Page 326 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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It should be noted that the quantification of risk in no way eliminates uncertainty. Rather, by quantifying it,
                    a better feel can be developed for how a project’s profitability may vary. Therefore, more informed and
                    rational decisions regarding whether to build a new plant can be made. However, the ultimate decision to
                    invest in a new chemical process always involves some element of risk.


                    Scenario Analysis.   Returning to Example 10.1 regarding the profitability analysis for a new chemical
                    plant, assume that, as the result of previous experience with similar chemicals and some forecasting of
                    supply and demand for this new product, it is believed that the product price may vary in the range –20%
                    to +5%, the capital investment may vary between –20% and +30%, and the cost of manufacturing may
                    vary in the range –10% to +10%. How can these uncertainties be quantified?


                    One  way  to  quantify  uncertainty  is  via  a scenario  analysis.  In  this  analysis,  the  best-  and  worst-case
                    scenarios  are  considered  and  compared  with  the  base  case,  which  has  already  been  calculated.  The
                    values for the three parameters for the two cases are given in Table 10.3.


                    Table 10.3 Values for Uncertain Parameters for the Scenario Analysis (All $ Figures in Millions)













                    Next, these values are substituted into the spreadsheet shown in Table E10.1, and all the cash flows are
                    discounted back to the start of the project to estimate the NPV. The results of these calculations are shown
                    in Table 10.4.


                    Table 10.4 Net Present Values (NPVs) for the Scenario Analysis (All $ Figures in Millions)














                    The results in Table 10.4 show that, in the worst-case scenario, the NPV is very negative and the project
                    will lose money. In the best-case scenario, the NPV is increased over the base case by approximately $45
                    million. From this result, the decision on whether to go ahead and build the plant is not obvious. On one
                    hand, the process could be highly profitable, but on the other hand, it could lose nearly $73 million over
                    the course of the ten-year plant life. By taking a very conservative philosophy, the results of the worst-

                    case scenario suggest a decision of “do not invest.” However, is the worst-case scenario realistic? Most
                    likely, the worst-case (best-case) scenario is unduly pessimistic (optimistic). Consider each of the three
                    parameters in Table 10.3. It will be assumed that the value of the parameter has an equal chance of being
                    at the high, base-case, or low value. Therefore, in terms of probabilities, the chance of the parameter
                    taking each of these values is 1/3, or 33.3%. Because there are three parameters (R, FCI ,  and COM ),
                                                                                                                           L
                                                                                                                                          d
                                                                                                                 3
                    each of which can take one of three values (high, base case, low), there are 3  = 27 combinations as
                    shown in Table 10.5.
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