[0001] The subject of the present invention is a process for the production of nanofibres
with a diameter below 500 nm, in electrostatic field.
[0002] A process for the formation of fibres from a spinning solution of cellulose acetate
in the mixture of acetone and ethyl alcohol in electrostatic field is known from
Patent Specification U.S. 1 975 504. The spun fibres are collected on a moving metallic tape.
[0003] There are known processes for the production of nanofibres with a diameter below
500 nm from synthetic polymers consisting in preparing a spinning solutions of synthetic
polymers in organic and inorganic volatile solvents and feeding it by means of a metallic
or glass capillary, linked to a current source, onto earthed electrodes with various
shapes placed in some distance from the capillary. The polymer solution flowing out
from the capillary is drawn in electrostatic field between the capillary and the earthed
electrode. The solvent is evaporated during fibre spinning, while the resultant fibres
are deposited on the earthed electrode in the form of a non-woven. These processes
are known from the following Patent Specifications:
U.S. 4 345 414,
U.S. 6 106 913,
WO 2004/016839A1,
U.S. 4 689 186,
U.S. 4 323 525 as well as from the journals:
Polymer 42, 9955-99667 (2001) and
Journal of Electrostatics 35, 151-160 (1995).
[0004] There are also known processes for the production of nanofibres with a diameter below
500 nm from melted polymers consisting in feeding polymer melt by means of a metallic
capillary linked to a current source to electrostatic field between the capillary
and the earthed electrode. The melt is drawn in electrostatic field to form a stream
that during cooling is solidified in the form of fibres deposited on the earthed electrode.
These processes are described in
Journal of Polymer Science: Polymer Physics Edition 1981, 19, 909-940.
The above processes of fibre formation in electrostatic field concern fibres spun
from polymer solutions in readily volatile solvents or from melted polymers.
[0005] There is also known from Patent Application P-362101 a process for the production
of nanofibres from solutions of natural polymers in non-volatile solvents, preferably
from cellulose solution in N-methylmorpholine-N-oxide, in electrostatic field generated
between a metallic capillary, feeding the spinning solution, linked to a current source,
and an earthed electrode placed under it or between an electrode linked to a current
source and, place inside the feeding capillary and the earthed electrode. Nanofibres
formed in electric field from polymer solutions in non-volatile solvents contain large
quantities of solvent and show a strong tendency towards sticking and changing shape.
[0006] The process for the production of nanofibres with a diameter below 500 nm, consisting
in preparing a spinning solution of natural polymer in a non-volatile solvent, especially
of cellulose in N-methylmorpholine-N-oxide, feeding this solution by means of a metallic
capillary, linked to a current source, to electrostatic field in which fibres are
formed from the solution, winding the resultant fibres onto a take-up device, according
to the present invention, is characterised by the fact that these fibres are formed
in electrostatic field generated between a feeding capillary and placed under it moving
coagulation bath linked to earth, followed by transporting the formed fibres on the
surface of the moving coagulation bath to remove the non-volatile solvent and to solidify
the fibres, which are finally taken-up in a usual way by a rotating drum or a tape
moving on rotating rollers. As a coagulation bath, water containing an addition of
a surface-active agent is preferably used, and besides as a coagulation bath there
is used water, water with an addition of solvent, volatile solvents.
[0007] In a modification of the process according to the invention, fibres are formed in
electrostatic field generated between a feeding capillary and placed under it, rotationally
mounted, metallic structure linked to earth. The formed fibres are led into a space
between elements of this structure, where fibres are subjected to the coagulating
action of a hot steam stream and finally the coagulated fibres are taken up.
[0008] In a further modification of the process according to the invention, fibres are formed
in electrostatic filed generated between a feeding capillary and moving under it woven
fabric, beneath which is placed an earthed and cooled electrode. The formed fibres
are directed onto the moving fabric, where they are coagulated with a hot stream of
steam first and then with a water stream that rinses off the solvent; finally, the
coagulated fibres are taken up.
[0009] The nanofibres produced by the process according to the present invention contain
no solvent and show no tendency towards sticking and changing shape.
[0010] The process according to the invention is illustrated by the below given examples
with reference to Figures from 1 to 14 that show the schemes of equipment an fragments
of equipment used to form the fibres in particular examples. The parts mentioned in
the examples mean parts by weight.
Example I.
