CA2137232A1 - Method of producing cellulose fibres with a decreased tendency to fibrillation - Google Patents
Method of producing cellulose fibres with a decreased tendency to fibrillationInfo
- Publication number
- CA2137232A1 CA2137232A1 CA002137232A CA2137232A CA2137232A1 CA 2137232 A1 CA2137232 A1 CA 2137232A1 CA 002137232 A CA002137232 A CA 002137232A CA 2137232 A CA2137232 A CA 2137232A CA 2137232 A1 CA2137232 A1 CA 2137232A1
- Authority
- CA
- Canada
- Prior art keywords
- fibres
- process according
- fibrillation
- textile
- textile agent
- 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.)
- Abandoned
Links
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F11/00—Chemical after-treatment of artificial filaments or the like during manufacture
- D01F11/02—Chemical after-treatment of artificial filaments or the like during manufacture of cellulose, cellulose derivatives, or proteins
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
- Artificial Filaments (AREA)
- Chemical Treatment Of Fibers During Manufacturing Processes (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Abstract Process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres and the freshly spun fibres are contacted with a textile agent comprising at least two reactive groups, and are heat-treated, characterized in that the heat treatment is carried out by means of irradiation with electromagnetic waves.
Description
'~1372~'~
PROCESS FOR THE PRODUCTION OF CELLULOSE FIBRES aAVING A REDUCED ~-~
TENDENCY TO FIBRILLATION
The invention is concerned with a process for the production of cellulose fibres having a reduced tendency to fibrillation.
As an alternative to the viscose process, in recent years there has been described a number of processes in which cellulose, without forming a derivative, is dissolved in an organic solvent, a combination of an organic solvent and an inorganic ,. ~, ,, . .~ .- .
salt, or in aqueous saline solutions. Cellulose fibres made;~
from such solutions have received by BISFA (The International Bureau for the Standardisation of man made Fibres) the géneric name Lyocell. As Lyocell, BISFA define~ a cellulose fibre obtained by a spinning process from an organic solvent. By "organic solvent", BISFA understands a mixture of an organic chemical and water. "Solvent-spinning" ist considered to mean disgolving and spinning without the forming of a derivative. ~.
So far, however, only one process for the production of a ;-~-cellulose fibre of the Lyocell type has achieved industrial~
scale realization. In this process, a tertiary amine-oxide, -particularly N-methylmorpholine-N-oxide (NMMO), is used as a ;
~olvent. Such a process is described for instance in US-A - ~ <-4,246,221 and provides fibres which present a high tensile ',.,"~.,':!'~;,~.'~,"~
~trength, a high wet-modulus and a high loop strength.
However, the usefulness of plane fibre assemblies, for example fabrics, made from the above fibres, is significantly ; ~ ~;
restricted by;~the pronounced,tendency of such fibres to ! :`' ~ ~''i';'."' fibrillate when wet. Fibrillation means the breaking up of the wet fibre in longitudinal direction at mechanical stress in a wet condition, so that the fibre gets hairy, furry. A fabric made from these fibres and dyed significantly loo~es colour intensity as it is washed several times. Additionally, light ~tripes are formed at the abrasion and crease edge3. The reason may be that the fibres consist of fibrils which are arranged in the longitudinal direction of the fibre axis and that the crosslinking between these is reduced. ~ J
- 2137 2? 2 -2- -:~
wo 92/14871 describe~ a process for the production of a fibre ~ i having a reduced tendency to fibrillation. The reduced tendency -to fibrillation is attained by providing all the baths with which the freshly spun fibre is contacted before the first drying with a maximum pH of 8,5.
wo 92to7l24 also describes a proce~s for the production of a fibre having a reduced tendency to fibrillation, according to ~ ~j which the freshly spun, i.e. not yet dried, fibre is treated with a cationic polymer. As such a polymer, a polymer with imidazole and azetidine groups is mentioned. Additionally, there may be carried out a treatment with an emulsifiable ~ ;
polymer, such as polyethylene or polyvinylacet~te, or a crosslinking with glyoxal.
In a lecture given by S. Mortimer at the CELLUCON conference in ~-1993 in Lund, Sweden, it was mentioned that the tendency to fibrillation rises as drawing is increased.
It is the objective of the invention to provide a process which can be carried out in an easy way, allowing the production of i ~ -;
cellulose fibres of the Lyocell type having a reduced tendency to fibrillation.
The process according to the invention for the production of "'''~',',~'~'''1`'',~'!'~'','~
cellulose fibres having a reduced tendency to fibrillation con~ist~ in that the freshly spun, not yet dried fibres are contacted with a textile agent, which carries at least two reactive groups, and are washed with an aqueous buffer, provided glyoxal is not used,a~ textile agent. :
A~ textile agent~, especially dyes having two reactive groups have shown good result~. According to the invention, however, ~-textile agents which are colourless, i.e. do not absorb visible light, may al~o be used.
According to the invention, the use of textile agents which ~ ji carry one or two vinylsulfone groups as reactive groups is ~ ' preferred. ~
I '~ '.,~ ;','`',`, A convenient embodiment of the process according to the ~;
invention is charactPrized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium. ~ t It was shown that the tendency to fibrillation is especially reduced when an alkali carbonate and an alkali hydroxide is ;
chosen as the alkaline medium.
