EP1505208A2 - Procédé de préparation de produits papier tissu contanant des fibres cellulosiques carboxylées - Google Patents

Procédé de préparation de produits papier tissu contanant des fibres cellulosiques carboxylées Download PDF

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Publication number
EP1505208A2
EP1505208A2 EP04254647A EP04254647A EP1505208A2 EP 1505208 A2 EP1505208 A2 EP 1505208A2 EP 04254647 A EP04254647 A EP 04254647A EP 04254647 A EP04254647 A EP 04254647A EP 1505208 A2 EP1505208 A2 EP 1505208A2
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EP
European Patent Office
Prior art keywords
carboxylated
pulp
fibers
tissue
wet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP04254647A
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German (de)
English (en)
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EP1505208A3 (fr
Inventor
Alan R. Winslow
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Weyerhaeuser Co
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Weyerhaeuser Co
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Publication date
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Publication of EP1505208A2 publication Critical patent/EP1505208A2/fr
Publication of EP1505208A3 publication Critical patent/EP1505208A3/fr
Withdrawn legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/14—Making cellulose wadding, filter or blotting paper
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21F—PAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00—Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/14—Making cellulose wadding, filter or blotting paper
    • D21F11/145—Making cellulose wadding, filter or blotting paper including a through-drying process
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
    • D21H27/30—Multi-ply
    • D21H27/38—Multi-ply at least one of the sheets having a fibrous composition differing from that of other sheets
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
    • D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
    • D21H11/20—Chemically or biochemically modified fibres
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/18—Reinforcing agents
    • D21H21/20—Wet strength agents

Definitions

  • the present invention relates to a tissue product containing carboxylated cellulosic fibers and methods for making the tissue product.
  • Tissue paper or sheets such as facial and toilet tissues and paper toweling, are common commercially available consumer products. Important physical attributes of these products include strength, absorbency, and softness, among others.
  • An ideal tissue product has high wet and dry strength. Strength is the ability of the tissue product, as well as tissue product webs, to maintain physical integrity and to resist tearing, bursting, and shredding under use conditions, including when wet.
  • An ideal tissue product, more specifically paper toweling, also has high liquid absorbency. Absorbency is the measure of the ability of the tissue product and tissue webs to absorb quantities to liquids, including aqueous solutions and dispersions. Ideally, a tissue product will have high absorbency with respect to the total quantity of liquid absorbed given a mass of the tissue product as well as a fast rate that the tissue product absorbs liquid.
  • Tissue products are paper sheets made by a process that includes the steps of forming an aqueous papermaking furnish, depositing the furnish on a forming wire, and removing the water from the furnish to provide the sheet.
  • the aqueous papermaking furnish is an aqueous slurry of papermaking fibers and chemicals.
  • wood pulp is the major constituent of papermaking fibers, other fibers can be included.
  • Wood pulps include chemical pulps, such as kraft and sulfite pulps; and mechanical pulps, such as ground wood, thermomechanical pulps, and chemi-thermomechanical pulps.
  • blends of pulp fibers are often used in the furnish for making tissue products, strengthening agents are commonly included to increase tissue product wet and dry strength.
  • the furnish includes chemicals, for example, strengthening agents and debonding agents, to enhance the strength and softness of the tissue product.
  • tissue products exist and significant advances in tissue products have occurred, there exists a need for further improvements in tissue products, particularly for tissue products having increased strength and more particularly, increased wet strength.
  • the invention provides a tissue product having two or more layers, with at least one layer including carboxylated cellulosic fibers.
  • the carboxylated fiber-containing layer can include from about 0.5 to about 100 percent by weight carboxylated cellulosic fibers.
  • the carboxylated fiber-containing layer can also include a variety of other cellulosic and synthetic fibers.
  • the carboxylated fiber-containing layer includes about 75 percent by weight carboxylated fibers and about 25 percent by weight bleached spruce chemi-thermomechanical pulp fibers.
  • the carboxylated fiber-containing layer can also include a wet strength agent and other additives, such as carboxymethyl cellulose (CMC).
  • CMC carboxymethyl cellulose
  • tissue product in another aspect of the invention, methods for making the tissue product are provided.
  • the product can be made on any type of tissue machine, such as a through-air dried tissue machine or a conventional tissue machine.
  • the tissue product is made by depositing a first fibrous furnish onto a forming wire to provide a first deposited furnish; depositing a second fibrous furnish onto the first deposited furnish to provide a wet web; withdrawing water from the wet web to provide a sheet; and drying the sheet to provide the tissue product having at least two layers.
  • At least one of the first fibrous furnish or the second fibrous furnish includes carboxylated cellulosic fibers to provide the tissue product in which at least one layer includes carboxylated cellulosic fibers.
  • more than two fibrous furnishes are deposited to provide a tissue product having more than two layers.
  • the present invention provides a tissue product that includes carboxylated cellulosic fibers.
  • methods for making the tissue product are provided.
  • the tissue product of the invention includes carboxylated cellulosic fibers that impart advantageous properties to these tissue products superior to those for other tissue products that do not include carboxylated cellulosic fibers.
  • the tissue product of the invention can be a facial tissue, toilet tissue, disposable wipe, napkin, handkerchief, or paper towel.
