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This paper studies an absorption machine driven by the heat recovered from a Solid Oxide Fuel Cell (SOFC). The absorption unit was first evaluated by a cycle analysis determining the sensitivity to the main boundary conditions and to the internal parameters. Then a specific simulation code of all the different devices of the absorption machine was developed to evaluate the performance and size of the unit together with its operating condition limits.

In the present paper, the effect of desorption temperature on the performance of adsorption cooling systems driven by waste heat from fuel cells was analyzed. The studied adsorption cooling systems employ activated carbon fiber (ACF) of type A-20–ethanol and RD type silica gel–water as adsorbent–refrigerant pairs. Two different temperature levels of waste heat from polymer electrolyte fuel cell (PEFC) and solid oxide fuel cell (SOFC) are used as the heat source of the adsorption cooling systems. The adsorption cycles consist of one pair of adsorption–desorption heat exchanger, a condenser and an evaporator. System performance in terms of specific cooling capacity (SCC) and coefficient of performance (COP) are determined and compared between the studied two systems. Results show that silica gel–water based adsorption cooling system is preferable for effective utilization of relatively lower temperature heat source. At relatively high temperature heat source, COP of ACF–ethanol based adsorption system shows better performance than that of silica gel–water based adsorption system.

Environmentally responsible and minimal natural variation in electric power generation has been a goal of researchers for several decades. With the establishment of the electrical power generation potential from microalgae’s photosynthesis, several researchers revealed interesting microbial fuel cell configurations to improve the output of electrical parameters. However, little work is done to understand the electrical charge collected from photosynthesis. This article proposes a fuel cell-based electrochemical modeling of the micro-photosynthetic power cell. The model is developed, excluding significant analytical assumptions at stationary conditions. Due to the complexity of modeling the electron release from photosynthesis, the electron release reactions are substituted with a simpler redox coupler of similar electric potential to that of photosynthesis. The micro-photosynthetic power cell revealed that the electron collection rate does not directly correlate to the photosynthesis electron chain. It might remain constant for a specific electrical load. The peak power is obtained at a different operating loading than the internal resistance of the device. The experimental open circuit voltage ($\sim$0.96V) and the peak power ($\sim$0.18mW) are predicted accurately by this modeling approach. The results show that the fill factor remains constant with respect to several effective electrode surface areas. Based on this theoretical modeling, we believe that with optimized algal physiological state and micro-photosynthetic power cell’s effective surface area, this micro-photosynthetic power cell will be useful for application in low-power applications.