EP0029949B1 - Verfahren zur Herstellung von querschnittstabilen, hygroskopischen Kern/Mantelstruktur aufweisenden Fasern und Fäden nach einem Trockenspinnprozess - Google Patents

Verfahren zur Herstellung von querschnittstabilen, hygroskopischen Kern/Mantelstruktur aufweisenden Fasern und Fäden nach einem Trockenspinnprozess Download PDF

Info

Publication number
EP0029949B1
EP0029949B1 EP80107098A EP80107098A EP0029949B1 EP 0029949 B1 EP0029949 B1 EP 0029949B1 EP 80107098 A EP80107098 A EP 80107098A EP 80107098 A EP80107098 A EP 80107098A EP 0029949 B1 EP0029949 B1 EP 0029949B1
Authority
EP
European Patent Office
Prior art keywords
solvent
spinning
polymer
filaments
fibers
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.)
Expired
Application number
EP80107098A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0029949A1 (de
Inventor
Ulrich Dr. Reinehr
Toni Herbertz
Hermann-Josef Jungverdorben
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer AG
Original Assignee
Bayer AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=6087029&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0029949(B1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Bayer AG filed Critical Bayer AG
Priority to AT80107098T priority Critical patent/ATE6275T1/de
Publication of EP0029949A1 publication Critical patent/EP0029949A1/de
Application granted granted Critical
Publication of EP0029949B1 publication Critical patent/EP0029949B1/de
Expired legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/18Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated nitriles, e.g. polyacrylonitrile, polyvinylidene cyanide
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/24Formation of filaments, threads, or the like with a hollow structure; Spinnerette packs therefor
    • D01D5/247Discontinuous hollow structure or microporous structure
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • D01D5/34Core-skin structure; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/08Addition of substances to the spinning solution or to the melt for forming hollow filaments
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00Stock material or miscellaneous articles
    • Y10T428/29Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
    • Y10T428/2913Rod, strand, filament or fiber
    • Y10T428/2973Particular cross section
    • Y10T428/2975Tubular or cellular

