Title: "SUPERABSORBENT MATERIAL, SUPERABSORBENT STRUCTURE, ABSOR¬ BENT ARTICLE AND PROCESS FOR PREPARING SAID SUPERABSORBENT"
The present invention relates to expanded superabsorbent materials, and in particular to expanded superabsorbents for use in absorbent products such as sanitary napkins, catamenial tampons, diapers, dressings or the like, for the absorption of body fluids.
A large variety of absorbent materials are currently known, and generally used in the forming of absorbent structures. For ex¬ ample, absorbent materials based on cellulose pulp are well known. Another type of absorbent material well known for its great capa¬ bility of absorbing liquids belongs to the class of naturally oc¬ curring absorbent materials and is known as sphagnum.
More recently, a new class of absorbent material has been developed, this class presenting a great capacity for retention and absorption of liquids. These materials are more commonly known in the art as "superabsorbents".
Much research is currently being undertaken to improve both the properties of retention and absorption of the above mate¬ rials, giving emphasis to sphagnum and other superabsorbent mate- rials as these are more directly related to the present invention.
About 350 different species of sphagnum, a moss of the family sphagnaceae, are found naturally in all parts of the world, generally in acid soils subjected to flooding such as swamps, lakes and shallow lagoons. The moss forms dense and extensive colonies, its vegetative propagation occurring by ramification and death of older parts of the plant. The leaves are formed of living and dead cells. The living cells are green and are called chlorocysts, ha¬ ving an assimilatory function. The dead cells are colourless and are called lencocysts, and these have spiral ribs and pores which function as reservoirs for water and other aqueous liquids.
The term "liquid" used herein signifies water or any a- queous liquid to be absorbed.
Superabsorbent materials, so-called due to their large capacity for absorption and retention of liquids, are generally polymeric materials whose polymeric chains have highly hydrophilic active sites.
Superabsorbent materials may be by nature entirely syn¬ thetic, or may be obtained from essentially natural polymers in whose chains are introduced highly hydrophilic groups. Outstanding the class of superabsorbent polymers are, inter alia, the aerylate based polymers such as sodium polyacry- late.
In addition to the examples of polymers cited above, su¬ perabsorbent polymers may include various other types of natural or synthetic polymers based on or modified by highly hydrophilic groups which are well known to those skilled in the art.
Table I below shows, by way of illustration, the liquid absorption capacities of some absorbent materials cited above, when subjected to a pressure in the range of from 0.05 to 0.5 psi. The apparatus used to evaluate this property was the GATS, with a 1% saline NaCl solution. TABLE I
* Conventional ground wood pulp used in the production of diapers and sanitary napkins.
** Sphagnum sample from Botanical Institute.
*** Favor SAB sodium polyacrylate based polymer produced
by STOCKHAUSEN - Germany.
By means of a simple comparison between the values of absorption capacity listed in the above table, the superiority of superabsorbents over sphagnum and Kraft pulp is evident. However, although the absorbent materials above, particu larly sphagnum and superabsorbent, present satisfactory indices of absorption capacity, these materials are subjected to limitations which prevent the obtention of an absorbent material or structure truly effective for the desired purpose. For example, pulp presents a high absorption rate, but itsabsorption capacity and retention are low. Sphagnum, on the other hand, shows a good absorption rate and a good capacity for retention, while most superabsorbents have a very low absorption rate associated with the highest absorption and retention capacity. It is well known in the art that one of the essential characteristics of an absorbent material consists in its initial absorption speed. However, it should be emphasized that as well as presenting a satisfactory absorption speed the absorbent material should simultaneously have satisfactory retention and absorption characteristics. Thus, for example, a high initial absorption rate is of little use if the capacity for retention or capacity for ab¬ sorption is unsatisfactory.
The present invention provides a superabsorbent material with improved liquid absorption properties and free of the disad- vantages shown by absorbent materials of improved properties here¬ in described.
A third aspect of the present invention -is the provision of new absorbent articles including the absorbent structμres cited above. Additionally the present invention deals with a process for the obtention of the said improved superabsorbent materials. More specifically, the present invention reveals a new superabsorbent material obtained from a superabsorbent material commercially available, which presents a combination of the effec- tive characteristics of the starting superabsorbent without simul¬ taneously presenting the disadvantages shown thereby.
