Source: https://patents.google.com/patent/EP0148762A2/en
Timestamp: 2018-09-24 16:21:22
Document Index: 361217647

Matched Legal Cases: ['Application No. 84', 'Application No. 84', 'Application No. 84', 'art 4', 'art 5', 'arts 4', 'art 4', 'art 5', 'art 11', 'art 12']

EP0148762A2 - Improvements in fibre reinforced moulded plastics articles - Google Patents
Improvements in fibre reinforced moulded plastics articles Download PDF
EP0148762A2
EP0148762A2 EP19850300033 EP85300033A EP0148762A2 EP 0148762 A2 EP0148762 A2 EP 0148762A2 EP 19850300033 EP19850300033 EP 19850300033 EP 85300033 A EP85300033 A EP 85300033A EP 0148762 A2 EP0148762 A2 EP 0148762A2
EP19850300033
EP0148762B1 (en )
EP0148762A3 (en )
A process for moulding articles of permeable sheet-like fibre-reinforced unconsolidated particulate plastics material which has been bonded together and which includes heating the material to a moulding temperature by the passage of hot temperature air through the sheet and then subjecting it to a moulding process.
Heretofore, fibre reinforced plastics articles have been moulded from consolidated rigid sheets embodying glass fibre mat formed from very long glass fibre strands (i.e. fibre bundles) of perhaps 200 centimetres or more in length which extend in a random serpentine manner throughout the sheet.
For the satisfactory moulding of such sheets, they must be homogeneously preheated. This requires both time and accurate temperature control if overheating and degradation of the sheet surfaces is not to occur whilst the core portions of the sheets are brought up to the required moulding temperature. Such materials do not lend themselves easily to deep draw moulding.
According to the present invention a process for moulding articles of permeable sheet-like fibre-reinforced unconsolidated particulate plastics material which has been bonded together and which includes heating the material to a moulding temperature by the passage of hot temperature air through the sheet and then subjecting it to a moulding process.
After preheating, the structure may simply be moulded into an impermeable article. Alternatively, it may be subjected to limited compression in the mould so as to remain permeable. Or it may be fully compressed in the mould so as to cause the molten thermoplastics material to wet the fibres. The mould is then slightly opened so as to allow the material to expand as a result of the resilience of the fibres and become permeable as described and claimed in United Kingdom Patent Application No. 84 00293 Filed 6th January 1984. In certain cases, and especially when a smooth or glazed surface finish is required, the structure may be impregnated with a liquid thermosetting resin before or after moulding as described and claimed in United Kingdom Patent Application No. 84 00294 Filed 6th January 1984.
Preferably, the open sheet-like structure comprises 20% to 60% by weight of reinforcing fibres having a high modulus of elasticity (as herein defined), and between about 7 and about 50 millimetres long, and 40% to 80% by weight of wholly or substantially unconsolidated particulate plastics material, and in which the fibrous and plastics components are bonded into an air permeable structure.
Preferably, the fibres are in the form of single discrete fibres. Thus, when glass fibres are used and are received in the form of chopped strand bundles, the bundles are broken down into single fibres before the structure is formed.
The high modulus of elasticity is to be taken as meaning a modulus of elasticity substantially higher than that of a consolidated sheet which could be formed from the structure. The fibres falling into this category include glass, carbon and ceramic fibres and fibres such as the aramid fibres sold under the trade names Kevlar and Nomex and will generally include any fibre having a modulus higher than 10,000 Mega Pascals.
A process for producing a structure of the kind above described is disclosed in co-pending United Kingdom Patent Application No. 84 00290 Filed 6th January 1984.
Figure 1 is a diagrammatic cross-section through an open permeable structure of the kind suitable for use as a starting material in the present invention,
Figure 2 is a sectional side elevation through a through air heating oven for use in the process of the invention, and
Figure 3 is a sectional side elevation through a mould showing a moulding being formed in accordance with the process of the invention.
Referring first to Figure 1, this shows an uncompacted fibrous structure 1 comprising fibres 2 interspersed with particulate plastics material 3, the fibres and plastics particles being bonded together so as to form a coherent but permeable structure.
Figure 2 shows an oven for heating a permeable structure 1 of the kind shown in Figure 1. The oven consists of an upper part 4 and a lower part 5, the parts 4 and 5 including plenum chambers 6 and 7 respectively. The lower wall 8 of the part 4 and the upper wall 9 of the part 5 consist of grilles which facilitate the substantially unrestricted passage of air.
