Additive fire retardants, process for their preparation and polymeric compositions containing them

Abstract

Novel fire retardant compounds are disclosed, which are poly-halogenated TMPI and MPI compounds containing three or more halogen atoms per molecule. A process for the preparation of these compounds and polymeric compositions containing them are also described.

Description

FIELD OF THE INVENTION

This invention refers to additive fire retardants, to processes for their preparation and to polymeric compositions containing them. More specifically, the additive fire retardants are halogenated derivatives of indan, and more specifically halogenated 1,1,3-trimethyl-3-phenyl indan (hereinafter briefly designated as TMPI) and halogenated 1-methyl-3-phenyl indan (hereinafter briefly designated as MPI). Said compounds are useful as fire retardants for a wide spectrum of resins, among them in particular ABS, polyamides, polyolefins, engineering thermoplastics, polyurethanes, and high impact polystyrene (HIPS), rubbers and thermosets. These flame retardants can also be used to produce flame retarded textiles.

BACKGROUND OF THE INVENTION

Fire retardation of polymeric compositions is a widespread requirement and a wide spectrum of fire retardants have been developed. A number of them are halogenated compounds. However fire retarded polymeric compositions, in particular those which contain halogenated fire retardants as additives, suffer from various deficiencies, in particular those due to thermal instability, to poor impact properties and to enhanced sensitivity to ultraviolet light irradiation.

It is a purpose of this invention to provide novel fire retardants which are free from these disadvantages, and in particular are thermally stable, impart good impact properties, and do not impart to polymeric compositions containing them higher sensitivity to ultraviolet irradiation.

It is another purpose of this invention to provide processes for the manufacture of said fire retardants.

It is a further purpose of this invention to provide polymeric compositions which contain said fire retardant as additives and have good mechanical properties, thermal stability and resistance to ultraviolet irradiation.

The fire retardants of this invention are additive fire retardants, and they are derivatives of phenyl indans, more specifically 1-methyl-3-phenyl indan (MPI) and 1,1,3-trimethyl-3-phenyl indan (TMPI). MPI can be obtained by condensing two molecules of styrene. It has been suggested as a starting material for the manufacture of anthraquinone (see Kirk-Othmer, Encyclopedia of Chemical Technology, vol. 3, p.705).

The preparation of TMPI by dimerization of alpha-methylstyrene is disclosed in DE 2,906,294. DE 2,659,597, U.S. Pat. No. 3,161,692 and Petropoulos and Fisher in J. Am. Chem. Soc., 80, 1938 (1958) relate to the dimerization of alpha-methylstyrene and/or ring alkylated alpha-methyl styrenes to yield the corresponding non-halogen containing TMPI compounds. EP 138766 gives an example of the dimerization of 4-chloro-alpha-methylstyrene to produce 6-chloro-1,1,3-trimethyl-1-(4'-chlorophenyl) indan. These products were used as heat transfer fluids and chemical intermediates for polymer manufacture.

U.S. Pat. No. 4,205,160 describes terpolymers of TMPI together with 2,4-diphenyl-4-methyl-2-pentene and 2,4-diphenyl-4-methyl-1-pentene. J. C. Wilson in the Journal of Polymer Science: Polymer Chemistry Edition 13, 749 (1975) describes various TMPI-based polyamides and polyesters. C. W. Paul et al describe in U.S. Pat. No. 4,988,785, resin compositions based on biphenol compounds which are TMPI derivatives.

SUMMARY OF THE INVENTION

The fire retardant additives according to the invention are characterized in that they are poly-halogenated TMPI and MPI compounds containing three or more halogen atoms per molecule, or mixtures of such compounds.

A process for the preparation of the compounds according to the invention consists in the dimerization of one or more appropriately halogen substituted alpha-methyl styrene or halogen-substituted styrene compounds.

Another, preferred, process for the manufacture of the compounds according to the invention is the ring halogenation of TMPI or MPI.

Said ring halogenation is preferable carried out by reacting the TMPI or MPI substrate with an halogenating agent in an organic solvent in the presence of a catalyst.

The fire retarded polymeric compositions according to the invention comprise a polymeric base and from 0.1 to 60% and preferably from 1 to 40% by weight of a fire retardant additive according to the invention.

