hydrogen thesis
TRANSCRIPT
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STUDIES ON HYDROGEN CHEMISORPTION ON TITANIUM NANO
POWDER
Dissertation submitted to
KANCHI MAMUNIAR CENTRE !OR POST GRADUATE STUDIES
"AUTONOMOUS#
PUDUCHERRY$%&' &&(
In Partia) !u)*i))ment o* t+e Re,uirements
!or t+e a-ard o* t+e de.ree o*
MASTER O! PHI/OSOPHY
IN
PHYSICS
01
K2SUSAINATHAN
"Re.ister No3 454%4&6#
Under t+e .uidan7e o*
Dr2 RAMADASS8 M2 S728 P+2 D2
(Research guide and Supervisor)
DEPARTMENT O! PHYSICS
KANCHI MAMUNIAR CENTRE !OR POST GRADUATE STUDIES
"AUTONOMOUS#
PUDUCHERRY$%&'&&(
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Dr 2RAMADASS8 M2S728 2P+2D8
Asso7iate 9ro*essor8
De9artment o* 9+1si7s8
K2 M2 C2 P2 G2 Studies "Autonomous#8
Pudu7+err1 $ %&' &&(2
0ONA!IDE CERTI!ICATE
This is to certify that the dissertation titled :STUDIES ON HYDROGEN
CHEMISORPTION ON TITANIUM NANO POWDER submitted to KANCHI
MAMUNIAR CENTRE !OR POST GRADUATE STUDIES "AUTONOMOUS#8
PUDUCHERRYis a bonafide research work carried out by Mr2 K2 SUSAINATHAN "Re.ister
No3 454%4&6# for the award of the degree of MASTER O! PHI/OSOPHY IN PHYSICS
under my guidance and supervision during the requisite period. This work is original and entirely
carried out by the candidate for the fulfillment of the project work. I also certify that this research
work has neither formed the basis for the award of any other Degree, Diploma, ellowship or
any other similar titles of the any university or institution.
This is also to certify that the dissertation represents the independent work of the candidate.
Dr2 RAGURAMAN Dr2 RAMADASS
!ead and "ssociate professor "ssociate professor
DIRECTOR
P)a7e3 Pudu7+err1
Date3
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DEPARMENT O! PHYSICS8
KANCHI MAMUNIAR CENTRE !OR POST
GRAGDUATE STUDIES8
"AUTONOMOUS#8
PUDUCHERRY$ %&' &&(2
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Shri. C. Ramesh., Place : Kalpakkam
Materials Chemistry Division, Date :
Chemistry Group, Inira
Ganhi Centre !or "tomic Research,
Kalpakkam#$%&'%(.
)*+"ID- C-RIIC"-
This is to certify that the project work titled /S0DI-S *+ 12DR*G-+
C1-MIS*RPI*+ *+ I"+I0M +"+* P*3D-R4 submitted to the K"+C1I
M"M0+I5"R C-+R- *R P*S GR"D0"- S0DI-S 6"0*+*M*0S7 for
the award of the degree of Master o! Philosophy is a bonafide record of theresearch work done byMr. K. S0S"I+"1"+, Re8. +o. ('($(%9, Department of
Physics, Kanchi Mamuniar !entre "or Post #raduate $tudies, Puducherry%&'('')
under my guidance and superision at the M"-RI"S C1-MISR2 DI5ISI*+,
C1-MISR2 GR*0P, I+DIR" G"+D1I C-+R- "*R "*MIC R-S-"RC1,
K"P"KK"M# $%&'%( during the period "ebruary 2'1* to +ugust 2'1*
Mr. C. R"M-S1
Scienti!ic *!!icer;G
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Mr2 K2SUSAINATHAN8
M2 P+i) Resear7+ S7+o)ar8
De9artment o* 9+1si7s8
K2 M2 C2 P2 G2 Studies "Autonomous#8
/a-s9et8
Pudu7+err1$ %&'&&(2
DEC/ARATION
I hereby declare that the dissertation titled :STUDIES ON HYDROGEN
CHEMISORPTION ON TITANIUM NANO POWDER; is a record of project work
done by me for the degree of Master o* P+i)oso9+1 in 9+1si7s under the guidance of Dr2
RAMADASS, Asso7iate Pro*essor8 Kan7+i Mamuni
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"ckno
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. wish to record my deep sence of gratitude and sincerethanks to my research guide shri C.Ramesh scientific officermaterial chemistry section, chemistry group .#!+0 kalpakkam,for his unstinted inspiration, inaluable guidance, encouragement,
keen interest, good wishes and aluable suggestions throughoutmy entire research tenure . am also grateful to him for criticallyreiewing this thesis
.t gies me immense pleasure to acknowledge to myresearch co%guide shri +.muru8asan, scientific officer, materialscience section, and chemistry group .#!+0 kalpakkam, for
critically ealuating my research actiities time to time and alsofor proiding the laboratory computational facilities and seeralaluable suggestions for completion of this work
. e/press my sincere thanks to Mr > Mrs. Mathan,Chanra mo8an, Shamima 1ussian ,helping me for recordingthe ? @ray i!!racto8ram, )- sur!ace area measurement ,S-M ima8e and many useful suggestions pertinent to thisdissertation
. would like to carry my thanks to my professor Dr. Guptha,Dr. Rama=ramam an Dr. Meenakshi Associate Professor,
Department of Physics, K.M.P.C.P.S, Pondicherry gien mea support
.t is a great pleasure to acknowledge my ab matesMr."!iAith !orhelping me and proiding kind supports andencouragement during my research work . am also thanks to allmy chemistry ivision collea8ues an sta!! mem=ersfortheir support at different times
ast but not least . want to say thanks to my friends Mr.$amilselvam, Mani%andanstand with me at all the cases andthanks for their loingness
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"inally, . am e/tremely thanks to all those people who werethe pillar of support to me
*RG"+IS"I*+ * 1- DISS-R"I*+
C1"P-R#I
.3T04D5!T.43
This chapter contains the basic information about hydrogen demand,hydrogen economy, hydrogen production methods, hydrogen storagemethods and hydrogen storage target which forms an aim of research in myproject
C1"P-R#II
iterature revie2produced for later
use, to transport stored hydrogen from the point of production to the point of
use, and to charge and discharge hydrogen coneniently from the storage
container according to need
.* >ydrogen Production Methods
Many production processes for hydrogen e/ist The hydrogen can be
produced from the fossil fuels ?eg, steam reforming of natural gas or other
light hydrocarbons, gasification of coal and other heay hydrocarbons@ or
water ?electrolysis of water, direct and indirect thermochemical
decomposition, and processes drien directly by sunlight %photo catalytic
route@ +lthough haing so many choices of resources sounds complicated,
but indeed it is a great adantage, because no one region or country has to
be dependent on one resource to produce hydrogen and whicheer
resources are suitable enironmentally and economically can be used .n an
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eneloping country like .ndia, by means of hydrogen economy, we can hae
decentrali8ed energy, as many remote areas are not haing access to
electricity?12@
Presently, the commerciali8ed hydrogen production processes aremostly fossil fuel based, like, steam methane reformation, partial o/idation
of methane, auto%thermal reforming and coal gasification E the cheapest and
largest being generated by steam%methane reformation Though all these
processes generates !42, !42 generated from the reformation process is
highly concentrated, therefore the recoery is much cheaper than the diluted
e/haust gas of the fossil fuel :ut the main adantages of hydrogen economy
comes if hydrogen is e/tracted from water, using !42%free primary sources ofenergy such as solar energy, wind energy, or nuclear energy?1*, 1-@ The
different production methods of hydrogen from water are described in the
following section
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$a#le'( Different hydrogen production methods, *here hydrogen is
produced from *ater
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Method Process "eed $tock ;nergy ;mission
Thermal
$team0eformation
3atural#as
>igh temperaturesteam
!arbonse7uestration canmitigate its small
emission
!oal #asification
!oal,:iomas
s
$team and o/ygenat hightemperature pressure
$mall emission!arbon$e7uestration canmitigate it
Pyrolysis:iomas
s
Moderately highTemperaturesteam
$mall emission!arbonse7uestration canmitigate it
Thermochemical=ater $plitting
=ater=aste heat fromhigh temperaturenuclear reactor
3o ;mission
;lectrochemical
;lectrolysis =ater
;lectricity from
wind, solar, hydro,nuclear
3o emission
Photoelectrochemical
=ater;lectricity fromdirect sunlight
3o emission
:iological
Photo biological=ater
+lgaeDirect $unlight 3o emission
+naerobic:iomas
s>igh temperature
heat$mall emission
"ermentatieMicro organism
:iomass
>igh temperatureheat
$mall emission
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.*1 >ydrogen production from water
>ydrogen generation from water can be depicted by the following
e7uation
1(* E 1( F ';( *(
The reaction is highly endothermic '! ( )*+ %mole- at )/0 %1, and for direct
thermolysis of water, a very high temperature is required '2)344 561. The energy required to
split water can be provided by a primary energy source, like, solar, wind, nuclear heat or by a
secondary energy source like electricity or a combination of these sources using a chemical
process. 7o, a large collection of diverse processes are involved for hydrogen generation from
water and some of which are listed in Table. 8one of the above processes e9cept electrolysis
has been commerciali:ed and although electrolysis is an established process, cost of hydrogen
production is very high. 7o, efforts are being taken to improve efficiency and to minimi:e cost of
these processes to make them commercially viable. Thus, $;D on various aspects like material
development, catalyst development, reactor design etc. has to be carried out
.-Hydrogen storage methods
.n principle, hydrogen can #e stored either in a physical form
+gas or liuid- or chemical form '(&). he methods #eing used to store
hydrogen are discussed #elo1.
