Abstract:
Glycerine is difficult to separate from bis(hydroxymethyl)tetrahydrofuran by conventional distillation or rectification because of the proximity of their boiling points. Glycerine can be readily separated from bis(hydroxymethyl)tetrahydrofuran by azeotropic distillation. Effective agents are m-xylene, beta-pinene and dicyclopentadiene.

Description:
FIELD OF THE INVENTION 
     This invention relates to a method for separating glycerine from bis(hydroxymethyl)tetrahydrofuran (BHMTHF) using certain organic liquids as the agent in azeotropic distillation. 
     DESCRIPTION OF PRIOR ART 
     Azeotropic distillation is the method of separating close boiling compounds or azotropes from each other by carrying out the distillation in a multiplate rectification column in the presence of an added liquid, said liquid forming an azeotrope with one orb orb of the compounds to be separated. Its presence on each plate of the rectification column alters the relative volatility in a direction to make the separation on each plate greater and thus require either fewer plates to effect the same separation or make possible a greater degree of separation with the same number of plates. The azeotrope forming agent is introduced with the feed to a continuous column. The azeotrope forming agent and the more volatile component are taken off as overhead product and the less volatile component comes off as bottoms product. The usual methods of separating theazeotrope former from the more volatile component are cooling and phase separation or solvent extraction. 
     The usual method of evaluating theeffectiveness of azeotropic distillation agents is the change in relative volatility of the compounds to be separated. Table 1 shows the degree of separation or purity obtainable by theoretical plates at several relative volatilities. Table 1 shows that a relative volatility of at least 1.2 is required to get an effective separation by rectification. 
     
                       TABLE 1______________________________________Effect of Relative Volatilityon Theoretical Stage Requirements.Separation Purity,       Relative VolatilityBoth Products       1.02   1.1    1.2 1.3  1.4 1.5 2.0 3.0(Mole Fraction)       Theoretical Stages at Total Reflux______________________________________0.999       697    144    75  52   40  33  19  120.995       534    110    57  39   30  25  14  90.990       463    95     49  34   26  22  12  70.98        392    81     42  29   22  18  10  60.95        296    61     31  21   16  14   8  40.90        221    45     23  16   12  10   5  3______________________________________ 
    
     There are a number of commercial processes which produce a complex mixture of glycerine, B.P.=290° C. and glycols. One of the glycols often present is bis(hydroxymethyl)tetrahydrofuran, B.P.=265° C. The relative volatility between these two is 1.09 which makes it very difficult to separate them by conventional rectification. Azeotropic distillation would be an attractive method of effecting the separation of glycerine from bis(hydroxymethyl)tetrahydrofuran (BHMTHF) if agents can be found that (1) will create a large apparent relative volatility between glycerine and BHMTHF and (2) are easy to recover from glycerine. Table 2 shows the relative volatility required to obtain 99% purity. With no agent, the relative volatility is 1.09 and 144 actual plates are required. With an agent giving a relative volatility of 2.0, only 19 actual plates are required. 
     
                       TABLE 2______________________________________Theoretical and Actual Plates Required vs. RelativeVolatility for Glycerine-BHMTHF SeparationRelative  Theoretical Plates Required                    Actual Plates RequiredVolatility  At Total Reflux, 99% Purity                    75% Efficiency______________________________________1.0.sup.9  108                14.sup.41.7    18                242.0    14                19______________________________________ 
    