Other fire retardants may be added to the polymeric compositions. Among them may be mentioned, by way of example, halogenated or non-halogenated organo-phosphorous compounds, oxides, sulfides or organic salts of antimony, boron or arsenic, zinc borate, magnesium oxide and hydroxide, aluminum trihydrate, as well as other haloorganics, such as decabromodiphenylether, chlorinated polyethylene and chlorinated PVC.

Further, conventional additives may be added to the polymeric compositions according to the invention. These may comprise other fire retardants, antioxidants (such as Irganox), processing aids, (e.g. lubricants), impact modifiers, UV stabilizers (such as Tinuvins), fillers, fiber reinforcements, smoke suppressors and pigments.

DESCRIPTION OF THE DRAWINGS

FIGS. 1 to 14 are HPLC chromatograms, TGA analysis graphs, IR spectra and .sup.1 H NMR spectra characterizing the examples of embodiments of the invention hereinafter described, as specified in each example.

DETAILED DESCRIPTION OF PREFERRED EMBODIMENTS

In preparing the fire retardant additives according to the invention by ring halogenation of TMPI or MPI, the preferred halogenation agents are elemental halogens, in particularly bromine and chlorine, but other halogenation agents known in the art, such as bromates, HX (wherein X is Cl or Br) plus hydrogen peroxide etc., can be used. The halogenation is carried out in an organic solvent. The organic solvent medium should be substantially anhydrous and be inert or exhibit low reactivity towards the reactants. Organic solvents free of non-aromatic carbon-to-carbon unsaturation are preferred. Especially useful are halogenated, particularly chlorinated, saturated aliphatic hydrocarbons, such as carbon tetrachloride, chloroform, tetrachloroethane, methylene chloride, trichloroethane, dibromoethane, dibromethane (DBM), and the like. Acetic acid, chlorobenzene and acetonitrile can be used too. Particularly preferred is dibromomethane.

The molar ration of the halogenating agent to the TMPI or MPI depends on the degree of halogenation desired. A slight excess over stoichiometric ration is desirable.

The catalyst is preferably a metal or metal halide Lewis acid catalyst, that is capable of effecting the halogenation on the aromatic rings. Examples are the bromides and chlorides of aluminum and iron and mixtures thereof. Specific examples are AlCl.sub.3, AlBr.sub.3, FeBr.sub.3, SbCl.sub.3, SbCl.sub.5, SbClBr.sub.4, TiCl.sub.4, SuCl.sub.2, SuCl.sub.4, BeCl.sub.2, CdCl.sub.2, ZnCl.sub.2, BF.sub.3 BBr.sub.3, BCl.sub.3, ZrCl.sub.4. Iodine can also be used. The most preferred catalyst is Fe. The catalysts are used in amounts of at least 1% by weight, based on the weight of indan. Amounts of about 5-10% are preferred. The halogenation is carried out at temperatures comprised between 15.degree. and 100.degree. C., and preferably between 50.degree. and 70.degree. C.

The ring halogenation of TMPI and MPI will generally produce a mixture of compounds having different halogenation degrees, but this is not a drawback because all those compounds are suitable as fire retardant additives. Therefore, when reference is made in this specification to compounds according to the invention, mixtures of such compounds are intended to be included.

The dimerization of styrene derivatives will generally yield a given compound: thus the dimerization of 3,5-dibromo-alpha-methylstyrene will produce 5,7-dibromo-1,3,3- trimethyl-1-(3',5'-dibromophenyl) indan exclusively. The dimerization can be carried out for example as disclosed in EPA 138,766, in the article by L. M. Adams, R. J. Lee and F. T. Wadsworth, J. Org. Chem., 24, 1186 (1959) and in the article by Petropoulos and Fisher hereinbefore cited. However, not all such styrene derivatives are adapted for dimerization, but only those in which at least one ortho position in respect to the alkylene group is free for cyclization to occur.

The fire retardant compounds according to the invention are added to thermoplastic polymers to produce fire retarded polymer compositions by mixing, usually at high temperature, with the polymer. The mixing technique is conventional and can be carried out in conventional equipment without any particular difficulties, especially since the fire retardants according to the invention are highly thermally stable. It is also possible to produce a masterbatch concentrate containing more than 30% of the fire retardant according to the invention, and in some cases synergists; this masterbatch can be diluted in the final resin compositions. When the polymer is a polyurethane, the fire retardants are added to one of its components.

