Abstract:
In accordance with the process of the present invention normally liquid, water-soluble poly(oxyethylene/oxypropylene) polyamine products are prepared using an initiator, which may contain oxyethylene groups. In a series of alkoxylation reaction steps the initiator is reacted with predetermined weight percentages of ethylene oxide and propylene oxide, said process comprising the steps of: 
     a. Charging a predetermined percentage of initiator to an alkoxylation reaction zone, 
     b. Alkoxylating said initiator therein with predetermined percentages of ethylene oxide and propylene oxide to provide an intermediate polyol, 
     c. Propoxylating said intermediate polyol with a predetermined percentage of propylene oxide to provide a normally liquid, water-soluble precursor polyol, and 
     d. Catalytically reductively aminating said precursor polyol in the presence of a reductive amination catalyst in a reaction zone under reductive amination conditions in the presence of ammonia and hydrogen to provide said water-soluble poly(oxyethylene/oxypropylene) polyamine product.

Description:
BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     This invention relates to modified normally liquid, water-soluble polyoxyalkylene polyamines and to a process by which they may be prepared. More particularly, this invention relates to normally liquid, water-soluble polyoxyethylene polyamines modified by the inclusion of oxypropylene groups and to a special process to be used in preparing the modified polyamines. 
     Still more particularly, this invention is directed to normally liquid, water-soluble poly(oxyethylene/oxypropylene)polyamine products having an average molecular weight of about 1000 to about 8000 and a functionality of about 2 to about 4 which are prepared by adding predetermined amounts of ethylene oxide and propylene oxide to an alkoxylation susceptible polyhydric alcohol initiator to form an intermediate which is then propoxylated to form a precursor polyol which, in turn, is reductively aminated in the presence of a hydrogenation/dehydrogenation catalyst to provide the desired normally liquid, water-soluble poly(oxyethylene/oxypropylene) polyamine. 
     The poly(oxyethylene/oxypropylene) polyamine may be used to form an aqueous solution containing from about 1 to about 50 wt.% of the polyamine. The aqueous solution of the polyamine may be used as such, e.g., as a major component of a functional fluid such as a hydraulic fluid, or as a feedstock for a further chemical processing step. 
     The poly(oxyethylene/oxypropylene) precursor polyols of the present invention are also water soluble liquids at ambient temperatures and may be used as feedstocks for the preparation of the poly(oxyethylene/oxypropylene) polyamines of the present invention or may be used to prepare aqueous solutions of the poly(oxyethylene/oxypropylene) polyol containing from about 1 to about 50 wt.% of the polyol. 
     2. Prior Art 
     Yeakey U.S. Pat. No. 3,654,370 discloses a process for the preparation of polyoxyalkylene polyamines by the reaction of a polyoxyalkylene polyol feedstock with ammonia in the presence of hydrogen under reductive amination conditions to provide the corresponding polyoxyalkylene polyamine. 
     Lee et al. U.S. Pat. No. 3,236,895 discloses a process for producing polyoxyalkylene polyamines such as polyoxyalkylene diamines by reacting a polyoxyalkylene diol with ammonia in the presence of hydrogen. 
     British Patent No. 934,636 also discloses the preparation of oxyalkylene amines by reacting polyoxyalkylene glycol ethers with ammonia using a hydrogenation/dehydrogenation catalyst. 
     Boettger et al. U.S. Pat. No. 4,014,933 discloses the reaction of alcohols with ammonia at elevated temperatures and pressures in the presence of hydrogen and a hydrogenation catalyst. 
     Nickel/copper/chromia catalysts of the type preferred by Yeakey are disclosed in Moss U. S. Patent No. 3,152,998. 
     SUMMARY OF THE INVENTION 
     1. Background of the Invention 
