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US4187141A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of producing bleached mechanical pulp

Assignee: Alf SA
•
Filing: 1978-06-19
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Granted: 1980-02-05
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Expires: 1998-06-19
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Abstract

Abstract Method of producing mechanical pulp of improved brightness and light-scattering properties in a defibration apparatus in which wood chips are ground between a pair of discs which rotate relative to one another in a pressurized grinding zone. Prior to the defibrating process, the chips are impregnated with a solution of alkali, selected from the group consisting of sodium hydroxide, alkali silicate, alkali carbonate and alkali bicarbonate, and peroxide, surplus impregnating solution is removed from the chips by compression of the chips, the chips are introduced into a pressure vessel which is in communication with the grinding zone and compressed air is introduced into the pressure vessel in an amount sufficient to maintain the chips in the pressure vessel at a temperature below 90° C. and to maintain superatmospheric pressure within the defibrating zone.

Inventors

  • 👤 Bo Ahrel

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 05:11
CPC Classifications
D; D21; D21B; D21B1/00; D21B1/04; D21B1/12; D21B1/14; D21B1/16

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 236 words
In the method of producing wood pulp in a defibrating apparatus in which wood chips, impregnated with an aqueous solution of a peroxide-containing bleaching composition and compressed to a predetermined dry content with consequent removal of bleaching solution, are introduced into a pressure vessel under superatmospheric pressure and then ground between a pair of discs which rotate relative to one another in a pressure sealed defibrating zone connected to said pressure vessel, the improvement. for minimizing the consumption of peroxide, comprising: (a) impregnating the wood chips with an aqueous solution of alkali, selected from the group consisting of sodium hydroxide, alkali silicate, alkali carbonate and alkali bicarbonate, and peroxide at a temperature ranging between 50° C. and 80° C. and for a correlated period of time ranging between 10 minutes and 2 hours to ensure presence of peroxide in the wood chips upon introduction thereof into the pressure vessel; (b) dewatering the thus impregnated wood chips by mechanical compression to a dry content between 35% and 50%; (c) introducing the thus impregnated and dewatered wood chips into said pressure vessel; and (d) introducing compressed air into said pressure vessel in an amount sufficient to maintain the impregnated and dewatered wood chips at a temperature below 90° C. and the pressure vessel at superatmospheric pressure while said impregnated and dewatered wood chips are being passed into said defibrating zone to ensure retention of peroxide during the defibration.
Claim 2
Dependent Claim 236 words
In the method of producing wood pulp in a defibrating apparatus in which wood chips, impregnated with an aqueous solution of a peroxide-containing bleaching composition and compressed to a predetermined dry content with consequent removal of bleaching solution, are introduced into a pressure vessel under superatmospheric pressure and then ground between a pair of discs which rotate relative to one another in a pressure sealed defibrating zone connected to said pressure vessel, the improvement. for minimizing the consumption of peroxide, comprising: (a) impregnating the wood chips with an aqueous solution of alkali, selected from the group consisting of sodium hydroxide, alkali silicate, alkali carbonate and alkali bicarbonate, and peroxide at a temperature ranging between 50° C. and 80° C. and for a correlated period of time ranging between 10 minutes and 2 hours to ensure presence of peroxide in the wood chips upon introduction thereof into the pressure vessel; (b) dewatering the thus impregnated wood chips by mechanical compression to a dry content between 35% and 50%; (c) introducing the thus impregnated and dewatered wood chips into said pressure vessel; and (d) introducing compressed air into said pressure vessel in an amount sufficient to maintain the impregnated and dewatered wood chips at a temperature below 90° C. and the pressure vessel at superatmospheric pressure while said impregnated and dewatered wood chips are being passed into said defibrating zone to ensure retention of peroxide during the defibration.
Claim 3
Dependent Claim 33 words
Method according to claim 1, in which the wood chips, after the dewatering step and before the defibrating step, are reacted with an acid sulphite or sulphur dioxide to neutralize said wood chips.
Claim 4
Dependent Claim 23 words
Method according to claim 2, in which the reaction with the acid sulphite or sulphur dioxide is carried out in the pressure vessel.

References Cited (Backward Citations)

US1987195A Cited
GB838893A Cited
US2958622A Cited
US3558428A Cited
US3652385A Cited
US3808090A Cited
US3811993A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-02-04 1983-08-06 1984-02-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-02-04 1987-08-06 1988-02-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-02-04 1991-08-06 1992-02-05 $7700.00 Window Closed / Lapsed

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