This invention relates to a liquid urethane containing adduct; a process for the preparation thereof; and applications therewith. More specifically this invention relates to a stable adduct which is a liquid at room temperature and which contains a plurality of urethane linkages, and yet which is substantially free of any isocyanate functionality or isocyanate- reactive functionality.

In general, urethane containing adducts may be prepared by reaction of organic isocyanates with active hydrogen-containing substances. The reaction may be conducted in the presence of a solvent and various addition sequences of isocyanate with active hydrogen- containing substances employed so as to arrive at an end product which is substantially free of any isocyanate functionality or isocyanate-reactive functionality. Illustrative of such products and various reaction techniques known to the art is that as disclosed by U.S. Patent 4,079,028.

For many applications including the field of surfactancy, for example when manufacturing polyurethane foams, lubricants or quenchants, it is desirable that the adduct have an attractive purity and be a liquid. For polyurethane applications, the presence of a lower molecular weight adduct can be detrimental, to the extent of being an antifoaming agent, when trying to exploit the surfactancy property of a higher molecular weight product. The liquid characteristic of the adduct is highly desirable as it enhances its versatility with respect to applications where stable systems with other substances in the liquid phase is required.

Our present investigations are directed to the development of a liquid urethane- containing adduct having an improved purity, and especially a liquid adduct having a branched structure.

From our investigations, it is now found that such adducts can be prepared via a solvent free process with careful control of the reactants, processing aids, and process conditions. By the term "processing aids", it is understood substances which act catalyze reactions involving the isocyanate functionality and especially substances which promote the formation of the urethane linkage.

In a first aspect, this invention relates to a urethane-containing adduct comprising the reaction product of a monoahl with an isocyanate-terminated intermediate, itself obtained by coupling a polyisocyanate with a polyahl, wherein the adduct being a liquid at room temperature and having a number average molecular weight of from 600 to 80000 is substantially free of any isocyanate functionality or any isocyanate-reactive functionality.

In a second aspect, this invention relates to a urethane-containing composition which is a liquid at room temperature, being the reaction product of a monoahl with an

isocyanate-terminated intermediate itself obtained by coupling a polyisocyanate with a polyahl, which based on total moles present of components (a), (b) and (c) and to a total of 100 percent, comprises

(a) from 65 to 100 mole percent of an adduct of the general structure (I);

B - (A - M) _f (I)

(b) from less than 35 to 0 mole percent of an adduct of the general structure (II); and

M - A - M (II)

(c) from less than 12 to 0 mole percent of an adduct (III) containing two or more B moieties per molecule,

M - A- (B - A) _n - B - A - M (III)

where n ≥ 1 wherein A is derived from polyisocyanate;

B is derived from polyahl; M is derived from monoahl; and f is is the number of isocyanate reactive groups formally present on the polyahl.

In a third aspect, this invention relates to A solvent-free two-step process for preparing an adduct containing a plurality of urethane linkages being a stable liquid at room temperature and being substantially free of isocyanate or isocyanate-reactive groups, which comprises reacting in a first step a polyisocyanate with a polyahl to provide an isocyanate- terminated intermediate, and in a second step reacting the said intermediate with a monoahl, wherein: a) the polyisocyanate comprises at least two isocyanate moieties/molecule with a different relative reactivity to the polyahl; b) the polyahl is an organic substance having a molecular weight of from 200 to 20000 and containing per molecule two or more isocyanate-reactive functional groups being of -OH, -SH, -COOH, or -NHR where R is hydrogen or alkyl; c) the monoahl is an organic substance containing one isocyanate-reactive functional groups being of -OH, -SH, -COOH, or -NHR where R is hydrogen or alkyl characterized in that: i) for the first step, conducted in essentially anhydrous conditions and in the absence of a urethane-promoting catalyst, the polyahl is added at a controlled rate to the polyisocyanate such that the reaction temperature does not exceed

100°C and the total amount of polyahl added is a stoichiometric equivalent or less with respect to the polyisocyanate; and ii) for the second step, the monoahl is added in a restricted amount sufficient to consume all isocyanate groups wherein such amount is determined by directly monitoring the reaction mixture for the presence of isocyanate functionality.

