Page 413 - Design of Simple and Robust Process Plants
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400  Chapter 9 Operation Optimization
                      These systems are subject to frequent changes due to demand, but even
                      more due to the supply of external power at different price sets, like during
                      peak hours and with switch-off contracts. At the same time, several power
                      units might be available, often at so-called ªhot standbyº conditions as back-
                      up. These systems described in a MINLP environment are provided with an
                      optimizer and will include options to influence plant capacities for demand.
                      The optimizations often run off-line and have a continuous advisory function
                      to operation. The optimization in general receives on-line updated informa-
                      tion about units availability and conditions; if required, parameters might
                      also be calculated/estimated. As the site vulnerability might be heavily
                      affected by this operation, procedures for back-up are included in the soft-
                      ware. The mixed integer problem is solved by running all available scenarios
                      and advising the optimal configuration and capacity set-points for the individ-
                      ual units within the defined constraints.
                  .   Dynamic optimization is currently applied only to a very limited extent, for
                      several reasons:
                  ±   Dynamic simulation is currently restricted, and the simulations are mainly
                      applied around a steady-state point for control design and operational studies.
                      The simulations of start-up and shut-downs are subject to a large number of
                      discontinuities which are still difficult to describe in a fundamental way. Dis-
                      continuities such as phase changes, filling and emptying of vessels and also
                      trays in columns, reverse and alternating flows, absorption followed by de-
                      sorption for regeneration, but also in correlations which describe a physical
                      phenomena over large operational ranges.
                  ±   Estimation and prediction of process parameters during operation depend on
                      the technique, but also require a high accuracy of the dynamic model.
                  ±   Simultaneous data reconciliation and parameter estimation in a dynamic
                      environment is commercial not yet available.

                Current applications are the optimization of transient trajectories during grade
                changes in a continuous process, and the optimization of batch cycle times.


                Summary project methodology for OO  This section provides an overview of project
                methodology with its activities that will lead to the successful implementation of an
                OO project. An overview of the overall approach is given in a project methodology
                flowsheet, see Table 9.2. The essence of each step will be discussed.

                  .   A feasibility study should give a detailed overview of the potentials of an OO
                      project. It will give a technical evaluation as well as an economic overview
                      based on a cost±benefit analysis. The study needs to include time schedule,
                      manpower planning, and an overview of factors which might have an impact
                      on site or company standardization.
                  .   Scope definition must be based on the results of the feasibility study, and
                      clearly define the objectives of the project.
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