US3617439A - Process for improving comminution pulp sheets and resulting air-laid absorbent products - Google Patents

Process for improving comminution pulp sheets and resulting air-laid absorbent products Download PDF

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US3617439A
US3617439A US789084A US3617439DA US3617439A US 3617439 A US3617439 A US 3617439A US 789084 A US789084 A US 789084A US 3617439D A US3617439D A US 3617439DA US 3617439 A US3617439 A US 3617439A
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comminution
pulp sheet
dimethylammonioacetate
percent
sheet
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Benjamin E Chapman Jr
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Georgia Pacific Nonwovens LLC
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Buckeye Cellulose Corp
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    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L15/00Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
    • A61L15/16Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
    • A61L15/20Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons containing organic materials
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61FFILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
    • A61F13/00Bandages or dressings; Absorbent pads
    • A61F13/01Non-adhesive bandages or dressings
    • A61F13/01008Non-adhesive bandages or dressings characterised by the material
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C9/00After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
    • D21C9/001Modification of pulp properties
    • D21C9/002Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives
    • D21C9/005Modification of pulp properties by chemical means; preparation of dewatered pulp, e.g. in sheet or bulk form, containing special additives organic compounds
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/03Non-macromolecular organic compounds
    • D21H17/05Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
    • D21H17/07Nitrogen-containing compounds
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61FFILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
    • A61F13/00Bandages or dressings; Absorbent pads
    • A61F2013/00361Plasters
    • A61F2013/00727Plasters means for wound humidity control
    • A61F2013/00731Plasters means for wound humidity control with absorbing pads

Definitions

  • a method for producing comminution pulp sheets from cellulosic fibers and the products resulting therefrom as pulp sheets and air-laid absorbent batts comprises impregnating the fibers of the comminution pulp sheets with about 0.1 to 2 percent of a selected zwitterionic surfactant, such as N-octadecyl -N, N- dimethylammonio- 1 2-dodecanoate either in slurry prior to or during comminution pulp sheet formation and prior to pulp sheet drying.
  • a selected zwitterionic surfactant such as N-octadecyl -N, N- dimethylammonio- 1 2-dodecanoate either in slurry prior to or during comminution pulp sheet formation and prior to pulp sheet drying.
  • the resulting comminution pulp sheet is easily and effectively fiberized or comminuted to yield fibers from which air-laid absorbent products are prepared, and the air-laid absorbent products are characterized by improved bulk, resili
  • This invention relates to processes for the manufacture of comminution pulp sheets comprised .of cellulosic fibers and intended for subsequent comminution and air laying to form absorbent fibrous batts, pads, or sheets.
  • the absorbent fibrous batts, pads, or sheets are used in the structures of bandages, diapers, sanitary napkins, tampons and like articles.
  • the invention relates to the fibrous impregnation of such comminution pulp sheets with selected zwitterionic surfactants whereby the pulp sheets are rendered easily comminutable into predominantly whole fibers.
  • the air-laid batts formed therefrom substantially retain the absorbency characteristics of conventional unimpregnated pulp sheets and by meaningful use tests exceed the fluid inhibition and resiliency of such air-laid batts prepared from fibers derived from unimpregnated comminution pulp sheets.
  • the fibrous impregnation in the present invention is effected prior to final dewatering ofthe pulp sheet in sheet formation.
  • the present invention consists of a method for impregnating the fibers of a comminution pulp sheet comprised of wood fibers or other cellulosic fibers with effective amounts of nitrogen containing zwitterionic surfactants more fully described below by means of structure and chemical nomenclature specification.
  • Air laying, or the process consisting of comminuting or fiberizing pulp sheets to form a mass of individual fibers dispersed in air and subsequent deposition of fibers on a foraminous screen to form a batt, pad, or sheet has long been practiced with varying degrees of success.
  • the air-laid batts, pads, or sheets have been accorded cohesiveness by various means including cohesive pressing, soluble glue spraying, latex dipping and thermal setting, where thermoplastic fibers were involved.
  • R is an alkyl or alkenyl group containing about 16 to about 22 carbon atoms
  • R, and R are selected from the group consisting of hydrogen and alkyl groups containing one to two carbon atoms
  • R is an alkylene group containing one to about 1 1 carbon atoms, which alkylene group can have one or more hydroxyl groups attached to carbon atoms
  • R is selected from the group consisting of-COO, SO;,, and OSO
  • applicant was surprised to discover that the use of the aforementioned zwitterionic surfactants as impregnants for woodpulp and other cellulosic fiber sheets resulted in improving their comminution characteristics while providing excellent power requirement and total absorptive capacity characteristics with regard to both cationic impregnated woodpulp sheets and woodpulp sheets devoid of any surfactant.
