US3691154A - Absorbent fibers of phosphorylated cellulose with ion exchange properties - Google Patents

Abstract

Highly absorbent cellulose fibers with ion exchange properties are obtained by phosphorylating cellulose fibers, hydrolyzing the fiber walls with acid, converting the phosphorylated fibers to the sodium salt form, mechanically refining these fibers to rupture the primary fiber wall and permit subsequent swelling or ballooning, acidifying the refined fibers to reconvert the phosphorylated cellulose into the acid form, and drying the fibers in a manner to substantially avoid appreciable hydrogen bonding. The acid pH of these highly absorbent fibers makes them ideally suited as an absorbent component in catamenial tampons employed to establish and maintain a desirable acidic condition in the vagina.

Description

nited States Patent 51 3,691,154 Bernardin [4 1 Sept. 12, 1972 [s41 ABSORBENT FIBERS OF FOREIGN PATENTS 0R APPLICATIONS PHOSPHORYLATED CELLULOSE WITH ION EXCHANGE PROPERTIES [72] Inventor: Leo J. Bernardin, Appleton, Wis.

[73] Assignee: Kimberly-Clark Corporation, Neenah, Wis.

[22] Filed: May 5, 1970 [21] Appl. No.: 34,878

[52] U.S. Cl. ..260/219, 8/116 P, 128/285 [51] Int. Cl. ...C08b 5/00, D06m 11/08, D06m 13/26 [58] Field of Search ..260/219, 212; 8/116;

[56] References Cited UNITED STATES PATENTS 3,052,593 9/1962 Battista ..260/212 3,091,241 5/1963 Kellett ..128/270 3,116,199 12/1963 Cruz et al. ..162/146 3,187,747 6/1965 Burgeni et a1. ..128/156 3,388,119 6/1968 Cruz ..260/212 3,423,284 1/1969 Marek et a1. ..162/157 3,521,637 7/1970 Waterbury ..128/270 838,973 6/1960 Great Britain ..260/219 899,284 6/ 1962 Great Britain ..260/219 OTHER PUBLICATIONS Industrial & Engineering Chemistry, Volume 41, No. 12, Pages 2828- 2834, December, 1949.

Primary Examiner-Donald E. Czaja Assistant Examiner-Ronald W. Griffin Attorney-Daniel J. l-lanlon, Jr. and Raymond J.

Miller [57] ABSTRACT Highly absorbent cellulose fibers with ion exchange properties are obtained by phosphorylating cellulose fibers, hydrolyzing the fiber walls with acid, converting the phosphorylated fibers to the sodium salt form, mechanically refining these fibers to rupture the primary fiber wall and permit subsequent swelling or ballooning, acidifying the refined fibers to reconvert the phosphorylated cellulose into the acid form, and drying the fibers in a manner to substantially avoid appreciable hydrogen bonding. The acid pH of these highly absorbent fibers makes them ideally suited as an absorbent component in catamenial tampons employed to establish and maintain a desirable acidic condition in the vagina.

9 Claims, No Drawings ABSORBENT FIBERS OF PI-IOSPHORYLATED CELLULOSE WITH ION EXCHANGE PROPERTIES CROSS REFERENCE TO RELATED APPLICATION Copending application of Leo J. Bernardin, Ser. No. 30,811, filed Apr. 22, 1970.

BACKGROUND OF THE INVENTION struation, however, a slightly alkaline pH is frequently established. Under such conditions growth of favorable microflora is inhibited while undesirable types thrive. This causes the vagina to be more susceptible to infection and inflammation during menses.

' Various attempts have I been made to control this condition by providing catamenial devices which act to lower the alkaline pH during menstruation to the desiredpH of 4.5 orless while simultaneously absorbing discharged menstrual fluids. One of these may be found in U.S. Pat. No. 3,091,241 to Kellett which employs glyceryl triacetate in an absorbent tampon as a physiological biostat or automatic pH controller.

In another U.S. Pat. No. 3,187,747 to Burgeni et al, catamenial tampons are made from multicomponent alloyfibers in which one of the components is absorbent, such as regenerated cellulose, while the other is an acidifying polymer, such as carboxymethyl cellulose in hydrogen form.

In each of the above patents, the tampon structure required at least two components, one performing the necessary absorbency function, while the other acts as the pH controller.

The present invention is directed to a cellulose fiber product which combines the pH control and the absorbency function in one fiber, without requiring chemical adjuvants or alloys.

