0.3 2 Operating line 0.2 Equilibrium line 0.1 2 O 0.05 0.10 0.15 Construct an operating line for example 20.1. Show ALL your work (in calculating intermediate points) and label ALL points (terminal and intermediate points) on your diagram. You will hand in a physical, tangible paper to me on Monday. Paper may be of any type - blank, lined, graphing, recycled, etc. I want you to use a straight edge to make your axes and increments as precise as possible. Your operating line will be only very slightly curved, so don't force it to be straight! Capilla Steam 182 Transfer and bes Applicatio 02 one in this colum. The second stage is located graphically on the diagram repeating the same construction, powing horizontally to the equilib point ouvingates and vertically to the operating line anal having coordinates. The third stage is found by again repeating the ruction, giving triangle web. For the situation shown in Fu, 20.5. the third is the best as the concentration of the presentering that stage is and the sig learing it is, which are the desired terminal concentrations. Three ideal tapes required for this separation The same construction can be used for determining the number of ideal stage needed in any cascade, whether it is used for gas absorption, stripping, diutius leaching or liquid extraction. The graphical step-by-step construction utilizing di emately the operating and equilibrium lines to find the number of ideal stages fine applied to the design of distillation columns, and is known as the McCur Thiele method. The construction can be started at either end of the commande general the last step will not eactly meet the terminal concentrations, as was the cae in Fig. 205. A fractional step may be assigned, or the number of deal stages may be founded up to the nearest whole number FIGURE factor of only 1.36 from with in the detection The number of ideals within relative to the chose that would be made hell la construction based on change the war be the operating and equilibrium the EXAMPLE 38. By means of a plane column, acetone is absorbed from with it in a non volatile absorption oil. The entering as contains Bound the enteng al is ceton-free. or the stone in the airport shared as the concentrated quer at the bottom of the tower is to come per cent The equilibrium relationship is y=19x, Mut the personal determine the number of ideal stages Si Chopse 100 montering gassbasis, and at this equal to V. meg is the 3 x 100 = 30 mol the air entering is 100 30 97 percase, the con leaving is 001 30 0.9 moland, 00127 de setme he is 30 - 09 = 29. mol. With 10 percent = being solution and to come in the entering - 29.1. und Then L = 91 - 2912519 mol Tu tienda intermediate police the operating line, make an cho and the top part of the wet inga particular hear, the w in the pas For 10 m left in the gas 10 = 0.125 10 + 10 Themes of accome lot by the pain this section 109 1 molested by the liquid. Hence where y 0.125 91 261,091 Similarities for V = 2020/900.222191 The ping line is plaitted in Fig. 2016. Although it was call the seat the top is 1.57 times the slope at the heale bol Lewis large the chat and because of the change in the total tow. The Absorption factor method for calculating the sumber da ste When the operating and with lines are given.com centration range to the number of ideas can be bacted directly, and graphical construction is mary Form for the posee derived Let the music of the equilibrium liebe follow here, by demandar att det - rachung 0.3 2 Operating line 0.2 Equilibrium line 0.1 2 O 0.05 0.10 0.15 Construct an operating line for example 20.1. Show ALL your work (in calculating intermediate points) and label ALL points (terminal and intermediate points) on your diagram. You will hand in a physical, tangible paper to me on Monday. Paper may be of any type - blank, lined, graphing, recycled, etc. I want you to use a straight edge to make your axes and increments as precise as possible. Your operating line will be only very slightly curved, so don't force it to be straight! Capilla Steam 182 Transfer and bes Applicatio 02 one in this colum. The second stage is located graphically on the diagram repeating the same construction, powing horizontally to the equilib point ouvingates and vertically to the operating line anal having coordinates. The third stage is found by again repeating the ruction, giving triangle web. For the situation shown in Fu, 20.5. the third is the best as the concentration of the presentering that stage is and the sig learing it is, which are the desired terminal concentrations. Three ideal tapes required for this separation The same construction can be used for determining the number of ideal stage needed in any cascade, whether it is used for gas absorption, stripping, diutius leaching or liquid extraction. The graphical step-by-step construction utilizing di emately the operating and equilibrium lines to find the number of ideal stages fine applied to the design of distillation columns, and is known as the McCur Thiele method. The construction can be started at either end of the commande general the last step will not eactly meet the terminal concentrations, as was the cae in Fig. 205. A fractional step may be assigned, or the number of deal stages may be founded up to the nearest whole number FIGURE factor of only 1.36 from with in the detection The number of ideals within relative to the chose that would be made hell la construction based on change the war be the operating and equilibrium the EXAMPLE 38. By means of a plane column, acetone is absorbed from with it in a non volatile absorption oil. The entering as contains Bound the enteng al is ceton-free. or the stone in the airport shared as the concentrated quer at the bottom of the tower is to come per cent The equilibrium relationship is y=19x, Mut the personal determine the number of ideal stages Si Chopse 100 montering gassbasis, and at this equal to V. meg is the 3 x 100 = 30 mol the air entering is 100 30 97 percase, the con leaving is 001 30 0.9 moland, 00127 de setme he is 30 - 09 = 29. mol. With 10 percent = being solution and to come in the entering - 29.1. und Then L = 91 - 2912519 mol Tu tienda intermediate police the operating line, make an cho and the top part of the wet inga particular hear, the w in the pas For 10 m left in the gas 10 = 0.125 10 + 10 Themes of accome lot by the pain this section 109 1 molested by the liquid. Hence where y 0.125 91 261,091 Similarities for V = 2020/900.222191 The ping line is plaitted in Fig. 2016. Although it was call the seat the top is 1.57 times the slope at the heale bol Lewis large the chat and because of the change in the total tow. The Absorption factor method for calculating the sumber da ste When the operating and with lines are given.com centration range to the number of ideas can be bacted directly, and graphical construction is mary Form for the posee derived Let the music of the equilibrium liebe follow here, by demandar att det - rachung