DE1469111A1 - Improved Highly Crystalline Polyolefin Filaments and Processes for Their Production - Google Patents
Improved Highly Crystalline Polyolefin Filaments and Processes for Their ProductionInfo
- Publication number
- DE1469111A1 DE1469111A1 DE19621469111 DE1469111A DE1469111A1 DE 1469111 A1 DE1469111 A1 DE 1469111A1 DE 19621469111 DE19621469111 DE 19621469111 DE 1469111 A DE1469111 A DE 1469111A DE 1469111 A1 DE1469111 A1 DE 1469111A1
- Authority
- DE
- Germany
- Prior art keywords
- threads
- heated
- mixtures
- spinneret
- crystalline polyolefins
- 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.)
- Pending
Links
Classifications
-
- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
- D01D5/00—Formation of filaments, threads, or the like
- D01D5/08—Melt spinning methods
- D01D5/084—Heating filaments, threads or the like, leaving the spinnerettes
-
- 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
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
-
- 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
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/04—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
- D01F6/06—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins from polypropylene
Landscapes
- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Artificial Filaments (AREA)
Description
DR.-ING. VON KREISLER DR.-ING. SCHÖNWALD 1469111 Dt.-ING. TH. MiYER DR. FUESDR.-ING. BY KREISLER DR.-ING. SCHÖNWALD 1469111 Dt.-ING. TH. MiYER DR. FUES
Montecatinl SooietA Generale per l'Induatrla Mlneraria e Chimica, 1-2 Largo Quldo Donegani,"Mailand (Italien)Montecatinl SooietA Generale per l'Induatrla Mlneraria e Chimica, 1-2 Largo Quldo Donegani, "Milan (Italy)
Verbesserte Fäden aus hochkristallinen PolyolefinenImproved threads made from highly crystalline polyolefins
Die Erfindung betrifft verbesserte, besonders zugfeste Mono- und Plurifile aus kristallinen Olefinpolymeren, insbesondere aus mit stereospezifischen Katalysatoren hergestelltem Polypropylen sowie ein Verfahren zu ihrer Gewinnung.The invention relates to improved, particularly high-tensile mono- and plurifiles made from crystalline olefin polymers, in particular from polypropylene produced with stereospecific catalysts and a process for their production.
In früheren Vorschlägen ist die Herstellung von Mono- und Plurifilen durch Auspressen von Olefinpolymeren, insbesondere Polypropylen, im geschmolzenen Zustand bereits beschrieben. Die nach den bekannten Verfahren erhaltenen Mono- und Plurifile besitzen bereits eine beträchtliche Zugfestigkeit, die jedooh im allgemeinen nicht über 6 bis 7 g/den liegt.In previous proposals, the manufacture of mono- and plurifiles by extrusion of olefin polymers, in particular Polypropylene, already described in the molten state. The mono- and plurifiles obtained by the known processes already have a considerable tensile strength which, however, generally does not exceed 6 to 7 g / den.
Es wurde nun überraschenderweise gefunden, daß polyolefinische Mono- und Plurifile sehr hoher Zugfestigkeit und norma-It has now surprisingly been found that polyolefinic Mono- and Plurifile very high tensile strength and normal
' ler Dehnung dadurch erhalten werden können, daß man kristalline Polyolefine, insbesondere im wesentlichen aus isotaktisehen Makromolekülen bestehendes Polypropylen mit einer Grenzviskosität /JqJ zwischen 2 und 5, die im geschmolzenen Zustand durch eine Spinndüse mit eines Länge/Durohmesser Verhältnis vorzugsweise größer als 1 ausgepreßt wurden, als Fäden beim Verlassen der Spinndüse durch.eine auf 130° bis 30O0C erhitzte rohrförmige Vorrichtung, die unmittelbar hin-'Ler elongation can be obtained by crystalline polyolefins, in particular polypropylene consisting essentially of isotactic macromolecules with an intrinsic viscosity / JqJ between 2 and 5, which were pressed in the molten state through a spinneret with a length / diameter ratio preferably greater than 1 , as threads when leaving the spinneret through a tubular device heated to 130 ° to 30O 0 C, which is immediately
809808/0664809808/0664
IntorlIntorl
ter der Spinndüse angeordnet 1st und einen 2 bis 5 om grösseren Durchmesser als den SplnndUsendurohmesser und «Ine · Länge von 2 cm bis 1 m hat, leitet und danach aufwlokelt.is arranged behind the spinneret and is 2 to 5 µm larger in diameter than the SplnndUsendurohmesser and «Ine · Has a length of 2 cm to 1 m, directs and then curls up.
Das erfindungsgemäße Verfahren kann sowohl auf Polyolefine, insbesondere Polypropylen, als auch auf Mischungen von Polyolefinen mit beispielsweise Färbemodifikatoren, Stabilisatoren, Mattierungsmitteln, Pigmenten oder Farbstoffen angewendet werden.The process according to the invention can be applied both to polyolefins, in particular polypropylene, and to mixtures of polyolefins with, for example, color modifiers, stabilizers, matting agents, pigments or dyes.
Als Färbemodifikatoren werden vorzugsweise durch Kondenaation von Epichlorhydrin mit Aminen erhaltene basische Stick stoffverbindungen verwendet, während als Stabilisator eine aus 0,02 bis 2 Gew.^, bezogen auf das Polymere, eines aliphatischen Thloesters, einem Dialkylphenolsulfld und Caloiurastearat bestehendes Gemisch bevorzugt wird.Basic sticks obtained by condensation of epichlorohydrin with amines are preferably used as color modifiers Substance compounds are used, while the preferred stabilizer is a mixture consisting of 0.02 to 2 wt.
