PAPER SHEET MULCHES AND METHODS OF MAKING THE SAME

Abstract

The present disclosure provides novel paper sheet mulch products having benefits over prior sheet mulches, which may include brown or recycled fibers, as well as additives, such as opacity, water-resistant, and strength additives, resulting in mulch products with an improved combination of basis weight, stretch, strength, opacity, and/or water-resistance characteristics.

Claims

1. A paper sheet mulch comprising: at least about 75% cellulosic papermaking fibers based on the dry weight of the sheet, a basis weight of from about 25 lb/3000 ft.sup.2 to about 45 lb/3000 ft.sup.2, an opacity of at least about 95%; and a machine-direction stretch of at least about 5% and a cross machine-direction stretch of at least about 5%.

2. The paper sheet mulch of claim 1, comprising from about 75% to 100% recycled cellulosic fibers based on the dry weight of the paper sheet.

3. The paper sheet mulch of claim 2, wherein the recycled cellulosic fibers comprise one of old newsprint fibers, corrugated container fibers, mixed recycled paper fibers, and combinations thereof.

4. The paper sheet mulch of claim 1, comprising from about 75% to 100% cellulosic fibers with an ISO brightness of less than about 80 based on the dry weight of the paper sheet.

5. The paper sheet mulch of claim 1, comprising a contact angle with water of at least about 75.

6. The paper sheet mulch of claim 1, comprising a kappa number of at least about 70.

7. The paper sheet mulch of claim 1, comprising at least one opacity modifier comprising one or more of carbon black, biochar, a pigment, a dye, clay, kaolin, titanium oxide, and combinations thereof.

8. The paper sheet mulch of claim 7, wherein the at least one opacity modifier comprises a black or blue pigment.

9. The paper sheet mulch of claim 7, wherein the at least one opacity modifier comprises carbon black.

10. The paper sheet mulch of claim 1, comprising at least one water-resistant modifier comprising one or more of an acrylic, wax, alkenyl ketene dimer (ALKD), alkyl ketene dimer (AKD), alkenyl succinic anhydride (ASA), fluorochemical, silicone, hydrophobically modified anionic polymer (HMAP), hydrophobically modified cationic polymer (HMCP), ethylene-acrylic acid (EAA), neutral rosin emulsion, and combinations thereof.

11. The paper sheet mulch of claim 1, comprising at least one wet strength additive comprising one or more of an aliphatic aldehyde, aromatic aldehyde, urea-formaldehyde resin, melamine formaldehyde resin, polyimide-epichlorohydrin resin, and combinations thereof.

12. The paper sheet mulch of claim 1, comprising at least one dry strength additive comprising one or more of a starch, guar gum, polyacrylamide, carboxymethyl cellulose, and combinations thereof

13. The paper sheet mulch of claim 1, wherein the sheet is single-ply.

14. The paper sheet mulch of claim 1, comprising a caliper of from about 4 mils/1 sht to about 8 mils/1 sht.

15. The paper sheet mulch of claim 1, comprising a machine-direction tensile strength of from about 5 lb/1 in to about 18 lb/1 in and a cross machine-direction tensile strength of from about 2 lb/1 in to about 10 lb/1 in.

16. The paper sheet mulch of claim 1, comprising a 0.1 ml water absorption rate of at least about 90 seconds

17. The paper sheet mulch of claim 1, comprising a machine-direction wet tensile strength of at least about 3 lb/1 in.

18. The paper sheet mulch of claim 1, comprising biodegradation rate of from about 200 mg to about 700 mg CO2 in 45 days.

19. A method of making a paper sheet mulch comprising: manufacturing a non-woven paper sheet having a basis weight of from about 25 lb/3000 ft.sup.2 to about 45 lb/3000 ft.sup.2 on a paper-making machine from a furnish comprising at least about 75% cellulosic papermaking fibers based on the dry weight of the sheet; adding at least one opacity modifier to the sheet, such that the paper sheet has an opacity of at least about 95%; and creping the sheet; wherein the sheet has a machine-direction stretch of at least about 5% and a cross machine-direction stretch of at least about 5%.

