Claims
- 1. A process for the bleaching of a cellulosic pulp to a target brightness of at least about G. E. 75 and a viscosity of at least about 14 cP comprising:
- a first stage which includes contacting said pulp at a consistency of between about 2% and about 15% and a pH of between about 1.5 and about 3 with a chlorination agent including at least about 50% chlorine dioxide and a chlorination factor of between about 0.1 and about 0.25 and, thereafter, without an intervening treatment other than an optional water wash,
- a second stage subsequent to the first stage which includes contacting said pulp at a pH of about 5 or lower and a consistency of between about 1% and about 30% with ozone and, thereafter, without an intervening treatment other than an optional water wash,
- a third stage subsequent to the second stage which includes contacting said pulp with chlorine dioxide at a pH at the end of the stage of from about 2.5 to about 3.5, wherein the effluent from said bleaching process contains less colored matter and exhibits a lower COD than the effluent from a pulp bleaching process wherein there is employed an alkali extraction between either of said first or second stages.
- 2. The bleaching process of claim 1 further comprising adding in said third stage sufficient alkali to cause the pH of the pulp to be about 3 at the completion of said third stage.
- 3. The bleaching process of claim 1 wherein said first stage comprises a D or D.fwdarw.C.sub.D stage, said third stage comprises a D or D.fwdarw.C.sub.D stage, and including a fourth stage selected from the group consisting of an E stage followed by a D stage, a peroxide stage, a Z stage, a Z stage followed by a D stage, and a D stage followed by a further D stage.
- 4. The bleaching process of claim 1 in which the stages are carried out without a water wash between said first and second stages.
- 5. The method of claim 4 wherein the pH of the pulp during the initial 3 stage sequence is maintained in the range of from between about 2 and about 4.
- 6. The bleaching process of claim 1 in which the stages are carried out without a water wash between said second and third stages.
- 7. A method for reducing the quantity of colored matter in effluent from a pulp bleaching process which comprises an initial three stage sequence wherein the first and third bleach stages of said sequence are carried out at an acidic pH using a bleaching agent comprising chlorine dioxide and the intervening second stage is carried out at an acidic pH using a bleaching agent comprising ozone, there being no alkaline extraction between said first and second or said second and third stages and no interstage treatment of the pulp between the first and second stages or between said second and third stages other than an optional water wash.
- 8. The method of claim 7 further comprising a water wash of the pulp between the first and second stages.
- 9. The method of claim 7 further comprising a water wash of the pulp between the second and third stages.
- 10. The method of claim 7 further comprising an alkaline extraction stage after said third stage.
- 11. The method of claim 10 wherein the pH of said pulp is maintained below about 5 prior to the alkaline extraction stage.
Parent Case Info
This application is a continuation of application Ser. No. 07/958,576 filed Oct. 8, 1992 and now abandoned, which is a continuation of application Ser. No. 07/682,728 filed Apr. 8, 1991, now abandoned.
US Referenced Citations (5)
Non-Patent Literature Citations (3)
Entry |
Leibergott, N. and van Lierop, B.; "Oxidative Bleaching --A Review"; 69th Annual Meeting, Technical Section, Canadian Pulp and Paper Association; Preprints "A"; Feb. 1-2, 1983; pp. A169-183. |
Gierer, Josef; "The Chemistry of Delignification, a General Concept"; Holzforschung, 1982, pp. 43-51. |
Singh, Rudra P. (Edit); "The Bleaching Of Pulp, 3rd Edition, Revised"; 1979, TAPPI Press, Atlanta, GA; pp 382 & 383. |
Continuations (2)
|
Number |
Date |
Country |
Parent |
958576 |
Oct 1992 |
|
Parent |
682728 |
Apr 1991 |
|