Titlebook: Syngas from Waste; Emerging Technologie Luis Puigjaner Book 2011 Springer-Verlag London Ltd. 2011 Conceptual Process Design.Energy Supply C

Antagonist

Introduction,g the syngas production process are enunciated. Second, the suitable raw materials for gasification, the products obtained, and their end uses are identified. Third, the advantages, opportunities, present commercial status, and future perspectives of gasification are discussed. Finally, the need for

PHIL

Raw Materials, Selection, Preparation and Characterization,on dioxide released during its use is an integral part of the carbon cycle. Increasing the share of biomass in the energy supply contributes to diminishing the environmental impact of CO. and to meeting the targets established in the Kyoto Protocol. The use of biomass waste material as a fuel, howev

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Raw Materials Supply,velopment of efficient energy supply chains from biomass it is required to properly integrate the various elements that comprise such systems (e.g., biomass supply, pre-treatment facilities and technologies for biomass to energy and/or fuels conversion). Additionally, it is recognised that a concert

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Modelling Syngas Generation, the generation process used and the raw material composition. Gasification is the referred technique to produce syngas. It can be used for different purposes, such as power and/or heat generation or for chemicals and fuels production. This chapter describes, we comment the generalities of syngas an

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Main Purification Operations,ls and fuels production to power and/or heat. This chapter deals with the description and the modelling of the required syngas treatment units before electricity production or before hydrogen generation, specifically in an IGCC power plant. In the case of electricity generation application, the purs

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Modelling Superstructure for Conceptual Design of Syngas Generation and Treatment,raws on how the superstructure can be built, while the second section depicts the different techniques that can be used to reduce the computational time required to run a superstructure optimisation. . describes the different integration and control considerations embedded in a possible superstructu

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Process Integration: HEN Synthesis, Exergy Opportunities,s heat exchanger network. Trade-offs between the income from power generation and utility costs plus the investment in HEN are studied with respect to the generation of different pressure-levels of steam and temperature driving force losses within the heat-recovery network. A combined pinch analysis

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Global Clean Gas Process Synthesis and Optimisation,e different techniques for tackling with multiple criteria are presented, emphasising the use of multi-criteria decision analysis (MCDA) and multi-objective optimisation (MOO). The different criteria elected here for optimisation are described and later used as key performance indicators (KPI) for t