20-36. (canceled)

Description

DETAILED DESCRIPTION

[0011] The base sheet for use in the paper sheet mulch products of the present disclosure may be made from any art recognized cellulosic papermaking fibers. The papermaking fibers may be either bleached, brown, recycled, or a mixture thereof. In some embodiments, the paper sheet mulch product comprises at least about 75% cellulosic papermaking fibers based on the dry weight of the sheet, for example, at least 85%, at least about 90%, or at least about 95%.

[0012] In some embodiments, the cellulosic papermaking fibers include at least some fibers having an ISO brightness of less than about 80 in order to reduce cost and increase opacity of the final product. In some embodiments, the papermaking fibers may include those having an ISO brightness of less than about 70 or less than about 60. ISO brightness may be determined according to TAPPI T525. In some embodiments, the paper sheet mulch product may comprise at least about 50% cellulosic papermaking fibers having an ISO brightness less than about 80 based on the dry weight of the sheet, for example at least about 75%, at least about 90%, at least about 95%, or from about 75% to about 100% fibers having an ISO brightness less than about 80 based on the dry weight of the sheet.

[0013] In some embodiments, the cellulosic papermaking fibers include at least some recycled fibers, for example mixed recycled fibers (MRF), old newsprint (ONP) fibers, old corrugated container (OCC) fibers, and the like. In some embodiments, the paper sheet mulch product may comprise at least about 50% recycled cellulosic papermaking fibers based on the dry weight of the sheet, for example at least about 75%, at least about 90%, at least about 95%, or from about 75% to about 100% recycled fibers based on the dry weight of the sheet. Without wishing to be bound by theory, it is believed that incorporation of high lignin recycled fibers such as, for example, ONP fibers and/or OCC fibers, may beneficially decrease the rate of biodegradation of the paper sheet. On the other hand, too much lignin can reduce inter-fiber bonding, resulting in a weaker sheet.

[0014] In some embodiments, the paper sheet may have a kappa number of at least about 45, at least about 70, at least about 130, or at least about 150, for example from about 45 to about 200, from about 70 to about 180, or from about 130 to about 160 (where kappa number is used as a valuation of lignin content). Kappa number may be determined by Tappi T236.

[0015] In some embodiments, the paper sheet mulch product may comprise at least about 30% ONP fibers based on the dry weight of the sheet, for example at least about 50%, or at least about 75%. In addition to slowing biodegradation through increased lignin content, it is also believed that incorporation of ONP fibers may beneficially increase the opacity of the paper sheet mulch product due to the inks and/or pigments used in the newsprint process. In some embodiments, the paper sheet mulch product may comprise at least about 30% OCC fibers based on the dry weight of the sheet, for example at least about 50%, or at least about 75%. In some embodiments, the paper sheet mulch product may comprise a combination of ONP and OCC fibers in an amount of at least about 75% based on the dry weight of the sheet, for example, at least 85%, at least about 90%, or at least about 95% based on the dry weight of the sheet.

[0016] The paper sheet mulch products of the present invention may be manufactured on a non-woven tissue paper-making machine. In a typical process, the fiber is fed into a headbox where it will be admixed with water and chemical additives, as appropriate, before being deposited on a forming wire. The chemical additives for use in the formation of the base sheets can be any known combination of papermaking chemicals. Papermaking chemicals include, for example, one or more of strength agents, softeners, debonders, creping modifiers, sizing agents, optical brightening agents, retention agents, and the like. As used herein sheet, web, tissue, nascent web, tissue product, base sheet or tissue sheet, can be used interchangeably to refer to the paper web during various stages of its development. Nascent web, for example, refers to the embryonic web that is deposited on the forming wire. Once the web achieves about 30% solids content, it is referred to as a tissue, or a sheet, or a web. Post-production, the single-ply of tissue is typically called a paper sheet or base sheet.

