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FLORIDA SOLAR ENERGY CENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Hydrogen Production via Photolytic Oxidation of Aqueous Sodium Oxidation of Aqueous Sodium Sulfite Solutions Sulfite Solutions Cunping Huang, Cunping Huang, Clovis A. Linkous Clovis A. Linkous , Olawale , Olawale Adebiyi & Ali T-Raissi Adebiyi & Ali T-Raissi Hydrogen 2008 – Materials Innovations in an Hydrogen 2008 – Materials Innovations in an Emerging Hydrogen Economy Emerging Hydrogen Economy Cocoa Beach, Florida, USA Cocoa Beach, Florida, USA February 27, 2008 February 27, 2008
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F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Dec 14, 2015

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Page 1: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

FLORIDA SOLAR ENERGY

CENTERA Research Institute of the University of Central Florida

Hydrogen Production via Hydrogen Production via Photolytic Oxidation of Aqueous Photolytic Oxidation of Aqueous

Sodium Sulfite Solutions Sodium Sulfite Solutions

Cunping Huang,Cunping Huang, Clovis A. LinkousClovis A. Linkous, , Olawale Adebiyi & Ali T-RaissiOlawale Adebiyi & Ali T-Raissi

Hydrogen 2008 – Materials Innovations in an Emerging Hydrogen 2008 – Materials Innovations in an Emerging Hydrogen EconomyHydrogen Economy

Cocoa Beach, Florida, USACocoa Beach, Florida, USAFebruary 27, 2008February 27, 2008

Page 2: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

BackgroundBackground

SO2 is a criteria air pollutant that can cause respiratory & other problems as an acid gas

SO2 emissions occur both naturally (20%) & anthropogenically (80%)

Natural sources include: geothermal (e.g. volcanic), oceanic, vegetative & land emissions.

Page 3: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Anthropogenic Sources of SOAnthropogenic Sources of SO22 EmissionsEmissions

Combustion of high-sulfur-containing fossil fuels

Sulfuric acid & ammonium sulfate plants

Power plants using coal, crude oil & crude oil-based fuel oil.

Page 4: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Major Global Anthropogenic Major Global Anthropogenic Sources of SOSources of SO22 Emissions Emissions

Emission Source Emission (%)

Electric utility 69.7

Industrial fuel combustion 13.6

Metal processing 3.8

Transportation 3.5

Others 9.4

Source: Schnelle, K.B., and Brown, C.A., Control of Sox, In Air Pollution Control Technology Handbook, ed. Kreith, F., CRC Press, Boca Raton, FL, 257, 2002

Page 5: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Generation of SO2 in 500 MW coal fired power plants can produce huge amounts of SO2 that can be used for the production of H2 as well as fertilizers.

Source: Pandey, R. A., et al, “Flue gas Desulfurization: Physicochemical and Biotechnological Approaches” Env. Sci. & Tech. 35:571-622., 2005.

SOSO22 is both a Pollutant & a is both a Pollutant & a ResourceResource

Page 6: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

ObjectivesObjectives

Develop an innovative process for utilizing SO2 in flue gas for the production of hydrogen

Explore chemistry & chemical engineering aspects of SO2 utilization

Investigate effects of reaction conditions on the hydrogen production rate.

Page 7: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Flue Gas Treatment and HFlue Gas Treatment and H22 ProductionProduction

Conventional process:Absorption: SO2 + NaOH = Na2SO3

Oxidation: Na2SO3 + O2 = Na2SO4 + H2O

FSEC Approach:Absorption: SO2 + NaOH = Na2SO3

SO2 + (NH4OH) = (NH4)2SO3

Photooxidation: Na2SO3 + H2O + UV light ( or E)= Na2SO4 + H2

(NH4)2SO3 + H2O + UV light (or E) = (NH4)2SO4+H2

Page 8: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Experimental Setup for SOExperimental Setup for SO22 TreatmentTreatment

Page 9: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Exp. Setup for HExp. Setup for H22 Production from Production from Aqueous NaAqueous Na22SOSO33 Solution Solution

