Thermal Energy Storage Developing for a Decarbonized Society
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Thermal Storage Impact on CHP Cogeneration Performance with Southwoods Case Study Edmonton, Alberta Michael Roppelt C.E.T
Thermal Storage Impact on CHP Cogeneration Performance with Southwoods Case Study Edmonton, Alberta Michael Roppelt C.E.T. CHP Cogeneration Solar PV Solar Thermal Grid Supply Thermal Storage GeoExchange RenewableAlternative & LowEnergy Carbon Microgrid Hybrid ConventionalSystemSystem System Optional Solar Thermal Option al Solar PV CNG & BUILDING OR Refueling COMMUNITY Station CHP Cogeneration SCALE 8 DEVELOPMENT Hot Water Hot Water DHW Space Heating $ SAVINGS GHG OPERATING Thermal Energy Cool Water Exchange & Storage ElectricalMicro Micro-Grid-Grid Thermal Microgrid Moving Energy not Wasting Energy Natural Gas Combined Heat and Power (CHP) Cogeneration $350,000 2,500,000 kWh RETAILINPUT OUTPUT VALUE NATURAL GAS $400,000. $100,000.30,000 Gj (85% Efficiency) CHP $50,000 Cogeneration15,000 Energy Gj Technologies CHP Unit Sizing Poorly sized units will not perform optimally which will cancel out the benefits. • For optimal efficiency, CHP units should be designed to provide baseline electrical or thermal output. • A plant needs to operate as many hours as possible, since idle plants produce no benefits. • CHP units have the ability to modulate, or change their output in order to meet fluctuating demand. Meeting Electric Power Demand Energy Production Profile 700 Hourly Average 600 353 January 342 February 500 333 March 324 April 400 345 May 300 369 June 400 July 200 402 August 348 September 100 358 October 0 362 November 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 Meeting Heat Demand with CHP Cogeneration Energy Production Profile Heat Demand (kWh) Electric Demand (kWh) Cogen Heat (kWh) Waste Heat Heat Shortfall Useable Heat CHP Performance INEFFICIENCY 15% SPACE HEATING DAILY AND HEAT 35% SEASONAL ELECTRICAL 50% IMBALANCE 35% 50% DHW 15% Industry Studies The IEA works to ensure reliable, affordable and clean energy for its 30 member countries and beyond. -
HEAT and TEMPERATURE Heat Is a Type of ENERGY. When Absorbed
HEAT AND TEMPERATURE Heat is a type of ENERGY. When absorbed by a substance, heat causes inter-particle bonds to weaken and break which leads to a change of state (solid to liquid for example). Heat causing a phase change is NOT sufficient to cause an increase in temperature. Heat also causes an increase of kinetic energy (motion, friction) of the particles in a substance. This WILL cause an increase in TEMPERATURE. Temperature is NOT energy, only a measure of KINETIC ENERGY The reason why there is no change in temperature at a phase change is because the substance is using the heat only to change the way the particles interact (“stick together”). There is no increase in the particle motion and hence no rise in temperature. THERMAL ENERGY is one type of INTERNAL ENERGY possessed by an object. It is the KINETIC ENERGY component of the object’s internal energy. When thermal energy is transferred from a hot to a cold body, the term HEAT is used to describe the transferred energy. The hot body will decrease in temperature and hence in thermal energy. The cold body will increase in temperature and hence in thermal energy. Temperature Scales: The K scale is the absolute temperature scale. The lowest K temperature, 0 K, is absolute zero, the temperature at which an object possesses no thermal energy. The Celsius scale is based upon the melting point and boiling point of water at 1 atm pressure (0, 100o C) K = oC + 273.13 UNITS OF HEAT ENERGY The unit of heat energy we will use in this lesson is called the JOULE (J). -
A Comprehensive Review of Thermal Energy Storage
sustainability Review A Comprehensive Review of Thermal Energy Storage Ioan Sarbu * ID and Calin Sebarchievici Department of Building Services Engineering, Polytechnic University of Timisoara, Piata Victoriei, No. 2A, 300006 Timisoara, Romania; [email protected] * Correspondence: [email protected]; Tel.: +40-256-403-991; Fax: +40-256-403-987 Received: 7 December 2017; Accepted: 10 January 2018; Published: 14 January 2018 Abstract: Thermal energy storage (TES) is a technology that stocks thermal energy by heating or cooling a storage medium so that the stored energy can be used at a later time for heating and cooling applications and power generation. TES systems are used particularly in buildings and in industrial processes. This paper is focused on TES technologies that provide a way of valorizing solar heat and reducing the energy demand of buildings. The principles of several energy storage methods and calculation of storage capacities are described. Sensible heat storage technologies, including water tank, underground, and packed-bed storage methods, are briefly reviewed. Additionally, latent-heat storage systems associated with phase-change materials for use in solar heating/cooling of buildings, solar water heating, heat-pump systems, and concentrating solar power plants as well as thermo-chemical storage are discussed. Finally, cool thermal energy storage is also briefly reviewed and outstanding information on the performance and costs of TES systems are included. Keywords: storage system; phase-change materials; chemical storage; cold storage; performance 1. Introduction Recent projections predict that the primary energy consumption will rise by 48% in 2040 [1]. On the other hand, the depletion of fossil resources in addition to their negative impact on the environment has accelerated the shift toward sustainable energy sources. -