[0017] In some embodiments, the paper sheet mulch products of the present invention may be manufactured using through-air-drying (TAD) methods. In TAD methods the nascent web is partially dewatered using vacuum suction. Thereafter, the partially dewatered web is dried without compression by passing hot air through the web while it is supported by a through-drying fabric. In some embodiments, the TAD processes use special fabrics or belts to impart a structure to the sheet during drying. While one through-air-drying operation is described above, the system is only exemplary and variations on the described system will be readily apparent to the skilled artisan.

[0018] In some embodiments, the paper sheet mulch products of the present invention may be manufactured using conventional wet pressing (CWP) methods. In conventional wet pressing, the nascent web is transferred to a papermaking felt and is dewatered by passing it between the felt and a press roll under pressure. The web is then pressed by a suction press roll against the surface of a rotating Yankee dryer cylinder that is heated to cause the paper to substantially dry on the cylinder surface. The moisture within the web as it is laid on the Yankee surface causes the web to transfer to the surface. Liquid adhesive may be applied to the surface of the dryer, as necessary, to provide substantial adherence of the web to the surface. The web is then removed from the Yankee surface with a creping blade. The creped web is then passed between calendar rollers and rolled up to be used in the downstream production of a paper product. This method of making tissue sheets is commonly referred to as wet-pressed because of the compactive method used to dewater the wet web. While one conventional wet pressing operation is described above, the system is only exemplary and variations on the described system will be readily apparent to the skilled artisan.

[0019] In some embodiments, the paper sheet may be creped to enhance stretch and bulk, for example creped from a Yankee dryer in a conventional wet pressing process. Creping may be performed by any conventual type of creping blade. In some embodiments, a non-Taurus (e.g., blue steel) blade is used. In some embodiments, a Taurus crepe blade is used. Without wishing to be bound by theory, it is believed that use of a Taurus blade may increase the stretch of the sheet (for example the cross-direction (CD) stretch), which is believed to improve the handling of the sheet during the mulch laying operation. In some embodiments, the paper-making machine may be run with a speed differential between the Yankee dryer and a rolling reel in order to increase MD stretch.

[0020] In a typical process, after drying, the base sheet is rolled and awaits converting. Converting refers to the process that changes or converts base sheets into final products. In some embodiments, wrinkles may be imparted to the sheet during converting, for example with a bowed roll or a roll with annular rings. Without wishing to be bound by theory, it is believed that adding wrinkles to the sheet further increases the stretch or give of the sheet. In some embodiments, wrinkles may be added in an orientation fully or partially aligned in the machine direction (the direction the sheet travels in the papermaking machine during formation and processing). Without wishing to be bound by theory, it is believed that adding wrinkles to the sheet that are fully or partially aligned in the machine direction provides particular increase to the cross-direction stretch of the sheet. In some embodiments, the paper sheet has wrinkles in a direction between about 30 and about 90 from the cross-machine direction, for example, between about 60 and about 90.

[0021] In some embodiments, folds may be imparted to the sheet during converting. In some embodiments, folds may be created during a rewinding operation by running the web over folding boards or plows to impart one or more folds in the sheet, for example in the form of back-and-forth folds, pleats, or gussets. The sheet may then be directed through one or more pressing nips, for example between calendar rolls, to fix the folds into place. Without wishing to be bound by theory, it is believed that creating folds in the sheets provides stress relief points that allow the sheet to relax, rather than tear, particularly during the mulch laying process. In some embodiments, folds may be added in an orientation fully or partially aligned in the machine direction. Without wishing to be bound by theory, it is believed that adding folds to the sheet that are fully or partially aligned in the machine direction provides particular increase to the cross-direction stretch of the sheet. In some embodiments, the paper sheet has folds running in a direction between about 30 and about 90 from the cross-machine direction, for example, between about 60 and about 90.

[0022] In some embodiments, the paper sheet mulch product may be single-ply, comprising only one paper base sheet. In some embodiments, the paper sheet mulch product may be a multi-ply product formed by combining two or more paper base sheets.