The present invention is prompted by the observation of the following two aspects:
1. Functional mechanism of natural sphagnum, pulp and of
superabsorbent materials.
The mechanism of absorption of natural sphagnumis is by a purely physical process. The structure of sphagnum is microporous, the mircopores being principally responsible for its absorptive properties. This mircroporous structure functions by capillary ac¬ tion, providing penetrating paths for the liquid to be absorbed. The liquid is stored in the reservoir cells present in the struc¬ ture of sphagnum.
The mechanism of absorption of pulp or other cellulosic material is very similar to sphagnum, except that the pores are Li mited to the void volume between the fibres. The resulting pores are much larger than those of sphagnum, and as a consequence the capillary action and retention are much less pronounced.
The absorption mechanism of superabsorbent materials is entirely different, occurring by an essentially chemical process. The highly hydrophilic groups present in the polymeric chains of superabsorbents are essentially those responsible for its high ab¬ sorption and retention capacity. The liquid to be absorbed attaches itself chemically to the hydrophilic groups present in the polyme- ric structure, by means of electrostatic forces of the hydrogen bridge type.
2. Limitative factors of the absorbent materials defined above:
The absence of a chemical absorption mechanism in the sphagnum or pulp structure results not only in a smaller capacity for absorption of liquids, but also reduces the retention capacity for liquids since the material absorbed is simply stored in reser¬ voir cells in the structure without being chemically attached to the material thereof. When subject to pressure, the absorbed liquid is readily expelled from the reservoir cells according to the pres¬ sure applied.
Notwithstanding the fact that the hydrophilic groups pre¬ sent in the polymeric chains of superabsorbent materials make them extremely efficient in their capacity for absorbing and retaining liquids, these materials are generally restricted in their absorp¬ tion and distribution speeds.
As liquids are absorbed into the structure of a superab¬ sorbent, a "blocking action" to the later absorbed liquid is absor¬ bed. This diminishes not only the absorption speed, but also the
capacity for distributing liquid through the structure. It has been seen that the disadvantages occur due to the fact that a structure of the superabsorbent is an extremely compact structure.
Thus the material aspect of the present invention resides in the fact that the properties of the superabsorbent material may be greatly improved by the modification of the original compact structure to a structure having micropores, such as those which e- xist in the structure of natural sphagnum.
As a result of this modification, there is obtained an expanded superabsorbent material having a high capacity for absorp_ tion and a satisfactory retention of liquids, without simultaneous ly presenting the limitations on the distribution speed caused by the "blocking action". The superabsorbent material obtained how¬ ever has a much reduced density in comparison to the original co - pact superabsorbent, due to its expanded structure. This allows a great improvement in the control and homogeniety of distribution of superabsorbent particles in the final process of forming an ab¬ sorbent structure. A further advantage of the present material is a relative reduction in cost per volume of the superabsorbent a- terial.
The modification of the original compact structure of the superabsorbent material for obtaining an expanded structure in ac¬ cordance with the invention is obtained by the expansion of the said original compact structure. The expanded superabsorbent poly- mer of the present invention has an absorption speed superior to that of the original compact polymer," principally in the initial period of absorption.
For example in the first five seconds, the expanded su¬ perabsorbent polymer shows absorption rates approximately 2 to 3.5 times higher than the original compact structured polymer.
The expansion may be performed by any suitable expansion process, which provides an expanded final structure. Preferably, thermoexpansion processes are used to perform the invention.
Among suitable thermoexpansion processes, the following are preferred: a) expansion by submitting the compact superabsorbent ma terial to thermotreatment in a microwave oven; and b) expansion by contacting the compact superabsorbent ma terial with an adequately heated surface.