I.;.( 8i0uid hydrogen storage 'Cryostorage)
i7uid hydrogen storage is currently the bulk hydrogen storagemedium of choice and has a ery impressie safety record 5nfortunately,
the energy re7uirements o+ li0ue+action are high, typically /%9 o+ the
hydrogen*s heating value. 8i0uid hydrogen 1ill remain the main techni0ue o+
#ul2 and stationary hydrogen storage +or the +oreseea#le +uture '(:).
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The hydrogen can also be stored as a li7uid in a cryogenic tank at
ambient pressure and low temperature ?%2(2oc). Hydrogen stored as a li0uid
has a relatively high volumetric density ' +irst, the li0ue+action process is costly. 6econd, small scale
li0uid hydrogen production is impractical. hirdly, lo1 volume
distri#utiondispensing o+ li0uid hydrogen are e-pensive '(igh pressure gas
cylinders can store hydrogen at a pressure of 2' MPa and storage is een
possible up%to pressure of )'MPa in newly deeloped light weight composite
cylinders where the hydrogen olumetric density can reach -'KgFm* $ince
the hydrogen graimetric density is low, there are also problem in holding
the high pressure, especially in the regions with high population density
!ompressed gaseous hydrogencontainers consisting o+ /;.& mpa '&%%% psi)
'/;$ atmospheres) gaseous hydrogen in metal or plastic lined car#on +i#re
1ound pressure vessels o++er advantages +or storage. 6implicity o+ design
and use, high hydrogen +raction, rapid re+ueling capa#ility, e-cellent
dormancy characteristics, minimal in+rastructure impact, high sa+ety due toinherent strength o+ the pressure vessel, and little to no development ris2
are evident advantages. he disadvantages are system volume, use o+ high
pressure, integrating the automotive designer etc. Compressed gas storage
is supporta#le #y small3scale hydrogen production +acilities as 1ell as large
scale hydrogen production +acilities. hus a possi#le hydrogen in+rastructure
transition path1ay e-ists. ?or these reasons, room temperature compressed
gas storage is vie1ed as the most appropriate +uel storage system +or 45M
+uel cell vehicles '(7).
.-./ 4hysical storage on high sur+ace area materials
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@ased on 1ea2 van der aals interaction #et1een gas molecules andsolids, hydrogen molecule can #e reversi#ly stored on high sur+ace area
materials such as car#on #ased materials, zeolits structures, and metal
organic +rame1or2 materials, respectively. Ho1ever, the amount o+
hydrogen that can #e adsor#ed on porous materials at am#ient temperature
and high pressure are much lo1er '%.&1t 9). he advantage o+ the sor#ed
materials lies in their ready reversi#ility. his is also their largest
disadvantage. Ho1ever, as they contain hydrogen #y means o+ 1ea2
4hysisorption +orces 'Bander aals), lo1 temperatures '3(:%C) and high
pressures are re0uired +or signi+icant adsorption '().
.-.; Metal Hydride storage method
Metal hydrides can be subdiided into two categoriesG low dissociation
temperature hydrides and high dissociation temperature hydrides The low
temperature hydrides suffer +rom lo1 H$ +raction ' $9). he high
temperature hydrides re0uire a heat source to generate the hightemperature o+ dissociation ' /%%!C). @oth systems o++er +airly dense H$
storage and good sa+ety characteristics. Indeed it is the #ad characteristics
o+ dissociation 'high temperature, high energy input) that create the good
sa+ety characteristics 'no or slo1 H$ release in a crash). ?or vehicular
hydrogen storage, metal hydrides are either too heavy or their operating
re0uirements are poorly matched to 45M vehicle systems. ithout a
dramatic #rea2through achieving high 1eight +raction, lo1 temperature, lo1dissociation energy, and +ast charge time, metal hydrides 1ill not #e an
e++ective storage medium +or 45M +uel cell vehicles. ?or stationary storage,
the 1eight o+ metal hydride system is not an adverse +actor. Conse0uently,
their attri#utes o+ high volumetric storage density and sta#ility ma2e them
0uite attractive. Improving resistance to gaseous contaminants and
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increasing system cycle li+e remain as o#stacles to #e overcome. It stores
hydrogen #y chemically #onding the hydrogen to metal or metalloid
elements and alloys '+ig;). Hydrides are uni0ue #ecause some can a#sor#
hydrogen at or #elo1 atmospheric pressure, then release the hydrogen at
signi+icantly higher pressure 1hen heated and there is a 1ide operating
range o+ temperatures and pressures depending on the metal and alloy
chosen. 5ach metal and alloy has di++erent per+ormance characteristics, such
as cycle li+e and heat o+ reaction '$%).
&igure( Schematic o! a Metal 1yrie # hyro8en is inserte in =etydrogen storage target
The current goal is to deelop an effectie on%board hydrogen storage
system for mobile applications .n order for hydrogen powered ehicles to be
competitie with comparable ehicles in the market place, the on%board
hydrogen storage system needs compact, light, safe and affordable
containment and should coer a driing range of -'' km ) kg of hydrogen is
needed for the combustion engine ersion in comparison to - kg hydrogen
for an electric car with a fuel cell +t room temperature and atmospheric
pressure, -kg of hydrogen gas occupies a olume of -(m*, which is hardly a
practical solution for a ehicle ?21@ >igh%pressure hydrogen cylinder,
li7uefied hydrogen tank, and solid metal hydride are possible options $olid
metal hydride has the largest olumetric density, and therefore is now
1
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considered a more safe and effectie way to handle hydrogen than
compressed gas and li7uid hydrogen The hydride offers olumetric
hydrogen densities substantially greater than that of compressed gas and is
comparable to or e/ceeding that of li7uid hydrogen >igh pressure
containment essels or cryogenic tanks ?1@ are not re7uired for solid metal
hydride storage
&igure/( $he gravimetric storage capacities of hydrogen in different form
.n 2''< the 5$ Department of energy ?5$ D4;@ updated the hydrogen
storage system performance targets for light duty ehicles ?22, 2*@ The
following criteria for the hydrogen storage technology suitable for
transportation were setG
>igh >2storage capacity ?((wtA> for system@
Moderate operation temperature for hydrogen release and uptake,
ideally between &'%12''!
"aorable kinetics for hydrogen absorptionFdesorption
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ow cost
ow to/icity and non e/plosie
The 5$ D4; hydrogen storage system targets help guide researchers
by defining system re7uirements in order to achiee commercially iable
hydrogen storage capacity, reaction enthalpy, and reaction kinetics for
efficient storage for mobile application ?fig -@
!onsidering these facts, the hydrogen storage using metal hydride is
the best method
'.$ Research aim an scope
Present fossil fuel based energy system has drawbacks of polluting
enironment by releasing green house gases .n the recent past, 0 D on
fuel cell based energy system are gaining momentum like in the areas of
catalysts, proton conductors and hydrogen storage materials .n sodium
cooled fast reactors, large 7uantities of hydrogen are released during arious
processes There is need to find suitable hydrogen storage material fortrapping the hydrogen released from such processes +lthough there are so
many substantial research and deelopment actiity in the field of hydrogen
storage materials, none of the materials studied to date has demonstrated
sufficient hydrogen storage capacity or efficiency at the re7uired operating
temperature range There is still considerable opportunity for study of new
materials or material systems that could fulfill all the re7uirements for
efficient hydrogen storage for mobile applications =ith regards to thee/isting materials or material systems research is still needed to improe the
chemisorptionFdesorption performance and understand the mechanisms of
chemisorption and desorption reactions with or without effectie catalyst
doping Therefore the research interest is turned to the light metal titanium
due to its high olumetric and graimetric storage capacity >oweer, use of
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this metal for hydrogen storage is challenging because the stability of a
metal hydride must lie within a specific range for the
chemisorptionFdesorption boundary at pressure and temperature that is
usable in practical application
The primary aim of this research is to promote the light metal such as
titanium for hydrogen storage The e/periment is done using TPD04
instrument for hydrogen uptakeFrelease studies The samples were
characteri8ed by 90D for structural information, $;M for morphology and
:;T for surface area measurement
Chapter#II
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iterature revieigh enthalpyG ('KjFmolQ>%)''KjFmol
+dsorption takes place only in a Monolayer
>igh temperature
Type of interactionG strongB coalent bond between adsorbate and
surface
>igh actiation energy
.ncrease in electron density in the adsorbent%adsorbate inter+ace.