[0023] In some embodiments, the paper sheet may be treated with an opacity modifier to increase opacity. The opacity modifier may be any additive sufficient to obtain substantially 100% opacity (at least 95% opacity). Opacity may be determined according to TAPPI T425. In some embodiments, the opacity modifier may comprise one or more of carbon black (for example a bio-based carbon black), biochar, pigments or dyes (for example organic and/or inorganic pigments or dyes), fillers (for example clay, kaolin, and titanium oxide), and the like.

[0024] In some embodiments, an opacity modifier may be an opacity surface coating. The opacity surface coating may be applied after sheet formation by any known technique, for example, by printing, coating, or spraying. In some embodiments, the opacity modifier may be applied as a coating on both sides of the sheet. In some embodiments, when applied as an opacity surface coating, the opacity modifier may be applied in an amount of from about 0.2 to about 20 lbs/ream based on the dry weight of the sheet, for example, from about 2 to about 10 lbs/ream. In some embodiments, carbon black may be applied as an opacity surface coating in an amount of from about 1 to about 10 lbs/ream based on the dry weight of the sheet, for example, from about from about 2 to about 5 lbs/ream. In some embodiments, biochar may be applied as an opacity surface coating in an amount of from about 2 to about 10 lbs/ream, for example from about 7 to about 10 lbs/ream or from about 8 to about 9 lbs/ream based on the dry weight of the sheet.

[0025] In some embodiments, an opacity modifier may be added in the wet-end of the papermaking machine prior to sheet formation. In some embodiments, the opacity modifier may be added in the headbox. In some embodiments, the opacity modifier may be added before the headbox, for example at the stuff box, fan pump, or machine chest pump. In some embodiments, an opacity modifier may be added at the machine chest pump. In some embodiments, the opacity modifier may be at least one organic and/or inorganic pigment, such as a blue or black pigment, added in the wet-end of the papermaking machine prior to sheet formation in an amount of from about 0.2 to about 30 pounds per ton of dry weight of the fiber, for example from about 2 to about 20, about 5 to about 15, or about 8 to about 12 pounds per ton of dry weight of the fiber.

[0026] In some embodiments, an opacity modifier may be added in the wet-end of the papermaking machine prior to sheet formation and an opacity modifier may be added as an opacity surface coating following sheet formation.

[0027] In some embodiments, the paper sheet may be treated with a water-resistant modifier. The water-resistant modifier can be any substance that will bond to cellulose and also repel a liquid such as water, for example an oleophobe or a hydrophobe. In some embodiments, the water-resistant modifier may comprise one or more of acrylics, waxes, alkenyl ketene dimers (ALKD), alkyl ketene dimers (AKD), alkenyl succinic anhydrides (ASA), fluorochemicals, silicones, hydrophobically modified anionic polymers (HMAP), hydrophobically modified cationic polymers (HMCP), ethylene-acrylic acids (EAA), neutral rosin emulsions, conventional paper sizing agents, and the like. In some embodiments, the water-resistance additive may be acrylic. In some embodiments, the water-resistance additive may be AKD.

[0028] In some embodiments, the water-resistant modifier may be applied as a surface coating. The water-resistant surface coating may be applied after sheet formation by any known technique, for example printing, coating, or spraying. In some embodiments, the water-resistant modifier may be applied as a coating on both sides of the sheet. In some embodiments, a water-resistant modifier may be applied as a surface coating in an amount of from about 0.2 to about 20 lbs/ream based on the dry weight of the sheet. In some embodiments, an acrylic containing water-resistant coating may be applied as a surface coating in an amount of from about 1 to about 15 lbs/ream based on the dry weight of the sheet, for example, from about 8 to about 12 lbs/ream.

[0029] In some embodiments, the water-resistant modifier may be added in the wet-end of the papermaking machine prior to sheet formation. In some embodiments, the water-resistant modifier may be added in the headbox. In some embodiments, the water-resistant modifier may be added before the headbox, for example at the stuff box, fan pump, or machine chest pump. In some embodiments, a water-resistant modifier may be added at the machine fan pump. In some embodiments, when applied in the wet-end of the papermaking machine, the water-resistant modifier may be applied in an amount of from about 0.2 to about 30 pounds per ton of dry weight of the fiber, for example, from about 2 to about 20 pounds per ton. In some embodiments, alkyl ketene dimer may be added in the wet-end of the papermaking machine prior to sheet formation as a water-resistant modifier in an amount of from about 1 to about 10 pounds per ton of dry weight of the fiber, for example from about 4 to about 6 pounds per ton of dry weight of the fiber.