  • zwitterionic surfactants are also enhanced, particularly in instances where batt or pad clarity or color is a desirable feature, by the fact that the present zwitterionic surfactants form clear or water-white solutions for sheet impregnation. While the present process and resultant products are primarily described in terms of wood fiber absorbent pads, it is specifically noted that the attendant benefits will accrue to comminution pulp sheets prepared from other cellulosic fibers or admixtures of other cellulosic fibers with wood fibers.
  • the ease of comminution efiects of the present invention are applicable to processes other than the preparation of air-laid absorbent structures wherein pulp sheets are comminuted, for example in the preparation of viscose rayon by the slurry process, the preparation of the cellulose nitrate, the preparation of cellulose acetate and other cellulose derivatives.
  • the displacement shower is comprised of an aqueous solution of the selected zwitterionic surfactant.
  • the displacement shower system of sheet impregnation offers desirable advantages in that it effects economy in surfactant use, since only the displacement shower water system and not the entire white water or slurry water systems of a paper machine must be loaded with surfactant. Further advantages accrue from displacement showering in that changes to nonimpregnated woodpulp sheets are easily effected because the entire white water system of the paper machine is not surfactant loaded.
  • a principal object of this invention is, accordingly, to provide woodpulp sheets for comminution and later formation into air-laid absorbent pads of various types and methods for their production, which cellulose sheets are impregnated with the zwitterionic surfactants disclosed herein.
  • a further objective of the present invention is to provide zwitterionic surfactant impregnated woodpulp sheets for comminution and later deposition to form air-laid absorbent pads, which woodpulp sheets exhibit a surprising ease of comminution to form fibers for deposition into air-laid absorbent pads having improved absorbent characteristics.
  • Another object of this invention is to provided improved air-laid batts, pads, and sheets, for catamenial tampons, sanitary napkins, surgical dressings, disposable diapers and other absorbent pads and fibrous structures, prepared from woodpulp sheets impregnated with the herein disclosed zwitterionic surfactants.
  • Yet another object of the invention is to provide comminution pulp sheets which are easily reduced to individual fibers for use in the production of cellulose chemicals and cellulose derivatives.
  • R is an alkyl or alkenyl group containing about 16 to about 22 carbon atoms
  • R, and R are selected from the group consisting of hydrogen and alkyl groups containing one to two carbon atoms
  • R is an alkylene group containing one to about I 1 carbon atoms, which alkylene group can have one or more hydroxyl groups attached to carbon atoms
  • R is selected from the group consisting of COO', SO;,', and OSO
  • comminution pulp sheets in general have a fairly high basis weight and thickness, for example a comminution pulp sheet can have a basis weight of about 200 lbs. per ream of 500 sheets measuring 19 inches by 24 inches, and a thickness of about 0.050 inches, although the present fiberization and absorbency effects will be noted in comminution pulp sheets of other basis weights and thicknesses.
  • Impregnation can be accomplished by adding the requisite amounts of zwitterionic surfactant to holding tanks or head boxes prior to sheet formation, however, this method of addition is considered wasteful of the relatively high-priced surfactants and is detrimental to continued paper formation in that the entire white water system of the paper machine is inevitably contaminated with surfactant.
  • Applicant has found that one excellent means of addition is that of adding the zwitterionic surfactants of this invention by showering an aqueous dodecanoate.
  • N-octadecyl-N,N-dlmethylarnmonlo-12- solution of the selected zwitterionic surfactant using about 2 lbs, to about 6 lbs. of solution per lb. of pulp (the solution containing about 2000 lbs. of water to about 1 lb. active surfactant) onto a comminution pulp sheet traveling on the forming wire of a paper machine prior to substantial dewatering in the formation process.
  • a preferred method of spray addition in
  • the zwitterionic surfactant addition point can be prior to, over, or following an initial formation vacuum box or dewatering device and can be prior to or within a dandy roll which is positioned prior to subsequent vacuum boxes.
  • These methods of zwitterionic surfactant addition are preferred in order to achieve a uniform distribution of the zwitterionic surfactant across and through the formed sheet and allow, as an additional benefit, adequate displacement of the initial water associated with the formed sheet by the zwitterionic surfactant solution.
  • Other systems for application of the zwitterionic surfactants to comminution pulp sheets will also be effective, if good distribution is achieved.
  • Applicant states that effective amounts of zwitterionic surfactant addition can be about 0.1 percent to about 2.0 percent preferably 0.2 percent, based on the weight of active" zwitterionic surfactant applied and the weight of bone dry pulp. Additions of less than about 0.1 percent by weight of zwitterionic surfactant to pulp sheets do not fully develop the improvement in comminution. Additions of zwitterionic surfactant of more than about 2.0 percent by weight do not contribute further substantial improvement to fiberization or to the absorbent characteristics of subsequently formed air-laid absorbent pads.
  • the zwitterionic surfactant is attracted to the fiber surfaces, and the subsequent sheet strength or fiberization characteristics are an indication of the ability of the surfactant to I) migrate to the fiber, (2) attach to the fiber, and (3) prevent hydrogen or other bonding mechanisms which normally result in the cohesion of fibers to form the type of fibrous sheets which are referred to collectively as paper. It is likely that the zwitterionic surfactants, due to'their structure, provide a larger number of substantive bonds of lesser strength on fibers and provide fibers of lower surface hydrophobicity than do cationic surfactants.