The process of expansion which resulted in a highly sat¬ isfactory expanded structure was that of submitting the original superabsorbent material to thermotreatment in a microwave oven, and is thus the preferred expansion process of the invention. The temperature of the thermotreatment may vary within a wide range from the softening temperature to a temperature lower than the corbonization temperature of the material. The preferred expansion temperature generally ranges from about 160 to 3009C more preferably from about 180 to 2509C. Additionally, the expansion may be performed by a process which uses thermotreatment in association with a variation of pres_ sure.
This process, here referred as "gun type" expansion, con sists in heating the superabsorbent compact material within a clo- sed tube, until a pressure in the range of approximately 8 to 200 lb/in 2 is achieved, approximatel 170 lb/in2. Thereafter the tube is opened so that the material contacts the atmosphere at a lower pressure, and the material is thereby expanded.
The expansion period is variable, and depends on the ini^ tial and final temperatures, the original moisture content of the polymer to prevent sticking of the polymer particles to each other and to the apparatus, the moisture being preferably between 0.5 and 5% and not greater than 15%. Generally, the preferred expansion time is between about 0.5 and about 30 minutes. According to the present invention, any polymeric mate¬ rial based on sodium aerylate and having a compact structure may be used as a superabsorbent material to be expanded.
The term "polymeric material based on sodium acrylate" as used here signifies a polymeric material constituted by monome- ric units of acrylic acid (AA) and sodium acrylate (SA) .
It has also been found according to the present invention that to obtain a satisfactory and efficacious expansion the propor¬ tion of AA and SA in the polymeric materials to be expanded should be in the range of 40 to 60% by weight of AA and 60 to 40% by weight of SA. Preferably, polymeric materials having from 50 to 60% by weight of SA are used. Polymeric material having a content of AA superior to these limits also permit expansion, but their particles become agglomerated during the heat treatment and thus impede the obtention of discrete expanded particles. A particularly preferred
superabsorbent material of the present invention is the superabsor bent polymer commercially known as Favor SAB, since the proportions of AA and SA monomers in the polymeric chain lies within the above ranges. Any commercially available polymeric material based on sodium acrylate which does not have the cited proportions of AA to SA may also be expanded to provide the improved superabsorbent ma¬ terials of the present invention, provided that they are duly treated so that the proportion of AA and SA monomers lies within the ranges specified above. This treatment consists essentially in transforming the AA groups present in the chain of the polymeric material into SA groups when the proportion of AA in the polymeric material is greater than 60% by weight, so that the quantitative ranges of AA and SA in the polymeric material to be expanded are within the limits established herein. This treatment, for example, may perform with any suitable compound for transforming SA groups into AA groups, for example by using an acidic compound such as hidrochloric acid or any suitable compound for transforming ; groups into SA groups, such as a basic sodium compound. In the following list, intended to be illustrative only, the chemical composition of various types of commercially availa¬ ble superabsorbents based on sodium acrylate are given: Type of Material Manufacturer %AA %SA Favor SAB STOCKHAUSEN • 50 - 57 50 - 43 Favor SAB 922 " 19 - 23 81 - 77
Aquakeep 10SH KINTETSU 13 - 21 82 - 79
Arasorb 720 ARAKAWA 17 - 20 83 - 80
Dow XV 43.40800 DOW CHEMICAL 18 - 20 72 - 80
Arasorb 802 ARAKAWA 18 - 20 81 - 80 Arasorb 803 " 18 - 20 82 - 80
Arasorb 804 " 18 20 82 - 80
As may be readily seen in the above list, the only commer cially available material having a proportion of AA and SA within the limits of the quantitative ranges of the present invention is Favor SAB. The other materials may be duly modified as already men tioned in order to obtain a polymeric material having proportions of AA and SA in the range of 60 to 40% by weight and 40 to 60% by weight respectively.
This commercial product is available in a granule size
ranging from 35 to 100 mesh, and may be readily expanded according to the present invention. However, it is preferable to use a partL cle size distribution between 50 and 100 mesh to provide greater uniformity and better absorption characteristics after expansion. The superabsorbent expanded materials in accordance with present invention should have a final density in the range of 0.05 to 0.4 g/cm 3, preferably, in the range of 0.05 to 0.14 g/cm3.