Another preferred embodiment of the process according to the invention consists in that the fibres contacted with the textile agent are heat-treated. The heat treatment drastically reduces the impregnation time.
EP-A - O 538 977, published on April 28, 1993, describes heat treatment of cellulose fibres impregnated with a dye. It was i~ ~ ^
shown, however, that heating of the fibres impregnated with the ~ ',.`;4:''~'.
textile agent by means of hot air may reduce the impregnation time, but that this carries the risk of the fibres not being heated uniformly. Thus for example, the fibres on the outside of a fibre bundle to be dried may already be partly dried, 2;
while the fibres inside the bundle have not yet reached the required temperature. This has a negative effect on the quality of the fibree produced.
It has been f ound that thi~ drawback occurring in a simple heat treatment can be overcome by irraidiating the fibres with electromagnetic waves, particularly microwaves. When irradiated with microwaves, on the one hand the fibres are heated ~;
uniformly and on the other hand premature drying of the fibres j;
can be avoided, since irradiation with electromagnetic waves provides the po~sibility to weld the fibre bundle for example into a plastic wrapping and expose it in a welded condition to the electromagnetic field. -~
' ;: ~ ''~`.. `'.'.' The above advantages are also given when the fibres, for ~;~
example lying a~ plane fibre assembly on a conveyor, are moved through a narrow channel, in which they are exposed to electromagnetic waves. This channel can be designed in a way that only little air space above the fibres is left, thereby .:' preventing a partial drying of the outer fibres of the bundle.
Simultaneously, this way of fixation of the textile agent also offers the possibility of a large-scale production easy to put into practice.
Thus, the invention further refers to a process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres, and the freshly spun fibres are contacted with a textile agent which carries at least two reactive groups and are heat-treated, characterized in that the heat treatment is carried out by irradiation with electromagnetic waves. ~-Also according to this embodiment of the process according to the invention, the use of a textile agent which carries vinylsulfone groups as the reactive groups, is preferred, ;~
preferably being a dye. However, textile agents which are `;i;~
colourless, i.e. do not absorb visible light, can also be used.
Another preferred embodiment of the process according to the ,~
invention consists in carrying out the heat treatment by means of microwaves.
The invention will be explained in more detail by the following example~. All references to % are to be understood as weight %.
Production of the cellulose fibres According to the process!described in EP-A - 0 356 419, a ! ~ ~ ""~''" ~' ~' ~olution of cellulose in NMM0 was prepared and extruded through a spinneret. The filaments thereby obtained were conducted through an air gap into an aqueous precipitation bath, in which the cellulose coagulated. The fibres obtained in the precipitation bath were washed, presenting a titer of 1,7 dtex.
The wa~hed fibres were used for the examples hereinafter described and represent those fibres which in the present description and in the present claims are referred to as fibres freshly spun, not yet dried.
' ' ''~;
2~372~
1) Treatment with textile agents without subsequent heat treatment -A) General procedure 1 g of each of the fibres produced according to the above process were impregnated in 190 ml of an aqueous solution (bath), which contained a textile agent comprising two reactive groups and Na2SO4, at 40C for 30 minutes. Then NaOH (3%), -~
Na2CO3 (4%) or a mixture of NaOH, Na2CO3 (4% Na2CO3 and 0,2 g/1 - -NaOH) were added for the fixation of the textile agent. After another 60 minutes at 40C the fibres were washed several times, in order to remove the textile agent not fixed to the '~
fibre. Then the washed fibres were treated for 30 minutes with an aqueous buffer, then again washed with water (for 15 minutes) and dried at 60C. Afterwards the fibres were examined to determine their tendency to fibrillation and to determine ;~
other fibre parameters.
Evaluation of fibrillation The abrasion of the fibres among each other in washing processes and finishing processes in wet condition was ~
~imulated by the following test: 8 fibres with a length of 20 j ~ ;
mm e~ch were put into a 20 ml sample bottle with 4 ml of water and ~haken during 9 hours in a laboratory mechanical shaker of the RO-10 type of the company Gerhardt, Bonn (Germany), at atage 12. Afterwards the fibrillation behaviour of the fibres ~ ;
was evaluated by microscope, by means of counting the number of ;~;
fibril~ per 0,276 mm fibre length.
: -~
"; ',,, . .,- ::. ~. , :-Further fibre parameters The fibre tensile strength and fibre elongation at break were ~ ~ -te~ited following the BISFA rule on "Internationally agreed methods for tei3ting vi~cose, modal, cupro, lyocell, acetat and -~;
triacetat staple fibres and tows", edition 1993. ~ `~; o B) Examples .,;,.;~"~ ,,,. ".,~ ,, According to the above process, fibres were treated with the dye Remazol Black B and Remazol Red RB as textile agent (made ;
by Hoechst AG). The dye Remazol Black B carries two -vinylsulfone groups and the dye Remazol Red B earries one vinylsulfone group and one monochlorotriazine group.
The bath contained 3~ Remazol Black B and 0,5% Remazol Red RB
respectively. The pH of the bath was 4,6 in each example. The ~ ~
used aqueous buffer was an aqueous solution which contained 3% ~ ~ -acetic acid and 7~ sodium acetate. The p~ value of this solution was 4,6. After the treatment with the buffer, the fibres were washed with water for 15 minutes and afterwards ~ ~-examined. Table la indicates the fixing agent used in each case, the fibrillation (number of fibrilsi), the titer (dtex), the fibre strength ~cN/tex) and the fibre elongation at break (%). Examples 1, 2 and 3 were carried out with the dye Remazol `~
Black B and Example 4 with the dye Remazol Red RB.
