Classifications

• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01C—CHEMICAL OR BIOLOGICAL TREATMENT OF NATURAL FILAMENTARY OR FIBROUS MATERIAL TO OBTAIN FILAMENTS OR FIBRES FOR SPINNING; CARBONISING RAGS TO RECOVER ANIMAL FIBRES
  • D01C1/00—Treatment of vegetable material
  • D01C1/02—Treatment of vegetable material by chemical methods to obtain bast fibres

Definitions

• My invention relates to the production of textile fibres from bast fibre material, such as flax, hemp, jute, ramie and the like.
• the customary method of obtaining spinning fibres from bast fibre material is to subject the crude material to a bacteriological retting process after which the woody material can be easily separated from the fibres by a mechanical treatment.
• This retting process has the drawback that it takes very much time and therefore many processes have been proposed to replace this retting process by a treatment with alkaline solutions, such as soda lye.
• alkaline solutions such as soda lye.
• these chemical retting methods have met with little success, which is mainly due to the fact that the crude material only consists for approximately /1 part of spinning fibres so that much lye is necessary to remove the /7 parts of nonfibrous woody material.
• the object of my invention is to remove this drawback.
• unretted bast fibrous material is subjected to a mechanical treatment in order to remove the greater part of the woody constituents.
• a suitable mechanical treatment to this end is the wellknown customary scutching operation.
• the fibres being deprived in this mechanical way of the larger part of the woody material are then subjected to a chemical treatment in order to further remove the woody constituents.
• This chemical treatment may consist in subjecting the fibrous material to the action of alkaline solutions.
• soda lye e. g. a 10% solution of sodium hydroxide in water, is very suitable, but aqueous solutions of other alkaline substances, e. g. potassium hydroxide, sodium carbonate, and
• the treatment depends on the temperature and the strength of the lye. At high temperatures a shorter duration is required than at lower temperatures, e. g. at the boiling point of the lye a treatment during half an hour or three quarters of an hour is generally suflicient, but at C. the treatment requires a few hours and at still lower temperatures a still longer duration is necessary.
• the strength of the lye should in general not be lower than 5% and preferably not more than 15%.
• the moist fibre mass is extracted with an organic solvent in order to prevent that the fibres will stick together on drying. It appeared that by this treatment the small amount of gummy or pectineous substances causing the stickness of the fibres is removed.
• organic solvents miscible with water. Suitable organic solvents are for instance methanol, acetone, aethanol, propanol or diaceton alcohol.
• low boiling organic solvents are e. g. methanol or acetone. It is also possible, however, to extract the fibrous material by means of higher boiling organic solvents, such as aethanol, propanol or diacetone alcohol and after the mechanical removal of the greater part of these solvents to remove the remaining part thereof by means of lower boiling organic solvents, e. g. acetone. In this case a lower boiling solvent not miscible with water may be used, such as ether.
• the removal of the organic solvent from the fibre material after the extraction may be executed by methods known per se, e. g. the organic solvent may be evaporated. To this end a hot current of gas, e. g. air may be circulated through the fibrous material. The solvent is recovered from this gas by condensation. In this way substantially no solvent is lost which makes the process very economical.
• a hot current of gas e. g. air may be circulated through the fibrous material.
• the solvent is recovered from this gas by condensation. In this way substantially no solvent is lost which makes the process very economical.
• the solvent may be evaporated in vacuo. In this case it is not necessary to make use of low boiling solvents, but the danger of solvent losses is greater.
• the alkaline lye Before the extraction by means of an organic solvent the alkaline lye is removed. The greater part may be mechanically eliminated after which the further part may be washed out with water. Any residual sodium hydroxide or other alkaline substance still remaining may be neutralized, e. g. by means of sulfuric or hydrochloric acid.
• the fibrous mass may be subjected to a bleaching treatment after the treatment with alkaline lye.
• a bleaching treatment after the treatment with alkaline lye.
• the fibrous mass after the mechanical removal of the excess of alkaline lye may be subjected to the action ofan'aqueous solution of an oxidizing agent, e. g. a hypochlorite, hydrogen peroxide or other active oxygen compounds.
• an oxidizing agent e. g. a hypochlorite, hydrogen peroxide or other active oxygen compounds.
• the alkali still present is neutralized by an acid or acid substance, e. g. hydrochloric, sulfuric orcarbonic acid.
• the necessary 10% sodium hydroxide solution is prepared from sodium chloride by electrolysis according to the well-known mercury process, chlorine and hydrochloric acid are formed besides the sodium hydroxide'solution. This chlorine is used for the bleaching.
• the electric current for the electrolysis is obtained by means of steam the exhaust steam may be utilized for the distillation of the organic solvent and for heating the lye bath.