     It is known that polyoxyethylene polyols have good water solubility characteristics. Therefore, it has been proposed in the past to ethoxylate alkoxylation susceptible initiator alcohols containing 2 to 4 hydroxyl groups and to reductively aminate the resultant polyoxyethylene polyol in order to provide water soluble products useful as epoxy curing agents, and also useful in the preparation of polyurea RIM elastomers, polyamides and functional fluids. For many applications it is desirable to use a comparatively high molecular weight material having a molecular weight of about 1000 to about 8000. However, typical polyoxyethylene polyols within this molecular weight range are normally solid materials which are processed with difficulty. Thus, unless special precautions are taken during the processing of the polyol, it can solidify or otherwise plug or interfere with the processing operations being conducted. 
     Another class of raw materials that are frequently prepared are polyoxypropylene polyols. The polyoxypropylene polyols are characterized, in general, by water insolubility and therefore their use is not favored in situations wherein water solubility is a desired characteristic. 
     It has been surprisingly discovered in accordance with the present invention that polyoxyethylene polyamines which are normally liquid at ambient temperatures of about 30° C., such as temperatures of 30°-35° C. and which have good watersolubility characteristics can be prepared by incorporating from about 20 to about 40 wt.% of propylene oxide into the polyoxyethylene polyol molecule in a special manner. 
     2. General Description 
     In accordance with the present invention normally liquid, water-soluble poly(oxyethylene/oxypropylene) polyamine products having an average molecular weight of about 1000 to about 8000 and a functionality of about 2 to 4 are provided. The poly(oxyethylene/oxypropylene) polyol precursors, used as feedstocks for the reductive amination step are also characterized by being normally liquid and watersoluble. 
     In order to obtain polyol precursors and polyamine products having the desired water solubility characteristics, it is necessary that a particular processing sequence be followed. 
     In accordance with the process of the present invention an initiator, which may contain oxyethylene groups, ethylene oxide and propylene oxide are charged to a reaction zone in a series of alkoxylation reaction steps with predetermined weight percentages of initiator, ethylene oxide and/or propylene oxide being charged for each step, based on the total weight of all of the initiator ethylene oxide and propylene oxide charged during all of the steps of the process. The alkoxylation reaction steps are conducted under basic alkoxylation conditions under substantially anhydrous conditions. 
     The initiator comprises an oxyalkylation susceptible polyhydric alcohol having 2 to 4 hydroxyl groups and a molecular weight of about 200 to about 1000 which, optionally, will comprise oxyethylene groups and will constitute about 10 to about 60% of the total molecular weight of the water soluble poly(oxyethylene/oxypropylene) polyamine product. 
     The processing sequence comprises the steps of: 
     a. Charging a predetermined percentage of the initiator to an alkoxylation reaction zone, 
     b. Alkoxylating said initiator in said alkoxylation reaction zone with predetermined percentages of ethylene oxide and propylene oxide to provide an intermediate polyol, 
     c. Propoxylating the intermediate polyol in the alkoxylation reaction zone with a predetermined percentage of propylene oxide to provide a precursor polyol, and 
     d. Catalytically reductively aminating the precursor polyol in the presence of a reductive amination catalyst in a reaction zone under reductive amination conditions in the presence of ammonia and hydrogen to provide the desired water soluble poly(oxyethylene/oxypropylene) polyamine product. 
     The predetermined percentages, when the initiator contains all oxyethylene groups are in the ranges of: 
     
