GB481631A - Process for the decomposition of wood for the production of cellulose - Google Patents

Process for the decomposition of wood for the production of cellulose

Info

Publication number
GB481631A
GB481631A GB35818/36A GB3581836A GB481631A GB 481631 A GB481631 A GB 481631A GB 35818/36 A GB35818/36 A GB 35818/36A GB 3581836 A GB3581836 A GB 3581836A GB 481631 A GB481631 A GB 481631A
Authority
GB
United Kingdom
Prior art keywords
steam
treatment
wood
air
mixture
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
GB35818/36A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB481631A publication Critical patent/GB481631A/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
    • D21C1/00Pretreatment of the finely-divided materials before digesting
    • D21C1/02Pretreatment of the finely-divided materials before digesting with water or steam

Abstract

In the manufacture of cellulose, wood is pretreated before applying thereto any lignin-removing or oxidizing treatment, with a controlled mixture of steam and oxygen or air, and then without intermediate oxidizing treatment with a known reagent to remove the greater part of the lignin. Temperatures and pressures in the lignin-removing step may be lower than usual due to the pretreatment. The steam and air mixture may be produced by causing hot air to act upon damp wood, part of the moisture content of the wood being given off as steam. The ratio between the partial pressures of steam and oxygen is preferably between 2 : 1 and 5 : 1 and the preferred temperature range is 100-200 DEG C. The wood may be subjected to a preliminary treatment with weakly acid or alkaline liquids, small quantities of substances to catalyze the oxidizing action, e.g. ferric nitrate being employed if desired. These preliminary treating solutions are not strong enough to effect decomposition themselves. A preliminary steaming treatment may also be employed. The ratio of oxygen to steam in the treating mixture may be reduced during the process if desired. Suitable encrustant solvents for the final treatment are alkalies, alkali hypochlorites, or organic solvents such as alcohols, ketones, phenols, or dioxane, hydrous or anhydrous. This treatment may be combined with a disintegration treatment. Organic solvents are readily recoverable. In examples: (1) spruce chips are steamed, treated with a mixture of equal volumes of steam and air, the ratio of oxygen to steam being reduced towards the end of the treatment, and then digested with alkali and disintegrated; (2) moist beech wood chips are heated in an autoclave with compressed air. Hot air or steam may be fed in and steam-air mixture may be let out and the partial pressure of the steam is kept just below saturation point. The current of air fed in may be increased and diminished several times in succession and is finally cut off altogether. The material is subsequently treated for a time with saturated steam, and then extracted with dilute alcohol and disintegrated. Other examples treat pine wood chips, the final treatment being with alkali; and aspen wood chips, the final treatment being with alkali and chlorine, in lower concentrations than those normally employed.
GB35818/36A 1935-12-31 1936-12-31 Process for the decomposition of wood for the production of cellulose Expired GB481631A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT481631X 1935-12-31

Publications (1)

Publication Number Publication Date
GB481631A true GB481631A (en) 1938-03-15

Family

ID=3674948

Family Applications (1)

Application Number Title Priority Date Filing Date
GB35818/36A Expired GB481631A (en) 1935-12-31 1936-12-31 Process for the decomposition of wood for the production of cellulose

Country Status (2)

Country Link
BE (1) BE419220A (en)
GB (1) GB481631A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2686120A (en) * 1952-01-14 1954-08-10 Ontario Paper Co Ltd Alkaline pulping of lignocellulose in the presence of oxygen to produce pulp, vanillin, and other oxidation products of lignin substance
FR2343855A1 (en) * 1976-03-12 1977-10-07 Union Carbide Corp Wood chip decomposition process - has an initial thermal and oxygen treatment to increase wood yield

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD154451A3 (en) * 1980-05-12 1982-03-24 Mihalne Atomyr PROCESS FOR THE PRODUCTION OF PULP FROM PLANTS, IN PARTICULAR STRAW

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2686120A (en) * 1952-01-14 1954-08-10 Ontario Paper Co Ltd Alkaline pulping of lignocellulose in the presence of oxygen to produce pulp, vanillin, and other oxidation products of lignin substance
FR2343855A1 (en) * 1976-03-12 1977-10-07 Union Carbide Corp Wood chip decomposition process - has an initial thermal and oxygen treatment to increase wood yield

Also Published As

Publication number Publication date
BE419220A (en)

Similar Documents

Publication Publication Date Title
GB427626A (en) Improvements in or relating to the manufacture of cellulose
US2394989A (en) Manufacture of cellulose
GB555985A (en) Improvements in or relating to the manufacture of cellulose
GB481631A (en) Process for the decomposition of wood for the production of cellulose
US2022664A (en) Manufacture of cellulose from lignocellulose materials
US2041745A (en) Manufacture of cellulosic prod
GB438436A (en) Improvements in the production of cellulose and cellulosic products
GB885605A (en) Improved method for the production of neutral sulfite pulp
US2061616A (en) Production of cellulose
US2118039A (en) Manufacture of cellulose
GB710257A (en) Wood pulp
US1859845A (en) Treatment of wood for the production of pulp
US3051611A (en) Hydrolysis of bagasse
US1581671A (en) Production of pulp and other products from wood
GB474305A (en) Improvements in or relating to the manufacture of cellulose from lignocellulosic materials
GB674079A (en) Improvements in or relating to a process for the production of fibre plates and formed bodies of lignocellulosic materials using the lignin of the lignocellulosic materials as a binding agent
GB477842A (en) Improvements in or relating to the manufacture of cellulose from lignin-containing cellulosic materials
GB640543A (en) Improvements in or relating to the production of cellulose
DE964560C (en) Process for the pretreatment of wood chips with ammonia during bisulfite pulping
US2005190A (en) Process for the digestion of vegetable growths to produce cellulose
LaForge The production of furfural by the action of superheated water on aqueous corncob extract
GB459531A (en) Improvements in or relating to the manufacture of cellulose
GB526399A (en) Improvements in or relating to processes for obtaining cellulose for the manufactureof rayon from resinous pine woods
US1813531A (en) Process for obtaining a product rich in cellulose and useful by-products from straw
GB244788A (en) Process of treating plant material