  • the tissue product of the invention includes two or more layers, and may include one or more plies. Layers can be made on a tissue machine. A layer can include one or more types of fibers.
  • a representative tissue of the invention is a three layered paper towel sheet with two fiber types in each layer.
  • a representative toilet tissue may have three layers with the middle layer having a different fiber type than the outer layers. Plies refer to combining two or more tissues (sheets) during the converting process.
  • a finished product paper towel, toilet tissue, facial tissue, or napkin may include one or more plies.
  • the tissue product of the invention includes at least two layers, with at least one layer including carboxylated cellulosic fibers.
  • the tissue product includes a layer that includes carboxylated cellulosic fibers, other cellulosic fibers, cationic additives such as wet strength agents, and, optionally, other strength additives.
  • the tissue product of the invention is characterized as having comparable or improved wet strength, cationic additive interaction, water retention value, bulk, dry strength, absorbency, fiber refining energy requirement, and on-machine dewatering compared to tissue products that do not include carboxylated cellulosic fibers.
  • the tissue product includes at least one layer that includes carboxylated cellulosic fibers.
  • Carboxylated fibers can be prepared by a variety of processes. Suitable carboxylated fibers have a carboxyl content from about 5 to about 60 meq/100 g cellulose and a degree of polymerization of at least about 600. Suitable carboxylated fibers can be prepared by carboxylation processes described in WO 01/29309 and U.S. Patent No. 6,379,494, entitled Method of Making Carboxylated Cellulose Fibers in Products of the Method, each incorporated herein by reference in its entirety.
  • the carboxylated fiber is produced by a two-stage process: (1) catalytic cellulose oxidation (e.g., a catalytic oxidizer and a secondary oxidizer, such as chlorine dioxide) and (2) oxidized cellulose stabilization (e.g., reduction or oxidation).
  • catalytic cellulose oxidation e.g., a catalytic oxidizer and a secondary oxidizer, such as chlorine dioxide
  • oxidized cellulose stabilization e.g., reduction or oxidation
  • the process can be integrated into a pulp mill bleach plant to provide the carboxylated fiber pulp.
  • suitable carboxylated fibers are prepared by chlorine dioxide oxidation using triacetone amine ethylene glycol ketal catalyst followed by oxidative stabilization with sodium chlorite and hydrogen peroxide.
  • Suitable carboxylated fibers can be made from hardwood and softwood chemical pulps. Suitable carboxylated fibers have a total carboxyl content greater than about 6 meq/100 g cellulose and less than about 60 meq/100 g cellulose. In one embodiment, the C6 carboxyl content is greater than about 2 meq/100 g cellulose. C6 carboxyl content refers to extent of carboxylation at C6 of the anhydroglucose unit of cellulose to provide a glucuronic acid derivative. Suitable carboxylated fibers have a low aldehyde content, less than about 1 meq/100 g cellulose.
  • Suitable carboxylated fibers has a degree of polymerization greater than 700 in pre-acid form and greater than 850 in sodium salt form.
  • the carboxylated fiber has an ISO brightness in the range from about 75 to about 95 percent.
  • the softwood carboxylated fiber viscosity is greater than about 18 mPa.
  • the carboxylated fiber can be provided to the tissue machine in either dried or never-dried form.
  • the carboxylated fiber can be refined to drainage and strength targets in a dilute aqueous suspension using commercially available pulp refiners.
  • the carboxylated fiber-containing layer of the tissue product of the invention can include one or more other pulp fibers.
  • Suitable other pulp fibers include, for example, recycled fibers, bleached kraft hardwood fibers, bleached kraft softwood fibers (e.g., northern bleached softwood kraft pulp, NBSK), bleached sulfite fibers, and bleached chemi-thermomechanical pulp (BCTMP) fibers.
  • the tissue product useful as a paper towel includes a layer that includes a combination of carboxylated cellulosic fibers and BCTMP fibers. Unbleached pulp fibers and non-pulp fibers can also be used. The selection criteria of other fibers for inclusion in addition to the carboxylated fiber will depend upon the end use product being produced, and are well know to those familiar with the art.
  • a paper towel may include a layer that can contain from about 0.5 to about 100 percent by weight carboxylated fiber based on the total weight of fiber
  • a facial or toilet tissue may include a layer that can contain from about 10 to about 100 percent carboxylated fiber based on the total weight of fiber.
  • the carboxylated fiber-containing layer of the tissue product of the invention includes a wet strength agent.
  • Suitable wet strength agents are cationic additives such as, for example, cationic starch, urea-formaldehyde resins, melamine-formaldehyde resins, polyethylenimine resins, polyacrylamide resins, and polyacrylamide-epichlorohydrin resins.
  • the wet strength agent is a polyacrylamide-epichlorohydrin resin commercially available under the designation KYMENE from Hercules Inc., Wilmington DE.
  • the wet strength agent can be present in the tissue product in an amount from about 5 to about 50 lb/ton fiber. In one embodiment, the wet strength agent is present in about 10 lb/ton fiber; in another embodiment, about 25 lb/ton fiber; and in another embodiment, about 40 lb/ton fiber.
  • the wet strength agent is a permanent wet strength agent, such as a polyacrylamide-epichlorohydrin resin.
  • the wet strength agent is a temporary wet strength agent, such as cationic starch.
  • the carboxylated fiber-containing layer of the tissue product can also include other strength additives.
