Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS3017317 A
Publication typeGrant
Publication date16 Jan 1962
Filing date12 Feb 1957
Priority date12 Feb 1957
Publication numberUS 3017317 A, US 3017317A, US-A-3017317, US3017317 A, US3017317A
InventorsDonnelly Harold F, Lamb Charles A, Voigtman Edward H
Original AssigneeKimberly Clark Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Method of creping tissue and product thereof
US 3017317 A
Abstract  available in
Images(2)
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

Jan. 16, 1962 E. H. volGTMAN ETAL Filed Feb. 12, 1957 METHOD OF CREPING TISSUE AND PRODUCT THEREOF' 2 Sheets-Shee'. l

ENTORS. ,img/y 'INV M, m, M1 M20 Jan. 16, -1962 E. H. volGTMAN ETAL 3,017,317

METHOD OF' CREPING TISSUE AND PRODUCT THEREOF' Filed Feb. 12, 1957 2 Sheets-Sheet 2 N INVENTORS. I muazg@ 2556 M, mam/va te States atent @hice 3,017,317 METHOD F CREPING TISSUE AND PRODUCT THEREUF Edward H. Voigtrnan, Neenah, Harold F. Donnelly, Ap-

pleton, and Charles A. Larnh, Neenah, Wis., assignors to Kimberly-Clark Corporation, Neenah, Wis., a corporation of Delaware Filed Feb. 12, 1957, Ser. No. 639,792 2 Claims. (Cl. 162-411) This invention in general relates to an improved tissue structure and la method of making the same. Th1s 1n- 'vention more particularly relates to improved multi-ply creped cellulosic tissue products and the manufacture thereof.

' Multi-ply creped tissue products utilized for certain applications such as for packaging, padding, cushioning, insulating, wiping, etc. require low density and high bulk. Where prior multi-ply creped tissue products, such as are used for insulating and cushioning, were manufactured so as to exhibit especially low density and high bulk, it was found they could be easily and permanently cornpressed or crushed to a condition of higher density and lower bulk. Accordingly, the originally high insulating and cushioning properties of these tissue products were materially reduced when subjected to stress.

Difliculties have also been encountered in providing multi-ply tissue products for wiping purposes which not only are of low density and high bulk and are relatively self-supporting and stable during use, but which also have a greatly decreased tendency to lint or cast off free fibers, and have a sufliciently coarse surface or bit to easily remove from the surface to be cleaned dirt, grime and other discrete substances.

It has now been found that improved multi-ply cellulosic -tissue products can be fabricated by differentially creping cellulosic tissue sheets in a suitable manner and then combining them to provide in the products improved structural stability, together with high bulk and low density. These high bulk and low density characteristics are retained even when such products are subjected to considerable compressive force. Accordingly, the irnproved multi-ply products are highly satisfactory for use as packing and padding materials.

The multi-ply cellulosic tissue products of the present invention present relatively coarse, uneven surfaces, so that they are also adaptable as wiping agents. Furthermore, the iibers of these products are more strongly bonded to each other in selected areas and have less tendency to lint, which adds to their utility as wiping agents.

The improved cellulosic tissue products of the present invention which comprise a plurality of plies of diiferentially creped cellulosic tissue are fabricated in a wholly unique manner in accordance with the method of the present invention.

Accordingly, it is an object of -this invention to provide improved, stable, creped, cellulosic tissue products and a method of making the same. More specifically, it is also an object of this invention to provide novel creped tissue products which, as a result of a differential creping process, are relatively lint-free and have improved coarse surfaces with improved bite characteristics, and a method of making the same. It is a further object of this invention to provide means and procedures for obtaining stable, differentially creped, multi-ply, cellulosic tissue products having improved low density and high bulk characteristics.

Further objects of this invetnion will be apparent from the following detailed description and the accompanying drawings of which:

FIGURE l is an isometric view and partial cross section of a multi-ply tissue product of the present invention;

FIGURE 2 is Ia schematic representation of apparatus on which the differential creping of the present invention may be carried out; and,

FIGURE 3 is a somewhat schematic representation of a micro-jet spray boom in relation to the drier surface.

Referring now more particularly to the accompanying drawings, FIGURE 1 shows a multi-ply, differentially creped tissue product, produced in accordance lwith the present invention. The illustrated product comprises a plurality of superposed, cellulosic tissue webs or sheets 5. VFor the' purposes of the present invention, the number of plies utilized in the product may be two or more, depending upon the particular application for which the product is to be used. The individual sheets in the productv are formed tissue webs having a basis weight, on a bone dry basis, before differential creping of between about 3.5 pounds and about 15 pounds per ream of 3,000 square feet. The preferred basis weight range for these sheets depends upon the particular end use for which the products are intended. For example, if the sheets are to be utilized for cushioning or insulating purposes, the preferred basis weight range is between about 4.5 pounds and about 7.5 pounds per ream of 3,000 square feet, on a bone dry basis, before dierential creping. For wiping purposes, this preferred range is 9 pounds to l5 pounds per ream.