After heating as decribed to, say, 200°C, the structure 1 is transferred to a mould, typically of the kind shown in Figure 3.
Referring now to Figure 3, this shows a mould having an upper part 11 and a complementary lower part 12 between which the structure 1 has been moulded. Before or after the heating step has been effected the structure 1 maytbe impregnated with a liquid thermosetting resin which cures, at least partially, whilst the structure is in the mould.
The mould may be used to fully consolidate the structure so that resulting moudling is solid and impermeable. Or. the moulding may be partially compacted so as to remain porous. Alternatively, a porous article can be achieved by partly or fully compacting and consolidating the article and then opening the mould slightly so as to allow the resilience/of the grass fibre content to expand the moulding to the desired thickness.
Suitable thermoplastics include polyethylene, polypropylene, polystyrene, acrylonitrylstrene butadiene, polyethylene terephthalate, and polyvinyl chloride, both plasticised and unplasticised. It is anticipated that any thermoplastics material may be used which is not chemically attacked by water and which can be sufficiently softened by heat without being chemically decomposed.
Thermosetting materials which may be used to impregnate the structure include phenolic and polyester resins, for example phenolformaldehyde resin, urea and melamine formaldehyde resins, epoxy resins, unsaturated polyesters and polyurethanes.
A sheet of lightly bonded unconsolidated permeable material comprising 33% single glass fibres 13 millimetres long and 11 microns in diameter, 67% polypropylene powder together with a proprietary antioxidant, and having a substance of 3,000 grams per square metre was placed in a through drying oven manufactured by Honeycomb Engineering Co. Hot air at 2300 C was fed to the upper face of the sheet and a partial vacuum applied to the under side. The porous nature of the sheet mat allowed hot air to pass through it so uniformly heating the material. After a short time (about 6 secs), the still porous material was fully heated to the air temperature of 230° C. This temperature, being some 50° C higher than the melting point of polypropylene, allowed the mat to be quickly removed from the oven and moulded into shape. During heating of the mat it was noted that pressure drop across the thickness of the material was substantially constant, being 76 cm water gauge to start and rising to 85 cm water gauge at completion of heating.
A further example utilised material containing 50% glass (13 millimetres long, 11 microns diameter as before), 50% polypropylene powder + antioxidant. The heating time was about 4 seconds with the pressure drop being the same as in the previous examples.
This ability to heat a porous unconsolidated web has a number of significant advantages :-
a) Saving in processing time and cost since manufacture is eliminated.
b) A more rapid heating of material prior to the moulding operation; approximately 6 seconds opposed to 3 minutes for a consolidated sheet in an infra red oven.
c) The development of a better temperature gradient throughout the thickness of the material, since the passage of hot air heats the mat uniformly through its thickness whilst infra red heating of a consolidated sheet develops a temperature profile from the surface to the centre with risk of thermal degradation of plastic at the surface before the centre has attained the desired temperature.
d) Blanks can be cut from the unconsolidated mat prior to heating and the 'waste' material readily "repulped" for re-use. Whereas waste arising from blanks cut from consolidated sheet must be ground at much higher cost into a particulate form for re-use.
1. A process for moulding articles of permeable sheet-like fibre-reinforced unconsolidated particulate plastics material which has been bonded together and which includes heating the material to a moulding temperature by the passage of hot temperature air through the sheet and then subjecting it to a moulding process.
2. A process as claimed in claim 1 in which the sheet is moulded into an impermeable article.
3. A process as claimed in claim 1 in which the sheet is moulded by limited compression in a mould so as to remain permeable.
4. A process as claimed in claim 1 in which the sheet is moulded by full compression in a mould so as to cause the molten thermoplastics material to wet the fibres, and the mould is then slightly opened to allow the material to expand as a result of the resilience of the fibres and become permeable.
5. A process as claimed in claims 1 to 4 in which the sheet is impregnated with a liquid thermosetting resin before or after moulding.
6. A process as claimed in claim 5 in which the thermosetting materials are phenolic and polyester resins.
7. A process as claimed in claim 6 in which the resins are phenolformaldehyde resin, urea and melamine formaldehyde resins, epoxy resins, unsaturated polyesters and polyurethanes.
8. A process as claimed in claims 1 to 7 in which the sheet-like material to be moulded comprises 20% to 60% by weight of reinforcing fibres having a high modulus of elasticity (as herein defined), and being between about 7 and 50 millimetres long, and 40% to 80% by weight of wholly or substantially unconsolidated particulate plastics material, and in which the fibrous and plastics components are bonded into an air permeable structure.