         ______________________________________  Minimum Weight                Maximum Weight  Percent of    Percent of  Initiator +       Initiator +  Ethylene          Propylene Ethylene  Propylene  Oxide   Oxide     Oxide     Oxide______________________________________Intermediate    60        15        80      25Precursor    60        20        80      40Polyol______________________________________ 
    
     When the initiator does not contain oxyethylene groups, the predetermined percentages are in the ranges of: 
     
         ______________________________________  Minimum Weight                Maximum Weight  Percent of    Percent of  Initiator +       Initiator +  Ethylene          Propylene Ethylene  Propylene  Oxide   Oxide     Oxide     Oxide______________________________________Initiator plus    80        15        60      25IntermediatePrecursor    80        20        60      40Polyol______________________________________ 
    
     In alkoxylating the initiator in order to prepare the intermediate polyol, the ethylene oxide and propylene oxide may be premixed before the alkoxylation to form a heteropolymer or the ethylene oxide and propylene oxide may be separately added to the alkoxylation reaction zone. 
     A preferred class of polyamines of the present invention are prepared by alkoxylating a polyoxyethylene glycol initiator having an average molecular weight of about 200 to about 1000 with a predetermined amount of a mixture of ethylene oxide and propylene oxide to provide a poly(oxyethylene/oxypropylene) hetero-polymer polyol intermediate which, in turn, is propoxylated to provide a poly(oxyethylene/oxypropylene) diol precursor for the reductive amination step. 
     DETAILED DESCRIPTION 
     As indicated earlier, the starting materials for the present invention are an alkoxylation susceptible polyhydric alcohol containing 2 to 4 hydroxyl groups having an average molecular weight  of about 200 to about 1000 and propylene oxide and ethylene oxide. 
     Hydrogen and ammonia are used in the processing sequence and a hydrogenation/dehydrogenation catalyst is used for the reductive amination step. 
     THE INITIATOR 
     The initiators to be used in accordance with the present invention are oxyalkylation susceptible polyhydric alcohols containing 2 to 4 hydroxyl groups, having an average molecular weight of about 200 to about 1000. Examples of such initiators include ethylene glycol, diethylene glycol, triethylene glycol, poly(oxyethylene) glycols, propylene glycol, dipropylene glycol, polypropylene glycol, 1,2,6-hexane triol, trimethylolethane, trimethylolpropane, glycerine, pentaerythritol and alpha methyl glucoside. 
     A preferred class of initiators are the polyoxyethylene glycols having a molecular weight of about 200 to about 1000, such as a molecular weight of about 600. 
     THE INTERMEDIATE POLYOL 
     In accordance with the present invention, the initiator is reacted with a predetermined amount of ethylene oxide and propylene oxide in an alkoxylation reaction zone in order to provide an intermediate polyol. 
     The alkoxylation is conducted in a conventional fashion, for example, by adding the propylene oxide and ethylene oxide to a kettle containing the initiator. The alkoxylation is conducted under basic conditions. 
     Suitable alkoxylation conditions include, for example, the use of temperatures within the range of about 75° to about 150° C. and pressures within the range of about 10 to about 100 psig. A base, such as an alkali metal or alkaline earth metal catalyst should be present in order to promote the alkoxylation and is used in an amount of about 0.25 to about 5.0 wt. %, based on the weight of the initiator (see, for example, Cuscurida et al. U.S. Pat. No. 3,535,307 and U.S. Pat. No. 4,316,991). 
     In the preparation of the intermediate polyol, the propylene oxide and ethylene oxide are preferably added to the alkoxylation zone in admixture in order to provide an intermediate polyol which is a poly(oxyethylene/oxypropylene) heteropolymer polyol. However, if desired, the initiator may be reacted first with a predetermined amount of ethylene oxide and then with the predetermined amount of propylene oxide or, first with the predetermined amount of propylene oxide and then with the predetermined amount of ethylene oxide in order to provide block copolymer polyoxyethylene polyoxypropylene polyols. 
     THE PRECURSOR POLYOL 
     In accordance with the present invention an initiator is reacted with a mixture of propylene oxide and ethylene oxide containing predetermined amounts of ethylene oxide and propylene oxide, as described herein, to form an intermediate polyol which is capped with a predetermined amount of propylene oxide to provide a precursor polyol for use as a feedstock for the reductive amination step. 
     The predetermined weight percentages of ethylene oxide and propylene oxide to be used when the initiator contains oxyethylene groups is given in the following table: 
     
         ______________________________________  Minimum Weight                Maximum Weight  Percent of    Percent of  Initiator +       Initiator +  Ethylene          Propylene Ethylene  Propylene  Oxide   Oxide     Oxide     Oxide______________________________________Intermediate    60        15        80      25Precursor    60        20        80      40Polyol______________________________________ 
    
     Note from the table that the final precursor polyol will contain from about 60 to about 80 wt. % of oxyethylene groups and, correspondingly, from about 40 to about 20 wt. % of oxypropylene groups. It will also be noted from the table, under the column heading of &#34;Minimum Weight Percent of&#34;, that 15/20 wt. % or 75% of the predetermined weight percentage of propylene oxide was added to the intermediate polyol and, under the column heading of &#34;Maximum Weight Percent of&#34;, that 24/40 wt. %, or about 62.5% of the predetermined weight percentage of propylene oxide was added to the intermediate polyol. 
     It is not necessary that the initiator be an oxyethylene containing initiator and when the initiator does not contain oxyethylene groups, the percentages of ethylene oxide and propylene oxide to be used are given in the following table: 
     
         ______________________________________  Minimum Weight                Maximum Weight  Percent of    Percent of  Initiator +       Initiator +  Ethylene          Propylene Ethylene  Propylene  Oxide   Oxide     Oxide     Oxide______________________________________Initiator plus    80        15        60      25IntermediatePrecursor    80        20        60      40Polyol______________________________________ 
    