The ring halogenation of TMPI produces compounds having the following general formula I (wherein X is Br or Cl): ##STR1##

Similarly, the ring halogenation of MPI produces compounds having the general formula II: ##STR2##

The degree of halogenation is expressed by the sum: m+n. It is controlled by the molar ration between the halogenating agent and the TMPI or MPI substrate. It also depends on the concentration (dilution) of the reagents, the temperature and the time of the reaction, and the strength of the catalyst.

TMPI and MPI substituted by three or more halogen atoms are novel compounds. TMPI substituted by two chlorine atoms has been described, as mentioned hereinbefore, in EP 138,766, but its use as fire retardant has not been suggested.

The fire retardant compounds according to the invention not only impart fire retardancy to the polymeric compositions which contain them, but they provide good physico-mechanical properties and resistance to degradation of the products containing them under UV radiation. This latter is a particular surprising feature, since compounds containing high concentrations of halogens, particularly bromine, in their structure, usually promote UV-degradation. Further, the unexpected high thermal stability of the compound according to the invention makes them particularly suitable for application in engineering thermoplastics.

The unexpected high solubility of the compounds according to the invention (12% in toluene at 100.degree. C.) provides a further advantage of the invention: the reactor and processing utilities can be cleaned of them easily.

A number of embodiments of the invention will now be described.

EXAMPLE 1

Preparation of Partially Brominated TMPI

Into a 3-necked flask (250 ml) equipped with a mechanical stirrer, a reflux condenser and a thermocouple, were added Br.sub.2 (35 g; 0.22 mol, 5.5 molar fold over TMPI); Fe (0.75 g; 13.4 mmol) and DBM (1.00 g). A solution of TMPI (9.45 g, 40 mmol) in DBM (30 g) was added dropwise to the stirred suspension at 35.degree.-65.degree. C. during 2 hrs (the released HBr was trapped in aqueous NaOH). When the reflux of Br.sub.2 ceased, water was added to the reaction flask, and the aqueous phase was removed. Then, a solution of Na.sub.2 S.sub.2 O.sub.5 was added to neutralize the residual Br.sub.2, and the aqueous phase was removed. Next, water was added again to wash the organic phase, and the aqueous phase was removed. The organic phase was filtered, and the solvent was evaporated. The residue (25 g) solidified. Elementary analysis: found for Br 63.9% (calculated for C.sub.18 H.sub.16 Br.sub.5 63.2). The residue consisted of several compounds. The HPLC chromatogram (FIG. 1) showed 3 major peaks.

The TGA (FIG. 2) analysis showed a weight loss of 5% at 257.degree. C., 10% at 297.degree. C. and a major peak at 371.degree. C.

IR (FIG. 3; cm.sup.-1); 3420, 2960, 2920, 2840, 1780, 1590, 1520, 1450, 1370, 1310, 1270, 1110, 1020, 875, 820, 785, 740.

.sup.1 H NMR (FIG. 5; .delta., in TCE): the spectrum is very complex due to the presence of many isomers in the sample (HPLC spectrum). Three main groups of chemical shifts are characteristic of halogenated TMPI: aromatic hydrogens observed as different singlets (between .delta. 7 and 8 ppm); the methylenic hydrogens of the cyclopentane ring of the indan observed as AB quartets between .delta. 2 and 3 ppm; and the methyl groups appearing as sharp peaks between .delta. 1 and 2 ppm.

EXAMPLE 2

Preparation of Partially Chlorinated TMPI

Into a 3-necked flask (250 ml) equipped with a mechanical stirrer, a reflux condenser and a thermocouple, were added AlCl.sub.3 (5.6 g; 42 mmol), CCl.sub.4 (130 ml) and TMPI (19.8 g, 84 mmol). Cl.sub.2 (30 g; 422 mmol; 5 molar fold over TMPI) was passed into the stirred solution through a dip-tube (3.5 hrs) at a rate which maintained the reaction temperature of 35.degree.-38.degree. C. (cooling of the reaction mixture with a water bath if necessary). The reflux condenser was cooled to -20.degree. C. (ethylene glycol) in order to avoid losses of Cl.sub.2 with the evolution of HCl (the released HCl was trapped in aqueous NaOH). Thirty minutes after the addition of all the Cl.sub.2, the evolution of HCl ceased. The reaction mixture was heated to 50.degree. C., and held at that temperature for 30 min. more. The reaction mixture was washed with water (100 ml). Then, a solution of Na.sub.2 S.sub.2 O.sub.5 was added to neutralize the residue of Cl.sub.2, and the aqueous phase was removed. Water was added again to wash the organic phase, and the aqueous phase was removed. The organic phase was treated with active carbon, filtered and the solvent was evaporated. A brown oily layer was obtained (23.5 g). Elementary analysis found: C52.1; H 4.2 and Cl 42.3% (for comparison purposes only, the values calculated for C.sub.18 H.sub.16 Cl.sub.5 are: C 52.8; H 3.9; Cl 43.3%).