Table lb show~ the results of comparative tests carried out i without dye.
,, ,! i , ! ' ,'" '.", , ' " ~ " ~' '''` "~i ' '' ' ;', ~' ; ~' "''``,' , ~ "~.
21~7232 ~;
Table la (Textile Agent) Ex. Fixing agent Fibrils Titer Tensile Strength Elongation 1 NaOH 22 1,82 28,81 11,14 . , .;.
2 Na2CO~ 2 2,07 26,39 10,67 3 NaOH+Na~CO~ 0 2,34 24,94 10,04 _ , .. ~ . .. .
PROCESS FOR THE PRODUCTION OF CELLULOSE FIBRES aAVING A REDUCED ~-~
TENDENCY TO FIBRILLATION
The invention is concerned with a process for the production of cellulose fibres having a reduced tendency to fibrillation.
As an alternative to the viscose process, in recent years there has been described a number of processes in which cellulose, without forming a derivative, is dissolved in an organic solvent, a combination of an organic solvent and an inorganic ,. ~, ,, . .~ .- .
salt, or in aqueous saline solutions. Cellulose fibres made;~
from such solutions have received by BISFA (The International Bureau for the Standardisation of man made Fibres) the géneric name Lyocell. As Lyocell, BISFA define~ a cellulose fibre obtained by a spinning process from an organic solvent. By "organic solvent", BISFA understands a mixture of an organic chemical and water. "Solvent-spinning" ist considered to mean disgolving and spinning without the forming of a derivative. ~.
So far, however, only one process for the production of a ;-~-cellulose fibre of the Lyocell type has achieved industrial~
scale realization. In this process, a tertiary amine-oxide, -particularly N-methylmorpholine-N-oxide (NMMO), is used as a ;
~olvent. Such a process is described for instance in US-A - ~ <-4,246,221 and provides fibres which present a high tensile ',.,"~.,':!'~;,~.'~,"~
~trength, a high wet-modulus and a high loop strength.
However, the usefulness of plane fibre assemblies, for example fabrics, made from the above fibres, is significantly ; ~ ~;
restricted by;~the pronounced,tendency of such fibres to ! :`' ~ ~''i';'."' fibrillate when wet. Fibrillation means the breaking up of the wet fibre in longitudinal direction at mechanical stress in a wet condition, so that the fibre gets hairy, furry. A fabric made from these fibres and dyed significantly loo~es colour intensity as it is washed several times. Additionally, light ~tripes are formed at the abrasion and crease edge3. The reason may be that the fibres consist of fibrils which are arranged in the longitudinal direction of the fibre axis and that the crosslinking between these is reduced. ~ J
- 2137 2? 2 -2- -:~
wo 92/14871 describe~ a process for the production of a fibre ~ i having a reduced tendency to fibrillation. The reduced tendency -to fibrillation is attained by providing all the baths with which the freshly spun fibre is contacted before the first drying with a maximum pH of 8,5.
wo 92to7l24 also describes a proce~s for the production of a fibre having a reduced tendency to fibrillation, according to ~ ~j which the freshly spun, i.e. not yet dried, fibre is treated with a cationic polymer. As such a polymer, a polymer with imidazole and azetidine groups is mentioned. Additionally, there may be carried out a treatment with an emulsifiable ~ ;
polymer, such as polyethylene or polyvinylacet~te, or a crosslinking with glyoxal.
In a lecture given by S. Mortimer at the CELLUCON conference in ~-1993 in Lund, Sweden, it was mentioned that the tendency to fibrillation rises as drawing is increased.
It is the objective of the invention to provide a process which can be carried out in an easy way, allowing the production of i ~ -;
cellulose fibres of the Lyocell type having a reduced tendency to fibrillation.
The process according to the invention for the production of "'''~',',~'~'''1`'',~'!'~'','~
cellulose fibres having a reduced tendency to fibrillation con~ist~ in that the freshly spun, not yet dried fibres are contacted with a textile agent, which carries at least two reactive groups, and are washed with an aqueous buffer, provided glyoxal is not used,a~ textile agent. :
A~ textile agent~, especially dyes having two reactive groups have shown good result~. According to the invention, however, ~-textile agents which are colourless, i.e. do not absorb visible light, may al~o be used.
According to the invention, the use of textile agents which ~ ji carry one or two vinylsulfone groups as reactive groups is ~ ' preferred. ~
I '~ '.,~ ;','`',`, A convenient embodiment of the process according to the ~;
invention is charactPrized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium. ~ t It was shown that the tendency to fibrillation is especially reduced when an alkali carbonate and an alkali hydroxide is ;
chosen as the alkaline medium.
Another preferred embodiment of the process according to the invention consists in that the fibres contacted with the textile agent are heat-treated. The heat treatment drastically reduces the impregnation time.
EP-A - O 538 977, published on April 28, 1993, describes heat treatment of cellulose fibres impregnated with a dye. It was i~ ~ ^
shown, however, that heating of the fibres impregnated with the ~ ',.`;4:''~'.
textile agent by means of hot air may reduce the impregnation time, but that this carries the risk of the fibres not being heated uniformly. Thus for example, the fibres on the outside of a fibre bundle to be dried may already be partly dried, 2;
while the fibres inside the bundle have not yet reached the required temperature. This has a negative effect on the quality of the fibree produced.