[0011] A spinning solution was prepared from 1 part of cellulose with a degree of polymerisation
(DP) of about 800 in 35 parts of N-methylmorpholine-N-oxide (NMMO) and 6.5 parts of
water with 0.1 parts of a stabiliser. This solution was placed in container
2 of the feeding device shown in Fig. 1, heated to 105°C, terminated with a metallic
capillary
1 with a diameter of 0.4 mm linked to current source
3 under a voltage of 6 kV. The solution was fed by means of capillary
1 to electrostatic field generated between capillary
1 and placed under it earthed tub
4 containing a coagulating bath. The distance between capillary
1 and bath
4 was 10 cm. The stream of polymer solution drawn in electrostatic field and cooled
was directed onto the surface of coagulation bath
4 consisting of water with an addition of a surface-active agent at a temperature of
10°C. In bath
4, the solvent is rinsed off and fibres are solidified. The reduced rate of taking off
fibres from bath
4 brings about the formation, on its surface, of a cellulose film composed from fibres
with a thickness of 150 nm.
Example II.
[0012] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 16.0 parts of NMMO and 3.0 parts of water with 0.1 part of a stabiliser. This solution
was placed in container
2 of the feeding device shown in Fig.2, heated to 125°C, terminated with metallic capillary
1 with a diameter of 0.6 mm linked to current source
3 under a voltage of 17 kV. The solution was fed be means of capillary
1 into electrostatic field generated between capillary
1 and placed under it earthed tub with flowing through it coagulating bath
4. The tub was equipped with rotating drum
5. The distance between capillary
1 and bath
4 was 12 cm. The drawn in electrostatic field and cooled stream of polymer solution
was directed onto the surface of flowing coagulation bath
4 consisting of water containing a surface-active agent, cooled down to a temperature
of 5°C. In bath
4, the solvent was rinsed off and fibres were solidified. Then, the formed fibres in
the form of tow
6 were wound on drum
5 pulling the fibres out from the surface of bath
4, which prevented the formation of cellulose film on the surface of bath
4.
The produced nanofibres showed a thickness of 70 nm.
Example III.
[0013] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 30.4 parts of NMMO and 3.1 parts of water with 0.1 part of a stabiliser. The solution
was placed in contained
2 of the feeding device shown in Fig. 3, heated to a temperature of 116°C, terminated
with metallic capillary
1 with a diameter of 0.8 mm, linked to current source
3 under a voltage of 19 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and placed under it tub
5 containing coagulation bath
4. The distance between capillary
1 and bath
4 was 8 cm. In the bottom of bath
5 containing bath
4 was made hole
6 with attached to its edges earthed discharging stub pipe
7 (Fig. 4) that was cone-shaped in its upper part and its lower part was a section
of pipe with a diameter of 1 cm. On the internal surface of discharging stub pipe
7 a spiral guide was made. Drum
8 rotating both around its axis of rotation and along this axis was placed under stub
pipe
7. The drawn in electrostatic field and cooled stream of polymer solution was directed
onto the surface of coagulating bath
4 consisting of water containing a surface-active agent, cooled to a temperature of
25°C. In bath
4 the solvent was rinsed off and fibres were solidified, and then the formed nanofibres
with bath
4 flowed out into discharging stub pipe
7, in which they were twisted into a thread with a thickness of 1 cm by the guide and
wound uniformly on drum
8.
Example IV.
[0014] Nanofibres were formed from the spinning solution prepared as in Example III, using
the equipment as in Example III (Fig. 5) with a difference that the thread formed
by means of the guide in stub pipe
7 was taken up on tape
9 stretched on two rollers moving both around and along the rotation axis.
Example V.
[0015] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 35.5 parts of NMMO and 6.5 parts of water containing 0.1 parts of stabiliser and
0.2 parts of fullerenes. The solution was placed in container
2 of the feeding device shown in Fig. 6, heated to a temperature 115°C, terminated
with metallic capillary
1 with a diameter of 0.9 mm, linked to current source
3 under a voltage of 17 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and placed under it earthed tub
4 with coagulating bath
5 flowing through it. The distance between capillary
1 and bath
5 was equal to 8 cm. The stream of polymer solution, drawn in electrostatic field and
cooled, was directed onto the surface of flowing through tub
4 coagulating bath
5 in the form of a thin film of water containing a surface-active agent, at a temperature
of 20°C, in which the solvent was rinsed off and fibres were solidified. The resultant
nanofibres, together with bath
5 flowed out from tub
4 on the surface of rotating drum
6.
The produced nanofibres showed a thickness of 290 nm.