The GC/MS (FIG. 5 & 6) spectrum reveals many peaks which were attributed to different isomers of partially chlorinated TMPIs: peaks between r.t. of 12.25 to 17.14 min. were identified (% area) as one trichlorinated isomer (3.1%; Mw 338), seven tetrachlorinated isomers (with a total of 50.3%; Mw 372) and eight pentachlorinated isomers (with a total of 37.4%; Mw 406). Small peaks (the remaining 10%; area %) are observed at r.t. 17.5-22. min. and are assigned to hexa- hepta and octa- isomers (i.e. the peak 19.5 min. was identified as a hexachlorinated TMPI, Mw 440). TGA (FIG. 7): 5% at 122.degree. C., 10% at 166.degree. C. and a major peak at 315.degree. C.

IR (FIG. 8; cm.sup.-1): 2960, 2920, 2840, 1580, 1560, 1460, 1380, 1360, 1310, 1270, 890, 785, 760.

.sup.1 H NMR (FIG. 9; .delta., in CDCl.sub.3): the spectrum is very complex due to the presence of many isomers in the sample (GC/MS analysis). Three main groups of chemical shifts are characteristic of a halogenated TMPI: aromatic hydrogens observed as different singlets (between .delta. 7 and 8 ppm); the methylenic hydrogens of the cyclopentane ring of the indan observed as AB quartets between .delta. 2 and 3 pm; and the methyl groups appearing as sharp peaks between .delta. 1 and 2 ppm.

The HPLC chromatogram is shown in FIG. 10.

EXAMPLE 3

Preparation of Octabromotrimethylphenyl Indan (OBITMPI) ##STR3##

This preparation is carried out in two cycles.

First Cycle

Into a 3-necked flask (5 liter) equipped with a mechanical stirrer, a reflux condenser and a thermocouple, were added Br.sub.2 (1619 g; 10.1 mol); Fe (7.7 g; 0.14 mol) and dibromomethane (DBM, 2938 g; 1906 ml). A solution of TMPI in DBM �9.5% of 2732 g; (259.6 g TMPI; 1.1 mol)!, was added dropwise to the stirred suspension at 25.degree.-40.degree. C., during 3.5 hrs, (the released DBr was trapped in aqueous NaOH). Mixing was continued for another 2.5 hrs at 40.degree.-75.degree. C. Another portion of Fe (4.4 g; 78.7 mmol) was added to the reaction mixture one hour before the end of the reaction. Water was added, to wash out the iron salts. The aqueous phase was removed. The organic layer was treated with aq. Na.sub.2 S.sub.2 O.sub.5, filtered, washed with water, neutralized with Na.sub.2 CO.sub.3 solution, washed again with water, with 800 ml acetone and then dried. An off-white solid (500 g) was obtained. The DBM layer, dried with anhydrous Na.sub.2 SO.sub.4, was kept for the next cycle (4997 g. containing 6.7% solid).

