Catalysts for alkoxylation reactions
This invention relates to the production of alkoxylated organic compounds by reacting said compounds with an alkoxylating agent in the presence of BF 3  or SiF 4  together with metal alkyls or metal alkoxides. More particularly, this invention relates to the production of alkoxylated organic compounds by reacting said compounds with the catalysts of the present invention in the presence of alkoxylating agents to yield a very sharply peaked alkoxylate distribution in the product. 
     In general, the reaction of a variety of organic materials together with an adducting material such as ethylene oxide or propylene oxide to form alkoxylated materials is well known in the art. U.S. Pat. No. 2,683,087 discloses that water adsorption by paper articles is improved by the use of amine adducts of ethylene oxide. British Pat. No. 847,714 teaches the processing of prehydrolyzed sulfate wood pulp into viscose by incorporating a propylene oxide/ethylene oxide adduct of ethylene diamine. French Pat. No. 1,122,729 discloses the use of acylarylpolyglycol adduct to the viscose pulp or slurry. Belgium Pat. No. 555,529 discloses an anti-static agent for synthetic fibers produced by esterifying one mole of lauric acid with one mole of an ethoxylated glycerol British Pat. No. 763,215 suggests an ethoxylated organic sulfamide as an anti-static agent for textiles. 
     British Pat. No. 705,117 discloses an emulsifier combination for pesticides comprising a mixture including a tall oil or dodecyl mercaptan adduct. Polyhydric alcohol ethoxylates find uses in foods and feeds as shown by U.S. Pat. No. 2,674,534 which discloses the use of sorbitol laurate and sorbitol oleate adducts in the coating of ice cream bars. Alkylene oxide adducts are also used in the leather industry in formulations for tanning, dyeing, and lubricating leather. Adducts of organic materials also have a variety of uses and metal working industries where ester, ether and amine adducts are the products used most frequently. Ethylene oxide adducts such as sorbitan monostearate adducts have been found useful in pharmaceutical and cosmetic preparations and are used to provide activities such as drug carriers, emulsifiers and solubilizers. Ethylene oxide adducts of nonyl phenols have been used to produce detertents and cleaning agents, domestic and industrial laundry detergents, detergent builders, polishers, sanitizers, and dry cleaning materials. Alkyl phenol adducts are especially good soil suspending materials when used in detergent formulations since they possess excellent detergency, fat emulsifying power, concentration effect, chemical resistance, hard water stability and pH properties. 
     Much literature is available in the general area of alcohol alkoxylation. These references relate to the catalytic ability of various materials in the mechanism of kinetics of these reactions. For example, French Pat. No. 1,365,945 teaches the use of compounds containing an active hydrogen atom reacted with ethylene oxide in the presence of an alkali metal base. 
     Both basic and acidic catalysts in general are known to produce alkoxylation of organic materials. However, alkoxylation of these materials invariably produces a distribution of various adducts. For example, in surfactant applications, an adduct of too few ethylene oxide molecules is not effective because of poor solubility. In contrast, an adduct with too many ethylene oxide molecules is likewise undesirable because surface tension reduction per unit mass decreases drastically as the molecular weight increases. Thus it has long been essential to produce and use alkoxylates with as sharp a distribution in the desired mole adduct range for the particular use of the material as can possibly be realized. 
     Normally, acid catalyzed reactions produce such alkoxylates, but these catalysts produce harmful side products which must be separated and removed prior to use. Base catalysts normally do not produce the level of by-products which acidic catalysts do, but provide a much broader distribution of alkoxylation adducts, thus making them economically unsuitable. Thus both methods have disadvantages. 
     Therefore, it would be desirable to provide a catalyst system for the alkoxylation of organic materials which provides low by-product levels, typical of base catalysts, yet provides a narrow distribution of the preferred mole adducts, normally obtained from acid catalysts. Such a catalyst would promote the narrowing of product distribution curve and would contribute significantly to the intrinsic value of the alkoxylate produced. 
     Such a catalyst is described in U.S. Pat. Nos. 4,239,917 and 4,306,093. However, these catalysts, while effective in producing a very sharply peaked distribution product, do not produce alkoxylate peaks as sharp as the catalysts to be described herein. 
     The use of dialkyl aluminum fluoride or alkyl aluminum difluoride is known as a catalyst for the polymerization of epoxides to produce polyalkoxy alcohols as described in U.S. Pat. Nos. 3,029,217 and 3,313,743. However, these catalysts were not used in the alkoxylation of alcohols and require water in the polymerization described. In addition, dialkyl aluminum halides or alkyl aluminum dihalides can be used to produce ethoxylated alcohols using different methods, such as the polymerization of ethylene oxide described in U.S. Pat. No. 3,321,533. However, in this process the materials are not used as catalysts, but rather as reactants since sodium hydroxide acts as the ethoxylation catalyst. 