Die ausgepreßten Fäden werden danach mit Streckverhältnissen zwischen 1:2 und 1:10 bei Temperaturen zwischen 80° bis 150°C in mit Heißluft, Dampf oder einem ähnlichen Medium beheizten Streckvorrichtungen oder über einer erhitzten Platte verstreckt.The extruded threads are then stretched in ratios between 1: 2 and 1:10 at temperatures between 80 ° and 150 ° C in stretching devices heated with hot air, steam or a similar medium or over a heated plate stretched.
Nach dem Verstrecken können die Fäden thermischen Formstabilisieru-ngsbehandlungen unter Bedingungen einer freien oder gehinderten Schrumpfung sowie üblichen Bndbehandlungen unterworfen werden.After stretching, the threads can undergo thermal shape stabilization treatments under free conditions or hindered shrinkage as well as conventional band treatments.
Auf die aus Mischungen von Polyolefinen mit Färbemodifikatoren erhaltenen Fäden kann man außerdem vor oder naoh dem Verstrecken beispielsweise Formaldehyd, Diisocyanate oder Diepoxyverbindungen einwirken lassen.The threads obtained from mixtures of polyolefins with color modifiers can also be used before or after the Stretching, for example, let formaldehyde, diisocyanates or diepoxy compounds act.
Die Erfindung wird in den folgenden,tabellarisch zusammengestellten Beispielen erläutert. Beispiel 6 zeigt die krI-The invention is illustrated in the following examples, which are compiled in tabular form. Example 6 shows the
809808/0664809808/0664
tlsohe Grenze der erfindungsgemäßen Behandlung. Überraschenderweise wurde festgestellt, daß eine Behandlung unterhalb 1500C in merklicher Weise die Zugfestigkeit der Polypropylenfasern herabsetzt.This is the same limit of the treatment according to the invention. Surprisingly, it was found that a treatment below 150 ° C. noticeably reduces the tensile strength of the polypropylene fibers.
46911:146911: 1
Zusammensetzung der MischungComposition of the mixture
a) Polypropylen #a) polypropylene #
Grenzviskosität (bestimmt in Tetra· hydronaphthalin bei 130 )Limiting viscosity (determined in tetrahydronaphthalene at 130)
AschegehaltAsh content
Rückstand nach HeptanextraktionResidue after heptane extraction
b) Caloiumstearat
o) Stabilisator i» b) caloium stearate
o) stabilizer i »
LaurylthiodipropionatLauryl thiodipropionate
4,41-Thiobis-3~tert♦butyl-metacresol Spinnbedingungen: Schneokentemperatur4,41-thiobis-3-tert-butyl-metacresol Spinning conditions: snail temperature
Spinnkopftemperatur S pinndüs ent emperatur SpinndüsentypSpinning head temperature Pin nozzle ent emperature Spinneret type
Temperatur der erhitzten rohrförmigen Vorrichtung unterhalb der1 SpinndüseTemperature of the heated tubular device below the 1 spinneret
Maximaldruok (kg/cm )Maximum pressure (kg / cm)
Aufwickelgesohwindigkeit (m/Minute;Take-up speed (m / minute;
Streekbedingungen:TemperaturStreek conditions: temperature
Mediummedium
Streckverhältnis Eigenschaften der vorstreckten Paser:Stretch ratio Properties of the pre-stretched fibers:
Zugfestigkeit (g/den)Tensile strength (g / den)
Sehnung (jt)Tendon (jt)
230° 235° 285° 40/0,8x16 mn230 ° 235 ° 285 ° 40 / 0.8x16 mn
160° 30160 ° 30
600
130° Dampf It 8,3600
130 ° steam It 8.3
9
189
18th
-S--S-
80 9808/06 6480 9808/06 64
Claims (7)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT1572361 | 1961-08-29 |
Publications (1)
Publication Number | Publication Date |
---|---|
DE1469111A1 true DE1469111A1 (en) | 1968-11-14 |
Family
ID=11148181
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19621469111 Pending DE1469111A1 (en) | 1961-08-29 | 1962-08-27 | Improved Highly Crystalline Polyolefin Filaments and Processes for Their Production |
Country Status (7)
Country | Link |
---|---|
BE (1) | BE621817A (en) |
DE (1) | DE1469111A1 (en) |
ES (1) | ES280357A1 (en) |
FI (1) | FI40025C (en) |
GB (1) | GB941199A (en) |
NL (1) | NL282439A (en) |
SE (1) | SE305923B (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4193961A (en) * | 1978-04-04 | 1980-03-18 | Kling-Tecs, Inc. | Method of extruding polypropylene yarn |
-
0
- NL NL282439D patent/NL282439A/xx unknown
- BE BE621817D patent/BE621817A/xx unknown
-
1962
- 1962-08-24 FI FI155662A patent/FI40025C/en active
- 1962-08-24 GB GB3260762A patent/GB941199A/en not_active Expired
- 1962-08-27 DE DE19621469111 patent/DE1469111A1/en active Pending
- 1962-08-28 SE SE930362A patent/SE305923B/xx unknown
- 1962-08-28 ES ES0280357A patent/ES280357A1/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
SE305923B (en) | 1968-11-11 |
FI40025B (en) | 1968-05-31 |
ES280357A1 (en) | 1963-03-16 |
BE621817A (en) | |
GB941199A (en) | 1963-11-06 |
NL282439A (en) | |
FI40025C (en) | 1968-09-10 |
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