In a fourth aspect, this invention relates to an isocyanate-terminated intermediate obtained by contacting in essentially anhydrous conditions and in the absence of a urethane-promoting catalyst, a polyahl having a molecular weight of from 200 to 20000 and containing per molecule two or more isocyanate-reactive functional groups being of -OH, -SH, - o COOH, or -NHR where R is hydrogen or alkyl, with a polyisocyanate comprising at least two isocyanate moieties/molecule with a different reactivity to the polyahl, wherein the polyahl is added at a controlled rate to the polyisocyanate such that the reaction temperature does not exceed 100°C and the total amount of polyahl added is a stoichiometric equivalent or less with respect to the polyisocyanate and the resulting intermediate, wherein said intermediate has an 5 isocyanate content of from 0.5 to 5 weight percent, and based on total weight present of components (a), (b) and (c) to a total of 100 percent, comprises:

(a) from 65 to 100 mole percent of an adduct of the general structure (IV);

B (- A) _f (IV)

(b) from less than 35 to 0 mole percent of an adduct of the general structure (V); and 0 ^A (V)

(c) from less than 12 to 0 mole percent of an adduct (VI) containing two or more B moieties per molecule, wherein A is polyisocyanate;

B is polyahl; and 5 f is the number of isocyanate reactive groups formally present on the polyahl. In yet another aspect, this invention relates to the use of the adduct, or composition thereof, as a lubricant, quenchant, hydraulic fluid, paint thickener, or surfactant. Such quenching and lubricating agents find value for example in the metal 0 processing industry where they may be employed in aqueous or non aqueous conditions. Surfactants or tensioactive agents find value in the manufacture of cellular polyurethane polymers. When the adduct is used as a hydraulic fluid it is advantageous present in an amount of from 1 to 50, preferably from 1 to 25 weight percent, based on total weight of the hydraulic fluid inclusive of adduct, and including any water present. When the adduct is employed as a 5 paint thickener it is advantageous present in an amount of from 0.1 to 10, preferably from 1 to 10 weight percent, based on total weight of the paint composition inclusive of adduct.

The adduct product of this invention is a substance, substantially free of any isocyanate functionality or any isocyanate-reactive group including hydroxyl, thiol, carboxylic

acid, thiocarboxylic acid, or primary amine functionality. The adduct is a liquid at room temperature (25°C) and comprises a plurality of urethane linkages. The adduct can be represented by the general structural formula (I). B - (A-M) _f (I) wherein: A is derived from polyisocyanate;

B is derived from polyahl; M is derived from monoahl; and f is is the number of isocyanate reactive groups formally present on the polyahl. It is to be appreciated that the linkage A-B and A-M will be a urethane linkage as derived from the reaction of an isocyanate group with an isocyanate-reactive group, for example a hydroxyl group.

When the adduct is based on a dif unctional polyahl it will have a linear structure; when based on a triol, it will have a branched or three limb structure, and so forth. For each polyisocyanate entity (A) incorporated into the adduct, at least two urethane linkages are introduced.

With reference to the process for preparing such liquid adducts, to be discussed in detail hereinafter, the product of this invention will in most cases be a composition comprising predominantly an adduct of structure (I), with minor amounts of adducts corresponding to Structures (II) and (III). Adduct II corresponds to a polyisocyanate (A) fully reacted with a monoahl (M); Adduct III corresponds to a structure containing two or more polyahl (B) entities per molecule. It is to be appreciated that adduct III may acquire a highly complexed, branched structure when the functionality of B is greater than 2, wherein each branch nominally will be terminated with an monoahl derived entity. By way of example, structures of Adduct II and III are given below, in this case (III) comprising two or more B moieties is depicted as a linear adduct originating through the polyahl containing two isocyanate reactive groups/molecule.

