Page 56 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
P. 56

The minimum spacing between equipment should be set early on in the design. These distances are set for
                    safety purposes and should be set with both local and national codes in mind. A comprehensive list of the
                    recommended minimum distances between process equipment is given by Bausbacher and Hunt [5]. The
                    values for some basic process equipment are listed in Table 1.11.


                    Table  1.11  Recommended  Minimum  Spacing  (in  Feet)  between  Process  Equipment  for  Refinery,
                    Chemical, and Petrochemical Plants





















                    The  sizing  of  process  equipment  should  be  completed  and  the  approximate  location  on  the  plot  plan
                    determined.  Referring  to Table  B.1.3  for  equipment  specifications  gives  some  idea  of  key  equipment
                    sizes. For example, the data given for the reflux drums V-202 and V-203, reactor R-201, and towers T-

                    201 and T-202 are sufficient to sketch these units on the plot plan. However, pump sizes must be obtained
                    from vendors or previous jobs, and additional calculations for heat exchangers must be done to estimate
                    their required footprint on the plot plan. Calculations to illustrate the estimation of equipment footprints
                    are given in Example 1.11.


                    Example 1.11


                    Estimate the footprint for E-202 in the DME process.


                    From Table B.1.3 we have the following information:
                          Floating Head Shell-and-Tube design
                          Area = 171 m   2

                          Hot Side—Temperatures: in at 364°C and out at 281°C
                          Cold Side—Temperatures: in at 154°C and out at 250°C
                          Choose a two-shell pass and four-tube pass exchanger
                          Area per shell = 171/2 = 85.5 m     2
                          Using 12 ft, 1-inch OD tubes, 293 tubes per shell are needed


                    Assuming the tubes are laid out on a 1¼-inch square pitch, a 27-inch ID shell is required.


                    Assume that the front and rear heads (where the tube fluid turns at the end of the exchanger) are 30 inches
                    in diameter and require 2 feet each (including flanges), and that the two shells are stacked on top of each
                    other. The footprint of the exchanger is given in Figure E1.11.


                    Figure E1.11 Approximate Dimensions and Footprint of Exchanger E-202
   51   52   53   54   55   56   57   58   59   60   61