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| United States Patent | 5102597 |
| Link to this page | http://www.wikipatents.com/5102597.html |
| Inventor(s) | Roe; Donald C. (Cincinnati, OH);
Lahrman; Frank H. (Cincinnati, OH);
Berg; Charles J. (Cincinnati, OH) |
| Abstract | Absorbent polymeric macrostructures that are porous and comprise an
interparticle crosslinked aggregate having a circumscribed dry volume
greater than about 10.0 mm.sup.3. The interparticle crosslinked aggregate
comprises a multiplicity of precursor particles of substantially
water-insoluble, absorbent, hydrogel-forming, polymer material; and an
interparticle crosslinking agent reacted with the polymer material of the
precursor particles to form crosslink bonds between the precursor
particles. Because of the particulate nature of the precursor particles,
the macrostructure has pores between adjacent precursor particles. The
pores are interconnected by intercommunicating channels such that the
macrostructure is liquid permeable. |
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Title Information  |
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| Publication Date |
April 7, 1992 |
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| Parent Case |
This is a division of application Ser. No. 503,393, filed on Apr. 2, 1990. |
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Title Information  |
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References  |
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U.S. References |
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| | Reference | Relevancy | Comments | Reference | Relevancy | Comments | 3661154
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|      Your vote accepted [0 after 0 votes] | | 5002986 Fujiura 524/47 Mar,1991 |      Your vote accepted [0 after 0 votes] | | 4861539 Allen 264/204 Aug,1989 |      Your vote accepted [0 after 0 votes] | | 4833179 Young 522/183 May,1989 |      Your vote accepted [0 after 0 votes] | | 4826880 Lesniak 521/53 May,1989 |      Your vote accepted [0 after 0 votes] | | 4824901 Alexander 524/555 Apr,1989 |      Your vote accepted [0 after 0 votes] | | 4822453 Dean 162/157.6 Apr,1989 |      Your vote accepted [0 after 0 votes] | | 4806598 Morman 525/63 Feb,1989 |      Your vote accepted [0 after 0 votes] | | 4798861 Johnson 524/458 Jan,1989 |      Your vote accepted [0 after 0 votes] | | 4783510 Saotome 525/329.7 Nov,1988 |      Your vote accepted [0 after 0 votes] | | 4766173 Bailey 524/819 Aug,1988 |      Your vote accepted [0 after 0 votes] | | 4758617 Tanioku 524/413 Jul,1988 |      Your vote accepted [0 after 0 votes] | | 4735987 Morita 524/436 Apr,1988 |      Your vote accepted [0 after 0 votes] | | 4734478 Tsubakimoto 527/300 Mar,1988 |      Your vote accepted [0 after 0 votes] | | 4693713 Chmelir 604/368 Sep,1987 |      Your vote accepted [0 after 0 votes] | | 4673402 Weisman 604/368 Jun,1987 |      Your vote accepted [0 after 0 votes] | | 4666983 Tsubakimoto 525/119 May,1987 |      Your vote accepted [0 after 0 votes] | | 4625001 Tsubakimoto 526/88 Nov,1986 |      Your vote accepted [0 after 0 votes] | | 4610678 Weisman 604/368 Sep,1986 |      Your vote accepted [0 after 0 votes] | | 4587308 Makita 525/373 May,1986 |      Your vote accepted [0 after 0 votes] | | 4578068 Kramer 604/368 Mar,1986 |      Your vote accepted [0 after 0 votes] | | 4551191 Kock 156/276 Nov,1985 |      Your vote accepted [0 after 0 votes] | | 4500670 McKinley 524/445 Feb,1985 |      Your vote accepted [0 after 0 votes] | | 4439385 Kuhls 264/37.18 Mar,1984 |      Your vote accepted [0 after 0 votes] | | 4429001 Kolpin 442/340 Jan,1984 |      Your vote accepted [0 after 0 votes] | | 4413995 Korpman 604/368 Nov,1983 |      Your vote accepted [0 after 0 votes] | | 4410571 Korpman 427/385.5 Oct,1983 |      Your vote accepted [0 after 0 votes] | | 4286082 Tsubakimoto 526/240 Aug,1981 |      Your vote accepted [0 after 0 votes] | | 4282121 Goodrich 525/54.26 Aug,1981 |      Your vote accepted [0 after 0 votes] | | 4190563 Bosley 523/111 Feb,1980 |      Your vote accepted [0 after 0 votes] | | 4127944 Giacobello 34/349 Dec,1978 |      Your vote accepted [0 after 0 votes] | | 4093776 Aoki 428/402 Jun,1978 |      Your vote accepted [0 after 0 votes] | | 3957741 Rembaum 526/312 May,1976 |      Your vote accepted [0 after 0 votes] | | 3670731 Harmon 604/368 Jun,1972 |      Your vote accepted [0 after 0 votes] | | 4541871 Obayashi 106/193.1 Dec,1969 |      Your vote accepted [0 after 0 votes] | | |