     REDUCTIVE AMINATION OF THE PRECURSOR POLYOL 
     The precursor polyol after being neutralized with any suitable acid or chemical adsorbent, such as for example, oxalic acid or magnesium silicate, and filtered for the removal of insoluble materials is charged to a reductive amination zone where it is brought into contact with a reductive amination catalyst, frequently referred to as a hydrogenation-dehydrogenation catalyst, in the presence of ammonia and hydrogen under reductive amination conditions. Such conditions may include, for example, a temperature from within the range of about 150° to about 275° C. and a pressure within the range of about 500 to about 5000 psig with temperatures within the range of about 180° to 240° C. and pressures within the range of about 1500 to about 3000 psig being preferred. 
     Any suitable hydrogenation catalyst may be used, such as a catalyst comprising one or more of the metals of group VIIIB of the Periodic Table, such as iron, cobalt, nickel, ruthenium, rhodium, palladium, platinum, mixed with one or more metals of group VIB of the Periodic Table such as chromium, molybdenum or tungsten. A promoter from group IB of the Periodic Table, such as copper, may also be included. As an example, a catalyst may be used comprising from about 60 to about 85 mole percent of nickel, about 14 to about 37 mole percent of copper and about 1 to about 5 mole percent of chromium (as chromia), such as a catalyst of the type disclosed in Moss U.S. Pat. No. 3,152,998. As another example, a catalyst of the type disclosed in Boettger et al. U.S. Pat. No. 4,014,933 may be used containing from about 70 to about 95 wt.% of a mixture of cobalt and nickel and from about 5 to about 30 wt.% of iron. As another example, a catalyst of the type disclosed in Habermann U.S. Pat. No. 4,152,353 may be used, such as a catalyst comprising nickel, copper and a third component which may be iron, zinc, zirconium or a mixture thereof, e.g., a catalyst containing from about 20 to about 49 wt.% of nickel, about 36 to about 79 wt.% of copper and about 1 to about 15 wt.% of iron, zinc, zirconium or a mixture thereof. 
     The reductive amination is preferably conducted on a continuous basis with the precursor polyol, ammonia and hydrogen being continuously charged to a reactor containing a fixed bed of catalyst and with the reaction product being continually withdrawn. 
     The reaction product is suitably depressured so as to recover excess hydrogen and ammonia for recycle and is then fractionated to remove byproduct water of reaction and to provide the desired poly(oxyethylene/oxypropylene) polyamine product. 
     In conducting the reductive amination, the reductive amination conditions to be utilized may suitably include the use of from about 4 to about 150 moles of ammonia per hydroxyl equivalent of feedstock. Hydrogen is preferably used in an amount ranging from about 0.5 to about 10 mole equivalents of hydrogen per hydroxyl equivalent of feedstock. The contact times within the reaction zone, when the reaction is conducted on a batch basis, may suitably be within the range of from about 0.1 to about 6 hours and more preferably from about 0.15 to about 2 hours. 
     When the reaction is conducted on a continuous basis using catalyst pellets, reaction times may suitably be from about 0.1 to about 2 grams of feedstock per hour per cubic centimeter of catalyst and, more preferably, from about 0.3 to about 1.6 grams of feedstock per hour per cubic centimeter of catalyst. 
     Also, the reductive amination may be conducted in the presence of about 1 to about 200 moles of ammonia per mole of percursor polyol and more preferably, from about 4 to about 130 moles of ammonia per mole of precursor polyol. From about 0.1 to about 50 moles of hydrogen per mole of precursor polyol may be employed and, more preferably, from about 1 to about 25 moles of hydrogen per mole of precursor polyol. 
     The molecular weight of the polyol is determined by the number of moles of epoxide that are reacted with the alcohol initiator. Since the addition is random, the final alkoxylation product will not be a pure compound but, rather, will be a mixture of poly(oxyethylene/oxypropylene) polyols. For example, if the precursor polyol has an average molecular weight of about 1000, it will actually be composed of a mixture of poly(oxyethylene/oxypropylene) polyols having molecular weights varying from about 800 to about 1200, the molecular weight distribution following a Gaussian distribution curve. As the molecular weight of the precursor polyol increases, the spread of the molecular weights will also increase. Thus, when the average molecular weight is about 3000, the deviation will be about ±400 molecular weight units so that most of the product will fall within the range of molecular weights ranging from about 2600 to about 3400. 
     As the molecular weight is still further increased, the percentage of deviation will increase still further. For example, a 5000 molecular weight poly(oxyethylene/oxypropylene) precursor polyol will have a molecular weight distribution of about ±1000 so that the actual molecular weight range will be from about 4000 to about 6000. Again, the molecular weight distribution will tend to follow a Gaussian distribution curve. 
    