M - A - M (II)

M - A- (B - A) _n - B - A- M (III)

where n ≥ 1

An adduct corresponding to structure (II) can result when polyisocyanate reacts uniquely with monoahl; an adduct corresponding to Structure (III) can result when multiple molecules of polyisocyanate are able to react with multiple molecules of polyahl prior to reaction with monoahl. The liquid urethane-containing adduct product,of this invention may be characterized in that it has a number average molecular weight of from 600 to 80000, preferably from 1000 to 60000, and more preferably from 2000 to 30000. Compositions comprising the mentioned adduct (I) are further characterized by the presence of substances

corresponding to Structures (II) and (III), which based on total mole amount of said substances present, comprise from: for (I), at least 65, preferably at least 75, more preferably at least 80, and up to 100 mole percent; for (II), less than 35, preferably less than 25, more preferably less than 15, and most preferably 0 mole percent; and for (III), less than 12, preferably less than 10, more preferably less than 7, yet more preferably less than 5, and most preferably 0 mole percent. In a preferred embodiment the adduct composition may comprises substances (I), (II), and (III) in the mole percent ranges of from 65 to 90: from 30 to 5: from 6 to 1 respectively, wherein the total is to 100. By reference to good purity, it is understood that the end product has a low content of adducts represented by structures (II) and (III). During the present investigation it has been found that if the presence of structure (III) type substances can be minimized, then the resulting adduct is more likely to have a liquid characteristic at room temperature and especially when the polyahl used in the preparation of the adduct formally contained three or more isocyanate reactive groups/molecule. The adduct composition is related to the manufacturing process, and particularly to the method of preparation of the intermediate product, from polyahl and polyisocyanate, prior to reaction with monoahl. The adduct of this invention can be prepared by a solvent-free process which comprises a first step wherein a polyisocyanate is reacted, in the absence of a urethane- promoting catalyst, with a polyahl containing isocyanate-reactive groups to provide an isocyanate-terminated intermediate; and subsequently in a second step, reacting the isocyanate-terminated intermediate with a monoahl to provide the end product. The intermediate can be characterized in that it has an isocyanate content of from 0.5 to 5, preferably from 1 to 4 weight percent and is a composition which comprises structures (1 V), (V), and (VI) represented by the structural formulae:

B (- A) _f (IV)

A (V)

A - (B - A) _n - B - A (VI) where n ≥ 1

wherein: A is derived from polyisocyanate;

B is derived from polyahl; and f is the number of isocyanate reactive groups formally present on the polyahl. The proportions and amounts of (IV), (V), and (VI) are as given for (I), (II), and (III). Again, in this instance for the purpose of clarity adduct VI is depicted with a linear structure. However, as discussed for adduct III it is to be appreciated that adduct VI can also have a highly complexed branched structure.

A more detailed description of reactants and processing parameters are given hereinbelow. The polyisocyanate

The polyisocyanate used in the process to prepare the adduct has at least two isocyanate moieties/molecules which can be distinguished by a relative difference in reactivity. The reactivity difference helps to optimize the obtention of a product having a narrow molecular weight distribution and reduces the potential for formation of substances corresponding to structures (III) and (VI). Suitable polyisocyanates can be aliphatic or preferably aromatic polyisocyanates and especially aromatic diisocyanates. A further o advantage to using aromatic diisocyanates, where the relative reactivities of the individual isocyanate groups are different, is that it permits the amounts of free, non reacted, polyisocyanate (V) that may be present in the isocyanate-terminated intermediate to be limited to the subsequent advantage of material requirements for the second process step, and further to the value of the adduct in end applications. Exemplary of suitable aromatic polyisocyanates 5 include toluene diisocyanate, methylene diphenylisocyanate and polymethylene polyphenyl isocyanates. Preferred are polyisocyanates comprising isomers of toluene diisocyanate, of methylene diphenylisocyanate or mixtures thereof. In a highly preferred embodiment preferred, for reasons of relative isocyanate reactivity, is 2,4'-methylene diphenylisocyanate and especially 2,4-toluene diisocyanate, or mixtures comprising such 0 diisocyanate. The polyahl