Example VI.
[0016] Nanofibres were formed from a spinning solution prepared as in Example V, in the
equipment as in Example V (Fig. 7) with the difference that the produced fibres together
with bath
5 flowed out from tub
4 onto the surface of tape
6 stretched on two rotating rollers.
Example VII.
[0017] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 35.5 parts of NMMO and 6.5 parts of water containing 0.1 part of stabiliser. The
solution was placed in container
2 of the feeding device shown in Fig. 8, heated to a temperature of 95°C, terminated
with metallic capillary
1 with a diameter of 0.4 mm linked to current source
3 under a voltage of 8 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and a stainless steel structure placed under it. This structure consisted of two
perpendicular frames
4 placed one in the other and linked to earth. The distance between capillary
1 and frames
4 was equal to 15 cm. The stream of polymer solution drawn in electrostatic field and
cooled was directed to the metallic structure and coagulated with hot steam
5 that removed the solvent and solidified the fibres. Steam was discharged from the
space of fibre formation through offtake
6. The solidified fibres were taken up by means of devices shown in Fig. 9.
The produced nanofibres showed a thickness of 160 nm.
Example VIII.
[0018] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 35.5 parts of NMMO and 6.0 parts of water containing 0.1 part of stabiliser. The
solution was placed in container
2 of the feeding device shown in Fig. 10, heated to a temperature of 98°C, terminated
with metallic capillary
1 with a diameter 0.4 mm linked to current source
3 under a voltage of 11 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and placed under it stainless steel structure composed of two rotating rings
4 situated in parallel and linked to earth. The distance between capillary
1 and rings
4 was equal to 16 cm. The stream of polymer solution drawn in electrostatic field and
cooled was directed onto the metallic structure and coagulated by hot steam
5 that removed the solvent and solidified the fibres, which were deposited within the
space between rings
4 (Fig. 11). Steam was discharged from the space of fibre formation through offtake
6.
The produced nanofibres showed a thickness of 120 nm.
Example IX.
[0019] Nanofibres were formed from a spinning solution as in Example VIII proceeding as
in Example VII with the difference that the stainless steel structure used was composed
of three rings situated in parallel and four rings situated in parallel (Fig. 12).
Example X.
[0020] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 26.5 parts of NMMO and 6.0 parts of water containing 0.1 parts of stabiliser and
0.18 parts of silica nanoparticles with a grain diameter of 9 nm. This solution was
placed in container
2 of the feeding device shown in Fig. 13, heated to a temperature of 105°C, terminated
with metallic capillary
1 with a diameter of 0.4 mm, linked to current source
3 under a voltage of 27 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and moving under it fabric
4, under which earthed and cooled electrode
5 was placed. The distance between capillary
1 and fabric
4 was equal to 12 cm. The stream of polymer solution drawn in electrostatic field and
cooled was directed onto moving fabric
4, on which it was coagulated first with hot steam stream
6 and then with stream
7 of rinsing solvent NMMO. The space of fibre formation was separated from the steam
blow-in zone with impermeable screen
8.
The produced nanofibres showed a thickness of 150 nm.
Example XI.
[0021] A spinning solution was prepared from 1 part of cellulose with a DP of about 800
in 35.5 parts of NMMO and 6.5 parts of water containing 0.1 parts of stabiliser and
0.15 parts of Fe
3O
4 with a grain diameter of 9nm. This solution was placed in container
2 of the feeding device shown in Fig. 14, heated to a temperature of 109°C, terminated
with metallic capillary
1 with a diameter of 0.6 mm, linked to current source
3 under a voltage of 12 kV. The solution was fed by means of capillary
1 into electrostatic field generated between capillary
1 and placed under it tub with flowing coagulating bath
4 composed of water and a surface-active agent cooled to a temperature of 23°C. Under
the surface of bath
4, earthed ring
5 was placed. The distance between capillary
1 and bath
4 was equal to 7 cm. The stream of polymer solution drawn in electric field and cooled
was directed onto the surface of coagulating bath
4 flowing through the tub where the solvent was rinsed off and the fibres were solidified.
The fibres formed on the surface of bath
4 were transported by means of rotating roller
6, placed under ring
5, onto roller
8 to take up the formed fibres in the form of tow
7. Rollers
6 and
8 rotated with a speed that ensured a continuous take-up of fibres from the surface
of bath
4.
The produced nanofibres showed a thickness of 350 nm.