    
     SPECIFIC EXAMPLES 
     The invention will be further illustrated by the following specific examples which are given by way of illustration and not as limitations on the scope of this invention. 
     EXAMPLE 1 
     Research Notebook 6158-27; Preparation of Polyoxyalkyleneamines Precursor Polyol 
     Into a ten-gallon kettle were charged 7 lb of a 600 m.w. polyethylene glycol (PEG 600) and 35.2g 45% aqueous potassium hydroxide. The reactor was then purged with prepurified nitrogen. Maintaining a nitrogen purge, the reactor was heated to 100° C. and stripped to a water content of less than 0.1%. A mixture of 12.4 lb propylene oxide (PO) and 54.9 lb of ethylene oxide (EO) was then reacted at 115°-120° C. at 50 psig. Approximately 7.0 hours were required for addition of the mixed oxides. The reaction mixture was then digested 1.7 hours to an equilibrium pressure. PO (8.3 lb) was then reacted at 120° C. and 50 psig over a 0.75 hour period. After digestion to an equilibrium pressure, the alkaline polyol was neutralized at 95° C. by stirring two hours with 141g magnesium silicate which was added as an aqueous slurry. Di-t-butyl p-cresol (37.6g) was added to stabilize the product. The neutralized product was then vacuum stripped to a minimum pressure, nitrogen stripped and filtered. The finished product had the following properties: 
     
         ______________________________________ Run no.                6158-27______________________________________PropertiesAcid no.; mg KOH/g      0.003Hydroxyl no. mg/KOH/g   17.6Water, wt. %            0.007Unsaturation, meq/g     0.032pH in 10:6 isopropanol-water                   8.2Color, Pt-Co            50Sodium, ppm             0.2Potassium, ppm          1.3Peroxide, ppm           2.0Viscosity, 100° F. cs                   2508PO/EO                   25.8/74.2Melting point, °C.                   33Water solubility        Yes______________________________________ 
    
     The product was a liquid at 30°-35° C. and readily dissolved in water at room temperature and was used to form a 33 wt.% solution in water. 
     The percentages of initiator, propylene oxide and ethylene oxide in the intermediate polyol and the precursor polyol were calculated as follows: 
     
         ______________________________________Component     Amount, lbs.______________________________________PEG 600       7Mixed PO      12.4Mixed EO      54.9cap PO        8.3______________________________________ 
    
     Percent EO in intermediate polyol equals ##EQU1## 
     Percent PO in intermediate polyol equals ##EQU2## 
     EXAMPLE 2 
     This example will illustrate the preparation of a prior art water soluble 5500 m.w. diol. 
     Into a 125-gallon kettle was charged 123 lbs of a 750 m.w. polyoxyethylene glycol which had an alkalinity of 5 mg KOH/g. The reactor was then purged with nitrogen and stripped while heating to 130° C. EO (770 lb) was then reacted at 125°-130° C. at 50 psig. The reaction mixture was circulated through an exchanger after the first 50 lb of EO had been added. Since the product freezes in the 50°-60° C. range it was necessary to maintain positive flow through the exchanger continuously and to keep the process lines heated. After digestion to an equilibrium pressure, the reactor was vented to a flare. PO (52 lb) was then reacted at 125°-130° C. and 50 psig. After digestion to an equilibrium pressure, the alkaline material was neutralized with 205g oxalic acid dihydrate to a pH of 7.5. An aqueous slurry of 181g magnesium silicate was then added to the product and digested an additional hour at 95°-100° C. Di-t-butyl p-cresol (53g) and Celite 545 filter aid (2 lb) were then added to the neutralized product. The product was then vacuum stripped to a minimum pressure at 110° C., nitrogen stripped, and filtered. The finished product had the following properties: 
     
         ______________________________________Acid no., mg KOH/g   0.03Hydroxyl no., mg KOH/g                20.4Water, wt. %         0.03pH in 10:6 isopropanol-water                6.0Sodium, ppm          2.3Potassium, ppm       0.7Melting point, °C.                48Water solubility     Yes______________________________________ 
    