Page 10: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Hydrogen ProductionHydrogen Production

Page 11: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

0

200

400

600

800

1000

1200

1400

1600

0 100 200 300 400 500 600 700 800 900 1000 1100 1200 1300

Time (min)

Hyd

rog

en (

mL

)

0.00

1.00

2.00

3.00

4.00

5.00

6.00

7.00

8.00

9.00

10.00

pH

Hydrogen

pHIII

III

I

II

III

I: HSO3- to SO4

2-

II: SO32- to SO4

2-

III: S2O62- to SO4

2-

Kinetics of HKinetics of H22 Production via Production via Photo-oxidation of NaPhoto-oxidation of Na22SOSO33

Page 12: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Material BalanceMaterial Balance

Ionic Species

Initial (mmol)

Final (mmol)

Diff.

(mmol)

SO32- 63.41 0.00 63.41

SO42- 2.40 63.59 61.19

Gas Produced

Theoretical (mL)

Exp.

(mL)

Diff.

(mL)

H2 1550 1390 160

Page 13: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

0

100

200

300

400

500

600

0 200 400 600 800 1000 1200 1400 1600 1800 2000

Reaction time (min)

Hyd

rog

en

evo

luti

on

(m

L) (a)

(b) (c) (d)

(e)(f)

(g)

(h)

Effect of Solution pH on HEffect of Solution pH on H22

ProductionProduction

Page 14: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Effect of Solution pH on HEffect of Solution pH on H22

ProductionProduction (cont’d)(cont’d)

0.00

0.40

0.80

1.20

1.60

2.00

2.40

7.00 8.00 9.00 10.00 11.00 12.00 13.00

pH

Init

ial

ra

te (

mL

/min

)

Page 15: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Concentration Effect on HConcentration Effect on H22

Production Rate (at pH = 9.70)Production Rate (at pH = 9.70)

0

200

400

600

800

1000

1200

1400

0 500 1000 1500 2000 2500 3000

Irradiation time (min)

Hyd

rog

en

evo

luti

on

(m

L)

0.05 M Na2SO3(pH=9.70)

0.025 M Na2SO3(pH=9.92)

Page 16: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Concentration Effect on HConcentration Effect on H22

Production Rate (at pH = 7.55)Production Rate (at pH = 7.55)

0

200

400

600

800

1000

1200

1400

0 200 400 600 800 1000 1200 1400 1600 1800

Irradiation time (min)

Hyd

rog

en e

volu

tio

n (

mL

)

0.05 M (pH=7.59)

0.025 M (pH=7.53)

a

bc

Page 17: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

SummarySummary

Conc. pH Conc. pH Conc. pH Conc. pHSolution 0.025 M 9.92 0.05 M 9.70 0.025 M 7.53 0.05 M 7.59

H2 prod rate 0.74 mL/min 1.40 mL/min 1.91 mL/min 1.91 mL/min

At pH = 9.95, H2 production rate increases with an increase in the concentration of the sulfite.At pH = 7.55, H2 production rate is independent of the sulfite concentration.

Page 18: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

ConclusionsConclusions

A novel approach for utilizing SO2 in flue gas for hydrogen production has been developed

Photolytic H2 production from aqueous Na2SO3 solutions is a clean and efficient process

Experimental data indicate that SO32- can be

fully converted into SO42-

FSEC process requires no catalysts, reducing the process capital & operating costs.

Page 19: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

Future WorkFuture Work

Investigate effects of other flue gases (e.g. NOx, CO2) on the photolytic production of hydrogen

Investigate effects of metal catalysts in enhancing the photolytic hydrogen production from SO2

Photoreactor design considerations Process design & optimization.

Page 20: F LORIDA S OLAR E NERGY C ENTER A Research Institute of the University of Central Florida Hydrogen Production via Photolytic Oxidation of Aqueous Sodium.

AcknowledgmentAcknowledgment

National Aeronautics and Space Administration (NASA) - Glenn Research Center (GRC) under contract No. NAG3-2751.