GB1106841A - Process for the production of bleached pulp - Google Patents

Process for the production of bleached pulp

Info

Publication number
GB1106841A
GB1106841A GB3130/65A GB313065A GB1106841A GB 1106841 A GB1106841 A GB 1106841A GB 3130/65 A GB3130/65 A GB 3130/65A GB 313065 A GB313065 A GB 313065A GB 1106841 A GB1106841 A GB 1106841A
Authority
GB
United Kingdom
Prior art keywords
washer
passed
liquor
pulp
mud
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
GB3130/65A
Inventor
William Howard Rapson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Electric Reduction Company of Canada Ltd
Original Assignee
Electric Reduction Company of Canada Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Electric Reduction Company of Canada Ltd filed Critical Electric Reduction Company of Canada Ltd
Priority to GB3130/65A priority Critical patent/GB1106841A/en
Priority to DE1692848A priority patent/DE1692848C3/en
Priority to FI660161A priority patent/FI43947C/en
Priority to NO161391A priority patent/NO120251B/no
Priority to ES0322174A priority patent/ES322174A1/en
Priority to FR46964A priority patent/FR1465228A/en
Priority to CS44666*BA priority patent/CS157014B2/cs
Priority to SE885/66A priority patent/SE315192B/xx
Priority to US522459A priority patent/US3453174A/en
Priority to AT69166A priority patent/AT265005B/en
Publication of GB1106841A publication Critical patent/GB1106841A/en
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00Regeneration of pulp liquors or effluent waste waters
    • D21C11/12Combustion of pulp liquors
    • D21C11/122Treatment, e.g. dissolution, of the smelt
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/40Production or processing of lime, e.g. limestone regeneration of lime in pulp and sugar mills
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S162/00Paper making and fiber liberation
    • Y10S162/08Chlorine-containing liquid regeneration

Abstract

1,106,841. Bleaching pulp; treating cellulosic pulp. ELECTRIC REDUCTION CO. OF CANADA Ltd. 24 Jan, 1966 [25 Jan., 1965], No: 3130/65. Heading DIP and D2W. Bleached pulp is produced by heating in a digestion stage a fibrous cellulosic material in an aqueous solution containing sodium hydroxide or sodium sulphide or both, separating the fibrous pulp from the solution, sending the solution to a recovery stage which includes evaporating the solution, burning the concentrated solution to form a smelt, dissolving the smelt in water and treating the solution so obtained to form a liquor for re-use in the digestion stage, and partially bleaching the pulp with an aqueous solution of chlorine or chlorine dioxide or both, extracting the partially bleached pulp in a caustic extraction step with a hot aqueous alkali solution and further bleaching it in at least one more bleaching step, e.g. with hypochlorite or chlorine dioxide, the effluent from the caustic extraction step being used at least partially as the agent for quenching and dissolution of the smelt from the furnacing of the solution at the recovery stage. In the drawing wood chips are digested in digestor 1 in a white liquor comprising an aqueous solution of sodium hydroxide and sodium sulphide and the pulp mixture is passed to separator 2 in which the pulp is separated from the black liquor which is then concentrated in evaporator 3, sodium sulphate is added to the concentrated black liquor and the liquor burnt in furnace 4, the smelt so obtained containing sodium carbonate and sodium sulphide being passed to smelt dissolver 5 where it is quenched with water and the green liquor so formed passed to clarifier 6 from which the dregs obtained are passed to dregs washer 7 and the clarified green liquor passed to causticiser 8 in which it is mixed with lime and the resulting liquor passed to white liquor clarifier 9 where the precipitated calcium carbonate is removed as a mud and passed to mud washer 10 and the white liquor passed via line 21 to digester 1. The pulp is washed with water in washer 11, bleached in the bleacher 12 with an aqueous solution containing Cl 2 , ClO 2 or both, washed in washer 13 where it is passed as a mat over a wire mesh on the periphery of rotating drum 14, mixed with steam and recycled white liquor which enters via line 20 from white liquor clarifier 9 in repulper 19, subjected to caustic extraction in tank 22, washed in washer 24 and passed via repulper 38 and washer 40 to further bleaching steps with chlorine dioxide. The effluent sucked from the washer 24 through line 27 passes to seal tank 28 from which it is pumped by pump 28a, a portion being recycled via lines 29 and 30 to the surface of the wash mat on drum 14 of washer 13, a portion passing through lines 31, 32 and 33 to the dregs washer 7 and through lines 31, 34 and 35 to mud washer 10 and a further portion if desired passing through lines 31, 34 and 36 to mud thickener 37. The water passing through line 33 to dregs washer 7 is subsequently passed through line 45 to mud washer 10 and the wash water passing through line 36 to mud thickener 37 is subsequently passed to mud washer 10 through line 46, the wash water leaving the mud washer 10 passing through line 47 to smelt dissolver 5 where it is used to quench and dissolve the smelt from the furnace 4. The thickened mud from 37 is passed to lime kiln 49 where it is calcined to regenerate lime which is returned through line 50 to causticiser 8 for causticisation of the green liquor.
GB3130/65A 1965-01-25 1965-01-25 Process for the production of bleached pulp Expired GB1106841A (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
GB3130/65A GB1106841A (en) 1965-01-25 1965-01-25 Process for the production of bleached pulp
DE1692848A DE1692848C3 (en) 1965-01-25 1966-01-18 Process for the manufacture of bleached pulp
FI660161A FI43947C (en) 1965-01-25 1966-01-21 Method for the production of bleached cellulose
NO161391A NO120251B (en) 1965-01-25 1966-01-24
ES0322174A ES322174A1 (en) 1965-01-25 1966-01-24 A procedure for the production of whitened wooden paste. (Machine-translation by Google Translate, not legally binding)
FR46964A FR1465228A (en) 1965-01-25 1966-01-24 Process for obtaining a bleached pulp from a fibrous cellulosic substance
CS44666*BA CS157014B2 (en) 1965-01-25 1966-01-24
SE885/66A SE315192B (en) 1965-01-25 1966-01-24
US522459A US3453174A (en) 1965-01-25 1966-01-24 Pulping and bleaching process wherein effluent liquor from alkaline extraction of bleached pulp is used to dissolve smelt
AT69166A AT265005B (en) 1965-01-25 1966-01-25 Process for the manufacture of bleached cellulose pulp

