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374                              Advances in Eco-Fuels for a Sustainable Environment


          Table 13.8 ANOVA table for CCD model

                                 Degree
                        Sum of   of       Mean
                                                          Prop>F
          Source        squares  freedom  square  F value
          Model         1116.36  20        55.82   45.75  <0.0001    Significant
          A-Temperature  154.97   1       154.94  127.03  <0.0001    Significant
          B-Time         76.88    1        76.88   63.02  <0.0001    Significant
          C-Molar ratio  243.13   1       243.13  199.29  <0.0001    Significant
          D-Catalyst      9.18    1        9.18     7.52   0.0191    Significant
          concentration
          E-Speed        31.44    1        31.44   26.5    0.0003    Significant
          AB             33.66    1        33.66   27.59   0.0003    Significant
          AC             11.66    1        11.66    9.57   0.0102    Significant
          AD              0.90    1        0.90     0.74   0.4092    Not
                                                                     Significant
          AE              6.37    1        6.37     5.22   0.0431    Significant
          BC              6.16    1        6.16     5.05   0.0461    Significant
          BD             36.00    1        36.00   29.51   0.0002    Significant
          BE              0.16    1        0.16     0.13   0.7220    Not
                                                                     Significant
          CD             16.71    1        16.71   13.70   0.0035    Significant
          CE             146.40   1       146.40  120.01  <0.0001    Significant
          DE             35.44    1        35.44   29.05   0.0002    Significant
          A2              0.018   1        0.018    0.015  0.9045    Not
                                                                     Significant
          B2             27.77    1        27.77   22.76   0.0006    Significant
          C2              9.96    1        9.96     8.16   0.0156    Significant
          D2             20.41    1        20.41   16.73   0.0018    Significant
          E2              4.84    1        4.84     3.96   0.0719    Significant
          Lack of fit    12.56   10        1.26     1.46   0.5722    Not
                                                                     Significant
          Pure error      0.86    1        0.86



         speed but increased with an increase in stirrer speed. Increasing stirrer speed improved
         the volatility of alcohol, which acts as a medium in the transesterification reaction.
         Higher stirrer speed enhanced the mixing intensity of oil and alcohol, which resulted
         in maximum biodiesel yield as compared to lower stirrer speed [43].


         13.3.3 Performance, emission, and combustion characteristics
                  of biodiesel-diesel-alcohol blends
         Fig. 13.7 shows the brake thermal efficiency (BTE) with respect to fuel injection
         timing (FIT) and nozzle opening pressure (NOP) for a biodiesel-diesel-alcohol blend.
         Fig. 13.7 shows that BTE is increased with n increase in NOP from 200 to 500bar and
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