Page 65 - Industrial Plants 2014
P. 65








Enhancing Energy Efficiency


of Gas Turbines




Mann+Hummel Vokes Air demonstrates the straightforward actions
of retrofit to existing air intakes




Thomas Helf, Carlo Coltri
Mann+Hummel Vokes Air








urope’s larger combined-cycle power prefilter and final filter, the second turbine trialled a new
plants are currently navigating rough filter which condensed the first two stages into one.
seas. Low-cost US coal, renewable Macrogen GT Duo employs a hydrophobic media that
energy and economic crisis have all provides effective water removal whilst also delivering
combined to slash the average running particle filtration to G4 or M5 efficiencies. This means
E hours of plants that utilize gas turbine that separate coalescer and prefiltration stages are
technology. In this market, energy operators are unnecessary and that the redundant filter phase can be
focused more on flexibility than the efficiency of their removed (figure 1).
equipment. This situation with two air intakes in near identical
Nevertheless, there remain a number of smaller gas environments provided an excellent opportunity to
turbine facilities that are continuing to work baseload. demonstrate the benefits of employing a combined
CHP (Combined Heat and Power) and district heating coalescer/prefilter system.

Stage 1 Pre-Filter Final Stage
Gas Turbine A [None] ? Macrogen GT Duo M5 ? Compact F9
Gas Turbine B Coalescer ? Bag Filter G4 ? Compact F9


plants are still working with more than 5000 running Results of Case study 1 Fig. 1 – Effective

hours/year and the operators of these plants are The key findings are: water removal of gas
definitely interested in energy efficiency. • Macrogen GT Duo exhibited very stable pressure turbines A and B
The main topic that will be discussed in this article is the drop performance over the observed period of 4800
air intake of a gas turbine (air filtration system) and how running hours, rising from 65 Pa in April 2012 to 90
it can be improved through the retrofit of existing power Pa in late January 2013 (figure 2, see graph of gas
plants. Evidences and real case studies will demonstrate turbine A);
the theory, while other aspects such as typical intake • gas turbine B’s separate coalescer panels required
problems will also be examined. changing after 2000 hours of operation in November
2012 (figure 2, see graph of gas turbine B);
• performance of the F9 final filters was very similar in
Case study 1: Employing both the air intakes;

a combined preflter/coalescer • the F9 final filters downstream from the Macrogen
GT Duo system ran for a greater number of hours
The first case study examines the air intakes of two and had a slightly lower pressure drop (105 against
neighbouring, 250 MW gas turbines. Both intakes had 110 Pa) over the trial period;
new filters installed in April 2012, but whilst the first • this result is due to the fact that the Macrogen has
turbine had the traditional arrangement of coalescer, not only reduced the pressure drop but, at the same

IndustrIal Plants - May 2014
61
   60   61   62   63   64   65   66   67   68   69   70