     U.S. Pat. No. 3,395,185 utilizes organoaluminum zinc compounds as catalysts in the preparation of low molecular weight polyoxymethylene glycols. Zinc, however, is not an effective catalyst in the present invention. U.S. Pat. No. 2,716,137 uses nitrogen containing catalysts. These materials are characterized by low reaction rates and objectionable odors. U.S. Pat. No. 4,282,387 uses catalysts such as calcium, strontium and barium acetates and naphthenates. These materials produce alkoxylate products more sharply peaked than current commercial basic catalysts such as sodium and potassium hydroxide, but do not provide the extremely high peaking of the present invention. 
     The ethoxylation of alcohols using aluminum compounds such as aluminum trifluoride or trialkyl aluminum is described in U.S. Pat. Nos. 2,879,220; 3,350,462; 3,719,636 and 3,969,417. Preparation of alkoxylated alcohols using a latent catalyst comprising a mixture of BF 3  and trialkyl phospheric is shown in U.S. Pat. No. 3,597,502 and 3,910,878. Zinc dialkyl catalysts for alcohol alkoxylation are shown in U.S. Pat. No. 3,395,185. 
     It is therefore an object of the present invention to provide a catalyst system which will yield a narrow alkylene oxide adduct distribution in the alkoxylation of organic materials, while providing low levels of undesirable by-products and non-desired alkoxylation adducts. Other objects will become apparent to those skilled in this art as the description proceeds. 
     It has now been discovered according to the instant invention that alkoxylation of organic materials can be carried out in the presence of at least one catalyst comprising BF 3  and metal alkyls, SiF 4  and metal alkyls or mixtures of these catalysts, wherein the metal alkyls have the general formula M(R) n  wherein each R is, independently, hydrogen and alkyl groups containing from 1 to 20 carbon atoms, and wherein M is selected from the group consisting of aluminum, galluim, indium, thallium, titanium, zirconium and hafnium, and n is 3 or 4, depending on valence of M. Aluminum and titanium metal alkyls are preferred. These alkyl groups will normally contain from about 1 to about 20 carbon atoms each, but the preferred catalysts are those containing from about 1 to about 14 carbon atoms each. 
     Representative but non-exhaustive examples of such catalysts are BF 3  /aluminum hydride, BF 3  /trimethylaluminum, BF 3  /triethylaluminum, BF 3  /tripropylaluminum, SiF 4  /aluminum hydride, SiF 4  /trimethylaluminum, SiF 4  /triethylaluminum, BF 3  /dimethyl ethyl aluminum, SiF 4  /dimethyl ethyl aluminum, BF 3  /(C 20  H 41 ) 3  Al, SiF 4  /C 20  H 41 ) 3  Al, BF 3  /titanium hydride, BF 3  /tetramethyltitanium, BF 3  /tetraethyltitanium, BF 3  /tetrapropyltitanium, SiF 4  /titanium hydride, SiF 4  /tetramethyltitanium, SiF 4  /tetraethyltitanium, BF 3  /dimethyl diethyl titanium, SiF 4  /dimethyl diethyl titanium, BF 3  /(C 20  H 41 ) 4  Ti, SiF 4  /(C 20  H 41 ) 4  Ti, BF 3  /trimethyl gallium; BF 3  /trimethyl indium; BF 3  /trimethyl thallium, BF 3  /tetramethyl zirconium, SiF 4  /tetramethyl hafnium. 
     Catalysts which provide similar adduct distributions but which are less expensive comprise BF 3  and metal alkoxides, SiF 4  and metal alkoxides, or mixtures of these catalysts, wherein the metal alkoxides have the general formula M(OR) n  where each R is, independently, hydrogen and alkyl groups containing from 1 to 20 carbon atoms each, M is aluminum or titanium, and n is 3 or 4 depending on valence of M. Preferred catalyst are those containing from 1 to 14 carbon atoms in each alkyl group. 