Each of the cellulosic tissue webs or sheets 5 has a Aseries of alternating coarsely creped areas 7 and more nely creped areas 9. The alternating coarsely creped areas 7 and more finely creped areas 9 provide alternating regular puied and fiat areas across the width of the sheet which give the product its unique properties. Thus, the coarsely creped areas 7 and more nely creped areas 9, as illustrated in FIGURE l of the accompanying drawings are arranged in a regular pattern, preferably across the entire width of each sheet. The fine crepes in the flat areas function as stabilizers holding the arches of the coarse crepe in place and enabling the latter to act as structural members to provide the product with its stable bulk characteristics. Although in FIGURE l these areas are shown as being a series of rather broad parallel bands, they may be in any suitable pattern such as diagonale,

concentric circles, dots, squares, discontinuous areas, crosshatched areas and the like. It isimportant, however, that the coarsely creped and more nely creped areas altern-ate or are interspersed so as to provide ,structural stability to each of the coarsely creped areas of the web. When alternated properly, the lfinely creped areas act in the manner of a structural truss tohold the vcoarsely creped areas in position.

It is well known in the art that up to a certain degree, coarser creping can be achieved by using thicker creping blades. However, this does not provide a product having the stabilized increased bulk of the present invention since the coarser crepe so produced has an incipient tendency to collapse or flatten out, and therefore has very little ability to support loads under stress. In the present invention, the coarsely creped areas provide vertical components of large comparative magnitude, while the ner creping imparts a structural rigidity to the coarse crepe to provide a relatively stable product of increased bulk and low density.

The coarsely creped areas 7 of the plies of the tissue product should have between about 5 and about 3() crepes per inch as the product is wound onto the reel at the end of the paper machine, and preferably between about l0 vand 20 crepes per inch. The more nely creped areas 9 of the respective plies should have between about 20 and about 200 crepes per inch, and preferablybetween about 30 and about 50 crepes per inch. Some stretching usually takes place as the sheets are plied up into the product of this invention, to extent of about percent of their length.

The webs or sheets comprising the plies of the product have a crepe ratio between about 1.25 and 2.5. A crepe ratio of about 2.0 is preferred. By crepe ratio is meant the ratio of the length of the fiat sheet before creping to the length of the sheet after creping.

The coarsely creped areas 7 of the plies of the product should comprise between about percent and about 85 percent of the total area of each of the plies, preferably between about 40 percent and about 60 percent. The finely creped areas 9 of the plies comprise the remainder of the creped area of the plies. The respective plies of the product may be assembled in uniform or-in random distribution with respect to lthe alignment of coarsely creped and finely creped areasof the plies. After the tissue sheets are assembled, the multi-ply product of the present invention has a density between about 1.3 pounds and about 2.0 pounds per cubic foot. The product has a bulk up to about 100 percent greater than comparable conventionally creped tissue products.

The manufacture of improved multi-ply creped cellulosic tissue products in accordance with the present invention involves the steps of forming sheets or webs of tissue in a conventional manner and then differentially creping each of the tissue webs or sheets so as to provide alternating or discontinuous desired areas of coarse crepe and of more fine crepe. A plurality of the individual sheets or webs of the differentially creped tissue are then assembled into a unitary structure which is the improved multi-ply tissue product of the present invention, as illustrated in FIGURE l.

In accordance with the method of the present invention, a sheet or web of fibrous tissue is formed by a water-laying technique on the usual Fourdrinier-type webforming equipment. The mat of fibers of which the web is composed is formed by applying to the upper surface ofthe Fourdrinier wire, as by flowing thereon, a layer of stock containing the required amountof fibers in an amount of water which is sufficient to produce the proper distribution of the fibers in the web, and subsequently eliminating sufficient of the water to produce a coherent web or sheet capable of being couched off the end of the wire.

For the purposes of the present invention, the sheet may be made of various cellulosic and other fibers which are normally used in the fabrication of tissue webs or sheets. The proportions and types of such fibers may be adjusted in accordance with the uses to which the tissue product is to be applied. The useful cellulosic fibers include chemical wood pulp fibers, mechanically produced wood pulp fibers, cotton fibers, etc. Suitable chemical wood pulp fibers include those produced by the sulfite, sulfate and semi-chemical pulping processes. The fibers may be bleached, but this is purely a matter of choice depending upon the type of end product desired. Various synthetic fibers such as rayon, nylon, glass, polyvinyl chloride and cellulose acetate fibers may be added in varying amounts to the furnish to provide webs having certain specific properties. The furnish is mixed with a suitable amount of water to make up a stock or suspension.

The tissue web may be formed on a Fourdrinier webforming machine having an open or spout type head box or on a cylinder vat machine. The drier section of a Fourdrinier machine is illustrated generally in the schematic view, FIGURE 2.

As produced on such a machine the formed cellulosic tissue web normally has a moisture content of approximately 85 percent by weight as it leaves the wire before drying. Mosture content of the web is further reduced to between 70 and 80 percent by the main press and to about 65 percent as the web is applied to the drier by the press roll. The drying of the tissue web comprises reducing the moisture content thereof by heat to between about 3 percentand about 14 percent by weight of the tissue, on a bone dry basis. The drying operation is carried out in the conventional manner on a single, large diameter, heated `drier roll of the Yankee type. The Yankee drier comprises a heated cylinder which may be as large as 15 feet or more in diameter and of equal or greater length. It may be fabricated from a single castingof cast iron which is ground to a smooth surface. Alternatively, the Yankee -drier may be constructed as set forth in U.S. Patent No. 2,725,640 of December 6, 1955, to Veigtman, or may be of any other suitable design or material.

