In order to further illustrate this invention, a three-layered tissue sheet suitable for single-ply bath tissue was made in which the two outer layers comprised a debonded mixture of Aracruz eucalyptus fibers and broke fibers and the center layer comprised refined northern softwood kraft (NSWK) fibers. Broke fibers comprised 16.5 percent of the sheet on a dry fiber basis. Prior to formation, the outer layer fibers were pulped for 15 minutes at 10 percent consistency and diluted to about 2.5 percent consistency after pulping. A debonder (ProSoft TQ1003) was added to the outer layer pulp in the amount of 1 kilogram of debonder per tonne of outer layer dry fiber. The NSWK fibers were pulped for 30 minutes at 4 percent consistency and diluted to about 2.7 percent consistency after pulping. The overall layered sheet weight was split 34 percent to the center layer on a dry fiber basis and 33 percent to each of the outer layers. The center layer was refined to levels required to achieve target strength values, while the outer layers provided surface softness and bulk. Parez 631NC was added to the center layer at 1.5 kilograms per tonne of center layer dry fiber.
A three-layer headbox was used to form the wet web with the refined NSWK stock in the center layer of the headbox. Turbulence-generating inserts recessed about 3.5 inches (89 millimeters) from the slice and layer dividers extending about 1 inch (25 millimeters) beyond the slice were employed. The net slice opening was about 0.9 inch (23 millimeters). The water flows in the headbox layers were split 28.5 percent to each of the outer layers and 43 percent to the center layer. The consistency of the stock fed to the headbox was about 0.1 weight percent.
The resulting three-layered web was formed on a twin-wire, suction form roll former, with the outer forming fabric being an Asten 867A, and the inner forming fabric being a Voith Fabrics 2164-33B. The speed of the forming fabrics was 2000 feet per minute (10.16 meters per second). The newly-formed web was then dewatered to a consistency of about 27-29 percent using vacuum suction from below the forming fabric before being transferred to a transfer fabric, which was traveling at 1600 feet per minute (8.13 meters per second) (25 percent rush transfer). The transfer fabric was a Voith Fabrics t1207-6. A vacuum shoe pulling about 10 inches (254 mm) of mercury rush transfer vacuum was used to transfer the web to the transfer fabric.
The web was then transferred to a Voith Fabrics Finelink BC linkbelt throughdrying fabric modified with a printed pattern as shown in
A vacuum transfer roll was used to wet mold the sheet into the throughdrying fabric at about 8 inches (203 mm) of mercury wet molding vacuum. The throughdrying fabric was traveling at a speed of about 8.13 meters per second. The web was carried over a pair of Honeycomb throughdryers operating at a supply temperature of about 390° F. (199° C.) and dried to final dryness of about 99 percent consistency.
The resulting tissue is shown in
Tissue sheets were made as described in Example 1, except that the speed of the forming fabrics was 2048 feet per minute (10.40 meters per second, 28% rush transfer) and the throughdrying fabric was a Voith Fabrics Finelink BC linkbelt modified with a printed pattern as shown in
The resulting tissue is shown in
Tissue sheets were made as described in Example 2, except that the throughdrying fabric was a Voith Fabrics Finelink BC linkbelt modified with a printed pattern as shown in
The resulting tissue is shown in
It will be appreciated that the foregoing examples, given for purposes of illustration, are not to be construed as limiting the scope of this invention, which is defined by the following claims and all equivalents thereto.