The wave and tidal energy sectors have received much interest in recent years, from policy-makers attentive to the prospect that ocean energy technologies could be capable of contributing towards meeting environmental targets; from utility companies that expressed interest in developing, constructing and operating array projects to export large quantities of clean energy from ocean based resources; and from Small to Medium Enterprises (SMEs) and large multi-national Original Equipment Manufacturers (OEMs) that were interested in undertaking technological development to commercialise wave and tidal energy converters that could successfully harness the energy contained within the ocean waves and tides. Within the existing research, development and innovation environment that has largely dominated the development of wave and tidal energy to date – rapid development of large MW-scale devices capable of utility scale power generation – technology developers have failed to reach the level of deployed capacity that was initially anticipated, despite the significant level of investment that has taken place. Indeed, the expected contribution of ocean energy in the wider energy mix, which has been written into policy documentation at both national and European level, has so far failed to materialise in the form of prolific multiple device array deployments. The research, development and innovation environment has not delivered on its intended objective of demonstrating commercial technology readiness, and the historic development trajectories for ocean energy technologies may not represent the most cost-effective route to product commercialisation. This research explores the wave and tidal energy research, development, and innovation environment through extensive stakeholder engagement within the ocean energy sector, and through application of suitable techniques from innovation theory. The purpose of this research was three-fold. Firstly, an objective analysis of the development of the wave and tidal energy sectors – building a comprehensive understanding of their development to date through extensive stakeholder engagement, and comparing wave and tidal energy technology development with that of historic energy technologies that have successfully entered into commercial operation – was necessary in order to identify whether the attempt by ocean energy technologies for rapid up-scaling of technology is consistent with the development pathway that was followed by energy technologies which have successfully transitioned from novel invention to full commercial operation. This work identified several dichotomies that are present in the nascent stages of technology development in the wave and tidal energy sectors. Secondly, the uncertainties surrounding existing capital and revenue costs, and the uncertainties within the potential future cost reductions associated with current technology trajectories, could lead to unsustainable investment requirements. Commercialisation of wave and tidal energy technology is predicated upon significant cost reduction – the current technology costs are not feasible for large scale roll out of technology. A research focus on the economic uncertainty through application of learning theory and a learning investment sensitivity analysis was anticipated to demonstrate the economic impact of minor perturbations from idealised reference assumptions. The results from this work suggest that even minor perturbations in input parameters have substantial negative impact on overall investment requirements to bring technology to a level of cost competitiveness. Thirdly, the policy landscape surrounding wave and tidal energy development has not been specifically compared and contrasted, using a number of performance metrics, to a technology which was subject to similar expectations in the form of income streams – wind energy technology. The causes and motivations for the rapid transition to large-scale technologies and ‘accelerated innovation’ within ocean energy technology were considered within this research, which suggested that a mismatch between policy support and technological readiness could misguide and misdirect the innovation pathway, harming the commercialisation prospects of ocean energy technology. In order for the successful emergence of economically sustainable wave and tidal energy technologies, a paradigm shift may be necessary, a change from the current approach that has to date dominated technological development within both the wave and tidal energy sectors. This research draws together industry consultation with academic insight to identify an optimised innovation pathway, culminating in a policy appraisal to guide and inform economically sustainable development of wave and tidal energy technologies.

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The nuclear industry lacks a well documented, systematic procedure defining the requirements for power plant cycle selection and optimisation. A generic technoeconomic optimisation methodology is therefore proposed that can serve in the selection of balance-of-plant configurations and design conditions for High Temperature Gas-cooled Reactor (HTGR) power plants. The example of a cogeneration steam plant coupled to a pebble bed reactor, with or without an intermediate buffer circuit, was used in search of a suitable methodology. The following analyses were performed: • First order thermal hydraulic analysis • Second order thermal hydraulic analysis including cost estimation • Third order steady state analysis to evaluate part-load operation • Third order transient analysis to test operability and controllability The assumptions, level of detail required, modelling methodology and the type of decisions that can be made after each stage are discussed. The cycles under consideration are evaluated and compared based on cycle efficiency, capital cost, unit energy cost and operability. The outcome of this study shows that it is worthwhile spending the effort of developing a second order costing model and a third order model capable of analysing off-design conditions. First order modelling could be omitted from the methodology. The advantage of a second order model is that the cycle configuration can be optimised from a unit energy cost perspective, which incorporates the effects of both capital cost and cycle efficiency. The optimum cycle configuration differs from that predicted by first order modelling, which illustrates that first order modelling alone is insufficient. Third order part-load operation analysis showed operability issues that were not apparent after first or second order modelling. However, transient analysis does not appear justified in the very early design stages. To conclude, the proposed methodology is summarised as follows: • Evaluate the user requirements and design constraints. • Apply design principles from the Second Law of thermodynamics in selecting cycle configurations and base case operating conditions. • Optimise the operating conditions by performing second order thermal hydraulic modelling which includes component design and cost estimation. • Evaluate part-load operation with third order analysis. • Select the cycle with the lowest Levelised Unit Energy Cost (LUEC) and simplest operating strategy. / Thesis (M.Ing. (Mechanical Engineering))--North-West University, Potchefstroom Campus, 2010.

