GB2072682A - Preparation of filler composition for dough moulding compounds - Google Patents

Preparation of filler composition for dough moulding compounds Download PDF

Info

Publication number
GB2072682A
GB2072682A GB8108362A GB8108362A GB2072682A GB 2072682 A GB2072682 A GB 2072682A GB 8108362 A GB8108362 A GB 8108362A GB 8108362 A GB8108362 A GB 8108362A GB 2072682 A GB2072682 A GB 2072682A
Authority
GB
United Kingdom
Prior art keywords
filler
dispersion
mixing
polymeric material
thermoplastic polymeric
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.)
Granted
Application number
GB8108362A
Other versions
GB2072682B (en
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.)
British Industrial Plastics Ltd
Original Assignee
British Industrial Plastics Ltd
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
Priority claimed from GB8009530A external-priority patent/GB2072195A/en
Application filed by British Industrial Plastics Ltd filed Critical British Industrial Plastics Ltd
Priority to GB8108362A priority Critical patent/GB2072682B/en
Publication of GB2072682A publication Critical patent/GB2072682A/en
Application granted granted Critical
Publication of GB2072682B publication Critical patent/GB2072682B/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C3/00Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
    • C09C3/10Treatment with macromolecular organic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00Processes of treating or compounding macromolecular substances
    • C08J3/20Compounding polymers with additives, e.g. colouring
    • C08J3/205Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase
    • C08J3/21Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase the polymer being premixed with a liquid phase
    • C08J3/215Compounding polymers with additives, e.g. colouring in the presence of a continuous liquid phase the polymer being premixed with a liquid phase at least one additive being also premixed with a liquid phase
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/04Ingredients treated with organic substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K9/00Use of pretreated ingredients
    • C08K9/08Ingredients agglomerated by treatment with a binding agent
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09CTREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
    • C09C1/00Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
    • C09C1/02Compounds of alkaline earth metals or magnesium
    • C09C1/021Calcium carbonates
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/20Powder free flowing behaviour

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

A filler for the manufacture of a DMC is prepared by mixing a finely divided substantially non-absorbent mineral filler with an aqueous emulsion or dispersion of a thermoplastic polymeric material. In order to prevent coagulation of the emulsion or dispersion upon mixing, the filler is treated with water before the mixing is carried out. The mixture is dried at elevated temperature to form a powder having the thermoplastic polymer homogeneously dispersed in the filler. A dough moulding compound can be made by mixing the treated filler with unsaturated polyester resin solution glass fibre and minor amounts of other additives. Good dispersion of the thermoplastic polymeric material in the DMC is thereby obtained.

