Page 417 - Design of Simple and Robust Process Plants
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404  Chapter 9 Operation Optimization
                Quality ofcontrol
                  ±   H Process that requires many operator interventions to compensate for dis-
                      turbances and requires ongoing adjustments to maintain quality operation.
                      The cause might be frequent changes in feedstock rates other external distur-
                      bances, and difficult quality control caused by interaction.
                  ±   M Processes that are less subject to disturbances and interaction, like con-
                      stant feed composition and major quality loops closed.
                  ±   L Process only minimal subject to external disturbances and interaction such
                      as constant feed streams and most quality loops closed.
                  ±   NA Process not impacted by external disturbances and interaction such as
                      total automated unit operations as refrigeration systems.

                Constraint operations
                  ±   H Process is running against different constraints at different units, like
                      capacity constraints and environmental constraints (by processing different
                      feeds, different constraints might become active also constraints at low capa-
                      city or changing meteorological conditions).
                  ±   M Process have a moderate number of constraints, like processes with feed
                      streams with constant composition and those running only incidentally
                      against constraints.
                  ±   L Process running below capacity and only incidentally forced to an extreme
                      operational regime which also may include low-capacity operation or
                      equipped with constraint controllers on most activated constraints.
                  ±   NA Almost never running against a constraint or fully provided with con-
                      straint controllers. Floating pressure controllers or maximum duty control on
                      a refrigeration system can also be considered as constraint controller next to
                      MIMO controllers.
                Note: after implementation of an off-line optimization, constraints become more
                visible and often there are more constraints than would be noticed without optimi-
                zation results at hand.

                Optimization closed loop
                  ±   H Processes with many economic disturbances at a frequency of a few times
                      per day, such as processes with wide feed slate and product distributions, a
                      high number of DOFs likely with a large number of units, highly constrained
                      operations which is implicitly coupled to the processing of wide feed and
                      product slates. Parameters that need a regular update.
                  ±   M Processes with several economic disturbances and a moderate number of
                      DOFs (5±10)on a daily basis.
                  ±   L Processes with a limited number of disturbances and DOFs (<5)on a less
                      than daily basis, with off-line optimization results available for manual imple-
                      mentation.
                  ±   NA process with low number of disturbances and DOFs that are already
                      manually implemented based on off-line optimization results.
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