     Representative but non-exhaustive examples of such catalysts are BF 3  /(C 2  H 5  O) 3  Al; BF 3  /(CH 3  O) 3  Al; SiF 4  /(C 2  H 5  O) 3  Al; SiF 4  /(CH 3  O) 3  Al; BF 3  /(CH 3  O) 2  (C 2  H 5  O)Al; SiF 4  /(CH 3  O) 2  (C 2  H 5  O)Al; SiF 4  /(CH 3  O) (C 2  H 5  O) 2  Al; BF 3  /(CH 3  O) 3  Al; BF 3  /(C 2  H 5  O) 3  Al; BF 3  /(C 20  H 41  O) 3  Al; BF 3  /C 2  H 5  O) 4  Ti; BF 3  /(CH 3  O) 4  Ti; SiF 4  /(C 2  H 5  O) 4  Ti; SiF 4  /(CH 3  O) 4  Ti; BF 3  /(CH 3  O) 2  (C 2  H 5  O) 2  Ti; BF 3  /(CH 3  O) 2  (C 2  H 5  O) 2  Ti and SiF 4  /(CH 3  O) 2  (C 2  H 5  O) 2  Ti. 
     The instant invention can be carried out at temperatures of from about 20° C. to about 260° C. However, more normal temperatures range from about 90° C. to about 200° C. For practical purposes, most commercial operations will be carried out in the temperature range of from about 100° C. to about 200° C. 
     BF 3  is a known alkoxylation catalyst at lower temperatures, 100° C. or lower. However, BF 3  is normally added to the reaction in a gaseous form. When present in this form, and at these temperatures, the presence of water in the reaction forms high levels of by-products which are undesirable and difficult to separate, such as polyethylene glycol and dioxane. 
     The catalysts of the present invention can be used in the processes described when carried out at ambient pressure. However, pressures above or below ambient can be used as desired. Pressure or lack of pressure is not a critical factor in the present invention and pressures may be used as convenient. Normally pressures of up to about 100 pounds per square inch (psig) can be used, but pressures below about 60 psig are preferred. It is simply more convenient to normally carry out the reactions in the pressure range of from about atmospheric to about 100 psig. 
     The alkoxylations of the present invention are normally carried out with materials or mixtures of materials comprising alpha and beta alkylene oxide. Of these materials, ethylene oxide, propylene oxide or mixtures of these are preferred. However, the process and catalysts of the present invention will be effective for any adducting material desired. 
     The reaction products can have any desired content of adducting material. For example, in alcohol alkoxylations, ethylene oxide will normally comprise from about 30 to about 90% of product content based on weight. However, for most purposes the content of ethylene oxide will range from about 40% to about 70% by weight. The weight of adducting material present in the reaction is not critical other than the minimum amount necessary to provide sufficient units to reach the mole adduct level desired for the materials to be reacted. 
     For practical purposes, normally from about 0.05 to about 5.0 weight percent catalyst based upon the weight of the material to be reacted is present in the reaction. Preferred levels of catalysts in the reaction mixture are from about 0.1 to about 3.0% by weight based on the total reaction mixture weight. 
     The catalysts of the present invention are normally added to the reaction mixture in a solution form. However, in order to render these catalysts less air sensitive and more stable, catalysts can optionally be supported on materials having active surface hydroxyl groups. Representative but non-exhaustive examples of such supports are alumina, diatomaceous earth, silica, bentonite glass, various clays and the like. 
     When utilizing the catalysts of the present invention, normally the catalysts are used in mole ratios of BF 3  to SiF 4  to metal alkyls or metal alkoxides of from about 0.1 to about 10 but from about 0.2 to about 2 are preferred. 
     If desired, the catalysts of the present invention can be prepared separately and added to the reactor either together or separately, or can be prepared separately, placed in an inert solvent for handling ease and placed in the reactor, or can be combined with the metal alkyls or alkoxides prior to insertion into the reactor, either alone or in the presence of an inert solvent. The relationship between BF 3  and/or SiF 4  and the normally inert metal alkyls and metal alkoxides is not clear, but apparently the mere presence of metal alkyls and metal alkoxides provides the sharpened distribution of the present invention. 
     Representative examples of inert solvents useful in the present invention include the saturated aliphatic hydrocarbons and low polynuclear aromatic hydrocarbons. Such inert solvents include heptane, hexane, octane, nonane, and decane. 
     The catalysts described herein do not impart large shifts in pH to a reaction system as do NaOH or BF 3  alone. In the catalyzed system of the present invention, pH has little meaning. 
     The catalysts of the present invention are useful for the alkoxylation of organic materials which can normally be alkoxylated. Among such materials are alcohols, whether polyhydric, unsaturated, linear or branched; saturated alcohols, alkyl phenols, polyols, aldehydes, ketones, amines, amides, organic acids and mercaptans. 