The nuclear industry lacks a well documented, systematic procedure defining the requirements for power plant cycle selection and optimisation. A generic technoeconomic optimisation methodology is therefore proposed that can serve in the selection of balance-of-plant configurations and design conditions for High Temperature Gas-cooled Reactor (HTGR) power plants. The example of a cogeneration steam plant coupled to a pebble bed reactor, with or without an intermediate buffer circuit, was used in search of a suitable methodology. The following analyses were performed: • First order thermal hydraulic analysis • Second order thermal hydraulic analysis including cost estimation • Third order steady state analysis to evaluate part-load operation • Third order transient analysis to test operability and controllability The assumptions, level of detail required, modelling methodology and the type of decisions that can be made after each stage are discussed. The cycles under consideration are evaluated and compared based on cycle efficiency, capital cost, unit energy cost and operability. The outcome of this study shows that it is worthwhile spending the effort of developing a second order costing model and a third order model capable of analysing off-design conditions. First order modelling could be omitted from the methodology. The advantage of a second order model is that the cycle configuration can be optimised from a unit energy cost perspective, which incorporates the effects of both capital cost and cycle efficiency. The optimum cycle configuration differs from that predicted by first order modelling, which illustrates that first order modelling alone is insufficient. Third order part-load operation analysis showed operability issues that were not apparent after first or second order modelling. However, transient analysis does not appear justified in the very early design stages. To conclude, the proposed methodology is summarised as follows: • Evaluate the user requirements and design constraints. • Apply design principles from the Second Law of thermodynamics in selecting cycle configurations and base case operating conditions. • Optimise the operating conditions by performing second order thermal hydraulic modelling which includes component design and cost estimation. • Evaluate part-load operation with third order analysis. • Select the cycle with the lowest Levelised Unit Energy Cost (LUEC) and simplest operating strategy. / Thesis (M.Ing. (Mechanical Engineering))--North-West University, Potchefstroom Campus, 2010.

Global pressure to reduce greenhouse gas (GHG) emissions, energy security concerns and increasing demand for liquid fuels incentivize the search for more sustainable and secure alternative methods for producing liquid fuels with improved efficiency and reduced environmental impacts. One of the economically attractive examples of these alternate methods is the gas-to-liquid process, however, its environmental impacts are worse than traditional petroleum refining. Carbon capture and sequestration is an option to reduce greenhouse gas emissions of processes, but it decreases the efficiency of the process and often results in economic infeasibility. Instead, integrating different processes and feedstocks was demonstrated to improve the efficiency, economic and environmental performance of the processes. The focus of this thesis is to design and simulate a novel integrated biomass, gas, nuclear to liquids (BGNTL) process with negative greenhouse gas emissions. In this process, nuclear heat from a high temperature gas-cooled reactor (HTGR) is used as the heat source for a steam methane reforming (SMR) process. The integrated HTGR and SMR process requires detailed analysis and modeling to address key challenges on safety, operability, economic and environmental impacts of the integrated process. To this end, a rigorous first principle based mathematical model was developed in gPROMS modeling environment for the integrated HTGR/SMR process. The results for a large scale design of this system indicate that hydrogen rich syngas with H2/CO ratio in the range of 6.3 can be achieved. To meet the desired H2/CO ratio (around 2) required for the downstream fuel synthesis processes, the HTGR/SMR derived syngas can be blended with a hydrogen lean syngas from biomass gasification. In this thesis, the large scale design of the BGNTL process to synthesize gasoline, diesel and dimethyl ether (DME) is investigated. The results from the gPROMS model of the integrated HTGR/SMR system are used for simulating the BGNTL process in Aspen Plus. The performance of the BGNTL process was compared with a biomass, gas to liquids (BGTL) process. The efficiency, economics, and environmental impact analyses show that the BGNTL process to produce DME is the most efficient, economic and environmentally friendly process among all the considered designs. The results demonstrate that process integration exploits certain synergies