Referring now more particularly to FIGURE 2 of the accompanying drawings, the wet tissue web 11, after being couched in the usual manner from the forming wire 10 at a moisture content of about 85 percent, is carried by a top felt 13 through the main press which includes a top press roll 15, a bottom suction press roll 17 and a bottom felt 18. r[he press rolls partially dewater the wet web to a moisture content of about 70 percent to about 75 percent by weight, on a bone dry basis. The web 11 is then carried by the top felt 13 around the usual tail roll 19, and into the pressure nip between the Yankee drier cylinder 21 and a rubber covered suction press roll 2.3. Press roll 23 acts to press web 11 rmly onto the surface of cylinder 21. At this point the moisture content of the web is about 65 percent by weight.

As indicated in FIGURE 2, cylinder 21 rotates in a clockwise direction, carrying web 11 with it during rotation. The creped web is Ywound up into a soft roll or reel 25 which rotates at a controlled peripheral speed. The drier operates at an even surface temperature between about l F. and about 212 F. and normally rotates at, surface speeds in excess of 1,000 feet per minute. At this temperature and speed of rotation the web is reduced to a moisture content of between about 3 and 14 percent by weight before it is creped. Beyond the pressure nip, top felt 13 leaves web 11, and passes around roll 27 and associated rolls to return for reuse in the processing of the tissue web.

Referring again to FIGURE 2, as cylinder 21 rotates, means 29 continuously applies a release agent in a predetermined pattern to the adjacent surface of cylinder 21.

The release agent for the purposes of the present invention may be one or more compounds which are miscible with water or another volatile carrier. By miscible is meant dispersible in or soluble in the volatile carrier. Air also can be used as the carrier, applying the release agent in the form of a mist. 'Ihe release agent must impart a degree of oiliness to steel of less than 0.3 at 20 C., expressed as the coefiicient of friction, determined as described later in this specification.

In FIGURE 3, means 29 is shown as a boom 31 having spaced micro-jets 33 directed at the adjacent drier surface 35 and extending substantially over the entire width of the drier 21. The release agent is applied to the drier surface in a predetermined pattern for differential creping, as hereinafter more specifically set forth. Generally, enough release agent must be applied to form a film on predetermined areas only of the drier surface. This film should be substantially completely absorbed by the web on the drier, so that there is substantially no residual release agent left on the drier surface beyond the creping doctor blade. The optimum amount of release agent suitable for the purposes of the present invention is just short of that which would leave a residual amount on the drier. However, a small residual is not detrimental to the process provided it does not canse excessive buildup on the surface of the dried. These release agents have been used with varying degrees of effectiveness in amounts ranging from 0.5 pound to 50 pounds per ton of product. (The preferred operating range is from 1 to l0 pounds per ton.)

Any other apparatus which applies the release agent to the drier surface in a controlled pattern may be utilized in this invention. In this connection, a patterned rubber printing roll may be used. If such a printing roll is keyed to the drier so that it prints the pattern in exact register at each revolution, the exact control of the amount of release agent used is not as critical because a residual carryover does not alter the pattern. ln addition, an arrangement of wicks or other equipment to wipe the release agent on certain areas of the drier surface may be used.

The release agent should be applied in a pattern to the exposed Yankee drier surface between the conventional creping doctor blade 37, attached to the drier, and the nip between drier cylinder 21 and press roll 23, as shown in FIGURE 2. Moreover, the point of application of the release agent should be so chosen as to allow a sutlicient period of time to elapse before the release agent on the drier surface enters the previously-mentioned nip. This is to allow the volatile components of the release agent on the drier surface to evaporate and leave behind the greasy or oily residue in a non-migrating pattern on the drier surface, which pattern will not substantially spread in the np between the press roll and drier. Accordingly, it is preferred to apply the release agent relatively near the creping doctor blade. The optimal point of application of the release agent necessarily depends on the amount and concentration of release agent applied to the drier surface, 'the surface temperature of the drier and the nature of thevolatile constituents of the release agent.

In the event a series of heated drier rolls are utilized in place of the Yankee drier, the release agent is applied in the previously described manner to the exposed surface of the drier roll on which the creping is performed and prior to the pressure nip between the drier roll and associated press roll.

It is also within the scope of the present invention to apply the release agent in a pattern to the exposed surface of the web, as by a patterned rubber printing roll, while the web is on the Yankee or other drier roll, so as to allow the pattern of release agent to penetrate the web to the drier surface and thereby effect the desired differential release of the web. In this connection, the point of application of the pattern of release agent to the web on the drier should be chosen so as to allow suliicient penetration of the release agent and evaporation of its volatile constituents, thereby assuring substantial differential release of the web.

As web 11 is carried on cylinder 21, as shown in FIGURE 2, it is dried to a moisture content of between about 3 and about 14 percent by weight by the time it reaches the creping doctor blade 37. This blade dry crepes the web from the drier.

It should be noted that the web is dry creped, as distinguished from wet creped or semi-creped, that is, the web is dried shortly after forming, and is creped directly oif the drier at a moisture content usually less than 14 percent. In wet creping, the sheet is dried, then rewetted and reapplied to a drier and creped therefrom. In semi-creeping, the doctor blade is used on a drier usually located about half way along in the drier section and produces only a limited amount of crepe (in the vicinity of to l5 percent). The natural adherence of the tissue web to the surface of the drying cylinder is reduced in those places where the release agent is present. Consequently, as the web is creped from the drier surface by the scraping action of the creping doctor blade, it assumes a differential crepe pattern caused by this differential degree of adherence to the drier surface.