Description

SPECIFICATION Improvements relating to fillers for dough moulding compounds This invention relates to an improved method of preparing the filler for use in a dough moulding compound.
Dough moulding compounds based on, for example, unsaturated polyester resins are well known and in common use for moulding of components such as insulation for electrical distribution equipment. Their principal ingredients are a solution of an unsaturated polyester resin in a monomer such as styrene, chopped glass fibres and mineral filler such as calcium carbonate.
UK Patent Specification No.936,351 describes moulding compounds of this type which contain a solution of an unsaturated polyester resin in a copolymerizable monomer, a peroxide catalyst, an inhibitor, a substantially non-absorbent powdered mineral filler and a finely divided thermoplastic polymeric material in an amount between 2 and 24 per cent by weight of the total composition.
The function of the thermoplastic polymeric material is to replace some of the powdered mineral filler and improve the crack resistance of thick mouldings moulded from the compound and the flow characteristics of the compound. UK Patent Specification No.936,351 describes essentially three methods of incorporating the thermoplastic polymeric material into the compound to achieve homogeneous dispersion. One such method when mixing the compound is to mix dry the thermoplastic polymeric material and the dry powdered mineral fillers of the formulation. In this method the polymeric additive has to be finely ground. This is difficult and costly and does not achieve very intimate dispersion.
Another method is to add the thermoplastic polymeric material to the filler as a solution in an inorganic solvent, conveniently the same reactive monomer as that in which the unsaturated polyester is dissolved.
This method achieves good dispersion but the undesired further addition of the reactive monomer adversely affects the flow of the compound and diminishes the quality of the final composition.
Yet another method is to mix an aqueous emulsion of the thermoplastic polymeric material with the dry powdered mineral filler in a heated mixer until the water has evaporated. By this method it is difficult to obtain uniform distribution of the thermoplastic polymeric material in the filler, particularly when the amount of the former is low, as is usual in practice. It appears that the mixing of the emulsion with the dry filler leads to coagulation of the emulsion, resulting in a lack of uniformity of distribution of the thermoplastic polymer.
The first two methods are the ones commonly used commercially, particularly the embodiment where the thermoplastic polymeric material is dissolved in a reactive monomer.
Our invention is concerned with obtaining a homogeneous dispersion of the thermoplastic polymeric material in the moulding compound by an improvement of the previously unused third method.
Thus, according to the present invention a method for the preparation of a filler for the manufacture of a dough moulding compound comprises mixing a finely divided mineral filler with an aqueous emulsion or dispersion of thermoplastic polymeric material wherein said mineral filler has intimately mixed therein, prior to its contact with said emulsion or dispersion, at least sufficient water to prevent coagulation of the aqueous emulsion or dispersion when the latter is mixed with said mineral filler and drying said mixture at an elevated temperature and forming a dry filler powder having said thermoplastic polymeric material uniformly dispersed therein.
We have found that if the emulsion or dispersion is mixed with wet filler, the hitherto unsatisfactory method of preparing the filler is improved to be superior to the others. Preferably the drying is carried out at a temperature low enough to ensure that said thermoplastic polymeric material does not become tacky. The finely divided mineral filler may be mixed with sufficient water to make a paste or thick slurry with the filler, but not so much water that when the emulsion is added the mixture becomes too runny. In some cases, hqwever, it may be sufficient to ensure that all the particles of filler are damp, and the filler may remain a flowable powder. Water has to be dried off and is therefore to be kept to the minimum necessary to obtain the homogenous dispersion by simple mixing.Also a need for filtration is undesirable because of the potential waste of emulsified thermoplastics polymer in such a step.
The preferred mineral filler is calcium carbonate either in its natural or synthetic form since it is both suitable and cheap, but other fillers such as clay, silicates, alumina, talc and asbestos may also be used instead.
The thermoplastic polymeric material is to be one which is of a class of suitable polymers well-known in the art. Clearly which monomer is to be used in the dough moulding compound will determine the suitability of thermoplastic polymeric materials. In practice, however, styrene is commonly used and polyvinyl acetate is a particularly suitable polymer. In the present invention the thermoplastic polymeric material is used in aqueous dispersion or emulsion and any polymer can be used which is compatible with the monomer to be present in the dough moulding compound and is also available as the necessary aqueous emulsion or dispersion.
The solids content of the aqueous emulsion or dispersion used is preferably as high as possible, to reduce the amount of water to be evaporated, while retaining the facility of mixing to a homogeneous mass with the filler. The usual range will be 30 to 75% solids but this is not essential.
The minimum amount of water required in the mineral filler to make a paste will depend on the absorption characteristics of the filler chosen and these vary very considerably. Generally a range from 10% by weight up to about 40% by weight will embrace most examples. Clearly the amount of water in the filler is preferably to be kept to a minimum to avoid unnecessary drying costs.
In the preparation of finely divided mineral fillers such as powdered calcium carbonate the grinding of the filler to size may be carried out in aqueous slurry, the wet filler then being filtered off. The wet filler cake is a thick pasty mass which may if desired, be used as the wet filler in the present invention.
The drying of the mixed thermoplastic polymeric material and filler can be accomplished by conventional means such as agitation in a heated mixer, or in an oven, and the dried material may be reground.
In the dried filler the proportion of the thermoplastic as polymeric material to filler will be made to suit the final formulation of the dough moulding compound. Thus in Example 1 below, a required 59.5 p.b.w. of calcium carbonate with 3 p.b.w. of the thermoplastic polymeric material in the dough moulding compound will make it desirable, for example, to prepare the treated filler with the same proportion of thermoplastic polymeric material filler in order that the treated filler can be used directly in the preparation of the dough moulding compound.
Alternatively the treated filler may be made with a higher proportion of thermoplastic polymeric additive, and used as a masterbatch, additional untreated filler being added to it during preparation of the dough moulding compound.
Other ingredients of a dough-moulding compound may be added to the filler with the thermoplastic polymeric material if desired. Preferred examples of such ingredients are surfactants and flame retardants (e.g. alumina trihydrate) which could with advantage be homogeneously dispersed in the filler.
The invention will now be described in more detail, by way of Example only.
Example I Dough moulding compounds of comparable composition were prepared by three different routes. In the first route a polyvinyl acetate powder was mixed dry with the filler, calcium carbonate, and in the second route polyvinyl acetate as a 50% solution in styrene was added to the other ingredients of the composition.
These two routes are the ones in commercial use.
In the third route 29759 of calcium carbonate filler ("Millicarb' commercially available from Plastichem Limited) was made into a thick slurry or paste by mixing with 12759 of water and 9g of dispersing agent, and 3009 of a 50% solids aqueous emulsion of polyvinyl acetate (9300 grade commercially available from Vinyl Products Ltd.) were added and stirred until evenly dispersed. The slurry was then dried in an oven and reground using a hammer mill and then a ball mill. This product - the treated filler - was then mixed with 1009 of calcium stearate in a sigma bladed mixer. 1 075g of a 66% solids solution of an unsaturated polyester resin in styrene, catalysed with 1.5% of t-butyl perbenzoate and inhibited with 0.2% of hydroquinone, were added to the treated filler and mixed until the filler was homogeneously dispersed, and finally 7009 of 6mm glass fibre was added and mixed in for a further 2.5 minutes.
The compositions of the three dough moulding compounds are given below in Table TABLE I Solid Polymer Treated Thermoplastic added Polymer Solution Filler as: 1 2 3 6mm Glass Fibre 14.0 pbw 14.0 pbw 14.0 bpw Treated filler (Note 1) - ~ 62.5 Millicarb (calcium carbonate) 59.5 59.5 Calcium Stearate 2.0 2.0 2.0 Polyester resin (Note 4) 21.5 18.5 ) 21.5 )Note Polyvinyl acetate 50% soln. in styrene - 6.0 ) Polyvinyl acetate solid (Note 2) 3.0 - t-Butyl peroctoate )based 1.5% 1.5% 1.5% Hydroquinone )on inhibitor )resin 0.2% 0.2% 0.2% Note 1 59.5 pbw of calcium carbonate filler with 3 pbw polyvinyl acetate.
Note 2 Polyvinvyl acetate less than 60 BS mesh size.
Note 3 Use of styrene solution accommodated by reducing normal resin control by amount equivalent to the extra styrene added but this then gives a much higher styrene content to the whole composition.
Note 4 Unsaturated polyester resin made from 6.6 moles propylene glycol, 5.0 moles maleic anhydride, 0.8 moles iso-phthalic acid, 0.4 moles benzoic acid (66% solids solution of resin in styrene monomer).
Mouldings were made from all three compounds, examined and tested. In the mouldings from the compounds made by using solid polyvinyl acetate there is a lack of homogeneity as evidenced by uneven gloss and colour on the surface.
Mouldings made from the compound using polyvinyl acetate in styrene solution were more homogenous, but the extra styrene monomer thus provided made the flow inferior (lower viscosity) and this also adversely affected the surface finish.
.Conversely, the compound made using the treated filler gave mouldings having a superior finish with respect to the evenness, gloss and colour.
The drying mixing of the thermoplastic polymeric material with the filler has the disadvantage that it is very difficult to obtain homogeneous dispersion. If a solution of the thermoplastic polymeric material in monomer is used there is improvement in homogeneity but there is extra monomer in the composition which cannot fully be compensated by increasing the solids content of the polyester resin solution. This extra monomer results in the dough moulding compound being slightly more tacky and having different flow characteristics during moulding, ie it is less viscous, which leads in turn to a tendency for greater porosity in mouldings produced.
Use of the filler treated as in the present invention enables a moulding compound with good homogeneous dispersion of the thermoplastic polymeric material to be made without this deterioration of the flow characteristics during moulding, and without the extra tackiness.

