A process equipment has been designed to make heat continuously available at a temperature level of 260o. The only source of energy is a continuous flow of saturated steam at 17.5 bar (h=2794.1 kJ/kg; s = 6.3853 kJ/kg-K). Cooling water is also available in large supply at 20oC. The steam is condensed in the equipment and comes out as condensate at 1 bar and 20oC (h=85.5 kJ/kg ; s = 0.2959kJ/kg-K). How much heat can be transferred from the process to the heat reservoir at 260oC, for every one kg of steam condensed in the process?