  • zwitterionic surfactants give rise to improved ease of comminution in comminution pulp sheets
  • applicant reemphasizes that incorporation of the zwitterionic surfactants in comminution pulp results in subsequent air-laid absorbent pads having the general characteristics of substantially improved absorbency and loft or bulk properties relative to air-laid absorbent pads prepared from either untreated woodpulp fibers or cationic impregnated wood fibers.
  • Suitable examples of specific zwitterionic surfactants for use in the present invention are:
  • NC1s-C1aalky1 (and aIkeny1)-N,N-dlmethyl- CH3 ammonioacetate.
  • pulp sheet samples are conditioned over night at percent relative humidity and 72 F.
  • the conditioned pulp sheet samples are then cut into 1 inch by 1 inch squares.
  • K whole number of squares weighing 10 W grams is weighed and the weight recorded to constitute a sample.
  • the weighed sample of 1 inch by l inch squares is placed into a Waring Blender (Model No. CB-S) with dull blades and whizzed at the lowest speed (16,500 rpm.) for 15 seconds.
  • the resulting fibers are placed, without densification, on the top of a standard l4-mesh screen placed between two airtight chambers.
  • Compressed air is introduced into the top chamber to violently agitate, but not further comminute the fibers, while the lower chamber is provided with a vacuum system for removing fibers which pass through the screen.
  • the compressed air and vacuum system acting in conjunction provide a 52 mm. Hg differential through the screen, which pressure differential is applied for 2 minutes.
  • the fraction of fiber remaining on the top of the l4-mesh screen and the fraction falling through are then recovered and weighed.
  • the percentage of total fiber weight remaining on the 14-mesh screen is recorded. At least two, and preferably 10, replicate Quick Disintegration tests are made, and their mathematical average is recorded as the test result.
  • the standard Tappi T-233 test method is a Clark fiber classification. As modified slightly by the applicant, this test is run as set forth in Tappi methods with the exception that a Clark classifier (Catalog No. 218-1, Ser. No. 18572) is employed in classification and the Clark method of classification is followed. The weight percentage of the sample retained on the standard 14-mesh screen is recorded as the test result.
  • a Clark classifier Catalog No. 218-1, Ser. No. 18572
  • the weight percentage of the sample retained on the standard 14-mesh screen is recorded as the test result.
  • the Absorptive Capacity test employed by applicant determines the absorptive capacity of air-laid pads in the as-formed state and under mild compression stress.
  • the Absorptive Capacity test is carried out on a 5 inch by 5 inch stainless steel plate inclined at an angle of 15 percent with the horizontal.
  • a 4 inch by 4 inch stainless steel cover plate provided with weights to result in a total loading of 16 lbs., or 1 p.s.i., applied on a 4 inch by 4 inch sample placed between the plates, is also provided.
  • applicant prepares eleven 4 inch by 4 inch air-laid pads whose basis weight varies in definite increments of 0.10 grams from 2.00 grams to 3.00 grams with an allowed tolerance in individual air-laid pads of $0.02 grams.
  • the weight of the individual pads is recorded as W,.
  • the air-laid pads are formed on a sheet of tissue, covered with a second tissue, and cohesively pressed in a dry state at 0.56 p.s.i.
  • the basis weight and absorptive capacity of the covering tissue under loaded and unloaded test compressive conditions is determined by tissue tests performed on the same equipment. The basis weight and absorptive capacity of the covering tissue is cancelled out of the test results by the method usedin test calculation.
  • each of the l 1 prepared and weighed air-laid pads is open end, single wrapped with a 4 inch by 9 inch piece of 1 mm. thickness polyethylene film secured with pressure-sensitive tape.
  • the wrapped sample is placed on a zit-inch thick, inch by 5 inch hard rubber plate, and the weight of the rubber plate together with wrapped sample pad is recorded as W,.
  • the rubber plate with the wrapped sample thereon is placed on the inclined plate, so that the tape-secured side of the sample is up, and the open ends of the wrapped sample are aligned toward the top and bottom of the inclined plate.
  • Distilled and aerated water from an overhead reservoir is distributed on the rubber plate above, outside of and running down into the top end of the wrapped sample at the rate of 500 ml. per minute for 1 minute. Then, beginning at the top and sides of the rubber plate, all excess water outside the wrapped sample is blotted up with absorbent blotting paper, taking care not to touch the wrapped sample pad on either open end.
  • the rubber plate with wrapped sample thereon is then removed from the inclined plate, and the rubber plate is carefully wiped dry in a horizontal position. The weight of the dry rubber plate with wet wrapped sample is then recorded as W;,.