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| Market Size |
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Market Review  |
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Technical Review  |
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Claims  |
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What is claimed is:
1. A method for producing a porous, absorbent, polymeric macrostructure
comprising an interparticle crosslinked aggregate having pores
interconnected by intercommunicating channels so that the macrostructure
is liquid permeable, the method comprising the steps of:
(a) providing a multiplicity of precursor particles of substantially
water-insoluble, absorbent, hydrogel-forming, polymer material;
(b) applying an interparticle crosslinking agent onto said precursor
particles, said interparticle crosslinking agent being capable of reacting
with said polymer material of said precursor particles;
(c) physically associating said precursor particles to form an aggregate
having pores interconnected by intercommunicating channels; and
(d) reacting said interparticle crosslinking agent with said polymer
material of said precursor particles of said aggregate, while maintaining
the physical association of said precursor particles, to form crosslink
bonds between said precursor particles to form an interparticle
crosslinked aggregate macrostructure.
2. The method of claim 1 additionally comprising the step of surface
crosslinking the macrostructure.
3. The method of claim 1 additionally comprising the step of shaping the
aggregate to a desired shape, size, and/or density prior to step (d).
4. The method of claim 1 wherein step (d) comprises heating.
5. The method of claim 1 additionally comprising the step of adding
reinforcing fibers to said precursor particles.
6. The method of claim 1 wherein said interparticle crosslinking agent
comprises a monomer that is polymerized to form polymeric crosslink bonds
between said precursor particles.
7. The method of claim 6 wherein step (d) comprises the step of initiating
the polymerization reaction by irradiating said monomer.
8. The method of claim 1 wherein said precursor particles have a mass
average particle size less than about 500 microns.
9. The method of claim 1 wherein said precursor particles have a mass
average particle size less than about 300 microns.
10. The method of claim 1 wherein said precursor particles comprise fibers.
11. A method for producing a porous, absorbent, polymeric macrostructure
comprising an interparticle crosslinked aggregate having pores
interconnected by intercommunicating channels so that the macrostructure
is liquid permeable, the method comprising the steps of:
(a) providing a multiplicity of substantially dry precursor particles of
substantially water-insoluble, absorbent, hydrogel-forming, polymer
material, said polymer material of said precursor particles being selected
from the group consisting of hydrolyzed starch-acrylonitrile graft
copolymer; partially neutralized starch-acrylonitrile graft copolymer;
starch-acrylic acid graft copolymer; partially neutralized starch-acrylic
acid graft copolymer; saponified vinyl acetate-acrylic ester copolymers;
hydrolyzed acrylonitrile or acrylamide copolymers; slightly network
crosslinked products of any of the foregoing copolymers; partially
neutralized polyacrylic acid; or slightly network crosslinked products of
partially neutralized polyacrylic acid;
(b) applying an interparticle crosslinking agent onto said precursor
particles, said interparticle crosslinking agent being selected from the
group consisting of polyhydric alcohol compounds, polyglycidyl ether
compounds, polyfunctional aziridine compounds, polyfunctional amine
compounds, and polyfunctional isocyanate compounds;
(c) physically associating said precursor particles to form an aggregate
having pores interconnected by intercommunicating channels;
(d) shaping the aggregate to a desired shape, size, and/or density; and
(e) subsequently heating said interparticle crosslinking agent and said
aggregate to react said interparticle crosslinking agent with said polymer
material of said precursor particles of said aggregate, while maintaining
the physical association of said precursor particles, to form crosslink
bonds between said precursor particles to form an interparticle
crosslinked aggregate macrostructure.