[0030] In some embodiments, a water-resistant modifier may be added in the wet-end of the papermaking machine prior to sheet formation and a water-resistant modifier may be added as a surface coating following sheet formation.

[0031] In some embodiments, one or more wet strength additives may be added to the paper sheet mulch. In some embodiments, the one or more wet strength additives may be added in the wet-end of the papermaking machine prior to sheet formation in an amount of from about 0.2 to about 30 pounds per ton of dry weight of the fiber, for example, from about 2 to about 20, or from about 5 to about 10 pounds per ton of dry weight of the fiber. Wet strength additives suitable for use include, but are not limited to, one or more of aliphatic and aromatic aldehydes, urea-formaldehyde resins, melamine formaldehyde resins, polyamide-epichlorohydrin resins, and the like. In one embodiment, the at least one wet strength additive may be a polyamide-epichlorohydrin (PAE) resin, and the like.

[0032] In some embodiments, one or more dry strength additives may be added to the paper sheet mulch. In some embodiments, the one or more dry strength additives may be added in the wet-end of the papermaking machine prior to sheet formation in an amount of from about 0.2 to about 10 pounds per ton of dry weight of the fiber, for example, from about 0.5 to about 7, or from about 1 to about 4 pounds per ton of dry weight of the fiber. Dry strength additives suitable for use include, but are not limited to, anionic polyacrylamide, carboxymethylcellulose, ethylene-maleamic acid copolymer, acrylamide-maleic acid copolymer, starch, guar gum, cationic guar gum, cationic starch, cationic polyacrylamide, poly-DADMAC, cationic polyacrylates, anionic starch, cationic latex, glyoxylated polyacrylamide, polyamine, cationic PVA, amphoteric dry strength resins, and the like.

[0033] In some embodiments, the paper sheet mulch products of the present disclosure may have a basis weight of from about 20 lb/3000 ft.sup.2 to about 50 lb/3000 ft.sup.2, for example, from about 25 lb/3000 ft.sup.2 to about 45 lb/3000 ft.sup.2, or from about 30 lb/3000 ft.sup.2 to about 40 lb/3000 ft.sup.2. Basis weight may be measured according to Tappi T410.

[0034] In some embodiments, the paper sheet mulch products of the present disclosure may have a caliper of from about 3 mils/1 sht to about 10 mils/1 sht, for example, from about 4 mils/1 sht to about 8 mils/1 sht. Caliper may be determined by Tappi T411.

[0035] In some embodiments, the paper sheet mulch products of the present disclosure may have a machine-direction tensile strength (Tensile MD) of at least about 5 lb/1 in, for example, at least about 10 lb/1 in, or from about 5 lb/1 in to about 20 lb/1 in, or from about 6 lb/1 in to about 13 lb/1 in. In some embodiments, the paper sheet mulch products of the present disclosure may have a cross machine-direction tensile strength (Tensile CD) of at least about 2 lb/1 in, for example, at least about 5 lb/1 in, or from about 2 lb/1 in to about 10 lb/1 in. Tensile MD and Tensile CD may be determined according to Tappi TM-494.

[0036] In some embodiments, the paper sheet mulch products may have a machine-direction stretch (Stretch MD) of at least about 1%, for example, at least about 5%, at least about 8%, or at least about 10%, or from about 1% to about 30%, for example, from about 5% to about 20%. In some embodiments, the paper sheet mulch products of the present disclosure may have a cross machine-direction stretch (Stretch CD) of at least about 1%, for example, at least about 5%, at least about 8%, or at least about 10%, or from about 1% to about 30%, for example, from about 5% to about 20%. Stretch MD and Stretch CD may be determined according to Tappi TM-494.