9. A process as claimed in any one of the preceding claims which includes heating the sheet in an oven in which the sheet is located between open supports through which hot air is passed.
10. A process as claimed in claim 9 in which the open supports are in the form of support grills.
11. A process for moulding articles of permeable sheet-like fibre reinforced unconsolidated particulate plastics material which has been bonded together substantially as desribed herein with reference to and as shown in the accompanying drawings.
12. A fibre reinforced plastics material article made by the process set forth in any one of the preceding claims.
EP19850300033 1984-01-06 1985-01-03 Improvements in fibre reinforced moulded plastics articles Expired - Lifetime EP0148762B1 (en)
GB8400292 1984-01-06
GB8400292A GB8400292D0 (en) 1984-01-06 1984-01-06 Fibre reinforced moulded plastics articles
EP0148762A2 true true EP0148762A2 (en) 1985-07-17
EP0148762A3 true EP0148762A3 (en) 1988-01-07
EP0148762B1 EP0148762B1 (en) 1992-10-28
ID=10554635
EP19850300033 Expired - Lifetime EP0148762B1 (en) 1984-01-06 1985-01-03 Improvements in fibre reinforced moulded plastics articles
EP (1) EP0148762B1 (en)
JP (1) JPH0347182B2 (en)
KR (1) KR920002331B1 (en)
CA (1) CA1244211A (en)
DE (2) DE3586777D1 (en)
DK (1) DK167180B1 (en)
ES (1) ES8606065A1 (en)
FI (1) FI84451C (en)
GB (1) GB8400292D0 (en)
EP0255316A2 (en) * 1986-07-31 1988-02-03 The Wiggins Teape Group Limited Process for the manufacture of a permeable sheet-like fibrous structure
WO1991005652A1 (en) * 1987-04-07 1991-05-02 Owens-Corning Fiberglas Corporation Process for producing preformable continuous strand mats and a therethrough made strand mat
DE4010441A1 (en) * 1990-03-31 1991-10-02 Roeder & Spengler Stanz Device having a heating station and a forming station
EP0453784A2 (en) * 1990-04-24 1991-10-30 General Electric Company Plastic based laminates
EP0646684A1 (en) * 1993-03-03 1995-04-05 Sumitomo Chemical Company, Limited Water-permeable concrete formwork
WO1999059792A1 (en) * 1998-05-21 1999-11-25 Lear Corporation Method and apparatus for preheating permeable, thermoformable material
FR2213152B1 (en) * 1973-01-08 1976-04-30 Renoux Robert
JPS6241185B2 (en) * 1982-03-19 1987-09-01 Nitto Boseki Co Ltd
EP0255316B1 (en) * 1986-07-31 1992-02-26 The Wiggins Teape Group Limited Process for the manufacture of a permeable sheet-like fibrous structure
EP0450482A3 (en) * 1990-03-31 1993-08-11 R + S Stanztechnik Gmbh Apparatus with a heating station and a forming station
EP0450482A2 (en) * 1990-03-31 1991-10-09 R + S STANZTECHNIK GmbH Apparatus with a heating station and a forming station
EP0453784A3 (en) * 1990-04-24 1992-01-02 General Electric Company Plastic based laminates
EP0646684A4 (en) * 1993-03-03 1995-07-05 Sumitomo Chemical Co Water-permeable concrete formwork.
ES539356D0 (en) grant
ES8606065A1 (en) 1986-04-16 application
FI850044A (en) application
FI84451C (en) 1994-04-18 grant
DE3586777D1 (en) 1992-12-03 grant
CA1244211A (en) 1988-11-08 grant
ES539356A0 (en) 1986-04-16 application
DK7385A (en) 1985-07-07 application
FI850044D0 (en) grant
DK7385D0 (en) 1985-01-04 grant
FI850044L (en) 1985-07-07 grant
JPH0347182B2 (en) 1991-07-18 grant
DE3586777T2 (en) 1993-03-18 grant
GB8400292D0 (en) 1984-02-08 grant
EP0148762B1 (en) 1992-10-28 grant
FI850044A0 (en) 1985-01-04 application
JPS60179233A (en) 1985-09-13 application
EP0148762A3 (en) 1988-01-07 application
FI84451B (en) 1991-08-30 application
KR920002331B1 (en) 1992-03-21 grant
CA1244211A1 (en) grant
DK167180B1 (en) 1993-09-13 grant
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