     These organic materials are normally selected from the group consisting of 
     (a) polyhydric alcohols containing a total of 2 to 30 carbon atoms and having the general formula ##STR1## wherein R 1 , R 2 , and R 3  are, independently, linear or branched acyclic groups, alicyclic groups, aryl groups, cyclic groups, or hydrogen and wherein the R-designated groups can in addition contain one or more functional groups selected from the group consisting of amine, carboxyl, hydroxy, halogen, nitro, carbonyl, and amide; 
     (b) aldehydes and ketones having boiling points above 100° C. and containing a total of from 2 to 30 carbon atoms, and having one or more carbonyl containing compounds of the general formula ##STR2## wherein R 1  and R 2  are, independently, hydrogen, linear or branched acyclic groups, alicyclic groups, cyclic groups, or aryl groups and wherein the R-designated groups can in addition contain one or more functionalities selected from the group consisting of carboxyl, hydroxyl, halogen, nitro, amine, or amide; 
     (c) primary, secondary or tertiary amides having a boiling point of above 100° C. and containing a total of from 1 to 30 carbon atoms and containing 1 or more amide containing compounds of the general formula ##STR3## wherein R 1 , R 2 , and R 3  are, independently hydrogen, linear or branched acyclic groups, alicyclic groups, cyclic groups, or aryl groups and wherein the R-designated groups can in addition contain one or more other functionalities selected from the group consisting of hydroxyl, carboxyl, carbonyl, amine, nitro, or halogen; 
     (d) primary, secondary or tertiary amines having a boiling point above 100° C., containing from a total of 1 to 30 carbon atoms and containing 1 or more amine containing compounds of the general formula ##STR4## wherein R 1 , R 2 , and R 3  are, independently, hydrogen, linear or branched acyclic groups, alicyclic groups, cyclic groups, or aryl groups, and wherein the R-designated groups can in addition contain one or more functionalities selected from the group consisting of hydroxyl, carbonyl, halogen, carboxyl, nitro or amide; 
     (e) organic acids having a boiling point of above 100° C., containing from a total of 1 to 30 carbon atoms and having 1 or more carboxylic acid containing compounds of the general formula ##STR5## wherein R 1  is a hydrogen, a linear or branched acyclic group, alicyclic group, cyclic group, or aryl group and wherein the R group can in addition contain one or more functionalities selected from the group consisting of carbonyl, hydroxyl, halogen, nitro, amine, or amide; 
     (f) alkyl phenols having a boiling point of above 100° C., containing a total of from 6 to 30 carbon atoms and having 1 or more compounds of the general formula ##STR6## wherein R 1 , R 2 , R 3 , R 4 , and R 5  are, independently, hydrogen, halogen, hydroxyl, nitro, or carbonyl, linear or branched acyclic groups, alicyclic groups cyclic groups, aryl groups, or substituted aryl groups and wherein in addition the R-designaged groups can contain one or more functionalities selected from the group consisting of halogen, ether, nitro, carboxyl, carbonyl amine, amide, or hydroxyl; 
     (g) mercaptans of the general formula ##STR7## wherein R 1 , R 2  and R 3  are, independently, hydrogen, linear or branched acyclic groups, alicyclic groups, cyclic groups or aryl groups containing from 1 to 30 carbon atoms and wherein the R 1 , R 2  or R 3  designated groups can in addition contain one or more functionalities selected from the group consisting of carboxyl, hydroxyl, halogen, nitro amine, or amide, and 
     (h) alcohols of the general formula ROH where R is a linear or branched alkyl group containing from 1 to 30 carbon atoms, an aryl group or a cyclic group containing from 6 to 30 carbon atoms, or an olefinic or acetylenic group containing from 1 to 30 carbon atoms. 
     While the instant invention is effective with all classes of alcohols, both saturated and unsaturated, saturated alcohols are preferred. Of these, alkanols are most preferred. The primary, secondary linear and branched, linear and branched primary alkanols are the most commonly used and are the preferred materials for alkoxylation using the present invention. 