Reversi#le only at high temperature.
Due to specificity, the nature of chemisorption can greatly differ from
system to
$ystem depending on the chemical identity and the surface structure
.N1-#as%surface !hemisorptions
.N1-1 +dsorption Kinetics
+s an instance of adsorption, chemisorption follows the adsorption
process The first stage is for the adsorbate particle to come into contact
with the surface The particle needs to be trapped onto the surface by not
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possessing enough energy to leae the gas%surface potential well .f it
elastically collides with the surface, then it would return to the bulk gas .f it
loses enough momentum through an inelastic collision, then it Csticks onto
the surface, forming a precursor state bonded to the surface by weak forces,
similar to Physisorption The particle diffuses on the surface until it finds a
deep chemisorption potential well Then it reacts with the surface or simply
desorbs after attaining enough energy ?*(@.
he reaction 1ith the sur+ace is dependent on the chemical species involved.
Applying Gi##s +ree energy e0uation +or reactions>
G=H-TS
#eneral thermodynamics states that for spontaneous reactions, the change
in free energy should be negatie $ince a free particle is restrained to a
sur+ace, and unless the sur+ace atom is highly mo#ile, entropy is lo1ered.
his means that the enthalpy term must #e negative, implying an
e-othermic reaction
I5.'..( Moelin8
"or e/perimental setupo+ chemisorptions, the amount o+
adsorption o+ a particular system is 0uanti+ied #y a stic2ing pro#a#ility value.
Ho1ever, chemisorptions are very di++icult to theorize. A multidimensional
potential energy sur+ace '456) derived +rom e++ective medium theory is used
to descri#e the e++ect o+ the sur+ace on a#sorption, #ut only certain parts o+
it are used depending on 1hat is to #e studied. here e-ist several models to
descri#e sur+ace reactions> the 8angmuir3Hinshel1ood mechanism in 1hich
#oth reacting species are adsor#ed, and the 5ley3Rideal mechanism in 1hich
one is adsor#ed and the other reacts 1ith it. Real systems have many
irregularities, ma2ing theoretical calculations more di++icult '/$)
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$olid surfaces are not necessarily at e7uilibrium
They may be perturbed and irregular.
Distri#ution o+ adsorption energies and odd adsorption sites.
@onds +ormed #et1een the adsor#ate.
!ompared to Physisorption where adsorbates are simply sitting on the
surface, the adsorbates can change the surface, along with its structure The
structure can go through rela/ation, where the first few layers change inter
planar distances 1ithout changing the sur+ace structure, or reconstruction
1here the sur+ace structure is changed.
I5.'..& Dissociation Chemisorption:
+ particular brand of gas%surface chemisorption is the dissociation
of diatomic gas molecules, such as hydrogen, o/ygen, and nitrogen 4ne
model used to describe the process is precursor%mediation The absorbed
molecule is adsorbed onto a surface into a precursor state The molecule
then diffuses across the surface to the chemisorption sites'/:). hey #rea2
the molecular #ond in +avor o+ ne1 #onds to the sur+ace. he energy toovercome the activation potential o+ dissociation usually comes +rom the
translational energy and vi#rational energy. 5-ample is the hydrogen and
copper system, one that has #een studied many times over. It has a large
activation energy o+ ./& 3 .7& eB. he vi#rational e-citation o+ the hydrogen
molecule promotes dissociation on lo1 inde- sur+aces o+ copper
.N2 Physisorption
The fundamental interacting force of Physisorption is caused by an
der =aals force ;en though the interaction energy is ery weak ?R1'E1''
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meN@, Physisorptionplays an important role in nature. ?or instance, the van
der aals attraction #et1een sur+aces and +oot3hairs o+ gec2os provides the
remar2a#le a#ility to clim# up vertical 1alls. Ban der aals +orces originate
+rom the interactions #et1een induced, permanent or transient electric
dipoles.
In comparison 1ith chemisorptions, in 1hich the electronic structure o+
#onding atoms or molecules is changed and covalent or ionic #onds +orm,
4hysisorption, generally spea2ing, can only #e o#served in the environment
o+ lo1 temperature 'thermal energy at room temperature L$: meB) and in
the a#sence o+ the relatively strong chemisorptions. In practice, the
categorization o+ a particular adsorption as 4hysisorption or chemisorptionsdepends principally on the #inding energy o+ the adsor#ate to the su#strate
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&igure
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gas pressure and usually decreases 1ith increasing temperature. In the
case o+ systems sho1ing hysteresis the e0uili#rium may #e metasta#le.
"nder appropriate conditions o+ pressure and temperature, molecules
+rom the gas phase can #e adsor#ed in e-cess o+ those in direct contact
1ith the sur+ace.
N;9P;0.M;3T+ T;!>3.S5;$
N1 .3T04D5!T.43 T4 TPD04?&H, %7.
6emperature Pro8ramme Desorption; Reuction;*Biation7
The characteri:ation of solids, intended as knowledge of chemical-physical properties,
structure, surface activity etc, is e9tremely important, particularly in the field of catalytic systems.
The major application of the surface actiity is related to the catalysis field.
The metal supported catalysts are used in most manufacturing processes of different industries, from the
petrochemical field to fine chemistry, from the pharmaceutical field to the food industry. In general they
are capable of optimi:ing the yield of a reaction by increasing its kinetics or allowing the use of less
drastic conditions for its occurrence and thus reducing the manufacturing cost.
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&igure=( $PDR5 ''>> $hermo model system.
The solid catalysts act by providing specific sites for the adsorption of molecules
reacting on the surface, loosening their links and making the reaction easier. In some instances they can
react selectively by inhibiting the reaction towards undesired products. @nce the reaction is over,
desorption of products from the catalyst surface makes the sites available for another reaction. In most
cases, the activity of a supported catalyst is proportional to the metal area, and the activity of this area is a
function of the si:e of the metal particles deposited on the inert support. To quantitatively assess the metal
surface accessible to the adsorbed molecules, a few analytical methods are available and the use of which
depends on the nature of the application of the catalyst under test.
Two analytical methods for the chemisorption of gases are available to calculate the metal surface area of
a catalystA
The static volumetric method
The in-flow methods applied with the TBD$@.
N.'.'. Principles an Methos The analytical methods available with the TBDC$C@ 44 allow the determination of the
gas quantity '!), @), 6@, etc.1 chemically adsorbed from the surface of a solid sample with the choice of
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appropriate e9perimental conditions 'temperatures, pretreatments, etc.1. They also allow the
determination of the type and number of the active sites, the evaluation of different thermodynamic and
kinetic parameters and the quantitative assessment of the reactivity of the systems towards all gases.
inally it is possible to perform very precise quantitative measurements of the acid and basic properties of
the systems under test.
N.'.(. In#lo< Metho This analytical method adopts conditions of atmospheric pressure, using gas flows
'inert or reactive1.The in-flow systems provide the advantage of being rapid and sensitive, and they do not
need calibrations concerning instrumental dead volumes and also reduce the problem of weakly adsorbed
gas. " qualitative description of the tests available with the in-flow instrument TBDC$C@ 44 is reported
hereunder.
N.'.&. PD 6emperature Pro8ramme Desorption7
The TBD analysis allows defining the strength, the number and the type of active sites
available on the surface of a catalyst by the determination of the quantity of gas desorbed from the
catalyst submitted to a linear temperature ramp. "fter degassing, reducing or otherwise pretreating the
sample to be analy:ed in order to eliminate contaminants, such as water naturally adsorbed on the sample
surface, a constant flow of properly chosen reactive gas is conveyed onto the sample to allow the reaction
between the sample active sites and the reactive gas according to a known stoichiometry.4nce the chemisorptions of the reactive gas is over, desorption is performed by linearly
increasing the sample temperature. The catalyst is placed into a reactor crossed by a flow of inert gas
'nitrogen, helium, argon1, which acts as carrier gas for the molecules of reactive gas desorbing from the
sample.
=hen the temperature at which heat e/ceeds the energy of actiation
of the gas%solid system is reached, the link between the atoms of adsorbate
and adsorbent is broken, and the phenomenon of programmed thermal
desorption takes place The desorbed molecules are dragged by the carrier gas as far as a thermal conductivity
detector 'T6D1, which measures the difference of concentration of the desorbed gas versus a reference
flow. =here necessary, a mass spectrometer can also be connected for a precise assessment of the nature
of the desorbed species.
