Matthias Schmidt, Christian Roßkopf, Marc Linder, Antje Wörner

Slides:



Advertisements
Similar presentations
CHAPTER 9 Water and Solutions 9.3 Properties of Solutions.
Advertisements

Slide 1 Insert your own content. Slide 2 Insert your own content.
1 Chapter 6 EnergyThermodynamics. 2 Energy is... n The ability to do work. n Conserved. n made of heat and work. n a state function. n independent of.
Specific heat capacity (a.k.a. Specific heat)
Chapter 8 Exergy: A Measure of Work Potential Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 7th edition by Yunus.
By D. Fisher Geometric Transformations. Reflection, Rotation, or Translation 1.
Ch 17 Thermochemistry.
Round 2! Double Jeopardy Calorim- etry Energy Changes in Heat Vocab Thermo Fun FJ.
Chemistry 5.12 Spri ng 2003, Week 3 / Day 2 Handout #7: Lecture 11 Outline IX. Free Radical Reactions (Read Chapter 4) A. Chlorination of Methane (4-2)
1 Environmentally friendly technology for municipal solid waste gasification From Science to Business October 2006 Kyiv Georgiy Geletukha t./fax:
Jeopardy Q 1 Q 6 Q 11 Q 16 Q 21 Q 2 Q 7 Q 12 Q 17 Q 22 Q 3 Q 8 Q 13
Jeopardy Q 1 Q 6 Q 11 Q 16 Q 21 Q 2 Q 7 Q 12 Q 17 Q 22 Q 3 Q 8 Q 13
0 - 0.
$1 Million $500,000 $250,000 $125,000 $64,000 $32,000 $16,000 $8,000 $4,000 $2,000 $1,000 $500 $300 $200 $100 Welcome.
$1 Million $500,000 $250,000 $125,000 $64,000 $32,000 $16,000 $8,000 $4,000 $2,000 $1,000 $500 $300 $200 $100 Welcome.
Chemistry I Honors Chapter 17 Notes.
ALGEBRAIC EXPRESSIONS
DIVIDING INTEGERS 1. IF THE SIGNS ARE THE SAME THE ANSWER IS POSITIVE 2. IF THE SIGNS ARE DIFFERENT THE ANSWER IS NEGATIVE.
MULTIPLYING MONOMIALS TIMES POLYNOMIALS (DISTRIBUTIVE PROPERTY)
SUBTRACTING INTEGERS 1. CHANGE THE SUBTRACTION SIGN TO ADDITION
MULT. INTEGERS 1. IF THE SIGNS ARE THE SAME THE ANSWER IS POSITIVE 2. IF THE SIGNS ARE DIFFERENT THE ANSWER IS NEGATIVE.
FACTORING Think Distributive property backwards Work down, Show all steps ax + ay = a(x + y)
Addition Facts
Year 6 mental test 10 second questions Numbers and number system Numbers and the number system, fractions, decimals, proportion & probability.
Biochar Properties & Production Techniques
Chart 1> IRES 2012> Breuer > Development of a solar driven tube receiver to superheat steam for the high temperature electrolysis.
SPD cooling Test bench Preliminary results CERN (Geneva) A.Francescon Università & INFN Padova 1.
EGR 334 Thermodynamics Chapter 3: Section 12-14
Air Conditioners.
Chapter 8 EXERGY: A MEASURE OF WORK POTENTIAL
Markku Lappalainen Aalto University Energy and Ecology in Finland.
Kinetics ; 13.11; December Assigned HW 13.22, 13.24, 13.26, 13.34, 13.36, 13.58, Due: Monday 6-Dec Lecture 33 1.
EGR 334 Thermodynamics Chapter 12: Sections 5-7
* Reading Assignments:
1 POLYGENERATION OF ELECTRICITY, HEAT and ULTRA PURE WATER for SEMICONDUCTOR INDUSTRY Chuanfeng Liu Supervisors: Andrew Martin EGI KTH Aapo Sääsk Xzero.
Chapter 6 Reaction Equilibrium in Ideal Gas Mixtures Physical Chemistry Chapter 6.
Reaction Equilibrium in Ideal Gas Mixture
Bolland Hybrid power production systems – integrated solutions Olav Bolland Professor Norwegian University of Science and Technology (NTNU) KIFEE-Symposium,
O X Click on Number next to person for a question.
Take from Ten First Subtraction Strategy -9 Click on a number below to go directly to that type of subtraction problems
Chemistry 17.2.
Le Châtelier.
Energy & Green Urbanism Markku Lappalainen Aalto University.
Chemical Systems and Equilibrium
Lets play bingo!!. Calculate: MEAN Calculate: MEDIAN
Past Tense Probe. Past Tense Probe Past Tense Probe – Practice 1.
Chapter 19 Principles of Reactivity: Entropy & Free Energy
Summary of Transport Application of the SRA draft, version December 2004 H2/FC TP SRA - Transport Applications Applications Fuel Cell System Technical.
Addition 1’s to 20.
25 seconds left…...
Test B, 100 Subtraction Facts
Kinetics (Reaction Rate)
11 = This is the fact family. You say: 8+3=11 and 3+8=11
EnvironmentEnvironnementCanada Nusa Dua, Bali, Indonesia September 5 – 7, Part 4: LFG Utilization.
EGR 334 Thermodynamics Chapter 4: Section 4-5
Week 1.
We will resume in: 25 Minutes.
Chapter 6 Thermochemistry John A. Schreifels Chemistry 211.
1 Unit 1 Kinematics Chapter 1 Day
Philip Dutton University of Windsor, Canada N9B 3P4 Prentice-Hall © 2002 General Chemistry Principles and Modern Applications Petrucci Harwood Herring.
Making Clean Local Energy Accessible Now December 16, 2013 Flattening the Duck Dynamic Grid Solutions for Integrating Renewables.
1 Chapter 2Energy and Matter 2.6 Changes of State Copyright © 2005 by Pearson Education, Inc. Publishing as Benjamin Cummings.
Lecture 36 Combustion Reactions.
DYNAMIC SIMULATION OF RESIDENTIAL BUILDINGS WITH SORPTION STORAGE OF SOLAR ENERGY – PARAMETRIC ANALYSIS ISES Solar World Congress Kassel (Germany.
E. Smith. Calorimetry The accurate and precise measurement of heat change for chemical and physical processes. Calorimeter An insulated device used to.
Thermochemistry Study of energy transformations and transfers that accompany chemical and physical changes. Terminology System Surroundings Heat (q) transfer.
Folie 1 ICEPAG 2012 > Leucht > Hydrogen Rich Natural Gas as a Fuel for SOFC Systems Florian Leucht, Moritz Henke, Caroline Willich, Christina.
Chemistry 100 Enthalpy and Hess’s Law. Energy Changes in Chemical Reactions Let’s take a typical reaction CH 4 (g) + O 2 (g)  CO 2 (g) + 2 H 2 O (l)
Dynamic modelling of adiabatic compressed air energy storage using packed bed thermal energy storage Wei He and Jihong Wang School of Engineering, University.
Knowledge Organiser – Energy Changes
Presentation transcript:

