a superabsorbent article which comprjse,. heating a superabsorbent, thermoplastic polymeric comg on to a temperature in the range from about the temper e at which the melt flow rate of the superabsorbent is at 20 g per 10 minutes to the temperature at which signi nt degradation of the composition begins to occur; and forming the he-e cposition; in which th t flow rate is determined at a temperature of 195 degrees 25 C, a 2.16 kg load, and with an orifice diameter of 2.0955 0.0051 mm. A method of preparing a superabsorbent, thermoplastic polymeric composition substantially as hereinbefore described with reference to any one of the Examples. 3-.36. A method for forming a superabsorbent article substantially as hereinbefore described with reference to any one of the Examples. 3.3t. The product of the process of any one of claims 1-35. DATED this FIFTH day of APRIL 1993 Kimberly-Clark Corporation S, Patent Attorneys for the Applicant ,Y SPRUSON FERGUSON