It is important to recognize that the present invention is directed primarily to the dry creping process. The products produced by dry creping differ materially from those produced by Wet creping and semi-creping, both in their appearance and in their functional char- .acteristics Acoefficient of friction for steel on steel is 0.6.

The release agent is applied to the dried surface t0 control the physical characteristics of the creping. The more easily the dried web is released from the drier surface, the coarser the type of creping effected by the creping doctor blade. Accordingly, when the release agent is applied to the surface of the drier in a pattern, there Will bea corresponding pattern of coarse crepe in the creped web. In the surface-areas of the drier left untreated with release agent, the corresponding areas of the web will be released in the normal manner. Consequently, these areas Will be more finely creped.

The differentially dry creped tissue product will show, as previously described, a pattern of coarsely and more finely creped areas,V which differentially creped areas have been found to be responsible for the unique combination of improved structural stability, with low density and high bulk characteristics of the product.

As previously described, at least about l5 percent and not more than about percent of the total area of the finished web should be coarsely creped, with the remainder of the area more finely creped. If more than about 85 percent of the total area of the Web is coarsely creped, the structural stability of the web is impaired. ln addition, the web will flatten out under compressive force and the initially increased bulk Will be lost. If less than about 15 percent of the ltotal surface of the web is coarsely creped, the tissue product does not have the low-density and high bulk to the degree desired by the present invention. As previously indicated, the preferred range for the coarsely creped areas is between about 40 percent and about 60 percent.

As previously described, the release agent of the present invention may be one or more compatible compounds miscible with water or other Volatile solvents and having an oiliness value or coeicient of friction of less than 0.3 at 207 C.

As used in this specification, the degree of oiliness expressed as the coefficient of friction is based on data obtained with the modified Deeley machine as used for static friction measurements in the commercial testing of lubricants. This machine consists of two opposing hard steel surfaces, one, a disc about 4 inches in diameter, and the other, three l/2 inch diameter balls equally spaced around a circle 3 inches in diameter on the underside of a circular carriage. The carriage engages with a torque measuring device consisting of a coiled spring with an indicating mechanism. The pressure between the surfaces can be varied by loading the carriage with weights. The disc or lower friction surface is carried in a bath which contains the lubricant under test, and a gas ring is provided under the bath for heating the lubricant, the temperature being measured by a thermocouple in the bath.

The machine is operated by slowly rotating the disc by means of an electric motor and gearing. The frictional resistance between the surfaces causes rotation of the carriage against the action of the spring, and the disc is rotated until slipping of the surfaces occurs, when a pawl-and-ratchet mechanism prevents the spring from unwinding. The torque produced by the spring on the carriage at slip is thus equal to the friction torque and, as the total load is known, the coefficient of friction is easily obtained. This value is a measure of the boundary lubrication afforded by the substance tested.

The Deeley machine, the scale of oiliness values and the associated test are described in detail in the Journal of the Institute of Petroleum, vol. 26, No. 195, January 1940, pages 1 to 18, A. Fogg and S. A. Hunwicks, The Static Friction of Lubricated Surfaces. Wherever reference is made to degree of oiliness or coeicient of friction in the specification and claims, it falls under the above description.

It has been found that at 20 C. the oiliness value o With 7 benzene present, the value is 0.5, with alcohol 0.42, with trichlorethylene 0.33, and with glycerol 0.2. Mineral oils and fatty oils have values in the range from about 0.1.2 to 0.15, while oleic acid has an exceptionally low value of about 0.06.

Examples of release agents which are suitable for the purposes of the present invention are the following:

Soaps comprising the sodium salts of oleic, stearic, and other fatty acids; emulsified mineral oil; wax emulsions; silicone emulsions; diglycol laurate; polyethylene glycol di-laurate; emulsified fatty acids of 6 to 18 carbon atom chain length, such as oleic, ricinoleic, palmitic, stearic and lauric acids; triethylene glycol; sulfonated castor oil; rewetting agents of the fatty ester type, and alkyl aryl polyether alcohols; alkyl ketene dimers. such as the ketene dimer of a fatty acid of 12 to 18 carbon atom chain length; softening agents of the sulfonated long chain hydrocarbon type; and, quaternary ammonium chlorides, such as dihydrogenated tallow di-methyl arnmonium chloride.

The amount of release agent necessary to effect the differential releasing will depend on the oiliness of the release agent, the type of tissue web being released, the temperature of the drier cylinder surface and other factors. As previouslv indicated, the release agent should be utilized in a sufficient amount to effect the desired differential creping but preferably should not be more than that which can be absorbed by the web on the drier. That is, retention of excess release agent on the drier after differentially crening;I off the web is undesirable. The amount of an agent may vary as much as 0.5 to 50 pounds per ton of tissue web, depending on the type of furnish and basis weight of the web utilized, the type and amount of differential creping desired, and the type of release agent used.

The selection of the particular release agent may depend not only on its oiliness Value but also on other characteristics of or imparted by particular release agents: water repellencv, absorbency, softness, color, toxicity, odor, bactericidal and antimycotic properties, and the like.

Since only a relatively minute amount of the release agent need be utilized in practicing the present invention, the cost of achieving the differential creping effect is generally slight. Moreover, the great increase in bulk (up to 100 percent) over webs creped in the conventional manner results in a considerable lowering of the total c^st of products assembled from differentially creped webs over comparable products made from conventionally creped webs.