IB Questionbank
Topic 3 Past Paper [94 marks] This question is about thermal energy transfer. A hot piece of iron is placed into a container of cold water. After a time the iron and water reach thermal equilibrium. The heat capacity of the container is negligible. specific heat capacity. [2 marks] 1a. Define Markscheme the energy required to change the temperature (of a substance) by 1K/°C/unit degree; of mass 1 kg / per unit mass; [5 marks] 1b. The following data are available. Mass of water = 0.35 kg Mass of iron = 0.58 kg Specific heat capacity of water = 4200 J kg–1K–1 Initial temperature of water = 20°C Final temperature of water = 44°C Initial temperature of iron = 180°C (i) Determine the specific heat capacity of iron. (ii) Explain why the value calculated in (b)(i) is likely to be different from the accepted value. Markscheme (i) use of mcΔT; 0.58×c×[180-44]=0.35×4200×[44-20]; c=447Jkg-1K-1≈450Jkg-1K-1; (ii) energy would be given off to surroundings/environment / energy would be absorbed by container / energy would be given off through vaporization of water; hence final temperature would be less; hence measured value of (specific) heat capacity (of iron) would be higher; This question is in two parts. Part 1 is about ideal gases and specific heat capacity. Part 2 is about simple harmonic motion and waves. Part 1 Ideal gases and specific heat capacity State assumptions of the kinetic model of an ideal gas. [2 marks] 2a. two Markscheme point molecules / negligible volume; no forces between molecules except during contact; motion/distribution is random; elastic collisions / no energy lost; obey Newton’s laws of motion; collision in zero time; gravity is ignored; [4 marks] 2b. -
Thermal Energy: Using Water to Heat a School
Thermal Energy: Using Water to Heat a School Investigation Notebook NYC Edition © 2018 by The Regents of the University of California. All rights reserved. No part of this publication may be reproduced or transmitted in any form or by any means, electronic or mechanical, including photocopy, recording, or any information storage or retrieval system, without permission in writing from the publisher. Teachers purchasing this Investigation Notebook as part of a kit may reproduce the book herein in sufficient quantities for classroom use only and not for resale. These materials are based upon work partially supported by the National Science Foundation under grant numbers DRL-1119584, DRL-1417939, ESI-0242733, ESI-0628272, ESI-0822119. The Federal Government has certain rights in this material. Any opinions, findings, and conclusions or recommendations expressed in this material are those of the author(s) and do not necessarily reflect the views of the National Science Foundation. These materials are based upon work partially supported by the Institute of Education Sciences, U.S. Department of Education, through Grant R305A130610 to The Regents of the University of California. The opinions expressed are those of the authors and do not represent views of the Institute or the U.S. Department of Education. Developed by the Learning Design Group at the University of California, Berkeley’s Lawrence Hall of Science. Amplify. 55 Washington Street, Suite 800 Brooklyn, NY 11201 1-800-823-1969 www.amplify.com Thermal Energy: Using Water to Heat a School -
Quenching & Tempering Salts
Park Thermal International (1996) Corporation 62 Todd Road, Georgetown, Ontario L7G 4R7 Tel: (905) 877-5254 Fax: (905) 877-6205 Toll Free: (877) 834-4328 Email: [email protected] www.parkthermal.com HEAT TREATING SALTS AND QUENCHANTS Molten Salt Bath Technology is recognized as a superior process for heat treating a variety of metals. Salt Bath Technology offers a variety of benefits such as uniform heat transfer, rapid heating, safety, automation, accurate control and versatility. Park Thermal International offers a complete line of salts and salt bath equipment for virtually any application. Our list includes Neutral Salts, High Speed Steel Hardening Salts, Quenching and Tempering Salts, Aluminum Heat Treat and Brazing Salts, Rubber Curing Salts, Heat Transfer Salts, Stripping, Cleaning and Descaling Salts QUENCHING & TEMPERING SALTS A. QUENCH SALTS Iso-Therm 135 is a eutectic nitrate-nitrite salt mixture that is used for the interrupted or isothermal quenching of austenitized steels (Austempering, Martempering, Marquenching etc.). Iso-Therm 135 can also be used for tempering or drawing hardened steels. Melt Point 135°C (275°F); Working Range 149-593°C (300-1,100°F). Iso-Therm 142 is a eutectic nitrate-nitrite salt mixture that is used for the interrupted or isothermal quenching of austenitized steels (Austempering, Martempering, Marquenching etc.). Iso-Therm 142 can also be used for tempering or drawing hardened steels. Melt Point 142°C (290°F); Working Range 163-593°C (325-1,100°F). Iso-Therm 146 is a eutectic nitrate-nitrite salt mixture that is used for the interrupted or isothermal quenching of austenitized steels (Austempering, Martempering, Marquenching etc.). -
Thermal Profiling of Residential Energy Consumption
1 Thermal profiling of residential energy consumption Adrian Albert and Ram Rajagopal Abstract—Demand Response (DR) programs aim to dynami- the thermal mass of the premise may act as “thermal bat- cally match consumption on the grid with available supply in tery”. Affecting the thermally-sensitive load may be typically real-time. Understanding the patterns in demand of individuals achieved through direct load control of the HVAC system (e.g., is now being facilitated by granular consumption data collected load curtailment or automatic adjustment of the thermostat via smart meter sensors that power utility companies have rolled setpoint), through adjustable rates (e.g., critical peak pricing), out at scale. In this paper we propose a dynamic model that uses or through incentive schemes [4], [5]. hourly electricity and weather readings to characterize residential users’ thermally-sensitive consumption. From this model we Here we propose a simple model of consumption for a extract useful benchmarks to build profiles of individual users residential premise that is driven by unobserved “occupancy for use with DR programs that focus on temperature-dependent states” that have different responses to ambient weather. These consumption such as air conditioning or heating. We present are consumption regimes of a given household that depend on example profiles generated using our model on real consumers, lifestyle (work schedule, familial composition etc.), premise and show its performance on a large sample of residential characteristics (heating/cooling mass, square footage etc.), users. We then compute metrics that allow us to segment the appliance stock, and weather patterns. It is a daunting task population dynamically for the purpose of a thermally-motivated to disentangle how much energy each of these components DR program. -
Introducing Electric Thermal Energy Storage (ETES) – Putting Gigawatt Hours of Energy at Your Command
Same forces. New rules. Introducing Electric Thermal Energy Storage (ETES) – putting gigawatt hours of energy at your command. Impossible is just another word for never done before. 100% renewables is said to be impossible. As were the first flight, space travel, the internet … Now here is something that makes a complete energy transition possible: Electric Thermal Energy Storage (ETES). A proven energy storage solution that is inexpensive, built with 80% off-the-shelf components, and scalable to several GWh. No need to explain that ETES is a giant step – for SGRE and for the energy industry. While the forces of nature remain the same, Electric Thermal Energy Storage has launched a new era. Find out how it will boost the energy transition and how new players, energy-intensive companies and even conventional power plants will profit from it. Or, in short: time for new rules. Welcome TiteltextRule #1: Power in. Power out. ETES is technology that can be charged with electricity or directly with heat and which then releases heat that, in return, can generate electricity. Unlike other storage technologies, it is made of rocks absorbing heat. This makes ETES very sustainable in design and the first gigawatt-hour scale energy storage that can be built almost anywhere – limiting its size and use only to your imagination. Flexible scalability of charging power, discharging power and storage capacity. Proven, reliable technology – discharging technology used for more than a 100 years. Cost-competitive, GWh scale, multiple revenue streams. ETES technology TiteltextRule #2: If it works for you, it works for all. ETES solutions basically prolong the availability of ETES and all of its components are fully scalable energy that otherwise would be “wasted“. -
Molten Salt Chemistry Workshop
The cover depicts the chemical and physical complexity of the various species and interfaces within a molten salt reactor. To advance new approaches to molten salt technology development, it is necessary to understand and predict the chemical and physical properties of molten salts under extreme environments; understand their ability to coordinate fissile materials, fertile materials, and fission products; and understand their interfacial reactions with the reactor materials. Modern x-ray and neutron scattering tools and spectroscopy and electrochemical methods can be coupled with advanced computational modeling tools using high performance computing to provide new insights and predictive understanding of the structure, dynamics, and properties of molten salts over a broad range of length and time scales needed for phenomenological understanding. The actual image is a snapshot from an ab initio molecular dynamics simulation of graphene- organic electrolyte interactions. Image courtesy of Bobby G. Sumpter of ORNL. Molten Salt Chemistry Workshop Report for the US Department of Energy, Office of Nuclear Energy Workshop Molten Salt Chemistry Workshop Technology and Applied R&D Needs for Molten Salt Chemistry April 10–12, 2017 Oak Ridge National Laboratory Co-chairs: David F. Williams, Oak Ridge National Laboratory Phillip F. Britt, Oak Ridge National Laboratory Working Group Co-chairs Working Group 1: Physical Chemistry and Salt Properties Alexa Navrotsky, University of California–Davis Mark Williamson, Argonne National Laboratory Working -
Lesson 8 Energy in Chemical Reactions Review
Name __________________________________________________ Date ______________________________ Lesson 8 Energy in Chemical Reactions Review Main Ideas Read each item. Then select the letter next to the best answer. 1. An ice pack is activated and placed on a person’s wrist. After the resulting chemical reaction, the average temperature of the hands-icepack system is lower. Which of the following statements best completes a statement about the transfer of energy in this chemical reaction. This reaction is: A. endothermic, because more thermal energy is absorbed than released. B. endothermic, because more thermal energy is released than absorbed. C. exothermic, because more thermal energy is absorbed than released. D. exothermic, because more thermal energy is released than absorbed. 2. Calcium ammonium nitrate is a chemical used in fertilizers. It can also be used to make an instant ice-pack. When the calcium ammonium nitrate is allowed to mix with the water inside the ice pack, a chemical reaction takes place. This reaction cannot occur on its own because it needs a source of heat to continue until it is complete. Which statement best describes the type of chemical reaction and the source of heat? A. Endothermic reaction, and the heat comes out of the water. B. Exothermic reaction, and the heat comes out of the water. C. Exothermic reaction, and the heat comes out of the reaction. D. Endothermic reaction, and the heat comes out of the reaction. 3. When a candle burns, a chemical reaction occurs changing wax and oxygen into carbon dioxide and water vapor. The average temperature of the candle-room system increases. -
Energy Storage Analysis
Energy Storage Analysis Chad Hunter, Evan Reznicek, Michael Penev, Josh Eichman, Sam Baldwin National Renewable Energy Laboratory Thursday, May 21, 2020 DOE Hydrogen and Fuel Cells Program 2020 Annual Merit Review and Peer Evaluation Meeting Project ID SA173 This presentation does not contain any proprietary, confidential, or otherwise restricted information. Overview: Hydrogen grid energy storage analysis Timeline Barriers (4.5) Start: October 2019 A. Future Market Behavior End: June 2020 • Assessing competitiveness of hydrogen for grid storage C. Inconsistent Data, Assumptions & Guidelines 50% complete • Consistent modeling methodology using established DOE cost/price and performance targets D. Insufficient Suite of Models and Tools • Develop hydrogen grid storage techno-economic tool Budget Partners Total Project Funding: $155k Project Management EERE Strategic Priorities and Impacts Analysis (SPIA) • FY20: $155k Collaborators and Peer Reviewers (alphabetical) Total DOE funds received to Ballard, Bioenergy Technology Office, Fossil Energy, NREL (Paul Denholm, Wesley Cole), Office of date: $50k Electricity, Solar Energy Technology Office, Water Power Technology Office NREL | 2 Relevance (1/3): HFTO Systems Analysis Framework Hydrogen Grid Energy Storage Analysis • H2@Scale • DOE Fuel Cell • SPIA/HFTO hydrogen Technologies Office Integrates System Analysis Framework: energy storage • DOE Strategic • ANL bulk hydrogen Priorities and • Leverages and expands existing storage analysis Impacts Analysis systems analysis models • PNNL hydrogen -
Grid Energy Storage
Grid Energy Storage U.S. Department of Energy December 2013 Acknowledgements We would like to acknowledge the members of the core team dedicated to developing this report on grid energy storage: Imre Gyuk (OE), Mark Johnson (ARPA-E), John Vetrano (Office of Science), Kevin Lynn (EERE), William Parks (OE), Rachna Handa (OE), Landis Kannberg (PNNL), Sean Hearne & Karen Waldrip (SNL), Ralph Braccio (Booz Allen Hamilton). Table of Contents Acknowledgements ....................................................................................................................................... 1 Executive Summary ....................................................................................................................................... 4 1.0 Introduction .......................................................................................................................................... 7 2.0 State of Energy Storage in US and Abroad .......................................................................................... 11 3.0 Grid Scale Energy Storage Applications .............................................................................................. 20 4.0 Summary of Key Barriers ..................................................................................................................... 30 5.0Energy Storage Strategic Goals .......................................................................................................... 32 6.0 Implementation of its Goals ...............................................................................................................