1. Process for the production of nanofibres with a diameter below 500 nm, consisting
in preparing a spinning solution of a natural polymer in a non-volatile solvent, especially
cellulose in N-methylmorpholine-N-oxide, feeding this solution by means of a metallic
capillary linked to a current source to electrostatic field, in which the solution
is converted into fibres, winding the resultant fibres on a take-up device, characterised in that the fibres are formed in electrostatic field generated between the feeding capillary
and a placed under it flowing coagulating bath linked to earth, followed by transporting
the formed fibres on the surface of the flowing bath and finally collecting the coagulated
fibres in a known way on a rotating drum or a tape stretched on rotating rollers.
2. Process according to claim 1, characterised in that as a coagulating bath there is preferably used water containing an addition of a
surface-active agent, and besides as a coagulating bath there is used water, water
with an addition of solvent, volatile solvents.
3. Process for the production of nanofibres with a diameter below 500 nm, consisting
in preparing a spinning solution of a natural polymer in a non-volatile solvent, especially
cellulose in N-methylmorpholine-N-oxide, feeding this solution by means of a metallic
capillary linked to a current source to electrostatic field, in which the solution
is converted into fibres, winding the resultant fibres on a take-up device, characterised in that the fibres are formed in electrostatic field generated between the feeding capillary
and a placed under it rotating metallic structure linked to earth, followed by directing
the formed fibres into the space between the elements of this structure where fibres
are coagulated with a stream of hot steam and finally taken up.
4. Process for the production of nanofibres with a diameter below 500 nm, consisting
in preparing a spinning solution of a natural polymer in a non-volatile solvent, especially
cellulose in N-methylmorpholine-N-oxide, feeding this solution by means of a metallic
capillary linked to a current source to electrostatic field, in which the solution
is converted into fibres, winding the resultant fibres on a take-up device, characterised in that the fibres are formed in electrostatic field generated between the feeding capillary
and a moving under it woven fabric, under which is placed an earthed cooled electrode,
followed by directing the formed fibres on the moving fabric where they are coagulated
with a stream of hot steam first and then with a stream of liquid that rinses the
solvent off, the coagulated fibres being finally taken up.
1. Verfahren zur Herstellung von Nanofasern von Durchmesser unter 500 nm besteht in der
Anfertigung der Spinnlösung des natürlichen Polymers in nichtflüchtigen Lösungsmittel
insbesondere Zellulose in N-Methylmorpholin-N-oxid, in der Dosierung dieser Lösung
mittels der mit einer Stromquelle verbundenen Metalkapillare an elektrostatisches
Feld, in dem die Lösung in Fasern geformt wird, in der Aufwicklung der fertigen Fasern
auf eine Aufnahmevorrichtung, dadurch gekennzeichnet, dass die Fasern im elektrostatischen Feld geformt werden, das zwischen der Dosierkapillare
und dem darunter angelegten, mit Erdung verbundenen und sich verlagerten Koagulationsbad,
erzeugt wurde, danach werden die geformten Fasern auf die Oberfläche des sich verlagerten
Bades versetzt und anschließend werden koagulierte Fasern auf bekannte Weise auf drehende
Trommel oder auf ein auf drehenden Walzen auf gespanntes Band.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, dass als Koagulationsbad wird vorteilhaft das Wasser verwendet, das den Zusatz des oberflächenaktiven
Mittels enthält und überdies als Koagulationsbad werden Wasser, Wasser mit Zusatz
eines Lösungsmittels, flüchtige Lösungsmittel verwendet.
3. Verfahren zur Herstellung von Nanofasern von Durchmesser unter 500 nm besteht in der
Anfertigung einer Spinnlösung des natürlichen Polymers im nichtflüchtigen Lösungsmittel
insbesondere Zellulose in N-Methylmorpholin-N-oxid, in der Dosierung dieser Lösung
mittels der mit einer Stromquelle verbundenen Metalkapillare an elektrostatisches
Feld, in dem die Lösung in Fasern geformt wird, in der Aufwicklung der fertigen Fasern
auf eine Aufnahmevorrichtung, dadurch gekennzeichnet, dass die Fasern im elektrostatischen Feld geformt werden, das zwischen der Dosierkapillare
und dem darunter drehbar befestigten, mit Erdung verbundenen Metallkonstruktion, erzeugt
wurde, dann werden die geformten Fasern in den Raum zwischen Elementen dieser Konstruktion
eingeführt, wo sie der koagulierten Wirkung des heißen Wasserdampfstrahles unterzogen
werden und anschließend werden koagulierte Fasern aufgenommen.