  • Other suitable strength additives include, for example, carboxymethyl cellulose (CMC).
  • CMC carboxymethyl cellulose
  • the carboxylated fiber-containing layer can include up to about 10 lb/ton CMC based on the total weight of fibers. In one embodiment, the carboxylated fiber-containing layer includes about 4 lb/ton CMC, and in another embodiment, the carboxylated fiber-containing layer includes about 8 lb/ton CMC.
  • Other chemicals useful in making tissue products can optionally be used during the tissue making process.
  • Other useful chemicals include retention aids, softeners, surfactants, Yankee coating, and through-air dryer release spray.
  • the tissue product of the invention is characterized as having greater wet tensile and burst strength than tissue made from commercial pulps (e.g., bleached northern softwood kraft pulps); greater wet strength/dry strength ratio (wet burst/dry tensile, WB/DT ratio, or wet tensile/dry tensile, WT/DT ratio) than tissues made with commercial pulps; dry tensile strength that is equal to or greater than that of tissue products made from commercial pulps; and a greater Tensile Energy Absorption (TEA) Index than tissue products made with commercial pulps.
  • TSA Tensile Energy Absorption
  • the tissue product of the invention including carboxylated fibers has a wet burst/dry tensile ratio from about 0.20 to about 0.40.
  • the other layers of the tissue product of the invention can include one or more of the materials described above including, for example, carboxylated cellulosic fibers.
  • a method for making a tissue product that includes carboxylated cellulosic fibers is provided.
  • the tissue product is made on a tissue machine.
  • the carboxylated fiber which may be refined, is combined with one or more other pulps, and strength additives, as desired, and fed into the tissue machine headbox.
  • the carboxylated fiber can be a separate furnish or one of several pulps mixed together to create one layer in the multi-layered tissue sheet.
  • the carboxylated fibers can make up from about 0.5 percent to 100 percent of the tissue furnish.
  • the carboxylated fiber can be present in one or more layers of a multi-layered tissue sheet.
  • the wet web or sheet produced by depositing the headbox contents onto a foraminous support is processed through the various unit operations of the tissue machine to produce a dry tissue jumbo roll.
  • the tissue jumbo roll can be further processed through various converting equipment into the finished consumer product, for example, toilet tissue, facial tissue, paper toweling.
  • the tissue product of the invention can be produced on a variety of tissue machines including, for example, conventional machines, creped through-air dried machines, or un-creped through-air dried machines.
  • tissue machine 100 includes layered head box 10 having top chamber 12, center chamber 16, and bottom chamber 14, Fourdrinier wire 20 looped over and about breast roll 101, vacuum suction boxes 30, and couch roll 102.
  • tissue machine 100 includes layered head box 10 having top chamber 12, center chamber 16, and bottom chamber 14, Fourdrinier wire 20 looped over and about breast roll 101, vacuum suction boxes 30, and couch roll 102.
  • a first papermaking furnish is pumped through top chamber 12
  • a second papermaking furnish is pumped through center chamber 16
  • a third furnish is pumped through bottom chamber 14 onto wire 20 to form embryonic web 40 having layers 40a, 40b, and 40c. Dewatering occurs through wire 20 and vacuum boxes 30.
  • showers 50 clean the wire prior to its beginning another pass over breast roll 101.
  • embryonic web 40 is transferred to foraminous carrier fabric 62 by the action of vacuum transfer box 64.
  • Carrier fabric 62 carries the web from transfer zone 60 past vacuum dewatering box 66 through predryers, or through-air dryers, 68 after which the web is transferred to a Yankee dryer 70 by the action of pressure roll 103.
  • the carrier fabric 62 is then cleaned and dewatered as it completes its loop by passing showers 52 and vacuum dewatering box 54.
  • the predried paper web is adhesively secured to the cylindrical surface of Yankee dryer 70 by adhesive supplied by spray applicator 80.
  • Drying is completed on steam-heated Yankee dryer 70 and by hot air heated and circulated through drying hood 90.
  • the web is then dry creped from Yankee drier 70 by doctor blade 82 after which sheet 42 including a Yankee-side layer 42a, a center layer 42b, and an off-Yankee-side layer 42c.
  • Sheet 42 then passes between calendar rolls 104 and 105 and is reeled onto core 106 disposed on shaft 107 to provide roll 44.
  • the carboxylated fiber-containing layer may be any one or more of the layers.
  • the carboxylated fiber-containing layer of the tissue product may be the middle layer of the tissue product, or one or both of the outer layers of the tissue product.
  • the NBSK (carboxylated fiber or control) inclusion rate was 75 percent; the basis weight split between layers (air/core/Yankee) was 33 percent/34 percent/33 percent; the reel basis weight was 20.5 gsm; the Yankee speed was 1100 mpm; and the twin-wire former/through-air drier wire speed ratio was 1.15 which created a fabric crepe of 15 percent.
  • the machine was operated to control several machine variables: (1) refining energy input to achieve target NBSK freeness or NBSK refining energy input; and (2) through-air drier energy input was adjusted to keep sheet solids exiting the through-air drier greater than 85 percent. This trial was conducted on Metso Paper Karlstad AB's pilot through-air dried paper machine located in Karlstad, Sweden.
  • tissue products in roll form were prepared on the tissue machine described above.
