GB2153368A - Liquid moulding compositions - Google Patents
Liquid moulding compositions Download PDFInfo
- Publication number
- GB2153368A GB2153368A GB08501518A GB8501518A GB2153368A GB 2153368 A GB2153368 A GB 2153368A GB 08501518 A GB08501518 A GB 08501518A GB 8501518 A GB8501518 A GB 8501518A GB 2153368 A GB2153368 A GB 2153368A
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- GB
- United Kingdom
- Prior art keywords
- liquid moulding
- composition according
- moulding composition
- liquid
- fibres
- 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.)
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K7/00—Use of ingredients characterised by shape
- C08K7/02—Fibres or whiskers
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Macromonomer-Based Addition Polymer (AREA)
Abstract
A pre-filled, pre-reinforced unsaturated resin moulding composition has a liquid composition so that it may be injection moulded at low temperatures and pressures. The length of the reinforcement fibres should not exceed 6mm.
Description
SPECIFICATION
Liquid Moulding Compositions
Many types of moulding compositions based on unsaturated polyester and similar resins are
known. They range in consistency from doughs, through sheet materials to dry pellets. They all contain polyester resin, monomer, filler, reinforcement and catalyst and are characterised in that they all need heat and pressure to be transformed into cured moulded products. The heat is
necessary not only to activate the cure but also to reduce the viscosity so that the material flows
readily and fills the mould cavity into which it is placed or forced.
Polyesters can also be used in liquid form in vacuum or pressure assisted filling of closed
moulds into which reinforcement is placed before closing the moulds. This is the resin injection
process and moulding takes place at ambient temperatures or slightly above.
The present invention provides a readily flowable liquid composition already containing
reinforcement which is capable of being injected into low pressure, low cost tools using simple
low cost equipment.
The basic ingredients of these liquid, storage stable, compositions are:
A. unsaturated polyester or similar resin dissolved in vinyl
type monomer,
B. inorganic filler,
C. 'reinforcement,
D. free radical catalyst,
However, the free radical catalyst need not be in the composition as sent out from the factory.
Owher ingredients which may be included are internal mould release agents, accelerators, inhibitors, rubbery or thermoplastic polymer to increase toughness and reduce cure shrinkage, blowing agents and pigments.
A. Resin Component
Unsaturated polyesters which may be used are those made by polyesterification of a ss unsaturated dicarboxylic acids or anhydrides, with or without saturated dicarboxylic acids or anhydrides and one or more glycols. The polyesters thus formed may, prior to blending with the modifying polymer, be dissolved in a vinyl type monomer with the incorporation of one or more inhibitors to give storage stability.
Typical ingredients that can be used to manufacture such polyester resin composition are:
(i) Unsaturated dicarboxylic acids-maleic an hydride fumaric acid, itaconic acid.
(ii) Saturated dicarboxylic acids-phthalic anhydride isophthalic acid, terephthalic acid, tetrahy
drophthalic anhydride, hexahydro-phthalic an hydride, endomethylene tetrahydrophthalic
anhydride, tetrachlorophthalic anhydride, tetrabromophthalic anhydride, chlorendic acid,
succinic acid, adipic acid, azelaic acid, sebacic acid.
(iii) Glycols-ethylene, diethylene, propylene, dipropylene, neopentyl and dibromoneopentyl
glycol.
1,3-propane-diol, butanediols, 1.6-hexanediol, hydrogenated Bisphenol A, ethylene and
propylene oxide aducts of Bisphenol A and similar 4,4-diphenols, 2,2,4-trimethyl-1 ,3
pentane-diol. 1,4-cyclohexane dimethanol or compounds with an oxirane group behaving as
glycols e.g. ethylene oxide, propylene oxide, glycidyl ethers.
(iv) Vinyl monomers-styrene, vinyl toluene, chlorostyrene bromostyrene, a methyl styrene, t
butyl styrene, p methylstyrene, methyl methacrylate, diallyl phthalate.
(v) Inhibitors -hydroquinone and ring substituted hydroquinones, benzoquinone and ring
substituted benzoquinones, 1,4 naphthaquinone, copper naphthenate, quaternary com
pounds.
Minor quantities of mono and poly function hydroxyl and carboxyl containing compounds such as benzoic acid, penta-erythritol, trimethylol propane, glycerol, trimellitic acid may be incorporated into the unsaturated polyester during manufacture thereof. Dicyclo-pentadiene may also be added during manufacture.
Suitable vinyl ester polymer resins are, for example, made by an addition between epoxide resins and acrylic or methacrylic acids again dissolved in a vinyl monomer.
Other resins which are usable are urethane acrylate resins, i.e. those containing both urethane linkages and acrylic groups and again dissolved in vinyl type monomer.
B. Typical fillers that can be used are clays, natural or synthetic calcium carbonates, silica, talcs, alumina hydrate, antimony oxide, dolomite, and these can be surface treated. Expanded fillers e.g. hollow glass spheres can also be utilised as can be waste products such as fly ash.