     Although the product had good water solubility, it had an undesirably high melting point. 
     EXAMPLE 3 
     The polyether diol of Example 1 was reductively aminated in a 1250 ml reactor using the following reaction conditions: (See U.S. Pat. No. 3,654,370) 
     
         ______________________________________Polyol feed rate, lb/hr             0.5Ammonia feed rate, lb/hr             1.0Hydrogen feed rate, l/hr              25Temperature, °C.              201Reactor pressure, psig             2000Catalyst          Proprietary copper,             chromium, nickel______________________________________ 
    
     The ammonia, polyol, and hydrogen were fed into the reactor through heated feed lines. The product was collected at atmospheric pressure at 70° C. Crude product was then stripped on a rotary evaporator at 99-100 psig and 5 mm Hg. Properties of the stripped product were as follows: 
     
         ______________________________________Total acetylatables, meq/g               0.36Total amine, meq/g  0.27Primary amine, meq/g               0.26Melting point, °C.               20Water solubility    Yes______________________________________ 
    
     Reductive amination of the polyether diol of Example 2 yielded a product having the following properties: 
     
         ______________________________________Total acetylatables, meq/g               0.315Total amine, meq/g  0.27Primary amine, meq/g               0.26Melting point, °C               49Water solubility    Yes______________________________________ 
    
     EXAMPLE 4 
     This example will illustrate the preparation of a 2150 m.w. polyol of this invention. 
     Into a 10-gallon kettle were charged 20 lb of a 600 m.w. polyethylene glycol and 30g 45% aqueous potassium hydroxide. The reactor was then purged with prepurified nitrogen. Maintaining a nitrogen purge the reactor was heated to 100° C. The initiator was then dried to a water content of less than 0.1% by using vacuum and nitrogen stripping. A mixture of 13.4 lb PO and 26.6 lb EO was then reacted at 120°-125° C. at 50 psig. Approximately five hours was required for addition of the mixed oxides. After digestion to an equilibrium pressure, the polyol was capped by reaction with 6.6 lb PO at 120°-125° C. at 50 psig. After digestion to an equilibrium pressure, the alkaline product was neutralized at 95° C. by stirring two hours with 120g magnesium silicate which was added as an aqueous slurry. Di-t-butyl p-cresol (30.2g) was then added to stabilize the product. The neutralized product was then vacuum stripped to a minimum pressure, nitrogen stripped, and filtered. The finished product was a liquid at room temperature (77° F.) which had the following properties: 
     
         ______________________________________Acid no., mg KOH/g  0.003Hydroxyl no., mg KOH/g               52.2Water, wt. %        0.03Unsaturation, meq/g 0.005pH in 10:6 isopropanol-water               7.7Color, Pt--Co       45Sodium, ppm         0.2Potassium, ppm      0.2Peroxides, ppm      1.44Viscosity, °F., cs 77°         442100°         235PO/EO               29.5/70.5______________________________________ 
    
     The polyol of this Example 4 was used to make a 50 wt.% aqueous solution. 
     The percentages of initiator, propylene oxide and ethylene oxide in the intermediate polyol and the precursor polyol were calculated as follows: 
     
         ______________________________________Component     Amount, lbs.______________________________________PEG 600       20Mixed PO      13.4Mixed EO      26.6cap PO        6.6______________________________________ 
    
     Percent EO in intermediate polyol equals ##EQU3## 
     PO in intermediate polyol equals ##EQU4## 
     EXAMPLE 5 
     This example will illustrate the preparation of a prior art water soluble 2000 m.w. diol. 
     Into a 125-gallon kettle was charged 315 lb of a 700 m.w. polyethylene glycol which had an alkalinity of 5 mg KOH/g. The reactor was then purged with nitrogen and stripped while heating to 130° C. Ethylene oxide (494 lb) was then reacted at 125°-130° C. at 50 psig. The reaction mixture was circulated through an exchanger during EO addition. Since the product freezes in the 42°-45° C. range it was necessary to maintain positive flow through the exchanger continuously and to keep the process lines heated. After digestion to an equilibrium pressure, the reactor was vented to a flare. PO (91 lb) was then reacted at 125°-130° C. at 50 psig. After digestion to an equilibrium pressure, the alkaline material was neutralized with 635g oxalic acid dihydrate to a pH of 7.5 Di-t-butyl p=cresol (104g) and Celite (2 lb) were then added to the neutralized product. The product was then vacuum stripped to a minimum pressure, nitrogen stripped, and filtered. The finished product had the following properties: 
     