  • the tissue product produced by the paper machine was typical of a premium consumer paper towel.
  • the tissue product included either commercial pulp (NBSK) or carboxylated NBSK pulp fibers, bleached chemi-thermomechanical pulp (BCTMP), a wet strength agent, and, optionally, carboxymethyl cellulose.
  • Experimental variables included NBSK or carboxylated fiber refining energy input and strengthening agents' addition rates.
  • PA control refers to a northern bleached softwood kraft pulp (Prince Albert, Saskatchewan); TR962 refers to carboxylated pulp fibers; TR963 refers to a fully bleached, Prince Albert northern bleached softwood kraft pulp dried in the same manner as TR962; inclusion rate refers to the percentage of the PA Control or TR962 or TR963 pulp included in the sheet, the remainder of the pulp included in the sheet was a bleached chemi-thermomechanical pulp (BCTMP) having a brightness of 80 and a Canadian Standard Freeness (CSF) of 525, commercially available from Södra Cell AB; the wet strength agent was a polyamide-epichlorohydrin resin, KYMENE SLX from Hercules; and the strength additive was carboxymethyl cellulose, CMC 7-MT from Metsa Chemical.
  • BCTMP bleached chemi-thermomechanical pulp
  • CSF Canadian Standard Freeness
  • FIGURE 3 is a table comparing the properties of sheets prepared from control pulps.
  • FIGURE 4 is a table summarizing the properties of sheets prepared from a carboxylated fiber pulp and a control at 460-480 CSF, 25 lb/ton wet strength agent, and 4 lb/ton carboxymethyl cellulose.
  • FIGURE 5 is a table illustrating the effect of carboxymethyl cellulose on the properties of sheets prepared from a carboxylated fiber pulp and a control pulp at 53 kWh/mt refining energy input and 25 lb/ton wet strength agent.
  • the data shows that the tissue products including the carboxylated cellulosic fibers have improved sheet properties at equal inclusion rate, equal NBSK refining energy input, equal wet strength agent addition rate, and equal CMC addition rate compared to the tissue product made from commercial pulps. Improvements were observed in dry tensile, wet tensile, and wet burst strength.
  • tissue machine data shows that through-air drier requires comparable total through-air drying power to dry the tissues containing the carboxylated cellulosic fibers compared to tissues made from commercial pulps at equal inclusion rate, equal NBSK refining energy input, equal wet strength agent addition rate, and equal carboxymethyl cellulose addition rate.
  • the data also shows that the carboxylated cellulosic fiber pulp has a lower unrefined freeness than the control pulp and refines to a lower freeness than the control pulp at equivalent refining energy input or refines to an equal freeness with lower refining energy.
  • tissue handsheets were prepared from carboxylated cellulosic fibers prepared from northern bleached softwood kraft pulp at three carboxyl levels (3, 7, and 12 meq/100 g cellulose). These pulps were refined to three different levels of refinement as measured by pulp filtration resistance (PFR), 7, 10, and 13 sec 2 . Pulp filtration resistance (PFR), like Canadian Standard Freeness (CSF), is a measure of drainage of water from the pulp. In these handsheets, the wet strength agent (KYMENE) was added at three different levels (20, 35, and 50 lb/ton fiber). The tissue products also included carboxymethyl cellulose (CMC) as a strength additive at three different levels, 0, 2, and 4 lb/ton fiber. The results are tabulated in FIGURE 6.
  • CMC carboxymethyl cellulose
  • the results show improvements in the tissue handsheet properties of handsheets that include carboxylated fibers compared to commercial NBSK pulp.
  • Typical commercially available NBSK pulps have a carboxyl level of about 3 to about 4 meq/100 g cellulose.
  • the data shows that handsheets including the carboxylated pulps have higher wet burst strength and wet burst strength/dry tensile strength ratio than handsheets made from commercial pulps.
  • Handsheets were also made including carboxylated pulp fibers and compared to handsheets made using a northern bleached softwood kraft pulp control (Prince Albert NBSK). The effect of refining, as well as the amounts of strengthening agents, was determined.
  • the handsheets including the carboxylated pulps have a higher wet burst strength and wet burst strength/dry tensile strength ratio compared to the control handsheets made from commercial pulps.
  • the handsheets including carboxylated fibers had a dry tensile strength that was slightly higher than control at lower refinement, and slightly lower than the control at higher refinement. The results are shown in FIGURES 7-10.
  • FIGURE 7 is a graph illustrating pulp filtration resistance (PFR) versus pulp PFI mill revolutions (PFI revs) for two representative carboxylated fibers compared to control. Pulp filtration resistance increases with pulp filtration instrument revolutions for all handsheets.
  • FIGURE 8 is a graph illustrating wet burst versus pulp filtration resistance for representative tissue (handsheets) compared to control with an equal wet strength agent addition rate for all samples.
  • Wet burst strength was measured on a Thwing Albert Model 1300-177 Wet Burst Tester manufactured by Thwing Albert Instrument Co., Philadelphia, Pennsylvania.
  • Wet burst increases with increasing pulp filtration resistance.
  • Handsheets including carboxylated fibers showed significantly greater wet burst as a function of pulp filtration resistance compared to the control handsheet.