  • the rubber plate with wet wrapped sample thereon is immediately returned to its original position in the inclined plate, and the stainless steel cover plate is gently appliedthereto to result in a l p.s.i. loading on the wet sample.
  • the l p.s.i. cover plate loading is maintained for 45 seconds while excess water is blotted from the rubber plate, as detailed above.
  • the stainless steel cover plate is then removed, and the rubber plate with wet sample thereon is again wiped dry in a horizontal position.
  • the weight of the rubber plate with pressed wrapped wet sample thereon is recorded as W
  • the rubber plate and pressed wrapped wet sample is immediately returned to its original position on the inclined plate and resaturated with 500 ml. of water for 1 minute, as was originally done.
  • the initial zero load wet weight (W,,) the l p.s.i. loaded weight (W and the precompressed zero load weight (W,), with tare of tape secured polyethylene wrap, tissue and rubber plate are determined for the l l samples.
  • the weight determinations W are determined separately for the tissue used as covering for the tested air-laid pads so that the tissue absorptive capacity can be eliminated from the air-laid pad absorbent capacity in calculating the test results.
  • the combined. tissue bottom and top cover sheets (32 sq.'in. per pad) used in the present determinations had a total weight of 0.39 grams.
  • the absorptive capacity of the tissue under test conditions was 12.80 grams H OIgram tissue under initial zero p.s.i. loading, 5.52 grams PLO/gram tissue under 1 p.s.i. loading and 9.23 grams H,O/gram tissue under final zero p.s.i. loading. Having determined the W weights for the l l samples and separate tissue data, the absorptive capacity of the air-laid pads is calculated according to the following formulas, wherein:
  • the Cellulose Absorbency test (drip method) is carried out by preparing three 4 inch by 4 inch tissue-backed, air-laid pads as for the Absorptive Capacity test above, except that the air-laid pad weights are not graduated and have a weight of about 2 grams to about 3 grams. The top and bottom tissue sheets are carefully stripped from the air-laid pads as prepared. The tissue weights and absorbent capacities are thereby eliminated from the calculations in this Cellulose Absorbency test; the weight in grams of the air-laid pad, without tissue covering, is recorded.
  • the prepared air-laid pad is then placed on a horizontally oriented and supported piece of x-inch-square mesh, galvan i zed hardware cloth.
  • An overhead gravity-flow reservoir containing aerated distilled water and equipped with a 56-inch rubber tubing for delivery thereof is provided.
  • the V4-inch rubber tubing is provided with a pinch clamp which is adjusted to give a controlled flow rate of 60 ml. per minute.
  • the waterflow is directed to the center of the horizontal sample from the tubing tip positioned l inch above the sample pad. waterflow is continued until the first drop of water is observed to drip from the bottom side of the supported sample pad.
  • the time elapsed in seconds between first waterflow and first drip is recorded and is equal to the grams of water absorbed by the pad under the Cellulose Absorbency test conditions.
  • the test results are reported as grams H O absorbed per gram pad weight, as calculated by multiplying the seconds of waterflow by the grams of H 0 flowing per second to first drip and dividing the result by the weight of the sample pad in grams.
  • the results for the three pads are calculated individually and mathematically averaged to record a test result.
  • the Cellulose Absorbency test (drip method) constitutes a different procedural method for determining initial zero-loading absorptive capacity.
  • the Bulk Fiber Sink test measures the rate of water absorption into comminuted cellulose fibers at a bulk density of0.05 grams/cubic centimeter.
  • the selected cellulose bulk density is substantially equivalent to the bulk density of a cellulose fiber pad as formed in conventional air-laying procedures.
  • the Bulk Fiber Sink test has advantage in that it is convenient, fast and reproducible to confidence limits of 99.9 percent.
  • a plexiglass tube having an ID of L5 inches, an OD of 1.75 inches and a length of 12 inches is fixed in a vertical position.
  • the plexiglass tube is provided with a 20-mesh screen for foraminously closing its bottom end.
  • the plexiglass tube is loaded with 16.9 grams of comminuted cellulose fibers in a vbiiim'eof's'as' cubic centimeters to result in the test bulk density of 0.05 grams/cubic centimeter.
  • Plexiglass tube loading is accomplished by taking small undensified increments of comminuted cellulose fibers and introducing them into the plexiglass tube to provide 16.9 grams of sample; the sample is then lightly compacted to result in the specified bulk density.
  • a 1,000 ml. graduated Pyrex cylinder is filled to the 800 ml. mark with distilled aerated water at 72 t 2 F.
  • the fiber-loaded plexiglass tube is then positioned vertically with its screen one-half inch above the water surface in the Pyrex graduated cylinder; the plexiglass tube is then released.
  • the time in seconds from release to complete submersion of the compacted cellulose fibers within the plexiglass tube is recorded.
  • Ten replicate tests are run with new fillings of distilled aerated water in the graduated cylinder and newly loaded comminuted fiber samples. The mathematical average of time for submersion in seconds for the tests is recorded as the test result.
