2020
DOI: 10.1016/j.enconman.2020.113444
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Energetic analysis and optimal design of a CHP plant in a frozen food processing factory through a dynamical simulation model

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Cited by 16 publications
(14 citation statements)
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“…Turbines and microturbines have been used in the food system for different purposes (Table 2), such as milk powder processing (Figure 4). Studies on the use of microturbines range from coffee roasting and frozen food processing to pasta production (Catalano et al, 2020;Pantaleo et al, 2018;Perone et al, 2017). Pantaleo et al (2018) installed two 100-kW microturbines to partially or fully replace a combustion chamber that generates hot air for the batch roasting process of coffee beans with a capacity of 3000 kg/h.…”
Section: Cogenerationmentioning
confidence: 99%
“…Turbines and microturbines have been used in the food system for different purposes (Table 2), such as milk powder processing (Figure 4). Studies on the use of microturbines range from coffee roasting and frozen food processing to pasta production (Catalano et al, 2020;Pantaleo et al, 2018;Perone et al, 2017). Pantaleo et al (2018) installed two 100-kW microturbines to partially or fully replace a combustion chamber that generates hot air for the batch roasting process of coffee beans with a capacity of 3000 kg/h.…”
Section: Cogenerationmentioning
confidence: 99%
“…As said above, consolidated techniques in specific systems such as energy supply and particularly in DSM used for smart grids, can be effectively applied in the management of FSC (Perone et al, 2017;Catalano et al, 2020), to precisely face the above-described difficulties in food systems modelling. In fact, the optimization of plant starting and stopping or sudden and unplanned modification of the process parameters can greatly affect costs and environmental impact.…”
Section: Demand Side Managementmentioning
confidence: 99%
“…The vegetation water (OMWW) and the pomace (OMSR) have an acidic pH, high values of chemical demand (COD) and biochemistry (BOD 5 ) of oxygen, low nitrogen content, and the presence of lipids and a phenolic fraction [9,10]. The high organic load (45-220 g/L of COD) represents a significant energy potential and would make the olive wastewater one of the most suitable agro-industrial wastes for anaerobic digestion [11,12]. The high content of cellulosic and toxic substances, such as phenols, long-chain fatty acids (LCFA), ethanol, tannins, etc., are considered the main obstacles to the anaerobic digestion of oil wastes; in fact, in addition to being hardly degradable, they also inhibit the activity of the micro-organisms responsible for the process [13].…”
Section: Introductionmentioning
confidence: 99%