Polysiloxane-polyoxyalkylene terpolymers for polyurethane foam manufacture

BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention provides polysiloxane-polyoxyalkylene terpolymers for the manufacture of conventional flexible polyurethane foam. The invention also provides a process for producing conventional flexible polyurethane foam formulations using these terpolymers as foam stabilizers, including flame retardant foams. The invention further provides conventional flexible polyurethane foam produced using the terpolymers of the invention including flame retardant flexible polyurethane foams.
2. Description of Prior Art
Polysiloxane-polyoxyalkylene copolymers were first disclosed in U.S. Pat. No. 2,834,748 (Bailey et al., 1958). These compositions were of the hydrolyzable type. Non-hydrolyzable polysiloxane-polyoxyalkylene copolymers were first disclosed in U.S. Pat. No. 2,846,458 (Haluska, 1958).
The first use of polysiloxane-polyoxyalkylene copolymers for the stabilization of one-shot flexible polyurethane foam appeared in Brit. Pat. No. 892,136 (Hostettler, 1958). The stabilizers so described were of the hydrolyzable variety. The application of non-hydrolyzable copolymers to the stabilization of polyurethane foams soon followed.
U.S. Pat. No. 4,478,957 discloses the use of certain polysiloxane-polyoxyalkylene block copolymers for the production of highly resilient, cold-curing polyurethane foams. These copolymers as defined are limited to lower molecular weight species (less-than-or-equal-to an average of 25 silicon atoms in the siloxane chain) and contain at least two polyoxyalkylene blocks, which are formed from oxyethylene and oxypropylene units, wherein one such block has a weight percent oxyethylene range of from 38 to 100% (45-100 mole %) and the other such block has an oxyethylene weight percent range of from 0 and 57% (0-50 mole %). The molecular weights of the polyoxyalkylene blocks are both between 150 and 1200 and the molar ratio of one block to another falling in the range of 0.25 to 4.00.
These block copolymer compositions showed improved stabilizing properties and formed open-cell high resilient foams at a relatively wide processing latitude. Those skilled in the art recognize that siloxane surfactants for high resilient (HR) urethane foam provide insufficient stabilization for conventional flexible urethane foam since HR surfactants serve primarily as cell control agents in the inherently more stable high resilient foam formulations.
Additionally, U.S. Pat. No. 4,031,044 discloses the use of polysiloxane-polyoxypropylene copolymers for the stabilization of high resilient polyurethane foams which have low shrinkage and are free of voids without sacrifice of other important physical properties. Again, those skilled in the art realize the inapplicability of HR surfactants in conventional flexible urethane systems.
OBJECTS OF THE INVENTION
It is an object of the invention to produce polysiloxane-polyoxyalkylene compositions for use as stabilizers in the production of polyurethane foam, including flame retardant foams.
Another object of the invention is to provide such compositions which allow the production of an open foam using a wide variety of concentrations of these compositions as stabilizers. This will be referred to as improved breathability latitude.
A further object of the invention is to provide such a stabilizer which can be used to produce flame retardant conventional flexible polyurethane foam.
Other objects will become apparent from the description and examples.
SUMMARY OF THE INVENTION
The present invention provides certain polysiloxane-polyoxyalkylene compositions and their use as stabilizers in the manufacture of polyether polyurethane foam. More particularly, the present invention provides such compositions, which have a polysiloxane chain substituted with at least two types of polyoxyalkylene polymers as pendants from the silicon atoms of the polysiloxane.
The polysiloxane chain is linear or branched and can have average molecular weights of up to 30,000 or higher, excluding the weight of the polyoxyalkylene polymers.
The distinctive feature of these compositions is the specific selection of polyoxyalkylene polymers. Preferably the polyoxyalkylene polymer pendants are provided as at least three different polyoxyalkylene polymers. One of these polyoxyalkylene polymers is composed of only oxypropylene units. This polyoxypropylene has an average molecular weight from about 130 to about 1200 excluding link and endcap. The other polyoxyalkylene polymers are composed of both oxyethylene and oxypropylene units.
The polysiloxane-polyoxyalkylene compositions of the invention are of the nominal formula: ##STR2## wherein R is an alkyl group having 1 to 3 carbon atoms and R.degree., R', R" and R'" are individually monovalent polyoxyalkylene polyethers attached to the silicon atom through a difunctional link (e.g., --C.sub.2 H.sub.4)O--, --C.sub.3 H.sub.6)O--; and
the polyoxyalkylene of R' is a poly(oxyethylene-oxypropylene) ether which contains 20% to 60% oxyethylene by weight and has an average molecular weight of from about 3,000 to about 5,000;
the polyoxyalkylene of R" is a poly(oxyethylene-oxypropylene) ether which contains 20% to 60% oxyethylene by weight and has an average molecular weight of from about 800 to about 2,900; and
the polyoxyalkylene of R'" is a polyoxypropylene polyether having an average molecular weight from about 130 to about 1200; R.degree. can be R', R" or R'"; a and e are individually 0 or 1; b, c and d are numbers such that b+c+d=y and where b or c may be zero, but not both; x and y are positive numbers such that the sum of x+y ranges from 25 to 400 and x is greater than y, wherein the ratio (b+c):d ranges from 0.8 to 1.9.
DETAILED DESCRIPTION OF THE INVENTION
In accordance with the objects of the invention the present invention provides a polysiloxane-polyoxyalkylene composition comprising polysiloxane and specific organic blocks as described below.
The end groups of the polysiloxane are silicon atoms with three organic substituents [(R.sub.3-a R.degree..sub.a --Si-- and --SiR.degree..sub.e R.sub.3-e)] as shown above. The silicon atom of the end group is attached to the terminal oxygen atom of the polysiloxane chain.
As stated above, R is an alkyl group having from 1 to 3 carbon atoms. R.degree. can be any of the polyoxyalkylene polyethers attached to the silicon atom through a difunctional link, which are designated R', R", R'', and are described in more detail below. In the above formula, a and e are individually 0 or 1.
As can be seen from the general formula, the compositions of the present invention are made up of four general difunctional siloxy units having organic substituents. The first unit contains only R as its substituents and this unit is present in an amount "x." The other three units, which contain polyoxyalkylene ethers are present in amounts "b", "c" and "d", respectively. The sum of b+c+d=y, the total number of polyoxyalkylene containing siloxy units in the polymer. The number x is greater than y and the sum of x+y ranges from 25 to 400.
The numerical ratio x:y can vary over a broad range. Generally this range is from about 3:1 to about 15:1. If the terpolymer is to be used as a surfactant in a flame retardant formulation it is preferred that the ratio of x:y be less than about 10:1.
Polyoxyalkylene Polyethers
The compositions of the invention contain poly(oxyethylene-oxypropylene) ether and poly(oxypropylene) ether as pendants from the polysiloxane.
Preferably, the terminal group of the polyoxyalkylene polyethers is any alkoxy group having 1 to 4 carbon atoms or an acyloxy group of a lower aliphatic carboxylic acid. The preferred terminal group of the polyoxyalkylene polyethers is an acetoxy group.
These polyethers are attached to silicon atoms in the polysiloxane through a difunctional link. The difunctional link is of the formula --C.sub.n H.sub.2n)O-- wherein n is a number from 0 to 6. Usually n is a number from 0 to 4. Preferably n is 3 or 4.
Poly(Oxyethylene-Oxypropylene) Polyethers
The poly(oxyethylene-oxypropylene) polyethers contain from 20% to 60% oxyethylene by weight, with the balance of the weight, excluding the link and terminal groups, made up of oxypropylene. Preferably the poly(oxyethylene-oxypropylene) polyether is 40% oxyethylene by weight.
It is preferred that the composition contain two poly(oxyethylene-oxypropylene) ether components of different average molecular weights.
The average molecular weight of the first, or higher molecular weight, poly(oxyethylene-oxypropylene) component (R') is generally from about 3,000 to about 5,500. The average molecular weight of the second, or lower molecular weight poly(oxyethylene-oxypropylene) component (R") is generally from about 800 to about 2,900.
The higher molecular weight poly(oxyethylene-oxypropylene) component, R', can be provided as (i) a poloxyalkylene copolymer having an average molecular weight in the range of from about 3000 to about 5500 wherein about 20 to about 60 weight percent of the oxyalkylene groups of said copolymer are oxyethylene, the remainder of the oxyalkylene groups being oxypropylene, or (ii) a blend of at least two polyoxyalkylene copolymers having different average molecular weights in the range of from about 3000 to about 5500 and wherein about 20 to 60 weight percent of the oxyalkylene groups of the copolymers in said blend are oxyethylene, the remainder of the oxyalkylene groups being oxypropylene, with the proviso that said blend has an average molecular weight in the range of from about 3000 to about 5500.
