Delignification and bleaching of wood pulp with oxygen

Claim 2

In a continuous method of bleaching and delignifying cellulose pulp comprising the steps of preparing a cellulose pulp slurry in an oxygenated alkaline aqueous solution, said slurry having a reaction temperature of between about 160°F. and its boiling point, a consistency of from about 2% to about 10% by weight, and having a pH of between about 9 and 14, said alkaline aqueous solution being oxygenated by dissolving and intimately dispersing oxygen into said alkaline aqueous solution so that no agglomerated bubbles are formed, continuously introducing said slurry into a vessel, subjecting the slurry to an initial pressure and thereafter gradually reducing that pressure, without subjecting the slurry to any substantial agitation, so that there is a pressure gradient of between about 1 and 10 atmospheres between the initial pressure and final pressure, and continuously withdrawing treated slurry from said vessel, the improvement which comprises subjecting said pulp slurry and not more than about 2/3 of said oxygenated alkaline aqueous solution to a pre-treatment in a pressurizing vessel at a temperature of between about 160° and 300° F. and pressure of up to about 300 p.s.i.g. and mixing said pressurized slurry with the remainder of said oxygenated alkaline aqueous solution.

Claim 3

In a continuous method of bleaching and delignifying cellulose pulp comprising the steps of preparing a cellulose pulp slurry in an oxygenated alkaline aqueous solution, said slurry having a reaction temperature of between about 160°F. and its boiling point, a consistency of from about 2% to about 10% by weight, and having a pH of between about 9 and 14, said alkaline aqueous solution being oxygenated by dissolving and intimately mixing oxygen into said alkaline aqueous solution so that no agglomerated bubbles are formed, continuously introducing said slurry into the lower region of a vertically elongated tower, flowing said slurry upwardly through said tower without any substantial agitation, while maintaining a pressure gradient of between 1 and 10 atmospheres between the point of introduction of said slurry into said tower and the point of withdrawal of said slurry from said tower, and continuously withdrawing treated slurry from the upper region of said tower, the improvement which comprises subjecting said pulp slurry and not more than about 2/3 of said oxygenated alkaline aqueous solution to a pre-treatment in a pressurizing vessel at a temperature of between about 160° and 300°F. and pressure of up to about 300 p.s.i.g. and mixing said pressurized slurry with the remainder of said oxygenated alkaline aqueous solution.

Claim 4

In a continuous method of bleaching and delignifying cellulose pulp comprising the steps of preparing a cellulose pulp slurry in an oxygenated alkaline aqueous solution, said slurry having a reaction temperature of between about 160°F. and its boiling point, a consistency of from about 2% to about 10% by weight, and having a pH of between about 9 and 14, said alkaline aqueous solution being oxygenated by dissolving and intimately mixing oxygen into said alkaline aqueous solution so that no agglomerated bubbles are formed, continuously introducing said slurry into the lower region of a vertically elongated tower, flowing said slurry upwardly through said tower without any substantial agitation, while maintaining a pressure gradient of between 1 and 10 atmospheres between the point of introduction of said slurry into said tower and the point of withdrawal of said slurry from said tower, and continuously withdrawing treated slurry from the upper region of said tower, the improvement which comprises subjecting said pulp slurry and not more than about 2/3 of said oxygenated alkaline aqueous solution to a pre-treatment in a pressurizing vessel at a temperature of between about 160° and 300°F. and pressure of up to about 300 p.s.i.g. and mixing said pressurized slurry with the remainder of said oxygenated alkaline aqueous solution.

Claim 5

A continuous method in accordance with claim 1, wherein at least about 2/3 of said alkaline aqueous solution is subjected to said pre-treatment.

Claim 6

A continuous method in accordance with claim 2, wherein at least about 1/3 of said alkaline aqueous solution is subjected to said pre-treatment.

Claim 7

A continuous process according to claim 1, wherein the consistency of pulp slurry subjected to said pre-treatment shall be between about 3 and 11%.

Claim 8

A continuous method in accordance with claim 1, wherein the consistency of the pulp slurry is between about 2 and 6% by weight.

Claim 9

A continuous method in accordance with claim 1, wherein the amount of oxygen introduced is between about 0.1 and 4% by weight of the pulp slurry.

Claim 10

A continuous method in accordance with claim 1, wherein the temperature in said treatment vessel subsequent to said pre-treatment is between about 195° and 212°F.

Claim 11

A continuous method in accordance with claim 2, wherein the tower is not higher than about 300 feet and the oxygenated slurry is introduced near the bottom of said tower.

Claim 12

A continuous method in accordance with claim 2, wherein the residence time of the slurry in said tower is between about 2 and 120 minutes.

Claim 13

A continuous method in accordance with claim 1, wherein the amount of oxygen introduced is between about 0.2 and 0.4% by weight of the pulp slurry.

Claim 14

A continuous method in accordance with claim 1, wherein the temperature during said pre-treatment is between about 16° and 300°F.

Claim 15

A continuous method in accordance with claim 1, wherein the pressure during said pre-treatment is between about 2 and 10 atmospheres.