Matthias Schmidt, Christian Roßkopf, Marc Linder, Antje Wörner High Temperature Thermochemical Heat Storage: Operation Modes of a 10kW Pilot Reactor based on CaO/Ca(OH)2 Matthias Schmidt, Christian Roßkopf, Marc Linder, Antje Wörner Welcome ladies and gentleman I know it has been a long day already and iam giving the last talk… we´ve all heard a lot it’s a big challenge since we are all working in energy research conference dinner Still hold on for 20 min Interesting results of our ongoing experimentals with a pilot thermochemical heat storage reactor

Content Introduction to thermochemical energy storage based on CaO/ Ca(OH)2 Material properties Reactor design and test bench development Experimental results of different operation modes Summary and outlook

Thermochemical Heat Storage reaction system CaO/Ca(OH)2 636 727 560 496 441 394 352 315 Temperature [°C] Ca(OH)2(s) exotherm H2O(g) CaO(s) + H2O(g) ⇌ Ca(OH)2(s) + ΔH H2O(g) CaO(s) endotherm Loss free storage of chemical potential Adjustable storage temperature Possibility of heat transformation A gas solid reaction is always characterized through it´s Van´t Hoff plot Left y-axis is the pressure of my reaction gas, in case of the calciumhydroxide system water vapor Top x-axis the temperatur at which I need to supply or release heat

From a reaction system to a heat storage system operation principle Process integration: Gashandling Reactor Design Reaction Material Properties

Material Properties - CaO/Ca(OH)2 Chemical properties: Reversible reaction (400-600°C) Sufficiently fast rates of reaction No chemical degradation observed F. Schaube et al., Thermochimica Acta, 2012 Thermophysical properties: Fine powder (d50 ~ 5 µm) low permeability Low thermal conductivity (0.1 – 0.4 W/mK) commerical available Ca(OH)2 Ca(OH)2 (4 Cycl)

Pilot Reactor Design (10kW; 25 kg Ca(OH)2) indirectly operated fixed bed Source: DEG Eingineering

Reaction Gas Handling vapor pressure holder(10mbar – 3bar)

Multifunctional Pilot Plant overall experimental set up for CaO/Ca(OH)2 reactor

Multifunctional Pilot Plant overall experimental set up for CaO/Ca(OH)2 reactor

Multifunctional Pilot Plant overall experimental set up for CaO/Ca(OH)2 reactor

Multifunctional Pilot Plant overall experimental set up for CaO/Ca(OH)2 reactor M. Schmidt et al., Applied Thermal Energy 62 (2014)

Multifunctional Pilot Plant overall experimental set up for CaO/ Ca(OH)2 reactor M. Schmidt et al., Applied Thermal Energy 62 (2014)

Charging Mode dehydration of Ca(OH)2 at ph2O = 100mbar

Buffer Storage Mode droping inlet temperature, hydration of CaO at 1 bar vapor Tequilibrium = 490°C @ (ph2O ~ 1bar)

Heat Generation Mode Hydration of CaO, starting temperature of 350°C Cold - Start Up If you think about a sensible or latent heat storage system the only possibility to get heat our of the system would be to lower the air inlet temperature What we do is, we trigger ther chemical reaction through the supply of water vapor and therefore we can immediately increase our air outlet temperature This is what we call heat generation, and is an outstanding advantage of a TCS-System since such a heat generation mode can be very useful if you think about start up procedures in different applications.

Summary and Outlook CaO / Ca(OH)2 combines low material costs with high storage density Reactor for 25kg (10 kWh) and 10 kW in operation Charging at temperatures >400°C demonstrated Discharging at adjustable temperatures (400-600°C) and in different operation modes possible Development of integration strategies (CSP and other applications) Performance evaluation through system modeling Material modifications to improve conveyance

Thank you! Matthias Schmidt German Aerospace Center (DLR) Institute of Technical Thermodynamics matthias.schmidt@dlr.de www.DLR.de Thanks to the european comission which partially founded this work through within the project tcs power and thank you especially for your questions