Similarly, the lower molecular weight poly(oxyethylene-oxypropylene), R", can be provided as (i) a polyoxyalkylene copolymer having an average molecular weight in the range of from about 800 to about 2900 wherein about 20 to about 60 weight percent of the oxyalkylene groups of said copolymer are oxyethylene, the remainder of the oxyalkylene groups being oxypropylene, or (ii) a blend of at least two polyoxyalkylene copolymers having different average molecular weights in the range of from about 500 to about 2900 and wherein about 20 to about 60 weight percent of the oxyalkylene groups of the copolymers in said blend are oxyethylene, the remainder of the oxyalkylene groups being oxypropylene, with the proviso that said blend has an average molecular weight in the range of from about 800 to 2900.
The higher molecular weight polyether component, R', is present in an amount designated as "b". The lower molecular weight polyether component, R", is present in an amount designated as "c". The proportions of R' and R" are generally such that
b/b+c=from 1 to 0,
The two polyether components are preferably used in proportions such that the blend average molecular weight of the two poly(oxyethylene-oxypropylene) polyethers is from about 2,400 to about 3,400.
About 20 to 60 weight percent of the oxyalkylene groups of the polyoxyalkylene copolymers (be they low or high molecular weight polyoxyalkylene polyethers) must be oxyethylene, the remainder of the oxyalkylene groups of said copolymers being oxypropylene. Of course, it is to be understood that the oxyethylene and oxypropylene groups of said copolymers may be present in the polyoxyalkylene block in a random or block fashion. The expression poly(oxyethylene-oxypropylene) copolymers as employed herein is used to represent copolymers in which oxyalkylene groups are present in random distribution (and indeed such is preferred) as well as copolymers in which the oxyalkylene groups are present as blocks. Therefore, in no way should the expression poly(oxyalkylene-oxypropylene) copolymer be interpreted as merely encompassing copolymers in which oxyalkylene groups are present in blocks, i.e., a block of oxyethylene and a block of oxypropylene. Of course, it is to be also understood that the term propylene oxide employed herein refers to 1,2-propylene oxide and the oxypropylene radical derived therefrom.
Polyoxypropylene Polyether
The third polyoxyalkylene polyether, R'", is a polyoxypropylene polyether.
The molecular weight of the polyoxypropylene polyether, R'" is generally greater than about 130. Usually the molecular weight of the polyoxypropylene is from about 130 to about 1200. The preferred molecular weight range for the polyoxypropylene is from about 200 to about 1,000. As with the other polyoxyalkylene components the polyoxypropylene may also be provided as a blend of at least two polyoxypropylene polyethers to provide a blend having an average molecular weight in the stated ranges.
Some of the polyoxypropylene polyether can be left uncapped; that is the terminal group is hydroxyl attached to the terminal carbon atom.
The polyoxypropylene R'" is present in an amount "d". The molar ratio of poly(oxyethylene-oxypropylene) pendants to poly(oxypropylene) pendants expressed as (b+c):d will generally range from about 0.8:1 to about 1.9:1.
Method of Preparation
The polyoxyalkylene polyether components are well known in the art and/or can be produced by any conventional process. For instance, monohydroxy terminated polyoxyalkylene polyethers which are convenient starting materials in the preparation of the terpolymer can be prepared by reacting a suitable alcohol with ethylene oxide and propylene oxide (1,2-propylene oxide) to produce the copolymer polyether, or with propylene oxide alone to produce the polyoxypropylene ether. Suitable alcohols are alkanols, e.g., methanol, ethanol, propanol, isopropanol, butanol, tertiary butanol, and the like; hydroxy aryl compounds, e.g. phenol, and the like; hydroxy aralkyl compounds, e.g., 2-phenyl ethanol, and the like; and hydroxy alkenyl compounds, e.g., allyl alcohol, methallyl alcohol and the like. In general the alcohol starter preferably is placed in an autoclave or other high-pressure vessel along with catalytic amounts of a suitable catalyst, such as sodium hydroxide, potassium hydroxide, other alkali metal hydroxides, or sodium or other alkali metals. Further details of preparation are set forth for example in U.S. Pat. No. 3,980,688.
The above-described alcohol-oxide reaction produces a monohydroxy end-blocked polyoxyalkylene polyethers in which the other end-blocking group is an alkoxy, aryloxy, aralkyloxy, or alkenyloxy radical.
These polyethers can be converted to monoalkenyloxy terminated polyoxyalkylene polyethers by converting (capping) the hydroxyl terminal group of said monohydroxy endblocked poly(oxyethyleneoxypropylene) copolymers by any conventional means. For example, when the monohydroxy terminated polyether is started with an alkanol, hydroxy aryl or hydroxy aralkyl compound the copolymer can be reacted with an alkali metal alkoxide preferably sodium methoxide to produce the alkali metal alkoxide of the polyether which is then reacted with an alkenyl halide, preferably a chloride and especially allyl chloride or methallyl chloride, to give the desired monoalkenyloxy endblocked polyoxyalkylene polyether in which the other end-blocking group is alkoxy, aryloxy, or aralkyloxy radical. Alternatively, when the monohydroxy terminated polyether is started with an hydroxy alkenyl compound, the hydroxyl terminal group of the copolymer can be capped in the same manner using alkyl, aryl or aralkyl halides (preferably chlorides) or by esterifying said hydroxy terminal group with an acyl (preferably acetic anhydride) compound to give the desired monoalkenyloxy endblocked polyethers in which the other endblocking group is an alkoxy, aryloxy, aralkyoxy or acyloxy radical.
The method of producing the novel polysiloxane-polyoxyalkylene block terpolymers of this invention can be conducted in the same manner as any conventional known method for producing polysiloxane-polyoxyalkylene block copolymers such as described, e.g., in U.S. Pat. Nos. 2,834,748, 2,920,1150 and 3,801,616. Such conventional methods have been described above. Production of the non-hydrolyzable compositions involve the common chemical reactions of reacting, for instance, a monoalkenyloxy endblocked polyoxyalkylene polyether with a polysiloxane containing silanic hydrogen at elevated temperatures, e.g., from about 60.degree. C. to about 140.degree. C. in the presence of a catalyst such as platinum catalysts (e.g., chloroplatinic acid), and the like, and optionally in the presence of a solvent (e.g., liquid hydrocarbons, such as toluene or isopropyl alcohol and the like) for the polyoxyalkylene polyether and polysiloxane reactants. The usual conventional amounts of components and reaction conditions can be employed and such is well within the knowledge of one skilled in the art. For instance, approximately stoichiometric amounts of slightly higher of the polyoxyalkylene polyether and the functional containing polysiloxane reactants are preferred, while the amount of catalyst need obviously only be a catalytic amount. The temperature of the reaction, of course, largely depends merely on the reactants involved and the polysiloxane-polyoxyalkylene block terpolymer desired to be produced.
Production of the hydrolyzable compositions involve the common chemical reactions of reacting monohydroxyl terminated polyoxyalkylene polyether with a polysiloxane containing, for instance, alkoxy radical(s), amino radical(s) or halogen atom(s) directly attached to a silicon atom(s) of the polysiloxane at elevated temperatures, e.g. from about 60.degree. C. to about 140.degree. C. in the presence of a catalyst such as Influoro acetic acid, and the like, and optionally in the presence of a solvent (e.g., liquid hydrocarbons such as toluene and the like) for the polyoxyalkylene polyether and polysiloxane reactants.
The usual conventional amounts of components and reaction conditions can be employed and such is well within the knowledge of one skilled in the art. For instance, approximately stoichiometric amounts of slightly higher of the polyoxyalkylene polyether and the functional containing polysiloxane reactants are preferred, while the amount of catalyst need obviously only be a catalytic amount. The temperature of the reaction, of course, largely depends merely on the reactants involved and the polysiloxane-polyoxyalkylene block composition desired to be produced.
Of course, it is to be understood that the polysiloxane-polyoxyalkylene block copolymers of this invention can contain small amounts of other siloxy units, e.g., SiH groups (owing to incomplete reaction thereof with the polyoxyalkylene reactant) and/or Si-alkoxy or Si--OH groups owing to the incomplete hydrolysis and condensation of the silanes used to produce the siloxane reactant.
Preparation of Conventional Flexible Polyurethane Foam
In addition to the novel polysiloxane polyoxyalkylene compositions of the present invention, the other essential types of components and reactants employed in providing flexible polyether polyurethane foams as described herein are polyether polyols, organic polyisocyanates, a catalyst system and blowing agent.
In producing the flexible polyether polyurethane foams of the present invention, one or more polyether polyols is employed for reaction with the polyisocyanate reactant to provide the urethane linkage. Such polyols have an average of at least two, and usually not more than six, hydroxyl groups per molecule and include compounds which consist of carbon, hydrogen and oxygen and compounds which also contain phosphorus, halogen and/or nitrogen.
Such polyether polyols are well known in the art and include, for example, polyethers exemplified by the following classes of composition:
a. Polyoxyalkylene polyols including alkylene oxide adducts of, for example, water; hexylene glycol; glycerol; 1,2,6-hexanetriol; 1,1,1-trimethylolpropane; pentaerythritol; sorbitol; triethanolamine; and the like. The alkylene oxides employed in producing the polyoxyalkylene polyols normally have 2 to 4 carbon atoms. Propylene oxide and mixtures of propylene oxide with ethylene oxide are preferred.
b. Polymer/polyether polyols which are produced by polymerizing one or more ethylenically unsaturated monomers dissolved or dispersed in a polyether polyol in the presence of a free radical catalyst. Suitable polyether polyols for producing such compositions include, for example, any of the above described polyols encompassed by paragraph (a) above. Illustrative of suitable ethylenically unsaturated monomers are those encompassed by the general formula ##STR3## where: R' is hydrogen, methyl or chlorine, and R" is cyano, phenyl or methyl-substituted phenyl groups. Typical examples of such polymerizable monomers are the following which may be employed individually or in combination; acrylonitrile, methacrylonitrile, vinyl chloride, vinylidene chloride, styrene and alpha-methylstyrene. These and other polymer/polyol compositions which are suitably employed either individually or in combination with polyethers mentioned in paragraph (a) above are described in British Pat. No. 1,063,222 and U.S. Pat. No. 3,383,351. Such compositions are prepared by polymerizing the monomers in the polyol at a temperature between about 40.degree. C. and about 150.degree. C. employing any free radical-generating initiator including peroxides, and azo-bis-(isobutyronitrile). The polymer/polyether polyol product may also contain a small amount of unreacted polyether, monomer and free polymer.
In preparing the flexible polyether polyurethane foams in accordance with the present invention it is, of course, to be understood that any of the aforesaid polyether polyols or mixtures thereof can be employed as reactants with the organic polyisocyanate. The particular polyether polyol or polyols employed merely depends upon the desired end-use of the polyurethane foam. Usually diols and triols provide soft foams, firmer foams are obtained by the incoporation of polyether polyols having three or more hydroxyl groups, including triols, tetra-ols, pentols and hexols. When it is desired to produce polyurethanes having comparatively high load-bearing properties and/or die-cutability, polymer/polyether polyols of the aforesaid type are used.
The hydroxyl number of the polyether polyol reactant including mixtures of polyols employed in the production of the flexible polyurethane foams of this invention may vary over a relatively wide range such as from about 20 to about 150, and is usually no higher than about 80. As is well known in this art, the hydroxyl numbers are determined by, and are defined as, the number of milligrams of potassium hydroxide required for the complete neutralization of the hydrolysis product of the fully acetylated derivative prepared from 1 gram of polyol or mixture of polyols. The hydroxyl number is also defined by the following equation which indicates its relationship with the molecular weight and functionality of the polyol: ##EQU1## wherein
OH=hydroxyl number of the polyol, f=average functionality, that is, the average number of hydroxyl groups per molecule of polyol and M.W.=average molecular weight of the polyol.
The organic polyisocyanates that are useful in producing flexible polyether polyurethane foam in accordance with the process of this invention are well known in the art and are organic compounds that contain at least two isocyanato groups and any such compounds or mixtures thereof may be employed. Among such suitable polyisocyanates are those conveniently represented by the general formula:
[D(NCO)].sub.i
wherein i is an integer of two or more and D is an organic radical having the valence of i. D can be a substituted or unsubstituted hydrocarbon group (e.g., alkylene, arylene, aralkylene and the like).
Illustrative of suitable organic polyisocyanate reactants are the following including mixtures thereof: 1,6-diisocyanato-hexane; 1,4-phenylene-diisocyanate; 2,4-tolylene-diisocyanate; 2,6-tolylene-diisocyanate; crude tolylene diisocyanates; xylylene diisocyanates; diphenylmethane-4,4'-diisocyanate; and many other organic polyisocyanates that are known in the art such as those disclosed in an article by Siefken, Ann. 565,75 (1949). In general, the aromatically unsaturated polyisocyanates are preferred.
Also, included as useful in the preparation of the conventional flexible polyether polyurethane foams in accordance with the process of this invention are the polyisocyanates of the aniline-formaldehyde polyaraomatic type which are produced by phosgenation of the polyamine obtained by acid-catalyzed condensation of aniline with formaldehyde. Poly(phenylmethylene) polyisocyanates of this type are available commercially under such trade names as PAPI and, Mondur MR. These products are low viscosity (50-500 centipoise at 25.degree. C.) liquids having average isocyanato functionalities in the range of about 2.25 to about 3.2 or higher, depending upon the specific aniline-to-formaldehyde molar ratio used in the polyamine preparation.
Other useful polyisocyanates are combinations of diisocyanates with polymeric isocyanates containing more than two isocyanato groups per molecule. Illustrative of such combinations are: a mixture of 2,4-tolylene diisocyanate, 2,6-tolylene diisocyanate and the aforesaid poly(phenylmethylene) polyisocyanates; and a mixture of isomeric tolylene diisocyanates with polymeric tolyene diisocyanates obtained as residues from the manufacture of the diisocyanates.
On a combined basis, the polyether polyol and organic polyisocyanate reactants usually constitute the major proportion by weight of the polyurethane-forming reaction mixture. In general, the polyisocyanate and polyether polyol reactants are employed in relative amounts such that the ratio of total-NCO equivalents to total active hydrogen equivalent (of the polyether polyol and any water, when used) is from 0.8 to 1.5, preferably from 0.9 to 1.2, equivalents of --NCO per equivalent of active hydrogen. This ratio is known as the Isocyanate Index and is often also expressed as a percent of the stoichiometric amount of polyisocyanate required to react with total active hydrogen. When expressed as a percent, the Isocyanate Index may be from 80 to 150, and is preferably within the range from about 90 to 120.
The urethane-forming reaction is effected in the presence of a minor amount of a catalyst, preferably an amine catalyst and usually a tertiary amine. Suitable amine catalysts include one or more of the following: N-ethylmorpholine; N,N,N',N'-tetramethyl-1,3-butane-diamine; N,N-dimethylethanolamine; hexadecyldimethylamine; N,N-dimethylbenzylamine; bis(2-dimethylaminoethyl)ether; triethylenediamine (i.e., 1,4-diazabicyclo[2.2.2]octane); the formate and other carboxylic acid salts of triethylenediamine, and bis(2-dimethylaminoethyl)ether; and the like. The amine catalyst may be introduced to the polyurethane producing reaction mixture as such or as a solution in suitable carrier solvents such as dipropylene glycol, preferably the amine catalyst is generally present in the final urethane-producing reaction mixture in an amount of from about 0.05 to about 3 parts by weight of active catalyst (that is, the amine exclusive of other components present in solutions thereof) per 100 parts by weight of the polyether polyol reactant (referred to by using the phrase pphp).
It is also preferred to include a minor amount of certain metal catalysts in addition to the amine catalyst in the reaction mixture for production of the polyurethane foam. Such supplementary catalysts are well known to the art of conventional flexible polyether-based polyurethane foam manufacture. For example, useful metal catalysts include organic derivatives of tin, particularly tin compounds of carboxylic acids such as stannous octoate, dibutyl tin dilaurate, and other such tin salts. In general, the amount of such metal cocatalysts which can be present in the polyurethane producing reaction mixture is within the range from about 0.05 to about 0.5 parts by weight per 100 parts by weight of the polyether polyol reactant (pphp).
Foaming is accomplished by employing a small amount of a polyurethane blowing agent such as water in the reaction mixture (e.g., about 0.5 to about 7 weight percent of water, based on the total weight of the reaction mixture) which upon reaction with isocyanate generates carbon dioxide in situ, or through the use of blowing agents which are vaporized by the exotherm of the reaction, or by a combination of the two methods. These various methods are known in the art. Thus, in addition to or in place of water, other blowing agents which can be employed in the process of this invention include methylene chloride, liquefied gases which have boiling points below 80.degree. F., and above -60.degree. F., or other inert gases such as nitrogen and carbon dioxide. Suitable liquefied gases include aliphatic and cycloaliphatic fluorocarbons which vaporize at or below the temperature of the foaming mass. Such gases are at least partially fluorinated and may also be otherwise halogenated. Fluorocarbon blowing agents suitable for use in foaming the formulations of this invention include trichloromonofluoromethane, dichlorodifluoromethane, 1,1-dichloro-1-fluoroethane, and the like. Another useful class of blowing agents include thermally-unstable compounds which liberate gases upon heating, such as N,N'-dimethyl-N,N'-dinitrosoterephthalamide, and the like. The generally preferred method for producing flexible foams is the use of water or a combination of water plus a fluorocarbon blowing agent such as trichloromonofluoromethane. The amount of blowing agent employed in the foaming reaction will vary with factors such as the density that is desired in the foamed product. Usually, however, from about 1 to about 30 parts by weight of the blowing agent per 100 parts by weight of the polyether polyol reactant is preferred.
The polyether-based polyurethane foams of this invention may be formed in accordance with any of the processing techniques known to the art such as, in particular, the "one-shot" technique. In accordance with this method, foamed products are provided by carrying out the reaction of the polyisocyanate and polyether polyol simultaneously with the foaming operation. It is sometimes convenient to add the polysiloxane-polyoxyalkylene block terpolymer foam stabilizer to the reaction mixture as a premixture with one or more of the blowing agent, polyether polyol, and catalyst components. Typically the amount of polysiloxane-polyoxyalkylene terpolymer is from about 0.1 to about 5.0 parts by weight per 100 parts by weight of the polyether polyol (pphp). Preferably the amount of terpolymer is from about 0.45 to about 3.0 pphp, and most preferably from about 0.75 to about 2.0 pphp.
