Rewetting of paper products during drying

Claim 3

The method of claim 1 wherein the web is rewet at least twice in succession during the initial drying stage.

Claim 4

The method of claim 1 wherein the web is rewet three or more times in succession during the initial drying stage.

Claim 5

The method of claim 3 wherein the web is rewet in succession when the web has a solids content (i) in the range of from about 45 to about 60 wt. %, (ii) in the range of from about 60 to about 63 wt. %, (iii) in the range of from about 65 to about 68 wt. %, (iv) in the range of from about 70 to about 75 wt. % and (v) in the range of from about 80 to about 85 wt. %.

Claim 6

The method of claim 3 wherein the web is dried in an impulse dryer.

Claim 7

The method of claim 3 wherein the web is dried on a dryer with steam filled cylinders.

Claim 8

In a method for drying an elongate paper or paperboard web on a papermaking machine, the method for increasing the drying rate and reducing the shrinkage rate of the web without substantially adversely affecting physical properties of the web, the method comprising drying the web emerging from the press section of the papermaking machine as it traverses a dryer section to a temperature in the range of from about 100° to about 150° C., and during the drying, rewetting the web with an amount of water substantially uniformly across the width of the web during an initial web drying stage when the web has a solids content in the range of from about 60 to about 85 wt. % wherein the amount of water added to the web ranges from about 0.5 wt. % to about 10 wt. % based on the total weight of the web including liquid and solids, at each web rewet step.

Claim 9

In a method for drying an elongate paper or paperboard web on a papermaking machine, the method for increasing the drying rate and reducing the shrinkage rate of the web without substantially adversely affecting physical properties of the web, the method comprising drying the web emerging from the press section of the papermaking machine as it traverses a dryer section to a temperature in the range of from about 100° to about 150° C., and during the drying, rewetting the web with an amount of water substantially uniformly across the width of the web during an initial web drying stage when the web has a solids content in the range of from about 60 to about 85 wt. % wherein the amount of water added to the web ranges from about 0.5 wt. % to about 10 wt. % based on the total weight of the web including liquid and solids, at each web rewet step.

Claim 10

The method of claim 7 wherein the web is rewet successively at least twice during said drying.

Claim 11

The method of claim 7 wherein the web is rewet three or more successive times during said drying.

Claim 12

The method of claim 9 wherein web is rewet in succession when the web has a solids content (i) in the range of from about 45 to about 60 wt. %, (ii) in the range of from about 60 to about 63 wt. %, (iii) in the range of from about 65 to about 68 wt. %, (iv) in the range of from about 70 to about 75 wt. % and (v) in the range of from about 80 to about 85 wt. %.

Claim 13

The method of claim 9 wherein the web is dried in an impulse dryer.

Claim 14

The method of claim 9 wherein the web is dried on a dryer with steam filled cylinders.

Claim 15

An improved paper or paperboard making process comprising: depositing an aqueous slurry of paper or paperboard fibers at a consistency of from about 15 to about 20 wt. % on a web former screen thereby forming a relatively thin layer of the slurry on the screen; dewatering the slurry on the screen thereby forming a fibrous web; wet pressing the web with one or more wet press nips to a solids content in the range of from about 45 to about 50% by weight; drying the web on one or more heated cylinders of a drying unit; and rewetting the web during the drying step with an amount of water substantially uniformly throughout the width of the web during an initial web drying stage before the web is dried to a solids content of greater than about 85 wt. %, whereby the paper or paperboard thus formed has a shrinkage rate of less than 5% and wherein the amount of water added to the web ranges from about 0.5 wt. % to about 10 wt. % based on the total weight of the web including liquid and solids, at each web rewet step.

Claim 16

An improved paper or paperboard making process comprising: depositing an aqueous slurry of paper or paperboard fibers at a consistency of from about 15 to about 20 wt. % on a web former screen thereby forming a relatively thin layer of the slurry on the screen; dewatering the slurry on the screen thereby forming a fibrous web; wet pressing the web with one or more wet press nips to a solids content in the range of from about 45 to about 50% by weight; drying the web on one or more heated cylinders of a drying unit; and rewetting the web during the drying step with an amount of water substantially uniformly throughout the width of the web during an initial web drying stage before the web is dried to a solids content of greater than about 85 wt. %, whereby the paper or paperboard thus formed has a shrinkage rate of less than 5% and wherein the amount of water added to the web ranges from about 0.5 wt. % to about 10 wt. % based on the total weight of the web including liquid and solids, at each web rewet step.

Claim 17

The process of claim 13 wherein the web is rewet in succession at least twice during the said drying.

Claim 18

The process of claim 13 wherein the web is dried on at least four steam-heated drying cylinders and wherein the web is rewet in succession at least three times during said drying.

Claim 19

The process of claim 15 wherein the web is rewet in succession when the web has a solids content (i) in the range of from about 45 to about 60 wt. %, (ii) in the range of from about 60 to about 63 wt. %, (iii) in the range of from about 65 to about 68 wt. %, (iv) in the range of from about 70 to about 75 wt. % and (v) in the range of from about 80 to about 85 wt. %.

Claim 20

The process of claim 13 wherein a plurality of aqueous slurries of paper or paperboard fibers are deposited on the web forming screen thereby forming a multiply board.