In the copending Bernardin application, referenced above, phosphorylated cellulose fibers in sodium salt form were found to have a markedly increased absorbency over unmodified cellulose. The product was obtained by chemically substituting phosphate groups for hydroxyls on the cellulose, hydrolyzing the fiber walls with acid, then converting the substituted and hydrolyzed fibers to the salt form by ion exchange, and solvent drying or otherwise drying the fibers in a manner to substantially avoid appreciable hydrogen bonding. It was found that the phosphorylated fibers in their acid form, before conversion to salt form, and whether solvent dried or not, showed no improvement in absorbency over unmodified cellulose, while the salt form was found to be up to five times as absorbent. These results appeared to confirm the belief, at that time, that in order for substituted celluloses to have a sufficient increase in absorbency to warrant commercial use, it was necessary for the cellulose to be in an alkaline salt forrn. Prior art developments involving carboxymethyl cellulose having particular degrees of substitution also supported this belief.

However, as work continued it was found that even greater absorbency could be developed in the phosphorylated cellulose in salt form if the fibers were refined for at least one minute before drying. Such refining increased absorbent properties almost threefold over the unrefined fibers. It was then found, rather unexpectedly,that if these refined fibers were reconvened to the acid form, they retained much of the increased absorbency developed by refining and exhibited by the salt form fibers. This finding seemed to contradict the earlier conclusion that the acid form of phosphorylated cellulose shows no increase in absorbency over unmodified pulp. This unexpected result immediately opened up a number of possibilities for use of the product in areas where absorbency and ion exchange complement one another.

SUMMARY OF THEINVENTION Phosphorylated fibers in acid form with improved absorbency characteristics combined with high ion exchange capacity are produced by first saturating cellulose pulp sheets in a phosphorylating bath; drying and reacting the saturated sheets at elevated temperature; dispersing the reacted sheets in water, which preferably is deionized, and washing the reactant therefrom; converting the washed phosphorylated fibers to the acid form by treatment with acid; converting the acidified fibers to sodium salt form; mechanically refining the fibers in aqueous dispersion; .reconverting the refined fibers to acid form; and finally drying the fibers in a manner to substantially avoid appreciable hydrogen bonding of the fibers to each other during the water removal process. When formed into mats the resulting fibers exhibit high ion exchange capacity and much higher capillary suction pressure and absorbent capacity than unmodified cellulose fibers.

These fibers are markedly superior in absorbent capacity to phosphorylated fibers in the acid form which have not been refined. They are also superior in absorbency to fibers which have been refined while in acid form. Accordingly, in order to obtain this improved absorbency in the acid-form fibers of this invention, it is necessary to first refine the fibers in salt form and then reconvert the refined fibers to acid form.

The preferred method of phosphorylating is the urea phosphate method, wherein the fibers are reacted at a temperature of from about to C for about five to over 30 minutes in a solution of urea and phosphoric acid. Other known but less satisfactory methods of phosphorylation may be used including treatment with phosphorous oxychloride and pyridine; phosphorous oxychloride and phosphoric acid; phosphorous oxychloride and dioxane; phosphorous oxychloride alone, and alkali metal salts of phosphoric acid.

When converting the washed phosphorylated fibers to acid form immediately after phosphorylation, cold acid may be used, but it is preferred to use hot acid because the latter more readily hydrolyzes the fiber walls which is highly desirable in developing the improved capillary suction pressures described herein.

In converting the phosphorylated fibers to salt form the alkali preferably employed is a dilute solution of sodium hydroxide. However, other solutions of basic salts such as sodium carbonates, phosphates and the like maybeused.

In order to dry the fibers in a manner to avoid hydrogen bonding, conventional solvents such as acetone, alcohol, alcohol followed by hexane, and the like maybeused.

Freeze drying may also be used since such a drying method also substantially avoids hydrogen bonding.

It is the primary object of this invention to provide chemically modified cellulose fibers which in their acid form have markedly improved fluid absorbency characteristics.

Another object is to provide absorbent pads from fibers which have high absorbency combined with high ion exchange capacity.

Other features, objects and advantages of the invention will become apparent by reference to the following specification.

DESCRIPTION OF THE PREFERRED EMBODIMENTS In a preferred embodiment, four sheets of unbeaten, bleached, northern softwood, draft pulp weighing about 14 grams each were immersed for about 30 minutes in a bath consisting of 50 percent urea, 18 percent orthophosphoric acid, and 32 percent water by weight. The saturated pulp sheets were drained to a consistency of 1 part fiber to 3 parts by weight of solution. The moist sheets were dried and reacted or cured in an oven for 20 minutes at l600 C. The cured sheets were dispersed in deionized water and the resulting slurry washed free of the treating solution by several rinses with deionized water using a suction filter.