The polyahl used in the process comprises two or more isocyanate-reactive functional groups per molecule where such functional groups include -OH, -SH, -COOH, or - NHR, with R being hydrogen or an alkyl moiety. Polyahls bearing -OH functionality are 5 preferred. The polyahl may contain up to 8 such functional groups per molecule, preferred is to use polyahls which contain from 2 to 8, preferably from 3 to 8, and more preferably from 3 to 6 functional groups per molecule.

The polyahl used in the process of this invention has a molecular weight of from 200 to 20000. The molecular weight of the polyahl preferably is from 500, more preferably 0 from 1000, and yet more preferably from 2000; and preferably up to 15000, and more preferably up to 10000. In a preferred embodiment the polyahl is a polyester or particularly a polyoxyalkylene polyol where the oxyalkylene entity comprises oxyethylene, oxypropylene, oxybutylene or mixtures of two or more thereof, including especially oxypropylene- oxyethylene mixtures. Alternative polyols that may be used in the invention include 5 polyalkylene carbonate-based polyols and polyphosphate-based polyols. The nature of the polyol selected depends on the desire of whether or not to impart some water solubility to the adduct, which can be advantageous for certain applications. Water solubility can be enhanced by selection of polyols having a lower molecular weight or an elevated oxyethylene content.

Suitable polyoxyalkylene polyols are exemplified by various commercially available polyols as used in polyurethane, lubricant, surfactancy applications and include polyoxypropylene glycols designated as VORANOL™ P-2000 and P-4000 with respectively molecular weights of 2000 and 4000; polyoxypropylene-oxyethylene glycols such as DOWFAX'" DM-30 understood to have a molecular weight of 600 and an oxyethylene content of 65 weight percent, and SYNALOX™ 25D-700 understood to have a molecular weight of 5500 and an oxyethylene content of 65 weight percent, all available from The Dow Chemical Company; polyoxyethylene triols available under the trademark TERRALOX™ and designated as product WG-98 and WG-116 understood to have a molecular weight of 700 and 980, respectively, polyoxypropylene-oxyethylene triols designated as VORANOL™ CP 1000 and CP 3055 understood to have respectively a molecular weight of 1000 and 3000, and VORANOL™ CP 3001 understood to have a molecular weight of 3000 and an oxyethylene content of 10 weight percent and VORANOL™ CP 6001 understood to have a molecular weight of 6000 and an oxyethylene content of 15 weight percent, all available from The Dow Chemical Company; polyoxypropylene hexols including VORANOL™ RN-482 understood to have a molecular weight of 700, and polyoxyethylene hexols including TERRALOX™ HP-400 understood to have a molecular weight of 975, both available from The Dow Chemical Company; higher functionality polyether polyols including those based on carbohydrate initiators such as, for example, sucrose and exemplified by VORANOL™ 370 available from The Dow Chemical Company. The Monoahl

The monoahl used in the process is an organic substance containing one isocyanate-reactive functional group per molecule being of -OH, -SH, -COOH, or -NHR where R is hydrogen or alkyl. Preferred is a monoahl having as the isocyanate-reactive functionality a hydroxyl group, hereinafter referred to an a monol. In addition to the isocyanate-reactive functional group the monoahl optionally may contain alternative functionality which under the conditions of the present invention are not considered as being isocyanate reactive. Exemplary of such alternative functionality can be alkene, alkyne, halogen.