that leads to significantly higher carbon and energy efficiencies and lower greenhouse gas emissions. In addition, it was found that all the studied designs yield a net negative greenhouse gas emissions when carbon capture and storage technology is implemented. As another sustainable alternative to meet the required H2/CO ratio of the syngas when biomass resources are not available, it is proposed to apply the nuclear heat to the mixed reforming of methane. This represents using steam and waste CO2 to reform methane into valuable syngas. The developed model for the integrated HTGR/SMR system is extended to the mixed reforming of methane (MRM) process and it was demonstrated that integrated HTGR/MRM process can be a promising option to achieve certain desired H2/CO ratios for the downstream energy conversion processes. / Thesis / Doctor of Philosophy (PhD)

This research project will investigate the potential business case and technical feasibility of using nuclear generated heat in a crude oil refinery located some distance away. The key design element is an energy transportation mechanism that doesn’t compromise the safety, licensing or operability of the nuclear plant. In a crude oil refinery processing heat is generated by combusting fuels that are generally sellable products. The inherent safety features and high output temperature of a HTGR make it an appropriate replacement heat source for such a processing plant. An opportunity thus exists to replace the refinery hydrocarbon fuel usage with nuclear energy thereby improving refinery profitability. Three alternate proposed were generated. Alt 1: Generation of steam at HTGR, piped to the refinery to replace current supply. Alt 2: Closed loop reversible methanation reaction delivering potential chemical energy to the refinery which is released to the process in heat exchangers. Alt 3: Hydrogen production from water splitting at the HTGR, piped to the refinery and combusted in boilers or used for hydrotreating diesel. Utilizing data from refinery plant historian and journals, a basic engineering study assessed technical feasibility thereof. An economic model for the 2 most promising alternates was set up using quotations and factored data and evaluated against the existing refinery situation. A consistently increasing crude price was assumed. Alternates 1, 2 and 3 proved technically feasible and delivered 86 MW, 59 MW and 48MW to the refinery respectively. Generating steam at the HTGR (Alt 1) demonstrated an attractive business case, strengthened by co-locating the nuclear plant at the refinery. It is therefore concluded that using a HTGR for process heat in a petrochemical plant such as a refinery is techno-economically practical and demands further consideration. If future carbon emission legislation is promulgated this proposal will be key component of the solution. / MIng (Nuclear Engineering), North-West University, Potchefstroom Campus, 2014

This research project will investigate the potential business case and technical feasibility of using nuclear generated heat in a crude oil refinery located some distance away. The key design element is an energy transportation mechanism that doesn’t compromise the safety, licensing or operability of the nuclear plant. In a crude oil refinery processing heat is generated by combusting fuels that are generally sellable products. The inherent safety features and high output temperature of a HTGR make it an appropriate replacement heat source for such a processing plant. An opportunity thus exists to replace the refinery hydrocarbon fuel usage with nuclear energy thereby improving refinery profitability. Three alternate proposed were generated. Alt 1: Generation of steam at HTGR, piped to the refinery to replace current supply. Alt 2: Closed loop reversible methanation reaction delivering potential chemical energy to the refinery which is released to the process in heat exchangers. Alt 3: Hydrogen production from water splitting at the HTGR, piped to the refinery and combusted in boilers or used for hydrotreating diesel. Utilizing data from refinery plant historian and journals, a basic engineering study assessed technical feasibility thereof. An economic model for the 2 most promising alternates was set up using quotations and factored data and evaluated against the existing refinery situation. A consistently increasing crude price was assumed. Alternates 1, 2 and 3 proved technically feasible and delivered 86 MW, 59 MW and 48MW to the refinery respectively. Generating steam at the HTGR (Alt 1) demonstrated an attractive business case, strengthened by co-locating the nuclear plant at the refinery. It is therefore concluded that using a HTGR for process heat in a petrochemical plant such as a refinery is techno-economically practical and demands further consideration. If future carbon emission legislation is promulgated this proposal will be key component of the solution. / MIng (Nuclear Engineering), North-West University, Potchefstroom Campus, 2014

