US1739683A - Treatment of fibrous vegetable materials - Google Patents

Treatment of fibrous vegetable materials Download PDF

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Publication number
US1739683A
US1739683A US325376A US32537628A US1739683A US 1739683 A US1739683 A US 1739683A US 325376 A US325376 A US 325376A US 32537628 A US32537628 A US 32537628A US 1739683 A US1739683 A US 1739683A
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treatment
fibres
fibre
flax
nodes
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US325376A
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Lucas Owen David
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Vickers Ltd
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Vickers Ltd
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    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01CCHEMICAL OR BIOLOGICAL TREATMENT OF NATURAL FILAMENTARY OR FIBROUS MATERIAL TO OBTAIN FILAMENTS OR FIBRES FOR SPINNING; CARBONISING RAGS TO RECOVER ANIMAL FIBRES
    • D01C1/00Treatment of vegetable material
    • D01C1/02Treatment of vegetable material by chemical methods to obtain bast fibres

Definitions

  • each of the external fibres of flax which may he, say, centimetres long, is made up of a number of short lengths, say 4 centimetres long, which are joined together by bonds or nodes, and may be termed the ultimate fibres.
  • the nodes in adjacent long fibres not being in alignment; that is, the ultimate short fibres in one long fibre-overlapping those in an adjacent long fibre, when a bunch of long fibres is cutacross or torn across.
  • bonds or nodes are destroyed or weakened by chemical action so that practically all the ultimate fibres will remain unbroken after passing through a carding or other suitable process to separate the ultimate fibres from each other.
  • a strong and glossy yarn can be made from the fibres thus produced.
  • the plant straw may or may not havebeen dried before this treatment, but in the case of flax is prefeably unretted, the results obtained with retted flax straw not being so good as those obtained with unretted straw.
  • it may then be scutched in the usual way to separate the shive from the textile fibre, the fibre alone being treated to weaken or destroy the bonds or nodes, but by the use of this invention it is possible to eliminate the operation of scutching.
  • the strawwithout previous scutching is first digested in an autoclavefor about an hour in plain water at a temperature of 182 C. and corresponding pressure, furfural being then distilled off, then the material is boiled for from 4 to 6 hours in a 3% to 5% caustic soda solution in quantity 5 to 8 times the weight of the material at a temperature of from 150 to 170 C. and corresponding pressure.
  • a suitable plasticizer may be added to the soda solution in the autoclave; this plasticizer may consist of 1 of Turkey redoil and oflin'seed oil on the weight of the straw.
  • the pulp is washed with water, preferably soft water, then immersed in an acid bath, preferably hydrochloric acid at a strength of to 2% in cold water, and again washed.
  • the pulp then contains flax fibres in which the bonds or nodes have been destroyed or weakened, anda considerably larger proportion of shive or fibre of very short length, and can be dried and sorted by carding or similar machinery intoflax fibres of a length suitable for spinning, and very short fibres consisting of cellulose, which latter if 'pure can be dissolved for making artificial silk, or if containing sub-normal cellulose (beta and gamma cellulose) can be used for making paper, cardboard or electrical insulating materials.
  • the mixed fibres can be sorted into their respective lengths by a wet method,employing screening as used in paper mills, the short fibres going directly from'thc separator to the paper making machine, while the longer fibres are retained and dried for spinning.
  • the fibre is treated in an autoclave in acaustic soda solution at a. temperature of 130 to 17 0 C. and corresponding pressure.
  • a suitable plasticizer is added to the solution originally placed in the autoclave; the said plasticizer may consist of 1 70 of Turkey red oil and linseed oil on the- Weight of the fibre treated.
  • the concentration of the caustic soda solution may vary between 1%, and 5% and the time of treatment in the autoclave from 20 minutes to 4 hours according to the degree of lustre and ultimate strength of fibre and degree of disintegration required. The shorter the time and the weaker the concentration of the solution,the less lustre and greater strength thefibres will possess, but
  • the lustre is not much diminished during treatment for the next 2 hours and the length centration of the solution being controlled ac cording to the extent to which weaking of the said bonds is desired, after which the material is washed in water, immersed in a cold acid bath, and again washed.
  • the time and/or concentration will be greater than for flax spinning machinery.
  • the fibre On removal from the autoclave, the fibre is washed in water, preferably soft water, then immersed in an acid bath, which may comprise to 2% of hydrochloric acid in cold water. I The acid neutralizes any soda left in the fibre and de hydrolyzes any hydrocellulose formed, as well as destroying any soda cellulose. The fibre is then again washed and dried for spinning.
  • a treatment similar to that herein described in detail with reference to flax is also applicable to other fibrous materials such as hemp, ramie and the like.
  • a process of obtaining from flax and other similar fibrous vegetable materials a fibre suitable for spinning comprising the steps of treating the said material at a temperature of 130 to 170 C. and'corresponding pressure with a caustic soda solutionof a strength between 1% and 5% containing a plasticizer fora length of time varying from twenty minutes to four hours sufficientto weaken the bonds or nodes be tween the ultimate short fibres composing each long fibre, the said time and the con-