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The volume of the desorbed species, which can be calculated by appropriate
calibrations of the instrument, together with the knowledge of the stoichiometric factor of the chemical
reaction and the desorption temperature, allow to calculate the number and the strength of the active site.
N.'.. PR 6emperature Pro8ramme Reuction7
The TB$ analysis allows determination of the number and quantity of the reducible
species present in the sample and the temperature at which the reduction itself takes place as a function of
the flow conditions, the percentage of reactive gas, the quantity of sample and the speed of the
temperature increase.
The gas used for this type of analysis is a mi9ture of reactive gas with an inert
gas, as hydrogen in argon or nitrogen at 3 or 4. #enerally the sample is previously o9idi:ed or
pretreated to eliminate possible contaminants and completely o9idi:e the metal portion of the catalyst."lso for this type of analysis, the sample is submitted to a linear increase of temperature and to a constant
flow of the gas mi9ture. The reaction generally starts at room temperature, but at an e9tremely low rate,
therefore negligible.
"t a certain temperature, the reaction rate becomes considerable and the hydrogen
consumption can be monitored through the T6D detector. The signal integration allows calculation of the
quantity of hydrogen consumed and therefore the number of reacting sites. The TB$ analysis also allows
checking the presence of different states of o9idation of the contained metals.
N.'.. P* 6emperature Pro8ramme *Biation7
The TB@ analysis allows evaluation of the temperature range in which a sample undergoes
o9idation due to an o9idi:ing agent contained in a gas mi9ture such as @ )C!e 3 that is flown inside the
reactor containing the sample. In this case, too, the sample is pretreated and the metal o9ides are
previously reduced with pure hydrogen before they are submitted to the gas mi9ture flow and to the linear
temperature ramp to record the o9ygen consumption.
N.'.$. emperature Pro8ramme Reaction
Eesides mi9tures of hydrogen and o9ygen in inert gases, the use of other reactive gases of
acidic or basic type is possible for the assessment of the basic and acidic sites present in a solid. In
general, the analyses in programmed temperature ramp provide spectra where the temperature is
put in relation to the intensity of the signal, which on its turn is proportional to the adsorbed or
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desorbed gas. The e9act amount of gas involved in the process is determined by means of
appropriate calibrations.
N.'.9. Pulse Chemisorption
This type of analysis is performed under isothermal condition. " suitable sampling
system injects known constant amounts of reactive gas 'e.g., hydrogen or o9ygen1 and they come in
contact with the sample surface sites accessible to the gas molecules. The active surface coming in
contact with the reactive gas chemisorbs a certain quantity there-of, until complete saturation of the sites.
The total amount of chemisorbed gas is calculated by difference between the area of the peaks recorded at
the end analysis 'saturated sample1 and the areas of the peaks recorded at the beginning of the analysis'when the chemisorption occurs and the sample is not yet saturated1. It has to be stressed that this type of
analysis is e9tremely quick and reproducible.
N.'.J. Pretreatment o! Samples Eefore being submitted to any of the described analyses, the samples must be properly
pretreated to obtain easily interpretable results.
The sample used must generally hae a weight ranging from '''( g to 1g,
according to the characteristics of the sample itself .t usually consists of
powders, pellets or balls of solid material containing a certain percentage of
metal or Cactie phase deposited on an inert support ?eg, alumina, silica,
etc@ The pretreatment is performed to remoe contaminants ?eg, carbon
compounds@ or adsorbed gases that may contribute to errors in the analytical results, as
for instance water. These substances are generally removed by submitting the sample to a gas flow
'reactive or inert1 and to a temperature increase leading to desorption and removal of the undesiredsubstances.
N.'.H "pplications The samples that can be characteri:ed belong to the following applicative fieldsA
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>eterogeneous catalysis
Metal corrosion
Measurement of the acidity and basicity of surfaces
0educibility ?o/idability@ of materials
The instrument used for measuring the !hemisorption surface area is TPD04
Thermo Modal 11'' and is shown in the following fig istory and deelopment of 90D
9%ray photon is a form of electromagnetic radiation production
following the ejection of an orbital electron and subse7uent transition of
atomic orbital electron from states to high to low energy. hen
monochromatic #eam o+ ray photons +all onto a specimen, three #asic
phenomena may result, namely a#sorption, scatter 'or) +luorescence. he
scattered photons may undergo su#se0uent inter+erance leading in turn to
the generation o+ di++raction ma-ima. hese three #asic phenomena +orm
the #ases o+ three important -3ray methods, the a#sorption techni0ue, 1hichis the #asis o+ radiographic analysis, the scattering e++ect, 1hich is the #asis
o+ R? 6pectrometry and 3ray di++ratction studies +or determining lattice
parameters.
The /%ray was discoered by =ilhelm 0oentgen in 1)
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&igure'>( A Simple 3?ray image
.n 1
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introduced the no1 +amous @ragg e0uation +n@ )d SinB), 1hich descri#es
the condition +or di++raction to occur in terms o+ the 1avelength o+ the 3ray
radiation 'O), the interplanar 'PdQ) spacing*s o+ the crystal, and the angle o+
incidence o+ the radiation 1ith respect to the crystal planes '). ?ather and
son @ragg shared the No#el 4rize in 4hysics +or their contri#utions to this
ne1 +ield, 1hich #ecame 2no1n as -3ray crystallography ';$).
N22 The ;lectromagnetic $pectrum, generation of 9%rays, and the :raggsU ;7uation
Nature o+ 3rays> 3rays can #e thought o+ as 1aves 1ith
1avelengths on the order o+ %.( S to (% S. 6horter the 1avelength, the more
energetic the 1ave. @ecause o+ the relatively short 1avelengths o+
electromagnetic radiation in the 3ray region, 3rays are high energy 1aves
and are much more penetrating compared to "B, visi#le, IR, or radio 1aves.
he conversion #et1een energy, +re0uency, and 1avelength is the 1ell3
2no1n de@roglie relationship> h hcE@, 1here is the +re0uency,h
is 4lanc2*s constant ':.:$ - (%3/; Ts), c is the speed o+ light '$.7 -
(%7msec), and@is the 1avelength o+ the radiation ';/).
N2* #eneration of 9 rays
=hen electrons strike a metal anode with sufficient energy, 9%rays
are produced This process is typically accomplished using a sealed /%ray
tube, which consists of a metal target ?often copper metal@ and a tungsten
metal filament, which can be heated by passing a current through it
?typically 1'%1( m+@, resulting in the Cboiling off of electrons from the hot
tungsten metal surface These Chot electrons are accelerated from the
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tungsten filament ?negatie bias@ to the metal target ?positie bias@ by an
applied oltage ?typically 1(%*' kiloolts@ The collision between these
energetic electrons and electrons in the target atoms results in electron from
target atoms being e/cited out of their core%leel orbitals, placing the atom
in a short%lied e/cited state The atom returns to its ground state by haing
electrons from lower binding energy leels ?ie leels further from the
nucleus@ making transitions to the empty core leels
&igure''( characteristic emission spectra of the target material
he di++erence in energy #et1een these lo1er and
higher #inding energy levels is radiated in the +orm o+ 3rays. his
process results in the production o+ characteristic 3rays in +ig ($ 'i.e. 3
rays 1hose energies are uni0ue to the target metal due to the 0uantized
nature o+ the electron energy levels o+ each atom and the uni0ue
energies o+ these energy levels) UCu =('8/ to = electronic transition> 5 7%; 5
7%&.$ eB, O (./$(< S)V. hus 3rays provide a convenient means o+
determining 1hat elements are present in a sample #ecause o+ the
uni0ue 1avelengths produced #y each uni0ue element. A lo1er energy
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process that involves the interaction o+ electrons 1ith the nucleus o+ an
atom in the target metal produces a continuum o+ lo1er intensity 3
radiation over a #road energy range 2no1n as @remstrahllung ';;). As
the voltage on an 3ray tu#e is increased, the characteristic line spectra
o+ the target element are superimposed upon the continuous spectrum
'at right).
&igure')( "eneration of 3?rays
N2- 9%ray diffraction
Crystals are ordered 1ith three3dimensional arrangements o+
atoms 1ith characteristic periodicities. As the spacing #et1een atoms is on
the same order as 3ray 1avelengths '(3/ S), crystals can di++ract the
radiation 1hen the di++racted #eams are in3phase. he @ragg e0uation is
given as n@ )dsinB. ?or a given 1avelength 'O), di++raction can only
occur at a certain angle ') +or a given d3spacing.