Definitions

  • threads and fibers obtainable by this process have the round or oval cross-sectional shapes expected for a wet-spun product.
  • threads and fibers with such cross sections can only be obtained if certain conditions are met which again influence the desired water absorption capacity. Threads and fibers with round to oval cross sections show advantages in further processing, which lie in the avoidance of fluffy and hairy yarns, a rough handle or an increased proportion of short fibers due to breaks in the yarn.
  • the present invention was therefore based on the object of producing hygroscopic fibers and threads with largely uniform round to oval fiber cross sections by a dry spinning process, since a plant suitable for dry spinning cannot be converted to a wet spinning process.
  • the spinning process is carried out in such a way that the non-solvent essentially does not evaporate in the spinning shaft and is washed out of the solidified threads after spinning.
  • Substances that meet these requirements are e.g. polymeric compounds from the series of polycarbonates, polystyrenes, polyvinyl acetates and cellulose esters.
  • threads and fibers are obtained from hydrophobic polymers which, in addition to the desired uniform round to oval cross-sectional profiles, have a water retention capacity of at least 10% and a core / shell structure in which the core is highly microporous, the pores predominantly with one another are connected and the jacket surrounding the core is considerably more compact compared to the core, but is penetrated by channels which allow the access of liquids to the pore system of the core.
  • polycarbonate is used as the polymeric additional compound, it can subsequently be recovered quantitatively from, for example, hygroscopic polyacrylonitrile fibers, for example by extraction with methylene chloride. If compounds are used which do not meet the stated conditions, there is no cross-sectional stabilizing effect.
  • an acrylonitrile homopolymer is used as the polymeric additive, this is probably soluble in the DMF spinning solvent, but not in the non-solvent, for example in glycerol or glycols.
  • the non-solvent for example in glycerol or glycols.
  • Another important advantage of the present invention is that such fibers not only no longer have the disadvantages mentioned at the outset, but that they additionally have a very stable pore system which is far less sensitive to manufacturing processes such as steaming, ironing and the like. Furthermore, the additives spun in increase the water retention capacity, which contributes to the comfort properties of such fibers.
  • the water retention capacity is determined on the basis of DIN regulation 53 814 (cf. Melliand Textile Reports 4, 1973, page 350).
  • the suspension was fed to a heating device via a gear pump and heated to 130.degree.
  • the residence time in the heating device was 3 minutes.
  • the spinning solution was then filtered and dry-spun in a spinning shaft in a manner known per se from a 240-hole nozzle.
  • the spinning material with a titer of 1580 dtex was collected on spools and folded into a band with a total titer of 110 600 dtex.
  • the fiber cable was then stretched 1: 4.0 times in boiling water, washed with water at 80 ° C., provided with antistatic preparation and dried in a sieve drum dryer at 100 ° C. under tension.
  • the fiber cable leaves the dryer with a moisture content of 41.5%.
  • the cable is then crimped in a stuffer box and then cut into fibers with a stack length of 60 mm.
  • the individual fibers with a final titer of 2.6 dtex have a strength of 2.2 centi Newton / dtex and an elongation of 32%.
  • the water retention capacity is 46%.
  • the fibers have a pronounced core / cladding structure with completely uniform round cross-sectional profiles, as shown by light microscope images in 700x magnification. As scanning electron micrographs in 1000x magnification also show, the pore system with strong cell walls is 2 - 5 ⁇ . Strength enforced.
  • the fiber cable left the dryer with a moisture content of 51%.
  • the fibers have a pronounced core / cladding structure with uniform round cross-sectional shapes, as shown by light microscope images at a magnification of 700 times. In the scanning electron microscope, strong cell walls of 2 - 5 ⁇ thickness in the pore system can be seen at a magnification of 1000 times.
  • Example 1 60 kg of dimethylformamide with 2.5 kg of cellulose ester based on butyric acid (Cellit BP 900), 17.5 kg of glycerol and 20 kg of an acrylonitrile copolymer with the chem.
  • the composition from Example 1 is stirred at room temperature in a kettle to form a suspension and then converted into a spinning solution as described in Example 1, filtered and the spinning solution is spun into threads and aftertreated into fibers with a final titer of 2.3 dtex.
  • the fiber cable left the dryer with a moisture content of 54%.
  • the fiber strength is 2.6 centi Newton / dtex, the elongation 29% and the water retention 45%.
  • the fibers have a core / man, as shown by light microscope images in 700x magnification tel structure with uniform round cross-sectional profiles. In the scanning electron microscope, strong cell walls of 2 - 5 ⁇ thickness in the pore system can be seen at a magnification of 1000 times.
  • the fibers have a distinctive core / shell structure with strange to asterisk-shaped, non-uniform cross-sectional profiles.
  • the scanning electron microscope at 10OOf magnification relatively thin cell walls of 1 - 2 ⁇ thickness can be seen in the pore system.
  • Example 1 62.5 kg of dimethylformamide with 2.5 kg of acrylonitrile homopolymer with a K value of 90, 15 kg of triethylene glycol and 20 kg of an acrylonitrile copolymer with the chem.
  • the composition from Example 1 is stirred into a suspension at room temperature in a kettle and then, as described in Example 1, transferred to a spinning solution, filtered and the spinning solution is spun into threads.
  • the acrylonitrile homopolymer used as a cross-section stabilizing additive in triethylene glycol is completely insoluble even in the heat.
  • the threads are collected again, folded into a cable and, as stated in Example 1, treated to give fibers with a final titer of 2.3 dtex.
  • the fiber cable left the dryer with a moisture content of 83%.
  • the fibers have a core / shell structure with non-uniform worm to rod-shaped strange cross-sectional profiles, as shown by light microscope images in 700x magnification. In the scanning electron microscope, at 1000x magnification, relatively thin cell walls of 1 - 2 ⁇ thickness in the pore system can be seen.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Artificial Filaments (AREA)
  • Multicomponent Fibers (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Absorbent Articles And Supports Therefor (AREA)
  • Materials For Medical Uses (AREA)
EP80107098A 1979-11-28 1980-11-15 Verfahren zur Herstellung von querschnittstabilen, hygroskopischen Kern/Mantelstruktur aufweisenden Fasern und Fäden nach einem Trockenspinnprozess Expired EP0029949B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT80107098T ATE6275T1 (de) 1979-11-28 1980-11-15 Verfahren zur herstellung von querschnittstabilen, hygroskopischen kern/mantelstruktur aufweisenden fasern und faeden nach einem trockenspinnprozess.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE2947824 1979-11-28
DE19792947824 DE2947824A1 (de) 1979-11-28 1979-11-28 Querschnittsstabile, hygroskopische kern/mantelstruktur aufweisende fasern und faeden und verfahren zu deren herstellung