Description

Patented Dec. 17, 1929 UNITED sTATEs PATENT OFFICE OWEN DAVID LUCAS, OF WESTMINSTER, ENGLAND, ASS IGNOR T0 VICKERS LIMITED,
' OF WESTMINSTER, ENGLAND, A BRITISH COMPANY TREATMENT OF FIBBOUS VEGETABLE MATERIALS I No Drawing. Application filed December 11, 1928, Serial No. 325,376, and in Great Britain December 8 hemp or ramie, fibres having a highgloss and adapted to be spun intoyarn bymachinery of the type generally used .in cottonmills aswell as by machinery of the type generally used in flax mills, valuable by-products as hereinafter described being also obtained from the said plants by the said method.
It is known that each of the external fibres of flax which may he, say, centimetres long, is made up of a number of short lengths, say 4 centimetres long, which are joined together by bonds or nodes, and may be termed the ultimate fibres. The nodes in adjacent long fibres not being in alignment; that is, the ultimate short fibres in one long fibre-overlapping those in an adjacent long fibre, when a bunch of long fibres is cutacross or torn across. at any point in order to produce fibres of such a short length that they can be dealt with by cotton spinning machinery, many of the ultimate fibres are broken at some part between the nodes, and the cut or broken ends will not'bind satisfactorily with'the other portions when spun into yarn, but project outside the yarn, which is therefore both roughened and weakened.
According to this invention the bonds or nodes are destroyed or weakened by chemical action so that practically all the ultimate fibres will remain unbroken after passing through a carding or other suitable process to separate the ultimate fibres from each other. A strong and glossy yarn can be made from the fibres thus produced.
The plant straw may or may not havebeen dried before this treatment, but in the case of flax is prefeably unretted, the results obtained with retted flax straw not being so good as those obtained with unretted straw. In the case of its having been dried, it may then be scutched in the usual way to separate the shive from the textile fibre, the fibre alone being treated to weaken or destroy the bonds or nodes, but by the use of this invention it is possible to eliminate the operation of scutching.
The strawwithout previous scutching is first digested in an autoclavefor about an hour in plain water at a temperature of 182 C. and corresponding pressure, furfural being then distilled off, then the material is boiled for from 4 to 6 hours in a 3% to 5% caustic soda solution in quantity 5 to 8 times the weight of the material at a temperature of from 150 to 170 C. and corresponding pressure. A suitable plasticizer may be added to the soda solution in the autoclave; this plasticizer may consist of 1 of Turkey redoil and oflin'seed oil on the weight of the straw. On completion of the treat ment in the autoclave the pulp is washed with water, preferably soft water, then immersed in an acid bath, preferably hydrochloric acid at a strength of to 2% in cold water, and again washed.
1 In the case of flax str'aw being treated, the pulp then contains flax fibres in which the bonds or nodes have been destroyed or weakened, anda considerably larger proportion of shive or fibre of very short length, and can be dried and sorted by carding or similar machinery intoflax fibres of a length suitable for spinning, and very short fibres consisting of cellulose, which latter if 'pure can be dissolved for making artificial silk, or if containing sub-normal cellulose (beta and gamma cellulose) can be used for making paper, cardboard or electrical insulating materials.
The aforesaid treatment with caustic soda I if continued for six hours, removes a considerable proportion of the sub-normal eel-- lulose, but if a less pure residue is required, for example for paper making, 4 hours treatment with caustic soda will suflice, and is advantageous in producing a stronger flax fibre for spinning.
Instead of being dried, the mixed fibres can be sorted into their respective lengths by a wet method,employing screening as used in paper mills, the short fibres going directly from'thc separator to the paper making machine, while the longer fibres are retained and dried for spinning.
It will be observed that when the invention is used in-a paper mill, a single operation separates the products required for paper making from t ose suitable for spinning.
In the application of the invention to the treatment of fibre which has been scutched the fibre is treated in an autoclave in acaustic soda solution at a. temperature of 130 to 17 0 C. and corresponding pressure. A suitable plasticizer is added to the solution originally placed in the autoclave; the said plasticizer may consist of 1 70 of Turkey red oil and linseed oil on the- Weight of the fibre treated. The concentration of the caustic soda solution may vary between 1%, and 5% and the time of treatment in the autoclave from 20 minutes to 4 hours according to the degree of lustre and ultimate strength of fibre and degree of disintegration required. The shorter the time and the weaker the concentration of the solution,the less lustre and greater strength thefibres will possess, but
although the maximum lustre is always reached after half an hours treatment wlth a I concentration of 1% and upwards at 130 C.
the lustre is not much diminished during treatment for the next 2 hours and the length centration of the solution being controlled ac cording to the extent to which weaking of the said bonds is desired, after which the material is washed in water, immersed in a cold acid bath, and again washed.
2. A process as in claim 1 applicable to the treatment of flax straw Without previous of time which the treatment is continued be yond this first half-hour depends on the degree of disintegration of the nodes of the fibre that may be desired, that is, the longer the treatment lasts, the higher the temperature, and the stronger the solution employed, which must not however exceed 5%, the more readily will the long fibres be subdivided by subsequent treatment into fine fibres of the lengths existing between the nodes of the long fibres.
Generally for cotton spinning machinery where shorter fibre is required, the time and/or concentration will be greater than for flax spinning machinery. On removal from the autoclave, the fibre is washed in water, preferably soft water, then immersed in an acid bath, which may comprise to 2% of hydrochloric acid in cold water. I The acid neutralizes any soda left in the fibre and de hydrolyzes any hydrocellulose formed, as well as destroying any soda cellulose. The fibre is then again washed and dried for spinning.
A treatment similar to that herein described in detail with reference to flax is also applicable to other fibrous materials such as hemp, ramie and the like.
What I claim and desire to secure by Letters Patent of the United States is l. A process of obtaining from flax and other similar fibrous vegetable materials a fibre suitable for spinning, said process comprising the steps of treating the said material at a temperature of 130 to 170 C. and'corresponding pressure with a caustic soda solutionof a strength between 1% and 5% containing a plasticizer fora length of time varying from twenty minutes to four hours sufficientto weaken the bonds or nodes be tween the ultimate short fibres composing each long fibre, the said time and the con-
US325376A 1927-12-08 1928-12-11 Treatment of fibrous vegetable materials Expired - Lifetime US1739683A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB33232/27A GB309210A (en) 1927-12-08 1927-12-08 Improvements in or relating to the treatment of flax straw and other fibrous materials

