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Tiêu đề Materials for the Hydrogen Economy
Trường học Georgia Institute of Technology
Chuyên ngành Materials Science
Thể loại Bài báo
Năm xuất bản 2007
Thành phố Atlanta
Định dạng
Số trang 30
Dung lượng 1,18 MB

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Boiler w/ stone C276 Dense-Super Heater C276 Solar Cavity Vycor Window Tank Boiler w/ stone C276 Dense-Super Heater C276 Solar Cavity Vycor Window Decomposer Incoloy 800H & aluminide c

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Construction materials capable of handling H2SO4 vapor were studied

exten-sively.during.the.early.stages.of.the.S-I.cycle.development,.as.it.was.thought.to.be

the most critical materials.issue of.the cycle Because of.the high

operating.tem-perature involved, materials candidates were chosen from those that derive their

strength from solid-solution strengthening instead of precipitation hardening, as

overage conditions can lead to a decrease in strength Different researchers have

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a superheater also made with Hastelloy C-276 At this stage, the vapor begins to.

.catalytic.decompo-sition to take place This decomposer was actually a heat exchanger constructed

Boiler w/

stone (C276)

Dense-Super Heater (C276)

Solar Cavity

Vycor Window

Tank

Boiler w/

stone (C276)

Dense-Super Heater (C276)

Solar Cavity

Vycor Window

Decomposer (Incoloy 800H & aluminide coated 800H tube filled with catalyst pellets)

Condenser (Incoloy 825)

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Since the final design and operation conditions of the nuclear S-I hydrogen.

loop are still being finalized, materials of construction development for H2SO4

estimated depth of Corrosion(mil)

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fIgure . A schematic and a prototype of a SiC bayonet H2 SO 4 vaporizer/.

decomposer.

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fIgure . Zr705.coupon.before.and.after.a.120-h.test.in.HIx.at.310ºC.

Table .

Corrosion rate of various materials in hI x at high Temperatures

Corrosion rate (mm/yr) material boiler (0°C) feed (°C)

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Other ceramic materials, such as Al2O3 or mullite, have also been shown to.

Corrosion rate of alloys in h  Po 

alloy Concentration Temperature (°C)

Corrosion rate (mm/yr)

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fIgure . A.Ta-10W.coupon.tested.in.HIx-H3PO4.at.140ºC.for.1,209.hours (A).0.h,.(B).

250.h,.(C).874.h.&.(D).1,209.h

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4.4.1.3.4 Materials for HI + I 2 + H 2 (Gaseous HI Decomposition)

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4.4.1.3.5 Effect of Stress Corrosion and Chemical Contaminants

Corrosion Test results in a vapor medium of hI–I  –h  o (//) vapor at

various Temperatures for ,000 h duration

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125°C has been successfully demonstrated (figure.4.22) The permeability or flux.

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Corrosion.products.from.other.sections III H3PO4.concentration H2SO4.and.HIx.from.Section.I.and.iodine.

separation.

Corrosion.products.from.other.sections III HI.distillation.(reactive.and.

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O–HI.gaseous.mix-ture at elevated temperatures (figure.4.24) A separation factor of more than 600.

fIgure . Schematic.of.the.electro-electrodialysis.process.to.concentrate.the.HIx acid.

feed.from.the.Bunsen.reaction.

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Te mp (°C)

H 2 /H 2

S1 S2 S3 L2 L1

a

0 100 200 300 400 500 600 700

b fIgure . Separation.factor.of.H2 from.H 2 -HI-H 2 O.for.various.silica.membranes.

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... sulfuric acid decomposition

Fe 2 O 3

CeO 2

Al 2 O 3

NiO

fIgure . Relationship.between.conversion.to.SO2 +.H2O.and.temperature.for.catalytic.

metal.oxides.and.Pt.in.a.N2.flow.containing.4.mol%.SO3.at.a.space.velocity.of.4,300.h.

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1 Miyamato, Y et al., R&D program on hydrogen production system with high

tem-perature cooled reactor, in International Hydrogen Energy Forum, Vol 2, Munich,.

Germany,.2000,.pp 271–278.

2 Brown, L.C., Funk, J.F., and Showalter, S.K., Initial Screening of

Thermochemi-cal Water Splitting Cycles for High Efficiency Generation of Hydrogen Fuels Using

3 Brown,.L.C.,.Besenbruch,.G.E.,.Lentsch,.R.D.,.Schultz,.K.R.,.Funk,.J.F.,.Pickard,.P.S.,.

Marshal, A.C., and Showalter, S.K., High Efficiency Generation of Hydrogen Fuels

10 High Efficiency Hydrogen Production from Nuclear Energy: Laboratory

11 Sakurai, M., Nakajima, H., Onuki, K., and Shimizu, S., Investigation of two liquid.

phase separation characteristics on the iodine-sulfur thermochemical hydrogen

pro-duction.process,.International Journal of Hydrogen Energy,.25,.605–611,.2000.

