Page 399 - Analysis, Synthesis and Design of Chemical Processes, Third Edition
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As stated previously and in Chapter 24, this section should be eliminated or minimized through pollution
                    prevention  and  green  engineering.  However,  especially  if  the  contaminant  has  little  or  no  value  if
                    concentrated, there will be relatively dilute waste streams generated and sent to the environmental control
                    section. Here, they are concentrated (by the separation techniques discussed earlier) and then disposed of
                    (by incineration, neutralization, oxidation, burial, or other means). The keys are to concentrate the waste
                    and to make it benign.


                    12.7 Major Process Control Loops





                    During the initial synthesis of the PFD, the major control loops are developed. These control loops affect
                    more than just one unit of a process. For example, the level control in the condensate tank of a distillation
                    column is necessary for plant operation. On the other hand, a reactor temperature controller that changes
                    the flowrate of molten salt through the cooling tubes of a reactor is a major loop and should be shown on
                    the PFD.


                    It is through the early development of major control loops that significant design improvements can be
                    made. In the high-temperature exothermic reactor, for example, failure to consider the control loop might
                    lead one to propose an integrated heat-exchanger network that is difficult or impossible to control.


                    Beyond  the  importance  of  the  control  loops  in  maintaining  steady-state  material  balance  control,
                    assurance of product purity, and safety, they provide focal points for the optimization that will follow the
                    initial PFD synthesis. As described in Chapter 14, the controlled variables are the variables over which
                    we  have  a  choice.  We  find  the  best  values  of  these  variables  through  optimization.  These  loops  also
                    provide early clues to the flexibility of the process operation. For example, if the feed to the reactor is cut
                    in half, less heat needs to be removed. Therefore, there must be an increase in the temperature of the
                    cooling medium, which occurs when the coolant flowrate is reduced. Process control can be both very

                    difficult and extremely important in biological processes, as demonstrated in Example 12.5.

                    Example 12.5



                    In biological waste treatment, microbes that eat the waste and produce benign products are used. In one
                    class  of  such  processes,  called activated  sludge,  the  culture  is  separated  from  reactor  output  and
                    recycled. What specfic process control issues arise in such a process?


                    The culture must maintain sufficient activity throughout the recycle. The recycle conditions may become
                    nutrient poor if nearly all the waste nutrient is consumed, leading to loss of activity. The activity of the
                    culture might be adversely affected by upsets in the feed conditions to the reactor, such as pH extremes or
                    high  concentrations  of  compounds  toxic  to  the  culture.  Therefore,  feed-forward  control  using
                    measurements of the feed conditions should be considered, as well as control of a reserve of the culture to
                    be  used  in  case  an  uncontrolled  process  upset  leads  to  culture  death.  Immediate,  on-line  analysis  of
                    culture activity is difficult, but off-line measurements can be incorporated into the control scheme.



                    12.8 Flow Summary Table
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