GB1396132A - Method of making semichemical pulp by means of an alkaline digesting liquid having as main constituents na2s and na2co3 - Google Patents

Method of making semichemical pulp by means of an alkaline digesting liquid having as main constituents na2s and na2co3

Info

Publication number
GB1396132A
GB1396132A GB2463472A GB2463472A GB1396132A GB 1396132 A GB1396132 A GB 1396132A GB 2463472 A GB2463472 A GB 2463472A GB 2463472 A GB2463472 A GB 2463472A GB 1396132 A GB1396132 A GB 1396132A
Authority
GB
United Kingdom
Prior art keywords
liquor
pulp
vessel
digesting
smelt
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
GB2463472A
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.)
Valmet AB
Original Assignee
Defibrator AB
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 Defibrator AB filed Critical Defibrator AB
Publication of GB1396132A publication Critical patent/GB1396132A/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
    • D21C11/06Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds
    • D21C11/08Deodorisation ; Elimination of malodorous compounds, e.g. sulfur compounds such as hydrogen sulfide or mercaptans, from gas streams
    • 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
    • D21C11/0057Oxidation of liquors, e.g. in order to reduce the losses of sulfur compounds, followed by evaporation or combustion if the liquor in question is a black liquor

Landscapes

  • Paper (AREA)

Abstract

1396132 Pulp manufacture DEFIBRATOR AB 25 May 1972 [4 June 1971] 24634/ 72 Heading D2W Pulp is made from lignocellulosic material in a yield of 65-90% by impregnating the lignocellulosic material with a digesting liquor comprising sodium sulphide and sodium carbonate, digesting the impregnated material in the vapour phase in an atmosphere of steam at 159-190‹C, cooling the resulting pulp and liquor to not less than 100‹C, adding molecular oxygen sulphur compounds therefrom, separating the pulp from the liquor, and recovering chemicals from the liquor. The latter step is carried out by concentrating the liquor by evaporation, and burning the concentrated liquor to yield a smelt consisting substantially of sodium sulphide and sodium carbonate, and dissolving the smelt in water to form fresh digesting liquor. As shown, wood chips are fed via conveyor 1 into a vessel 2 in which they steamed and then into a digester 7. The digesting liquid is supplied to the vessel via pipe 47 and steam via pipe 17. Digested chips and liquor are then fed into vessel 10 which is supplied with compressed air via line 12 from compressor 13, and subsequently blown therefrom into a centrifugal cleaner 20. Pulp removed from the bottom of the cleaner is defibrated by difibrator 25 and passed to a filter 26 for separation of liquor, liquor recovered in tank 28 is concentrated in evaporator 43, and burnt in furnace 44. The smelt obtained is dissolved in tank 45 and the fresh digestion liquor recirculated via line 47. The digested chips may be cooled during thier transfer from digester 7 to vessel 10 by using a watercooled conveyor.
GB2463472A 1971-06-04 1972-05-25 Method of making semichemical pulp by means of an alkaline digesting liquid having as main constituents na2s and na2co3 Expired GB1396132A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE729371A SE350078B (en) 1971-06-04 1971-06-04

Publications (1)

Publication Number Publication Date
GB1396132A true GB1396132A (en) 1975-06-04

Family

ID=20270971

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2463472A Expired GB1396132A (en) 1971-06-04 1972-05-25 Method of making semichemical pulp by means of an alkaline digesting liquid having as main constituents na2s and na2co3

Country Status (6)

Country Link
JP (1) JPS5335601B1 (en)
CA (1) CA994961A (en)
DE (1) DE2226777C3 (en)
FR (1) FR2140222A1 (en)
GB (1) GB1396132A (en)
SE (1) SE350078B (en)

Also Published As

Publication number Publication date
JPS5335601B1 (en) 1978-09-28
DE2226777A1 (en) 1973-02-08
FR2140222A1 (en) 1973-01-12
DE2226777C3 (en) 1975-04-10
DE2226777B2 (en) 1974-08-29
SE350078B (en) 1972-10-16
CA994961A (en) 1976-08-17

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee