Potential of refrigerant based district heating and cooling networks

Urban areas represent an ever increasing challenge in terms of energy use and environmental impact associated with it. Projections from the United Nation expect this number to reach 66% by 2050. In Europe 40% of the final energy consumption and 36% of the emissions of greenhouse gases are caused by buildings. The building sector is also one of the area where there is a great potential of reduction of the greenhouse gases emissions and of the dependence on fossil fuels. Among the measures that can help realise this potential, efficient energy conversion technologies supplying thermal energy services could play an important role. The present thesis aims at demonstrating the potential of a new type of district network, capable of delivering indistinctly cooling and heating services using a two-pipe network and in which the transfer of energy across the network is done by exploiting the evaporation/condensation of a refrigerant. The main research question is: "Is it possible to build and operate safe, reliable, energy efficient and economically profitable district heating and cooling networks that use a refrigerant as a transfer fluid?" The demonstration followsthree axes, the first being a thermoeconomic analysis. Thisanalysis focuses on a test case area in Geneva’s city centre where 5 variants of refrigerant based district heating and cooling networks, one cold water network and the mix of conversion technologies currently in use are compared on the basis of their energy and exergy performances and on the economic profitability. Considerations on economic uncertainty, safety and technical issues are also included in the analysis. The key findings are: • All the variants of network can potentially reduce the final energy consumption of over 80% as compared to the current situation. • All the variants of network have rather similar exergy efficiencies comprised between 39.5% and 45%. • The most profitable variant uses CO2 as a transfer fluid and an open cycle CO2 heat pump at the central plant. It costs initially between 27 and 35 mio € , reaches break-even in 4 to 6 years and the net present value after 40 years is comprised between 40 and 80 mio €. • A cold water network is the second best option, although more expensive initially and thus less profitable, it has several advantages in terms of safety and availability of components. • The CO2 variants exhibit a much better compactness than the cold water network. The second axis is the design, construction and testing of a lab scale refrigerant network. First a description of the design process and of the test facility is provided. It is followed by a presentation of the results of the test campaign. The tests aimed at demonstrating the practical feasibility of the concept, mostly by assessing the controllability of the network. Overall the good behaviour of the test facility and its ability to be smoothly and automatically controlled could be demonstrated, which further improved confidence in the practicality of the concept. The third axis is the development of dynamic models of simulation. These models are described in the present manuscript. They include, heat exchangers, pipes, pumps and valves. A short comparison between experimental and simulation results is also provided. The comparison between experiment and simulation showed that at their current stage of development the models cannot simulate accurately enough a refrigerant based network.

[1]  A B Pearson,et al.  CO2 as a refrigerant , 2014 .

[2]  Daniel Favrat,et al.  Thermodynamics and Energy Systems Analysis: From Energy to Exergy , 2010 .

[3]  Leif Gustavsson,et al.  Cost and primary energy efficiency of small-scale district heating systems , 2014 .

[4]  S. Jayaraj,et al.  Environment friendly alternatives to halogenated refrigerants—A review , 2009 .

[5]  Jürg Alexander Schiffmann Integrated design, optimization and experimental investigation of a direct driven turbocompressor for domestic heat pumps , 2008 .

[6]  Marc A. Rosen,et al.  District heating and cooling: Review of technology and potential enhancements , 2012 .

[7]  André Lallemand,et al.  Comportement dynamique d'une pompe à chaleur au CO2 en cycles sous critique et transcritique. , 2007 .

[8]  W. Focke,et al.  The effect of the corrugation inclination angle on the thermohydraulic performance of plate heat exchangers , 1985 .

[9]  Vincent Lemort,et al.  Dynamic modeling and optimal control strategy of waste heat recovery Organic Rankine Cycles , 2011 .

[10]  Peter Hofer,et al.  Analyse des schweizerischen Energieverbrauchs 2000-2006 nach Verwendungszweck; ; ; , 2008 .

[11]  J. Thome,et al.  New Prediction Methods for CO2 Evaporation Inside Tubes: Part II - An Updated General Flow Boiling Heat Transfer Model Based on Flow Patterns , 2008 .

[12]  Bruno Wick L'énergie dans le bâtiment , 1987 .

[13]  Samuel Henchoz On a Multi-service, CO2 Based, District Energy System for a Better Energy Efficiency of Urban Areas , 2011 .

[14]  Jørgen Erik Christensen,et al.  Low-energy district heating in energy-efficient building areas , 2011 .

[15]  J. Thome,et al.  New prediction methods for CO2 evaporation inside tubes: Part I – A two-phase flow pattern map and a flow pattern based phenomenological model for two-phase flow frictional pressure drops , 2008 .