• the hydrochloric acid formed by the electrolysis is preferably not used for the neutralization which I prefer to realize by means of sulfuric acid, but for converting the woody constituents, removed from the bast fibres into sugar material, which may be used in fruit preserving or in cattle fodder.
• My process is particularly suitable for the production of spinning fibres from flax straw but can also be applied toother bast fibres requiring a chemical retting.
• Crude fiax is subjected to scutching in the usual way.
• the scutched .flax is completely submerged. in soda lye (which may have been prepared by electrolyzing a common salt solution) and heated therein at boiling temperature during half an hour to three quarters of an hour.
• the excess of lye is removed by a mechanical treatment, e. g. pressing out or centrifugal action and returned to the bath for the treatment of further scutched fiax.
• the fibrous mass with the lye remaining therein is transferred to a bath with water and 01110-- rine is slowly introduced. In this wayv sodium hypochlorite is formed which bleaches the fibrous material. After the bleaching action the fibre mass is rinsed in plain water. Any residues of soda lye are neutralized by means of sulfuric or hydrochloric acid.
• the excess of water is mechanically removed from the fibre mass, e. g. by passing the mass between rollers under pressure.
• the damp fibre mass so obtained is extracted by means of acetone in a proportion of six litres of acetone to 1kg. of moist fibres. This extraction treatment is repeated three times with two litres of acetone each time. 'The'acetone remainingin the fibre mass is then removed by means of a circulating 4 current of hot air or by vacuum. From this air the acetone may be recovered by condensation and the mixture of acetone and water so obtained can be separated by means of fractional distillation. The acetone so recovered may then be used for the extraction of further flax material.
• the dried fibres thus produced are now ready forthe further mechanical treatment such as haekling or spinning.
• said alkali solution comprises a compound selected from the group consisting of sodium hydroxide, potassium hydroxide andsodium carbonate.
• alkali'solution having a concentration of between about 5% and 15%, bleaching the resulting fibers, washing the resulting bleached fibers-with Water, and extracting thewater from the resulting 'moist'fibers with awater miscible organic solventselected from the group consisting of methanol, ethanol, propanol, acetone and diacetone alcohol, to thereby produce dry-noncohesive fibers.
• a processfor converting .unretted bastfibrous material into-drynon-cohesive fibers ready for spinning consisting .of the steps of: subjecting saidunretted fibrous material to the action of an aqueousalkali solution at a temperature between about 80 C. and the boiling temperature of said alkali solution to remove woody constituents from said bast fibrous material, said alkali solution having a concentration of 'between about 5% and 15%, washing the resulting fibers with watenxextracting the water from the resulting'moist washed fibers with a high boiling water miscible organic solvent selected from the group consisting of methanol, ethanol, propanol, acetone. and diacetonealcohol, extracting said organic solvent from said fibers with a lower. boiling organic-solvent. selected from the group consisting of methanol, acetone and ether, and removingsaid low boiling solvent fromsaidfibers.
• A. process for .converting unretted bast fibrous material into dry non-cohesive fibers-ready for spinning consisting of the steps of: scutching said bast fibrous material to remove the larger part of the woody material, subjecting the resulting scutched fibers to the action of an aqueous alkali solution at about the boiling temperature of said solution for one half to three quarters of an hour to remove further woody constituents from said bast fibrous material, said alkali solution having a concentration of between about 5% and 15%, said alkali solution comprising a compound selected from the group consisting of sodium hydroxide, potassium hydroxide and sodium carbonate, mechanically removing said alkali solution from said fibers, bleaching said fibers in an aqueous solution containing chlorine, mechanically removing said fibers from said bleaching solution, washing said fibers with water, extracting the water from the resulting moist washed fibers with a water miscible organic solvent selected from the group consisting of methanol, ethanol, propan

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• Chemical & Material Sciences (AREA)
• General Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Health & Medical Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Molecular Biology (AREA)
• Wood Science & Technology (AREA)
• Zoology (AREA)
• Textile Engineering (AREA)
• Artificial Filaments (AREA)
• Chemical Or Physical Treatment Of Fibers (AREA)

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Citations (12)

• 0
  • LU LU28107D patent/LU28107A1/xx unknown
  • NL NL60524D patent/NL60524C/xx active
  • BE BE468348D patent/BE468348A/xx unknown
• 1943
  • 1943-02-16 DE DEN1439D patent/DE922786C/de not_active Expired
• 1945
  • 1945-12-12 US US634614A patent/US2639988A/en not_active Expired - Lifetime
• 1946
  • 1946-08-12 FR FR948919D patent/FR948919A/fr not_active Expired

Patent Citations (12)

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