Biomass conversion into forms of energy is receiving current attention because of environmental, energy and agricultural concerns. The purpose of this thesis is to analyze the environmental, energy, economic, and technological aspects of using a form of biomass, switchgrass (panicum virgatum), as a partial or complete replacement for coal in power generation and cogeneration systems. To examine the effects of such a substitution, an environmental biocomplexity approach is used, wherein the agricultural, technological, economic, and environmental factors are addressed. In particular, lifecycle analysis (LCA) and a three-dimensional integrated economic, energy and environmental analysis is employed. The effectiveness of alternate technologies for switchgrass preparation, harvest and use in terms of greenhouse gas impact, cost and environmental implications is examined. Also, different scenarios of cofiring and biomass preparation pathways are investigated. Optimization of the total biomass power generation cost with minimum greenhouse gas effect is undertaken using mathematical programming for various alternate competitive biomass processing pathways. As a byproduct of this work a generic tool to optimize the cost and greenhouse gas emissions for allocation of fuel sources to the power generating sinks is developed. Further, this work discusses the sensitivity of the findings to varied cofiring ratios, coal prices, hauling distances, per acre yields, etc. Besides electricity generation in power plants, another viable alternative for reducing greenhouse gases (GHGs) is the utilization of biomass in conjunction with combined heat and power (CHP) in the process industries. This work addresses the utilization of biowaste or biomass source in a processing facility for CHP. A systematic algebraic procedure for targeting cogeneration potential ahead of detailed power generation network design is presented. The approach presented here effectively utilizes the biomass and biowaste sources as external fuel, and matches it with the use and dispatch of fuel sources within the process, heating and non-heating steam demands, and power generation. The concept of extractable energy coupled with flow balance via cascade diagram has been used as a basis to construct this approach. The work also discusses important economic factors and environmental policies required for the cost-effective utilization of biomass for electricity generation and CHP.

Biomass conversion into forms of energy is receiving current attention because of environmental, energy and agricultural concerns. The purpose of this thesis is to analyze the environmental, energy, economic, and technological aspects of using a form of biomass, switchgrass (panicum virgatum), as a partial or complete replacement for coal in power generation and cogeneration systems. To examine the effects of such a substitution, an environmental biocomplexity approach is used, wherein the agricultural, technological, economic, and environmental factors are addressed. In particular, lifecycle analysis (LCA) and a three-dimensional integrated economic, energy and environmental analysis is employed. The effectiveness of alternate technologies for switchgrass preparation, harvest and use in terms of greenhouse gas impact, cost and environmental implications is examined. Also, different scenarios of cofiring and biomass preparation pathways are investigated. Optimization of the total biomass power generation cost with minimum greenhouse gas effect is undertaken using mathematical programming for various alternate competitive biomass processing pathways. As a byproduct of this work a generic tool to optimize the cost and greenhouse gas emissions for allocation of fuel sources to the power generating sinks is developed. Further, this work discusses the sensitivity of the findings to varied cofiring ratios, coal prices, hauling distances, per acre yields, etc. Besides electricity generation in power plants, another viable alternative for reducing greenhouse gases (GHGs) is the utilization of biomass in conjunction with combined heat and power (CHP) in the process industries. This work addresses the utilization of biowaste or biomass source in a processing facility for CHP. A systematic algebraic procedure for targeting cogeneration potential ahead of detailed power generation network design is presented. The approach presented here effectively utilizes the biomass and biowaste sources as external fuel, and matches it with the use and dispatch of fuel sources within the process, heating and non-heating steam demands, and power generation. The concept of extractable energy coupled with flow balance via cascade diagram has been used as a basis to construct this approach. The work also discusses important economic factors and environmental policies required for the cost-effective utilization of biomass for electricity generation and CHP.