The monol used in the process is chosen with consideration towards the intended end application. When it is desired to influence, for example, the water miscibility of the adduct product an appropriate hydrophilic or hydrophobic monol is used. Any hydrophilic/hydrophobic characteristics introduced by way of the polyahl will also contribute to the overall characteristics of the adduct. Similarly when it is desired to exercise additional control of for example the tensioactive properties of the adduct, an appropriate branched or fluorine or silicon containing monol is chosen.

Preferred monols for use in this invention are polyoxyalkylene monols with a molecular weight of from 150 to 6000: preferably from 250, more preferably from 500, yet more preferably from 1000; and preferably up to 5000, more preferably up to 4000. The

oxyalkylene entity of the monol oxyalkylene entity comprises oxyethylene, oxypropylene, oxybutylene or mixtures of two or more. As an alternative to polyoxyalkylene-based monoahls, or monols, substances containing polycarbonate, polysiloxane or polyphosphate moieties may also be employed. In a preferred embodiment of this invention the polyisocyanate is toluene diisocyanate comprising, substantially, the 2,4-isomer; the polyahl is a polyoxyalkylene polyol, especially a polyoxyethylene-oxypropylene polyol containing from 3 to 6 hydroxyl groups; and the monoahl is a polyoxyalkylene monol especially containing oxybutylene groups. Particularly preferred monols, when intending to enhance hydrophobic characteristics, are those o comprising the oxybutylene entity, especially in an amount of more than 50 weight percent by total weight of the monol. The Process

The method of preparing the urethane-containing adduct is a two step process comprising a first and a second step, optionally between the first and second step is an 5 intermediate step.

The first step relates to the preparation of an isocyanate-terminated intermediate by reacting the polyisocyanate with the polyahl at a reaction temperature which does not exceed 100°C, in essentially anhydrous conditions. By essentially anhydrous conditions it is understood less than 1500, preferably less than 750, more preferably less than 350 ppm of 0 water. The reaction temperature advantageously is from 20°C, more preferably from 35°C; and preferably up to 80°C, more preferably up to 70°C. Operating in such a temperature range provides for an optimum reaction rate without loss of the difference in the relative reactivities of the individual isocyanate groups of the polyisocyanate. At higher temperature, the beneficial effect of the relative isocyanate reactivities can be substantially diminished, and 5 additionally isocyanate may be consumed by an undesirable allophanate reaction. The polyahl is added at a controlled rate to the polyisocyanate such that the reaction temperature does not exceed 100°C, with the total amount of polyahl added being a stoichiometric equivalent or less with respect to the polyisocyanate. The total amount of polyahl advantageously does not exceed 0.99, preferably does not exceed 0.95 of an equivalent; and advantageously is at least 0 0.4, preferably at least 0.6, and more preferably from 0.85 of an equivalent per equivalent of isocyanate. In a highly preferred embodiment when the polyahl is a polyol it is present in a total amount corresponding to from 0.85 to 0.95 of an equivalent.

As already mentioned, the first process step is conducted in essentially anhydrous conditions and in the absence of a processing aid, as defined hereinabove. To minimize 5 potential gel formation, or even solidification, it is advantageous to use polyahls which do not contain any alkoxyaltion catalyst or catalyst finishing residues, for example potassium acetate, which might promote urethane formation or isocyanate dimerization ortrimerization. Additionally to minimize gel formation when preparing the intermediate it is advantageous to

use polyahls, especially polyols, that have an acid content; such procedures when preparing' isocyanate-terminated prepolymers are known from the general art and need not be further described. In the course of the present investigations it is found that the absence, in the first process step, of a urethane-promoting catalyst is particularly advantageous with respect to exercising some control on the formation of substances corresponding to Structure (VI), and eventually structure (III) of the adduct composition.

When the resulting isocyanate-terminated intermediate has a higher free, unreacted, isocyanate content, corresponding to Structure (V), and before proceeding with the second step of the process it can be advantageous to reduce such content by, for example, distillation or extraction techniques using suitable solvents including pentane or hexane. Free, unreacted diisocyanate can participate in the second process step providing capped products, the presence of which in the final product may be detrimental to performance in certain end applications.