Claims (10)

1. A method for preparation of a filler for the manufacture of a dough moulding compound which comprises mixing a finely divided mineral filler intimately with an aqueous emulsion or dispersion of a thermoplastic polymeric material wherein said mineral filler has intimately mixed therein, prior to its contact with said emulsion or dispersion at least sufficient water to prevent coagulation of the aqueous emulsion or dispersion when the latter is mixed with said mineral filler, and drying said mixture at an elevated temperature, and forming a dry filler powder having said thermoplastic polymeric material uniformly dispersed therein.
2. A method according to claim 1 in which the amount of water used in said mineral filler is the minimum necessary to facilitate obtaining a homogeneous dispersion of said thermoplastic polymeric material in said filler by simple mixing.
3. A method according to claim 1 or 2 in which the amount of water in the mineral filler is in the range 10% to 40% by weight of filler.
4. A method according to claim 1,2 or 3 in which the mineral filler is calcium carbonate.
5. A method according to any preceding claim in which the solids content of the aqueous emulsion or dispersion is in the range 30 to 75% solids.
6. A method according to any preceding claim in which the filler is mixed with an aqueous emulsion of polyvinyl acetate.
7. A method of making a dough moulding compound which comprises preparing a treated filler by a method as claimed in any preceding claim, mixing said filler with solution of an unsaturated polyester resin in a reactive monomer, and mixing glass fibres into the resin solution/filler mixture so produced.
8. A method of preparing a treated filler as claimed in claim 1 substantially as described herein with reference to the foregoing Example.
9. A treated filler produced by a method as claimed in any one of claims 1 to 6.
10. A dough moulding compound produced buy a method as claimed in claim 5.
GB8108362A 1980-03-21 1981-03-17 Preparation of filler composition for dough moulding compounds Expired GB2072682B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB8108362A GB2072682B (en) 1980-03-21 1981-03-17 Preparation of filler composition for dough moulding compounds