It is to be understood that the relative amounts of the various components of the foam formulations are not narrowly critical. The polyether polyol and polyisocyanates are present in the foam-producing formulation in a major amount. The relative amount of these two components is the amount required to produce the desired urethane structure of the foam and such relative amounts are well known in the art. The blowing agent, catalyst and polysiloxane-polyoxyalkylene block terpolymer foam stabilizer are each present in a minor amount necessary to achieve the function of the component. Thus the blowing agent is present in an amount sufficient to foam the reaction mixture, the catalyst is present in a catalytic amount (i.e., an amount sufficient to catalyze the reaction to produce the urethane at a reasonable rate), and the polysiloxane-polyoxyalkylene block copolymers of this invention are present in a foam stabilizing amount, that is, in an amount sufficient to stabilize the foam. The preferred amounts of these various components are as given hereinabove.
If desired other additional ingredients can be employed in minor amounts in producing the polyurethane foams in accordance with the process of this invention. Illustrative of such additives that can be employed are: cross-linking agents such as glycerol, triethanolamine and their oxyalkylene adducts, as well as fillers, dyes, pigments, anti-yellowing agents and the like. Flame retardant agents can also be employed if desired. Such flame retardants are well known in the art and include a variety of compounds which preferably contain phosphorus or halogen or both phosphorus and halogen. Illustrative of such flame retardant agents include those disclosed in U.S. application Ser. No. 279,883 filed Aug. 11, 1972, now U.S. Pat. No. 3,846,462 and U.S. Pat. Nos. 3,075,927; 3,075,928; 3,222,305; and 3,574,149.
The polyurethanes produced in accordance with the present invention can be used in the same areas as other conventional flexible polyether polyurethanes. For example, the foams of the present invention can be used with advantage in the manufacture of cushions, mattresses, paddings, carpet underlay, packaging, gaskets, and the like.
Whereas the exact scope of the instant invention is set forth in the appended claims, the following specific examples illustrate certain aspects of the present invention and, more particularly, point out methods of evaluating the same. However, the examples are set forth for illustration only and are not to be construed as limitations on the present invention except as set forth in the appended claims. All parts and percentages are by weight unless otherwise specified.

EXAMPLES
In the following examples the formula MDD'M is used to describe the polyhydridosiloxane polymer reactant. It is to be understood that M=(CH.sub.3).sub.3 SiO.sub.1/2, D=(CH.sub.3).sub.2 SiO.sub.2/2 and D'=CH.sub.3 Si(H)O.sub.2/2. In the following examples, R', R" and R'" are used to indicate starting materials which correspond to the pendant so designated in the claimed structure. The term terpolymer is used herein to denote the final composition comprising polysiloxane, poly(oxyethylene-oxypropylene) and polyoxypropylene.
EXAMPLE 1
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, Friedrich condenser and nitrogen sparge tube were combined 25.77 grams of an allyl started, acetoxy endcapped polyoxyalkylene polymer (R") with an average molecular weight of about 1638 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether A), 49.33 grams of an allyl started, acetoxy endcapped polyoxyalkylene polymer (R') with an average molecular weight of about 4301 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether B), 3.89 grams of an allyl started, acetoxy endcapped polyoxypropylene ether (R'") with an average molecular weight of about 233 (designated herein as Polyether C) and 42.82 grams of toluene. Then, 21.10 grams of a polyhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 ccH.sub.2 /gram) was added to the pot. This mixture was heated to 85.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 25 ppm Pt. After holding the pot contents at 85.degree. C. for one hour, 1 wt.% NaHCO.sub.3 was added followed by a nitrogen sparge assisted solvent strip. After completion of the strip, the pot contents were pressure filtered and the product collected. This product, designated herein as Surfactant 1, was a clear, amber colored liquid.
EXAMPLES 2-5
Following the procedure of Example 1, the following siloxane-polyether terpolymers were prepared.
TABLE I______________________________________ R" Poly- R' Poly- R'" Poly-Surf. Polyhydridosiloxane ether A ether B ether C______________________________________2 MD.sub.76 D'.sub.9 M - 22.25 g 27.87 g 45.57 9 4.34 g3 MD.sub.76 D'.sub.9 M - 23.56 g 30.04 g 41.57 g 4.87 g4 MD.sub.76 D'.sub.9 M - 22.46 g 30.81 g 42.62 g 4.14 g5 MD.sub.76 D'.sub.9 M - 22.16 g 25.12 g 48.18 g 4.58 g______________________________________
These preparations cover a range of 2500 to 2700 for the average molecular weight of Polyethers A and B and a molar ratio range of Polyethers A and B to Polyether C of 1.45-1.75.
EXAMPLES 6-9
Following the procedure of Example 1, the following siloxane-polyether terpolymers were prepared.
TABLE II______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether A ether B ether D______________________________________6 MD.sub.76 D'.sub.9 M - 21.17 g 24.33 g 46.66 g 7.88 g7 MD.sub.76 D'.sub.9 M - 20.85 g 24.58 g 47.14 g 7.47 g8 MD.sub.76 D'.sub.9 M - 19.49 g 18.20 g 55.09 g 7.26 g9 MD.sub.76 D'.sub.9 M - 19.18 g 18.38 g 55.62 g 6.87 g______________________________________
Polyether D is an allyl started, acetoxy endcapped polyoxypropylene ether (R'") with an average molecular weight of about 424.
The above prepared terpolymers covered an average molecular weight range of 2700 to 3000 for Polyethers A and B and a molar ratio of Polyethers A and B to Polyether D of 1.5 to 1.6.
EXAMPLES 10-13
Following the procedure in Example 1, the following siloxane-polyether terpolymers were prepared.
TABLE III______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether A ether E ether F______________________________________10 MD.sub.76 D'.sub.9 M - 19.27 g 25.84 g 45.74 g 9.14 g11 MD.sub.76 D'.sub.9 M - 19.74 g 25.34 g 44.85 g 10.08 g12 MD.sub.76 D'.sub.9 M - 17.23 g 18.60 g 56.00 g 8.17 g13 MD.sub.76 D'.sub.9 M - 17.68 g 18.27 g 55.02 g 9.03 g______________________________________
Polyether E is an allyl started, acetoxy endcapped polyoxyalkylene polymer (R') with an average molecular weight of about 3989 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups.
Polyether F is an allyl started, acetoxy endcapped polyoxypropylene ether (R'") with an average molecular weight of about 590.
The terpolymers described in Table III cover a molecular weight range for polyethers A and E of 2450-2750 and a molar ratio of Polyethers A and E to Polyether F of 1.6-1.8.
EXAMPLES 14-18
Following the procedures outlined in Example 1, the following siloxane-polyether terpolymers were prepared.
TABLE IV______________________________________ R" Poly- R' Poly- R'" Poly-Surf. Polyhydridosiloxane ether A ether E ether F______________________________________14 MD.sub.76 D'.sub.9 M - 20.96 g 29.52 g 38.82 g 10.71 g15 MD.sub.76 D'.sub.9 M - 22.34 g 34.26 g 31.99 g 11.41 g16 MD.sub.76 D'.sub.9 M - 20.31 g 24.71 g 43.74 g 11.24 g17 MD.sub.76 D'.sub.9 M - 18.24 g 17.87 g 53.80 g 10.10 g18 MD.sub.76 D'.sub.9 M - 18.65 g 21.61 g 50.21 g 9.53 9______________________________________
Terpolymers 14 and 15 represent compositions where the molar ratio of Polyethers A and E to Polyether F is held at 1.6 and the average molecular weight of Polyethers A and E are 2300 and 2150, respectively.
Terpolymers 16-18 represent compositions where the molar ratio of Polyethers A and E to Polyether F is held at 1.4 and the average molecular weight of Polyethers A and E are 2450 and 2750, respectively.
EXAMPLES 19-23
The following terpolymers were prepared following the procedures outlined in Example 1.
TABLE V______________________________________ R" Poly- R' Poly- R'" Poly-Surf. Polyhydridosiloxane ether G ether H ether I______________________________________19 MD.sub.76 D'.sub.9 M - 22.3 g 29.2 g 44.4 g a20 MD.sub.76 D'.sub.9 M - 22.4 g 29.3 g 44.6 g b21 MD.sub.76 D'.sub.9 M - 22.3 g 28.4 g 46.3 g c22 MD.sub.76 D'.sub.9 M - 22.4 g 29.2 g 44.4 g d23 MD.sub.76 D'.sub.9 M - 21.0 g 24.4 g 50.8 g e______________________________________
Polyether G is an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1638 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (R").
Polyether H is an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 3989 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (R').
