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Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed C. Rokopf, M. Haas, M. Linder, A. Wrner German Aerospace Center (DLR), Stuttgart, Germany www.DLR.de Slide 2 > 7 th World


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SLIDE 1

Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed

  • C. Roßkopf, M. Haas, M. Linder, A. Wörner

German Aerospace Center (DLR), Stuttgart, Germany

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SLIDE 2

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 2

Thermochemical Heat Storage

Application & Potential Application:

  • Storage of industrial waste heat
  • Reduction of energy generation cost
  • Base load capability of renewable energy systems

Potential:

  • High storage densities
  • Long-term and loss-free storage
  • Heat release at any time
  • Possibility of heat transformation
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SLIDE 3

Thermochemical Heat Storage

Reaction System Reversible Gas-Solid-Reaction:

CaO(s) + H2O(g) ⇌ Ca(OH)2(s) + 99,5 kJ/mol

Temperature range ~ 400-700 °C

Main advantage: Low price (55-65 € / ton)

  • Poor thermal conductivity and permeability of CaO/Ca(OH)2

High demand on reactor geometry leads to high costs Adjustment of reactor to required power Supply of capacity in cheap tanks

Material flow through the reactor is essential!

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 3

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SLIDE 4

Motivation

Separation of Power and Capacity

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 4

H2O(g) Heat transfer fluid Heat transfer fluid Process integration

CaO(s) / Ca(OH)2(s)

Heat transfer fluid Heat transfer fluid Process integration

CaO(s) / Ca(OH)2(s) CaO(s) / Ca(OH)2(s)

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SLIDE 5

Challenge

Poor Powder Properties

Low thermal conductivity vs Poor flowability

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 5

HTF HTF Reaction Bed Heat Flux Heat Conduction vReaction Bed

Plate heat exchanger

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SLIDE 6

Approaches

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 6

Pellets unstabile during cycling Increasing the roughness of particle surface

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SLIDE 7

Modification of Material

Increasing the Roughness of Surface

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 7

Extension of Van-der-Waals Eq. : 𝐺

𝑊𝑊𝑊 = 𝐷𝐼 6 𝑆∙𝑠 𝑏2(𝑆+𝑠) + 𝑆2 (2𝑏𝑄)2∙2𝑆

 Increasing of the roughness of the surface

and distance between the particles by addition of nano particles

State of the art:

  • 1 Improving powder flowability in bulk and pharmaceutical industries
  • 2 Combination of nano particle agglomerates with CaO to improve fluidization

behavior for CO2 adsorption

Coating of Ca(OH)2 by nano particles in order to improve flowability is uninvestigated

R R α x0 x0 r x1 2h

1 K.Köpker et al., Application of nano particles, Landesanstalt für Umwelt, Messungen und Naturschutz Baden-Wuerttemberg,2007 2 Pontiga et. al, Dry fas-solid carbonation in fludized beds of Ca(OH)2 and nanosilica/Ca(OH)2 at ambient temperature and low CO2 pressure, Chemical Engineering Journal, 2013

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SLIDE 8

Dry particle coating

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 8

Ca(OH)2 + 0,5 - 15% Aerosil 300

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SLIDE 9

Results of Material Modification

Effects of Variable Power Inputs

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 9

1000 2000 3000 4000 5000 6000 7000 1500 2000 2500 3000

Compressive strength (σ1=6000) / N/m² Mixing intensity / U/min Aerosil 300 2% Aerosil 300 6% Aerosil 300 11%

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SLIDE 10

Cycling stability

Tests in pilot-scale reactor

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 10

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SLIDE 11

Cycling stability

After Cycling

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 11

Calcium silicates lead to

  • Reduction of storing capacity
  • Hardening of surface structure

Roßkopf et al., Investigations of Nano Coated CaO/Ca(OH)2 Cycled in Thermochemical Storage, in preparation

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SLIDE 12

Conclusion & Outlook

  • Thermochemical Heat storage based on

Ca(OH)2 demands a flow-through of the reactor

  • Improvement of Ca(OH)2 flowability by adding nano particles at

ambient conditions is shown

  • Homogeneous flow through thermochemical reactor at room

temperature achieved

  • Cycling stability is proven over 10 cycles in pilot-scale reactor

 Flow behaviour during thermochemical reaction will be investigated

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 12

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SLIDE 13

Thank you for your attention

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 13

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SLIDE 14

Thermodynamic equilibrium

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 14

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SLIDE 15

Storage densities

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 15

Typical storage densities in kWh/m³:

  • Sensible, mortar, ΔT=50K

25 - 30

  • Sensible, Water, ΔT=50K

50

  • Latent, solid-liquid

50 - 100

  • Physical oder chemical sorption

50 - 140

  • Thermochemical reaction

100 – 700

  • Storage capacity in 1 kg Ca(OH)2

0,373 Wh

  • Storage capacity of pilot-scale reactor

~200 kWh/m³

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SLIDE 16

> 7th World Conference on Particle Technology > Christian Roßkopf • Improving Powder Flowability by Adding Nanoparticles for Thermochemical Heat Storage with Moving Reaction Bed > 19th to 22nd May 2014 www.DLR.de • Slide 16

Particle size

Pelletizing the material

  • Increase of weight force by increasing the particles diameter

 Problem: Volume change of the material by chemical reaction leads to tensions within the pellet  Cracking of the pellet after few cycles in thermochemical reactor