It has been f ound that thi~ drawback occurring in a simple heat treatment can be overcome by irraidiating the fibres with electromagnetic waves, particularly microwaves. When irradiated with microwaves, on the one hand the fibres are heated ~;
uniformly and on the other hand premature drying of the fibres j;
can be avoided, since irradiation with electromagnetic waves provides the po~sibility to weld the fibre bundle for example into a plastic wrapping and expose it in a welded condition to the electromagnetic field. -~
' ;: ~ ''~`.. `'.'.' The above advantages are also given when the fibres, for ~;~
example lying a~ plane fibre assembly on a conveyor, are moved through a narrow channel, in which they are exposed to electromagnetic waves. This channel can be designed in a way that only little air space above the fibres is left, thereby .:' preventing a partial drying of the outer fibres of the bundle.
Simultaneously, this way of fixation of the textile agent also offers the possibility of a large-scale production easy to put into practice.
Thus, the invention further refers to a process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres, and the freshly spun fibres are contacted with a textile agent which carries at least two reactive groups and are heat-treated, characterized in that the heat treatment is carried out by irradiation with electromagnetic waves. ~-Also according to this embodiment of the process according to the invention, the use of a textile agent which carries vinylsulfone groups as the reactive groups, is preferred, ;~
preferably being a dye. However, textile agents which are `;i;~
colourless, i.e. do not absorb visible light, can also be used.
Another preferred embodiment of the process according to the ,~
invention consists in carrying out the heat treatment by means of microwaves.
The invention will be explained in more detail by the following example~. All references to % are to be understood as weight %.
Production of the cellulose fibres According to the process!described in EP-A - 0 356 419, a ! ~ ~ ""~''" ~' ~' ~olution of cellulose in NMM0 was prepared and extruded through a spinneret. The filaments thereby obtained were conducted through an air gap into an aqueous precipitation bath, in which the cellulose coagulated. The fibres obtained in the precipitation bath were washed, presenting a titer of 1,7 dtex.
The wa~hed fibres were used for the examples hereinafter described and represent those fibres which in the present description and in the present claims are referred to as fibres freshly spun, not yet dried.
' ' ''~;
2~372~
1) Treatment with textile agents without subsequent heat treatment -A) General procedure 1 g of each of the fibres produced according to the above process were impregnated in 190 ml of an aqueous solution (bath), which contained a textile agent comprising two reactive groups and Na2SO4, at 40C for 30 minutes. Then NaOH (3%), -~
Na2CO3 (4%) or a mixture of NaOH, Na2CO3 (4% Na2CO3 and 0,2 g/1 - -NaOH) were added for the fixation of the textile agent. After another 60 minutes at 40C the fibres were washed several times, in order to remove the textile agent not fixed to the '~
fibre. Then the washed fibres were treated for 30 minutes with an aqueous buffer, then again washed with water (for 15 minutes) and dried at 60C. Afterwards the fibres were examined to determine their tendency to fibrillation and to determine ;~
other fibre parameters.
Evaluation of fibrillation The abrasion of the fibres among each other in washing processes and finishing processes in wet condition was ~
~imulated by the following test: 8 fibres with a length of 20 j ~ ;
mm e~ch were put into a 20 ml sample bottle with 4 ml of water and ~haken during 9 hours in a laboratory mechanical shaker of the RO-10 type of the company Gerhardt, Bonn (Germany), at atage 12. Afterwards the fibrillation behaviour of the fibres ~ ;
was evaluated by microscope, by means of counting the number of ;~;
fibril~ per 0,276 mm fibre length.
: -~
"; ',,, . .,- ::. ~. , :-Further fibre parameters The fibre tensile strength and fibre elongation at break were ~ ~ -te~ited following the BISFA rule on "Internationally agreed methods for tei3ting vi~cose, modal, cupro, lyocell, acetat and -~;
triacetat staple fibres and tows", edition 1993. ~ `~; o B) Examples .,;,.;~"~ ,,,. ".,~ ,, According to the above process, fibres were treated with the dye Remazol Black B and Remazol Red RB as textile agent (made ;
by Hoechst AG). The dye Remazol Black B carries two -vinylsulfone groups and the dye Remazol Red B earries one vinylsulfone group and one monochlorotriazine group.
The bath contained 3~ Remazol Black B and 0,5% Remazol Red RB
respectively. The pH of the bath was 4,6 in each example. The ~ ~
used aqueous buffer was an aqueous solution which contained 3% ~ ~ -acetic acid and 7~ sodium acetate. The p~ value of this solution was 4,6. After the treatment with the buffer, the fibres were washed with water for 15 minutes and afterwards ~ ~-examined. Table la indicates the fixing agent used in each case, the fibrillation (number of fibrilsi), the titer (dtex), the fibre strength ~cN/tex) and the fibre elongation at break (%). Examples 1, 2 and 3 were carried out with the dye Remazol `~
Black B and Example 4 with the dye Remazol Red RB.
Table lb show~ the results of comparative tests carried out i without dye.
,, ,! i , ! ' ,'" '.", , ' " ~ " ~' '''` "~i ' '' ' ;', ~' ; ~' "''``,' , ~ "~.