  • FIGURE 9 is a graph illustrating dry tensile strength versus pulp filtration resistance for representative tissue products of the invention (handsheets) compared to control. Dry tensile increases with increasing pulp filtration resistance for all handsheets. The greatest increase in dry tensile is seen from 5 to about 10 sec 2 .
  • FIGURE 10 is a graph comparing wet burst/dry tensile strength ratio versus pulp filtration rate for representative tissue products of the invention (handsheets) compared to control with an equal wet strength agent addition rate for all samples.
  • the wet burst/dry tensile ratio increased slightly with increasing pulp filtration resistance.
  • the wet burst/dry tensile ratio for the handsheets containing carboxylated fibers was significantly greater than for the control handsheet.
  • FIGURES 11A and 11B The composition and properties of representative tissue products of the invention (handsheets) and handsheets made from commercial pulps (controls) are summarized in FIGURES 11A and 11B.
  • PA-pilot dried refers to a fully bleached, never-dried northern bleached softwood kraft pulp that was dried at the Paper and Pulp Research Institute of Canada (Point-Claire, Quebec); Prince Albert refers to a northern bleached softwood pulp produced commercially at Weyerhaeuser's Prince Albert, Saskatchewan pulp mill; carboxylated refers to a carboxylated cellulosic fiber pulp dried at the Paper and Pulp Research Institute of Canada (Point-Claire, Quebec); CSF refers to Canadian Standard Freeness (an alternative measure of drainage to PFR); BSWT refers to basis weight (gsm); WB/DT refers to the wet burst/dry tensile ratio; and WRV refers to water retention value.
  • the control handsheets included either a NBSK control pulp (Prince Albert) or a second NBSK control pulp (PA-pilot dried) that was dried in the same manner as the carboxylated fiber used in the handsheets of the invention.
  • CSF was either 375, 475, or 575 ml
  • KYMENE was included at either 10, 25, or 40 lb/ton
  • CMC was included at either 0, 4, Or 8 lb/ton.
  • the handsheets including the carboxylated fibers had improved wet burst strength, tensile strength, and wet burst/dry tensile ratio compared to those handsheets made from either commercial NBSK pulps at any given drainage (CSF).
  • FIGURES 12-14 compare the actual and predicted performance of these handsheets based on regression analysis of the handsheets data, and compare wet burst strength, dry tensile strength, and wet burst/dry tensile strength versus wet strength agent amount at various freeness.
  • FIGURES 12A and 12B are graphs comparing the actual and predicted wet burst strength of handsheets made with carboxylated fibers with those of handsheets made with a control pulp at various KYMENE addition rates. NBSK refining varies for each graph, and CMC addition rate is 0 lbs./ton in both examples. The wet burst strength of the handsheets containing carboxylated fibers is higher than the control's at all KYMENE addition rates.
  • wet strength agents e.g., KYMENE
  • the dashed curve is the predicted curve for tissues containing carboxylated pulp
  • the (+) points are actual points for tissues containing carboxylated fiber pulp
  • the solid curve is the predicted curve for control tissues including non-carboxylated fiber pulp
  • the ( ⁇ ) points are actual points for control tissues containing non-carboxylated fibers.
  • Handsheets prepared from the carboxylated fiber pulp have greater wet burst strength than the control pulp in the commercially useful wet strength addition ranges.
  • FIGURES 13A and 13B are graphs comparing actual and predicted dry tensile strength of handsheets made with carboxylated fibers with those of handsheets made with control pulp at various KYMENE addition rates. NBSK refining varies for each graph, and CMC addition rate is 0 lbs./ton in both examples. The dry tensile strength of the two handsheets are comparable up to approximately 25 lbs. KYMENE/ton. Therefore, one familiar with the art will recognize that that the dry strength of the two handsheets are comparable in the normally commercially viable range for KYMENE inclusion.
  • the dashed curve is the predicted curve for tissues containing carboxylated pulp
  • the (+) points are actual points for tissues containing carboxylated fiber pulp
  • the solid curve is the predicted curve for control tissues including non-carboxylated fiber pulp
  • the ( ⁇ ) points are actual points for control tissues containing non-carboxylated fibers.
  • Handsheets prepared from the carboxylated fiber pulp have comparable dry tensile strength to the control pulp in the commercially useful wet strength addition ranges.
  • FIGURES 14A and 14B are graphs comparing actual and predicted wet burst/dry tensile strength ratio of handsheets made with carboxylated fibers with those of handsheets made with control pulp versus KYMENE addition rate.
  • NBSK refining varies for each graph, and CMC addition rate is 0 lbs./ton in both examples.
  • This wet burst strength/dry tensile strength ratio combines the data from FIGURES 12A - 13B. Products of the invention show substantial improvement in this ratio at all KYMENE addition rates.
  • the dashed curve is the predicted curve for tissues containing carboxylated pulp
  • the (+) points are actual points for tissues containing carboxylated fiber pulp
  • the solid curve is the predicted curve for control tissues including non-carboxylated fiber pulp
  • the ( ⁇ ) points are actual points for control tissues containing non-carboxylated fibers.
  • Handsheets prepared from the carboxylated fiber pulp have greater wet burst/dry tensile ratio than the control pulp in the commercially useful wet strength addition ranges.
  • FIGURE 15A illustrates a representative two-layer tissue product (200) having first layer 202 and second layer 204.