In accordance with the method of the present invention, a plurality of the differentially dry creped expanded cellulosic tissue webs or sheets. fabricated as previously described, are then assembled in superposed relation to provide the desired multi-plv, cellulosic tissue product. For many purposes, the individual plies of the product adhere sufficiently together so that no other uniting means are required. However, when the product is to be subjecfed to considerable handling, it may be desirable to unite the plies to a greater extent by embossing or other suitable means.

The following examples set forth certain features of the present invention:

Example I An unbleached cellulosic furnish, comprising primarily reclaimed fibers obtained from kraft cuttings and corrugates, was processed in a conventional manner on a commercial tissue making machine to produce a cellulosic tissue web having a basis weight of 5.34 pounds per ream of 3.000 square feet, on a bone dry basis, before creping. While the web was being dn'ed to about 5 percent by weight moisture content in less than one second on a l2-foot diameter Yankee drier operating at about 190 F. surface temperature and a surface speed of approximately 1,600 feet per minute, a 0.167 percent, by Weight, oil-in- Water emulsion of a release agent, in this case the ketene dimer o-f a fatty acid of 18 carbon atom chain length, was jetted onto the surface of the Yankee drier cylinder at 40 pounds per square inch pressure through a microjet spray boom. The microjet spray boo-m had nozzles of 0.008 inch diameter spaced at 3% inch intervals across the entire width of the 12 feet diameter cylinder. The keene dimer was utilized in an amount of about 1.23 pounds per ton of tissue product. The boom was located about .5 inch from the exposed surface of the drying cylinder, between the creping doctor blade and the associated press roll, about 24 inches from the pressure rcll nip. The boom was so positioned as to allow time for the water to evaporate from the release agent before the sprayed-on material reached the press roll, thereby preventing the release agent from spreading in the pressure nip between the press roll and drier surface. The web was creped olf the drier with a standard creping doctor blade at a crepe ratio of 2.00. The differentially creped web had roughly parallel lines of coarse crepe and fine crepe, each line of creping being about 3/8 inch wide. The coarsely creped areas and the finely creped areas each accounted for about 50 percent .of the total area of the web. The finely creped areas had about 32 crepes per inch. The coarsely creped areas had about 15 crepes per inch.

A plurality of plies of the differentially dry creped web were assembled in random superposed relation into a v finished tissue product. This product and a control product, dry creped to the same crepe ratio without the use of a pattern of release agent on the drier, were measured for height after 10 days aging. lt was found that the differentially creped product had an average of 43.5 percent greater bulk than the conventionally creped control product. The density of the product of the present invention was 1.95 pounds per cubic foot as compared with 2.9'pounds per cubic foot for the control. The product was suitable for a variety of uses, including a packing material, padding and wiping cloth.

lt is normal practice in the industry to permit creped wadding products to age before taking bulk and density measurements, in order to allow it to establish a moisture equilibrium with its environment and avoid unnecessary variability caused by shrinkage.

Bulk measurements were made using the conditions set forth in paragraph 4.5 of Federal Specification PPP-C- 843, Cushioning Material, Cellulosic. Density was computed as outlined in paragraph 4.8 of the same Federal specification.

Example II A furnish comprised essentially of bleached sulfate fiber was processed in the manner described in Example l to obtain a tissue web. The formed cellulosic tissue web had a drier basis weight before creping of 4.60 pounds per ream of 3,000 square feet. A 0.167 percent, by weight, oil-in-water emulsion of the ketene dimer of a fatty acid of 18 carbon atom chain length was microjetted at 60 pounds pressure, onto the surface of the Yankee drier of Example I operating at approximately 1,600 feet per minute surface speed, and, utilizing the same equipment and the same point of application as set forth in Example I. The ketene dimer was utilized in an amount of about 1.37 pounds per ton of tissue product. The web was dry creped off the drier with a standard creping doctor bade at a crepe ratio of 1.94. The differentially creped web had roughly parallel, inch wide strips of coarse creping and fine creping, each type of creping covering about 50 percent of the total area of the web. The finely creped strips had an average of 40 crepes per inch, and the coarsely creped strips 15 crepesper inch.

A control sample was fabricated without the use of a pattern of release agent on the drier. A plurality of plies of the differentially dry creped web were assembled in random superposed relation into a finished tissue product, as were the same number of plies of theV conven- `other uses.

,was the point'of application of the release agent.

diglycol laurate was `utilized inan amount of about 6.3

tionaly dry creped control tissue web. After 10 days 'aging of each of the products, it was found that the difuct of the present invention was suitable for use as a wiping agent, padding means and packing material, among Example III A furnish comprised essentially of bleached sulfate fiber was processed into a cellulosic tissue web inthe same manner as setfforth in Example I. The web hada drier basis weight before creping of 4.80 pounds per ream of 3,000 square feet. A water solution containing 0.33 percent by weight of diglycol laurate was then microjetted at .120 pounds pressure onto the surface of the Yankee drier of Example I operating at a surface speed of approximatelyl,600 feet per minute. The microjetting equipment was the same as was utilized in Example I, as The pounds per ton of tissue product. The web was differentially dry creped o the drier at a crepe ratio of A1.94. The resulting differentially dry creped web had an appearance comparrb`e to the webs of Examples l and II, that is, approximately 50 percent of the web was coarsely creped and approximately 50 percent was finely creped. The finely creped areas had about 37 crepes per inch and the coarsely creped areas about 14 crepes per inch. A control dry creped tissue web was fabricated without using a pattern of diglycol laurate or other release agent on the drier. The webs were plied-up to form the dfferentially dry creped tissue product of the present invention and the conventionally dry creped control tissue product. After l days of aging. the two products were compared and it was found that the tissue product of the present invention had an average of 48.6 percent greater bulk than the control tissue product. The density of the product of the present invention was 2.0 pounds per cubic foot, w'ei'e that of the conventional product was 3.3 pounds per cubic foot. The product of the present invention was narticularlv suitable for use as a p^cking material, as well as a wiping agent and padding means.

