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Consider that you are part of a team responsible for debottlenecking the process shown in Fig.1 to make it more energy-efficient: Chemical Engineering Assignment, UOC, UK
| University | University Of Cambridge (UOC) |
| Subject | Chemical Engineering |
Description
Consider that you are part of a team responsible for debottlenecking the process shown in Fig.1 to make it more energy-efficient. In the PFD, 9 streams have been highlighted (RED for hot streams and BLUE for cold streams. Hot streams are labeled H1 to H4 and cold streams are labeled C1 to C5 ). The information for the highlighted streams – mass flow rate, specific heat capacity, start and target temperature (i.e.: Ts and Tt) are given in Table 1. The minimum approach temperature for this process is 10oC.
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- Provide an evaluation of the external utility cost (cooling water and steam) for the heat exchangers (HX1 to HX9) as shown in Fig 1
- Illustrate a strategy for reducing external utility use in the process. This should be shown using the HEN grid.
- Provide an evaluation of the external utility cost (cooling water and steam) for the modified process.
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