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Lipid Simulation

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Firstly the shortcut simulation of BTX separation was conducted. The first shortcut column that receives the feed is representative of the prefractionator, which is the left side of the dividing wall. Therefore this first column is meant to do sloppy splits of the feed. In this case, the prefractionator is expected to do a sharp split of Benzene and p-Xylene and a sloppy split of Toluene. For the prefractionator (SRCT-1), the heavy key will be p-Xylene and light key will be Benzene. This is because Benzene is the lightest component that is to be removed from the top of the column and p-Xylene is the heaviest component that is to be removed from the bottom. Since a sloppy split of Toluene is done, it is divided to the top and bottom of the shortcut …show more content…

In this part of the column, the main separation that occurs is between Benzene and Toluene, which is the lightest component and the middle component. The presence of p-Xylene at this part of the column is low and irrelevant. Therefore the light key is Benzene and the heavy key is Toluene. Since the required mole fraction of Benzene in the distillate is 99.5%, the allowable “impurity” in the distillate is only 0.5%. Since p-Xylene is a heavy component, any p-Xylene present in the SRCT-2 column will go into the bottoms product of the column. Therefore all the 0.5% in the distillate will be Toluene, so specify the heavy key in the distillate to be 0.005. For the light key in the bottoms, it can vary depending on the total impurity level in the side stream. Since the specified Toluene purity is 91%, there is a total of 9% impurity in the stream. Therefore an initial guess of 0.045 can be taken as the mole fraction of light key in the bottoms. This will give a minimum reflux of 2.43 and a reflux of 2.9 is specified. The conditions at which the product streams SRCT2 Distillate and SRCT2 Bottoms is produced can be seen on table 6. The shortcut column can be seen on figure 35.The distillate stream in this SRCT-2 column represents the distillate product that will be produced and the bottom product represents a portion of the side product that is …show more content…

In this column, the main separation occurs between the heavy and middle components. Therefore, p-Xylene is the heavy key and Toluene is the light key. Since the required purity of p-Xylene in the bottoms is 92%, the remaining 8% must be made of Toluene. Therefore the mole fraction of light key in the bottoms is specified to be 0.08. Since Toluene is meant to have 9% impurity and 4.5% is already accounted by Benzene from the top part of the column, the mole fraction of p-Xylene in the top can be estimated to be 0.045. This is done under the assumption that the molar flow rates of both middle streams are the same. When SRCT2-Bottoms stream and SRCT3-Distillate stream is mixed using a mixing unit, it showed the mole fraction of Toluene to be 0.9098. To make the shortcut simulation to reach the specification, the light key in the SRCT-2 column and heavy key in the SRCT-3 column was adjusted. After several trail and errors a mole fraction of 0.0505 for Benzene in SRCT-2 and 0.0402 for p-Xylene in SRCT-3 column gave a mole fraction of 0.91 for toluene in the side stream. The number of stages calculated by the SRCT-3 column was 29 and the optimal feed stage was 18. The conditions at which SRCT3-Distillate and SRCT3-Bottoms are produced can be seen on table 6. Figure 36 shows the SRCT-3 shortcut column. When SRCT2-Bottoms and SRCT3-Distillate

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