[16]  J. Widén,et al.  Sensitivity of district heating system operation to heat demand reductions and electricity price variations: A Swedish example , 2012 .

[17]  Norbert Jansen,et al.  PRE-INSULATED POLYMER DISTRICT HEATING PIPES : A SERVICE LIFETIME STUDY , 2006 .

[18]  André Mermoud,et al.  HCR building : Measuring cooling installations and Auditing for Deep Lake Direct Cooling Network connectivity , 2007 .

[19]  Xavier Pelet,et al.  Performances of 3.9 MWTH Ammonia Heat Pumps within a District Heating Cogeneration Power Plant: Status After Eleven Years of Operation. , 1997 .

[20]  Luc Girardin A GIS-based Methodology for the Evaluation of Integrated Energy Systems in Urban Area , 2012 .

[21]  Andrew G. Alleyne,et al.  A dynamic model of a vapor compression cycle with shut-down and start-up operations , 2010 .

[22]  E. Sciubba,et al.  Advances in exergy analysis: a novel assessment of the Extended Exergy Accounting method , 2014 .

[23]  P. G. Jolly,et al.  Distributed steady and dynamic modelling of dry-expansion evaporators , 1999 .

[24]  Vinicio Curti Modélisation et optimisation environomiques de systèmes de chauffage urbain alimentés par pompes à chaleur , 1998 .

[25]  Léda Gerber Integration of Life Cycle Assessment in the conceptual design of renewable energy conversion systems , 2012 .

[26]  Svend Svendsen,et al.  Improving the Dimensioning of Piping Networks and Network Layouts in Low-Energy District Heating Systems Connected to Low-Energy Buildings: A Case Study in Roskilde, Denmark , 2012 .

[27]  Brian Vad Mathiesen,et al.  4th Generation District Heating (4GDH) Integrating smart thermal grids into future sustainable energy systems , 2014 .

[28]  Daniel Favrat,et al.  Conventional and advanced district energy systems , 2007 .

[29]  Daniel Favrat,et al.  Thermoeconomic analysis of a solar enhanced energy storage concept based on thermodynamic cycles , 2012 .

[30]  J. O. Lewis,et al.  Cities of Tomorrow – Action Today. URBACT II Capitalisation. Building energy efficiency in European cities , 2013 .

[31]  Didier Houssin,et al.  Linking heat and electricity systems: Co-generation and District Heating and Cooling Solutions for a Clean Energy Future (Introductory Webinar Slides) , 2014 .

[32]  Christophe Nicolet,et al.  Hydroacoustic modelling and numerical simulation of unsteady operation of hydroelectric systems , 2007 .

[33]  M. Mourshed Relationship between annual mean temperature and degree-days , 2012 .

[34]  Yang Zhao,et al.  Retrofits and options for the alternatives to HCFC-22 , 2013 .

[35]  Junqiang Fan,et al.  Dynamic Modeling of CO2 Supermarket Refrigeration System , 2010 .

[36]  Stig Hammarsten,et al.  A critical appraisal of energy-signature models , 1987 .

[37]  Zhen Lu,et al.  Dynamic modeling and simulation of an Organic Rankine Cycle (ORC) system for waste heat recovery , 2008 .

[38]  Henrik Lund,et al.  A renewable energy system in Frederikshavn using low-temperature geothermal energy for district heating , 2011 .

[39]  Shuangquan Shao,et al.  Dynamic simulation of variable capacity refrigeration systems under abnormal conditions , 2010 .

[40]  Pierre-Alain Viquerat,et al.  Utilisation des réseaux d'eau lacustre profonde pour la climatisation et le chauffage des bâtiments; bilan énergétique et impacts environnementaux: Etude de cas: le projet GLN (Genève-Lac-Nations) à Genève , 2012 .

[41]  Céline Isabelle Weber,et al.  Multi-objective design and optimization of district energy systems including polygeneration energy conversion technologies , 2008 .

[42]  François Maréchal,et al.  Key Energy and Technological Aspects of Three Innovative Concepts of District Energy Networks , 2016 .

[43]  I Chaer,et al.  Refrigerant emissions and leakage prevention across Europe - Results from the RealSkillsEurope project , 2012 .

[44]  Daniel Favrat,et al.  Performance and profitability perspectives of a CO2 based district energy network in Geneva's City Centre , 2012 .

[45]  R. Longchamp Commande numérique de systèmes dynamiques , 1995 .

[46]  Sebastian Herkel,et al.  Power Generation Using District Heat: Energy Efficient Retrofitted Plus-energy School Rostock☆ , 2014 .

[47]  Yan Li,et al.  A new type of district heating system based on distributed absorption heat pumps , 2011 .