Page 201 - Biofuels Refining and Performance
P. 201

184   Chapter Six


           TABLE 6.2 Comparison of Biodiesel Production by Acid, Alkali, and Enzyme
               Acid-catalyzed       Base-catalyzed          Enzymatic
             transesterification  transesterification    Transesterification

           The glycerides and   The glycerides and alcohol   The alcohol needs to be
            alcohol need not be   must be substantially   anhydrous
            anhydrous           anhydrous
           Does not make a soap-  Soap formation taking   Does not make a soap-like
            like product        place during the reaction  product
           Easy to water wash   Water washing is difficult   Separation of the product is
            for product separation  due to soap emulsifier  very easy; product is obtained
                                                      only by filtration
           Recommended for any   Recommended for low   Recommended for any free-
            free-fatty acid content   free-fatty acid content of   fatty acid content of
            of vegetable oil    vegetable oil         vegetable oil
           Converts free fatty acid   Converts free fatty acid to   Converts free fatty acid to
            to ester            soap                  ester
           Product yield is high  Product yield is com-  Product yield depends on
                                paratively low        different types of enzymes
                                                      used; reaction is selective
           Is slower than alkali-  Is faster comparatively  Ezymatic reaction is slower
            catalyzed transesteri-                    than acid and alkali-
            fication                                  catalyzed reaction
           Percentage of conversion  Percentage of conversion   Percentage of conversion is
            is low              is high               high
           Under low water content  Water content in the   Under low water conditions,
            in reactants (oil or  reactant inhibits the  the hydrolysis reaction is
            alcohol),           reaction rate         reversible, i.e., the ester bond
            transesterification                       is  synthesized rather than
            reaction is not hindered                  hydrolyzed. Lipases break
                                                      down the triacylglycerols into
                                                      free fatty acids and glycerol
                                                      that exhibit maximum activity
                                                      at the oil–water interface
           Need high temperature  Reacts even at room   Conversion takes place at low
                                temperature           temperature




           heavy carbon deposits. But specific emissions and visible smoke char-
           acteristics of diesel fuel and esterified cottonseed oil were comparable.
             Ziejewski and Kaufman [55] conducted a long-term test using a 25–75%
           blend of alkali-refined sunflower oil and diesel fuel in a diesel engine, and
           compared the results with that of a baseline test on diesel fuel. Engine
           power output over the tested speed range was slightly higher for this blend.
           At 2300 rpm, the difference was 25%. At 1800 rpm, the gain in power was
           6%. The smoke level increased at a higher engine speed from 1 to 2.2 and
           decreased at a lower engine speed. Greater exhaust temperature was caused
           by a higher intake air temperature. The major problems experienced were:

           1. Abnormal carbon buildup in the injection nozzle tips.
           2. Injector needle sticking.
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