For illustrative purposes there are shown in the drawings the structures of absorbent materials of the prior art, and the structure of the new superabsorbent materials of the present inven tion, in which: Figure 1 is a photomicrograph of the structure of natural sphagnum, magnified 675 times; Figure 2 is a microphotograph of the structure of natural sphagnum magnified 675 times, showing the micropores;
Figure 3 is a microphotograph of the compact structure of a super- absorbent polymer (sodium polyacrylate) magnified 54 times; Figure 4 is a microphotograph os a superabsorbent polymer (sodium polyacrylate) expanded according to the present invention and magnified 54 times; Figure 5 is a microphotograph of the structure of an unexpanded superabsorbent polymer (sodium polyacrylate) magnified
270 times, and Figure 6 is a microphotograph of a superabsorbent polymer (sodium polyacrylate) expanded according to the present invention and magnified 270 times.
The superabsorbent materials of the invention may be useα either in isolation for the absorption of liquids, or in associa- tion with other materials to provide an absorbent structure.
The improved absorbent structures according to the inven¬ tion include the new superabsorbent material in association with a suitable absorbent support. Such structures can comprise one or more layers or nucleous of said expanded superabsorbent material in association with one or more layers of an auxiliary material. Gene¬ rally, wood pulp is used as the support. The quantity of superabsor_ bent material necessary to form an effective absorbent structure depends on the specific nature of the structure to be produced, and is well known to those skilled in this art. Proportions of about 2%
to 60%, preferably, 5% to 10% by weight of superabsorbent materials with respect to the weight of the support materials, preferably ground wood pulp, are satisfactory to provide such structure.
The absorbent structures above are suitable for forming absorbent articles such as disposable diapers, sanitary napkins, tampons and absorbent bandages or their like. The articles thus formed have effective liquid absorption and retention properties, without simultaneously presenting the disadvantages of conventio¬ nal absorbent articles and the disadvantages presented by using the regular compact superabsorbent product without the expanded final structure. Illustrative Examples
The superabsorbent starting polymer used in the illustra¬ tive examples is that commercially known by the name "Favor SAB", whose characteristics are listed below: Chemical nature - Sodium polyacrylate Appearance - white powder Granin size - 160 to 500 microns Apparent density - 660 - 30 g/1 Flowability - very good
Moisture content - 5 - 2% pH (bel at 1%) - 5.2 to 5.5
The expansion of the above material was performed in a microwave oven at 400 to 700 watts. The expansion time varied from about 0,5 to 30 minutes at a temperature of from 180 to 2509C.
In the following tables, some of the comparative results obtained in laboratory tests on compact regular Favor SAB and on the ter ally expanded Favor SAB, together with pulp and natural sphagnum, and absorbent structures formed from these materials. Table II - Density Reduction
Grain Size Bulk Density (g/cm~) Expansion Parameters Mesh Regular Favor Expanded Temp. (9C) Time
SAB (not expanded) Favor SAB apprcx. (Min apprαx.)
35 - 100 0,82 0,140-0,050 200 25
50 - 100 0,86 0,100-0,065 200 25
35 - 50 0,82 0,083-0,050 200 25
> 35
Bulk Density determined .through mass/volume relationship
3 of 50 cm ooff mmaatteerriiaallss..
Expansion in lab scale through thermal treatment into a
Sanyo Microwave Oven - Model EM 90038, microwave frequency of 2450 MHz.
Absorption Rate - Tea Bag Test
Test method: 0.2 g of superabsorbent material is set in heat sealable paper bags, commonly used commercially for tea bags. The dry weight is exactly determined and after the bags are sealed each sample is imersed in a 1% sodium chloride solution for in¬ tervals of 5, 10, 30, 60 and 120 seconds. After allowance to drain until excess solution is lost each weight is noted again. The same procedure as above described is repeated without superabsorbent.
The absorption after each imersion is calculated from the difference of both weight and converted to grams of saline solution absorbed per gram of material.