Example IV An unbleached cellulosic furnish comprising primarilv reclaimed bers obtained from kraft cuttings and corrugates was processed in the manner described in Example l to obtain a tissue web. The formed cellulosic tissue web had a drier basis weight before creping of 5.34 pounds per ream of 3.000 square feet. A .167 percent bv weight oil-in-water emulsion of fatty acid of 18 carbon atom chain 'ength was microjetted at 20 pounds pressure onto the surface of the Yankee drier of Example I operating at approximately 1,800 feet per minute surface speed. and utilizing the same equipment and the same point of application as set forth in Example I. lThe fatty acid was used in the amount of about 1 pound per ton of product. The web was dry creped oi t"e drier with a standard crepinty doctor blade at a crepe ratio of 2.00. The differentiallv creped web had roughly parallel. 3A; inch wide strips of coarse creping and fine creping. each type of ceping covering about 50 percent of the total area of the web. The finely creped strips had an average of 40 crepes per inch and the coarsely creped strips about 15 crepes per inch.

A dry creped control sample was made without using a pattern of fatty acid or other release agent on the drier. The webs were plied up to form the differentially dry creped tissue product of the present invention and the nontrol conventionally dry creped tissue product. After l0 days of aging, the two products were compared and it was found that the tissue product of the present invention had an average of 95 percent greater bulk than the control tissue product. The density of the product was 1.58 pounds per cubic foot while that of the conventional product was 2.9 pounds per cubic foot. The product of the present invention was particularly suitable for use as a packing material as well as a wiping agent and padding means.

Examples I, II, III, and IV clearly demonstrate the improved results obtained by differentially dry creping cellulosic tissue webs through the application of a release agent in a pattern to the drier surface, rather than conventionally dry creping the tissue web to the same crepe ratio without the use of a pattern of release agent applied to the drier surface. In this connection, the differentially dry creped tissue products of the presentv invention exhibited had 43.5 percent, 73.2 percent, 48.6 percent, and

95 percent greater bulk than the respective conventionally creped controls. The densities of the multi-ply tissue products made by assembling sheets of the differentially dry creped webs made in accordance with the present invention were correspondingly lower than those of the respective conventional control products. The commercial importance in reducing the weight and hence the cost of tissue required for a given use or end result will be apparent.

Energy absorption tests were also run on the differentially dry creped tissue products of the present invention and it was found that these products had up to 50 percent more energy absorption per pound of product under low stress conditions than conventionally creped controls and lup to 40 percent more energy absorption under high stress conditions. Moreover, the tissue products of the present invention were found to be stable under stress, that is, they did not lose any more of their greater bulk after repeated impacts than did an equivalent thickness of conventional lower bulk material. Accordingly, the greater bulk of these products represents a substantial and permanent improvement in their cushioning properties.

The differentially dry creped tissue products of the` present invention can be provided with certain other valuable properties by combining the plies thereof with various other materials which do not substantially impair the improved characteristics of the products. For example, bonding materials may be added during the assembling of the plies of the product of the present invention into a finished unitary construction.

The number of plies of the tissue products of the present invention are varied so as to provide the bulk and cushioning properties required for any given use.

As is seen from the above, the differentially creped tissue products of the present invention constitute an important novel product having certain highly advantageous characteristics not present in the dry creped tissue products previously known in the art. Moreover, the products of the invention can be manufactured at high speed and in an economical manner on existing papermaking equipment. These products have the necessary low density, high bulk and surface characteristics for use as packing materials, wiping cloths, padding agents and the like and, as above noted, when used for these purposes, have important advantages over the prior art products.

Other suitable modifications of the differentially dry creped cellulosic tissue products of the present invention and the method of making the same, as are within the skill of those versed in the art, are contemplated as being within the scope of the present invention.

We claim:

1. A multi-ply cellulosic tissue product having improved bulk and density comprising a plurality of superposed, dry creped, substantially lint-free cellulosic tissue sheets, each of said sheets having a basis weight of from about 3.5 to about 15 pounds per 3,000 square foot ream and a crepe ratio of from about 1.25 to about 2.5, each of said sheets being characterized by a differentially creped configuration comprising substantially parallel longitudinally extending strips of relatively coarse crepe alternating withlongitudinally extending strips of relatively line crepe in a regular pattern across substantially the entire width of each of said sheets, said coarsely creped strips com-k prising from about 15% to about 85% of the total area of each sheet and having from about to about 20 crepes per inch, said finely creped strips comprising the remaining area of each sheet and having from about 30 to about 50 crepes per inch, the finely creped strips Vimparting stability to the adjacent coarsely creped strips in each sheet to maintain the improved bulk of the multi-ply product, which bulk is provided in each sheet by the coarsely creped strips, at a level from about 43.5 to about 95% higher than the bulk provided in a product formed of sheets having a single type of crepe.