Terpolymers 19-21 represent compositions where the molar ratio of Polyethers G and H to Polyether I(a-c) is held at 1.75, the blend average molecular weight of Polyethers G and H are held at 2500. Both Polyether G and H have 40% by weight oxyethylene units. Polyethers I(a-c) represent R'" and are based upon the same allyl started polypropylene oxide polymer with a molecular weight of 191 and differ only in the degree of acetoxy capping where Ia is 98.3% capped, Ib is 54% capped and Ic is completely hydroxyl terminated.
Terpolymer 22 represents a composition of blend average molecular weight of Polyethers G and H of 2500, and molar ratio of Polyethers G and H to Polyether Id of 1.75 where Polyether Id is based upon an allyl started polyether with a molecular weight of 191 which has been acetoxy endcapped to an efficiency of 77.2%.
Terpolymer 23 represents a composition with blend average molecular weight of Polyethers G and H of 2700, and a molar ratio of Polyethers G and H to Polyether Ie of 1.75 where Polyether Ie is the same as Polyether Id, described above.
Amounts used in the preparations of terpolymers 19-23 were a=4.5 grams, b=3.7 grams, c=3.0 grams, d=4.1 grams and e=3.8 grams.
EXAMPLES 24-30
The following silicone polyether terpolymers were prepared according to the procedure outlined in Example 1.
TABLE VI______________________________________ R" Poly- R' Poly- R'" Poly-Surf. Polyhydridosiloxane ether G ether H ether D______________________________________24 MD.sub.76 D'.sub.9 M - 19.82 g 26.57 g 47.03 g 6.59 g25 MD.sub.76 D'.sub.9 M - 20.35 g 26.13 g 46.24 g 7.29 g26 MD.sub.76 D'.sub.9 M - 21.02 g 25.57 g 45.26 g 8.15 g27 MD.sub.76 D'.sub.9 M - 17.66 g 19.07 g 57.41 g 5.87 g28 MD.sub.76 D'.sub.9 M - 18.81 g 18.42 g 55.48 g 7.30 g29 MD.sub.76 D'.sub.9 M - 18.17 g 18.78 g 56.55 g 6.51 g30 MD.sub.76 D'.sub.9 M - 23.13 g 35.47 g 33.13 g 8.28 g______________________________________
The terpolymers described above (24-30) have been prepared in 30 weight percent toluene. The terpolymers of this example cover a blend average molecular weight range for Polyethers G and H of 2150-2750 and a molar ratio of polyethers G and H to Polyether I of 1.4-1.8.
EXAMPLES 31-35
The following terpolymers were prepared according to the method described in Example 1.
TABLE VII______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether J ether K ether D______________________________________31 MD.sub.76 D'.sub.9 M - 21.7 g 25.2 g 45.1 g 8.1 g32 MD.sub.76 D'.sub.9 M - 22.5 g 24.6 g 43.9 g 9.1 g33 MD.sub.76 D'.sub.9 M - 20.7 g 18.7 g 52.3 g 8.4 g34 MD.sub.76 D'.sub.9 M - 19.9 g 19.1 g 53.6 g 7.4 g35 MD.sub.76 D'.sub.9 M - 21.1 g 21.8 g 48.9 g 8.2 9______________________________________
Polyether J is an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1578 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (R").
Polyether K is an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4300 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (R').
Terpolymers 31-35 represent compositions where the blend average molecular weight of Polyethers J and K together are 2600-2900 and the molar ratio of Polyethers J and K to Polyether I is 1.3-1.4.
EXAMPLE 36
The following terpolymer was prepared according to the following procedure.
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, Friedrich condenser and nitrogen sparge tube were combined 24.6 grams of R", an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1578 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether L), 43.9 grams of R', an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4300 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether M), 9.1 grams of R'", an allyl started, acetoxy endcapped polyoxypropylene ether with an average molecular weight of about 424 (designated herein as Polyether I) and 42.8 grams of isopropanol. Then, 22.5 grams of a polyhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 ccH.sub.2 /gram) was added to the pot. This mixture was heated to 75.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 25 ppm Pt. After an induction period of 7 seconds, an exotherm of 9.degree. C. was generated and a clear time of 71 seconds was noted. After holding the pot contents at 75.degree. C. for one hour, 1 wt.% NaHCO.sub.3 was added followed by a nitrogen sparge assisted solvent strip. After completion of the strip, the pot contents were pressure filtered and the product collected. This product, designated herein as Surfactant 36, was a clear, amber colored liquid.
EXAMPLES 37-38
The next two terpolymers were prepared following the procedures outlined in Example 36.
TABLE VIII______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether L ether M ether D______________________________________37 MD.sub.76 D'.sub.9 M - 19.9 g 19.1 g 53.6 g 7.4 g38 MD.sub.76 D'.sub.9 M - 21.1 g 21.8 g 48.9 g 8.2 g______________________________________
Terpolymers 36 through 38 represent compositions where the blend average molecular weight of Polyethers L and M range from 2600-2900 and the molar ratio of Polyethers L and M to Polyether I ranges from 1.3 to 1.5. Polyethers L and M are described in Example 35.
EXAMPLE 39
The next terpolymer was made according to the following procedure.
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, Friedrich condenser and nitrogen sparge tube were combined 24.5 grams of R", an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1560 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether N), 50.0 grams of R', an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4300 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether M), 4.3 grams of R'", an allyl started, acetoxy endcapped polyoxypropylene ether with an average molecular weight of about 233 (designated herein as Polyether O) and 24.9 grams of isopropanol. These polyether charges represent a blend average molecular weight of 2650 of Polyethers N and M and a molar ratio of Polyethers N and M to Polyether O of 1.75. Then, 21.3 grams of a polyhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 cchH.sub.2 /gram) was added to the pot. This mixture was heated to 65.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 25 ppm Pt. After an induction period of 59 seconds, an exotherm of 10.degree. C. was generated and a clear time of 559 seconds was noted. After holding the pot contents at 65.degree. C. for one hour, 1 wt. % NaHCO.sub.3 was added followed by a a nitrogen sparge assisted solvent strip. After completion of the strip, the pot contents were pressure filtered and the product collected. This product, designated herein as Surfactant 39, was a clear, amber colored liquid.
EXAMPLES 40-42
The following three terpolymers were preprared according to the procedure of Example 36.
TABLE IX______________________________________ R" Poly- R' Poly- R' " Poly-,Surf. Polyhydridosiloxane ether N ether M ether O______________________________________40 MD.sub.76 D'.sub.9 M - 23.2 g 33.4 g 39.3 g 4.1 g41 MD.sub.76 D'.sub.9 M - 22.4 g 29.2 g 44.4 g 4.1 g42 MD.sub.76 D'.sub.9 M - 21.6 g 25.4 g 48.9 g 4.1 g______________________________________
Polyethers M, N and O are described in Example 38.
Terpolymers 40-42 represent compositions where the blend average molecular weight of Polyethers N and M range from 2350-2650 and the molar ratio of Polyethers N and M to Polyether O ranges from 1.65-1.85.
EXAMPLE 43
The following terpolymer was prepared according to the procedures outlined below.
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, Friedrich condenser and nitrogen sparge tube were combined 24.5 grams of R", an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1560 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether N), 50.0 grams of R', an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4300 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (desginated herein as Polyether M), 4.3 grams of R'", an allyl started, acetoxy endcapped polyoxypropylene ether with an average molecular weight of about 233 (designated herein as Polyether O) and 17.6 grams of dipropylene glycol. These polyether charges represent a blend average molecular weight of 2650 of Polyethers N and M and a molar ratio of Polyethers N and M and a molar ratio of Polyethers N and M to Polyether O of 1.75. Then, 21.3 grams of a polyhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 ccH.sub.2 /gram was added to the pot. This mixture was heated to 65.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 25 ppm Pt. After an induction period of 42 seconds, an exotherm of 8.degree. C. was generated and a clear time of 370 seconds was noted. After holding the pot contents at 65.degree. C. for one hour, 1 wt. % NaHCO.sub.3 was added followed by a filtration at 40 psi to remove solids. This product, designated herein as Surfactant 43, was a clear, amber colored liquid.
EXAMPLES 44-47
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE X______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether N ether M ether O______________________________________44 MD.sub.76 D'.sub.9 M - 22.4 g 28.0 g 45.2 g 4.5 g45 MD.sub.76 D'.sub.9 M - 21.8 g 24.2 g 49.4 g 4.6 g46 MD.sub.76 D'.sub.9 M - 20.9 g 24.7 g 50.5 g 4.0 g47 MD.sub.76 D'.sub.9 M - 20.4 g 21.3 g 54.3 g 4.1 g______________________________________
The terpolymers 43-47 represent compositions where the blend average molecular weight of Polyethers N and M ranges from 2500-2800 and the molar ratio of Polyethers N and M to Polyether O ranges from 1.6-1.9.
