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Thursday, June 30, 2016 Mars ISRU PEC CO 2 Splitting, KISS, Caltech, Pasadena, CA Ultra-Light Weight PEC… and Chemistry/Purity Information Shane Ardo Department of Chemistry Department of Chemical Engineering & Materials Science University of California, Irvine, USA

Ultra-Light Weight PEC…

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Page 1: Ultra-Light Weight PEC…

Thursday, June 30, 2016 Mars ISRU – PEC CO2 Splitting, KISS, Caltech, Pasadena, CA

Ultra-Light Weight PEC…and Chemistry/Purity Information

Shane Ardo

Department of ChemistryDepartment of Chemical Engineering & Materials Science

University of California, Irvine, USA

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ULW PEC Device/System

• Design• Photon Management

• Deployment• Metrics (W/kg, kg/m2)• System Scaling• Filter (chemical inputs/outputs)

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ULW PEC Device/System

3M

• Design• Photon Management

• Deployment• Metrics (W/kg, kg/m2)• System Scaling• Filter (chemical inputs/outputs)

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ULW PEC Considerations

• Transport dry/empty and fill on Mars• Roll out material• Autonomously

• Adopts flat geometry• Creates volume for electrolyte

• Less structural support required, due to 1/3 g• What does that look like?

• Vapor vs. Liquid (Water) Feed?• Liquid: Failures due to gravity• Vapor: Failures due to pressure, but aspect ratio can alleviate this

• Compressor is "free" mass (scroll pump from MOXIE)• Reactants: CO2, water (vapor)• Products: O2, CO (or other)

• Can the device handle temperature cycles/swings (esp. Nafion)?

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ULW PEC Device/System

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Cell/Module Bill of Materials

• Containment• Gorilla Glass (25 µm) 60 g/m2

• or HDPE (75 µm) 75 g/m2

%T = 95, leak rate = 45 g H2/m2/year (3.5% of H2 produced)[i]

• PV (assume ηSTH = 10% at 1 Sun on Earth)

• PV Materials and Contacts 20 g/m2

• Kapton Support (15 µm) 15 g/m2

• MEA• Catalysts (2 mg/cm2) 20 g/m2

• C Fiber (25 µm) 25 g/m2

• Nafion (50 µm) 50 g/m2

• C Fiber (25 µm) 25 g/m2

• Catalysts (2 mg/cm2) 20 g/m2

Nearly everything "cost" ~1 g/m2 per µm thick = 1 g/mL

+ 20% for structural support+ x% for pipes, control system, etc.

One person’s propellant requires~1000 m2, which here equates toa (370 + y) kg payload (< 0.5 mt)!

[i] Directed Technologies, Inc., DOE Report, 2009 & Pinaud, …, Ardo, …, Jaramillo, Energy Environ. Sci., 2013, 6, 1983

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Teflon (PTFE) / Gore-Tex / Nafion

Mauritz & Moore, Chemical Reviews, 2004, 104, 4535 http://www.nafion.mysite.com/

Nafion–SO2N-CH2CH3 (hydrophobic)

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Teflon (PTFE) / Gore-Tex / Nafion

PTFE Nafionor Nafion–R

PV MEA PV MEA …

Nafion–SO2N-CH2CH3 (hydrophobic)

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Teflon (PTFE) / Gore-Tex / Nafion

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Summary

3M

• Design• Photon Management

• Deployment• Metrics (W/kg, kg/m2)• System Scaling• Filter (chemical inputs/outputs)

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PS 1 (of 3): Summary

• Design• Photon Management

• Deployment• Metrics (W/kg, kg/m2)• System Scaling• Filter (chemical inputs/outputs)

5-6x photocurrent increaseAM0, no dust, capacity factorsmall transmission lossHeat ice

(need AC–DC conversion)

3M

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PS 1 (of 3): Summary

• Design• Photon Management

• Deployment• Metrics (W/kg, kg/m2)• System Scaling• Filter (chemical inputs/outputs)

Waterless resources• Nafion + catalytic water• Ionic liquid gel at cathode• Carbonate cycle

5-6x photocurrent increaseAM0, no dust, capacity factorsmall transmission lossHeat ice

(need AC–DC conversion)

3M

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PS 2: Motivation for other feedstocks

Shane Ardo ([email protected]) 13

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Maximizing round-trip efficiency

Shane Ardo ([email protected]) 14

Difficult 4-e– PCET reaction,

that nature figured out

Facile 2-e– ET reaction,

that we can do today

Semiconductor(s)

H+ H2

Redox

Flow

Battery

Fuel

Cell

H2OO2

H+

Semiconductor(s)

H+ H2

X–X2

h+e–h+

e–

Johnson, IEEE IEDM (1981) 81-2–6; McKee, IEEE Trans. (1982) CHMT-5, 336–341;

Luttmer & Trachtenberg, J. Electrochem. Soc. (1985) 132, 1312–1315

GOAL: Efficiently, inexpensively, and robustly store photon energy for use when dark