  • the Embossed Pad Wicking test measures the time for water to proceed under the impetus of capillary action along a vertically oriented zigzag linear embossed region, with a total length of 5.6 inches, in a tissue-backed air-laid pad.
  • the zigzag embossed line has a width of about one-thirtysecond inch.
  • the zigzag linear embossed region is formed by part of an enclosed rectilinear embossing pattern formed by two sets of parallel embossed lines. The embossed lines in each set are spaced 1 inch apart, and the intersections of the lines in the two sets have included angles of 53.2" and 126.8 where they cross.
  • a sample cut to include an unbroken zigzag embossed line and oriented so that the 126.8" included angles are vertically opposed is held by a clip in a vertical position.
  • the bottom oneeighth inch of the sample resides in an aerated distilled-water reservoir maintained at 72 i 2 F.
  • tissue-covered air-laid pads for the Embossed Pad Wicking test are prepared in the same rnanner as pads for the Absorptive Capacity test with exception that six pads having a weight per 4 inch by 4 inch pad of 2 to 3 grams are prepared. These tissue-covered pads are then embossed with the pattern described above by use of an embossing platen on which the test pad and 0.002 inch metal shim for final plate clearance are laid. The pad is then pressed in a hydraulic press (Carver Press pressure of 20,000 p.s.i.g.) to emboss the pattern on the pad. The water is changed after each six samples, and the mathematical average time in seconds for the six samples is taken as the test result.
  • a hydraulic press Carver Press pressure of 20,000 p.s.i.g.
  • the Loft test which determines the bulk density of an airlaid pad with tissue backing, is carried out by preparing 4 inch by 4 inch tissue-backed pads as in the Absorptive Capacity test, with the exception that 10 pads are prepared at a 2- to 3- gram tissue-backed pad weight. The 10 pads are stacked and the height measured. The volume is then taken as 4 inches X 4 inches X the stack height in inches and converted to cubic centimeters. The bulk density (neglecting the neglible volume of the thin tissue backing sheets) is equal to the weight of the 10-pad stack minus 3.9 grams of tissue weight divided by the determined volume in cubic centimeters. A lower bulk density figure is indicative of greater bulk or loft.
  • the cellulose fibers used to prepare air-laid pads in the foregoing test procedures can be prepared by hammer-milling comminution pulp sheets in a mill equipped with an 8-mesh screen plate and dull hammers to avoid fiber cutting.
  • a Sprout-Waldron mill was also used effectively to prepare cellulose fibers for test purposes.
  • comminution sheets of Southern pine bleached fiber woodpulp were formed and dried to have a basis weight, at a 5 percent by weight moisture content, of 210 lbs. per ream of 500 sheets measuring 19 inches by 24 inches.
  • the sheet had an average thickness of 0.050 inches.
  • a distribution system of showers delivered approximately 300 g.p.m. of an aqueous solution containing 00005 lbs. of active surfactant per pound of aqueous solution. This amount of surfactant resulted in a pulp sheet containing about 0.2 percent active surfactant by weight based on the weight of bone dry pulp.
  • comminution pulp sheets were prepared containing the stated amount of the zwitterionic surfactant, N-tallowalkyl-N,N-dimethylammonioacetate (supplied under the trade name Culveram TDG by Culver Chemical Co.) and the cationic surfactant, dimethyl dihydrogenated tallow alkyl quaternary ammonium chloride, (supplied under the trade name Formonyte 1703 by the Foremost Chemical Products Co.). lndentical comminution pulp sheets containing no surfactant were also prepared. The described tests were performed on the compared comminution pulp sheets, and the test results are tabulated in table 1 below.
  • the results of the Tappi T-233 test illustrate that the Standard Pulp sample without surfactant was not only incompletely fiberized, but was, in part, reduced in fiber length by comminution; since 51.4 percent of the sample was retained on the standard 14-mesh screen prior to fiberization, and only 44.4 percent of the sample was retained after fiberization.
  • the Tappi T-233 test illustrates that the zwitterionic surfactant impregnated sample not only provided ease of comminution TABLE I.-ABSORPTIVE CAPACITY TAPPI Cellulose T-233 absorbency Wicking Quick (Clark 0 p.s.i. 0 psi. (drip (embossed disinteclassifi- Avg.
  • the test results presented for the Absorptive Capacity test illustrate an overall advantage for the zwitterionic surfactantimpregnated sample over both the Standard Pulp sheet and the cationic surfactant-impregnated sample; the superiority of zwitterionic surfactant impregnation is also illustrated by the results of the Cellulose Absorbency test.
  • results tabulated for the Bulk Fiber Sink and Wicking tests illustrate the clear superiority of zwitterionic surfactant impregnation over cationic surfactant impregnation in pulp sheet samples which otherwise exhibit the characteristic of improved cornminution.
  • the tabulated results of the Loft test illustrate the superiority of the zwitterionic-impregnated sample in the bulk and resiliency properties desirablein absorbent disposable batts, pads and sheets.