     Representative but non-exhaustive examples of alcohols which can be alkoxylated according to the present invention are 1-dodecanol; 1-tridecanol; 1-tetradecanol; 1-pentadecanol; 1-hexadecanol; 1-heptadecanol; 1-octadecanol; 1-nonadecanol; 1-eicosanol; 1-docosanol; 2-methyl-1-undecanol; 2-propyl-1-nonanol; 2-butyl-1-octanol; 2-methyl-1-tridecanol; 2-ethyl-1-dodecanol; 2-propyl-1-undecanol; 2-butyl-1-decanol; 2-pentyl-1-nonanol; 2-hexyl-1-octanol; 2-methyl-1-pentadecanol; 2-ethyl-1-tetradecanol; 2-propyl-1-tridecanol; 2-butyl-1-dodecanol; 2-pentyl-1-undecanol; 2-hexyl-1-decanol; 2-heptyl-1-decanol; 2-hexyl-1-nonanol; 2-octyl-1-octanol; 2-methyl-1-heptadecanol; 2-ethyl-1-hexadecanol; 2-propyl-1-pentadecanol; 2-butyl-1-tetradecanol; 1-pentyl-1-tridecanol; 2-hexyl-1-dodecanol; 2-octyl-1-decanol; 2-nonyl-1-nonanol; 2-dodecanol; 3-dodecanol; 4-dodecanol; 5-dodecanol; 6-dodecanol; 2-tetradecanol; 3-tetradecanol; 4 -tetradecanol; 5-tetradecanol; 6-tetradecanol; 7-tetradecanol; 2-hexadecanol; 3-hexadecanol; 4-hexadecanol; 5-hexadecanol; 6-hexadecanol; 7-hexadecanol; 8-hexadecanol; 2-octadecanol; 3-octadecanol; 4-octadecanol; 5-octadecanol; 6-octadecanol; 7-octadecanol; 8-octadecanol; 9-octadecanol; 9-octadecenol-1; 2,4,6-trimethyl-1-heptanol; 2,4,6,8-tetramethyl-1-nonanol; 3,5,5-trimethyl-1-hexanol; 3,5,5,7,7-pentamethyl-1-octanol; 3-butyl-1-nonanol; 3-butyl-1-undecanol; 3-hexyl-1-undecanol; 3-hexyl-1-tridecanol; 3-octyl-1-tridecanol; 2-methyl-2-undecanol; 3-methyl-3-undecanol; 4-methyl-4-undecanol; 2-methyl-2-tridecanol; 3-methyl-3-tridecanol; 4-methyl-3-tridecanol; 4-methyl-4-tridecanol; 3-ethyl-3-decanol; 3-ethyl-3-dodecanol; 2,4,6,8-tetramethyl-2-nonanol; 2-methyl-3-undecanol; 2-methyl-4-undecanol; 4-methyl-2-undecanol; 5-methyl-2-undecanol; 4-ethyl-2-decanol; 4-ethyl-3-decanol; tetracosanol; hexacosanol; octacosanol; triacontanol; dotriacontanol; hexatriacontanol; 2-decyltetradecanol; 2-dodecylhexadecanol; 2-tetradecyloctadecanol; 2-hexadecyleicosanol, and unsaturated alcohols such as 1-hexyn-3-ol; oleyl alcohol (technically names cis-9-octadecene 1-ol); 2,5-dimethyl-4-octyne-3,6-diol; 2,4,7,9-tetramethyl-n-decyne-4,7-diol; 3-dodecene-1-ol; and 3,6-dimethyl-8-dodecene-1-ol. 
     Representative but non-exhaustive examples of various polyhydric alcohols which can be alkoxylated according to the present invention are 
     ethylene glycol 
     1,2-propylene glycol 
     1,4-butanediol 
     1,6-hexanediol 
     1,10-decanediol 
     1,3-butylene glycol 
     diethylene glycol 
     diethylene glycol monobutyl ether 
     diethylene glycol monomethyl ether 
     diethyl glycol monoethyl ether 
     dipropylene glycol 
     dipropylene glycol monomethyl ether 
     ethylene glycol monomethyl ether 
     ethylene glycol monoethyl ether 
     ethylene glycol monobutyl ether 
     hexylene glycol 
     mannitol 
     sorbitol 
     pentaerythritol 
     dipentaerythritol 
     tripentaerythritol 
     trimethylolpropane 
     trimethylolethane 
     neopentyl glycol 
     diethaholamine 
     triethanolamine 
     diisopropanolamine 
     triisopropanolamine 
     1,4-dimethylolcyclohexane 
     2,2-bis(hydroxymethyl)propionic acid 
     1,2-bis(hydroxymethyl)benzene 
     4,5-bis(hydroxymethyl)furfural 
     4,8-bis(hydroxymethyl)tricyclo[5,2,1,0]decane 
     tartaric acid 
     2-ethyl-1,3-hexanediol 
     2-amino-2-ethyl-1,3-propanediol 
     triethylene glycol 
     tetraethylene glycol 
     glycerol 
     ascorbic acid 
     Representative but non-exhaustive examples of various aldehydes and ketones which can be alkoxylated according to the present invention are 
     lauryl aldehyde 
     benzaldehyde 
     2-undecanone 
     acetophenone 
     2,4-pentandione 
     acetylsalicyclic acid 
     ortho-chlorobenzaldehyde 
     para-chlorobenzaldehyde 
     cinnamic aldehyde 
     diisobutyl ketone 
     ethylacetoacetate 
     ethyl amyl ketone 
     camphor 
     para-hydroxybenzaldehyde 
     2-carboxybenzaldehyde 
     4-carboxybenzaldehyde 
     salicylaldehyde 
     octyl aldehyde 
     decyl aldehyde 
     p-methoxybenzaldehyde 
     p-aminobenzaldehyde 