[0037] In some embodiments, the paper sheet mulch products of the present disclosure may have a machine-direction wet tensile strength (Wet Tensile MD) of at least about 1 lb/1 in, for example, at least about 3 lb/1 in, at least about 5 lb/1 in, or from about 1 lb/1 in to about 7 lb/1 in, or from about 1.5 lb/1 in to about 3 lb/1 in. In some embodiments, the paper sheet mulch products of the present disclosure may have a cross machine-direction wet tensile strength (Wet Tensile CD) of from about 0.5 lb/1 in to about 6 lb/1 in, for example, from about 0.7 lb/1 in to about 2 lb/1 in. Wet Tensile MD and Wet Tensile CD may be determined according to Tappi TM-494.

[0038] In some embodiments, the paper sheet mulch products of the present disclosure may have an opacity of at least about 95%, for example, at least about 98%, or about 100%. Opacity may be determined according to TAPPI T425.

[0039] In some embodiments, the paper sheet mulch products of the present disclosure may have a 0.1 ml water absorption rate (WAR) of at least about 90 seconds, for example, at least about 200 seconds, at least about 500 seconds, or at least about 1000 seconds. WAR may be determined by Tappi T432.

[0040] Contact angle is often used to evaluate the wettability or water resistance of cellulose-based surfaces. In some embodiments, the paper sheet mulch products of the present disclosure may have a contact angle of from about 0 to about 150. The contact angle may depend on the method by which water resistance is imparted to the sheet. In some embodiments where water resistance is imparted by addition of a water-resistant modifier in the wet-end of a papermaking machine, the contact angle may be less than about 50, for example, from about 0 to about 20. In some embodiments where water resistance is imparted by addition of a water-resistant modifier to the surface of the sheet, the contact angle may be greater than about 75, for example great than about 90, greater than about 110, or from about 110 to about 150. Contact angle may be determined by Tappi T558.

[0041] The biodegradation rate of the paper sheet mulches described herein may be evaluated by measuring gaseous carbon generation over time. The biodegradation rate may be measured using ASTM method D5988. Paper sheet mulch samples are mixed with defined amounts of soil to create test samples, which are placed in sealed jars and incubated at a controlled temperature of 40 C for 45 days. Reference samples consisting of only the defined amount of soil are similarly prepared and incubated for 45 days. After 45 days, the CO2 generated by each of the test samples and the reference samples are measured. The biodegradation rate is the amount of CO2 generated by a test sample minus the amount of CO2 generated by its corresponding reference sample. In some embodiments, the paper sheet mulch products described herein may have a biodegradation rate of from about 100 mg to about 900 mg of CO2 in 45 days, for example, from about 200 mg to about 700 mg of CO2 in 45 days.

[0042] In some embodiments, the paper sheet mulch products of the present disclosure may have a Gurley Porosity of from about 1 s/100 cm.sup.3 to about 100 s/100 cm.sup.3. Gurley Porosity may be determined by Tappi T460.

[0043] It will be understood that various modifications may be made without departing from the spirit and scope of the disclosure.

Example 1

[0044] Single-ply paper basesheets were produced at different basis weights using conventional wet press drying methods with non-Taurus crepe blades. The basesheets were produced using a furnish of 60% OCC fibers and 40% mixed recycled paper fibers. Process parameters for manufacturing the basesheets are reported in Table 1.

TABLE-US-00001 TABLE 1 27.5# 34.0# Yankee Speed fpm 2575 2450 AD Speed fpm 2382 2265 Reel Speed fpm 2422 2306 Refiner - North amps 28 28 Refiner - South amps 25 34 Hood Temp WE F 740 800 Hoof Temp DE F 740 800 Yankee Steam psi 75 82 AD Steam psi 4 30 Wet Strength Flow ml/min 1250 1350 Dry Strength Flow ml/min 1600 1600 PVOH ml/min 455 455 Modifier ml/min 31 31 Coating ml/min 46 46 Stock Flow gpm 915 1070

[0045] Chemicals added to the basesheets in the wet-end of the papermaking process during production are reported in Table 2 as a percentage based on the dry weight of the fiber. Less than 100% of the chemicals added in the wet-end are retained in the final basesheet. For example, it is estimated that only 5% of the Yankee coating package ends up in the final basesheet.