Τα τελευταία χρόνια δίνεται μεγάλη έμφαση στην ανάπτυξη ηλεκτρικών συστημάτων φιλικών προς το περιβάλλον. Στην κατεύθυνση αυτή πραγματοποιείται προοδευτική αντικατάσταση συστημάτων συμβατικών πηγών ενέργειας (όπως το πετρέλαιο) με νέα ανανεώσιμων. Σε αυτή την εργασία έχει μελετηθεί, με την βοήθεια του προγράμματος προσομοίωσης – βελτιστοποίησης HOMER, η λειτουργία διαφόρων αυτόνομων ηλεκτρικών συστημάτων με στόχο την κάλυψη των ηλεκτρικών αναγκών (φορτίου) μιας μικρής κοινότητας. Ως περιοχή μελέτης έχει επιλεγεί η Χούλου, μια κοινότητα που βρίσκεται στην Πάφο της Κύπρου. Η Χούλου κατοικείται όλο το χρόνο. Σε αυτή τη περιοχή, κατά την τουριστική περίοδο, το καλοκαίρι, παρατηρείται απότομη αύξηση σε απαιτήσεις φορτίου. Τα δεδομένα έχουν συλλεχθεί από την Αρχή Ηλεκτρισμού Κύπρου (Α.Η.Κ.). Η μελέτη διεξήχθη αρχικά με βάση το υπάρχον εγκατεστημένο σύστημα και έπειτα για τρία εναλλακτικά σχέδια – προτάσεις που βασίζονται σε αντικατάσταση συμβατικών με ανανεώσιμες πηγές ενέργειας. Οι συνδυασμοί είναι οι εξής: α) Προϋπάρχον σύστημα (Ντίζελ), β) Φωτοβολταϊκά - Ντίζελ - Μπαταρίες, γ) Ανεμογεννήτρια - Ντίζελ - Μπαταρίες, δ) Ανεμογεννήτρια - Φωτοβολταϊκά – Μπαταρίες. Ακολούθως, παρουσιάζεται μια εκτενής αναφορά του προγράμματος HOMER Οι τρεις βασικές λειτουργίες, του προγράμματος είναι η προσομοίωση, η βελτιστοποίηση και η ανάλυση ευαισθησίας. Τα αποτελέσματα της προσομοίωσης προκύπτουν με βάση το χαμηλότερο συνολικό καθαρό κόστος (Net Present Cost - NPC). Στο τελευταίο μέρος παρουσιάζονται τα αποτελέσματα της προσομοίωσης. Τα ηλιακά και αιολικά δεδομένα της εξεταζόμενης περιοχής εισάγονται αυτόματα στο πρόγραμμα και έχουν ως πηγή πληροφοριών την NASA. Τα είδη των ανεμογεννητριών, των φωτοβολταϊκών πάνελ, των μετατροπέων, των μπαταριών και των γεννητριών καθώς και τα χρηματοοικονομικά στοιχεία που συγκεντρώθηκαν για την εκτέλεση των προσομοιώσεων προήλθαν από εταιρείες της Κύπρου. Τέλος, γίνεται μια σύγκριση μεταξύ των αποτελεσμάτων που λαμβάνονται, με στόχο την εξεύρεση του βέλτιστου συνδυασμού που θα ταιριάζει στην περιοχή, με βασικά κριτήρια το συνολικό κόστους της επένδυσης, το πλεόνασμα της ηλεκτρικής ενέργειας, την ποσότητα των ρύπων που εκπέμπονται στο περιβάλλον και την ετήσια παραγωγή της ηλεκτρικής ενέργειας σε kWh . / Nowadays there is great emphasis on building environmentally friendly electric systems by replacing the conventional energy sources with renewable. In this project, the function of various autonomous systems has been studied, to cover the electric load requirements of a small community using HOMER simulation program. Study area has been chosen Choulou, a community located in Paphos (Cyprus). The Choulou inhabited all year round. It is observed sudden increase in load requirements during the summer months due to the tourist season. Data have been collected from E.A.C. (Electricity Authority of Cyprus). The study was conducted for the existing installed system in the region as well as three alternative designs of this based on renewable energy sources. The combinations are the following: Primary installed System-Diesel System, Photovoltaic – Diesel System- Batteries, Wind Turbine- Diesel System- Batteries, Wind Turbine –Photovoltaic – Batteries Subsequently is presented an extensive report of HOMER program. The three main functions, incurred by HOMER, are the simulation, optimization and sensitivity analysis which are evidential in this work. The simulation results in this work are based on the lowest total net cost (NPC). In the last part, we present the HOMER simulations results. The solar and wind data of the area examined is granted by NASA sources and are automatically inserted in the program. The types of wind turbines, photovoltaic panels, batteries inverters and generators as well as the financial item are setted as data on the program to perform the simulations which were gathered by Cyprus companies. Finally, a comparison is made between the obtained results by the aim of finding the optimal combination of the region, with essential criteria overall the investment cost, the surplus electricity, the quantity of pollutants emitted into the environment and the annual production of electricity in kWh.