EXAMPLE 48
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, FriedZrich condenser and nitrogen sparge tube were combined 33.3 grams of R", an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 1578 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether L), 39.2 grams of R', an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4300 and containing about 40 weight percent oxethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyether M), 4.5 grams of R'", an allyl started, acetoxy encapped polyoxypropylene ether with an average molecular weight of about 233 (designated herein as Polyether C) and 42.8 grams of dipropylene glycol. These polyether charges represent a blend average molecular weight of 2350 of Polyethers N and M and a molar ratio of Polyethers N and M to Polyether O of 1.85. Then, 23.1 grams of a polyhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 ccH.sub.2 /gram was added to the pot. This mixture was heated to 65.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 25 ppm Pt. After an induction period of 31 seconds, an exotherm of 7.degree. C. was generated and a clear time of 271 seconds was noted. After holding the pot contents at 65.degree. C. for one hour, 1 wt. % NaHCO.sub.3 was added followed by a filtration at 40 psi to remove solids. This product, designated herein as Surfactant 48, was a clear, amber colored liquid.
EXAMPLES 49-54
The following terpolymers were prepared according to the procedure outlined in Example 48.
TABLE XI______________________________________ R" R' R'" Polyether Polyether PolyetherSurf. Polyhydridosiloxane N M O______________________________________49 MD.sub.76 D'gM - 23.7 g 32.8 g 38.6 g 4.9 g50 MD.sub.76 D'gM - 22.3 g 29.1 g 44.3 g 4.5 g51 MD.sub.76 D'gM - 22.9 g 28.6 g 43.5 g 5.0 g52 MD.sub.76 D'gM - 21.0 g 25.6 g 49.4 g 4.0 g53 MD.sub.76 D'gM - 23.1 g 33.3 g 39.2 g 4.5 g54 MD.sub.76 D'gM - 21.6 g 25.3 g 48.8 g 4.5 g______________________________________
Terpolymers 49-54 represent compositions where the blend average molecular weight of Polyethers N and M ranges from 2350-2650 and the molar ratio of Polyethers N and M to Polyether O ranges from 1.55-1.85.
EXAMPLES 55-64
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XII______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether N ether M ether D______________________________________55 MD.sub.76 D'.sub.9 M - 21.2 g 21.0 g 49.7 g 8.2 g56 MD.sub.76 D'.sub.9 M - 19.4 g 18.7 g 55.3 g 6.7 g57 MD.sub.76 D'.sub.9 M - 19.1 g 16.8 g 57.3 g 6.9 g58 MD.sub.76 D'.sub.9 M - 18.9 g 16.9 g 57.8 g 6.5 g59 MD.sub.76 D'.sub.9 M - 18.6 g 17.0 g 58.2 g 6.2 g60 MD.sub.76 D'.sub.9 M - 18.4 g 15.2 g 60.1 g 6.4 g61 MD.sub.76 D'.sub.9 M - 20.5 g 21.4 g 50.7 g 7.4 g62 MD.sub.76 D'.sub.9 M - 19.1 g 18.9 g 55.7 g 6.4 g63 MD.sub.76 D'.sub.9 M - 18.1 g 15.3 g 60.6 g 6.0 g64 MD.sub.76 D'.sub.9 M - 5.5 g 0.0 g 32.6 g 1.9 g______________________________________
Terpolymers 55-64 represent compositions where the blend average molecular weight of the Polyethers N and M range from 2750-4300 and the molar ratio of Polyethers N and M to Polyether O ranges from 1.4-1.8.
EXAMPLES 65-69
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XIII______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether N ether M ether O______________________________________65 MD.sub.76 D'.sub.9 M - 22.4 g 28.0 g 45.2 g 4.5 g66 MD.sub.76 D'.sub.9 M - 21.8 g 24.2 g 49.4 g 4.6 g67 MD.sub.76 D'.sub.9 M - 21.3 g 24.5 g 50.0 g 4.3 g68 MD.sub.76 D'.sub.9 M - 20.9 g 24.7 g 50.5 g 4.0 g69 MD.sub.76 D'.sub.9 M - 20.4 g 21.3 g 54.3 g 4.1 g______________________________________
Terpolymers 65-69 represent compositions where the blend average molecular weight of Polyethers N and M range from 2500-2800 and the molar ratio of Polyethers N and M to Polyether O ranges from 1.6 to 1.9.
EXAMPLES 70-79
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XIV______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether P ether Q ether F______________________________________70 MD.sub.76 D'.sub.9 M - 19.8 g 20.2 g 49.1 g 11.0 g71 MD.sub.76 D'.sub.9 M - 19.7 g 17.0 g 51.4 g 11.9 g72 MD.sub.76 D'.sub.9 M - 21.9 g 15.4 g 46.5 g 16.2 g73 MD.sub.76 D'.sub.9 M - 19.6 g 13.3 g 54.1 g 13.0 g74 MD.sub.76 D'.sub.9 M - 19.3 g 12.6 g 55.2 g 12.8 g75 MD.sub.76 D'.sub.9 M - 17.3 g 9.7 g 62.6 g 10.4 g76 MD.sub.76 D'.sub.9 M - 19.4 g 8.9 g 57.4 g 14.3 g77 MD.sub.76 D'.sub.9 M - 18.4 g 13.0 g 57.6 g 11.1 g78 MD.sub.76 D'.sub.9 M - 18.2 g 9.5 g 60.1 g 12.1 g79 MD.sub.76 D'.sub.9 M - 18.1 g 5.4 g 63.2 g 13.4 g______________________________________
The terpolymers described above in Table XIV represent compositions that cover a range of 2750-3763 for the blend average molecular weight of Polyethers P and Q and a molar ratio range of Polyethers P and Q to Polyether F of from 0.8-1.4.
Polyether P is the same polyether as Polyether N above. Polyether Q is an allyl started, acetoxy endcapped polyoxyalkylene polymer with an average molecular weight of about 4400 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene units (R').
EXAMPLES 80-84
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XV______________________________________ Poly- Poly- Poly-Surf. Polyhydridosiloxane ether P ether Q ether C______________________________________80 MD.sub.229 D'.sub.27 M - 21.2 g 27.5 g 47.1 g 4.3 g81 MD.sub.229 D'.sub.27 M - 16.9 g 13.6 g 66.1 g 3.4 g82 MD.sub.152 D'.sub.18 M - 18.8 g 19.7 g 57.6 g 3.8 g83 MD.sub.37 D'.sub.4.5 M - 20.4 g 24.3 g 51.1 g 4.1 g84 MD.sub.17.5 D'.sub.2.25 M - 20.4 g 24.3 g 51.1 g 4.1 g______________________________________
Terpolymers 80-84 represent compositions where the calculated average molecular weight ranges from 5580-71730. The blend average molecular weight of Polyethers P and Q range from 2350-2950 with a molar ratio of Polyethers P and Q to Polyether C of 1.75 for terpolymers 80-82. The blend average molecular weight of Polyethers P and Q is 2650 and the molar ratio of Polyethers P and Q to Polyether C is 1.75 for terpolymers 83 and 84.
EXAMPLES 85-87
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XVI______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether P ether Q ether R______________________________________85 MD.sub.76 D'.sub.9 M - 18.7 g 13.0 g 50.4 g 17.9 g86 MD.sub.76 D'.sub.9 M - 19.7 g 12.2 g 47.2 g 21.0 g87 MD.sub.76 D'.sub.9 M - 17.6 g 8.1 g 54.3 g 19.4 g______________________________________
Terpolymers 85-87 represent compositions having a blend average molecular weight of Polyethers P and Q of from 3076-3445 and a molar ratio of Polyethers P and Q to Polyether R of 0.8-1.0. Polyether R is an allyl started, acetoxy endcapped polyoxypropylene polymer with an average molecular weight of approximately 924 (R'").
EXAMPLES 88-93
The following terpolymers were prepared according to the procedure outlined in Example 43.
TABLE XVII______________________________________ R" Poly- R' Poly- R' " Poly-Surf. Polyhydridosiloxane ether P ether Q ether D______________________________________88 MD.sub.76 D'.sub.9 M - 20.5 g 20.8 g 50.9 g 8.0 g89 MD.sub.76 D'.sub.9 M - 19.3 g 18.3 g 55.2 g 7.2 g90 MD.sub.76 D'.sub.9 M - 19.3 g 17.2 g 56.0 g 7.5 g91 MD.sub.76 D'.sub.9 M - 20.0 g 17.9 g 54.0 g 8.1 g92 MD.sub.76 D'.sub.9 M - 18.3 g 14.0 g 60.6 g 7.1 g93 MD.sub.76 D'.sub.9 M - 19.2 g 15.5 g 57.6 g 7.8 g______________________________________
EXAMPLE 94
In a 250 mL three necked flask fitted with a heating mantle, mechanical stirrer, thermometer, Dean-Stark trap, Friedrich condenser and nitrogen sparge tube were combined 24.3 grams of an allyl started, acetoxy endcapped polyoxyalkylene polymer (R") with an average molecular weight of about 1560 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxypropylene groups (designated herein as Polyeter N) 51.0 grams of an allyl started, acetoxy endcapped polyoxyalkylene polymer (R') with an average molecular weight of about 4400 and containing about 40 weight percent oxyethylene groups and about 60 weight percent oxyypropylene groups (designated herein as Polyether Q) and 4.1 grams of an allyl started, acetoxy endcapped polyoxypropylene ether (R'") with an average molecular weight of about 233 (designated herein as Polymer C). No solvent was added. The, 20.6 grams of a polhydridosiloxane polymer having the average formula
MD.sub.76 D'.sub.9 M
(Calculated: 31.82 ccH.sub.2 /gram; Analyzed: 31.4 cch.sub.2 /gram) was added to the pot. This mixture was heated to 85.degree. C. and 0.36 mL of an H.sub.2 PtCl.sub.6 /ethanol solution (10 mg Pt/mL) was added, corresponding to 22 ppm Pt. After holding the pot contents at 85.degree. C. for one hour, 1 wt. % NaHCO.sub.3 was added followed by a nitrogen sparge assisted solvent strip. After completion of the strip, the pot contents were pressure filtered and the product collected. This product, designated herein as Surfactatn 94, was a clear, amber colored liquid.