21~7232 ~;
Table la (Textile Agent) Ex. Fixing agent Fibrils Titer Tensile Strength Elongation 1 NaOH 22 1,82 28,81 11,14 . , .;.
2 Na2CO~ 2 2,07 26,39 10,67 3 NaOH+Na~CO~ 0 2,34 24,94 10,04 _ , .. ~ . .. .
4 NaOH+Na~CO3 5 2,34 30,00 11,74 . ~ ~ .
Table lb (Comparative Examples) ~ ~ ~
. -. ~
Ex. Fixing agent Fibrils Titer Tensile Strength Elongation ;~
Table lb (Comparative Examples) ~ ~ ~
. -. ~
Ex. Fixing agent Fibrils Titer Tensile Strength Elongation ;~
5 NaOH >60 1,80 33,76 12,71 ~ b.
6 Na~CO3 60 1,56 33,78 12,15 :~
7 NaOH+Na~CO3 >60 1,72 30,18 12,14 8 NaOH+Na2CO3 >60 1,72 32,00 12,70 ~ .
A comparison of the results of Tables la and lb shows that the ~. '`~' textile agent, in the present case the dyes Remazol Black B and Remazol Red RB, drastically reduces the tendency to fibrillation and that the combination of NaOH+Na2CO3, which is used for the fixation of the textile agent, also drastically further reduce~ the tendency to fibrillation.
It was shown that the above results are obtained also when u~ing other textile agents which comprise two reactive groups.
Thu~, Remazol Black B and Remazol Red RB may represent other :.
textile agents which also carry at least two reactive groups.
2) Treatment with textile agents and subsequent heat treatment ~:;
1 g of each of the fibres produced according to the above process was impregnated in 190 ml of a bath (containing 0,2% ~ :
Remazol Black B, 2% Na2CO3, 0,2% NaOH, pH a 11,53 three times for 30 ~econds each, the fibres being squeezed off after each impregnation. Afterwards, each sample was heat-treated twice for 40 seconds in each case in a circulating-air oven at 180C. ; `~`
Subsequently, each heat-treated sample was treated for 30 minutes with the above mentioned acetate buffer (pH = 4,6), : .
''. '.,';:'';,~,' ,'.
washed with water for 15 minutes, dried at 60C and examined.
The results are shown in Table 2, Example 10 representing a Control Sample (for Example 10, Example 9 was repeated without using a textile agent).
Table 2 ¦ Ex. ¦ Fibrils ¦Titer¦Tensile Strength¦Elongation~
A comparison of the results of Tables la and lb shows that the ~. '`~' textile agent, in the present case the dyes Remazol Black B and Remazol Red RB, drastically reduces the tendency to fibrillation and that the combination of NaOH+Na2CO3, which is used for the fixation of the textile agent, also drastically further reduce~ the tendency to fibrillation.
It was shown that the above results are obtained also when u~ing other textile agents which comprise two reactive groups.
Thu~, Remazol Black B and Remazol Red RB may represent other :.
textile agents which also carry at least two reactive groups.
2) Treatment with textile agents and subsequent heat treatment ~:;
1 g of each of the fibres produced according to the above process was impregnated in 190 ml of a bath (containing 0,2% ~ :
Remazol Black B, 2% Na2CO3, 0,2% NaOH, pH a 11,53 three times for 30 ~econds each, the fibres being squeezed off after each impregnation. Afterwards, each sample was heat-treated twice for 40 seconds in each case in a circulating-air oven at 180C. ; `~`
Subsequently, each heat-treated sample was treated for 30 minutes with the above mentioned acetate buffer (pH = 4,6), : .
''. '.,';:'';,~,' ,'.
washed with water for 15 minutes, dried at 60C and examined.
The results are shown in Table 2, Example 10 representing a Control Sample (for Example 10, Example 9 was repeated without using a textile agent).
Table 2 ¦ Ex. ¦ Fibrils ¦Titer¦Tensile Strength¦Elongation~
9 24 1,S6 33,78 I 12,15 ~`
10 >57 1,80 33,76 1 12,71 3 From table 2 it can be seen that a heat treatment of the fibres impregnated with the textile agent drastically reduces the impregnation time, a~ well as the tendency to fibrillation is -reduced.
With the dye Remazol Red RB, similarly good results could be j~
attained.
3. Treatment with textile agents and subsequent irradiation with microwaves ~ ~H
10 g of the fibres produced according to the above process were -~ .,`",,:":~:,,!,~"j~", lmprognated in a 900 ml bath (10% Remazol Black B, 10% Na2SO4, 8% Na2CO3; the pH wa~ adjusted with NaOH to 11,5) for 9 minutes. Afterwards, the fibres were squeezed off and divided into 2 parts of equal amount (Examples 12, 13). Example 11 was a Control Sample, indicating the properties of the fibres not treated with a textile agent. For Examples 12 and 13, the fibrés were ~quéezed offlafterlimpregnation with the bath,land they either were heated to 180C for 180 seconds (Example 12) ;;~
or irradiated with 90 watt microwave~ for 50 seconds (Example 13). Afterward~, the fibres were treated for 30 minutes in the ~ -above acetate buffer at a pH of 4,6, washed with water for 15 ~;~
minutes and dried at 60C. The results of the tests are Yhown ln Table 3. ~
. - . ..