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Before the TI82 calculator there was …

Shane Ardo ([email protected]) 15Johnson, IEEE IEDM (1981) 81-2–6; McKee, IEEE Trans. (1982) CHMT-5, 336–341;

Luttmer & Trachtenberg, J. Electrochem. Soc. (1985) 132, 1312–1315

Jack Kilby

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Before the TI82 calculator there was …

Shane Ardo ([email protected]) 16Johnson, IEEE IEDM (1981) 81-2–6; McKee, IEEE Trans. (1982) CHMT-5, 336–341;

Luttmer & Trachtenberg, J. Electrochem. Soc. (1985) 132, 1312–1315

Jack Kilby

Si Si

Nafion

2 H–Br H2

+ Br2/Br

3

–ΔE

o= -1.05 V

~100 µm Si

Pt/Ir catalysts

ηSTF ≈ 8%

ηfull ≈ 5%

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H2

The Lewis Group approach

• Charge carrier collection

• Voltage drop/loss in electrolyte (= iR)

• Crossover of H2/O2

• Flexibility

LD(τ, D)ε, α-1

I3–

= electron

= “hole”

H+

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sample region shown here is 1/10th of an inch wide

Microwire arrays

Shane Ardo ([email protected]) 18

Boettcher, …, Atwater & Lewis, Science (2010) 327, 185–187

Kayes, Atwater & Lewis, J. Appl. Phys. (2005) 97, 114302-11

Chemical Vapor Deposition Protocol

Cu VLS growth catalyst, square 3 x 7 µm pattern

1000 °C H2, SiCl4, PH3, and/or BCl3Post processing to remove Cu and mask base

Radial pn junctions via diffusion doping

Doped 1E17 cm-3 with > 5E19 cm-3 emitters

crystalline

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2 μm

Interfaced catalysts

Shane Ardo ([email protected]) 19Boettcher, Warren, …, Atwater & Lewis, J. Am. Chem. Soc. (2011) 133, 1216–1219

McKone, Warren, …, Lewis & Gray, Energy Environ. Sci. (2011) 4, 3573–3583

≤ 15 μg/cm2

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100 μm

Semiconductor–Separator composite

Shane Ardo ([email protected]) 20 Ardo, Park, Warren & Lewis, , Energy Environ. Sci. (2015) 8, 1484–1492

Spurgeon, …, Kohl & Lewis, Energy Environ. Sci. (2011) 4, 1772–1780

CONCLUSION: Microwire arrays decrease purity/design constraints and maximize efficiency

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The Tandem

Shane Ardo ([email protected]) 21

Image credit: Santori

NSF–CCI Solar

H2

2 H+

I3–

3 I–

2 H+

20 μm

n+p-Si–Pt

n-Si–CH3–Pt

PEDOT:PSS–AgNWs–Nafion

Nafion

Nafion

Nafion + PEDOT:PSS

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Functioning peeled devices

Shane Ardo ([email protected]) 22 Ardo & Lewis, Full Patent (submitted), California Institute of Technology (2013)

Photocathode

Photoanode

Tandem

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PS 3: Electrolyzer (Fuel cell) requirements

ANSWER: I’m not certain.

Can I spell "fveI ce11"?

What chemical phase (G/L/S) is required?

What chemical purity is required?

Can it handle variable power input?

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Phase requirements

"MOXIE," backward

< 100 °C > 700 °C

• Electrocatalysis/membrane dominates Vloss

• Need pure H2 feed stream (see next slide)• CO poisons H2 catalyst (see next slide)• Nafion transports CO slower than O2

• Need an H+ source like H2O (or AEM)

• Ohmic drop dominates Vloss

• Easy to make reversible• Dirty feeds permissible• In situ reforming to H2 / CxHyOz

(possibly some coking)

COCxHyOz

CO2CO

CxHyOz

CO2

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Purity requirements

See NREL’s database on PEM fuel cell contaminants:http://www.nrel.gov/hydrogen/system_contaminants_data/

H2 purity standard (ISO 14687-2:2012): > 99.97 % H2; < 0.2 ppm CO; < 4 ppb H2S

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Purity requirements

http://www.astm.org/DATABASE.CART/HISTORICAL/D1193-99E1.htm

DOE: electrolyzed to ~20 bar and ~700 bar in cars

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CO interactions with Nafion

http://www.sciencedirect.com/science/article/pii/S0925400597800408

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Variability performance of electrolyzer

https://www.hydrogen.energy.gov/annual_review16_fuelcells.html#performance

Peters (NREL)

See NREL document from DOE-EERE-FCTO-AMR’s website

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Summary

• ~0.5 mt "today"… that payload seems reasonable!

• When do we start testing prototypes on Earth?

• Transmit power to Mars using microwaves and cell-phone-sized receivers in catalyst layers (with rectifiers)

• Alternative electrolytes could be useful

• Alternative redox couples could be useful

• Pure chemical feeds could be useful

Shane Ardo :: [email protected] :: http://www.chem.uci.edu/~ardo