In the second step of the process, the isocyanate-terminated intermediate is reacted with a controlled amount of a monoahl to provide the adduct. The controlled amount is such to essentially convert all isocyanate functionality without leading to the accumulation of any isocyanate-reactive functionality in the end adduct product. The amount required to achieve this result is determined by adding in increments the monoahl and directly monitoring the reaction mixture for presence of free reactive functionality, in this case isocyanate functionality. The incremental addition continuing until the presence of isocyanate functionality is reduced to a minimum or zero, without accumulation of any other isocyanate reactive functionality.

In the process of the present invention it is preferred to employ on-line, in situ, spectrometry techniques. Especially of value is infrared spectrometry which permits the ready observation of the presence of isocyanate functionality by observing absorption at wavelengths of, for example, from 2200 to 2300 cm- ¹ . Observation at other wavelengths in, for example, near-IR frequencies is also possible. Use of a fourier transfer infrared spectrometer provides a convenient means of rapid observation for isocyanate functionality directly in the reaction vessel thus avoiding the need to take isolated samples. Traditional monitoring methods involving isolation and subsequent reactive chemical analysis, for example by titration itself subject to operator error, of material is thereby avoided.

For the second step, the process temperature is chosen for convenience of reaction time and can be greater than 100°C without detriment to the performance of the adduct in end applications. In general, extended exposure to a temperature greater than 100°C should be minimized for the purpose of avoiding undesirable side reactions including allophanate formation. The reaction of the isocyanate-terminated intermediate with the monoahl can, if desired, be accelerated by use of a suitable urethane-promoting catalyst. Representative of such catalysts include tertiary amine compounds and organotin compounds

as used when preparing for example polyurethane foam by reaction of a polyisocyanate with a polyol.

The above described two-step process is the preferred method of manufacturing the adduct as it provides the possibility of manufacturing a standard intermediate master batch which can be reacted with various monoahls selected to provide adducts suited to different application areas. Other methods can be envisaged including for example first reacting the monoahl with polyisocyanate to provide an alternative isocyanate-terminated intermediate and subsequently reacting this with the polyahl. In such an alternative reaction sequence, it will be necessary to adapt the direct online, jn situ, method such that it provides for monitoring of the amount of polyahl and avoidance of accumulation of isocyanate-reactive moieties yet not lead to any unreacted isocyanate functionality.

The invention is illustrated by the following examples in which all parts and percentages are by weight, unless otherwise stated. Example 1 (absence of catalyst in first step) This example teaches the preparation of an adduct by first reacting 2,4-toluene diisocyanate (95% purity, 5% 2,6- isomer) with a glycerine-initiated polyoxypropylene- oxyethylene triol (molecular weight 2150, EO content 53 wt% , random) to provide an intermediate product which is subsequently reacted with a polyoxybutylene monoalcohol of 500 molecular weight, SYNALOX™ OA-15, available from The Dow Chemical Company. The toluene diisocyanate, 20.2 parts, was introduced into a closed reactor equipped with a stirrer, nitrogen supply, FTIR immersion probe and external temperature control mantel. The toluene diisocyanate was brought to a temperature of 50°C and 75 parts of polyol added in increments at a rate such that the contents of the reactor do not exceed 60°C. The polyol is present in an amount of 0.45 of an equivalent per equivalent of polyisocyanate. On completion of the addition of the polyol, 0.6 parts of dibutyltin dilaurate was added followed by rapid incremental additions of the polyoxybutylene monoalcohol until the FTIR spectrum did not indicate any absorption at

2273 cm- ¹ (isocyanate band). After the addition of a total of 56.95 parts of polyoxybutylene monoalcohol no isocyanate absorption was observed in the IR spectrum. The resulting product is a stable liquid at room temperature having a molecular weight of 4140, and being substantially free of isocyanate or hydroxyl end groups. Example 2 (absence of catalyst in the first step)

