Process for manufacture of high bulk paper

Claim 2

A process for the manufacture of a high bulk paper or a high bulk layer of a multi-layered paper, said paper or layer being creped, in which an aqueous slurry consisting essentially of ligno-cellulosic fibers in a papermaking bond forming state is dewatered in contact with a foraminous surface to form a web which is subsequently pressed and dried, characterized in that dry fibers consisting essentially of ligno-cellulosic fibers of the type which when fully wetted have interfiber bonding capacity are introduced into the slurry and interspersed with said bond forming state fibers shortly before formation of the web and in such manner that the web incorporates initially dry fibers which entered the slurry in said introducing step and which remain incompletely wetted by reason of having a short water contact time of less than 45 minutes while the web is formed and pressed and is creped by being passed over a Yankee cylinder, the amount of said incompletely wetted fibers being between 10% and 80% of the total fibers used to form the web.

Claim 3

A process according to claim 1, including the step of subjecting said dry fibers to dry defibration before introduction into the slurry.

Claim 4

A process for the manufacture of a high bulk paper or a high bulk layer of a multi-layered paper said paper or layer being creped, which process comprises the steps of: (a) forming an aqueous slurry consisting essentially of ligno-cellulosic fibers in a papermaking bond forming state, (b) subjecting dry pulp consisting essentially of ligno-cellulosic pulp to dry defibration and introducing the dry fibers so produced into said slurry and mixing these with the bond forming state fibers, said dry fibers consisting essentially of the type which when fully wetted have interfiber bond forming capacity; and shortly thereafter, (c) dewatering the slurry of mixed fibers in contact with a foraminous surface to form a web which is subsequently pressed, dried and creped by being passed over a Yankee cylinder, and wherein the web incorporates fibers produced by said dry defibration step which remain incompletely wetted during forming, pressing and drying of the web by reason of their having a short contact time with water which is less than 45 minutes, the amount of said incompletely wetted fibers being between 10% and 80% of the total fibers used to form the web.

Claim 5

A process for the manufacture of a high bulk paper or a high bulk layer of a multi-layered paper said paper or layer being creped, which process comprises the steps of: (a) forming an aqueous slurry consisting essentially of ligno-cellulosic fibers in a papermaking bond forming state, (b) subjecting dry pulp consisting essentially of ligno-cellulosic pulp to dry defibration and introducing the dry fibers so produced into said slurry and mixing these with the bond forming state fibers, said dry fibers consisting essentially of the type which when fully wetted have interfiber bond forming capacity; and shortly thereafter, (c) dewatering the slurry of mixed fibers in contact with a foraminous surface to form a web which is subsequently pressed, dried and creped by being passed over a Yankee cylinder, and wherein the web incorporates fibers produced by said dry defibration step which remain incompletely wetted during forming, pressing and drying of the web by reason of their having a short contact time with water which is less than 45 minutes, the amount of said incompletely wetted fibers being between 10% and 80% of the total fibers used to form the web.

Claim 6

A process according to claim 1 or claim 3 wherein said dry fibers are mixed with water shortly prior to being introduced into the slurry.

Claim 7

A process according to any of claims 1, 2 or 3, wherein said short contact time is less than 30 minutes.

Claim 8

A process according to any of claims 1, 2 or 3, wherein said short contact time is less than 10 minutes.

Claim 9

A process according to any of claims 1, 2 or 3 wherein the dry fibers are introduced into the slurry of bond forming state fibers in the vicinity of the head box of a papermaking machine.

Claim 10

A process according to any of claims 1, 2 or 3 wherein the dry fibers are introduced into the slurry of bond forming state fibers in the vicinity of the suction inlet of the fan pump of a papermaking machine.

Claim 11

A process according to any of claims 1, 2 or 3, wherein the amount of dry fibers entering the process is between 25% and 50% of the total fibers used for forming the web.

Claim 12

A process according to any of claims 1, 2 or 3, wherein the web incorporates fibers which are initially dry fibers and retain a solids content of at least 50% while the web is formed and pressed.

Claim 13

A process according to any of claims 1, 2 or 3, wherein the web incorporates fibers which are initially dry fibers and retain a solids content of at least 70% while the web is formed and pressed.

Claim 14

A process according to any of claims 1, 2 or 3, wherein the web incorporates fibers which are initially dry fibers and retain a solids content of at least 25% greater than the solids content of the bond forming state fibers while the web is formed and pressed.

Claim 15

A process according to any of claims 1, 2 or 3, wherein after the web is formed the major amount of water is removed by pressing.

Claim 16

A process according to any of claims 2, 3, or 4, wherein the dry fibers are subjected to mechanical defibration before introduction into the slurry.

Claim 17

A process according to any of claims 1, 2, 3 or 4, wherein said ligno-cellulosic bond forming state fibers have a solids content of less than 45%.