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.t should be taken into account that if only two planes of atoms were
diffracting, as sho1n in the +ig(/,
then the transition +rom
constructive to destructive
inter+erence 1ould #e gradual as
the angle is varied. Ho1ever,
since many atomic planes are
inter+ering in real materials, very
sharp pea2s surrounded #y
mostly destructive inter+erence result ';;)
&igure'( 3 ray Diffraction
N2( $ingle !rystal ?aue@ Diffraction
aue Diffraction is one of the oldest,
common 9%ray techni7ues + single crystal of the
material is irradiated with a beam of 9%rays The
diffracted beams produce spots on photographic
film + series of diffraction spots surround the
central point o+ the #eam, corresponding to
di++raction +rom a given series o+ atomic planes
'+ig(;).
&igure'/( lauediffraction pattern
he position o+ the #eam depends on the @ragg di++raction angle,
1hich is determined #y the 1avelength o+ the 3rays and the periodic
spacing o+ the crystal planes o+ atoms 'interplanar spacing ';&).
The symmetry of the diffraction pattern shows the symmetry of the
crystal 9%rays are used to study the crystal structure of materials "or
e/ample, the 9%ray diffraction spectra can be used to identify a material
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&igure'7( Modern Automated 3?ray Diffractometer
N2& Powder Diffraction
+ powder is used to ensure completely random crystal orientation to
get diffraction from all possible planes The diffraction pattern can be
recorded on a flat photographic film or on a !0T ?cathode ray tube@ =hen
the incident beam satisfies the :ragg condition, a set of planes forms acone of diffracted radiation at an angle to the sample $ince the cone of
9%rays intersects the flat photographic filmstrip in two arcs e7ually spaced
from the direct 9%ray beam, two cured lines will be recorded on the
photographic film The distance of the lines from the center can be used to
determine the angle, which can then be used to determine the inter%
planarXdU spacing ?-&@3ray po1der di++ractometers record all re+lections
using a scintillation detector 'in counts per second o+ 3rays).
he pattern o+ di++racted 3rays is uni0ue +or a particular structure
type and can #e used as a P+ingerprintQ to identi+y the structure type.
Di++erent minerals have di++erent structure types, thus 3ray di++raction is
an ideal tool +or identi+ying di++erent minerals.
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&igure'8( $*o 3?ray diffraction patterns produced on photographic film using theDe#ye?Scherrer po*der cameras on the 3?ray diffraction generator.
&igure';( 3?ray diffraction pattern for a po*dersample +aCl-
The diffraction pattern of an unknown sample is measured and is comparedwith already known standards ?Y!PD$ cards@ to identify ithe po
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N26 $cherrer e7uation
The $cherrer method predicts the si8e of crystallites, instead of the
si8e of particle arge particles might contain seeral crystallites >oweer, it
is common that nanometer%si8ed particle contains only one crystallite
Therefore, the si8e of crystallites in nanometer%si8ed Particle as predicted by
the $cherrer relation also indirectly figures out the si8e of particle itself
;/periments proed that the smaller the crystallite si8e, broader the
diffraction peak Nery large crystal with a single orientation produces
diffraction peaks which are nearly ertical line in shape 4n the other hand,
small crystal produces ery wide peak Therefore, the width of the diffraction
peaks gies information on the crystal si8es ?-(@
t thickness of crystallite
/%ray waelength
) "=>M ?full width at half ma/@ or integral breadth
N) :ragg +ngle
N2) +pplication?-6@
6dentificationG The most common use o+ po1der 'polycrystalline) di++raction
is chemical analysis. his can include phase identi+ication 'searchmatch),
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hickness, t O %.H ; 6)cos N)7
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investigation o+ highlo1 emperature phases, solid solutions and
determinations o+ unit cell parameters o+ ne1 materials.
Polymer crystalline(+ polymer can be considered partly crystalline and
partly amorphous The crystalline domains act as a reinforcing grid, like the
iron framework in concrete, and improe the performance oer a widerange
o+ temperature. Ho1ever, too much crystalinity causes #rittleness. he
crystalline parts give sharp narro1 di++raction pea2s and the amorphous
component gives a very #road pea2 'halo). he ratio #et1een these
Intensities can #e used to calculate the amount o+ crystalline in the material.
N* $!+33.3# ;;!T043 M.!04$!4PZ ?$;M@
N*1 =hat is $canning ;lectron Microscopy ?$;M@ The scanning electron microscope ?$;M@ uses a focused beam ofhigh%energy electrons to generate a ariety of signals at the surface of solid
specimens The signals that derie from electron% sample interactions reeal
information about the sample including e/ternal morphology ?te/ture),
chemical composition, crystalline structure and orientation o+ materials
ma2ing up the sample. In most applications, data are collected over a
selected area o+ the sur+ace o+ the sample, and a $3dimensional image isgenerated that displays spatial variations in these properties. Areas ranging
+rom appro-imately ( cm to & microns in 1idth can #e imaged in a scanning
mode using conventional 65M techni0ues 'magni+ication ranging +rom $% to
appro-imately /%,%%%, spatial resolution o+ &% to (%% nm). he 65M is also
capa#le o+ per+orming analyses o+ selected point locations on the sample
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this approach is especially use+ul in 0ualitatively or semi30uantitatively
determining chemical compositions 'using 5D6), crystalline structure, and
crystal orientations 'using 5@6D). he design and +unction o+ the 65M is very
similar to the 54MA and considera#le overlap in capa#ilities e-ists #et1een
the t1o instruments ';7).
N*2 "undamental Principles of $canning ;lectronMicroscopy ?$;M@
Accelerated electrons in an 65M carry signi+icant amounts o+
2inetic energy and this energy is dissipated as a variety o+ signals produced
#y electron3sample interaction 1hen the incident electrons are decelerated
in the solid sample. hese signals include secondary electrons 'that produce
65M images), #ac2scattered electrons '@65), di++racted #ac2scattered
electrons '5@6D that are used to determine crystal structures and
orientations o+ minerals), photons 'characteristic 3rays that are used +or
elemental analysis and continuum 3rays), visi#le light
'cathodoluminescence33C8), and heat. 6econdary electrons and
#ac2scattered electrons are commonly used +or imaging samples> secondary
electrons are most valua#le +or sho1ing morphology and topography onsamples and #ac2scattered electrons are most valua#le +or illustrating
contrasts in composition in multiphase samples 'i.e. +or rapid phase
discrimination). 3ray generation is produced #y inelastic collisions o+ the
incident electrons 1ith electrons in discrete or#ital 'shells) o+ atoms in the
sample. As the e-cited electrons return to lo1er energy states, they yield 3
rays that are o+ a +i-ed 1avelength 'that is related to the di++erence in
energy levels o+ electrons in di++erent shells +or a given element) ';:). hus,characteristic 3rays are produced +or each element in a mineral that is
Ke-citedK #y the electron #eam. 65M analysis is considered to #e Knon3
destructiveK that is, -3rays generated #y electron interactions do not lead to
volume loss o+ the sample, so it is possi#le to analyze the same materials
repeatedly.
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N** $canning ;lectron Microscopy ?$;[email protected] % >ow Does .t =ork[
&igure'
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Nibration%free floor
0oom free of ambient magnetic and electric fields
65Ms al1ays have at least one detector 'usually a secondary
electron detector), and most have additional detectors. he speci+ic
capa#ilities o+ a particular instrument are critically dependent on 1hich
detectors it accommodates.
The $;M is an instrument that produces a largely magnified image by
using electrons instead of light to form an image + beam of electrons is
produced at the top of the microscope by an electron gun The electron
beam follows a ertical path through the microscope, which is held within aacuum The beam traels through electromagnetic fields and lenses, which
focus the beam down toward the sample ?-ow is a sample prepared
:ecause the $;M utili8es acuum conditions and uses electrons to
form an image, special preparations must be done to the sample +ll water
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must be remoed from the samples because the water would apori8e in the
acuum +ll metals are conductie and re7uire no preparation before being
used +ll non%metals need to be made conductie by coering the sample
with a thin layer of conductie material This is done by using a deice called
a \sputter coater\
N*( $trengths and imitations of $canning ;lectronMicroscopy ?$;M@[?('@
...*(1 $trengths
here is argua#ly no other instrument 1ith the #readth o+
applications in the study o+ solid materials that compares 1ith the 65M. he65M is critical in all +ields that re0uire characterization o+ solid materials.
hile this contri#ution is most concerned 1ith geological applications, it is
important to note that these applications are a very small su#set o+ the
scienti+ic and industrial applications that e-ist +or this instrumentation. Most
65MEs are comparatively easy to operate, 1ith user3+riendly KintuitiveK
inter+aces. Many applications re0uire minimal sample preparation. ?or many
applications, data ac0uisition is rapid 'less than & minutesimage +or 65I,
@65, spot 5D6 analyses.) Modern 65Ms generate data in digital +ormats,
1hich are highly porta#le.
