(19)
(11) EP 0 476 230 A3

(12) EUROPEAN PATENT APPLICATION

(88) Date of publication A3:
09.06.1993 Bulletin 1993/23

(43) Date of publication A2:
25.03.1992 Bulletin 1992/13

(21) Application number: 91108241.0

(22) Date of filing: 22.05.1991
(51) International Patent Classification (IPC)5D21C 3/02, D21C 7/00
(84) Designated Contracting States:
AT DE FR GB IT SE

(30) Priority: 17.09.1990 US 583043

(71) Applicant: Kamyr, Inc.
Glens Falls, New York 12801-3686 (US)

(72) Inventors:
  • Stromberg, Bertil Kamyr Inc.
    New York 12801-3686 (US)
  • Jiang, Jian Kamyr Inc.
    New York 12801-3686 (US)
  • Laakso, Richard Kamyr, Inc.
    New York 12801-3686 (US)
  • Phillips, Joseph Kamyr Center
    New York 12801-3686 (US)
  • Greenwood, Brian Kamyr Center
    New York 12801-3686 (US)
  • Prough, James Kamyr Inc.
    New York 12801-3686 (US)

(74) Representative: UEXKÜLL & STOLBERG 
Patentanwälte Beselerstrasse 4
22607 Hamburg
22607 Hamburg (DE)


(56) References cited: : 
   
       


    (54) Extended kraft cooking with white liquor added to wash circulation


    (57) In the continuous kraft pulping of comminuted cellulosic fibrous material (e.g. wood chips) to produce paper pulp, viscosity for a given Kappa Number is significantly increased (e.g. at least about 20%) by adding kraft white liquor to the wash recirculation loop (38-40) in a continuous digester (19). Optimum results are obtained when kraft white liquor is also added to a recirculation loop (28-30) at a central portion of the digester, so that the majority of the digester has countercurrent flow between white liquor and cellulosic material. About 5-20% of the total white liquor necessary to effect kraft cooking is introduced in the wash circulation, and about 10-20% is introduced into the central portion recirculation. The temperature in the wash zone is maintained at about 140-175°C.







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