Process for recovery of chemicals from pulping waste liquor

Claim 2

A process for recovery of chemicals from sodium sulfite pulping waste liquor comprising the steps of: (1) introducing and incompletely dissolving a smelt, obtained by burning a concentrated waste liquor and containing mainly sodium sulfide and sodium carbonate, in a large body of aqueous slurry, which comprises a solid phase the main component of which is sodium carbonate and a liquid phase the main component of which is aqueous sodium sulfide, adding to said body make up water and a weak aqueous slurry recycled from step (2), and supplying a portion of the resulting aqueous slurry to step (2), maintaining the total solid content of said body of aqueous slurry at from about 35 to about 70% by weight, the proportion of sodium carbonate in the total solid material at lower than that of the smelt, and the temperature at from about 55° to about 90° C. (2) separating the slurry supplied from step (1) into (a) a wet cake containing water in a proportion of from about 10 to about 50% by weight and (b) a weak aqueous slurry, recycling said weak slurry (b) to step (1), and supplying said wet cake (a) to step (3), and (3) mixing a feed consisting of said wet cake (a) and sufficient additional solid material to adjust the total molar ratio of S/Na 2 O of said feed to that of said smelt with hot particles containing sodium sulfite and sodium carbonate while supplying simultaneously a molecular oxygen-containing gas to effect oxidation of sodium sulfide present in said feed into sodium sulfite, wherein said additional solid material is obtained by contacting at least one of a portion of said slurry supplied to step (2) and a portion of said weak aqueous slurry (b) obtained in step (2) with a cooled surface to obtain said solid material.

Claim 3

A process for recovery of chemicals according to claim 1, wherein in the step (1) said body of aqueous slurry is circulated between a smelt receiving means and a smelt dissolving means, and said smelt is introduced into said aqueous slurry in said smelt receiving means.

Claim 4

A process for recovery of chemicals according to claim 2, wherein the amount of the circulating slurry is from 20 to 200 times by weight that of the smelt introduced in the receiving means.

Claim 5

A process for recovery of chemicals according to claim 2, wherein said weak aqueous slurry recycled from step (2), and said make up water are added to said body in said smelt dissolving means.

Claim 6

A process for recovery of chemicals according to claim 20, wherein said smelt is impinged with an air or steam stream to effect cooling and dividing out into particles.

Claim 7

A process for recovery of chemicals according to claim 2, wherein said smelt receiving means comprises a smelt hopper and a screening means, and wherein lumps remaining after said smelt is introduced into said smelt hopper through which is circulating said body of aqueous slurry are separated from smaller solidified smelt particles by said screening means and said separated lumps are separately dissolved in make up water to form a weak green liquor.

Claim 8

A process for recovery of chemicals according to claim 1, wherein said make up water is a weak green liquor.

Claim 9

A process for recovery of chemicals according to claim 1, wherein said make up water is wash water recovered from a means for washing an exhaust gas from the smelt receiving means.

Claim 10

A process for recovery of chemicals according to claim 1, wherein said aqueous slurry is cooled by means of cooling water having a temperature by 5° to 40° C. lower than that of the slurry.

Claim 11

A process for recovery of chemicals according to claim 1, wherein the amount of said molecular oxygen-containing gas to be supplied to the oxidation reaction is from 2 to 20 times that required to completely oxidize the sodium sulfide present in the smelt into sodium sulfite.

Claim 12

A process for recovery of chemicals according to claim 1, wherein the temperature of said molecular oxygen-containing gas to be supplied to the oxidation reaction is from 100° to 200° C.

Claim 13

A process for recovery of chemicals according to claim 1, wherein the temperature of the reaction mixture to be oxidized is from 100° to 300° C.

Claim 14

A process for recovery of chemicals according to claim 1, wherein sodium hydroxide is added to the reaction mixture to be oxidized.

Claim 15

A process for recovery of chemicals according to claim 1, wherein at least one of a part of said aqueous slurry and a part of said weak aqueous slurry are supplied to the reaction mixture to be oxidized.

Claim 16

A process for recovery of chemicals according to claim 1, wherein said oxidation reaction is effected in two stages, the first stage being mixing said wet cake with said hot particles while supplying said molecular oxygen-containing gas to form an oxidized product in the form of particles, and a second stage being contact of said oxidized product particles and a molecular oxygen-containing gas within a confined space.

