(19) |
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(11) |
EP 0 045 560 A1 |
(12) |
EUROPEAN PATENT APPLICATION |
(43) |
Date of publication: |
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10.02.1982 Bulletin 1982/06 |
(22) |
Date of filing: 15.06.1981 |
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(51) |
International Patent Classification (IPC)3: D02G 3/18 |
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(84) |
Designated Contracting States: |
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BE DE FR IT NL SE |
(30) |
Priority: |
21.06.1980 GB 8020414
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(71) |
Applicant: TBA Industrial Products Limited |
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Manchester M3 2NL (GB) |
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(72) |
Inventors: |
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- Munro, Alexander
Atherton
Greater Manchester (GB)
- Entwistle, Lester
Hindley Green
Wigan (GB)
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(74) |
Representative: Crux, John Anthony (GB) et al |
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T & N plc
Bowdon House
Ashburton Road West
Trafford Park GB-Manchester M17 1RA GB-Manchester M17 1RA (GB) |
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(54) |
Method of producing a glass fibre roving |
(57) Continuous multifilament glass fibre roving is rendered coherent and catenary-free
by passing it through an air treatment zone without positive overfeed so that there
is no bulking thereof.
[0001] This invention relates to the processing of continuous glass filaments and in particular
it is concerned with the preparation of rovings from strands comprised of such filaments
for conversion into fabrics by weaving and for use in the reinforcement of plastics,
especially by the pultrusion process.
[0002] A well-known problem in the preparation of such rovings is the phenomenon sometimes
known as "catenary". This is the lateral separation of individual strands from an
untwisted roving made up of a bundle of such strands. It is caused by variations in
tension present in the individual reel packages which are unwound and assembled side-by-side
together to form the roving. "Catenary" gives rise to problems in further processing
and in the final conversion of the roving; various methods are known for minimising
its effect. These methods include sizing treatments and twisting processes, both of
which give the desired cohesion, but at the expense of processing properties or the
use of an extra process step, respectively.
[0003] According to the present invention, a method of producing a coherent, essentially
catenary - free untwisted continuous multifilament glass fibre roving comprises the
steps of withdrawing individual continuous multifilament glass fibre strands from
each of a plurality of creel packages, assembling them side-by-side to form a single
roving, passing said roving through an air treatment zone without positive overfeed
so that there is no bulking thereof, and thereafter winding the treated roving into
a package.
[0004] Air treatment zone in this particular context means a confined passageway into which
air is introduced under pressure. It has been found that relatively small air pressures
and volume throughputs are highly effective to produce an essentially catenary-free
strand, even with strand linear densities of from 3000 to 9000 tex and at strand throughputs
in the range 150-300 metres/minute. Air pressures of the order of 400 to 600 KN/metre
2 and air volume throughputs of 0.5 to 1.5 cubic metres/minute are effective for present
purposes; this is much less than would be used in conventional air jet texturing processes.
The present process has some similarity to the so-called co-mingling process, but
the latter has hitherto been used for moderate texturing (bulking) of relatively fine
manmade fibre yarns, in conjunction with heating to "set" the bulk developed. A degree
of positive overfeed is used to ensure that such bulking is achieved.
[0005] By contrast, the present process when applied to a very much coarser glass fibre
roving in the complete absence of positive overfeed results in a roving which is not
bulked, but essentially free from catenary. If the throughput is reduced towards 150
metres/minute, the May product exhibit an apparent bulk. This bulk is only apparent,
in the sense that on applying moderate tension to the roving, it exhibits minimal
or even zero extensibility, coupled with practically no change in its catenary properties.
This type of product has been found to be valuable for use as a plastics reinforcement,
particularly in pultrusion processes.
[0006] At roving throughputs of the order of 300 metres/minute the product is catenary-free
and useful as a weavinq grade roving.
[0007] A particularly advantageous aspect of the invention lies in the fact that both of
the two specific roving products just described can be made by incorporating the air
treatment zone into the normal creel-to-package winding operation, with out introducing
any separate extra processing step. Conventional bulking apparatus is not needed for
this.
[0008] A typical air treatment zone for present pruposes comprises a V-shaped trough with
a hinged lid clampable in sealing relation thereto. A trough about 2.5 cm long and
about 0.5 cm deep has been found satisfactory, the airflow being introduced half way
along the trough through an aperture about 0.25 cm in diameter, in the bottom of the
V. Obviously, the precise geometry of the air treatment zone may be varied and some
experimentation may be necessary in order to arrive at the optimum conditions for
a particular roving and throughput. In particular, the degree of tangling and the
amount of apparent bulk (if any) developed can be varied within sensibly wide limits
whilst still achieving the desired catenary-free characteristic.
1. A method of producing a coherent, essentially catenary-free untwisted continuous
multifilament glass fibre roving, the method being characterised by the steps of withdrawing
individual continuous multifilament glass fibre strands from each of a plurality of
creel packages, assembling them side-by-side to form a single roving, passing said
roving through an air treatment zone without positive overfeed so that there is no
bulking thereof, and thereafter winding the treated roving into a package.
2. The method of claim 1 characterised in that the roving is passed at a rate of from
150 to 300 metres/minute through an air treatment zone constituted by a confined passageway
into which air is introduced at 0.5 to 1.5 cubic metres/minute, under a pressure of
from 400 to 600 KN/metre2.
3. The method of claim 1 or claim .2 characterised in that the roving has a linear
density of from 300 to 9000 tex.