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB3130/65A GB1106841A (en) 1965-01-25 1965-01-25 Process for the production of bleached pulp
US52245966A 1966-01-24 1966-01-24

Publications (1)

Publication Number Publication Date
GB1106841A true GB1106841A (en) 1968-03-20

Family

ID=26238074

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3130/65A Expired GB1106841A (en) 1965-01-25 1965-01-25 Process for the production of bleached pulp

Country Status (4)

Country Link
US (1) US3453174A (en)
DE (1) DE1692848C3 (en)
FR (1) FR1465228A (en)
GB (1) GB1106841A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3617434A (en) * 1967-05-31 1971-11-02 Mitsubishi Heavy Ind Ltd Regeneration of cooking chemicals from spent alkaline cooking liquor
CA928007A (en) * 1969-12-30 1973-06-12 H. Rapson William Chemical recovery process
US4196043A (en) * 1970-12-21 1980-04-01 Scott Paper Company Kraft pulp bleaching and recovery process
FI53728C (en) * 1974-03-12 1978-07-10 Ahlstroem Oy FOERFARANDE FOER AOTERVINNING AV KEMIKALIER UR AVLUTAR FRAON SULFATCELLULOSAKOK OCH AVFALLSVATTEN FRAON BLEKNING
ZA761255B (en) * 1975-03-11 1977-03-30 Erco Envirotech Ltd Bleachplant operation
WO1996006978A1 (en) * 1994-08-31 1996-03-07 Hoffman Environmental Systems, Inc. Method of papermaking having zero liquid discharge
SE505249C2 (en) * 1994-11-04 1997-07-21 Kvaerner Pulping Tech Recovery of bleach filtrate by using the filtrate in a gas cooling system in a gasification plant
FI127442B (en) 2014-03-31 2018-06-15 Upm Kymmene Corp Method and system for reducing phosphorus in effluent or filtrate
US20220074142A1 (en) * 2020-09-10 2022-03-10 The Babcock & Wilcox Company Smelt shattering method and apparatus

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3269941A (en) * 1964-03-23 1966-08-30 Kimberly Clark Co Method of neutralizing acid bleachery effluent
US3366534A (en) * 1964-08-14 1968-01-30 Hooker Chemical Corp Complete chemical system for a kraft mill

Also Published As

Publication number Publication date
DE1692848B2 (en) 1974-05-30
DE1692848A1 (en) 1971-10-21
DE1692848C3 (en) 1975-01-23
US3453174A (en) 1969-07-01
FR1465228A (en) 1967-01-06

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