Publications (2)

Publication Number Publication Date
EP0029949A1 EP0029949A1 (de) 1981-06-10
EP0029949B1 true EP0029949B1 (de) 1984-02-15

Family

ID=6087029

Family Applications (1)

Application Number Title Priority Date Filing Date
EP80107098A Expired EP0029949B1 (de) 1979-11-28 1980-11-15 Verfahren zur Herstellung von querschnittstabilen, hygroskopischen Kern/Mantelstruktur aufweisenden Fasern und Fäden nach einem Trockenspinnprozess

Country Status (11)

Country Link
US (1) US4438060A (es)
EP (1) EP0029949B1 (es)
JP (1) JPS5685418A (es)
AT (1) ATE6275T1 (es)
BR (1) BR8007730A (es)
CA (1) CA1163071A (es)
DD (1) DD154720A5 (es)
DE (2) DE2947824A1 (es)
ES (1) ES8107337A1 (es)
GR (1) GR73034B (es)
PT (1) PT72072B (es)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0052897B1 (en) * 1980-11-24 1984-11-07 Akzo N.V. A sized multifilament yarn of an aromatic polyamide, a yarn package, a woven fabric and a process for making said yarn
KR100658124B1 (ko) * 1999-10-13 2006-12-15 가부시키가이샤 가네카 다공질 아크릴계 섬유 및 그것으로 되는 직물, 및 그제조방법
US8453653B2 (en) * 2007-12-20 2013-06-04 Philip Morris Usa Inc. Hollow/porous fibers and applications thereof