...*(2 imitations
6amples must #e solid and they must +it into the microscope
cham#er. Ma-imum size in horizontal dimensions is usually on the order o+
(% cm vertical dimensions are generally much more limited and rarely
e-ceed ;% mm. ?or most instruments samples must #e sta#le in a vacuum
on the order o+ (%3& 3 (%3:torr. 6amples li2ely to outgas at lo1 pressures
'roc2s saturated 1ith hydrocar#ons, K1etK samples such as coal, organic
materials or s1elling clays, and samples li2ely to decrepitate at lo1
pressure) are unsuita#le +or e-amination in conventional 65MEs. Ho1ever,
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Klo1 vacuumK and KenvironmentalK 65Ms also e-ist, and many o+ these types
o+ samples can #e success+ully e-amined in these specialized instruments.
5D6 detectors on 65MEs cannot detect very light elements 'H, He, and 8i),
and many instruments cannot detect elements 1ith atomic num#ers less
than (( 'Na). Most 65Ms use a solid state 3ray detector '5D6), and 1hile
these detectors are very +ast and easy to utilize, they have relatively poor
energy resolution and sensitivity to elements present in lo1 a#undances
1hen compared to 1avelength dispersive 3ray detectors 'D6) on most
electron pro#e micro analyzers '54MA). An electrically conductive coating
must #e applied to electrically insulating samples +or study in conventional
65MEs, unless the instrument is capa#le o+ operation in a lo1 vacuum mode.
N- :;T ?:runauer, ;mmett and Teller@%$urface areaDetermination
N-1 .ntroduction The surface of a material is the diiding line between a solid and
its surroundings, namely li7uid, gas or another solid =e can anticipate
therefore, that the amount of surface, or surface area, is an important factorin the behaior of a solid $urface area affects, for e/ample, dissolution rates
of pharmaceuticals, the actiity of an industrial catalyst, how fast cement
hydrates, adsorption capacity of air and water purifiers, and the processing
of most powders and porous materials =heneer solid matter is diided into
smaller particles new surfaces are created thereby increasing the surface
area $imilarly, when pores are created within the particle interior ?by
dissolution, decomposition or some other physical or chemical means@ the
surface area is also increased ?(1@
N-2 +ssumptions of :;T ;7uation
The :;T .sotherm ?named for its inentors, :runauer, ;mmett, and
Teller@ allows nitrogen molecules to adsorb on each site
The assumptions used to derie the :;T isotherm are
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1 #aseous molecules behae ideally
2 Multiple nitrogen molecules can be adsorbed to each site
* ;ach adsorbed molecule proides a site for the adsorption of the molecule
in the layer aboe it
- +ll sites on the surface are e7uialent
( 3o adsorbate % adsorbate interactions
& +n adsorbed molecule is immobile
6 3itrogen in the second and higher layers is assumed to be li7uid like
N1* #as $orption
The true surface area, including surface irregularities and poreinteriors, cannot be calculated from particle si8e information, but is rather
determined at the atomic leel by the adsorption o+ nonreactive, or inert gas
The amount adsorbed, letUs call it, is a function not only of the total amount
of e/posed surface, but also ?i@ temperature, ?ii@ gas pressure and ?iii@ the
strength of interaction between gas and solid $ince most gases and solids
interact weakly, the surface must be cooled substantially in order to cause
measurable amounts of adsorption E enough to coer the entire surface +sthe gas pressure is increased, more gas molecules gets adsorbed on the
surface ?in a non%linear way@ :ut, adsorption of a cold gas does not stop
when it has coered the surface in a complete layer one molecule thick ?letUs
call the theoretical monolayer amount of gas 5m@] +s the relatie pressure is
increased, e/cess gas is adsorbed to form PmultilayersQ.$o, gas adsorption %
as a function of pressure % does not follow a simple relationship, and we must
use an appropriate mathematical model to calculate the surface area =e
use the :;T e7uation ?(2@
';5 6Po; P7#'Q O 6C#'7 6Po; P7 ; 5m C F'; 5m C
=here
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N% Nolume of gas adsorbed,
P% ;7uilibrium pressure of adsorbent,
Po% saturation apour pressure,
Nm% monolayer olume of adsorbant,
!%:;T constant
N-- .sotherm types ?(*@
&igure'=( types of isotherm
$ype 6
Pores are typically microspores with the e/posed surface residing almost
e/clusiely inside the microspores, which once filled with adsorbateB leae
little or no e/ternal surface for further adsorption
$ype 66
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Most fre7uently found when adsorption occurs on nonporous powders or
powders with diameters e/ceeding microspores .nflection point occurs near
the completion of the first adsorbed monolayer
$ype 666
.sotherm characteri8ed by heat of adsorption lesser than the heat of
li7uefaction of adsorbate +dsorption proceeds as the adsorbate interaction
with an adsorbed layer is greater than the interaction with the adsorbent
surface
$ype 6V
4ccur on porous adsorbents with pores in the range of 1( E 1''nm +t
higher pressures the slope shows increased uptake of adsorbate as pores
become filled, inflection point typically occurs near completion of the first
monolayer
$ype V
+re obsered where there is small adsorbate absorbent interaction potentials
?similar to type
...@, and are also associated with pores in the 1( E1''nm range
N-( Principles of Measurement
The gas most commonly used is nitrogen "irstly, it is readily
aailable in high purity $econdly, the most appropriate coolant, li7uid
nitrogen, is also readily aailable Thirdly, the interaction of nitrogen with
most solid surfaces is relatiely strong astly, there is wide acceptance ofthe cross3sectional area .n the classical manometric techni7ue, relatie
pressures less than unity are achieed by creating conditions of partial
acuum ?absolute pressures of pure nitrogen below atmospheric pressure@
>igh%precision and accurate pressure transducers monitor those pressure
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changes ?in a fi/ed and known olume@ due to the adsorption process. This
method is easily automated and the amount of gas adsorbed is made at a
number different relatie pressures 5sually, the analy8er obtains at least
three data points in the relatie pressure range between ''2( torr and '*'
torr ;/perimentally measured data are recorded as pairs of aluesG the
amount of gas adsorbed ?Bads@ and the corresponding relatie pressure
?44o@ + plot of these data is called an isotherm The :;T analyser used in
the present study is shown in "ig2'
&igure)>( :$? sorptomotic?'==>
N-& Principles of !alculation
The computer program takes oer and a least%s7uares linear
regression is used to fit the best straight line through a trans+ormed data set
consisting of the following pairs of aluesG
';5as6P%;P7#'Q and P;Po The monolayer capacity, 5m, is calculated
from the slope, S, and the intercept, i, of the straight line,
S+C?'-EVmC
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i'EVmC
$oling for 5m,
5mO';6sFi7
3ow we need the number of molecules in the monolayer, and we get
from that the number of moles Yust diide 5mby the molar olume ?M5) for
the number of moles Multiply number of moles by +ogadroUs number to
arrie at the number of molecules coering the surface in a layer one
molecule thick .f we know how much area one molecule occupies, the total
area is one simple multiplication of number of molecules with cross sectional
area of a molecule Different gas molecules hae different si8es and occupy
different areas =e call that area the Ccross3sectional area?(*@ Therefore,
the total surface area, St,is then calculated from
StO5m"v"m;M5
=here "v is +ogadroUs number, "m is the cross%sectional
area,M5#molar olume of the sample and 5m%3umber of moles ?The surfacearea community@ takes a pragmatic approach, and assumes it to be 1&2
s7uare angstroms ?'1&2 nm2@ on all surfaces +ll surface area results are
finally reported normali8ed by sample weight, or mass, as s7uare meter pergram, written m2Fg or m2g%1
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N.;9P;0.M;3T+
N.1 !haracteri8ation of !hemisorption ?TPD04@G
TPD04 e7uipment ?Thermo Modal 11''@ was used for the
characteri8ation of chemisorption surface area of the hydrogen storage
material, namely Ti and is shown in the figure ?1*@
TPD04 11'' is the single instrument in which one can do temperature
programmed desorption ?TPD@, reduction ?TP0@ and o/idation ?TP4@ and
pulse !hemisorption using a range of pure gas and mi/tures .t can perform
the actiation of one material in one reactor while analy8ing another on the
same instrument The instrument comes as standard with two electrically
heated oens TPD04 11'' is an automatic surface area characteri8ation
unit with good sensitiity
This instrument was used for the characteri8ation of titanium
