Question: please show coding in r thank you. Consider the surronta in a Perform a thorough residual analysis of these sa b. Identify the most appropriate
please show coding in r thank you.
Consider the surronta in a Perform a thorough residual analysis of these sa b. Identify the most appropriate transformation for these and repeat the residual analysis Roodes required to handwerstep by step guidelines this model 562 APPENCE TABLE (Cow S oodusere DSBOCHUM LABLE 19 Pressure Drop Data 214 414 RIS 214 414 0.34 04 04 034 04 034 034 lo RIS 214 4.14 RIS 2.14 4.14 0245 02379 0474 0.141 0234 0111 0.005 112 0.154 014 014 14 15 034 14 TUNO 2.14 4.14 RIS 2.14 0:34 0.14 4.14 RIS 263 044 04 034 09 0.514 0672 ON 0106 0506 . 2.14 4.14 R15 2.14 17.1 18.3 33.8 31.7 263 4.14 0.34 0.14 0.34 263 1.25 014 18.1 0.34 15.4 1-25 1.25 1.25 263 263 263 263 0.34 0.34 OS 0.737 0.651 0554 0745 0.682 0524 0.472 191 162 0.34 0.34 04 16.3 15.8 0.25 19.2 0.25 0.25 R4 101 101 101 101 101 101 101 101 101 0.25 014 Pertttt8888888ttttt 07 0,677 059 0.520 079 0.677 059 0523 0741 0617 04 0.34 04 0.14 04 tol 101 101 101 0615 101 10.1 101 0:34 04 562 APPENDIX TABLE 6.9 (Continued) 101 0.55 5.6 10.1 0255 OSS 0.677 0.59 0.52 252 101 5.6 2.14 112 562 APPENDIX B TABLE B.9 (Continued) 30.8 27.5 25.2 5.6 5.6 5.6 5.6 2.14 4.14 10.1 10.1 10.1 10.1 112 112 112 8.15 2.14 0.55 0.55 0.55 0.55 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.789 0.677 0.59 0.523 0.68 0.803 0.889 0.514 0.672 0.801 0.306 0.506 0.668 112 22.8 41.7 33.7 29.7 41.8 37.1 40.1 42.7 48.6 42.4 112 4.14 8.15 2.14 4.14 8.15 112 112 112 y: Dimensionless factor for the pressure drop through a bubble cap x: Superficial fluid velocity of the gas (cm/s) Xz: Kinematic viscosity xz: Mesh opening (cm) x Dimensionless number relating the superficial fluid velocity of the gas to the superficial fluid velocity of the liquid Source: "A Correlation of Two-Phase Pressure Drops in Screen-plate Bubble Column." by C. H. Liu, M. Kan, and B. H. Chen, Canadian Journal of Chemical Engineering, 71, 460 463. DATA SETS FOR EXERCISES 561 TABLE 9 Pressure Drop Data 28.9 0. 341 264 272 0.246 0.379 0.474 0.141 0.234 26.1 23.2 19.7 8.15 2.14 4.14 0.311 2.14 4.14 8.15 2.14 4.14 8.15 22 2.14 4.14 8.15 2.14 4.14 8.15 0.514 0.672 0.801 0.346 0.506 0.669 18.3 33.8 2.14 31.7 28.1 16.5 15.4 19.1 16.2 163 15.8 0.848 0.737 0.651 0.554 0.748 0.682 0.524 0.472 0.398 0.789 0.677 0.59 0.523 0.789 0.677 0.59 0.523 0.741 0.617 0.524 0.457 0.615 0.473 0.381 0.32 10.1 10.1 10.1 10.1 14.7 22.1 15.8 13.2 (Continued) 562 APPENDIX B X3 0.55 0.789 0.55 0.677 30.8 27.5 25.2 22.8 41.7 112 TABLE B.9 (Continued) X1 X2 5.6 10.1 5.6 10.1 5.6 10.1 5.6 10.1 2.14 4.14 112 8.15 112 2.14 112 4.14 112 8.15 112 2.14 112 4.14 112 8.15 112 33.7 0.55 0.55 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.59 0.523 0.68 0.803 0.889 0.514 0.672 0.801 0.306 0.506 0.668 29.7 41.8 37.1 40.1 42.7 48.6 42.4 y: Dimensionless factor for the pressure drop through a bubble cap Xy: Superficial fluid velocity of the gas (cm/s) xz: Kinematic viscosity xz: Mesh opening (cm) xx: Dimensionless number relating the superficial fluid velocity of the gas to the superficial fluid velocity of the liquid Source: "A Correlation of Two-Phase Pressure Drops in Screen-plate Bubble Column" by C. H. Liu, M. Kan, and B. H. Chen, Canadian Journal of Chemical Engineering, 71, 460-463. 