  • the absorbent air-laid pads comprised of zwitterionic surfactant impregnated fibers have specific utility in bandages, diapers, sanitary
  • a method for the manufacture of a comminution pulp sheet which method comprises impregnating the cellulosic fibers of said pulp sheet, prior to final dewatering in sheet formation, with about 0.1 percent to about 2.0 percent, based on the weight of active surfactant and the bone dry weight of said pulp sheet, of a zwitterionic surfactant having the general structure:
  • R is a alkyl or alkenyl group containing about 16 to about 22 carbon atoms
  • R: and R ' are selected from the group consisting of hydrogen and alkyl groups containing one to two carbon atoms
  • R is an alkylene group containing one to about 1 1 carbon atoms, which alkylene group can have one or more hydroxyl groups attached to carbon atoms
  • R is selected from the group consisting of -COO, SO and OSO whereby the comminution of said pulp sheet and the absorbency characteristics of air-laid absorbent pads produced therefrom are improved.
  • a method for the manufacture of a comminution pulp sheet which method comprises impregnating the cellulosic fibers of said pulp sheet, prior to final dewatering in sheet formation, with about 0.1 percent to 2.0 percent of a zwitterionic surfactant selected from the group consisting of N-octadecyl- N ,N-dimethylammoniol Z-dodecanoate, N-eicosyl-N ,N- dimethylammonio-3-propane-1-sulfonate, N-tallowalkyl-N,N- dimethylammonio-2-hydroxy-B-propane-l-sulfonate, N-C C alkyl (and alkenyl)-N,N-dimethylammonioacetate, N-( 2- hydroxy, C -C alkyl)-N,N-dimethylammoniacetate, N-tallowalkyl-N,N-dimethylammonioacetate, N-soyaal
  • a method for the manufacture of a comminution pulp sheet which method comprises impregnating the cellulosic fibers of said pulp sheet prior to final dewatering in sheet formation with about 0.1 percent to about 2.0 percent of N-tallowalkyl-N,N-dimethyiammonioacetate, whereby the comminution of said pulp sheet and the absorbency characteristics of air-laid absorbent pads produced therefrom are improved.
  • a comminution pulp sheet the cellulosic fibers of which pulp sheet are impregnated with about 0.1 percent to about 2.0 percent, based on the weight of active surfactant and the bone dry weight of said pulp sheet, of a zwitterionic surfactant having the general structure:
  • R is an alkyl or alkenyl group containing about l6 to about 22 carbon atoms
  • R, and R are selected from the group consisting of hydrogen and alkyl groups containing one to two carbon atoms
  • R is an alkylene group containing one to about 1 1 carbon atoms, which alkylene group can have one or more hydroxyl groups attached to carbon atoms
  • R is selected from the group consisting of -CO0', SO;,, and -OSO;,', whereby the comminution of said pulp sheet and the absorbency characteristics of air-laid absorbent pads produced therefrom are improved.
  • a comminution pulp sheet the cellulosic fibers of which pulp sheet are impregnated with about 0.1 percent to about 2.0 percent, based on the weight of active surfactant and the weight of bone dry pulp, of a zwitterionic surfactant selected from the group consisting of N-octadecyl-N,N-dimethylammonio-l2'dodecanoate, N-eicosyl-N,N-dimethylammonio-3- propane-l-sulfonate, N-tallowalkyl-N,N-dimethylammonio-2- hydroxy-3-propane-l-sulfonate, N-C -C alkyl (and alkenyl)- N,N-dimethylammonioacetate, N-(2-hydroxy,C, -C alkyl)- N,N-dimethylammonioacetate, N-tallowalkyl-N,N- dimethylammonioacetate, N-soyaal

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US789084A 1969-01-02 1969-01-02 Process for improving comminution pulp sheets and resulting air-laid absorbent products Expired - Lifetime US3617439A (en)

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DE (1) DE2000028C3 (fi)
FI (1) FI55534C (fi)
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NL (1) NL164914C (fi)
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Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4026291A (en) * 1974-05-25 1977-05-31 Tadashi Nagano Article for treating secreting fluid of the human body
US4065347A (en) * 1975-02-26 1977-12-27 Molnlycke Ab Method of producing fluffed pulp
US4130637A (en) * 1977-01-31 1978-12-19 Colgate-Palmolive Company Anti-plaque agents
US4259249A (en) * 1979-06-13 1981-03-31 The Procter & Gamble Company Preparation of hydroxyl zwitterionic compounds