Combinations of two or more fillers can be used and if required mixtures of various particle sizes can be employed.
C. The reinforcement is preferably glass fibre either hammer milled or chopped fibre of up to 5-6mm length. Other reinforcements such as carbon fibre, KEVLAR(g), etc. can be used wholly or in part.
D. The free radical catalyst can be selected from the wide range of peroxide, hydroperoxide, perester, perketal types available on the market according to the temperature at which cure is to occur. Azo compounds yielding free radicals can also be used.
Amongst the optional materials that may be incorporated in the compositions are:
Mould release agents e.g. zinc stearate accelerators e.g. tertiary aromatic amines. metal salts, inhibitors such as TopanolG) O, Rubbery or thermoplastic polymers such as LP60 (Union
Carbide) modified styrene/butadiene copolymers, blowing agents e.g. CelogenO XP100 (Uniroyal).
The amount of filler used is between 25 and 1 50 pphr preferably 50-100 pphr and the amount of reinforcement depends on the length of the fibres but varies between 0 and 60% preferably between 5 and 40%.
The viscosity of the composition must be such that it is sufficiently fluid to be injected into a closed, vented, mould at relatively low pressures and should be below 500 poise preferably 50-150 poise when measured using a capillary extrusion rheometer constructed according to
Zlochower, Das and Hudson 34th SPI Conference 1979, Section 11 C. Such viscosities will be referred to as being "as herein defined".
In order to fully cure the moulded articles in a reasonable time it is necessary to have a mould heated to betwen 80"C and 200"C preferably 120"-150"C. At these temperatures mould residue times of 60-120 seconds are possible. Although single pot injectable liquid systems are described in Examples l-VI below it is possible to use two or more pot systems and lower temperatures e.g. a catalysed resin and an accelerated resin. both filled and reinforced, injected into a mould at ambient temperatures. Again a blowing agent may be incorporated such that expansion occurs when the injectable composition meets the hot mould and curing subsequently occurs.
Examples
Six resins are used in the examples below and these are made by standard polycondensation methods from the following.
Type 1. maleic anhydride 3 mole
phthalic anhydride 1 mole
propylene glycol 4.4 mole
styrene monomer to non volatile content of 63%.
Type 2. fumaric acid 3 mole
isophthalic acid 1 mole
propylene glycol 4.25 moles
styrene monomer to 63% non volatile content.
Type 3. maleic anhydride 1.4 mole
isophthalic acid 1 mole
neopentyl glycol 2 mole
propylene glycol 0.5 mole
styrene monomer to 65% non volatile content.
Type 4. as Type 3 but terephthalic acid used in place of isophthalic acid.
Type 5. as Type 4 but neopentyl glycol 1.875 moles and 0.625 moles diethylene glycol.
Type 6. maleic an hydride 1 mole
phthalic anhydride 1 mole
diethylene glycol 1.03 mole
propylene glycol 1.02 mole
styrene to non volatile content of 65%.
In all cases about 1 50 ppm of inhibitor was included.
Example 1
The following composition was prepared:
Resin Type 1 100 pbw Omya BLH (Calcium carbonate filler) 76 pbw
Hammer milled glass fibre 33 pbw 1.5mm chopped glass fibre (Fibreglass WX 6450) 6.7 pbw
Zinc stearate (release agent) 4 pbw Trigonox(E) 21S (free radical catalyst) 2 pbw 20% Topanol(E) O in styrene 0.15 pbw
This mix has a viscosity of 50 poise* and was injected into a mould heated to 120"C. After 90 seconds the moulding was released cleanly and was free from crazing and cracks with a smooth surface appearance.
Example 2
A similar composition to Example 1 was used except that 20 pbw hammer milled glass and 20 pbw 3mm chopped glass fibres were used. This composition had a viscosity of 1 25 poise* and like Example 1 gave good mouldings.
*Measured as previously described.
Example 3-7
These were similar to Example 1 except that the resins used were those previously described as numbers 2-5. The results are given in the Table attached.
TABLE
I Example Number 1 2 3 4 5 6 7 Resin Type 1 1 2 3 4 5 6 H.D.I of resin OC 110 - 130 98 105 80 81 Tensile Strength MPa 28 16 22 22 37 33 31 Tensile Modulus cPa 8.6 3.7 8.4 6.6 8.4 7.8 7.0 Elongation 4'0 0.46 0.6 0.41 o.g3 0.56 0.6 1.0 Bend Strength MPa 64 7 38 63 72 78 70 65 I Bend Modulus GPa 6.6 4.2 6.5 6.6 7.2 6.3 6.4 Charpy Impact kJm2 7.18 11.1 4.8 6.0 6.0 5.9 7.0 Izod Impact Jm-1 76.2 130 67.1 53 58.3 50.1 51.0
Claims (8)
1. A liquid moulding composition including
(a) an unsaturated resin dissolved in a vinyl monomer
(b) an inorganic filler
(c) a reinforcement which is fibres of up to 6mm in length.