,",~.",:~
21372~2 9 ..~. ,: ,.
. ,~. .
Table 3 - .- ~ ~ .
Ex.Heating Fibrils Titer Tensile Strength Elongation 11 ___ 56 1,83 31,98 11,52 _ .
With the dye Remazol Red RB, similarly good results could be j~
attained.
3. Treatment with textile agents and subsequent irradiation with microwaves ~ ~H
10 g of the fibres produced according to the above process were -~ .,`",,:":~:,,!,~"j~", lmprognated in a 900 ml bath (10% Remazol Black B, 10% Na2SO4, 8% Na2CO3; the pH wa~ adjusted with NaOH to 11,5) for 9 minutes. Afterwards, the fibres were squeezed off and divided into 2 parts of equal amount (Examples 12, 13). Example 11 was a Control Sample, indicating the properties of the fibres not treated with a textile agent. For Examples 12 and 13, the fibrés were ~quéezed offlafterlimpregnation with the bath,land they either were heated to 180C for 180 seconds (Example 12) ;;~
or irradiated with 90 watt microwave~ for 50 seconds (Example 13). Afterward~, the fibres were treated for 30 minutes in the ~ -above acetate buffer at a pH of 4,6, washed with water for 15 ~;~
minutes and dried at 60C. The results of the tests are Yhown ln Table 3. ~
. - . ..
,",~.",:~
21372~2 9 ..~. ,: ,.
. ,~. .
Table 3 - .- ~ ~ .
Ex.Heating Fibrils Titer Tensile Strength Elongation 11 ___ 56 1,83 31,98 11,52 _ .
12 180 sec.;180C 11 1,91 23,70 9,77 ~ ;
, ., 13 50 sec.; 90 W 7 1,92 31,23 11,34 From Table 3 it can be seen that the irradiation with microwaves further reduces the heating time, the tendency to fibrillation being still further reduced. Similarly good results in terms of a reduced tendency to fibrillation were obtained, when instead of Remazol Black B other textile agents with at least two reactive groups were used. Particularly it was shown that the positive effect upon the tendency to - ,~;-fibrillation is similarly pronounced as with glyoxal. ~ ~
Furthermore it was shown that the above positive effect brought - ~ ;
about by irradiation with microwaves can also be observed with ~ ~ -: , .-. ..
glyoxal and other dialdehydes, as can be deduced from the ; ~-following example.
2 g of fibres produced according to the process described in section 1 were impregnated twice for 3 minutes each with 140 ml of a bath, containing 2% glyoxal and 0,66% crosslinking catalyst (for example Condensol FB, a mixture of ZnCl2 and MgClz, made by BASF). Afterwards, the fibres were squeezed off 4nd divided into 2 parts (Examples 15, 16). Example 14 was a Control Sample, for Example 15 the fibres were treated for 10 minutes in a circulating-air oven at 100C, and for Example 16 the fibres were subjected to a power of 500 watt by means of a microwave. The fibrillation results are indicated in the i ;
following Table 4. -The above methode was repeated, using glutardialdehyde ~3,4%) instead of glyoxal. The fibrillation results of the obtained fibres are also reflected in Table 4 (Examples 17, 18 and 19 corre~pond to Examples 14, 15 and 16 respectively). ;
:: ~ ;.:
-` 21~7232 ;
--1 0-- , " ~, Table 4 Exam~leTextile agent Treatment Fibrils . ,.
_14 ____ ____ 35,5 15 _Glyoxal 10 min.; 100C 24,0 -~
~ - . . - -16 Glvoxal 60 sec.; 500w 8,5 17 _ ____ 35,5 _ 18Glutardialdehyde10 min.; 100C 10,5 19Glutardialdehyde60 sec.; 500 w _ 21,0 ~
~ .:
''' ~ ',' '"''','":,i'';' ''".,` ~',.'~' '~''`'''"
` ~; ,' ', ,, ',,'',''
, ., 13 50 sec.; 90 W 7 1,92 31,23 11,34 From Table 3 it can be seen that the irradiation with microwaves further reduces the heating time, the tendency to fibrillation being still further reduced. Similarly good results in terms of a reduced tendency to fibrillation were obtained, when instead of Remazol Black B other textile agents with at least two reactive groups were used. Particularly it was shown that the positive effect upon the tendency to - ,~;-fibrillation is similarly pronounced as with glyoxal. ~ ~
Furthermore it was shown that the above positive effect brought - ~ ;
about by irradiation with microwaves can also be observed with ~ ~ -: , .-. ..
glyoxal and other dialdehydes, as can be deduced from the ; ~-following example.
2 g of fibres produced according to the process described in section 1 were impregnated twice for 3 minutes each with 140 ml of a bath, containing 2% glyoxal and 0,66% crosslinking catalyst (for example Condensol FB, a mixture of ZnCl2 and MgClz, made by BASF). Afterwards, the fibres were squeezed off 4nd divided into 2 parts (Examples 15, 16). Example 14 was a Control Sample, for Example 15 the fibres were treated for 10 minutes in a circulating-air oven at 100C, and for Example 16 the fibres were subjected to a power of 500 watt by means of a microwave. The fibrillation results are indicated in the i ;
following Table 4. -The above methode was repeated, using glutardialdehyde ~3,4%) instead of glyoxal. The fibrillation results of the obtained fibres are also reflected in Table 4 (Examples 17, 18 and 19 corre~pond to Examples 14, 15 and 16 respectively). ;
:: ~ ;.:
-` 21~7232 ;
--1 0-- , " ~, Table 4 Exam~leTextile agent Treatment Fibrils . ,.
