Page 48 - Design of Simple and Robust Process Plants
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32  Chapter 2 Simple and Robust Plant Design
                 umbrella of ªrobustnessº± which in itself can be subdivided into several types:
                 mechanical; control; and operational.


                 2.4.1
                 Mechanical Robustness

                 First, we have to consider manual, incorrect operations that challenge mechanical
                 robustness, for example the wrong lining up of a pump. For instance, an operator
                 may forget to open the suction valve, leading to cavitation of a pump, but it is
                 unclear whether the pump is sufficiently robust to withstand this operational error
                 for a short period. Numerous other examples exist where the robustness of the
                 design has been improved. In the past, many accidents have occurred because plug
                 valves were equipped with handles, which incidentally were opened, but today most
                 of these are equipped with hand-wheels. Another example is the casings of pumps
                 which, in the past were often designed from cast iron ± a material which cannot
                 withstand thermal shocks. Nowadays, pumps that may be exposed to fire are de-
                 signed from cast steel. The design of piping also provided the knowledge that ASA
                 flanges are more robust than DIN flanges, and resulting in less leakage. By contrast,
                 the selection of API pumps (which are known for their heavier construction) for
                 standard applications did not show any major improvement in performance com-
                 pared with ANSI pumps.
                   In general, mechanical robustness is reflected in the selection of equipment, pip-
                 ing items and instruments, but is also applied in control terminology.

                 2.4.2
                 Control Robustness

                The term ªrobust controlºinfers that a process is able to recover from set-point
                 changes and disturbances within a wide range, and achieves set-point tracking and
                 disturbance rejection to its target values within a reasonable time frame. The distur-
                 bances considered are mainly changes in feed rates or composition, utilities and
                 environmental conditions. Interruptions in conditions as trips are seldom consid-
                 ered under robust control. A good control design must achieve a certain robustness
                 due to the most likely disturbances.

                 2.4.3
                 Operational Robustness

                The term ªrobust operationºmight be used for the implementation of:
                   .  Automatic start-up, shut-down, and implementation of regeneration se-
                      quences.
                   .  Recovery of situations where interruptions such as pump trips or alarms
                      must be anticipated. Such situations must be foreseen and result in an auto-
                      matic actions, either in process recovery or end-up in a defined standby con-
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