EXAMPLE 95
The surfactants described above in Examples 1-94 (excluding 19-23) were evaluated in the polyurethane foam formulation shown below.
______________________________________FORMULATIONMaterial pphp* (wt.)______________________________________Polyol I 100.0Distilled Water 5.5Bis-(2-dimethylamino)ether 0.02Triethylene Diamine 0.02Dimethylaminoethoxyethanol (DMEE) 0.06Dipropylene Glycol 0.10Methylene Chloride 10.0Stannous Octoate 0.23TDI 80/20 (112 Index) 69.44Polysiloxane-polyoxyalkylene Terpolymer VARIEDTest I 1.50Test II 1.25Test III 1.00Test IV 0.85Test V 0.75Test VI 0.50Test VII 0.45______________________________________ *parts per hundred parts polyol.
Polyol I is a polyol produced from glycerol and a mixture 84 weight percent propylene oxide and 16 weight percent ethylene oxide. Polyol I has a hydroxyl number of 56.
TDI 80/20 (112 Index) is a mixture of 80 weight percent 2.4 tolylene diisocyanate and 20 weight percent 2,6-tolylene diisocyanate.
The results of the said foam evaluations of the above surfactants are reported in Table XVIII below. These results demonstrate the superior performance of the novel polysiloxane-polyoxyalkylene compositions of this invention over a range of concentrations.
TABLE XVIII______________________________________Product of Height inExample Foam Test Rise (in) Airflow Rate______________________________________1 II 37.0 4.51 III 36.3 5.21 V 36.3 5.51 VI 33.6 6.02 II 37.2 5.32 III 35.9 5.52 V 34.9 5.72 VI 32.7 5.53 II 36.0 6.23 III 35.0 6.53 V 33.3 6.93 VI 33.3 7.04 II 36.7 5.54 III 36.5 6.04 V 35.4 7.04 VI 34.5 7.35 II 36.7 5.85 III 35.6 5.65 V 35.7 6.05 VI 31.2 5.96 II 35.8 7.56 III 35.7 7.86 V 33.9 7.46 VI 30.6 7.07 II 34.0 5.77 III 33.1 5.57 V 32.9 5.47 VI 26.5 voids8 II 36.1 5.88 III 35.9 5.98 V 34.6 5.68 VI 33.9 5.59 II 36.0 5.59 III 35.1 5.59 V 34.2 4.59 VI 30.5 4.610 II 34.2 5.510 III 34.1 6.010 V 31.9 5.410 VI 29.8 voids11 II 32.5 5.111 III 31.6 5.211 V 27.7 voids11 VI COLLAPSE12 II 35.4 4.512 III 35.3 4.512 V 32.9 4.012 VI 30.6 voids13 II 35.3 5.013 III 34.8 4.813 V 33.3 4.813 VI 29.7 voids14 II 31.5 5.214 III 29.8 5.014 V 27.7 voids14 VI COLLAPSE15 II 32.0 5.515 III 30.0 6.815 V 29.5 7.415 VI 25.2 voids16 II 33.3 6.816 III 33.5 7.516 V 31.1 4.016 VI 28.4 voids17 II 34.0 5.617 III 33.5 5.817 V 32.5 5.917 VI 30.9 5.418 II 35.3 6.018 III 35.2 5.718 V 33.4 6.018 VI 30.6 3.624 II 36.6 6.424 III 36.3 6.824 V 35.0 6.924 VI 32.3 6.525 II 34.3 5.525 III 32.3 5.425 V 30.1 7.325 VI 22.9 voids26 II 34.5 7.026 III 34.2 7.226 V 31.7 7.326 VI 29.6 7.327 II 36.9 5.027 III 35.7 5.627 V 33.8 5.527 VI 31.1 5.028 II 36.5 7.028 III 35.3 7.228 V 34.8 7.528 VI 33.9 7.529 II 36.8 5.029 III 37.0 5.529 V 35.5 6.129 VI 33.4 6.530 II 32.7 6.030 III 31.2 7.030 V 29.4 7.030 VI 26.2 voids31 II 36.5 6.931 III 36.2 7.031 VI 33.0 7.032 II 35.7 7.632 III 36.0 8.232 VI 34.0 8.433 II 36.7 7.233 III 36.7 7.433 VI 33.2 7.134 II 37.0 5.834 III 37.7 6.534 VI 33.9 6.535 II 36.9 7.035 III 36.9 7.435 VI 32.0 6.536 II 36.5 8.036 III 36.0 8.436 VI 35.4 8.537 II 37.4 5.637 III 37.3 6.537 VI 33.9 6.738 II 37.0 6.538 III 37.0 7.338 VI 34.5 8.039 II 37.5 5.539 IV 36.8 6.539 VII 33.9 7.040 II 37.1 5.440 V 36.4 7.540 VI 35.1 9.041 II 37.4 5.041 V 37.1 7.041 VI 35.5 8.942 II 38.2 5.142 V 36.4 7.042 VI 35.2 8.543 II 37.8 4.043 IV 37.2 5.043 VII 34.9 6.544 II 37.3 4.544 IV 37.3 6.244 VII 34.6 7.645 II 37.9 3.945 IV 37.7 5.545 VII 35.2 7.146 II 37.4 5.046 IV 37.4 5.546 VII 34.4 6.047 II 37.9 4.347 IV 37.5 5.047 VII 34.9 5.648 II 36.2 4.648 IV 35.9 5.548 VII 32.6 6.949 II 35.2 8.049 IV 35.0 8.149 VII 32.9 8.550 II 35.6 5.350 IV 36.0 6.050 VII 33.1 7.551 II 36.2 5.051 IV 34.6 5.551 VII 33.8 6.252 II 37.4 5.352 IV 37.1 5.952 VII 34.4 5.853 II 36.3 6.953 IV 35.2 6.053 VII 33.6 5.854 II 37.3 5.554 IV 36.8 5.854 VII 35.0 6.655 II 37.1 7.055 IV 36.5 7.555 VII 35.1 8.856 II 38.2 4.856 IV 37.4 5.056 VII 34.9 6.557 11 38.2 4.557 IV 37.4 6.057 VII 35.9 6.658 II 38.6 3.458 IV 38.1 3.558 VII 36.8 3.559 II 38.8 4.059 IV 37.6 4.059 VII 35.9 5.060 II 38.7 3.860 IV 37.6 3.860 VII 35.0 3.761 II 37.7 5.061 IV 36.7 5.961 VII 35.0 7.662 II 38.8 3.862 IV 37.7 4.562 VII 35.7 5.563 II 37.9 3.063 IV 37.9 3.863 VII 35.6 4.064 II 37.2 3.464 IV 36.8 3.564 VII 33.9 2.265 II 37.3 4.565 IV 37.3 6.265 VII 34.6 7.666 II 37.9 3.966 IV 37.7 5.566 VII 35.2 7.167 II 37.8 4.067 IV 37.2 5.067 VII 34.9 6.568 II 37.4 5.068 IV 37.4 5.568 VII 34.4 6.069 II 37.9 4.369 IV 37.5 5.069 VII 34.9 5.670 I 36.5 5.570 III 36.7 6.870 VI 34.6 9.071 I 36.7 5.471 III 36.1 6.571 VI 34.9 8.572 I 20.9 3.972 III 29.1 7.072 VI 28.3 8.173 I 36.2 7.073 III 36.6 8.373 VI 33.9 8.574 I 36.7 6.374 III 36.5 7.874 VI 34.5 8.575 I 38.7 3.075 III 37.4 4.075 VI 36.3 6.676 I 36.5 7.876 III 35.8 9.076 VI 33.9 9.077 I 37.2 3.777 III 37.2 5.577 VI 36.0 7.678 I 37.5 4.078 III 37.4 5.878 VI 35.7 7.579 I 37.4 5.979 III 37.4 7.079 VI 34.5 8.080 II 36.2 5.580 IV 36.4 5.480 VII 35.6 5.881 II 36 5 1.581 IV 36.0 2.081 VII 35 6 1.882 II 38.1 2.382 IV 38.0 3.582 VII 35.3 2.883 I 38.0 5.283 III 36.4 5.583 VI 35.1 7.584 I 27.9 7.884 III 29.0 8.084 VI 27.4 voids85 I 37.4 3.185 III 37.2 5.285 VI 35.6 8.586 I 35.7 4.686 III 35.4 7.586 VI 33.5 9.187 I 36.9 4.287 III 35.7 7.587 VI 36.0 8.188 I 36.2 6.888 III 34.9 7.588 VI 34.5 8.589 I 37.4 5.589 III 36.2 5.789 VI 36.4 7.590 I 36.6 6.590 III 36.4 7.590 VI 34.8 8.491 I 36.6 5.591 III 35.9 6.491 VI 35.5 7.992 I 37.3 5.492 III 36.8 4.092 VI 35.4 6.693 I 36.8 3.593 III 36.3 4.193 VI 36.5 4.894 I 38.4 3.594 III 37.9 5.094 VI 35.6 7.2______________________________________
EXAMPLE 96
The terpolymers described in Examples 19-23 were evaluated in the polyurethane foam formulation shown below.