         ______________________________________Acid no., mg KOH/g  0.027Hydroxyl no., mg KOH/g               56.9Water, wt. %        0.2pH in 10:6 isopropanol-water               6.8Sodium, ppm         0.04Potassium, ppm      7.3Color, Pt--Co       &gt;50Melting point, °C.               43.95Water solubility    Yes______________________________________ 
    
     EXAMPLE 6 
     The polyol of Example 4 was reductively aminated using Ni-2715 catalyst. Best results were obtained at 200° C. and a total space velocity of 0.88 g/cc cat/hr. The resultant product was a liquid at room temperature. Its properties were as follows: 
     
         ______________________________________Total acetylatables, meq/g             0.95Total amine, meq/g             0.85Primary amine, meg/q             0.84Water, wt. %      0.01Viscosity, 77° F., cs             354Melting point, °C.             Liquid at room             temperatureWater solubility  Yes______________________________________ 
    
     Reductive amination of the prior art 2000 m.w. diol of Example 5 formed a liquid product which had the following properties: 
     
         ______________________________________Total acetylatables, meq/g               0.96Total amine, meq/g  0.90Primary amine, meg/q               0.87Melting point, °C.               40.5Water solubility    Yes______________________________________ 
    
     EXAMPLES 7 AND 8 
     Two additional water-soluble precursor polyols were prepared using a polyethylene glycol having an average molecular weight of 600 as an initiator. The procedure used was essentially that described in Example 1, the materials were used in the following reaction sequence: 
     Example 7--Polyoxyethylene glycol (600 m.w.) plus a mixture of 107 moles EO/18.3 moles PO plus 12.3 moles PO; 
     Example 8--Polyoxyethylene glycol initiator (average molecular weight 600) plus a mixture of 18.1 moles EO with 6.9 moles PO plus 3.4 moles PO. 
     Reaction charges, details of preparation and the properties of the diols are given in the following table. 
     
                       TABLE I______________________________________Water Soluble Precursor PolyolsRun no.           6197-3   6197-5   6197-15______________________________________ChargePEG-600, lb       7        7        20Potassium hydroxide, flaked, g.sup.a             17.6     17.6     15 Propylene oxide, lb       12.4   12.4   13.4             mixedEthylene oxide, lb        54.9   54.9   26.6Propylene oxide, lb             8.3      8.3      6.6Magnesol 30/40, g 141      141      120Di-t-butyl p-cresol, g             37.6     37.6     30.2Reaction DetailsOxide addition time, hr             5.8      5.4      5.5Temperature, °C.             105-110  105-110  105-110Pressure, psig    50       50       50PropertiesAcid no., mg KOH/g             0.002    0.003    0.003Hydroxyl no., mg KOH/g             18.2     17.3     52.2Water, wt. %      0.04     0.17     0.03Unsaturation, meq/g             0.025    0.033    0.005pH in 10:6 isopropanol-water             8.1      8.0      7.7Color, Pt-Co      100      75       45Sodium, ppm       0.2      0.2      0.2Potassium, ppm    0.2      0.2      0.2Peroxide, ppm     1.5      --       1.44Viscosity, 100° F., cs             2568     2146     235PO/EO ratio       24.9/75.1                      26.8/73.2                                29.5/70.5Melting point, °C.             33       32       liquid______________________________________ .sup.a Added as 45% aqueous solution, dried to water content of less than 0.1 before oxide addition. 
    
     The amination of polyol 6197-15 was accomplished using a 1250 ml tubular reactor filled with a nickel oxide-chromium oxide-copper oxide catalyst. The reactor was capped at 20° C. and 2000 psig. The feed rates into the reactor were: polyol 0.8  lb/hr, ammonia 1.6 lb/hr, and hydrogen 76 l/hr. The crude effluent was stripped at 100° C. and 10 mm Hg. The resultant have the following properties: 
     
         ______________________________________Total acetylatables, meg/g               0.95Total amine, meg/g  0.85Primary amine, meg/g               0.84pH                  12.9Water, wt. %        0.01Viscosity, 77° F., cs               354Flash point, PM cc, °F.               480Color, Pt--Co       20______________________________________