  • FIGURE 15B illustrates a representative three-layer tissue product (210) having first layer 212, second layer 214, and third layer 216.
  • the area of several sheets of paper is determined from lineal measurements and the mass is determined by weighing.
  • the ratio of the mass to the area is the basis weight (i.e., g/m 2 ).
  • the values of many physical properties of paper such as burst, tear, tensile, bulk, and caliper are interpreted and specified with regard to the particular basis weight involved.
  • Ten sheets of sample paper are selected and cut to obtain a total sample target area of 5,000 cm 2 . From each sample, randomly select two sheets. Measure each side of the selected sheet. If the lengths of any two opposite edges differ by more than 1 mm, the sample must be recut, as the sides are not sufficiently parallel. Average the measurements of the opposing sides and record to the nearest 0.25 mm. Weigh each specimen on the balance and record the weight.
  • This method is used to determine three breaking properties of paper: the force required to cause tensile failure in a specimen of specified width (breaking load or tensile strength); the elongation of the specimen at failure (the difference between the strained length and the original length expressed as a ratio); and the energy absorbed per unit area by the specimen for failure (tensile energy absorption or TEA).
  • the tests are performed on an Instron 4422 Universal Testing System. The crosshead moves at a uniform predetermined rate of speed. The modulus of elasticity (Young's modulus) can also be determined with this method.
  • basis weight of the sample is required for measuring tensile index and/or breaking length.
  • the tensile properties of paper in paper products generally indicate resistance to potential breaking during printing and other converting operations where a variety of in-plane stresses act upon the sheet.
  • the elongation is indicative of the ability of the paper to conform to a desired contour, and this occurs repeatedly in printing presses and other processes.
  • the tensile energy absorption (TEA) is an indicator of how the paper will stand up to repetitive stresses, and is, therefore, a measure of durability.
  • Tensile properties are dependent upon characteristics of the original pulp (wood species, pulping type and conditions, degree of bleaching) and subsequent treatment during papermaking (degree of refining, type and amount of additives, amount of recycled material).
  • Tensile strength is important in pulp manufacture because its strength properties influence those of the paper from which it is made.
  • All samples should be conditioned and tested at 23+/- 1°C and 50 +/- 2% relative humidity. Cut specimens 25 mm (about 1 inch) wide and about 250 mm long, with the test direction (machine direction or cross machine direction) parallel with the long dimension. Handsheet specimens should be cut 15 mm wide by 125 - 145 mm long. The specimen length must be sufficient for the test span plus clamping regions of about 25 mm for each clamp. Select the load cell appropriate for the materials being tested. For most tests, a 50 kg type load cell having a test range from 1 - 50 kg is used. For testing very strong grades (linerboard and containerboard), use a "CT" type load cell having the capacity to test from 5 - 250 lb (100 kg).
  • a 25 kg load cell having a test range from 0.5 - 25 kg is appropriate.
  • Prepare the Instron instrument by identifying the test method needed, which is instrument frame specific and load cell specific. Alternatively, the method can be created or modified using the technician's guidebook and Instron manuals.
  • Rezero the span by activating GL reset on the control panel. Label the specimen and test direction (i.e., MD or CD). For determination of modulus of the elasticity, measure each test strip for thickness at three positions along the strip length. Record the average strip thickness in mm.
  • Modulus of elasticity can be calculated by drawing a line tangent to the elastic region of the curve and calculating the slope. Ten specimens per sample are tested.
  • T (Nm/g) 9810f/wg
  • g condition to basis weight (g/m 2 ).
  • Tensile energy absorption J/m 2
  • J/g Tensile energy absorption
  • This method is used to determine the single sheet thickness of paper and paperboard by use of a motor driven micrometer using a specified load applied for a specified time.
  • the method is suitable for using the IPC Soft Platen technique for measuring apparent thickness.
  • This technique employs a micrometer with pressure faces covered with soft neoprene rubber. This has the effect of reducing thickness readings due to the ability of the latex to conform to surface irregularities. This is useful when measuring materials with rough or irregular surfaces, such as linerboard and corrugated medium.
  • Thickness is an important property for paper as it influences properties such as structure (bulk), stiffness, opacity, and fold. Variations in thickness are also very useful in order to monitor important machine variables.
  • Samples are conditioned and tested at 23 +/- 1°C and at 50 +/- 2% relative humidity.
  • the samples should be sufficient to obtain a minimal of 20 and up to 50 readings. Clean the surfaces of the platens with lint-free paper and adjust the micrometer reading to zero. Insert a single specimen into the caliper opening, allowing the pressure faces to close and the reading to stabilize. Perform 50 tests per sample (e.g., 5 readings per sheet on each of 10 sheets). After each sample, check that the instrument zero has not drifted. If it has, clean the platens and readjust as necessary.
  • TAPPI T 411 om-97 Thickness (Caliper) of Paper, Paperboard, and Combined Board
  • TAPPI T 551 pm-92 Thickness of Paper and Paperboard (Soft Platen Method)
  • ISO 534 1988(E) Paper and Board, Determination of Thickness and Apparent Bulk Density or Apparent Sheet Density.
  • the Canadian Standard Freeness (CSF) test method is used to evaluate the changes in the drainage characteristics of pulp during refining.
  • the method is used to monitor head box stock as a precursor of how the dilute pulp suspension will behave on the wet end of the paper machine in releasing water.