2. A liquid moulding composition according to claim 1, including also (d) a free-radical catalyst.
3. A liquid moulding composition according to claim 1 or claim 2, wherein the reinforcement fibres are up to 5mm in length.
4. A liquid moulding composition according to any one of the preceding claims wherein the fibres are hammer milled or chopped glass fibres.
5. A liquid moulding composition according to any one of the preceding claims having a viscosity of below 500 poise as herein defined.
6. A liquid moulding composition according to claim 5, wherein the viscosity is between 50-150 poise as herein defined.
7. A liquid moulding composition substantially as herein described and exemplified.
8. A method of injection moulding an article comprising injecting a composition according to any one of the preceding claims at low temperatures and pressure into a closed, vented mould.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB848401815A GB8401815D0 (en) | 1984-01-24 | 1984-01-24 | Liquid moulding compositions |
Publications (3)
Publication Number | Publication Date |
---|---|
GB8501518D0 GB8501518D0 (en) | 1985-02-20 |
GB2153368A true GB2153368A (en) | 1985-08-21 |
GB2153368B GB2153368B (en) | 1987-04-08 |
Family
ID=10555447
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB848401815A Pending GB8401815D0 (en) | 1984-01-24 | 1984-01-24 | Liquid moulding compositions |
GB08501518A Expired GB2153368B (en) | 1984-01-24 | 1985-01-22 | Liquid moulding compositions |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB848401815A Pending GB8401815D0 (en) | 1984-01-24 | 1984-01-24 | Liquid moulding compositions |
Country Status (1)
Country | Link |
---|---|
GB (2) | GB8401815D0 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102993662A (en) * | 2012-08-22 | 2013-03-27 | 常熟市筑紫机械有限公司 | Flame retardant unsaturated polyester molding material with high temperature resistance |
CN102993660A (en) * | 2012-08-22 | 2013-03-27 | 常熟市筑紫机械有限公司 | Preparation method of flame retardant unsaturated polyester molding material with high temperature resistance |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1382244A (en) * | 1971-04-06 | 1975-01-29 | Bp Chem Int Ltd | Moulding process |
US4128527A (en) * | 1976-05-12 | 1978-12-05 | Hitachi, Ltd. | Dynamoelectric machine having coil windings and core encapsulated with resin-filler composition |
US4245059A (en) * | 1973-08-29 | 1981-01-13 | Mitsubishi Rayon Co., Ltd. | Unsaturated polyester composition for molding compound and coated molded article thereof |
GB2069510A (en) * | 1980-02-15 | 1981-08-26 | Asahi Chemical Ind | Thermosetting unsaturated polyester resin composition |
US4287115A (en) * | 1979-11-13 | 1981-09-01 | The Dow Chemical Company | Filler mixtures and thermoset resins containing same |
-
1984
- 1984-01-24 GB GB848401815A patent/GB8401815D0/en active Pending
-
1985
- 1985-01-22 GB GB08501518A patent/GB2153368B/en not_active Expired
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1382244A (en) * | 1971-04-06 | 1975-01-29 | Bp Chem Int Ltd | Moulding process |
US4245059A (en) * | 1973-08-29 | 1981-01-13 | Mitsubishi Rayon Co., Ltd. | Unsaturated polyester composition for molding compound and coated molded article thereof |
US4128527A (en) * | 1976-05-12 | 1978-12-05 | Hitachi, Ltd. | Dynamoelectric machine having coil windings and core encapsulated with resin-filler composition |
US4287115A (en) * | 1979-11-13 | 1981-09-01 | The Dow Chemical Company | Filler mixtures and thermoset resins containing same |
GB2069510A (en) * | 1980-02-15 | 1981-08-26 | Asahi Chemical Ind | Thermosetting unsaturated polyester resin composition |
US4329438A (en) * | 1980-02-15 | 1982-05-11 | Asahi Kasei Kogyo Kabushiki Kaisha | Thermosetting unsaturated polyester resin composition and method for preparation thereof |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102993662A (en) * | 2012-08-22 | 2013-03-27 | 常熟市筑紫机械有限公司 | Flame retardant unsaturated polyester molding material with high temperature resistance |
CN102993660A (en) * | 2012-08-22 | 2013-03-27 | 常熟市筑紫机械有限公司 | Preparation method of flame retardant unsaturated polyester molding material with high temperature resistance |
CN102993660B (en) * | 2012-08-22 | 2014-09-10 | 常熟市亚美模特儿衣架有限公司 | Preparation method of flame retardant unsaturated polyester molding material with high temperature resistance |
Also Published As
Publication number | Publication date |
---|---|
GB8401815D0 (en) | 1984-02-29 |
GB2153368B (en) | 1987-04-08 |
GB8501518D0 (en) | 1985-02-20 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 20040122 |