12. The method of claim 11 additionally comprising the step of adding
fibers to said precursor particles prior to reacting said interparticle
crosslinking agent with said polymer material of said precursor particles.
13. The method of claim 11 additionally comprising the step of surface
crosslinking the macrostructure.
14. The method of claim 11 wherein said precursor particles comprise
fibers.
15. The method of claim 11 wherein said interparticle crosslinking agent is
mixed with water, an organic solvent, or mixtures thereof.
16. The method of claim 15 wherein step (d) comprises molding the
aggregate.
17. The method of claim 15 wherein step (d) comprises forming the
aggregate.
18. The method of claim 17 wherein step (d) comprises extruding said
aggregate and subsequently rolling said aggregate to form a sheet.
19. The method of claim 11 wherein said interparticle crosslinking agent is
selected from the group consisting of trimethylol propane, ethylene
glycol, 1,2-propanediol, 1,3-propanediol, or glycerol; and said polymer
material consists essentially of slightly network crosslinked products of
partially neutralized polyacrylic acid.
20. The method of claim 19 wherein step (e) is carried out at a temperature
in the range of from about 170.degree. C. to about 220.degree. C. for
between about 3 hours and about 30 minutes.
21. The method of claim 20 wherein said interparticle crosslinking agent is
mixed with water, an organic solvent, or mixtures thereof.
22. The method of claim 21 wherein step (d) comprises the steps of
extruding the aggregate and then rolling said aggregate to form a sheet.
23. The method of claim 22 wherein step (b) comprises atomizing said
interparticle crosslinking agent onto said precursor particles.
24. The method of claim 22 wherein the mass average particle size of said
precursor particles is less than about 300 microns.
25. The method of claim 24 wherein at least about 95% by weight of said
precursor particles have a particle size between about 150 microns and
about 300 microns.
26. The method of claim 22 wherein the mass average particle size of said
precursor particles is less than about 180 microns; and at least about 95%
by weight of said precursor particles have a particle size between about
90 microns and about 180 microns.
27. The method of claim 19, 24, 25, or 26 additionally comprising the step
of surface crosslinking said precursor particles of said macrostructure
simultaneously with step (e).
28. The method of claim 14, 19, 21, or 24 additionally comprising the step
of adding reinforcing fibers to said precursor particles prior to reacting
said polymer material of said precursor particles with said interparticle
crosslinking agent. |
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Claims  |
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Description  |
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FIELD OF THE INVENTION
The present invention relates to absorbent polymeric compositions which,
upon contacting liquids such as water or body exudates, swell and imbibe
such liquids. More specifically, the present invention relates to
polymeric compositions that are macrostructures such as a sheet, film, or
strip. Such absorbent polymeric macrostructures are porous so as to be
liquid permeable. These porous, absorbent, polymeric macrostructures are
useful by themselves or in absorbent articles such as diapers, adult
incontinence pads, sanitary napkins, and the like. The present invention
also relates to methods of producing such porous, absorbent, polymeric
macrostructures.
BACKGROUND OF THE INVENTION
Particulate, absorbent, polymeric compositions are capable of absorbing
large quantities of liquids such as water and body exudates and which are
further capable of retaining such absorbed liquids under moderate
pressures. These absorption characteristics of such polymeric compositions
make them especially useful for incorporation into absorbent articles such
as diapers. For example, U.S. Pat. No. 3,699,103 issued to Harper et al.
on June 13, 1972 and U.S. Pat. 3,670,731 issued to Harmon on June 20,
1972, both disclose the use of particulate, absorbent, polymeric
compositions (also referred to as hydrogels, superabsorbent, or
hydrocolloid materials) in absorbent articles.
Conventional particulate, absorbent, polymeric compositions, however, have
the limitation that the particles are not immobilized and are free to
migrate during processing and/or use. Migration of the particles during
processing can lead to material handling losses during manufacturing
operations as well as nonhomogeneous incorporation of the particles into
structures in which the particles are being used. A more significant
problem, though, occurs when these particulate materials migrate during or
after swelling. Such mobility leads to high resistance to liquid flow
through the material due to the lack of stable interparticle capillary or
liquid transport channels. This phenomenon is one form of what is commonly
referred to as "gel blocking".
