Pulping of lignocellulosic material by sequential treatment thereof with nitric oxide and oxygen

Claim 2

A process of preparing high strength pulp from particles of lignocellulosic material having a capillary structure which comprises treating said material with 2 to 8% nitric oxide, based on the dry weight of said material, and then reacting said nitric oxide treated material with molecular oxygen to form nitric acid in situ, said reaction being carried out at a temperature below 40° C for a time sufficient to substantially effect consumption of nitric acid and at a moisture content of 10 to 80% of the lignocellulosic material, the nitric oxide being added sufficiently prior to the oxygen to effect substantially thorough penetration of the material with the nitric oxide before reaction occurs with the oxygen, washing the nitric acid treated material with an alkaline solution and delignifying the washed material by extracting the washed material with a strong alkali at a temperature above about 140° C resulting in a cellulosic pulp.

Claim 3

The process of claim 1 wherein the alkaline solution used to wash the material is black liquor which neutralizes acid and initiates dissolving of the freed lignin, and the extraction with the strong alkali is at a temperature of about 140° to 180° C.

Claim 4

The process of claim 1 wherein after extraction with the strong alkali the cellulosic pulp has liquid expressed therefrom to bring the consistency of the pulp to at least about 35% and is then treated with nitric acid at a temperature of below about 40° C, with the amount of nitric acid being about 1 to 5 percent by weight of said pulp expressed as nitric oxide, washed with an alkaline solution and then extracted with a strong alkali at a temperature below about 130° C.

Claim 5

The process of claim 1 wherein the cellulosic pulp is bleached with oxygen in an alkaline medium.

Claim 6

The process of claim 4 wherein the oxygen bleaching is followed by treatment of said cellulosic pulp with chlorine.

Claim 7

The process of claim 5 wherein the amount of chlorine is about 1 to 2% by weight of the pulped material on the dry basis thereof.

Claim 8

The process of preparing high strength pulp from particles of lignocellulosic material having a capillary structure which comprises treating the material at a moisture content of at least about 10% and below about 80% based on the dry weight of the material, with nitric oxide and oxygen gas which react with moisture present in the material to form nitric acid in situ, the nitric oxide being added prior to the oxygen to effect substantially thorough penetration of the material with the nitric oxide before reaction occurs with the oxygen, the amount of nitric oxide being about 2 to 8 percent based on the dry weight of said material, the amount of oxygen being at least sufficient to convert substantially all nitric oxide to nitrogen dioxide, controlling the rate of addition of the oxygen to the material to preclude excessive rise in temperature above about 50° C and thereby preclude excessive degradation of cellulosic fibers in the material, washing the nitric acid treated material substantially free of acid, and delignifying the washed material by removing freed lignin therefrom by extracting said washed material with a strong alkali at a temperature above about 140° C resulting in a cellulosic pulp.

Claim 9

The process of preparing high strength pulp from particles of lignocellulosic material having a capillary structure which comprises treating the material at a moisture content of at least about 10% and below about 80% based on the dry weight of the material, with nitric oxide and oxygen gas which react with moisture present in the material to form nitric acid in situ, the nitric oxide being added prior to the oxygen to effect substantially thorough penetration of the material with the nitric oxide before reaction occurs with the oxygen, the amount of nitric oxide being about 2 to 8 percent based on the dry weight of said material, the amount of oxygen being at least sufficient to convert substantially all nitric oxide to nitrogen dioxide, controlling the rate of addition of the oxygen to the material to preclude excessive rise in temperature above about 50° C and thereby preclude excessive degradation of cellulosic fibers in the material, washing the nitric acid treated material substantially free of acid, and delignifying the washed material by removing freed lignin therefrom by extracting said washed material with a strong alkali at a temperature above about 140° C resulting in a cellulosic pulp.

Claim 10

The process of claim 7 wherein the nitric oxide is added to the material under vacuum or pressure to enhance penetration of the nitric oxide into the material, and the alkali extraction is performed at a temperature of about 140° to 180° C.

Claim 11

The process of claim 7 wherein the washing of the nitric acid treated material substantially free of acid is performed with black liquor to neutralize acidic components and to initiate dissolving of the freed lignin, and the cellulosic pulp resulting from extraction with strong alkali at about 140° C has liquid expressed therefrom to bring the consistency of the pulp to at least about 35% and is then treated with nitric acid at a temperature of below about 40° C, with the amount of nitric acid being about 1 to 5 percent by weight of said pulp expressed as nitric oxide, washed with an alkaline solution and then extracted with a strong alkali at a temperature below about 130° C.