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No. 2 fuel oil is the final fossil fuel that is commonly used as an energy source in the chemical industry.
                    Until recently, it has been the highest-cost fossil fuel source. It is most readily available near coastal
                    regions where oil enters the country and refining takes place. The United States has become increasingly
                    dependent  on  imported  oil,  which  may  be  subject  to  large  upsets  in  cost  and  domestic  availability.
                    Uncertainties in the availability of supplies, high storage costs, and large fluctuations in cost make this
                    source  of  energy  least  attractive  in  many  situations.  However,  recently  the  cost  of  natural  gas  has
                    increased substantially to the point that No. 2 fuel oil is now a viable alternative to natural gas in many
                    plants.


                    Figure  8.1  shows  that  fuel  costs  have  increased  somewhat  more  rapidly  and  in  a  much  more  chaotic
                    fashion than the cost index (CEPCI) that we have used previously to correct costs for inflation. As a result
                    of the regional variations in the availability and costs of fossil fuels, along with the inability of the cost
                    index to represent energy costs, we take the position that site-specific cost and availability information
                    must be provided for a valid estimation of energy costs. We assume, in this text, that natural gas is the fuel

                    of choice unless otherwise stated.

                    The PFD for the toluene hydrodealkylation process (Figure 1.5) represents the “battery-limits” plant. The

                    equipment necessary to produce the various service or utility streams, which are used in the process and
                    are necessary for the plant to operate, are not shown on the PFD. However, the utility streams such as
                    cooling water and steam for heating are shown on the PFD. These streams, termed utilities, are necessary
                    for the control of stream temperatures as required by the process. These utilities can be supplied in a
                    number of ways.
                          1.    Purchasing from a Public or Private Utility: In this situation no capital cost is involved, and
                                the utility rates charged are based upon consumption. In addition the utility is delivered to the
                                battery limits at known conditions.
                          2.   Supplied by the Company: A comprehensive off-site facility provides the utility needs for many
                                processes at a common location. In this case, the rates charged to a process unit reflect the fixed
                                capital and the operating costs required to produce the utility.
                          3.    Self-Generated  and  Used  by  a  Single  Process  Unit:  In  this  situation  the  capital  cost  for
                                purchase and installation becomes part of the fixed capital cost of the process unit. Likewise the

                                related operating costs for producing that particular utility are directly charged to the process
                                unit.

                    Utilities that would likely be provided in a comprehensive chemical plant complex are shown in Table

                    8.3.

                    Table 8.3 Utilities Provided by Off-Sites for a Plant with Multiple Process Units (Costs Represent

                    Charges for Utilities Delivered to the Battery Limit of a Process)
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