Family Cites Families (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1996753A (en) 1928-06-16 1935-04-09 Celanese Corp Artificial yarn and method of preparing the same
GB312203A (en) 1930-04-15 1929-05-21 Henry Dreyfus Improvements in or relating to the manufacture of artificial products by dry-spinning processes
GB392160A (en) 1931-11-05 1933-05-05 Henry Dreyfus Improvements in or relating to the manufacture or treatment of artificial filaments,threads, ribbons, yarns, fabrics and the like
US2073414A (en) 1933-07-01 1937-03-09 Dosne Henry Process for manufacturing colored cellulose-ester material
US2376934A (en) 1942-12-05 1945-05-29 Du Pont Dry spun and dry cast structures of synthetic materials
BE528051A (es) 1953-06-25
GB1009894A (en) 1960-11-30 1965-11-17 Kurashiki Rayon Kk Method of manufacturing fibres or foils of mixed polymers
US3410819A (en) 1963-06-28 1968-11-12 American Cyanamid Co Addition of insoluble additives to fibers during manufacture
CA960824A (en) 1969-12-20 1975-01-14 American Cyanamid Company Wet-spinning polymer solution containing dispersion of solid in insoluble liquid
US4012459A (en) 1973-08-15 1977-03-15 American Cyanamid Company Acrylic fiber of improved properties
JPS568645B2 (es) 1974-09-05 1981-02-25
JPS51119069A (en) 1975-03-20 1976-10-19 Nippon Oil Co Ltd Method of producing permeable film
DE2554124C3 (de) * 1975-12-02 1986-07-10 Bayer Ag, 5090 Leverkusen Verfahren zur Herstellung von hydrophilen Fasern und Fäden aus Acrylnitrilpolymerisaten
DE2719019A1 (de) * 1977-04-28 1978-11-02 Bayer Ag Hydrophile faeden und fasern
DE2607071C2 (de) 1976-02-21 1985-09-19 Bayer Ag, 5090 Leverkusen Synthesefasern und -fäden mit hoher Feuchtigkeitsaufnahme und großem Wasserrückhaltevermögen
DE2607996A1 (de) * 1976-02-27 1977-09-01 Bayer Ag Hydrophile fasern und faeden aus synthetischen polymeren
DE2609829A1 (de) 1976-03-10 1977-09-15 Bayer Ag Verfahren zur herstellung von hydrophilen fasern und faeden aus synthetischen polymeren
DE2611193A1 (de) 1976-03-17 1977-09-29 Bayer Ag Verfahren zur herstellung von hydrophilen fasern und faeden aus synthetischen polymeren
JPS5939460B2 (ja) 1976-12-10 1984-09-22 日石三菱株式会社 多孔膜の製法
DE2657144C2 (de) 1976-12-16 1982-12-02 Bayer Ag, 5090 Leverkusen Verfahren zur Herstellung hydrophiler Fasern
DE2713456C2 (de) * 1977-03-26 1990-05-31 Bayer Ag, 5090 Leverkusen Verfahren zur Herstellung von hydrophilen Fasern
DE2706032A1 (de) * 1977-02-12 1978-08-17 Bayer Ag Verfahren zur herstellung hydrophiler acrylfasern
DE2736065A1 (de) 1977-08-10 1979-02-22 Bayer Ag Verfahren zur herstellung von hydrophilen faeden und fasern nach dem trocken-duesen-nasspinnverfahren
AT351661B (de) * 1978-01-05 1979-08-10 Chemiefaser Lenzing Ag Verfahren zur herstellung von hydrophilen faeden oder fasern aus einem acryl- nitrilhomo- oder acrylnitrilmischpolymerisat
JPS5818444B2 (ja) * 1978-01-19 1983-04-13 東レ株式会社 改良された吸水性を有する微多孔質アクリル系繊維
US4185038A (en) 1978-07-14 1980-01-22 Conoco, Inc. Hydroformylation catalysts containing rhodium (I) or iridium (I) chemically bound directly to inorganic polymers

Also Published As

Publication number Publication date
DE3066642D1 (en) 1984-03-22
JPS5685418A (en) 1981-07-11
ATE6275T1 (de) 1984-03-15
BR8007730A (pt) 1981-06-09
PT72072A (en) 1980-12-01
ES497194A0 (es) 1981-10-01
PT72072B (en) 1981-09-29
US4438060A (en) 1984-03-20
DE2947824A1 (de) 1981-07-23
EP0029949A1 (de) 1981-06-10
ES8107337A1 (es) 1981-10-01
CA1163071A (en) 1984-03-06
JPS6214643B2 (es) 1987-04-03
DD154720A5 (de) 1982-04-14
GR73034B (es) 1984-01-26