The filtered material which is believed to be comprised of cellulose monoammonium monohydrogen phosphate was dispersed in a 3 percent solution of hot hydrochloric acid and soaked at a temperature of between 60 and 70 C for h hour. The acid form of phosphorylated fiber thus obtained was washed free of excess acid and separated into two portions. One portion was refined in a conventional PFI laboratory refiner for 2% minutes at 10 percent consistency and solvent dried from acetone, the other portion was converted to salt form by soaking in a 5 percent solution of Na CO for 1% hour. The fiber was washed again and then refined at percent consistency in a conventional PFl laboratory refiner for 2% minutes. The refined pulp was reconverted to acid form, i.e., a pH of 3, with hydrochloric acid, washed free of excess acid, and then solvent dried from acetone.

Absorbency characteristics in terms of capillary suction pressure of the two kinds of phosphorylated cellulose in acid form obtained by the above described process were then compared to each other and to an unmodified cellulose which was also refined for 2% Absorption of liquid water as a function of capillary suction pressure on airlaid mats of fiber is measured by means of a known capillary tension cell apparatus of the type described in an article from the Textile Research Journal, Vol. 37, No. 5, May, 1967, pp. 356-366, A. A. Burgeni and C. Kapur, Capillary Sorption Equilibria in Fiber Masses. Absorption capabilities for a fiber mass are cited in the number of grams of water per gram of fiber which a mat of fibers will absorb under the specified capillary suction head or pressure indicated.

The results indicate that when phosphoryaltcd pulp is merely converted to acid form and then refined, it shows no measurable improvement over unmodified pulp.

The results also show very clearly that when the phosphorylated pulp is refined in its salt form before converting back to acid form there is a dramatic increase in its absorbent properties.

It became apparent that the refining of the fibers in salt form and converting to acid form has a different effect on the fibers than when they are originally refined while in acid form.

Microscopic examination of the fibers, before and after refining, indicated that, before refining, the fibers of the phosphorylated pulp in acid form look very much like ordinary wood pulp fibers when wet with the fiber walls substantially intact, while the walls of the phosphorylated pulp in salt form showed signs of rupture or fraying with some ballooning of the internal structure in a number of places. Refined unmodified pulp and phosphorylated pulp in acid form also appeared quite similar, showing some fraying of the fiber wall, but little ballooning or swelling. The refined phosphorylated fibers in salt form, on the other hand, exhibited considerable ballooning and swelling, as the internal structure expanded down the length of the fiber with only a few confining rings appearing where the primary fiber wall remained unruptured and intact. The ballooned and swelled form of the main internal body of the fiber structure was retained when these fibers in salt form were converted back to acid fon'n.

Refining phosphorylated fibers in the salt form prior to reconversion to the acid fonn is therefore considered to be a necessary step in the preparation of the highly absorbent fibers in the acid form of this invention. Without such refining the acid form of phosphorylated fibers show no improvement in absorbency. In structure therefore, the acid form of phosphorylated fibers must be substantially stripped or denuded of the primary fiber wall in order to obtain the demonstrated improvement in absorbency.

In considering this improved acid form of phosphorylated cellulose fiber for tampon usage it was also determined that ion exchange capacity is significant. Accordingly, ion exchange capacity was tested by potentiometric titration with 0.1N sodium hydroxide. As indicated in the Burgeni et al US. Pat. No. 3,187,747, the acidifying capacity of a tampon in vivo can be approximated in terms of the volume of 0.1N sodium hydroxide consumed by the fibers in an environment of 0.8 percent NaCl solution at pH values up to about 4.5. It is also indicated that in distilled water, less sodium hydroxide would be required for equivalent capacity because NaCl tends to aid in the liberation of hydrogen ions. Accordingly the ion exchange capacity exhibited under actual use would be higher than the capacity indicated by titration in distilled water.

A number of samples of the acid form of phosphorylated cellulose fibers refined in salt form as described above were titrated in distilled water with 0.1N NaOl-l to determine ion exchange capacities. One gram of fiber was found to consume about 12.5 ml of 0.1N sodium hydroxide in reaching a pH of about 4.5. Accordingly a .normal tampon weight of about 3 grams would have adequate capacity for maintaining an acid pH in the vagina under even the most severe conditions of use. Since such a tampon acts to maintain the menstrual fluids at an acid pH, the surrounding skin surface -is also maintained slightly acid whereby the environment for the useful microflora stays favorable. In view of this high ion exchange capacity it is not necessary to make the entire absorption device of the phosphorylated fibers of this invention. They may be admixed with ordinary wood pulp fibers, with phosphorylated fibers in salt form, with other absorptive fibers, or with resilient fibers as set forth in the prior art to provide better expansion properties when used incompressed form.