Claim 17

A process for recovery of chemicals according to claim 1, wherein at least one of said smelt, and said aqueous slurry formed in step (1) are contacted with a molecular oxygen-containing gas to effect preliminary oxidation of the sodium sulfide.

Claim 18

A process for recovery of chemicals from sodium sulfite pulping waste liquor comprising the steps of: (1) introducing and incompletely dissolving a smelt, obtained by burning a concentrated waste liquor and containing mainly sodium sulfide and sodium carbonate, in a large body of aqueous slurry, which comprises a solid phase the main component of which is sodium carbonate and a liquid phase the main component of which is aqueous sodium sulfide, adding to said body make up water and a weak aqueous slurry recycled from step (2), and supplying a portion of the resulting aqueous slurry to step (2), maintaining the total solid content of said body of aqueous slurry at from about 35 to about 70% by weight, the proportion of sodium carbonate in the total solid material at lower than that of the smelt, and the temperature at from about 55° to about 90° C. (2) separating the slurry supplied from step (1) into (a) a wet cake containing water in a proportion of from about 10 to about 50% by weight and (b) a weak aqueous slurry, recycling said weak slurry (b) to step (1), and supplying said wet cake (a) to step (3), and (3) mixing a feed consisting of said wet cake (a) and sufficient additional solid material to adjust the total molar ratio of S/Na 2 O of said feed to that of said smelt with hot particles containing sodium sulfite and sodium carbonate while supplying simultaneously a molecular oxygen-containing gas to effect oxidation of sodium sulfide present in said feed into sodium sulfite to obtain a product mixture of sodium sulfite and sodium carbonate, wherein said additional solid material is obtained by contacting at least one of a portion of said slurry supplied to step (2) and a portion of said weak aqueous slurry (b) obtained in step (2) with a cooled surface to obtain said solid material, (4) dissolving the product mixture in water, separating insoluble material from the resulting aqueous solution to obtain a clarified aqueous solution, contacting the clarified solution with a sulfur dioxide-containing gas to effect conversion of sodium carbonate present into sodium sulfite and separating insoluble material from the final aqueous solution, and (5) combining both insoluble materials, washing with water and recycling the wash water to step (1) for dissolving the smelt and/or step (4) for dissolving the oxidation product.

Claim 19

A process for recovery of chemicals from sodium sulfite pulping waste liquor comprising the steps of: (1) introducing and incompletely dissolving a smelt, obtained by burning a concentrated waste liquor and containing mainly sodium sulfide and sodium carbonate, in a large body of aqueous slurry, which comprises a solid phase the main component of which is sodium carbonate and a liquid phase the main component of which is aqueous sodium sulfide, adding to said body make up water and a weak aqueous slurry recycled from step (2), and supplying a portion of the resulting aqueous slurry to step (2), maintaining the total solid content of said body of aqueous slurry at from about 35 to about 70% by weight, the proportion of sodium carbonate in the total solid material at lower than that of the smelt, and the temperature at from about 55° to about 90° C. (2) separating the slurry supplied from step (1) into (a) a wet cake containing water in a proportion of from about 10 to about 50% by weight and (b) a weak aqueous slurry, recycling said weak slurry (b) to step (1), and supplying said wet cake (a) to step (3), and (3) mixing a feed consisting of said wet cake (a) and sufficient additional solid material to adjust the total molar ratio of S/Na 2 O of said feed to that of said smelt with hot particles containing sodium sulfite and sodium carbonate while supplying simultaneously a molecular oxygen-containing gas to effect oxidation of sodium sulfide present in said feed into sodium sulfite to obtain a product mixture of sodium sulfite and sodium carbonate, wherein said additional solid material is obtained by contacting at least one of a portion of said slurry supplied to step (2) and a portion of said weak aqueous slurry (b) obtained in step (2) with a cooled surface to obtain said solid material, (4) dissolving the product mixture in water, separating insoluble material from the resulting aqueous solution to obtain a clarified aqueous solution, contacting the clarified solution with a sulfur dioxide-containing gas to effect conversion of sodium carbonate present into sodium sulfite and separating insoluble material from the final aqueous solution, and (5) combining both insoluble materials, washing with water and recycling the wash water to step (1) for dissolving the smelt and/or step (4) for dissolving the oxidation product.