2. A multi-ply cellulosic tissue product having improved bulk and density comprising a plurality of superposed, dry creped, substantially lint-free cellulosic tissue sheets, each of said sheets having a basis Weight of from about 3.5 to about pounds per 3,000 square foot ream and a crepe ratio of about 2.0, each of said sheets being characterized by a diterentially creped configuration in which substantially parallel longitudinally extending strips of relatively coarse crepe alternate with juxtaposed 1ongitudinally extending strips of relatively line crepe in a regular pattern across substantially the entire width of each of said sheets, the strips of coarse crepe comprising from about to about 60% of the total area of each of said sheets and having from about 10 to about, 20 crepes per inch, the strips of fine crepe comprising the remaining area of each of said sheets and having from about 3,0 to crepes per inch, the tine crepes imparting stability to the coarse crepes in each adjacent strip of each sheet to maintain the improved bulk of the product, which bulk is provided by the coarse crepes in each sheet, at a level of from about 43.5 to about higher than sheets having a single type of crepe, to provide a density in theresulting multi-ply product of from about 1.5 to about 2.0 pounds per cubic foot.

References Cited in the tile of thisr patent UNITED STATES PATENTS 1,033,992 Crane July 30, 1912 1,224,650 Kitchen May 1, 1917 1,588,732 Hoberg June 15, 1926 1,595,991 Cannard Aug. 17, 1926 1,764,676 Campbell June, 17, 1930 1,975,286 Pinoft Oct. 2, 1934 2,018,244 Alm Oct. 22, 1935 2,061,748 Augier Nov. 24, 1936 FOREIGN PATENTS' 456,032 Great Britain Nov. 2, 1936 303,522 Germany i Feb. 18,1916

UNITED STATES PATENT oFFCE CERTIFICATE OF CORRECTION Patent No. 31,0177317 January 116 i962 Edward H., Vpigtman et .eL

It is hereby certified that error appears in the above numbered petent requiring correction and that the seid Letters Patent should read as corrected below.

Column l, line 32Y for bit read bite --5 eolumn 3 line HY for "Mosture read e- Moisture oolumm L line TO, for dried read drier column 5 iine 23 for up read nip --3 column 6, line iI for "'dried" read drier Signed and sealed this 24th day of July 1962.

(SEAL) Atteat:

ERNEST* w. SWIDER` DAVID L. LADD Attestig 0fficer f Commissioner of Patents

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1033992 *21 Dec 191030 Jul 1912Frank G CranePaper towel.
US1224650 *25 Feb 19161 May 1917Joseph Moses Ward KitchenToilet-paper.
US1588732 *23 May 192315 Jun 1926Hoberg Frank HDoctor plate
US1595991 *7 Apr 192417 Aug 1926Cannard William HCrepe paper or the like material and method of and apparatus for producing same
US1764676 *20 Dec 192417 Jun 1930Campbell Samuel JCreping machine
US1975286 *5 Dec 19312 Oct 1934Patent & Licensing CorpProcess of manufacturing waterproof crepe-paper
US2018244 *7 Oct 193122 Oct 1935Dennison Mfg CoPaper product and method of making
US2061748 *20 Jan 193424 Nov 1936Angier Edward HProduction of coated creped paper
DE303522C * Title not available
GB456032A * Title not available
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3230136 *22 May 196418 Jan 1966Kimberly Clark CoPatterned tissue paper containing heavy basis weight ribs and fourdrinier wire for forming same
US4208459 *12 Nov 197617 Jun 1980Becker Henry EBonded, differentially creped, fibrous webs and method and apparatus for making same
US4464224 *30 Jun 19827 Aug 1984Cip Inc.Process for manufacture of high bulk paper
US4816320 *16 Jun 198628 Mar 1989St Cyr NapoleonToilet tissue and facial tissue
US4894118 *6 Aug 198616 Jan 1990Kimberly-Clark CorporationRecreped absorbent products and method of manufacture
US5173351 *30 Oct 199022 Dec 1992Kaysersberg, S.A.Absorbent combined sheet matierial
US5309828 *21 Feb 199210 May 1994Merry Wayne MMethod of compacting flat, stacked non-woven articles
US5524531 *17 Jun 199311 Jun 1996Merry; Wayne M.Method of compacting a plurality of flat, stacked, non-woven articles
US5558923 *20 Oct 199424 Sep 1996Mercamer OyPackage padding material and apparatus for forming package padding material
US5571382 *29 Apr 19925 Nov 1996Berglund; Roode P.Method of measuring and controlling adhesion/release of a paper web which is removed by a doctor blade from a yankee cylinder and a web tension gauge
US5972456 *23 Mar 199826 Oct 1999Esquivel; RobertoMulti-ply toilet paper product
US6042693 *30 Apr 199928 Mar 2000Fort James CorporationExtended life doctor blade and method of forming the same
US6074526 *18 Aug 199713 Jun 2000Fort James CorporationMethod of creping tissue
US6113470 *30 Apr 19995 Sep 2000Fort James CorporationMethod of forming a creping member
US61744121 Mar 199916 Jan 2001Purely Cotton, Inc.Cotton linter tissue products and method for preparing same
US641978911 Oct 199616 Jul 2002Fort James CorporationMethod of making a non compacted paper web containing refined long fiber using a charge controlled headbox and a single ply towel made by the process
US6436511 *25 Jan 200020 Aug 2002Ranpak Corp.Cushioning conversion machine, method and product
US6454901 *22 Aug 200024 Sep 2002Maintech Co., Ltd.Method of making quality crepe paper
US6458243 *27 Apr 20011 Oct 2002Kimberly Clark Worldwide Inc.Soft absorbent paper product containing deactivated ketene dimer agents
US6558510 *21 Aug 20006 May 2003Fort James CorporationWet-crepe process utilizing narrow crepe shelf for making absorbent sheet
US6846383 *10 Jul 200225 Jan 2005Kimberly-Clark Worldwide, Inc.Wiping products made according to a low temperature delamination process
US6918993 *28 May 200319 Jul 2005Kimberly-Clark Worldwide, Inc.Multi-ply wiping products made according to a low temperature delamination process
US69917062 Sep 200331 Jan 2006Kimberly-Clark Worldwide, Inc.Clothlike pattern densified web
US699801620 Dec 200114 Feb 2006Fort James CorporationMethod of making a non compacted paper web containing refined long fiber using a charge controlled headbox and a single ply towel made by the process
US71893072 Sep 200313 Mar 2007Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US722952915 Jul 200412 Jun 2007Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US725274127 Oct 20057 Aug 2007Georgia-Pacific Consumer Products LpMethod of making a paper web containing refined long fiber using a charge controlled headbox and a single ply towel made by the process
US729723115 Jul 200420 Nov 2007Kimberly-Clark Worldwide, Inc.Binders curable at room temperature with low blocking
US736125318 Jul 200522 Apr 2008Kimberly-Clark Worldwide, Inc.Multi-ply wiping products made according to a low temperature delamination process
US74353129 Nov 200514 Oct 2008Kimberly-Clark Worldwide, Inc.Method of making a clothlike pattern densified web
US74490851 Nov 200611 Nov 2008Kimberly-Clark Worldwide, Inc.Paper sheet having high absorbent capacity and delayed wet-out
US7468117 *29 Apr 200523 Dec 2008Kimberly-Clark Worldwide, Inc.Method of transferring a wet tissue web to a three-dimensional fabric
US756638116 Apr 200728 Jul 2009Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US767822817 Sep 200716 Mar 2010Kimberly-Clark Worldwide, Inc.Binders curable at room temperature with low blocking
US767885617 Sep 200716 Mar 2010Kimberly-Clark Worldwide Inc.Binders curable at room temperature with low blocking
US768248827 Jun 200723 Mar 2010Georgia-Pacific Consumer Products LpMethod of making a paper web containing refined long fiber using a charge controlled headbox
US834662028 Sep 20101 Jan 2013Google Inc.Automatic modification of web pages
US846621616 Apr 200718 Jun 2013Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US862076011 Oct 201031 Dec 2013Google Inc.Methods and systems for initiating application processes by data capture from rendered documents
US8691051 *6 Apr 20078 Apr 2014Gruppo Cordenons S.P.A.Security paper material, in particular for labelling and packaging, and manufacturing method thereof
US96695962 Aug 20136 Jun 2017Ranpak Corp.Dunnage conversion machine and method
US20040007339 *10 Jul 200215 Jan 2004Kimberly-Clark Worldwide, Inc.Wiping products made according to a low temperature delamination process
US20040031578 *28 May 200319 Feb 2004Kimberly-Clark Worldwide, Inc.Multi-ply wiping products made according to a low temperature delamination process
US20050045292 *2 Sep 20033 Mar 2005Lindsay Jeffrey DeanClothlike pattern densified web
US20050045293 *2 Sep 20033 Mar 2005Hermans Michael AlanPaper sheet having high absorbent capacity and delayed wet-out
US20050045294 *2 Sep 20033 Mar 2005Goulet Mike ThomasLow odor binders curable at room temperature
US20050045295 *15 Jul 20043 Mar 2005Kimberly-Clark Worldwide, Inc.Low odor binders curable at room temperature
US20050247417 *18 Jul 200510 Nov 2005Maurizio TirimaccoMulti-ply wiping products made according to a low temperature delamination process
US20060014884 *15 Jul 200419 Jan 2006Kimberty-Clark Worldwide, Inc.Binders curable at room temperature with low blocking
US20060032595 *27 Oct 200516 Feb 2006Fort James CorporationMethod of making a paper web containing refined long fiber using a charge controlled headbox and a single ply towel made by the process
US20060243408 *29 Apr 20052 Nov 2006Kimberly-Clark Worldwide, Inc.Method of transferring a wet tissue web to a three-dimensional fabric
US20070051484 *1 Nov 20068 Mar 2007Hermans Michael APaper sheet having high absorbent capacity and delayed wet-out
US20070187056 *16 Apr 200716 Aug 2007Goulet Mike TLow odor binders curable at room temperature
US20070194274 *16 Apr 200723 Aug 2007Goulet Mike TLow odor binders curable at room temperature
US20080006382 *17 Sep 200710 Jan 2008Goulet Mike TBinders curable at room temperature with low blocking
US20090173463 *6 Apr 20079 Jul 2009Gruppo Cordenons S.P.A.Security paper material, in particular for labelling and packaging, and manufacturing method thereof
EP2937212A1 *24 Sep 200828 Oct 2015Ranpak Corp.Dunnage conversion machine and method
Classifications
U.S. Classification162/111, 428/154, 162/132, 428/535
International ClassificationB31F1/12, B31F1/00
Cooperative ClassificationB31F1/12
European ClassificationB31F1/12