powder by purging the probe gas such as hydrogen carried by carrier gassuch as argon to the reactor The chemisorption of hydrogen by the titanium
sample was carried out by temperature programmed reduction ?TP0@ and
temperature programmed desorption ?TPD@ During the TP0 process, some
of the supplyied hydrogen gets chemisorbed on the sample used for analysis
?Ti@ and the remaining gas will pass into the T!D producing the signal Thus
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the chemisorption of hydrogen is monitored online by logging the T!D signal
The 7uantity of >2chemisorbed is obtained by the integration of TP0 and
TPD cures Prior to the analysis, the T!D signal was calibrated by injection
of known mass of hydrogen The reactor essel used in the e/periements is
made up of twin 7uart8 tubes in inner and outer configuration $ample gas
enters through outer tube and then enters into the inner tube through
bottom hole and passes oer sample and then reaches the T!D detector
&igure )'( Schematic representation of Pulse Chemisorption in $PDR5
:efore doing the e/periment, the reactor essels were washed
with soap solution and dried in acuum oen for an hour to remoe any
contamination of the sample Pure titanium powder was placed between
glass wool in the inner tube of reactor Then the reactor was fitted into the
instrument The sample was pretreated by flushing with 5>P argon at room
temperature for some time and then heated to 12('! to remoe any olatile
materials and moisture present in the sample +fter completing the
pretreatment, the sample was processed for analysis mode TP0 and TPD
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analysis for the >2chemisorption was carried out as function of temperature
from -''o! to &''o! >eating rates is 2'o!Fmin to optimi8e the heating
parameters at which net hydrogen uptake efficiency was ma/imum .n TP0
in analysis mode, hydrogen gas from hydrogen generator was purged at
constant flow rate through the reactor using argon carrier gas and sample
was heated to pre%determined temperature at the fi/ed heating rate
+fter the TP0, the samples were subjected to TPD analysis at the same
fi/ed temperature to estimate the release of hydrogen at the corresponding
temperature "rom the TP0 and TPD profile, the net hydrogen chemisorption
at the particular temperature was determined The TP0 and TPD analysis
were carried out as a function of heating rate to study the mechanism of
titanium hydrogen reaction and to calculate the actiation energy of the
reaction
N.2 characteri8ation using 90D Techni7ueG
9%ray powder diffraction ?90D@ is a rapid nondestructie
analytical techni7ue primarily used for phase identification of a crystalline
material and can proide information on unit cell dimensions and to
determine the particle si8e
90D studies were carried out for the Different Titanium
samples collected from arious sources as gien below
?i@Pure Ti Powder?+lpha +ldrich@
?ii@!ommercial Titanium hydride?+lpha +ldrich@
?iii@Titanium Powder $ubjected to full cycles of TPD04
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The typical instrument related parameters were operating oltage of -' kN,
current of *' m+ for the /%ray tubeB scan speed of ''2$ %1 with counting time
of *s per step and an angular range ?2@ of 1'' to )'' The 9%ray
diffractometer was calibrated using silicon $0M &-'a as an e/ternal
standard $cintillation detector was used to detect the diffracted 9%rays
The sample was installed in 8ero reflection glass plate and
mounted on to the sample holder of the 9%ray powder diffractometer +
collimated beam of the 9%rays was allowed to fall onto the sample The
diffracted 9%rays were made to fall on the detector by moing the detector
by an angle of 2 ^ degrees relatie to the incident beam The detector output
was collected and stored in a data base The relatie intensities were plottedas a function of 2 ^ to obtain the diffractogram and were superimposed in
order to facilitate inter%comparison
N.* !haracteri8ation of Physisorption surface area
using ?:;T@
#as adsorption was the most widely used techni7ue for the
total surface area measurements #as molecules of known si8e are
condensed onto the unknown sample surface, by completely coering the
surface and opening the pores of each particle with a condensed gas The
gas surface area analy8er can be characteri8ing the surface, including
irregularities and the pore interiors down to an atomic leel The techni7ue
re7uires a clean surface, as the sample has to be taken to an eleated
temperature under acuum to Coutgas as a necessary step To measure the
Physisorption surface area of the titanium sample, Cout gassing is the firststep to remoe any impurities and moisture present in the surface of the
sample "or out gassing 1g of sample was taken in the sample holder and
subjected to out gassing at 12( _! for 2- hrs +fter out gassing the sample is
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ready for analysis The instrument is used for the measurement of
Physisorption surface area
3itrogen is often the gas used as its molecular si8e was inert
and was aailable in high purity at a reasonable cost The Cout gassedsample under high acuum in the sample tube is immersed in a coolant bath
of li7uid nitrogen at %1
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!%:;T constant
"inally the Physisorption surface area of the sample is calculated
using the formula,
StO5m"v"m;M5
=here
"vis +agadroUs number
"mis the cross%sectional area
M5#molar olume
5m%3umber of moles
N.-!haracteri8ation of micro structure of the Titaniumsample using ?$;M@G
The $canning ;lectron Microscopy and ;nergy Dispersie+nalysis ?$;MF;D+9@ 5ses electron instead of light to form the image .t hasa ery high resolution than any other techni7ues >ere this techni7ue is usedto determine the microstructure of the titanium sample
The samples were imaged using + Philips 9%*' modal ;lectron
microscope with proision for ;D+9 This techni7ue is one of the most usefulmethods for inestigating the microstructure of materials The electron beam
emitted from a heated anthanum he/a boride cathode gets focused by a
system of magnetic lens ?usually two condenser lenses and one objectie
lens@ +cceleration oltage of 2'KN is used to accelerate the electrons To
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generate the re7uired acuum, ion getter pump was used which produces a
acuum leel of about 1'%)millibar The electron beam scans the specimen in
much the same way as in cathode ray tube for image formation on the
screen =hen the primary electron interacts with the specimen, electrons
and other radiation are produced that can be used to form images and to
analy8e chemically the elements present on the surface of the sample Three
modes of operations are secondary electron mode, backscattered electron
mode and 9%ray spectroscopy $econdary electrons are formed by interaction
of the primary electrons with loosely bound atomic electrons .nformation on
the chemical composition is obtained by energy dispersie spectrometry
?;D+9@ 9%rays are produced during de%e/citation of outer electrons into the
inner shell acancies of the analyte atoms These acancies are produced
due to the interaction of inner shell electrons with the high energy electron
beam + $i ?i@ detector was used for detection of 9%ray The Titanium
sample was made into small pellets and was mounted on the sample holder
and placed in the analysis chamber of $;M +fter attaining a acuum leel of
1'%6torr, the electron beam was impinged on the surface of the diffusion
electrode where catalyst was placed $ince the electrode was haing carbon
as supporting substrate, conductie coating was not re7uired The surfacemicrostructure was studied at arious magnifications and the chemical purity
of the catalyst was inestigated by ;D+9
!>+PT;0N..
N.. 0esult and discussion
The systematic study of any e/periment will not be fulfilled without
discussing its results The results and discussion are of much importance for
the analysis .t also gies an interpretation results for internal behaior of the
material structure and its properties
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>ence, in this chapter results of studies related to hydrogen sorption
capability carried out on titanium samples are discussed The fresh titanium
powder was characteri8ed by 90D, :;T and $;M "igure1 shows the 90D
pattern of fresh titanium powder and the alues of the sample peaks are
matching with Y!PD$ alues for Ti The titanium powder has the ma/imum
peak at -'1'and has the crystal structure of he/agonal closed pack ?>!P@
The chemisorption studies were carried out using TPD04 instrument
The structural and morphological studies of the samples were carried out by
90D, $;M and the surface area measurement by :;T
0 10 20 30 40 50 60 70 80 90
-200
0
200
400
600
800
1000
1200
1400
1600
004
112103
110102
002
100
101
Intensity
2 theta
Untreated Fresh Titani!