While the improved pulp fibers are indicated as being of particular use in catamenial tampons, they may also be employed where the dual characteristics of 6 ture having been obtained by first providing phosphorylated cellulose pulp fibers in their salt form; mechanihigh absorbency and high ion exchange capacity are 7 required.

The invention is particularly applicable to fibers converted from wood pulp because of their low cost and ready availability. However, other fibers normal to the paperrnaking art may also be employed such as hemp, jute, esparto, cereal straws, flax, bagasse, bamboo, reds, cotton linters, kenaf and the like.

What is claimed is:

1. The acid form of phosphorylated cellulose pulp fibers characterized by a structure in which a major portion of the primary wall of said fibers is broken away leaving the main internal body structure of said fibers substantially unconfined by said primary wall, said internal body structure being in swelled and ballooned condition, whereby said fibers provide an improved capability for absorbing aqueous fluids, said fiber struccally refining said fibers while in said salt form; and then converting said refined fibers to the said acid form.

2. A'method for producing modified cellulose fibers in acid form with improved absorbency and ion exchange capacity which comprises saturating cellulose pulp fibers with an aqueous phosphorylating solution; reacting the saturated pulp at elevated temperature to obtain phosphorylated cellulose fiber; dispersing the reacted fibers in water and washing said fibers free of reactant; treating the washed fibers with acid to convert said fibers to acid form; treating the acidified fibers with an alkaline solution to convert said acidified fibers to salt form; washing the salt form of said fibers free of excess alkali, subjecting said fibers while in salt form to mechanical refining; reconverting said refined fibers to the acid form; washing said acidform fibers free of excess acid; and drying said acidf fibe b e the water throu v l ii h subs tan 33233? appreciable inte 1 rbonding.

3. The method of claim 2 in which said phosphorylating solution is selected from the group consisting of a solution of (a) urea and phosphoric acid, (b)

phosphorous oxychloride and pyridine, (c) phosphorous oxychloride and phosphoric acid, (d) phosphorous oxychloride and dioxane, (e) phosphorous oxychloride alone, and (f) alkali metal salts of phosphoric acid.

4. The method of claim 2 in which said acid is hydrochloric acid.

5. The method of claim 4 in which said acid is hot.

6. The method of claim 2 in which said alkali is selected from the group consisting of sodium hydroxide, sodium carbonates, and sodium phosphates.

7. The method of claim 2 in which said reaction is carried out at a temperature of from about 130 to 195 means

Claims (8)

1. 2. A method for producing modified cellulose fibers in acid form with improved absorbency and ion exchange capacity which comprises saturating cellulose pulp fibers with an aqueous phosphorylating solution; reacting the saturated pulp at elevated temperature to obtain phosphorylated cellulose fiber; dispersing the reacted fibers in water and washing said fibers free of reactant; treating the washed fibers with acid to convert said fibers to acid form; treating the acidified fibers with an alkaline solution to convert said acidified fibers to salt form; washing the salt form of said fibers free of excess alkali, subjecting said fibers while in salt form to mechanical refining; reconverting said refined fibers to the acid form; washing said acid-form fibers free of excess acid; and drying said acid-form fibers by removing the water through means which substantially avoids appreciable interfiber bonding.
2. 3. The method of claim 2 in which said phosphorylating solution is selected from the group consisting of a solution of (a) urea and phosphoric acid, (b) phosphorous oxychloride and pyridine, (c) phosphorous oxychloride and phosphoric acid, (d) phosphorous oxychloride and dioxane, (e) phosphorous oxychloride alone, and (f) alkali metal salts of phosphoric acid.
3. 4. The method of claim 2 in which said acid is hydrochloric acid.
4. 5. The method of claim 4 in which said acid is hot.
5. 6. The method of claim 2 in which said alkali is selected from the group consisting of sodium hydroxide, sodium carbonates, and sodium phosphates.
6. 7. The method of claim 2 in which said reaction is carried out at a temperature of from about 130* to 195* C for from about five to over 30 minutes.
7. 8. The method of claim 2 in which said water is removed by solvent in the drying step.
8. 9. The method of claim 2 in which in the drying step said water is removed by freeze drying.