US4314060A (en) * 1979-07-16 1982-02-02 The Procter & Gamble Company Oxaalkanoate anti-ulcer compounds
EP0184603A1 (en) * 1984-12-07 1986-06-18 Korsnäs-Marma Ab Process for preparing a fluff pulp
US4600462A (en) * 1981-09-29 1986-07-15 James River/Dixie-Northern, Inc. Incorporation of a hydrophile in fibrous webs to enhance absorbency
US4786367A (en) * 1987-08-06 1988-11-22 Scott Paper Company Chemically treated paper products--towel and tissue
WO1990005808A1 (en) * 1988-11-17 1990-05-31 Sca Pulp Ab Easily defibered web-shaped paper product
US5458737A (en) * 1993-07-27 1995-10-17 Hoechst Celanese Corporation Quaternary compounds as brightness enhancers
US5560805A (en) * 1993-07-27 1996-10-01 Hoechst Celanese Corporation Enhanced decolorization of waste paper with selected amines
US5580422A (en) * 1993-07-27 1996-12-03 Hoechst Celanese Corporation Brightening color dyed wastepaper with a bleaching agent and a quaternary compound
US5749863A (en) * 1994-03-18 1998-05-12 The Procter & Gamble Company Fluid acquisition and distribution member for absorbent core
US5873979A (en) * 1994-03-18 1999-02-23 The Procter & Gamble Company Preparing individualized polycarboxylic acid crosslinked cellulosic fibers
US6344109B1 (en) 1998-12-18 2002-02-05 Bki Holding Corporation Softened comminution pulp
US20040214702A1 (en) * 2003-04-25 2004-10-28 Stroud Herbert D. Process for the conversion of cellulose acetate waste fibers into a suitable form for paper production and the resultant paper products
WO2004113608A2 (de) * 2003-06-16 2004-12-29 Hakle-Kimberly Deutschland Gmbh Airlaidverfahren mit verbessertem durchsatz
US20050023714A1 (en) * 1996-11-13 2005-02-03 Manner D. Lee Absorbent and time release material
US20140102655A1 (en) * 2009-08-05 2014-04-17 International Paper Company Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality
US20150184338A1 (en) * 2013-12-31 2015-07-02 Weyerhaeuser Nr Company Treated kraft pulp compositions and methods of making the same
US10260201B2 (en) 2009-08-05 2019-04-16 International Paper Company Process for applying composition containing a cationic trivalent metal and debonder and fluff pulp sheet made from same
US10415190B2 (en) 2009-08-05 2019-09-17 International Paper Company Dry fluff pulp sheet additive
US11447893B2 (en) 2017-11-22 2022-09-20 Extrusion Group, LLC Meltblown die tip assembly and method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB8811955D0 (en) * 1988-05-20 1988-06-22 Allied Colloids Ltd Absorbent products & their manufacture

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US2313573A (en) * 1938-01-17 1943-03-09 Gen Aniline & Film Corp Capillary active compounds and process of preparing them
US2548428A (en) * 1949-05-06 1951-04-10 Goodrich Co B F Preparation of quaternary amines from tertiary amines and betalactones
US2778749A (en) * 1952-12-22 1957-01-22 Monsanto Chemicals Paper products and manufacture thereof
US3296065A (en) * 1963-10-07 1967-01-03 Monsanto Co Paper products containing carboxylic acid esters and process for preparing such products
US3377382A (en) * 1964-07-16 1968-04-09 Gen Mills Inc Difatty alkyl-diloweralkyl quaternary ammonium compounds
US3395708A (en) * 1966-11-09 1968-08-06 Riegel Textile Corp Method for improving a fluffed fibrous wood pulp batt for use in sanitary products and the products thereof
GB1128836A (en) * 1966-06-10 1968-10-02 Procter & Gamble Ltd Detergent composition
CA796279A (en) * 1966-02-08 1968-10-08 The Procter & Gamble Company Soap compositions

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Publication number Priority date Publication date Assignee Title
US2313573A (en) * 1938-01-17 1943-03-09 Gen Aniline & Film Corp Capillary active compounds and process of preparing them
US2548428A (en) * 1949-05-06 1951-04-10 Goodrich Co B F Preparation of quaternary amines from tertiary amines and betalactones
US2778749A (en) * 1952-12-22 1957-01-22 Monsanto Chemicals Paper products and manufacture thereof
US3296065A (en) * 1963-10-07 1967-01-03 Monsanto Co Paper products containing carboxylic acid esters and process for preparing such products
US3377382A (en) * 1964-07-16 1968-04-09 Gen Mills Inc Difatty alkyl-diloweralkyl quaternary ammonium compounds
CA796279A (en) * 1966-02-08 1968-10-08 The Procter & Gamble Company Soap compositions
GB1128836A (en) * 1966-06-10 1968-10-02 Procter & Gamble Ltd Detergent composition
US3395708A (en) * 1966-11-09 1968-08-06 Riegel Textile Corp Method for improving a fluffed fibrous wood pulp batt for use in sanitary products and the products thereof