&igure))( 3RD pattern for fresh titanium
sample
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400 450 500 550 600
-2000
0
2000
4000
6000
8000
10000
12000
14000
,ea+ted-antity*.H2#!
i+r*!*'e/(&
Te!"eratre#$%&
hydr*(en +he!is*r"ti*n#T,&
&igure)/( uantity of hydrogen reacted on titanium po*der +FmoleEg-
and maintaining at the re7uired temperature The integration of TP0 graph
gae the peak area in mNs The peak area was conerted to 7uantity of
hydrogen from calibration parameters
"rom the graph it ery clear that up%to sample temperature of -'' 4!, therewas no hydrogen chemisorption on the titanium powder =hen temperature
was increased to -2(4!, the sample started to chemisorbs hydrogen The
7uantity of hydrogen chemisorbed was estimated by integration of the TP0
graph The 7uantity of hydrogen chemisorbed by sample as a function of
temperature is gien in the "ig%2- "ig%2- clearly reeals that the 7uantity of
hydrogen chemisorption increases from -2(o! and reaches peak alue of
126*- `molFg at (''o! ?which corresponds to &'A stoichiometry@
=hen the temperature was increased further to (2(4!, chemisorption of
hydrogen on titanium sample was decreasing to )1*6`molFg =hen the
sample temperature was increased further to (('4!, chemisorption of
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.t is seen that the hydrogen storage capacity of Ti increases steadily with
temperature up to (''4! and further increase in temperature bring down the
hydrogen storage capacity drastically "ig2& shows the hydrogen desorption of
titanium sample at temperature -'' %&''4!.t can be found that the hydrogen
releasing from Ti sample steadily increases with temperature up to &''4
420 440 460 480 500 520 540 560 580 600 620
0
1000
2000
3000
4000
5000
6000
7000
8000
,e'eased-an
tity*.H
2#!i+r*!*'e/(&
Te!"eratre#$%&
Hydr*(en diss*r"ti*n#T&
"ig26 shows the comparison of TP0 and TPD profiles of hydrogen for
Ti .t is desirable to hae high chemisorption and less desorption of hydrogen
to hae net hydrogen storage "rom the graph it is eident that at
temperatures between -2(o! to (''o!, the net storage is high The net
hydrogen storage results obtained by TP0 and TPD studies are gien in table%
1 The temperature of (''o! was selected to be optimum to hae high net
hydrogen chemisorption +t (''o!, the study on repeatability of
chemisorption and desorption were carried out and the chemisorption was
highly reproducible and is shown in "ig2)
6&| P a g e
&igure)8( uantity of hydrogen released on titanium
po*der +FmoleEg-
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.n this techni7ue, the chemisorption was measured by the amount of
hydrogen gas chemisorbed on the gien sample, .e -6))gFmol of Ti reacts
stochiometrically with 2gFmol of >2
&igure);( +et trappin8 e!!iciency uantity of hydrogen on titanium
po*der +FmoleEg-
to form -
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&igure.)< 0ydrogen chemisorption on titanium po*der at 7>>5C
temperature
$a#le( trapping efficiency of hydrogen chemisorption on titanium po*der*ith )>5CEM6 on different temperature />>?8>>5c
6)| P a g e
S.+
*
3-IG1
6m87
PR
-M
P.
6 *C7
ty o!
1(
reacte
6Tmol;8
7
rapp
e ty
U
PD
-M
.
6 *C
7
ty o!
1(
release
6Tmol;87
rapp
e ty
+et
trappin8
e!!iciency
6Tmol;87
1 ''2)1 -''4
!
3. ''A -''4
!
3. ''A 3.
2 ''*'6 -2(4
!
)-&' -'A -2(4
!
66(
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?#Ray i!!raction stuies on lattice moi!ication o!
titanium on chemisorption o! hyro8en
"ig 2< shows the 90D pattern of untreated Ti powder, commercial Ti>2
and Ti metal with chemisorberd >2The phase purity of the commercially
aailable titanium powder was inestigated by 90D diffraction
measurement "igure2< displays the 90D pattern of the sample and all the
major reflection can be inde/ed to the titanium phase, which were in
e/cellent agreement with the Y!PD$ The crystalline planes andcorresponding ?hkl@ alues of titanium are ?11'@,?''2@,?1'1@,?1'2@,?11'@,
?1'*@ and ?2'1@are obsered
The figure ?2@ as well as itanium ?Ti@ phase The ma/imumintensity peaks, 111 planes correspond to titanium hydride ?Ti>2@ and ''2
planes corresponds to the titanium ?Ti@ $ince we obsere titanium peaks, we
conclude that hydrogen chemisorption on titanium is taking place at the
optimi8e leel only
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The 90D peaks gae clear indication of nano si8ed titanium
powder The particle si8eXdU of titanium was estimated by Debye%$cherrerUs
e7uation
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&igure>( :$ result for titanium
0.6
p/p00.0 0.1 0.2 0.3 0.4 0.5 0.6
0.5
p/(Vads
(p0-p))/cm-3
g
0.1
0.2
0.3
0.4
0.5
&igure'( :$ result for titanium hydride
Table ?-@ shows the measurements of Physisorption surface area of
the titanium and titanium hydrides powder There is much difference found
between surface area of titanium ?'))@ and titanium hydride ?))2@ The
graphs 1 and 2 were obtained from the two samples ?Ti, Ti>2@ The graphs
were obtained by plotting PF ?Nads?P4%P@ Ns ?PFPo@ and a straight line ise/pected "rom the graphs we obsere that the e/tent of adsorption
increases with increase in pressure
$a#le/( Measurement of Physisorption surface area using :$
)*| P a g e
$ample $ample wt?g@ Physisorption surface
area ?m2Fg@Titanium 1(-(( '))
Titanium hydride 16-2* )2)
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$;M Measurement
+fter the chemisorption of hydrogen on Ti powder by TP0, the sample was
characteri8ed by $;M for studying surface morphology $ince powder samples
cannot be handled in the $;M instrument, the sample was pellatised The $;Mimage of Ti with chemisorbed hydrogen ?Ti>2@ is shown in the "ig *2 "rom the "ig it
is obsered that particles si8e is around 2'%*' nm Particle si8e was also estimated
by 9%0ay diffraction using $cherrer e7uation The particle si8e for Ti> 2 formed by
TP0 was 2) nm which was in agreement with $;M results >oweer, due to the
pelleti8ation some regions in the samples were obsered to hae flattened surface
een for highest resolution
&igure )( SM image of hydrogen chemisor#ed $itanium
+$i0)-
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C+a9ter III
Summary an conclusion
The earlier studies done in this field proided remarkable opportunities
for the research on the subject as it is an actie field of research in which
new inestigation are currently being carried out The literature surey done
by the author reiews the work done in the field of hydrogen chemisorptionF
desorption .t has created a thirst to research scholars to know more about
chemisorption behaior of metals and its applications
The present study is mainly focused on the hydrogen
chemisorptionFdesorption on Ti powder samples by TP0 and TPD methods
The optimum temperature for hydrogen storage on the samples was
established and the parameters will be of great importance in storing
hydrogen produced from industrial processes +t the gien parameters, the
ma/imum storing capacity of hydrogen in titanium powder samples were
demonstrated and was found to be 11( g of hydrogen per litre of titanium
sample which is in ery good agreement with literature alues and the
storage capacity is obsered to be similar to that of li7uid hydrogen
The titanium before and after chemisorption were characteri8ed by
90D, :;T and $;M techni7ues for its structure, morphology and surface
area
The structural studies with 90D shows a ery sharp peak for fresh
Titanium and broad peak for Titanium chemisorbed hydrogen ?Ti>2@ 3o
peaks of impurities are detected The 90D pattern is good agreement with
the Y!PD$ and the particle si8e calculated from the 90D pattern is found to
be of *' nm
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The surface area measurement for the "resh Titanium and hydrogen
chemisorbed Titanium ?Ti>2@ sample using :;T is studied and the
measurement of surface area is found to be for Titanium ?')) m2Fg@ and
Titanium hydride ?))2m2Fg@ due to the high surface area in the Titanium
hydride
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0eference
1 ight metal hydrides for reersible hydrogen storage application
Yianfeng Mao uniersity of =ollongong
2 =orld business council for sustainable deelopment,?2''-@ #enea,
$wit8erland +ailable an ine atG www =bcsd 4rg
* The impact of fuel economics regulation in .ndia, uniersity of
Maryland, college park department of economics?2'1'@ on Eline at G
wwwnscw ;duFcerrepFworkshopsF documentsFchugh%comporesources
Pdf
- ;nergy and transportation science diision ?;T$D@ on% line at
wwwornlgo?2'1*@
( >ydrogen based ehicalee research initiatie is making on line at
www 0enewable energy world !om?2'')@
& 5s department of energy hydrogen program 2''& annual merit reiew
proceedings, technology,www >ydrogen energy #o and www "uel
economy #o
6 3 3 #reenwood, + ;arnshaw, C!hemistry of the ;lements, 4/fordB
:oston, :utterworth%>einemann ?1
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1allar,, " >ofmeister,
; 3ewbacher, +, Vieger, M+#3+%$T;N0 "ahr8engtechnik +# !o K#
+%)'-1 #ra8, +wstric
2' >igh capacity hydrogen storage materialsG attributes for
automotie application and techni7ues for materials discoeryG% Yum
yang +ndrea $udik, !hristopher wolerton and Denaid j siegel
published as an +dance article on the wet 1- th$eptember 2''
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2) #erd utiering, Yames ! =illiams, engineering materials and
processingG titanium, second edition, $pringer publications, ?2''6@
2
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*
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(' $canning ;lectron Microscopy ?$;M@ $usan $wapp, uniersity of
=yoming
(1 Porous material PrimersG% $urface +rea Determination, Suanta
chrome instruments
(2 >anot et al, ;niron $ci tecnal, **, -2('%-2((, ?1