  • the freeness is highly dependent on degree of refining and therefore is a fairly good indicator of pulp bulk and strength properties.
  • the method is suitable for all types of pulps that can be used by itself or in connection with other test methods (laboratory refining using the PFI, Escher-Wyss, Valley Beater).
  • the method is based on a modification of ISO 5267-2.
  • the volume of water drained from 3 oven-dried (OD) g of pulp at 0.3% consistency in a standard tester is captured and measured.
  • the amount drained depends mainly on the quantity of debris (i.e., fines) present and to a lesser extent on the degree of fibrillation, flexibility, and compressibility of the fibers.
  • Pulps with a dry matter content equal to or greater than 20% are soaked in deionized water for at least four hours and for no longer than 48 hours.
  • the pulp is then disintegrated as described in method WM I-5263 Disintegration of Pulp.
  • the CSF of refined pulps can change with time.
  • the oven-dry consistency of the sample being tested should be 0.3% +/- 0.02%.
  • testing device which includes a chamber and a funnel having a traditional bottom orifice and a second side orifice, place a graduated cylinder under the side orifice of the funnel to collect discharge. Place a 1000 mL beaker under the bottom orifice to collect all discharge. Thoroughly mix the diluted sample and withdraw the equivalent of 3.00 OD g in a 1000-mL graduated cylinder. This amount is calculated from a consistency measurement of the sample:
  • Amount of sample withdrawn (g) 3.00 g (100)/% consistency. Adjust the sample to 0.30% consistency by diluting the graduated cylinder contents to the 1000 mL mark. Pour the contents into the upper chamber of freeness tester. Close and clamp the top lid of the chamber and close the air-cock on the top lid of the chamber. Open the bottom lid and open the air-cock on the top. When the discharge has completely stopped from the side orifice, collect the volume in the appropriate graduated cylinder. Read the volume of this discharge to the nearest 1 mL for values below 100 mL, to the nearest 2 mL for values between 100 mL and 250 mL, and to the nearest 500 mL for values exceeding 250 mL. Freeness (CSF) is reported to the nearest whole mL.
  • Water retention value can be a useful tool in evaluating the performance of pulps relative to dewatering behavior on the paper machine.
  • the usefulness of the method on a particular application may vary depending upon the type of stock, additives, machine configuration, and other factors.
  • the method provides standard values of centrifugal force, time of centrifuging, and simple preparation so that results can be compared at standard values.
  • WRV as measured by this method, is the amount of water retained by a pulp sample after being subjected to a centrifugal force equal to 900 times the force of gravity for 30 minutes (2 minutes to reach maximum speed).
  • the basis weight of the pulp is 1400 g/m 2 (OD).
  • the method is a modification of TAPPI UM-256. To perform the tests, a laboratory centrifuge with free-swinging head (IEC model HN-SII or equivalent) with digital rpm meter is required.
  • Pulp filtration resistance is a measure of a pulp's resistance to drainage. PFR is an important tool for judging a pulp's ability to dewater at various levels of refining. This has a direct impact on paper machine predrier temperatures and machine speed.
  • the test consists of three timed filtrations of 100 mL of the slurry through a screen in the PFR nozzle. This screen is made of the same monofilament material used as handsheet wires. The method for carrying out the PFR measurement is described in U.S. Patent No. 5,228,954.
  • the PFR is, like the Canadian Standard Freeness (CSF), a method for measuring the drainage rate of pulp slurries. It is believed that the PFR is a superior method for characterizing fibers with respect to their drainage characteristics.
  • a more accurate method of measuring the PFR is as follows.
  • the PFR is measured by discharging three successive aliquots of a 0.1% consistency slurry from a proportioner and filtering through a screen connected to the proportioner discharge. The time required to collect each aliquot is recorded and the screen is not removed or cleaned between filtrations.
  • the proportioner (obtained from Special Machinery Corporation, 546 Este Avenue, Cincinnati, OH 45232, Drawing #C-PP-318) is equipped with a PFR attachment (also obtained from Special Machinery Corporation, Drawing #4A-PP-103, part #8).
  • the PFR attachment is loaded with a clean screen (a 1-1/8" die cut circle of the same type of screen used for handsheeting, Appleton Wire 84 ⁇ 76M, is used and it is loaded with the sheet side "up" in the tester).
  • a 0.10% consistency slurry of disintegrated pulp is prepared in the proportioner at a volume of 19 liters, with the PFR attachment in position.
  • a 100 ml volumetric flask is positioned under the outlet of the PFR attachment.
  • the proportioner outlet valve is opened and a timer started, the valve is closed and timer stopped the instant 100 ml is collected in the volumetric flask (additional liquid will probably drain into the flask after the valve is closed). The time is recorded to the nearest 0.10 seconds, noted as "A".
  • PFR ( E ) ⁇ ( B + C - (2 ⁇ A )) 1.5
  • A, B, and C are the recorded time intervals
  • Handsheet Preparation About 30-31 g of pulp was refined in a PFI Refiner to 570 ⁇ 5 mL Canadian Standard Freeness. Nineteen grams (dry basis) of the refined pulp in a total of 2000 mL of water was placed in a British disintegrator, 2.28 g of 12.5% KYMENE 557H solution was added, and the slurry was disintegrated for 10 minutes. The resulting disintegrated pulp slurry was diluted to 19 L to form a 0.1% consistency slurry. The drainage rate of this slurry was measured by the amount of time taken to pass 300 mL of filtrate water, using a liquid slurry head height of 36 inches, through a 1.0 inch diameter circular handsheet forming wire containing 84 ⁇ 76 wires per inch. The forming wire was obtained from Albany International, 435 Sixth St., Menasha, Wis., 54952.