Crystallization

The product (500 g) was dissolved in hot toluene (2250 ml), treated with active carbon (10 g) and cooled. The precipitate (after cooling) was filtered, washed with acetone and dried. A slightly yellow solid was isolated (352 g), m.p. 248.6.degree. C. Elementary analysis calculated for C.sub.18 H.sub.12 Br.sub.8 : C 24.9; H 1.4; Br 73.7%. Found: C 25.6; H 1.3; Br 73.0%. TGA (FIG. 11) 1/5% =296.degree./346.degree. C., 10%=365.degree. C. and the major peak at 426.degree. C. HPLC (FIG. 12): 3 peaks at 24.4, 26.5 and 28 min. with 3.7, 5.4 and 90.6% ratio, respectively. The major peak is assigned to the octabromo- derivative. IR (FIG. 13; KBr; cm.sup.-1); 3440, 2960, 2920, 2880, 1630, 1600, 1480, 1430, 1380, 1360, 1320, 1300, 1220, 1190, 1170, 1120, 1000, 955, 905, 850, 800, 750, 700. .sup.1 H NMR (FIG. 14; TCE; .delta.): 1.50 ppm (CH.sub.3 ; s; 3H); 1.57 ppm (CH.sub.3 ; s; 3H)l 1.78 ppm (CH.sub.3 ; s 3H); AB quartet centered at 2.27 ppm (CH.sub.2, 2H); 7.74 ppm (aromatic, s, 1H).

The concentration of the mother liquor afforded another 109 g of material of similar properties. Evaporation of the solvent to dryness left 20 g of solid.

Second Cycle

The same procedure as above was carried out.

Material used: the mother liquor from the previous run (4900 g; containing 328 g of solids); Br.sub.2 (1664 g; 10.4 mol); Fe (7.7 g; 138 mmol); A solution of TMPI (260 g, 1.1 mol) in DBM (840 g).

The TMPI solution was added dropwise during 2 hours at 28.degree.-43.degree. C. Mixing was continued (43.degree.-78.degree. C.) for 3 hours more. After 4.5 hrs (from the start) Fe (4.4 g; 78.8 mmol) was added and 30 min. later Br.sub.2 (10 ml) was added. The reaction was stopped when the evolution of HBr ceased (after a total of 5.5 hours).

The work-up was carried out as in the first cycle. A yellowish solid (880 g; 92.5% yield) was obtained. TGA: 1/5%=271.degree./338.degree. C., 10%=363.degree. C. and a major peak at 436.degree. C. HPLC: 3 peaks at 23.9, 26 and 27.4 min. with a ration of 3.8, 6.4 and 89.3%, respectively.

Crystallization

The above solid (855 g) was dissolved in hot toluene (reflux; 18% concentration, 4.7 liters) and 13 g of active charcoal were added. The precipitate was washed with toluene and with acetone. The dry solid (590 g) was obtained in 69% yield; m.p. 248.6.degree. C. TGA: 1/5%=294.degree./348.degree. C., 10%=370.degree. C. and the major peak at 437.degree. C. HPLC: 3 peaks at 24.6, 26.8 and 28.3 min. with a ratio of 2.7, 5.2 and 91.8%, respectively. Elementary analysis, calculated for C.sub.18 H.sub.12 Br.sub.8 : C 24.9; H 1.4; Br 73.7%. Found: C 25.7; H 1.4; Br 73.2%.

Concentration of the mother liquor to 20% of its weight afforded a second crop of a solid of similar properties after washing with toluene and acetone and drying (190 g; 22% yield). TGA: 1/5%=302.degree./346.degree. C., 10%=365.degree. C. and a major peak at 423.degree. C. HPLC: 3 peaks at 24.3, 26.5 and 28 min. with a ratio of 3.6, 7.0 and 89.1%, respectively. Elementary analysis, found: C 25.4; H 1.2; Br 73.1%.

EXAMPLE 4

Preparation of Partially Brominated 1-methyl-3-phenylindan (MPI)

Following the procedure used in Example 1, 20.8 g. (0.1 mole) of MPI was brominated with 88 g. (0.55 mole) of bromine in a total of 200 g DBM as solvent, using 1.5 g. Fe as catalyst. The isolated product (55 g.) contained 65.2% Br (calculated for C.sub.16 H.sub.11 Br.sub.5, 66.3% Br).

EXAMPLE 5

Preparation of a Fire-Retardant Polyester

To 15 g of a liquid polyester (410 brand, Fiberplast Ltd.) there were added OBTMPI (73.1% Br; 1.1 g), twelve drops of a 7% cobalt octoate solution and 3 drops of methyl ethyl ketone peroxide at ambient temperature with mixing. The mixture was quickly cast into a Teflon mould containing cavities of dimensions 6.times.100.times.3 mm. Curing was performed at ambient temperature for 24 hrs and then in an oven at 100.degree. C. for 2 hrs. The specimens were removed and left to cool and the LOI (Limiting Oxygen Index) was measured and compared with that of an identically prepared sample not containing the fire retardant compound. The LOI of the control specimen was 17.5 LOI for 5% loading (only 3.6% Br) was 19.6.