4. Verfahren zur Herstellung von Nanofasern von Durchmesser unter 500 nm besteht in der
Anfertigung einer Spinnlösung des natürlichen Polymers im nichtflüchtigen Lösungsmittel
insbesondere Zellulose in N-Methylmorpholin-N-oxid, in der Dosierung dieser Lösung
mittels der mit einer Stromquelle verbundenen Metalkapillare an elektrostatisches
Feld, in dem die Lösung in Fasern geformt wird, in der Aufwicklung der fertigen Fasern
auf eine Aufnahmevorrichtung, dadurch gekennzeichnet, dass die Fasern im elektrostatischen Feld, geformt werden, das zwischen der Dosierkapillare
und dem sich darunter verschiebenden Gewebe, unter dem eine geerdete gekühlte Elektrode
angelegt ist, dann werden die geformten Fasern auf sich verschiebendes Gewebe eingeführt
und danach der koagulierten Wirkung zuerst des heißen Wasserdampfstrahles und dann
des Flüssigkeitstrahles, die das Lösungsmittel ausspült unterzogen werden und anschließend
werden die koagulierten Fasern aufgenommen.
1. Procèdè pour la production de nanofibres de diamètre de moins que 500 nm reposant
sur la préparation d'une solution de polymère naturel textile dans le solvant non
volatil, en particulier de la cellulose dans la N-méthylmorpholine-N-oxyde, sur le
dosage de ladite solution, à l'aide d'un capillaire en métal lié avec une source de
courant, au champ électrostatique dans lequel la solution est formée en fibres, sur
l'enroulement des fibres finis sur un dispositif récepteur, laquelle façon est caractérisée en ce que les fibres sont formés dans le champ électrostatique généré entre le capillaire de
dosage et le bain de coagulation qui est situé sous ledit capillaire et qui se déplace,
ledit bain est lié avec l'installation de mise à la terre, après quoi on déplace les
fibres formés sur la surface du bain qui se déplace et enfin on reçoit d'une façon
connue les fibres coagulés sur le tambour tournant ou sur le ruban tendu sur les rouleaux
tournants.
2. Procèdè selon une revendication No 1 est caractérisé en ce qu'on utilise pour le bain de coagulation l'eau contenant l'additif d'un agent tensioactif,
en plus pour le bain de coagulation on utilise l' eau, l'eau avec un solvant, les
solvants volatils.
3. Procèdè pour la production de nanofibres de diamètre de moins que 500 nm reposant
sur la préparation d'une solution de polymère naturel textile dans le solvant non
volatil, en particulier de la cellulose dans la N-méthylmorpholine-N-oxyde, sur le
dosage de ladite solution, à l'aide d'un capillaire en métal lié avec une source de
courant, au champ électrostatique dans lequel la solution est formée en fibres, sur
l'enroulement des fibres finis sur un dispositif récepteur, laquelle façon est caractérisée en ce que les fibres sont formés dans le champ électrostatique généré entre le capillaire de
dosage et une construction en métal fixée à pivot, située sous ledit capillaire et
liée avec l' installation de mise à la terre, après quoi on introduit les fibres formés
dans l'espace entre les éléments de cette construction où les fibres sont soumis à
l'action coagulatrice d'un jet de vapeur d'eau chaude et enfin on reçoit les fibres
coagulés.
4. Procèdè pour la production de nanofibres de diamètre de moins que 500 nm reposant
sur la préparation d'une solution de polymère naturel textile dans le solvant non
volatil, en particulier de la cellulose dans la N-méthylmorpholine-N-oxyde, sur le
dosage de ladite solution, à l'aide d'un capillaire en métal lié avec une source de
courant, au champ électrostatique dans lequel la solution est formée en fibres, sur
l'enroulement des fibres finis sur un dispositif récepteur, laquelle façon est caractérisée en ce que les fibres sont formés dans le champ électrostatique généré entre le capillaire de
dosage et un tissu se déplaçant sous ledit capillaire, sous lequel tissu est mise
une électrode mise à la terre et refroidie, après quoi on introduit les fibres formés
sur le tissu qui se déplace où les fibres sont premièrement soumis à l'action coagulatrice
d'un jet de vapeur d'eau chaude et ensuite à l'action d'un jet de liquide qui élimine
le solvant et enfin on reçoit les fibres coagulés.