     phenylacetaldehyde 
     acetoacetic acid 
     2,5-dimethoxybenzaldehyde 
     1-naphthyl aldehyde 
     terephthaldehyde 
     Representative but non-exhaustive examples of amides which can be alkoxylated according to the instant invention are: 
     formamide 
     benzamide 
     acetanilide 
     salicylamide 
     acetoacetanilide 
     ortho-acetoacetotoluidide 
     acrylamide 
     N,N-diethyltoluamide 
     N,N-dimethylacetamide 
     N,N-dimethylformamide 
     phthalimide 
     octylamide 
     decylamide 
     laurylamide 
     stearylamide 
     N,N-dimethylollaurylamide 
     N,N-dimethylacrylamide 
     para-chlorobenzamide 
     para-methoxybenzamide 
     para-aminobenzamide 
     para-hydroxybenzamide 
     ortho-nitrobenzamide 
     N-acetyl-para-aminophenol 
     2-chloroacetamide 
     oxamide 
     N,N-methylene-bis-acrylamide 
     Representative but non-exhaustive examples of amines which can be alkoxylated according to the present invention are: 
     aniline 
     benzylamine 
     hexadecylamine 
     triphenylamine 
     aminoacetic acid 
     anthranilic acid 
     cyclohexylamine 
     tert-octylamine 
     ortho-phenylenediamine 
     meta-phenylenediamine 
     para-phenylenediamine 
     N-acetyl-para-aminophenol 
     2-amino-4-chlorophenol 
     2-amino-2-ethyl-1,3-propanediol 
     ortho-aminophenol 
     para-aminophenol 
     para-aminosalicylic acid 
     benzyl-N,N-dimethylamine 
     tert-butylamine 
     2-chloro-4-aminotoluene 
     6-chloro-2-aminotoluene 
     meta-chloroaniline 
     ortho-chloroaniline 
     para-chloroaniline 
     4-chloro-2-nitroaniline 
     cyclohexylamine 
     dibutylamine 
     2,5-dichloroaniline 
     3,4-dichloroaniline 
     dicyclohexylamine 
     diethanolamine 
     N,N-diethylethanolamine 
     N,N-diethyl-meta-toluidine 
     N,N-diethylaniline 
     diethylenetriamine 
     diisopropanolamine 
     N,N-dimethylethanolamine 
     N,N-dimethylaniline 
     2,4-dinitroaniline 
     diphenylamine 
     ethyl-para-aminobenzoate 
     N-ethylethanolamine 
     N-ethyl-1-naphthylamine 
     N-ethyl-ortho-toluidine 
     N-ethylaniline 
     ethylenediamine 
     hexamethylenetetraamine 
     2,4-lutidine 
     N-methylaniline 
     methyl anthranilate 
     p,p&#39;-diaminodiphenyl methane 
     ortho-nitroaniline 
     para-nitroaniline 
     tert-octylamine 
     piperazine 
     ethanolamine 
     isopropanolamine 
     ortho-toluidine 
     para-toluidine 
     2,4-tolyenediamine 
     triethanolamine 
     tributylamine 
     triisopropanolamine 
     2,4-dimethylxylidine 
     para-methoxyaniline 
     nitrilotriacetic acid 
     N-phenyl-1-naphthylamine 
     Representative but non-exhaustive examples of organic acids which can be alkoxylated according to the present invention are: 
     formic acid 
     acetic acid 
     valeric acid 
     heptanoic acid 
     2-ethylhexanoic acid 
     lauric acid 
     stearic acid 
     oleic acid 
     tall oil acids 
     hydrogenated tall oil acids 
     benzoic acid 
     salicyclic acid 
     adipic acid 
     azelaic acid 
     fumaric acid 
     citric acid 
     acrylic acid 
     aminoacetic acid 
     para-aminosalicylic acid 
     anthranilic acid 
     butyric acid 
     propionic acid 
     ricinoleic acid 
     chloroacetic acid 
     ortho-chlorobenzoic acid 
     2,4-dichlorophenoxyacetic acid 
     tert-decanoic acid 
     para-aminobenzoic acid 
     abietic acid 
     itaconic acid 
     lactic acid 
     glycolic acid 
     malic acid 
     maleic acid 
     cinnamic acid 
     para-hydroxybenzoic acid 
     methacrylic acid 
     oxalic acid 
     myristic acid 
     palmitic acid 
     tert-pentanoic acid 
     phenylacetic acid 
     mandelic acid 
     sebacic acid 
     tallow fatty acids 
     hydrogenated tallow fatty acids 
     tartaric acid 
     trichloroacetic acid 
     2,4,5-trichlorophenoxyacetic acid 
     undecylenic acid 
     crotonic acid 
     pelargonic acid 
     acetoacetic acid 
     para-nitrobenzoic acid 
     ascorbic acid 
     nitrilotriacetic acid 
     naphthenic acids 
     1-naphthoic acid 
     trimellitic acid 