_14 ____ ____ 35,5 15 _Glyoxal 10 min.; 100C 24,0 -~
~ - . . - -16 Glvoxal 60 sec.; 500w 8,5 17 _ ____ 35,5 _ 18Glutardialdehyde10 min.; 100C 10,5 19Glutardialdehyde60 sec.; 500 w _ 21,0 ~
~ .:
''' ~ ',' '"''','":,i'';' ''".,` ~',.'~' '~''`'''"
` ~; ,' ', ,, ',,'',''
Claims (12)
1. A process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres and the freshly spun fibres are contacted with a textile agent, which carries at least two reactive groups, and are washed with an aqueous buffer, provided that as a textile agent glyoxal is not used.
2. A process according to Claim 1, characterized in that as a textile agent a dye or a colourless substance is used.
3. A process according to Claim 1 or 2, characterized in that a textile agent is used which carries at least one vinylsulfone group as reactive group.
4. A process according to one of the Claims 1 to 3, characterized in that the freshly spun fibres are contacted with the textile agent in an aqueous alkaline medium.
5. A process according to Claim 4, characterized in that an alkali carbonate and an alkali hydroxide is chosen as the alkaline medium.
6. A process according to one or more of the Claims 1 to 5, characterized in that the fibres contacted with the textile agent are heat-treated.
7. A process for the production of cellulose fibres having a reduced tendency to fibrillation, in which a solution of cellulose in a tertiary amine-oxide is spun into fibres and the freshly spun fibres are contacted with a textile agent, which carries at least two reactive groups, and heat-treated, characterized in that the heat treatment is carried out by irradiation with electromagnetic waves.
8. A process according to Claim 7, characterized in that as a textile agent a dye or a colourless substance is used.
9. A process according to Claim 7 or 8, characterized in that a textile agent is used which carries at least one vinylsulfone group as reactive group.
10. A process according to one of the Claims 7 to 9, characterized in that the freshly spun fibres are contacted with the textile agent in an alkaline medium.
11. A process according to Claim 10, characterized in that the alkaline medium is formed by an alkali carbonate and an alkali hydroxide.
12. A process according to one or more of the Claims 7 to 11, characterized in that the heat treatment is carried out by means of microwaves.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT78793 | 1993-04-21 | ||
| ATA787/93 | 1993-04-21 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA2137232A1 true CA2137232A1 (en) | 1994-10-27 |
Family
ID=3499747
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002137232A Abandoned CA2137232A1 (en) | 1993-04-21 | 1994-04-20 | Method of producing cellulose fibres with a decreased tendency to fibrillation |
Country Status (27)
| Country | Link |
|---|---|
| EP (1) | EP0647281A1 (en) |
| JP (1) | JP2753396B2 (en) |
| KR (1) | KR0183419B1 (en) |
| CN (1) | CN1041948C (en) |
| AU (1) | AU684274B2 (en) |
| BG (1) | BG63049B1 (en) |
| BR (1) | BR9405150A (en) |
| CA (1) | CA2137232A1 (en) |
| CH (1) | CH685944A5 (en) |
| CZ (1) | CZ303094A3 (en) |
| DE (1) | DE4492198D2 (en) |
| FI (1) | FI945695A7 (en) |
| GB (1) | GB2284177B (en) |
| HR (1) | HRP940261A2 (en) |
| HU (1) | HU214882B (en) |
| LV (1) | LV11194B (en) |
| MD (1) | MD906C2 (en) |
| NZ (1) | NZ263770A (en) |
| PL (1) | PL176125B1 (en) |
| RO (1) | RO112768B1 (en) |
| RU (1) | RU2127775C1 (en) |
| SK (1) | SK152994A3 (en) |
| TR (1) | TR27503A (en) |
| TW (1) | TW257811B (en) |
| UA (1) | UA32560C2 (en) |
| WO (1) | WO1994024343A1 (en) |
| ZA (1) | ZA942727B (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2307203B (en) * | 1993-04-21 | 1997-09-10 | Chemiefaser Lenzing Ag | Process for the production of cellulose fibres having a reduced tendency to fibrillation |
| AT401271B (en) * | 1993-07-08 | 1996-07-25 | Chemiefaser Lenzing Ag | METHOD FOR PRODUCING CELLULOSE FIBERS |
| ATA249893A (en) * | 1993-12-10 | 1994-12-15 | Chemiefaser Lenzing Ag | METHOD FOR PRODUCING CELLULOSIC MOLDED BODIES AND MOLDED OR. SPIDING MASS |
| GB9407496D0 (en) * | 1994-04-15 | 1994-06-08 | Courtaulds Fibres Holdings Ltd | Fibre treatment |
| GB9408742D0 (en) * | 1994-05-03 | 1994-06-22 | Courtaulds Fibres Holdings Ltd | Fabric treatment |
