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5.5.1.5.5 Condenser The saturated vapor leaving the preheater at point 35 enters the condenser. The saturated liquid leaves the condenser and is divided into two branches: one to an ORC pump to return to the ORC cycle and another to an expansion valve to provide the cooling capacity of the system. An energy rate balance for the condenser can be written as ̇ ̇( ) (5.61) 5.5.1.5.6 ORC pump The ORC pump work can be expressed using an energy rate balance for a control volume around the ORC pump as follows: ̇ ̇( ) (5.62) (5.63) 5.5.1.5.7 Expansion valve An energy balance for the expansion valve gives 5.5.1.5.8 Evaporator As shown in Fig. 4.1, an evaporator is used for district cooling. An energy rate balance for this component is written as ̇ Hydrogen as an energy carrier can facilitate sustainable energy systems. The development of sustainable carbon-neutral energy sources has become one of the most significant issues in the world today. Hydrogen can be produced from various energy sources using methods like biomass conversion, steam methane reforming and water splitting. Hydrogen can be produced in a relatively environmentally benign manner (depending on the source of the input energy) via splitting water by photocatalysis, thermochemical cycles and electrolysis. Currently, both thermochemical and photocatalysis hydrogen production are not economically competitive. Water electrolysis is a mature technology for large scale hydrogen production. Hydrogen production by proton exchange membrane (PEM) electrolysis has numerous advantages, such as low environmental impact and easy maintenance. ̇( ) (5.64) 5.5.1.6 PEM Electrolyzer 77PDF Image | Energy Systems for Multigeneration Purposes
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