     Representative but non-exhaustive examples of various phenols which can be alkoxylated according to the present invention are 
     phenol 
     ortho-cresol 
     meta-cresol 
     para-cresol 
     2,4-dimethylphenol 
     2,5-dimethylphenol 
     2,6-dimethylphenol 
     ortho-chlorophenol 
     meta-chlorophenol 
     para-chlorophenol 
     para-nitrophenol 
     para-methoxyphenol 
     salicylic acid 
     meta-hydroxyacetophenone 
     para-aminophenol 
     ortho-phenylphenol 
     nonylphenol 
     octylphenol 
     t-butyl-para-cresol 
     hydroquinone 
     catechol 
     resorcinol 
     pyrogallol 
     1-naphthol 
     2-naphthol 
     4,4&#39;-isopropylidenediphenol (bisphenol A) 
     methyl salicylate 
     benzyl salicylate 
     4-chloro-2-nitrophenol 
     para-t-butylphenol 
     2,4-di-t-amylphenol 
     2,4-dinitrophenol 
     para-hydroxybenzoic acid 
     8-hydroxyquinoline 
     methyl para-hydroxybenzoate 
     2-nitro-para-cresol 
     ortho-nitrophenol 
     para-phenylphenol 
     phenyl salicylate 
     salicylaldehyde 
     p-hydroxy benzaldehyde 
     2-amino-4-chlorophenol 
     ortho-aminophenol 
     salicylamide 
    
    
     The invention is more concretely described with reference to the examples below wherein all parts and percentages are by weight unless otherwise specified. The examples are provided to illustrate the instant invention and not to limit it. 
     EXAMPLE 1 
     A catalyst was prepared in two components. The first component prepared by reacting 10 grams (g) of BF 3  with 100 grams of alcohol containing from 12 to 14 carbon atoms (ALFOL 1214, trademark of and sold by Conoco Inc.) The second component was prepared by introducing 60 cubic centimeters (cc) of 0.593M aluminum triethyl in hexane into 100 gram 12 to 14 alcohol. Hexane was subsequently removed by rotary evaporation. Both the first component (0.0175 gram) and in the second component (5.7 gram) were introduced into a stainless steel reactor together with 120 grams of 12 to 14 carbon atom alcohol. After purging with nitrogen at 400 cc per minute for 30 minutes, an alkoxylation was carried out at 170° C. and 40 psig ethylene oxide partial pressure, which was maintained throughout the reaction. Under these conditions, 1.22 moles of ethylene oxide (EO) per mole of alcohol was introduced in 130 minutes. Residual free alcohol in the product was 13.7 weight percent. In contrast, the ethoxylated product produced by BF 3  catalyst at the same EO/alcohol mole ratio yielded free alcohol levels of 24%. 
     EXAMPLE 2 
     An experiment was carried out exactly as described in Example 1 except that the catalyst was made up of 3.0 grams of the first component and 11.3 grams of the second component. 2.22 moles of EO per mole of alcohol was introduced in 67 minutes. Free alcohol content was 0.60%. A similar experiment carried out using only BF 3  catalyst rather than the duel components of the present invention free alcohol content was 8.0%. 
     EXAMPLE 3 
     An alcohol with 12 to 14 carbon atoms (ALFOL 1214, 300 g) was ethoxylated as in Example 1, with 2.0 g SiF 4  and 10 cc of 0.593M triethylaluminum in hexane as a catalyst mixture. The product after 145 minutes of reaction contained 2.68 mol EO per mol alcohol. The ethylene oxide distribution obtained is compared with that obtained with BF 3  catalyst in table 1. 
     
                       TABLE 1                                                     
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          W % Adduct                                                      
Cat.        0      1      2    3    4    5    6                           
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SiF.sub.4 /(C.sub.2 H.sub.5).sub.3 Al                                     
            1.2    14.0   25.7 27.6 18.5 8.7  3.2                         
BF.sub.3    5.1    13.8   21.6 22.5 17.4 10.7 5.4                         
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     The data clearly shows SiF 4  /(C 2  H 5 ) 3  M produces an adduct peak much more sharply defined than BF 3  alone. 