     OBJECTIVE OF THE INVENTION 
     The object of this invention is to provide a process or method of azeotropic distillation that will enhance the relative volatility of glycerine from BHMTHF in their separation in a rectification column. It is a further object of this invention to identify organic compounds which in addition to the above constraints, are stable, can be separated from glycerine and recycled to the azeotrope column with little decomposition. 
     SUMMARY OF THE INVENTION 
     The objects of this invention are to provide a process for separating glycerine from bis(hydroxymethyl)tetrahydrofuran which entails the use of certain organic compounds as the agent in azeotropic distillation. 
     DETAILED DESCRIPTION OF THE INVENTION 
     I have discovered that certain organic compounds will greatly improve the relative volatility of glycerinelto bis(hydroxymethyl)tetrahydrofuran and permit the separation of glycerine from BHMTHF by rectification when employed as the agent in azeotropic distillation. Table 3 lists the compounds that I have found to be effective. They are benzyl benzoate, ethyl salicylate, 3-carene, ethyl benzene, o-xylene, m-xylene, p-xylene, diisopropyl benzene, 2,3,4-trimethyl pentane, terpinolene, limonene, pyridine, carane, p-mentha-1,5-diene, alpha-terpinene, decane, dodecane, decalin, tetralin, cyclohexane, 1-octene, heptane, hexane, isobutyl acetate, beta-pinene and dicyclopentadiene. 
     
                       TABLE 3______________________________________Effective Azeotropic Distillation Agents For SeparatingGlycerine From bis(Hydroxymethyl) tetrahydrofuran (BHMTHF)              RelativeCompounds          Volatility______________________________________None               1.09Benzyl benzoate    2.0Ethyl salicylate   1.83-Carene           1.6Ethyl benzene      2.0o-Xylene           1.9m-Xylene           1.71**p-Xylene           1.2Diisopropyl benzene              2.0*2,3,4-Trimethyl pentane              2.0*Terpinolene        2.0Limonene           2.0Pyridine           2.0*Carane             2.0p-Mentha-1,5-diene 2.0alpha-Terpinene    2.0Decane             2.0Dodecane           2.0***Decalin            2.0Tetralin           1.5Cyclohexane        1.81-Octene           2.0Heptane            2.0*Hexane             2.0*Isobutyl acetate   1.3*beta-Pinene        1.7**Dicyclopentadiene  1.6______________________________________ *Very little glycerine in the azeotrope **Data from rectification column ***Brings BHMTHF out as overhead product 
    
     THE USEFULNESS OF THE INVENTION 
     The usefulness or utility of this invention can be demonstrated by referring to the data presented in Tables 2 and 3. All of the successful agents show that glycerine can be separated from BHMTHF by means of azeotropic distillation in a rectification column and that the ease of separation as measured by relative volatility is considerable. 
    
    
     WORKING EXAMPLES 
     Example 1 
     Thirty-two grams of glycerine, 8 grams of BHMTHF and 40 grams of dicyclopentadiene were charged to a vapor-liquid equilibrium still and refluxed for four hours. Analysis indicated a vapor composition of 84.1% glycerine, 15.9% BHMTHF; a liquid composition of 76.2% glycerine, 23.8% BHMTHF. This is a relative volatility of 1.65. 
     Example 2 
     Seventy-five grams of glycerine, 25 grams of BHMTHF and 140 grams of m-xylene were placed in the stillpot of a 5.6 theoretical plate glass perforated plate rectification column and refluxed for nine hours. The overhead composition was 97.6% glycerine, 2.4% BHMTHF; the bottoms composition was 66.9% glycerine, 33.1 % BHMTHF. This is a relative volatility of 1.71. 
     Example 3 
     Seventy-five grams of glycerine, 25 grams of BHMTHF and 140 grams of beta-pinene were placed in the stillpot of a 5.6 theoretical plate glass perforated plate rectification column refluxed for nine hours. The overhead composition was 95.2% glycerine, 4.8% BHMTHF; the bottoms composition was 50.2% glycerine, 49.8% BHMTHF. This is a relative volatility of 1.7. 
     Example 4 
     Thirty-two grams of glycerine, 8 grams of BHMTHF and 40 grams of dodecane were charged to a vapor-liquid equilibrium still and refluxed for four hours. Analysis indicated a vapor composition of 39.1% glycerine, 60.9% BHMTHF; a liquid comoosition of 63.7% glycerine, 36.3% BHMTHF. This is a relative volatility of BHMTHF to glycerine of 2.7.