Chlorine free process for bleaching lignocellulosic pulp

Claim 2

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 20° to 90° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp, said peroxide being selected from the group consisting of alkaline hydrogen peroxide, acid hydrogen peroxide, and peracid; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp.

Claim 3

The process of claim 1 wherein each intermediate of said ozone stages is followed, subsequent to said washing, by a caustic extraction stage carried out with a caustic extraction solution followed in sequence by separating the caustic extraction solution from and washing the pulp at about 1% pulp consistency to afford final removal of the caustic extraction solution.

Claim 4

The process of claim 2 wherein the wash for said washing of the pulp following each of said stages is selected from the group consisting of the effluent from the next later stage, the effluent from the washing of said pulp following said next later stage, make-up water, effluent from a recovery process and any combination of same.

Claim 5

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp.

Claim 6

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp.

Claim 7

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp; each intermediate of said ozone stages being followed, subsequent to said washing, by a caustic extraction stage carried out with a caustic extraction solution followed in sequence by separating the caustic extraction solution from and washing the pulp at about 1% pulp consistency to afford final removal of the caustic extraction solution.

Claim 8

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp; each intermediate of said ozone stages being followed, subsequent to said washing, by a caustic extraction stage carried out with a caustic extraction solution followed in sequence by separating the caustic extraction solution from and washing the pulp at about 1% pulp consistency to afford final removal of the caustic extraction solution.

Claim 9

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp; each intermediate of said ozone stages being followed, subsequent to said washing, by a caustic extraction stage carried out with a caustic extraction solution followed in sequence by separating the caustic extraction solution from and washing the pulp at about 1% pulp consistency to afford final removal of the caustic extraction solution; the wash for said washing of the pulp following each of said stages is selected from the group consisting of the effluent from the next later stage, the effluent from the washing of said pulp following said next later stage, make-up water, effluent from a recovery process and any combination of same.

Claim 10

A non-chlorine multi-stage process for bleaching chemical lignocellulosic pulp which minimizes changes in temperature and pH from stage to stage, said process comprising in sequence: (a) an oxygen bleaching stage carried out at about 3% to 30% pulp consistency, at 80° to 120° C. and at a pH of 9 to 12 for a reaction time of 10 to 60 minutes with an oxygen treatment solution comprising 0.2% to about 3% oxygen, based on oven-dried pulp, followed in sequence by separating the oxygen treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the oxygen treatment solution from the pulp; then (b) a peroxide bleaching stage carried out at 10% to 25% pulp consistency, at 40° to 80° C. and at a pH of 3 to 5 for a reaction time of 10 to 300 minutes, with a peroxide treatment solution comprising 0.2% to about 2% acid hydrogen peroxide, based on oven-dried pulp, followed in sequence by separating the peroxide treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the peroxide treatment solution from the pulp; and then (c) at least one ozone bleaching stage carried out at 1% to 40% pulp consistency, at 15° to 60° C. and at a pH of 2 to 7, with an ozone treatment solution until 0.2% to 1% ozone on an oven-dried pulp basis is consumed, each said ozone bleaching stage being followed by separating the ozone treatment solution from and washing the pulp at about 1% pulp consistency to afford final removal of the ozone treatment solution from the pulp; each intermediate of said ozone stages being followed, subsequent to said washing, by a caustic extraction stage carried out with a caustic extraction solution followed in sequence by separating the caustic extraction solution from and washing the pulp at about 1% pulp consistency to afford final removal of the caustic extraction solution; the wash for said washing of the pulp following each of said stages is selected from the group consisting of the effluent from the next later stage, the effluent from the washing of said pulp following said next later stage, make-up water, effluent from a recovery process and any combination of same.