5.10 Consider the pressure drop data in Table B.9. a. Perform a thorough residual analysis of these data. b. Identify the most appropriate transformation for these data. Fit this model and repeat the residual analysis. Consider the surronta in a Perform a thorough residual analysis of these sa b. Identify the most appropriate transformation for these and repeat the residual analysis Roodes required to handwerstep by step guidelines this model 562 APPENCE TABLE (Cow S oodusere DSBOCHUM LABLE 19 Pressure Drop Data 214 414 RIS 214 414 0.34 04 04 034 04 034 034 lo RIS 214 4.14 RIS 2.14 4.14 0245 02379 0474 0.141 0234 0111 0.005 112 0.154 014 014 14 15 034 14 TUNO 2.14 4.14 RIS 2.14 0:34 0.14 4.14 RIS 263 044 04 034 09 0.514 0672 ON 0106 0506 . 2.14 4.14 R15 2.14 17.1 18.3 33.8 31.7 263 4.14 0.34 0.14 0.34 263 1.25 014 18.1 0.34 15.4 1-25 1.25 1.25 263 263 263 263 0.34 0.34 OS 0.737 0.651 0554 0745 0.682 0524 0.472 191 162 0.34 0.34 04 16.3 15.8 0.25 19.2 0.25 0.25 R4 101 101 101 101 101 101 101 101 101 0.25 014 Pertttt8888888ttttt 07 0,677 059 0.520 079 0.677 059 0523 0741 0617 04 0.34 04 0.14 04 tol 101 101 101 0615 101 10.1 101 0:34 04 562 APPENDIX TABLE 6.9 (Continued) 101 0.55 5.6 10.1 0255 OSS 0.677 0.59 0.52 252 101 5.6 2.14 112 562 APPENDIX B TABLE B.9 (Continued) 30.8 27.5 25.2 5.6 5.6 5.6 5.6 2.14 4.14 10.1 10.1 10.1 10.1 112 112 112 8.15 2.14 0.55 0.55 0.55 0.55 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.789 0.677 0.59 0.523 0.68 0.803 0.889 0.514 0.672 0.801 0.306 0.506 0.668 112 22.8 41.7 33.7 29.7 41.8 37.1 40.1 42.7 48.6 42.4 112 4.14 8.15 2.14 4.14 8.15 112 112 112 y: Dimensionless factor for the pressure drop through a bubble cap x: Superficial fluid velocity of the gas (cm/s) Xz: Kinematic viscosity xz: Mesh opening (cm) x Dimensionless number relating the superficial fluid velocity of the gas to the superficial fluid velocity of the liquid Source: "A Correlation of Two-Phase Pressure Drops in Screen-plate Bubble Column." by C. H. Liu, M. Kan, and B. H. Chen, Canadian Journal of Chemical Engineering, 71, 460 463. DATA SETS FOR EXERCISES 561 TABLE 9 Pressure Drop Data 28.9 0. 341 264 272 0.246 0.379 0.474 0.141 0.234 26.1 23.2 19.7 8.15 2.14 4.14 0.311 2.14 4.14 8.15 2.14 4.14 8.15 22 2.14 4.14 8.15 2.14 4.14 8.15 0.514 0.672 0.801 0.346 0.506 0.669 18.3 33.8 2.14 31.7 28.1 16.5 15.4 19.1 16.2 163 15.8 0.848 0.737 0.651 0.554 0.748 0.682 0.524 0.472 0.398 0.789 0.677 0.59 0.523 0.789 0.677 0.59 0.523 0.741 0.617 0.524 0.457 0.615 0.473 0.381 0.32 10.1 10.1 10.1 10.1 14.7 22.1 15.8 13.2 (Continued) 562 APPENDIX B X3 0.55 0.789 0.55 0.677 30.8 27.5 25.2 22.8 41.7 112 TABLE B.9 (Continued) X1 X2 5.6 10.1 5.6 10.1 5.6 10.1 5.6 10.1 2.14 4.14 112 8.15 112 2.14 112 4.14 112 8.15 112 2.14 112 4.14 112 8.15 112 33.7 0.55 0.55 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.34 0.59 0.523 0.68 0.803 0.889 0.514 0.672 0.801 0.306 0.506 0.668 29.7 41.8 37.1 40.1 42.7 48.6 42.4 y: Dimensionless factor for the pressure drop through a bubble cap Xy: Superficial fluid velocity of the gas (cm/s) xz: Kinematic viscosity xz: Mesh opening (cm) xx: Dimensionless number relating the superficial fluid velocity of the gas to the superficial fluid velocity of the liquid Source: "A Correlation of Two-Phase Pressure Drops in Screen-plate Bubble Column" by C. H. Liu, M. Kan, and B. H. Chen, Canadian Journal of Chemical Engineering, 71, 460-463. 5.10 Consider the pressure drop data in Table B.9. a. Perform a thorough residual analysis of these data. b. Identify the most appropriate transformation for these data. Fit this model and repeat the residual analysis
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