In this example, the same reactants and general procedure as given for Example 1 has been used, but with a reverse addition sequence. In the first step, 20.2 parts of 2,4-toluene diisocyanate is reacted with a total of

56.95 parts of the polyoxybutylene monoalcohol. Subsequently the resulting intermediate is reacted, in the presence of 0.6 part of dibutyltin dilaurate with the glycerine-initiated polyoxypropylene-oxyethylene triol. The polyol is added in increments until no isocyanate

absorption was observed in the IR spectrum, which occurred after the addition of a total of 120 parts of polyol. The resulting product is a liquid, but is observed to have a hydroxyl content. Comparative Example A (with catalyst in the first step)

In this example, the same reactants and general procedure as given for Example 1

5 has been used.

In the first step, 20.2 parts of 2,4-toluene diisocyanate is mixed with 0.6 part of dibutyltin dilaurate and the mixture brought to a temperature of 50°C and incremental addition of the polyol started. After the addition of polyol to a total amount of only 55 parts, the synthesis procedure was terminated due to the formation of a gel/solid. 0 Comparative Example B (with catalyst in the first step)

In this example, the same reactants and general procedure as given for Example 1 has been used, but with a reverse addition sequence.

In the first step, 20.2 parts of 2,4-toluene diisocyanate is mixed with 0.6 part of dibutyltin dilaurate and the mixture brought to a temperature of 50°C prior to the incremental

15 addition of a total of 56.95 parts of the polyoxybutylene monoalcohol over a period of one hour. Subsequently, a total of 75 parts of the polyoxyethylene-oxypropylene polyol was added incrementally to the product of the first step. After 40 minutes the viscosity of the mixture started to increase and shortly after this a gelled, solid, product resulted.

Examples 1, 2 and Comparative Examples A and B demonstrate the importance of

20 having in the first process step the absence of a urethane-promoting catalyst. The examples also demonstrate the value of first reacting the polyisocyanate with polyahl, and then subsequently reacting the intermediate with a monoahl. Example 3

In order to obtain a better understanding of the role of the dibutyltin dilaurate in

25 the preparation procedure, a series of isocyanate-terminated intermediate products has been prepared.

A series of isocyanate-terminated intermediates has been prepared using the general procedure as given in Example 1, first step, by reacting 2,4-toluene diisocyanate (95% purity) with a polyoxyethylene-oxypropylene diol (molecular weight 4000, EO content

30 50 wt%, primary hydroxyl content > 70%) in the absence of a urethane-promoting catalyst. The proportion of polyol to polyisocyanate is such to provide 0.91, 0.77, 0.66, 0.5 and 0.27 equivalent of polyol per equivalent of polyisocyanate. The resulting intermediate compositions are analyzed using ¹³ C NMR analytical techniques to establish the proportion of products corresponding to structures (IV), (V) and (VI).

35 A parallel comparative series of isocyanate-terminated intermediates is prepared form the same reactants in the same proportions but in the presence of a catalyst, dibutyltin dilaurate.

Table 1 reports the observations, for which the following remarks can be made. With a desire to enhance the formation of substances corresponding to Structure (IV) it is advantageous to employ the polyol in an equivalent amount approaching that of the polyisocyanate. At high equivalency rates the occurrence of free polyisocyanate (Structure V) is reduced, however it is noted that the occurrence of a chain extended substance (VI) increases. It is the presence of such substances corresponding to structure (VI) which generally cause gellation or solidification of product, especially when employing higher functionality reactants. From the comparison of procedures conducted in the presence and absence of catalyst, it is found that the presence of catalyst favors the undesirable formation of structure (VI) type substances. Accordingly, in this invention no urethane-promoting catalyst should be present in the first step of the process. It is also surprisingly found, when employing the polyol in an amount of more than 0.8 equivalent per equivalent of polyisocyanate, that in the absence of catalyst a greater formation of the desired intermediate (IV) is observed. Although intermediates prepared in the absence of a catalyst may have a higher free polyisocyanate content (V), such substance optionally can be removed as discussed hereinabove providing for an intermediate composition in which the amounts of non desirable substance (V) has been significantly reduced.