Similar Documents

Publication Publication Date Title
DE102006022009B3 (de) Verfahren zur Herstellung cellulosischer Mehrkomponentenfasern
DE2554124C3 (de) Verfahren zur Herstellung von hydrophilen Fasern und Fäden aus Acrylnitrilpolymerisaten
DE2625908C2 (de) Hydrophile Bikomponentenfäden aus Acrylnitrilpolymerisaten und ihre Herstellung
WO1995016063A1 (de) Verfahren zur herstellung cellulosischer formkörper
DE2951803C2 (es)
DE2607996A1 (de) Hydrophile fasern und faeden aus synthetischen polymeren
EP0019870B1 (de) Fäden und Fasern aus Acrylnitril-Copolymer-Mischungen sowie Verfahren zu ihrer Herstellung
EP0029949B1 (de) Verfahren zur Herstellung von querschnittstabilen, hygroskopischen Kern/Mantelstruktur aufweisenden Fasern und Fäden nach einem Trockenspinnprozess
EP0048846B1 (de) Fäden und Fasern aus Carboxylgruppen haltigen Acrylpolymeren, ihre Verwendung und Verfahren zu ihrer Herstellung
DE2713456C2 (de) Verfahren zur Herstellung von hydrophilen Fasern
EP0051189B1 (de) Verfahren zur Herstellung von trockengesponnenen Polyacrylnitril-Profilfasern und -fäden
DE2719019C2 (es)
DE2657144C2 (de) Verfahren zur Herstellung hydrophiler Fasern
WO1997004148A1 (de) Cellulosefaser
DE3418943A1 (de) Verfahren zur herstellung von faeden und fasern aus acrylnitrilpolymerisaten
DD144574A5 (de) Verfahren zur herstellung von hydrophilen synthesefasern und-faeden
DE2607659A1 (de) Hydrophile fasern und faeden aus synthetischen polymeren
EP0069268B1 (de) Verfahren zur Herstellung trockengesponnener Polyacrylnitrilhohlfasern und -fäden
AT363168B (de) Verfahren zur herstellung von hydrophilen fasern oder faeden aus einem acrylnitrilhomo- oder -copolymerisat
EP0013764B1 (de) Hydrophile Polycarbonatfasern mit hoher Einfriertemperatur und Verfahren zu deren Herstellung
DE2706032A1 (de) Verfahren zur herstellung hydrophiler acrylfasern
DE2737404A1 (de) Hydrophile fasern und faeden aus synthetischen polymeren
DE1964193C (de) Verbundfäden aus Acrylnitrilpolymerisaten
DE2724952A1 (de) Hydrophile schwerbrennbare faeden und fasern aus acrylnitrilpolymerisaten
DE2905424A1 (de) Verfahren zur herstellung von staerkehaltigen reyonfasern

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19801115

AK Designated contracting states

Designated state(s): AT BE DE FR GB IT NL

ITF It: translation for a ep patent filed

Owner name: SOCIETA' ITALIANA BREVETTI S.P.A.

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): AT BE DE FR GB IT NL

REF Corresponds to:

Ref document number: 6275

Country of ref document: AT

Date of ref document: 19840315

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3066642

Country of ref document: DE

Date of ref document: 19840322

ET Fr: translation filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19841106

Year of fee payment: 5

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 19841114

Year of fee payment: 5

PLBI Opposition filed

Free format text: ORIGINAL CODE: 0009260

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19841130

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19841231

Year of fee payment: 5

26 Opposition filed

Opponent name: RHODIA AG

Effective date: 19841108

26 Opposition filed

Opponent name: HOECHST AKTIENGESELLSCHAFT, FRANKFURT

Effective date: 19841114

NLR1 Nl: opposition has been filed with the epo

Opponent name: HOECHST AKTIENGESELLSCHAFT.

Opponent name: RHODIA AG.

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Effective date: 19851115

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Effective date: 19851130

BERE Be: lapsed

Owner name: BAYER A.G.

Effective date: 19851130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19860601

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee
PLBN Opposition rejected

Free format text: ORIGINAL CODE: 0009273

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: OPPOSITION REJECTED

27O Opposition rejected

Effective date: 19860815

GBPC Gb: european patent ceased through non-payment of renewal fee
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19880729

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19881118

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19901025

Year of fee payment: 11

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19920801