EXAMPLE 6

Application Tests with Several Thermoplastic Resins

Several resins were compounded with OBTMPI as fire retardant. The formulations (Tables 1-3) were prepared in a Brabender Plasticorder, and samples for the evaluation of product performance were molded at temperatures appropriate for each resin.

The compounding and press temperatures were as follows:

______________________________________ Temperature ofResin Table Compounding Molding______________________________________ABS 1 220.degree. C. 200.degree. C.Polyamide 2 260 250Polypropylene 3 230 200HIPS 4 230 200______________________________________

The flammability and mechanical properties obtained are recorded in the tables. Their definition is as follows:

Flammability

UL-94 vertical burning test in a flammability hood (according to UL); Limiting oxygen index (LOI) (ASTM D 2863-77) on a FTA Flammability Unit Stanton Redcroft.

Izod Notched Impact Energy

(ASTM D 256-81) on a Pendulum impact tester type 5102 Zwick.

HDT

Deflection temperature under flexural load (18.5 kg/cm.sup.2) (ASTM D 648-72) on a CEAST 6055.

U.V. Stability

Accelerated weathering test-irradiation for 250 hrs and measuring of the color change by color deviation, on an Accelerated Weathering Tester Q-U-V (B-lamps), (The Q-Panel Co.).

Color Deviation

Color measurement and comparison with reference specimen, on a Spectro Color Meter SCM-90, (Techno-Instruments Ltd.).

TABLE 1______________________________________COMPARISON BETWEEN OBTMPI ANDOCTABROMODIPHENYL ETHER (OCTA) IN ABS______________________________________COMPONENTS %ABS NOVODUR P2H AT (BAYER) 75.3 75.7OBTMPI 15.8OCTA 15.4ANTIMONY TRIOXIDE 7.7 7.7ADDITIVES 1.2 1.2PROPERTIESBROMIDE CONTENT % 12 12FLAMMABILITY-UL94 (1.6 mm) VO VOUV STABILITY-QUV (250 H), DE 41 44HDT (264 psi), C 84 81______________________________________ TABLE 2______________________________________USE OF OBTMPI IN NYLON 6______________________________________COMPONENTS %NYLON 6 CAPRON 8022HS (ALLIED) 72.6OBTMPI 19.2ANTIMONY TRIOXIDE 6.8HOSTAFLON TF 8202 (HOECHST) 1AC-400A (ALLIED) 0.4PROPERTIESBROMINE CONTENT % 15FLAMMABILITY-UL94 (1.6 mm) VOIZOD NOTCHED IMPACT, J/m 49HDT (264 psi), C 51______________________________________ TABLE 3______________________________________COMPARISON BETWEEN OBTMPI ANDDECABROMODIPHENYL ETHER (DECA) IN HIPS______________________________________COMPONENTS %HIPS VESTYRON 638 (HUELS) 81.9 83OBTMPI 13.2DECA 12.2ANTIMONY TRIOXIDE 3.8 3.7ADDITIVES 1.1 1.1PROPERTIESBROMINE CONTENT, % 10 10FLAMMABILITY-UL94 (3.2 mm) VO VOIZOD NOTCHED IMPACT, J/m 52 48UV STABILITY-QUV (250 H) YELLOWNESS INDEX 51 60______________________________________

EXAMPLE 7

Application of Brominated Methylphenylindans as Fire Retardants in Polyurethanes

The products of Examples 2 and 3 were incorporated into polyurethane foams in the following manner.

A sorbitol-based polyether polyol having an hydroxyl number of 490 mg KOH/g served in two parallel application tests. In each of the tests, 1.38 g of Santicizer 141 (an alkyl-aryl phosphate produced by Monsanto), 0.25 g water, 1.0 g of a silicone surfactant and 1.0 g of dimethylcyclohexylamine as catalyst. When homogeneity was observed, 15.0 g of Freon 11 were added to each mixture, which were then stirred vigorously for 45 seconds. Diphenylmethane diisocyanate (MDI, 51.2 g) was then added to each and stirring was continued for 5 seconds more. The mixtures were poured into cardboard boxes lined with wrapping paper and left to rise freely. The cream times (measured from the moment of MDI introduction) were 31 and 40 seconds, respectively, whereas the rise times were 282 and 253 seconds, respectively. The foams obtained had Limiting Oxygen Indexes of 23.3 and 23.5 versus 18.6 for the blank foam, i.e. containing no fire retardant.