     EXAMPLE 4 
     An experiment was performed as in Example 1 with 2.0 g BF 3  etherate and 10 cc of 0.593M triethylaluminum in hexane. The product contained 3.17 mol EO per mol alcohol. The EO distribution of this product was compared with that obtained with BF 3  etherate catalyst in table 2. 
     
                       TABLE 2                                                     
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         W % Adduct                                                       
Cat.       0      1     2     3    4     5    6                           
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BF.sub.3 etherate/                                                        
           0.3    8.4   19.6  26.5 22.3  13.3 6.4                         
(C.sub.2 H.sub.5).sub.3 Al                                                
BF.sub.3 etherate                                                         
           3.1    9.5   17.4  21.3 19.3  13.9 8.3                         
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     The data clearly shows that BF 3  etherate/(C 2  H 5 ) 3  Al produces an adduct peak much more sharply defined than BF 3  etherate alone. 
     EXAMPLE 5 
     A series of reactions was carried out to determine the effect of metal alkoxide addition to BF 3  as an alkoxylation catalyst. Alcohols of various molecular weight were ethoxylated. (ALFOL 1412 molecular weight 205.5; ALFOL 6 molecular weight 1033, a six carbon atom alcohol and ALFOL 610 molecular weight 134.3/, a six to ten carbon atom alcohol, all trademarks of and sold by Conoco Inc.). All reactions were carried out in the same fashion as the following specific reaction. 
     Gaseous BF 3  (10 g) was added to 100 g of six carbon atom alcohol for ease of handling small amount of BF 3 . Ten grams of this mixture was combined with 3.8 g aluminum alkoxide containing from 2 to 22 carbon atoms in each alkoxide group, and this combination was added to 100 g of a six carbon atom alcohol (ALFOL 6) to form a reaction mixture. 
     After purging for 30 minutes at 100° C. with N 2  (400 cc/min.), the mixture was heated to 170° C., and ethylene oxide was charged to give total pressure of 35 psig. The ethoxylation was performed at this constant pressure for 103 minutes. The product containing 2.67 moles ethylene oxide per mole alcohol. Table 3 shows that the distribution (determined by high pressure liquid chromatography) is very much more peaked than that obtained with BF 3  catalyst: 
     
                       TABLE 3                                                     
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              Weight %, Adduct                                            
                BF.sub.3 /                                                
Moles EO        Alkoxide BF.sub.3                                         
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0               0.83     3.8                                              
1               10.8     12.0                                             
2               26.3     20.7                                             
3               29.3     22.9                                             
4               19.8     18.5                                             
5               9.1      11.8                                             
6               3.2      6.1                                              
7               0.7      2.7                                              
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     Further experiments were repeated using various alcohols. Similar adduct distributions were obtained. The effect of catalyst type on residual unreacted free alcohols is shown in table 4, where BF 3  and NaOH catalysts were compared to BF 3  /alkoxide catalysts. 
     
                       TABLE 4                                                     
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CATALYST EFFECT ON RESIDUAL FREE ALCOHOLS                                 
        Mol EO/ BF.sub.3 /                                                
                         Free Alcohol, Weight %                           
Alcohol   Mol ROH   Alkoxide BF.sub.3                                     
                                    NaOH                                  
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1412      2.91      0.56     4.0    17.4                                  
1412      2.20      2.1      8.5    24.2                                  
1412      1.31      11.4     22.2   38.5                                  
1412      1.37      10.0     20.8   37.2                                  
6         2.78      0.71     3.4    13.5                                  
6         2.67      0.83     3.8    14.2                                  
6         2.96      0.48     2.8    12.3                                  
6         2.01      2.4      8.0    20.5                                  
6         1.04      17.5     25.4   38.1                                  
610       1.72      4.4      12.4   27.0                                  
610       2.84      0.54     3.6    14.5                                  
6.0       2.08      2.3      8.3    22.0                                  
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     Higher peaking of the distribution of EO in the adducts appears to be directly proportional to the decreased level of unreacted alcohols. 
     COMPARATIVE EXAMPLE 6 
     Alkoxylation of an alcohol containing from 12 to 14 carbon atoms was attempted using an aluminum alkoxide catalyst under the conditions of Example 1. No alkoxylation occurred. 
     While certain embodiments and details have been shown for the purpose of illustrating this invention, it will be apparent to those skilled in this art that various changes and modifications may be made herein without departing from the spirit or scope of the invention.