______________________________________FORMULATIONMaterial pphp (wt.)______________________________________Polyol 100.0Distilled Water 5.7Bis-(2-dimethylamino)ether 0.01Triethylene Diamine 0.01Dimethylaminoethoxyethanol (DMEE) 0.03Dipropylene Glycol 0.05Methylene Chloride 9.0Stannous Octoate 0.2TDI 80/20 (110 Index) 70.6Polysiloxane-polyoxyalkylene Terpolymer VARIEDTest I 1.50Test II 1.00Test III 0.70Test IV 0.60Test V 0.42______________________________________
The results of the said foam evaluations of the above surfactants are reported in Table XIX below. These results demonstrate the superiority of the novel polysiloxane-polyoxyalkylene compositions of this invention as compared to a polysiloxane-polyoxyalkylene copolymer surfactant (CNTRL A).
TABLE XIX______________________________________Product of Height inExample Foam Test Rise (in) Airflow Rate______________________________________CNTRL A I 14.7 5.00CNTRL A II 14.0 6.00CNTRL A V 12.0 5.5019 V 13.3 7.2520 V 14.5 4.5021 V 14.6 1.2522 II 14.7 4.0022 III 14.5 4.7522 VI 13.7 5.5023 II 14.8 4.0023 III 14.7 4.7523 VI 14.0 4.25[19 + 20] (50/50) II 14.8 5.50[19 + 20] (50/50) (III 14.7 6.00[19 + 20] (50/50) VI 13.4 5.50______________________________________
CNTRL A is commercially available as B-8021 from Th. Goldschmidt A.G. It is a hydrolyzable type surfactant that is not applicable in Flame Retardant formulations.
The following table documents for R' and R", the calculated molecular weight of R'" (R'"-MW) molar ratios of R' and R' to R'"; (b+c:d), calculated blend average molecular weight (BAMW) and the calculated total blend average molecular weight (TOTAL BAMW) for all of the polyethers for the terpolymers described above (Examples 1-94).
TABLE XX______________________________________ R' & R"SurfactantMW BAMW R'" (b + c):d TOTAL BAMW______________________________________ 1 2700 233 1.75 1803 2 2600 233 1.60 1690 3 2500 233 1.45 1575 4 2500 233 1.75 1676 5 2700 233 1.45 1693 6 2700 424 1.50 1790 7 2700 424 1.60 1825 8 3000 424 1.50 1970 9 3000 424 1.60 200910 2450 590 1.80 178511 2450 590 1.60 173512 2750 590 1.80 198013 2750 590 1.60 192014 2300 590 1.60 164015 2150 590 1.60 155016 2450 590 1.40 167517 2750 590 1.40 185018 2600 590 1.60 183019 2500 233 1.75 167620 2500 233 1.75 167621 2500 233 1.75 167622 2500 233 1.75 167623 2700 233 1.75 180324 2450 424 1.80 172625 2450 424 1.60 167126 2450 424 1.40 160627 2750 424 1.80 191928 2750 424 1.40 178129 2750 424 1.60 185530 2150 424 1.60 148631 2600 424 1.50 173032 2600 424 1.30 165433 2900 424 1.30 182334 2900 424 1.50 191035 2750 424 1.40 178136 2750 424 1.30 173937 2900 424 1.50 191038 2600 424 1.40 169339 2650 233 1.75 177140 2350 233 1.85 160741 2500 233 1.75 167642 2650 233 1.65 174043 2650 233 1.75 177144 2500 233 1.75 166545 2650 233 1.60 172046 2650 233 1.90 181547 2800 233 1.75 186548 2350 233 1.85 160749 2350 233 1.65 155150 2500 233 1.75 167651 2500 233 1.55 161152 2650 233 1.85 180253 2350 233 1.85 160754 2650 233 1.65 174055 2750 424 1.40 178156 2900 424 1.70 198357 3000 424 1.60 200958 3000 424 1.70 204659 3000 424 1.80 208060 3100 421 1.70 210961 2750 424 1.60 185562 2900 424 1.80 201663 3130 424 1.80 214464 4300 424 1.75 289165 2500 233 1.75 167566 2650 233 1.60 172067 2650 233 1.75 177068 2650 233 1.90 181569 2800 233 1.75 186570 2750 590 1.40 185071 2900 590 1.20 185072 2900 590 0.80 161573 3050 590 1.00 185074 3163 590 1.00 188075 3425 590 1.20 213576 3425 590 0.80 185077 3175 590 1.20 200078 3410 590 1.00 200079 3763 590 0.80 200080 2350 233 1.75 158081 2950 233 1.75 196282 2650 233 1.75 177183 2650 233 1.75 177184 2650 233 1.75 177185 3076 924 1.00 202686 3076 924 0.80 190387 3445 924 0.80 207188 2750 424 1.40 178089 2900 424 1.50 191090 2950 424 1.40 189891 2900 424 1.30 182392 3150 424 1.40 201493 3050 424 1.30 190894 2650 233 1.75 1771______________________________________
EXAMPLE 97
The terpolymers described in Examples 67, 79 and 90 were evaluated in the Flame Retardant polyurethane foam formulations shown below.
______________________________________FORMULATION 96 A 96 B 96 C 96 DMaterial pphp pphp pphp pphp*______________________________________Polyol I 100.0 100.0 100.0 100.0Distilled Water 4.8 4.8 4.8 4.8Bis-(2-dimethylamino)ether 0.01 0.01 0.01 0.01Triethylene Diamine 0.01 0.01 0.01 0.01Dimethylaminoethoxyethanol (DMEE) 0.03 0.03 0.03 0.03Dipropylene Glycol 0.05 0.05 0.05 0.05Methylene Chloride 5.0 5.0 5.0 5.0Thermolin-101** 8.0 8.0 10.0 10.0Stannous Octoate 0.23 0.23 0.23 0.23TDI 80/20 (110 Index) 60.9 60.9 60.9 60.9Surfactant 0.8 1.2 0.8 1.2______________________________________ *parts per hundred parts polyol **Thermolin101 is a flame retardant additive available from Olin Chemical Company.
The results of the said foam evaluations of the above surfactants are reported below. These foams were evaluated in California Burn Test 117.
TABLE XXI______________________________________ Char AfterProduct of Foam Height of Airflow Length FlameExample Test Rise (in) (scfm) (in) (seconds)______________________________________67 96 A 13.9 4.0 4.14 1.067 96 B 14.0 3.0 4.38 0.467 96 C 13.8 4.5 4.42 0.467 96 D 14.0 3.3 4.70 1.479 96 A 14.0 7.0 4.50 0.879 96 B 14.3 6.3 4.44 0.879 96 C 13.3 6.0 4.92 0.679 96 D 13.7 5.5 3.18 0.090 96 A 13.8 7.5 5.54 0.690 96 B 13.9 6.3 4.70 0.490 96 C 13.3 7.0 3.42 0.090 96 D 13.8 6.5 5.22 1.0______________________________________
All of the above surfactants passed the burn test. These tests are for evaluation purposes and are conducted under controlled conditions. The results are not intended as a warranty of how foams will burn under actual fire conditions.

Number	Name	Date
3272762	Ibbotson et al.	Sep 1966
3398104	Haluska	Aug 1968
3505377	Morehouse	Apr 1970
3532732	Rossmy	Oct 1970
3629308	Bailey et al.	Dec 1971
3686254	Morehouse	Aug 1972
3703489	Morehouse	Nov 1972
3887601	Kanner et al.	Jun 1975
3980688	Litteral et al.	Sep 1976
4025456	Litteral	May 1977
4031044	Wallace	Jun 1977
4071483	Litteral et al.	Jan 1978
4309508	Baskent et al.	Jan 1982
4478957	Klietsch et al.	Oct 1984

Number	Date	Country
1066142	Apr 1967	DEX
3508292	Jun 1986	DEX

Polysiloxane-polyoxyalkylene terpolymers for polyurethane foam manufacture

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Continuation in Parts (1)