EXAMPLE 8

Preparation of an Epoxy Specimen (In a 1:1 Base:Hardener Epoxy)

To 15 g of a liquid resin (Araldite-rapid; Ciba-Geigy, Nr. 92.7251) there were added the halogenated TMPI (see table), 15 g of liquid hardener (Araldite-rapid Ciba-Geigy, Nr. 92.7522) at ambient temperature with mixing. The mixture was quickly cast into a Teflon mould containing cavities of dimensions 6.times.100.times.3 mm. Curing was performed at ambient temperature for 30 min. and then in an oven at 100.degree. C. for 2 hrs. The specimens were removed and left to cool and the LOI (Limiting Oxygen Index) was measured and compared with that of an identically prepared sample not containing the fire retardant compound. The LOI of the control specimen and of the specimens containing the halogenated compound are given below:

______________________________________ Composition of specimen Base:hardener:sample % Hal.% Hal. in FR (g):(g):(g) in specimen LOI______________________________________blank 15:15:0 0 19.473.1 Br 15:15:4.74 10 22.973.1 Br 15:15:2.37 5 21.442.9 Cl 15:15:4.55 10 20.7blank 10:20:0 0 17.932.9 Cl 10:20:4.55 10 20.642.9 Cl 10:20:9.1 20 22.8______________________________________

A number of embodiments of the invention have been described, but it will be understood that the invention can be carried out with many variations, adaptations and modifications, by persons skilled in the art, without departing from its spirit or exceeding the scope of the claims.

Claims

1. Process for the preparation of a polyhalogenated 1,1,3-trimethyl-3-phenylindan, i.e., TMPI or 1-methyl-3-phenylindan, i.e., MPI containing three or more halogen atoms per molecule comprising the ring halogenation of TMPI or MPI with a halogenation agent in an organic solvent in the presence of a catalyst, wherein said catalyst is a metal or metal halide Lewis acid catalyst selected from the group consisting of aluminum and iron bromides and chlorides and mixtures thereof.

2. Process for the preparation of a polybrominated 1,1,3-trimethyl-3-phenyl indan, i.e., TMPI or 1-methyl-3-phenyl indan, i.e., MPI containing three or more bromine atoms per molecule, comprising the ring bromination of TMPI or MPI with a bromination agent in an organic solvent in the presence of a metal or metal halide Lewis acid catalyst selected from among aluminum and iron bromides and mixtures thereof.

3. Process according to claim 1, wherein the catalyst is used in amounts of at least 1% by weight, based on the weight of the indan.

4. Process according to claim 1, wherein the halogenation agent is an elemental halogen.

5. Process according to claim 1, wherein the organic solvent is a halogenated hydrocarbon, acetonitrile or acetic acid.

6. Process according to claim 1, wherein the halogenation is carried out at temperatures from 15.degree. to 100.degree. C.

7. Process according to claim 2, wherein the catalyst is selected from the group consisting of Fe, AlCl.sub.3, AlBr.sub.3, FeBr.sub.3, SbCl.sub.3, SbCl.sub.5, SbClBr.sub.4, TiCl.sub.4, SnCl.sub.2, SnCl.sub.4, BeCl.sub.2, CdCl.sub.2, ZnCl.sub.2, BF.sub.3, BBr.sub.3, BCl.sub.3, ZrCl.sub.4 and iodine.

8. Process according to claim 2, wherein the catalyst is used in amounts at least 1% by weight, preferably about 5-10%, based on the weight of the indan.

9. Process according to claim 2, wherein the bromination agent is elemental bromine.

10. Process according to claim 2, wherein the organic solvent is a halogenated hydrocarbon, acetonitrile or acetic acid.

11. Process according to claim 2, wherein the halogenation is carried out at temperatures from 15.degree. to 100.degree. C.

12. A process according to claim 1 wherein the catalyst is used in amounts of from 5 to 10%, based on the weight of the indan.

13. A process according to claim 8 wherein the catalyst is used in amounts of from 5 to 10%, based on the weight of the indan.