TABLE-US-00002 TABLE 2 Additive Type Additive 27.5# 34.0# Wet Strength polyamide-epichlorohydrin 0.35% 0.34% (PAE) resin Dry Strength glyoxylated polyacrylamide 0.13% 0.12% (GPAM) Creping Adhesive Poly (vinyl alcohol) (PVOH) 0.02% 0.02% Creping Modifier polyolefin and mineral oil 0.01% 0.01% Creping Adhesive polyamide-epichlorohydrin 0.01% 0.01% (PAE) resin

[0046] The basesheets were tested for physical properties and then split into two 50.25 inch parent rolls and tested for opacity, WAR (water absorption), and contact angle (water resistance). The results of these tests are reported in Table 3.

TABLE-US-00003 TABLE 3 27.5# 27.5# 34.0# 34.0# Before After Before After Property Units Splitting Splitting Splitting Splitting Basis Weight lb/3000 ft2 27.8 33.6 Caliper mils/8 sht 56.7 52.5 55 50.9 Stretch MD % 10.8 9.6 10.8 9.1 Stretch CD % 3.2 4.1 Tensile CD g/3 in 5815 6943 Tensile MD g/3 in 9656 9669 11001 11974 Wet Tensile CD g/3 in 2015 2158 Wet Tensile MD g/3 in 3326 3247 WAR 0.1 mL sec 180+ 139 Contact Angle degree 0 0 Opacity MacBeth opacity 91.2 95.6 units

[0047] The trial produced reels at approximately 27.5 lbs/ream and 34 lbs/ream basis weights. Reducing the caliper and increased smoothness were target properties to improve the final coated sheet. The 34 lbs/ream sheet had lower caliper than the 27.5 lbs/ream sheet. This was attributed to higher sheet moisture at the Yankee and steam in the after dryers. Reel moisture increased from 1.6% on the 27.5 lbs/ream to 2.5% for the 34 lbs/ream.

[0048] Paper sheets made with target basis weights of 27.5 and 34 lbs/ream were further coated with a carbon black ink opacity coating and/or an acrylic water-resistance coating. The sheets were tested for certain properties reported in Table 4.

TABLE-US-00004 TABLE 4 Property Units 27.5# 27.5# 34# 34# Basis Weight lb/3000 ft.sup.2 28.6 30.2 36.5 37.1 Carbon black ink coating lb/3000 ft.sup.2 2.0 2 2.4 2.4 Acrylic coating lb/3000 ft.sup.2 0 1.2 0 1.1 Caliper mils/1 sht 5.3 5.4 6.4 6.4 Tensile MD lb/1 in 6.3 6.0 7.7 7.4 Tensile CD lb/1 in 3.8 4.0 5.0 4.8 Stretch MD % 5.4 6.0 7.3 7.7 Stretch CD % 2.6 2.6 2.8 2.7 TEA MD in-lb/in.sup.2 0.19 0.20 0.32 0.31 TEA CD in-lb/in.sup.2 0.06 0.06 0.09 0.08 Tensile Modulus MD psi/1000 20 23 22 23 Tensile Modulus CD psi/1000 53 59 55 55 Wet Tensile MD lbf/1 in 1.9 1.9 2.3 2.3 Wet Tensile CD lbf/1 in 1.1 1.2 1.4 1.5 Tear MD g 31 32 40 39 Tear CD g 37 40 51 56 Gurley Stiffness MD 6 6 10 10 Gurley Stiffness CD 12 12 21 26 Trapezoidal MD Tensile gf 906 911 1844 2313 Trapezoidal MD Elongation % 7.6 6.5 9.2 10.1 Trapezoidal MD Energy gf-mm 1702 1735 4764 6344 Opacity MacBeth Opacity units 96.3 96.3 97.7 98.3 WAR (0.1 ml) s 176 180+ 135 157 Contact Angle degrees 0 0 0 0 Gurley Porosity s/100 cm.sup.3 1.1 1.4 1.6 1.7