Page 98 - Plant design and economics for chemical engineers
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76  PLANT DESIGN AND ECONOMICS FOR CHEMICAL ENGINEERS

     TABLE 6
     !hquence  of steps in developing a project?
                            Time sequence
             Process  identification
              Laboratory  verification
               ‘Reaction flow schematic
                 Preliminary flow process
                   Preliminary  economic  evaluation
                     Process  development
                      Mass and energy balance
                        Process flow scheme
                         Site selection
     Project steps         Refined  economic  evaluation
                            Design fixed
                              Detailed  economic  evaluation
                                Engineering flow scheme
                                 Basic design
                                   Detailed construction plan
                                    Detail design
                                      Procurement
                                        Construction
                                         Startup
     t  Modified from Ann.  Occup.   Hyg.,  30~232   (1986).




          The disposal of waste streams that contain large amounts of water is
     another challenge which faces a process engineer. Deep-well injection has been
     used in the past, but this method has been constrained by regulatory agencies.
     Recently, refinery wastewater and storm water runoff has been subject to more
     stringent Best Available Technology (BAT) effluent controls. The agreement
     covers nonconventional pollutants such as phenolic compounds, ammonia sul-
     fide, and toxic pollutants such as chromium and hexavalent chromium.
         Hydrocarbon emissions is an environmental problem which is prominent
     in some areas of the country. In these areas, pollutant levels occasionally exceed
     the national ambient air quality standard. One source of these pollutants
     involves emissions from refineries where about 85 percent of the hydrocarbons
     emitted to the atmosphere are from fugitive emissions. The principal contribu-
     tors generally are valves, flanges, pumps, and compressors. Since 1981, valves
     and flanges must be repaired if they have emission concentrations greater than
     10,000 ppm, when measured at the source with a hydrocarbon analyzer. They
     must be inspected every six months to a year. Pumps and compressors, however,
     need to be checked every shift to verify that they meet current emission
     standards.
          It is becoming increasingly clear that chemical engineers must be versed in
     the latest federal and state regulations involving environmental protection,
     worker safety, and health. This need is especially great for engineers in
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