Page 40 - Industrial Plant 2015
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As a result, the general recommendation for plant In order to control efficiency and hence maximize
profits, the APC system should vary HP and MP
operators is, whenever possible, to increase the load of turbines generation. However, considering that the
plant operates as an electrical island, it is not
the HP turbine at the expense of the MP turbine so to appropriate to move separately HP and MP turbine, as
the total generation must continuously equal the total
increase overall efficiency. electric consumption in the plant.
It is obvious, therefore, that any decrease in MP turbine
Load distribution between turbines, although important generation must counterbalance a similar increase in
HP turbine generation, so that the action of APC
for the overall efficiency, must be operated with system is neutral to the frequency control.
However, this specific Powerhouse did not allow direct
caution: it is known from practical experience that the control of turbine generation due to equipment age.
Turbine generation trim was possible only by means of
turbine of HP loses frequency control ability when its up/down signals, adding further complexity to the APC
implemented. The project team implemented a DCS
actuator position is over 92%. Similarly, scheme to automatically generate up/down pulses to
the two turbines as needed distribute the load in a
Equipment efficiency plant operators should avoid bringing balanced way and following APC software requests.
is quite different for MP turbine to its low limit as this A further hurdle to the power management efficiency is
the two boilers and, condition may also affect overall ability that shifting production between the two turbines has
especially, for the to control frequency. an effect on the overall power factor for the generators,
two turbines. The In addition to that, there is a general which in turn has an impact on the internal grid
HP turbine is quite target of reducing the average opening electrical losses. So, in order to keep the two generators
newer compared to of Pressure Reduction Valves (PRVs) with a balanced power factor and optimize the internal
the MP turbine and its between the headers. Although this grid efficiency, ABB implemented an automatic trim of
specific production, objective is obvious from the energy generators output voltage to rebalance power factors
expressed as power point of view, in practice the demand as the APC system acts on the generators active
produced divided by for process steam is on average higher power output.
the steam flow inlet, is than steam needed to balance the The table 1 shows a list of the main controlled and
significantly higher electric load, so PRVs needs to be constrained variables (CVs) and manipulated variables
partially open in most cases. Therefore, (MVs).
if a complete closure of these valves is Project execution
not possible, valve-opening minimization is extremely One of the key points in the execution of successful
APC projects is the need for a continuous and
important and should be pursued at all times. proactive cooperation between the APC supplier and
the customer. In fact, the very nature of this technology
Combining these practical limitations with the requires that the APC implementation team members
have a good understanding of the process, including
continuous changes in plant loads and in plant steam its bottlenecks and basic economics. Although it is
demand renders powerhouse optimization a minimize
keep close to a maximum
demanding task. In practice, Operators tend to minimize
optimize powerhouses only to a certain extent, always strong link to product quality
retaining significant safety margins. With no APC strong link to product quality
system in place, operators do not update setpoints as
process conditions change continuously, thanks to
these safety margins, but that happens at the expenses
of additional production costs.
Implementing an APC system for supervision and
control of powerhouse along with process to streamline
utility management looked to be the ideal solution to
optimize production. Still, introducing APC in a
Powerhouse is not a trivial task due to several reasons
e.g. fast dynamics and use of complex equipment.
Table 1 APC main CVs Process constraints
variables for
Powerhouse PRVs valve openings
HP turbine actuator
MVs Methane usage
FFs HP steam pressure
MP steam pressure
LP steam pressure
MP boiler output
Attemperators HP / MP / LP
Turbine load distribution
Sugar production load
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