matthias schmidt , christian roßkopf, marc linder, antje wörner

17
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 www.DLR.de Chart 1

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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. Content. Introduction to thermochemical energy storage based on CaO / Ca (OH) 2 Material properties - PowerPoint PPT Presentation

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Page 1: 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

www.DLR.de • Chart 1

Page 2: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 2

Page 3: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

Thermochemical Heat Storage reaction system CaO/Ca(OH)2

- Loss free storage of chemical potential

- Adjustable storage temperature

- Possibility of heat transformation

www.DLR.de • Chart 3

CaO(s) + H2O(g) ⇌ Ca(OH)2(s) + ΔH

endotherm

exotherm

1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.70.001

0.01

0.1

1

10

Temperatur 1000 / T [1/K]

pga

s [b

ar]

Ca(OH)2(s)

CaO(s)

636727 560 496 441 394 352 315

Temperature [°C]

H2O(g)

H2O(g)

Page 4: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

From a reaction system to a heat storage systemoperation principle

www.DLR.de • Chart 4

Reactor DesignGashandling

Process integration:

ReactionMaterial

Properties

Page 5: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

Material Properties - CaO/Ca(OH)2

www.DLR.de • Chart 5

Thermophysical properties:

- Fine powder (d50 ~ 5 µm)

- low permeability

- Low thermal conductivity (0.1 – 0.4 W/mK)

F. Schaube et al., Thermochimica Acta, 2012

Ca(OH)2 (4 Cycl) commerical available Ca(OH)2

Chemical properties:

- Reversible reaction (400-600°C)

- Sufficiently fast rates of reaction

- No chemical degradation observed

Page 6: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 6

Source: DEG Eingineering

Page 7: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

Reaction Gas Handlingvapor pressure holder(10mbar – 3bar)

www.DLR.de • Chart 7

Page 8: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 8

Page 9: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 9

Page 10: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 10

Page 11: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 11

M. Schmidt et al., Applied Thermal Energy 62 (2014)

Page 12: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 12

M. Schmidt et al., Applied Thermal Energy 62 (2014)

Page 13: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

0.00 50.00 100.00 150.00 200.00 250.00 300.00 350.00 400.00250

300

350

400

450

500

550

600

0.00

0.10

0.20

0.30

0.40

0.50

0.60

0.70

0.80

0.90

1.00

T_air_outlet

T_air_inlet

Conversion

Time [min]

Tem

per

atu

re [

°C]

Co

nve

rsio

n

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

www.DLR.de • Chart 13

Page 14: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

0.00 20.00 40.00 60.00 80.00 100.00 120.00 140.00 160.00 180.00 200.00300

350

400

450

500

550

T_air_inlet

T_R_01

T_R_05

T_R_11

T_R_13

time [min]

Tem

per

atu

re [

°C]

Buffer Storage Modedroping inlet temperature, hydration of CaO at 1 bar vapor

www.DLR.de • Chart 14

Tequilibrium = 490°C@ (ph2O ~ 1bar)

Page 15: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

Heat Generation ModeHydration of CaO, starting temperature of 350°C

www.DLR.de • Chart 15

0.00 50.00 100.00 150.00 200.00 250.00330

350

370

390

410

430

450

470

490

0.00

0.10

0.20

0.30

0.40

0.50

0.60

0.70

0.80

0.90

1.00

T_air_inlet

T_air_outlet

Conversion

time [min]

Tem

per

atu

re [

°C]

Co

nve

rsio

n

Page 16: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

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

www.DLR.de • Chart 16

Page 17: Matthias Schmidt , Christian Roßkopf, Marc Linder, Antje Wörner

Thank you!

Matthias SchmidtGerman Aerospace Center (DLR)Institute of Technical Thermodynamics

[email protected]

www.DLR.de • Chart 17