I

I-* )

I

Not an example of this invention

Example 4

A number of liquid urethane-containing adducts have been prepared according to the general procedure of a Example 1 using different polyisocyanate, polyahls and monoahls. Table 2 summarizes the adducts which have been prepared.

Polyisocyanate A: 2,4- , 2,6-toluene diisocyanate (95: 5)

Polyahl A: a 4000 molecular weight polyoxypropylene-oxyethylene diol with a 40 weight percent oxyethylene content. Polyahl B: a 2150 molecular weight polyoxypropylene-oxyethylene triol with a 50 weight percent oxyethylene content, randomly distributed. Polyahl C: a 5125 molecular weight polyoxypropylene-oxyethylene hexol with a 50 weight percent oxyethylene content, randomly distributed. Monoahl A: C ₆ F ₁₃ CH ₂ CH ₂ OH.

Monoahl B: Dodecanol.

Monoahl C: a 500 molecular weight butanol-initiated polyoxybutylene product.

Monoahl D a 2000 molecular weight butanol-initiated polyoxybutylene product.

Monoahl E a 650 molecular weight oxypropylene adduct of a polyoxyfluoropropane alcohol. Monoahl F a 1000 molecular weight trimethylsiloxy-hydroxyethoxypropyl polydimethylsiloxane oligomer. EXAMPLE 5

The lubrication performance of Products 4.9 and 4.10 has been compared to that of commercially available fluids SYNALOX™ 50-300B and SYNALOX™ 100-D280. SRV observations (according to DIN 51834): Product 4.9: viscosity, 5300 cSt at 40°C friction 0.13 mu max load 730 Newton Product 4.10 viscosity, 8500 cSt at 40°C friction 0.13 mu max load 680 Newton SYNALOX™ 50-300B friction 0.12 mu max load 400 Newton SYNALOX™ 100-D280 friction 0.12 mu max load 430 Newton Four Ball Scar Test (according to DIN 51350): Product 4.9: no scar detected (< 0.1 mm)

Product 4.10 no scar detected (< 0.1 mm)

SYNALOX™ 50-300B 0.55 mm scar SYNALOX™ 100-D2800.59 mm scar

In the SRV (swing, friction, wear) observations, normally the friction increases with viscosity, the adducts of this invention having high viscosity are found, unexpectedly to have equivalent friction properties as lower viscosity adducts. Such a finding provides a possibility of high temperature lubrication or quenching end uses. The further observation of little or no scar formation indicates that the products of this invention exhibit excellent film formation under running conditions. Example 6

In this example, the ability of products of this invention to function as tensioactive agents in the preparation of rigid polyurethane foam is demonstrated. Polyurethane foam is prepared using a low pressure machine with the below given formulation. Polyurethane foam having a molded density of from 30 to 32 kg/m3 is prepared and the cell size and initial thermal insulation per ormance observed.

100 pbw oxypropylene adduct of sorbitol and glycerine having an average hydroxyl number of 261 1.0 pbw N,N-dimethylcyclohexylamine

0.10 pbw NIAX A-1, a proprietary amine-based urethane catalyst from OSi.

0.6 pbw CURITHANE 206, a proprietary amine-based urethane catalyst from

The Dow Chemical Company 4.0 pbw water SURFACTANT - various, see following Table.

152 pbw VORANATE M220, a polymeric MDI available from The Dow

Chemical Company (Index 120)

The observations reported in the attached table clearly demonstrate the ability, under non optimized conditions, of the products of this invention to function as surfactants. Surfactant L6900 is a commercially available silicon-based surfactant commonly used when preparing polyurethane foam.