14 Trester,.P.W and.Staley,.H.G.,.Assessment and Investigation of Containment Materials

for the Sulfur-Iodine Thermochemical Water-Splitting Process for Hydrogen

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20 Porisini,.F.,.Selection and.evaluation of materials.for the construction of a pre-pilot.

plant.for.thermal.decomposition.of.sulfuric.acid,.International Journal of Hydrogen

26 Wong,.B.,.Brown,.L.C.,.and.Besenbruch,.G.E.,.Corrosion Screening of Construction

high.temperature,.Journal of Membrane Science,.267,.8–17,.2005.

34 Nomura, M., Kasahara, S., Okuda, H., and Nakao, S., Evaluation of the IS process.

featuring.membrane.techniques.by.total.thermal.efficiency,.International Journal of

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H2SO4.and.production.of.HBr.by.the.reaction.of.SO2.with.Br2.and.H2O,.International

39 Ballinger,.R.,.The.Development.of.Self.Catalytic.Materials.for.Thermochemical.Water.

Splitting.Using.the.Sulfur-Iodine.Process,.paper.presented.at.the.UNLV-HTHX.quar-terly.meeting,.Univerity.of.Nevada,.Las.Vegas,.December.5,.2005.

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for Photobiological Hydrogen Production

Daniel M Blake, Wade A Amos, Maria L Ghirardi, and Michael Seibert

ConTenTs

5.1 Introduction 123

5.2 Description.of.the.Process 124

5.2.1 Oxygen-Tolerant.Hydrogenase.Systems 126

5.2.2 Anaerobic.Hydrogenase.Systems 127

5.3 Reactor.Materials 129

5.3.1 Photobioreactors 130

5.3.2 Photobioreactor.Materials 131

5.4 Economics.and.Cost.Drivers.for.Photobiological.Hydrogen.Production 135

5.4.1 Operating.Costs 135

5.4.2 Capital.Costs 137

5.4.3 General.Design.Considerations 138

5.4.4 Case.Study 139

5.5 Conclusion 140

Acknowledgments 140

References 140

. InTroduCTIon The.world’s.energy.infrastructure.is.under.pressure.from.rapidly.increasing.demand

Recent.worldwide.events.have.increased.public.anxiety.about.the.cost.of.gasoline

and.heating.fuels,.and.the.security.of.these.resources.has.become.an.issue Finally,

the.amount.of.pollution.and.CO2.that.society.is.generating.is.increasing,.and.every-

one,.from.individual.villages.to.entire.countries,.is.looking.for,.or.should.be.look-ing.for,.a.sustainable,.secure.energy.system Currently,.the.world.has.over.6.billion

individuals,.all.powered.by.solar.energy The.food.we.eat.and.the.oxygen.we.breathe

come.from.photosynthesis Can.energy.from.the.sun,.which.indirectly.powers.all

animal.life.on.the.planet,.including.ourselves,.also.give.us.hydrogen.from.water.to

be.used.as.a.renewable.energy.carrier?

This.review.will.discuss.the.development.of.photobiological.hydrogen.produc-tion processes, where microorganisms (algae or cyanobacteria) funcThis.review.will.discuss.the.development.of.photobiological.hydrogen.produc-tion as living

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as starch molecules (the normal function of photosynthesis), these organisms can.

recombine.the.protons.and.electrons.and.evolve.H2.gas.under anaerobic conditions

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1 The.hydrogenase.genes.in.green.algae.and.in.some.cyanobacteria.are.not.

2 The.expression.and.function.of.the.genes.that.catalyze.the.assembly.of.the

catalytic metallocluster of the algal [FeFe]-hydrogenases require

Maness, personal communication) The second approach involves the manipulation

of green algal physiology to induce culture anaerobiosis, expression of the

Redox Chemistry

(water oxidation produces O 2 , electrons and a proton gradient across the chloroplast membrane through an electron- transport- facilitated reaction)

CO 2 fixation

CO 2 + e - + ATP starch (ATP is obtained in a coupled dissipation of the

H + gradient by the ATP synthase) + O 2

H 2 gas production

2 H + + 2 e - H 2 (catalyzed by the hydrogenase enzyme) fIgure . Representation.of.the.major.steps.required.for.photosynthetic.CO2 fixation.

(upper.right.box).and.hydrogen.production.(lower.right.box).

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