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8 Antonino La Rocca et al. end users facilities and returning to the regasification site, is made via a gaseous phase CO2 pipeline (the pressure losses along the flow path are accounted in the design of the service cycles, see Figs. 6 and 7). Fig. 4 – The Service Cycle for the Agro Food Factories (La Rocca, 2010). Fig. 5 – The Service Cycle for the Hypermarket (La Rocca, 2010). The pumping process of the CO2 in liquid phase is a good practice for saving energy (Dispenza et al., 1979). The process proposed works at hypercritical pressures (LNG in the regasification process has pressure lying in the range 80 ÷ 75 bar). 3.1. The Feasibility Study The recovery of cold from LNG regasification in the proposed process considers two kind of facilities as end user: first a cluster of Agro Food Factories, where there is need of cold for the freezing process of foods and to maintain these at low temperature; second Supermarkets and Hypermarkets where the need of cold is mainly for space air conditioning and some cold is required for the refrigeration of display cases and cabinets in the sales area and for the preparation of foodstuffs and their cold storage in cold storage rooms.
Bul. Inst. Polit. Iaşi, t. LVIII (LXII), f. 4, 2012 9 The two clusters have a mean distance of 2 km from the regasification site. Fig. 6 – The cooling cycle for transfer an utilization of cold in Agro Food Factories diagram: courtesy of IIR (La Rocca, 2010). Fig. 7 – The cooling cycle for transfer an utilization of cold in Hypermarket diagram: courtesy of IIR (La Rocca, 2010).
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