One attempt to overcome the performance limitations associated with
particle mobility in the context of their use in absorbent articles has
been the incorporation of the particulate, absorbent, polymeric
compositions into tissue laminates (layered absorbent members). By
encapsulating the particles between tissue layers, the overall particle
mobility within an absorbent member is diminished. However, upon liquid
contact, the particles within the laminate are often free to move relative
to each other resulting in the breakdown of any preexistent interparticle
capillary channels.
Another attempted solution has been to immobilize the particulate,
absorbent, polymeric compositions by the addition of large quantities of
liquid polyhydroxy compounds that act as an adhesive to hold the particles
together or to a substrate. An example of this technology is disclosed in
U.S. Pat. No. 4,410,571 issued to Korpman on Oct. 18, 1983. While this
approach does limit migration before and, to some extent, during swelling,
the particles eventually become detached from each other upon presentation
of excess liquid to such polymeric compositions, resulting again in the
breakdown of any preexisting capillary channels between the particles.
A further attempt to overcome the problem has been to produce a
superabsorbent film via extrusion of a solution of a linear polymer and
subsequent crosslinking of the polymer. An example of this technology is
disclosed in U.S. Pat. No. 4,861,539 issued to Allen et al. on Aug. 29,
1989. While these superabsorbent films may absorb significant quantities
of liquids, they have limited liquid transport properties and are prone to
gel blocking due to their lack of internal capillary channels.
Therefore, the present invention seeks to resolve the above problems by
providing a porous, absorbent, polymeric macrostructure.
Thus, it is an object of the present invention to provide absorbent
polymeric macrostructures that are porous.
It is a further object of the present invention to provide absorbent
polymeric macrostructures that remain intact and transport liquid even
upon saturation with excess liquid.
It is a still further object of the present invention to provide absorbent
polymeric macrostructures wherein the component precursor particles and
pores retain their relative geometry and spatial relationships even upon
saturation with excess liquid.
It is an even further object of the present invention to provide absorbent
polymeric macrostructures that increase in liquid permeability upon
swelling.
It is another object of the present invention to provide a method for
producing such absorbent polymeric macrostructures.
It a further object of the present invention to provide improved absorbent
products, absorbent members, and absorbent articles (such as diapers or
sanitary napkins) incorporating the absorbent polymeric macrostructures of
the present invention.
SUMMARY OF THE INVENTION
The present invention provides an absorbent polymeric macrostructure that
is porous. The porous, absorbent, polymeric macrostructure comprises an
interparticle crosslinked aggregate having a circumscribed dry volume
greater than about 10.0 mm.sup.3. The interparticle crosslinked aggregate
comprises a multiplicity of precursor particles of substantially
water-insoluble, absorbent, hydrogel-forming, polymer material; and an
interparticle crosslinking agent reacted with the polymer material of the
precursor particles to form crosslink bonds between different precursor
particles. Because of the particulate nature of the precursor particles,
the macrostructure has pores between adjacent precursor particles. The
pores are interconnected by intercommunicating channels such that the
macrostructure is liquid permeable (i.e., has capillary transport
channels).
Due to the interparticle crosslink bonds formed between the precursor
particles forming the interparticle crosslinked aggregate, the resultant
macrostructure has improved structural integrity, increased liquid
acquisition and distribution rates, and minimal gel blocking
characteristics. It has been found that when the macrostructure is
contacted with liquids, the macrostructure swells generally isotropically
even under moderate confining pressures, imbibes such liquids into the
precursor particles, and absorbs such liquids into the pores. The
isotropic swelling of the macrostructure allows the precursor particles
and the pores to maintain their relative geometry and spatial
relationships even when swollen. Thus, the macrostructures are relatively
"fluid stable" in that the precursor particles do not dissociate from each
other, thereby minimizing the incidence of gel blocking and allowing the
capillary channels to be maintained and enlarged when swollen so that the
macrostructure may acquire and transport subseque | | |