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372    Cha pte r  T h i r tee n

               other processes. However, the process is expensive because solvent
               cannot be recovered completely.
               Oil Recovery: A Novel Azeotropic Mixture for Extracting Solvents from Edible
               Oils  Edible oil extracted by a conventional mechanical press bears
               many impurities such as free fatty acids, colored and other gummy
               materials, which are known to be detrimental to oil flavor and stabil-
                  2
               ity.  Hexane is generally used as a solvent to extract oil, but a question
                                 3
                                                           2
               arises about its safety  due to the presence of solvent  in the oil as well
               as solvent vapor, which is a hazardous air pollutant. Ethanol, metha-
               nol, and acetone have been recommended as solvents for for extract-
               ing vegetable oils. Nag et al. carried out oil extraction from flax and
                                       4
               bahera seeds with isopropyl alcohol, ethanol, and ethyl acetate and
               have reached the following conclusions:
                   1.  Isopropyl alcohol, ethanol, and ethyl acetate are equally effec-
                      tive for extracting oil compared with n-hexane (Table 13.1).
                    2.  The aqueous solvent and the respective azeotropes are also
                      effective, but an added advantage of a higher content of aque-
                      ous solvent in azeotrope solvent is that it reduces the amount
                      of organic solvent.
                    3.  The azeotrope solvent reduces organic gummy materials in
                      solvent-extracted oil.

                   The advantage of a higher aqueous content solvent is the lower
               amount of organic solvent required; however, more energy would be
               required to remove the water from the solvent. However, amendments
               to the U.S. Clean Air Act—1990, Lusas et al.  suggested for alternative
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               solvents to avoid the formation of hazardous air pollutants.


                                                Temperature (°C )
                Solvent                30   40  50  60  70  80   90  100
                n-Hexane               M
                Ethanol                4.4  21  41  74  M
                Isopropanol (IPA)      67   83  M
                Ethyl acetate          M
                Ethanol + water        2.5  12  25  40  55  65   M
                Isopropanol (IPA) + water  35  50  60  65  M
                Ethyl acetate + water  35   50  60  70  75  M

               IPA = isopropyl alcohol; M = miscible.
               TABLE 13.1  The Solubility of Oils in Different Absolute Solvents and
               Mixture Solvents at Different Temperatures (°C)
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