| ES2120243T5 (en) * | 1994-12-02 | 2006-11-16 | NEWCELL GMBH & CO. KG | PROCEDURE FOR THE PRODUCTION OF CELLULOSED MOLDED BODIES AND A SPIN OF CELLULOSIC FILAMENTS. |
| AT403296B (en) * | 1995-08-11 | 1997-12-29 | Chemiefaser Lenzing Ag | METHOD FOR PRODUCING A CELLULOSE MOLDED BODY |
| CA2247423A1 (en) | 1996-03-06 | 1997-09-12 | Mitsubishi Rayon Co., Ltd. | Fibril based fibers, method of manufacturing same, spinning nozzle used in same, and moldings obtained therefrom |
| AT409144B (en) * | 1996-06-21 | 2002-05-27 | Chemiefaser Lenzing Ag | METHOD FOR TREATING CELLULOSE FIBERS AND FORMS OF THESE FIBERS |
| DE19919259A1 (en) * | 1999-04-28 | 2001-01-11 | Thueringisches Inst Textil | Process for reducing the fibrillation tendency of cellulose fibers spun from solvents |
| AT507051B1 (en) | 2008-06-27 | 2015-05-15 | Chemiefaser Lenzing Ag | CELLULOSE FIBER AND METHOD FOR THE PRODUCTION THEREOF |
| WO2012137219A2 (en) | 2011-04-05 | 2012-10-11 | Grasim Industries Limited | A process for making fibril-free lyocell fabrics |
| TWI667378B (en) * | 2014-01-03 | 2019-08-01 | 奧地利商蘭精股份有限公司 | Cellulosic fibre |
| CN104005225B (en) * | 2014-06-05 | 2016-08-24 | 山东英利实业有限公司 | A kind of method reducing lyocell fiber cellulose fiber fibrillation tendency |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH402806A (en) * | 1961-12-22 | 1965-05-15 | Ciba Geigy | Process for dyeing and printing textile material with reactive dyes, using high-frequency alternating electrical fields |
| US4416698A (en) * | 1977-07-26 | 1983-11-22 | Akzona Incorporated | Shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent and a process for making the article |
| US4246221A (en) * | 1979-03-02 | 1981-01-20 | Akzona Incorporated | Process for shaped cellulose article prepared from a solution containing cellulose dissolved in a tertiary amine N-oxide solvent |
| GB9022175D0 (en) * | 1990-10-12 | 1990-11-28 | Courtaulds Plc | Treatment of fibres |
| GB9103297D0 (en) * | 1991-02-15 | 1991-04-03 | Courtaulds Plc | Fibre production method |
| GB9109091D0 (en) * | 1991-04-25 | 1991-06-12 | Courtaulds Plc | Dyeing |
| GB9122318D0 (en) * | 1991-10-21 | 1991-12-04 | Courtaulds Plc | Treatment of elongate members |
| JP5517153B2 (en) | 2007-12-26 | 2014-06-11 | 塩野義製薬株式会社 | Glycopeptide antibiotic glycosylated derivatives |
-
1994
- 1994-04-06 TR TR00308/94A patent/TR27503A/en unknown
- 1994-04-06 TW TW083102969A patent/TW257811B/zh active
- 1994-04-20 BR BR9405150A patent/BR9405150A/en not_active Application Discontinuation
- 1994-04-20 HR HRA-787/93A patent/HRP940261A2/en not_active Application Discontinuation
- 1994-04-20 HU HU9403717A patent/HU214882B/en not_active IP Right Cessation
- 1994-04-20 SK SK1529-94A patent/SK152994A3/en unknown
- 1994-04-20 WO PCT/AT1994/000049 patent/WO1994024343A1/en not_active Application Discontinuation
- 1994-04-20 RU RU94046330A patent/RU2127775C1/en active
- 1994-04-20 CA CA002137232A patent/CA2137232A1/en not_active Abandoned
- 1994-04-20 UA UA94129226A patent/UA32560C2/en unknown
- 1994-04-20 PL PL94306801A patent/PL176125B1/en unknown
- 1994-04-20 DE DE4492198T patent/DE4492198D2/en not_active Expired - Fee Related
- 1994-04-20 KR KR1019940704628A patent/KR0183419B1/en not_active Expired - Fee Related
- 1994-04-20 CZ CZ943030A patent/CZ303094A3/en unknown
- 1994-04-20 FI FI945695A patent/FI945695A7/en unknown
- 1994-04-20 RO RO94-01951A patent/RO112768B1/en unknown
- 1994-04-20 AU AU64992/94A patent/AU684274B2/en not_active Ceased
- 1994-04-20 ZA ZA942727A patent/ZA942727B/en unknown
- 1994-04-20 GB GB9424722A patent/GB2284177B/en not_active Expired - Fee Related
- 1994-04-20 CN CN94190217A patent/CN1041948C/en not_active Expired - Fee Related
- 1994-04-20 NZ NZ263770A patent/NZ263770A/en unknown
- 1994-04-20 JP JP6522531A patent/JP2753396B2/en not_active Expired - Lifetime
- 1994-04-20 EP EP94912409A patent/EP0647281A1/en not_active Withdrawn
- 1994-04-20 CH CH387394A patent/CH685944A5/en not_active IP Right Cessation
- 1994-07-11 MD MD94-0168A patent/MD906C2/en active IP Right Grant
- 1994-11-24 LV LVP-94-223A patent/LV11194B/en unknown
- 1994-12-02 BG BG99236A patent/BG63049B1/en unknown
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