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8009530A GB2072195A (en) 1980-03-21 1980-03-21 Preparation of fillers for unsaturated polyester moulding compositions
GB8108362A GB2072682B (en) 1980-03-21 1981-03-17 Preparation of filler composition for dough moulding compounds

Publications (2)

Publication Number Publication Date
GB2072682A true GB2072682A (en) 1981-10-07
GB2072682B GB2072682B (en) 1983-10-05

Family

ID=26274907

Family Applications (1)

Application Number Title Priority Date Filing Date
GB8108362A Expired GB2072682B (en) 1980-03-21 1981-03-17 Preparation of filler composition for dough moulding compounds

Country Status (1)

Country Link
GB (1) GB2072682B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8603236B2 (en) 2010-12-01 2013-12-10 Mattel, Inc. Play composition including crosslinkable binder
US8633269B2 (en) 2010-12-01 2014-01-21 Mattel, Inc. Play modeling dough
USD803326S1 (en) 2013-03-15 2017-11-21 Mattel, Inc. Toy projectile

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8603236B2 (en) 2010-12-01 2013-12-10 Mattel, Inc. Play composition including crosslinkable binder
US8633269B2 (en) 2010-12-01 2014-01-21 Mattel, Inc. Play modeling dough
US9193859B2 (en) 2010-12-01 2015-11-24 Mattel, Inc. Play modeling dough
USD803326S1 (en) 2013-03-15 2017-11-21 Mattel, Inc. Toy projectile
US9829290B2 (en) 2013-03-15 2017-11-28 Mattel, Inc. Toy projectile and method of making
US9964383B2 (en) 2013-03-15 2018-05-08 Mattel, Inc. Toy projectile and method of making

Also Published As

Publication number Publication date
GB2072682B (en) 1983-10-05

Similar Documents

Publication Publication Date Title
US4623390A (en) Insulating paint for interior and exterior of buildings and method of making same
DE69914967T2 (en) Powder coating mixture containing unsaturated polyesters and their use
JPS60255843A (en) Vinyl tile
US4111881A (en) Polyoxyhydrocarbylene dihydrocarbyl ethers as coalescing agents for synthetic polymer latexes
GB2072682A (en) Preparation of filler composition for dough moulding compounds
EP0036749A1 (en) Improvements relating to fillers for dough moulding compounds
US4257817A (en) Method of reducing binder demand of inorganic filler
US3462390A (en) Color concentrates
US3398113A (en) Thermosetting resin pigment composition and process therefor
US3867335A (en) Tape joint cement additive
US3084133A (en) Tape joint cement comprising polyvinyl alcohol and clay and method for preparing same
US4717452A (en) Composition for sizing agent and process for using the same composition
US2687394A (en) Coated particles of calcium carbonate and method of making same
US3251798A (en) Elastomer compounding process
US4810301A (en) Composition for sizing agent and process for using the same composition
DE19500195A1 (en) Use of white-tinted plastics for tinting paper coating slips and such white-tinted paper coating slips
JP3481883B2 (en) Method for stabilizing inorganic compounds treated with unsaturated fatty acids and use thereof
US3278479A (en) Clay coated with ethoxylated amide and polyester resins containing the same
US3169073A (en) High solids protein-polymeric dialde-hyde coating compositions
US1609506A (en) Method of plasticizing phenolic molding materials
US2042795A (en) x jjd ih
US2093213A (en) Plastic composition and the method of compounding the same
US2876126A (en) Process of mixing fine aggregates with asphalt
JPS61211353A (en) Production of flame-retardant polyolefin resin composition
RU2016019C1 (en) Method of producing bitumen polymer mastic

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee