In Brescia, Italy, heat is delivered to 70% of 200.000 city inhabitants by means of a district heating system, mainly supplied by a waste to energy plant, utilizing the non recyclable fraction of municipal and industrial solid waste (800,000 tons/year, otherwise landfilled), thus saving annually over 150,000 tons of oil equivalent and over 400,000 tons of CO2 emissions. This study shows how the performance of the waste-to-energy cogeneration plant can be improved by optimising the condensation system, with particular focus on the combination of wet and dry cooling systems. The analysis has been carried out using two subsequent steps: in the first one a schematic model of the steam cycle was accomplished in order to acquire a knowledge base about the variables that would be most influential on the performance. In the second step the electric power output for different operating conditions was predicted and optimized in a homemade program. In more details, a thermodynamic analysis of the steam cycle, according to the design operating condition, was performed by means of a commercial code (Thermoflex©) dedicated to power plant modelling. Then the off-design behaviour was investigated by varying not only the ambient conditions but also several parameters connected to the heat rejection rate, like the heat required from district heating and the auxiliaries load. Each of these parameters has been addressed and considered in determining the overall performance of the thermal cycle. After that, a complete prediction of the cycle behaviour was performed by simultaneously varying different operating conditions. Finally, a Matlab© computer code was developed in order to optimize the net electric power as a function of the way in which the condensation is operated. The result is an optimum set of variables allowing the wet and dry cooling system to be regulated in such a way that the maximum power is achieved. The best strategy consists in using the maximum amount of heat rejection in the wet cooling system to reduce the operational cost of the dry one.
[1]
A. I. Petruchik,et al.
Mathematical Modeling of Evaporative Cooling of Water in a Mechanical-Draft Tower
,
2002
.
[2]
Pertti Heikkilä,et al.
A COMPREHENSIVE APPROACH TO COOLING TOWER DESIGN
,
2001
.
[3]
S. Fisenko,et al.
Evaporative cooling of water in a mechanical draft cooling tower
,
2004
.
[4]
Syed M. Zubair,et al.
A complete model of wet cooling towers with fouling in fills
,
2006
.
[5]
Masud Behnia,et al.
CFD simulation of wet cooling towers
,
2006
.
[6]
S. Fisenko,et al.
Toward to the control system of mechanical draft cooling tower of film type
,
2005
.
[7]
A. K. M. Mohiuddin,et al.
Knowledge base for the systematic design of wet cooling towers. Part I: Selection and tower characteristics
,
1996
.
[8]
René van Berkel,et al.
Waste prevention in small and medium sized enterprises
,
1993
.
[9]
Mehmet Sait Söylemez,et al.
On the optimum performance of forced draft counter flow cooling towers
,
2004
.
[10]
A. Rahman Al-Kassir,et al.
Influence of the cooling circulation water on the efficiency of a thermonuclear plant
,
2005
.
[11]
Jan W. Bloemkolk,et al.
Design alternatives for the use of cooling water in the process industry: Minimization of the environmental impact from cooling systems
,
1996
.
[12]
P. A. Lindahl,et al.
Plume abatement and water conservation with the wet/dry cooling tower
,
1995
.
[13]
S. Fisenko,et al.
Simulation of a cross-flow cooling tower performance
,
2007
.
[14]
Reinhard Harte,et al.
Large-scale cooling towers as part of an efficient and cleaner energy generating technology
,
2002
.
[15]
Detlev G. Kröger,et al.
Performance evaluation of dry-cooling systems for power plant applications
,
1996
.
[16]
Brane Širok,et al.
Improving the efficiency of natural draft cooling towers
,
2006
.