The results are listed in tests III.l, III.2 and III.3 below. III.l - Regular Favor SAB
III.2 - Expanded Favor SAB Absorption•Rate (g/g)
III.3 - Regular and Expanded Favor SAB
Absorption rate (g/g)
Regular Favor SAB Expanded Favor SAB
After 5 seconds 2.60 - 6.20 9.15 12.95 After 10 seconds 5.22 - 15.67 13.93 21.48 After 30 seconds 9.11 - 28.66 19.02 30.17
Regular Favor SAB Expanded Favor SAB
After 60 seconds 13. 30 - 33 . 65 24 . 85 - 34 . 36 After 120 seconds 19. 07 - 37.20 30. 66 - 38.59
The results above show an increasing of the initial ab¬ sorption rate in the order of 2.0 to 3.5 times for the expanded Favor SAB in relation to the non expanded product. Liquid Retention
Cylindrical packs in form of tubes (to be introduced in¬ to centrifuge tubes) are manually prepared with light-weight non-
2 woven material of about 20 g/m .
Samples of .0,2 g of the superabsorbent materials were encased into them, the packs sealed and imersed in 1% sodium chlo¬ ride solution. The samples were removed after two hours, allowed to drain for 10 minutes and were weighed and their respective to¬ tal absorption rates were calculated (initial wet weight) .
Thereafter the samples were subjected to two consecutive cycles of centrifuging, 15 minutes at 900 rpm and then 15 minutes at 1400 rpm.
The quantity of liquid retained by the sample was calcu¬ lated by difference between the weights registered before and af¬ ter the centrifuging cycles and were expressed in percentage terms, The results are shown in table IV below: Table IV - Liquid Retention
After centrifuging at
Ground wood pulp
Sphagnum
Regular Favor SAB
The results above show a practically unaffected reten¬ tion capacity in the expanded Favor SAB in relation to the Regular
Favor SAB .
Reduction of Blocking effect
Test Method
Sample disks of ground wood pulp and ground wood pulp containing ιegular and expanded Favor SAB were manually prepared in lab scale. They were mixed through a kitchen blender, vacuum compacted in a 9 cm diameter mould and pressed to a thickness be¬ tween 1.0 and 1.5 mm.
Individual sample disks weighed approximately 2.0 g. A 2 x 2 cm pad of a wood pulp structure with an infe¬ rior skin of PCAc was centrally disposed on the disks.
Five ml of a 1% sodium chloride solution was added to this 2 x 2 cm pad to be absorbed by the disks.
After 2 minutes the stained area of the disk and the a- mount of saline solution absorbed by the disk were determined.
The area was measured by a planimeter and the quantity of absorbed solution was determined from the difference of final and initial weights of the disks. Table V - Reduction of blocking effects Disk Composition (%)
Notes 1. A larger stained area indicates a reduced blocking action. 2. More liquid absorbed indicates as higher ability to "pump" 1iquids.
The detail of Table V above shows the superior perfor¬ mance of expanded Favor SAB. Absorption capacity and velocity. Test Method
GATS apparatus, 1% NaCl saline solution, pressure of
0.05 psi and orifice centralized in the plate.
Disks manually prepared in the laboratory, mixed in li¬ quidizer, vacuum compacted, in a 9 cm diameter mould and pressed at 1 ton pressure. Pads weighed between 1.856 and 1.970 g. Table VI - Absorption capacity and velocity for experimental absorbent structures.
Experimental Pads density Absorption Absorption structure (g/cm3) capacity velocity
(g/g) (g/min)
100% ground wood pulp 0.123 - 0.142 8.2 - 7.5 11.4 - 11.9
90% pulp + 10% expanded Favor SAB 0.133 12.1 3.24
90% pulp + 10% expanded Favor SAB 0.139 - 0.147 11.1 - 11.3 8 - 8.8
The deatils above show an increase in absorption veloci- ty of the structure of the invention by about 2.5 times relative to the structure using normal Favor SAB (3.24g/min as opposed to - 8.4 g/min) .
The improvements listed above are of great importance, since the superabsorbents of the present invention present, in combination, a high velocity of absorption, a high capacity for absorption, a satisfactory liquid retention and low density due to the expansion. This is not presented by any of the conventional absorbent materials cited here.