  • Wet Burst Test Method A 12 inch ⁇ 12 inch deckle box was used to form handsheets of approximately 26 g/m 2 basis weight and approximately 240 kg/r 3 density on the forming wire described above. Five sheets were formed for each pulp. The sheets were not wet pressed. Dewatering of the handsheets was accomplished by passing the sheets still on the forming wire over a vacuum slit. The sheets were dried on a steam-heated drum dryer and cured in an oven for one hour at 105°C. Wet burst strength of the sheets was measured on a Thwing Albert Model 1300-177 Wet Burst Tester manufactured by Thwing Albert Instrument Co., Philadelphia, Pa., 19154. Eight measurements were made for each pulp and the average calculated and taken as the wet burst strength.

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  • Paper (AREA)
  • Materials For Medical Uses (AREA)
  • Sanitary Thin Papers (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Laminated Bodies (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)
EP04254647A 2003-08-05 2004-08-02 Procédé de préparation de produits papier tissu contanant des fibres cellulosiques carboxylées Withdrawn EP1505208A3 (fr)

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US10/635,098 US20050028956A1 (en) 2003-08-05 2003-08-05 Method for making tissue product containing carboxylated cellulosic fibers
US635098 2003-08-05

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WO2011138366A1 (fr) * 2010-05-05 2011-11-10 Basf Se Composition fibreuse pour la fabrication de papier et de carton
US8454799B2 (en) 2010-05-05 2013-06-04 Basf Se Pulp composition for paper and solid board production
EP3636830A1 (fr) * 2009-05-28 2020-04-15 GP Cellulose GmbH Cellulose modifiée à base de fibres kraft chimiques et procédés de fabrication et d'utilisation de celle-ci

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DE602007006042D1 (de) * 2006-11-23 2010-06-02 Tno Biopolymere als nassfestmittel
WO2010044752A1 (fr) 2008-10-13 2010-04-22 Agency For Science, Technology And Research Polymères amphiphiles et nanocristaux revêtus avec ceux-ci
US9512563B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Surface treated modified cellulose from chemical kraft fiber and methods of making and using same
US9511167B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Modified cellulose from chemical kraft fiber and methods of making and using the same
US9512237B2 (en) 2009-05-28 2016-12-06 Gp Cellulose Gmbh Method for inhibiting the growth of microbes with a modified cellulose fiber
WO2011088889A1 (fr) * 2010-01-19 2011-07-28 Södra Skogsägarna Ekonomisk Förening Procédé de fabrication d'une pâte cellulosique oxydée
JP5901129B2 (ja) * 2011-03-28 2016-04-06 ユニ・チャーム株式会社 不織布の製造方法
BR112015019882A2 (pt) 2013-03-14 2017-07-18 Gp Cellulose Gmbh fibra kraft clareada oxidada e métodos para fazer polpa kraft e fibra kraft de madeira macia e para clarear polpa kraft de celulose em sequência de branqueamento de multi-estágios
BR112015020000A2 (pt) 2013-03-15 2017-07-18 Gp Cellulose Gmbh fibra kraft quimicamente modificada e métodos de fabricação da mesma
CN104099803A (zh) * 2013-04-15 2014-10-15 金东纸业（江苏）股份有限公司 造纸工艺
JP6582482B2 (ja) * 2015-03-25 2019-10-02 王子ホールディングス株式会社 衛生用紙およびその製造方法
JP6529124B2 (ja) * 2015-08-28 2019-06-12 日本製紙株式会社 重包装用クラフト紙の破袋評価方法および重包装用クラフト紙
EP3541849B1 (fr) 2016-11-16 2023-11-15 GP Cellulose GmbH Cellulose modifiée à base de fibre chimique et methodes de fabrication et d'utilisation
CN107663805B (zh) * 2017-10-11 2020-10-30 山东恒安纸业有限公司 一种无菌擦手纸及其生产工艺
US11035078B2 (en) 2018-03-07 2021-06-15 Gpcp Ip Holdings Llc Low lint multi-ply paper products having a first stratified base sheet and a second stratified base sheet

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WO2001029309A1 (fr) * 1999-10-15 2001-04-26 Weyerhaeuser Company Procede de fabrication de fibres de cellulose carboxylees et produits fabriques selon ledit procede
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EP3636830A1 (fr) * 2009-05-28 2020-04-15 GP Cellulose GmbH Cellulose modifiée à base de fibres kraft chimiques et procédés de fabrication et d'utilisation de celle-ci
WO2011138366A1 (fr) * 2010-05-05 2011-11-10 Basf Se Composition fibreuse pour la fabrication de papier et de carton
US8454799B2 (en) 2010-05-05 2013-06-04 Basf Se Pulp composition for paper and solid board production

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MXPA04007598A (es) 2005-03-31
EP1505208A3 (fr) 2006-02-01
US20050028956A1 (en) 2005-02-10

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