Novel, cost-effective configurations of combined power plants for small-scale cogeneration from biomass: Design of the immersed particle heat exchanger. (15th September 2017)

• Record Type: Journal Article
• Authors: Amirante, Riccardo; Distaso, Elia; Tamburrano, Paolo
• Is Part Of: Energy conversion and management. Volume 148(2017)
• Page Start: 876
• Page End: 894
• Publication Date: 2017-09-15
• Subjects: Biomass -- Combined cycle -- Gas to gas heat exchanger; Direct energy conversion -- Periodicals; Energy storage -- Periodicals; Energy transfer -- Periodicals; Énergie -- Conversion directe -- Périodiques; Direct energy conversion; Periodicals; 621.3105
• DOI: 10.1016/j.enconman.2017.06.047
• Languages: English
• ISSNs: 0196-8904

Abstract

Highlights: A general approach for the design of a novel gas to gas heat exchanger is proposed. The exchanger is suitable to externally fired combined plants using carbon-neutral biomass. A new architecture for the novel heat exchanger is presented. A fluid dynamic optimization procedure is developed along with analytical models. The exchanger has a small size, with negligible pressure drops and negligible energy losses. Abstract: This paper aims at proposing a general design procedure for the application of the Immersed Particle Heat Exchanger to a novel, small scale, externally fired combined cycle capable of generating electrical and thermal power from carbon-neutral biomass. The Immersed Particle Heat Exchanger serves as the high temperature heat exchanger needed to couple the Brayton cycle with an external combustor of biomass; it is composed of either one module or more modules, with each module being constituted by two heat exchange columns. The combustion gases and the working fluid (clean air) flow separately in the two columns, and ceramic particles are employed as solid intermediate medium to transfer heat between the two columns. Three particle-handling systems, mainly composed of rotary valves coupled with guillotine valves, are conceived in this paper to move the particles within the heat exchanger; analytical models are developed for the design of these systems and for the evaluation of the associated energy losses. A new architecture employing internal cooling channels is also proposed for the two heat exchange columns. In addition, an optimization design procedure, based on the coupling between a computational fluid dynamic model and a genetic algorithm, is developed to correctly select the number of heat exchanger modules as well as the main project parameters, with application to a combined cycle of 110 kWe with an overall efficiency of about 70%. The numerical results show that the project is highly viable. Only a negligible part of the compressed air is lost because of the particle handling systems (about 0.2%); furthermore, the size of the heat exchanger results to be compact, as the selected optimum is characterized by two heat exchanger modules, with each having an overall height, necessary for the heat exchange, of about 4 m and a maximum diameter of 1.2 m.