Various other comparative test results will be shown in the following tables, comparing samples of absorbent structures prepared with the compact superabsorbent and with the expanded su¬ perabsorbents of the present invention. Experimental absorbent structures
Experimental absorbent structures as similar as possi- ble to commercial product were prepared in lab scale.
They were formed by the deposition of two layers of ground wood pulp, the inferior one having a PCAc skin, aiming to reproduce as much as possible an existing commercial sanitary pad. The total weight of this structure was in the order of 6,0 g (3,0
- -
g per layer) and with dimensions of about 18,0 x 7,0 cm (around 126 cm2) .
The final absorbent structure was composed with the su¬ perabsorbent materials spread between the two layers of ground wood pulp. Samples:
A - Control - 100% ground wood pulp around 6,0 g final weight and
2 around 126 cm .
B - Composite containing 2% of expanded Favor SAB spread between the two layers of ground wood pulp.
C - Composite containing 10% of expanded Favor SAB spread between the two layers of ground wood pulp.
D - Composite containing 10% of the Regular Favor SAB (not expan ded) spread between the two layers of ground wood pulp. Test Method:
GATS apparatus, pressure of 0,05 psi, 1% sodium chloride solution, point source.
The results are listed in the table VII below.
Table VII - Absorption characteristics at 0.05 psi
As shown by the above table, the advantages of the expan ded superabsorbent lie in the results of volume variation and ab¬ sorption velocity when compared to structures containing the same amount of superabsorbent, one being unexpanded the other being ex-
panded.
Fluid Distribution
Test Method
45 ml of 1% sodium chloride solution is discharged through a burette in the central point of an experimental absor¬ bent structure similar to the one described for Table VII.
The solution was poured in 3 consecutive discharges of 15 ml each, at intervals of 30 minutes.
The wetted absorbent structure is then cut in 6 equal sections (S1-Sfi) and the quantity is determined as well as the percentage of utilization of the absorbent structure. Illustrative sections of the structure:
Table VIII below indicates improved results of distri¬ bution and utilization in the structures containing the expanded Favor SAB over those ones containing the unexpanded regular Favor SAB.
Table VIII - Fluid Distribution and-percentage of utilization
Absorption of each section (g/g)
The % of utilization is calculated as follows:
% of utilization = Average Wetness - Absorb. Average Deviation _. Q
Average Wetness
Pumping Power Test Method
A 2 x 2 cm pad of ground wood pulp with PCAc skin was centrally disposed on the absorbent structure similar to that des_ cribed for Table VII.
30 ml of 1% saline solution is poured in the 2 x 2 pads in 6 consecutive discharges of 5 ml each at intervals of 10 minu¬ tes.
The pumping power of the absorbent structure is then measured by weighing the quantity of solution each structure pum¬ ped from the 2 x 2 pad after each discharge.
The results according to Table IX below indicate the higher pumping effect of the structures containing the expanded Favor SAB structure containing the regular Favor SAB, principally at the initial discharge of the saline solution. Table IX - Pumping Power
Fluid Control Expanded Favor Regular Favor added (cm3) 100% pulp SA ABB SSAABB
2% 10% 10%
B D
5 5.2 10 30.2 15 52.6
20 62.2
25 68.2
Example "X" This example illustrates the chemical modification of a commercially available sodium acrylate based polymer to obtain a proportion of AA and SA monomers within the operative ranges according to the present invention.
As starting materials, ARASORB 720, FAVOR SAB 922 and DOW XV 43 48800 having 80% of SA and 20% of AA were used. Each of these materials was treated with hydrochloric acid to obtain a polymeric material having 50% by weight of SA and 50% by weight of AA. There were used potentially 0.32 eqg of HC1 for each 100g of starting material to perform the substitution of 0.32 egg of
positive sodium ions for each 100g of starting material, and thus obtain a polymeric material having 50% AA and 50% SA. When submit¬ ted to thermo expansion of Favor SAB in the first example, there were obtained polymeric materials having an expanded structure an- alogous to the expanded structure obtained starting with Favor SAB. It should be clear that the examples above are indicated here only to illustrate the present invention; and thus should not be limitative thereof in any way. The scope of the invention is clearly much broader than that described in the specific examples presented here.