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Schwarty and Perry, Surface Active Agents, 1949 p. 172. *

Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4026291A (en) * 1974-05-25 1977-05-31 Tadashi Nagano Article for treating secreting fluid of the human body
US4065347A (en) * 1975-02-26 1977-12-27 Molnlycke Ab Method of producing fluffed pulp
US4130637A (en) * 1977-01-31 1978-12-19 Colgate-Palmolive Company Anti-plaque agents
US4259249A (en) * 1979-06-13 1981-03-31 The Procter & Gamble Company Preparation of hydroxyl zwitterionic compounds
US4314060A (en) * 1979-07-16 1982-02-02 The Procter & Gamble Company Oxaalkanoate anti-ulcer compounds
US4600462A (en) * 1981-09-29 1986-07-15 James River/Dixie-Northern, Inc. Incorporation of a hydrophile in fibrous webs to enhance absorbency
EP0184603A1 (en) * 1984-12-07 1986-06-18 Korsnäs-Marma Ab Process for preparing a fluff pulp
US4786367A (en) * 1987-08-06 1988-11-22 Scott Paper Company Chemically treated paper products--towel and tissue
WO1990005808A1 (en) * 1988-11-17 1990-05-31 Sca Pulp Ab Easily defibered web-shaped paper product
US5262005A (en) * 1988-11-17 1993-11-16 Sca Pulp Ab Easily defibered web-shaped paper product
US5458737A (en) * 1993-07-27 1995-10-17 Hoechst Celanese Corporation Quaternary compounds as brightness enhancers
US5560805A (en) * 1993-07-27 1996-10-01 Hoechst Celanese Corporation Enhanced decolorization of waste paper with selected amines
US5580422A (en) * 1993-07-27 1996-12-03 Hoechst Celanese Corporation Brightening color dyed wastepaper with a bleaching agent and a quaternary compound
US5749863A (en) * 1994-03-18 1998-05-12 The Procter & Gamble Company Fluid acquisition and distribution member for absorbent core
US5873979A (en) * 1994-03-18 1999-02-23 The Procter & Gamble Company Preparing individualized polycarboxylic acid crosslinked cellulosic fibers
US20050023714A1 (en) * 1996-11-13 2005-02-03 Manner D. Lee Absorbent and time release material
US6533898B2 (en) 1998-12-18 2003-03-18 Bki Holding Corporation Softened comminution pulp
US6344109B1 (en) 1998-12-18 2002-02-05 Bki Holding Corporation Softened comminution pulp
US20040214702A1 (en) * 2003-04-25 2004-10-28 Stroud Herbert D. Process for the conversion of cellulose acetate waste fibers into a suitable form for paper production and the resultant paper products
WO2004113608A2 (de) * 2003-06-16 2004-12-29 Hakle-Kimberly Deutschland Gmbh Airlaidverfahren mit verbessertem durchsatz
WO2004113608A3 (de) * 2003-06-16 2005-04-21 Hakle Kimberly De Gmbh Airlaidverfahren mit verbessertem durchsatz
US20070266503A1 (en) * 2003-06-16 2007-11-22 Hakle-Kimberly Deutschland Gmbh Airlaid Method with an Improved Through-Put Rate
AU2004249862B2 (en) * 2003-06-16 2010-08-19 Hakle-Kimberly Deutschland Gmbh Airlaid method with an improved through-put rate
US20140102655A1 (en) * 2009-08-05 2014-04-17 International Paper Company Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality
US9260820B2 (en) * 2009-08-05 2016-02-16 International Paper Company Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality
US10260201B2 (en) 2009-08-05 2019-04-16 International Paper Company Process for applying composition containing a cationic trivalent metal and debonder and fluff pulp sheet made from same
US10415190B2 (en) 2009-08-05 2019-09-17 International Paper Company Dry fluff pulp sheet additive
US10513827B2 (en) 2009-08-05 2019-12-24 International Paper Company Composition containing a cationic trivalent metal and debonder and methods of making and using the same to enhance fluff pulp quality
US20150184338A1 (en) * 2013-12-31 2015-07-02 Weyerhaeuser Nr Company Treated kraft pulp compositions and methods of making the same
CN107740303A (zh) * 2013-12-31 2018-02-27 韦尔豪泽Nr公司 处理过的硫酸盐浆粕组合物及其制造方法
US11332883B2 (en) 2013-12-31 2022-05-17 International Paper Company Treated Kraft pulp compositions and methods of making the same
US11447893B2 (en) 2017-11-22 2022-09-20 Extrusion Group, LLC Meltblown die tip assembly and method

Also Published As

Publication number Publication date
NL164914B (nl) 1980-09-15
DE2000028B2 (de) 1978-04-13
DE2000028C3 (de) 1978-12-14
FR2027674A1 (fi) 1970-10-02
NO128668B (fi) 1973-12-27
SE366788B (fi) 1974-05-06
GB1300236A (en) 1972-12-20
FI55534C (fi) 1979-08-10
NL164914C (nl) 1981-02-16
DE2000028A1 (de) 1970-07-16
NL6919620A (fi) 1970-07-06
FI55534B (fi) 1979-04-30

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