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2583994A (en) * 1946-06-21 1952-01-29 Rayonier Inc Wood pulp digestion
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
US2700608A (en) * 1950-12-27 1955-01-25 Procedes Lourd Soc D Expl Des Process for degumming vegetable textile fibers
US2932600A (en) * 1953-02-25 1960-04-12 Brown And Root Inc Process for the production of pulp from bagasse
US2999783A (en) * 1957-10-05 1961-09-12 Hodogaya Chemical Co Ltd Process for simultaneous production of high alpha-pulp with furfural from latifoliate tree materials

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2757583A (en) * 1949-03-23 1956-08-07 Basler Hermann Method for the production of hard fiberboards
US3013933A (en) * 1953-01-28 1961-12-19 Rayonier Inc Method for preparation of wood cellulose

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2583994A (en) * 1946-06-21 1952-01-29 Rayonier Inc Wood pulp digestion
US2700608A (en) * 1950-12-27 1955-01-25 Procedes Lourd Soc D Expl Des Process for degumming vegetable textile fibers
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
US2932600A (en) * 1953-02-25 1960-04-12 Brown And Root Inc Process for the production of pulp from bagasse
US2999783A (en) * 1957-10-05 1961-09-12 Hodogaya Chemical Co Ltd Process for simultaneous production of high alpha-pulp with furfural from latifoliate tree materials

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Publication number Publication date
GB309213A (en) 1929-04-08
FR664524A (en) 1929-09-04
GB309211A (en) 1929-04-08
FR664523A (en) 1929-09-04
GB309210A (en) 1929-04-08
FR664522A (en) 1929-09-04

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