Free Energy and State Equilibriaruben.ucsd.edu/20/r06.pdf · Free Energy and State Equilibria Gibbs...
Transcript of Free Energy and State Equilibriaruben.ucsd.edu/20/r06.pdf · Free Energy and State Equilibria Gibbs...
FreeEnergyandStateEquilibria
Gibbs Free Energy (G)
G=H-TS G1 = G2 G→minimum
Objec5ves:• understandaerosoldispensers• boilingcondi5ons• drugcrystalsandcrystaltransi5ons• mixturesandchemicalpoten5al
Phasesandphasetransi5onsofdrugsubstances
Smole=kBln(Ntotal_nof_states)=Rln(nstates_of_one_molecule)ΔS= nR ln(n1/n2)
PhaseEquilibria• Tradingenthalpyforentropy• Theentropiccontribu5on–TSgainsmagnitudewithtemperature.
• Thetemperatureatwhich
G1=G2,thephasesareinequilibrium,e.g.
0=Δ−Δ
−=−
STHTSHTSH
trstrs
ggll
Clapeyron Equation
dPdT
=Sα − SβVα −Vβ
=ΔStrsΔVtrs
EntropyandPhaseChanges
• Considerasystemanditssurroundingsatnormaltransi2ontemperatureTtrs
• Thesystemisinequilibrium⇒anyheattransferisreversible.
• Entropychange:
Increase in entropy
Increase in entropy
€
Δ trsS =Δ trsHTtrs
trs1 trs2
Ttrs =ΔtrsHΔtrsS
DispensingDrugsasAerosolsforAsthma,COPD,etc.
ThefirstaerosolspraycanpatentwasgrantedinOslo,Norwayin1926toErikRotheim
SalbutamolandBeclometasone:asthmaandallergicrhini5sIpratropiumbromide:COPDoracuteasthmaTolna6ate:forjockitch,athlete'sfootandringworm.Cromoglicicacid:nasalspray,non-steroid,leukotrieneRagonistNedocromil:alsoamastcellstabilizer
metered-doseinhalers
Propellants:FromChlorofluorocarbons(banned)toHydrofluoroalkanes(HFA)
Howdotheywork?HowdoestheoutsidetemperatureaffectitsfuncHon?
(nor)EpinephrineSalbutamolβ2adrenergicreceptoragonist
USAdultswithasthma:18.9million(8.2%)
BoilingLiquidtoGas
• Bubblescontainsolventingasstate,pressuregrowswithT
• Whenvaporinbubblesreachesexternalpressure(atmospheric)solventboils.
• Boilingpointislowerathighal5tudesorlowerpressure.
Pexternal = Pvapor (depends on T)
WaterVaporPressure• Isonly0.03atm@25degC.• Reaches1atm@100degC.•
Pb(Tb)Clausius-Clapeyron
€
ln P2P1
"
# $
%
& ' = −
ΔHvap
R1T2−1T1
"
# $
%
& '
ΔHvap = TΔSvap ≈ −TR ln(Pvap )ln(P) = −ΔHvap / RT
Trouton’srule,BoilingTemperature
• Liquidssubstancesboilatverydifferenttemperatures
• ΔH~TB
€
Δ vapS =Δ vapHTBoiling
≈ const
Benzene +30.8 80.1 +87.2 carbon tetrachloride +30. 0 76.7 +85.8 cyclohexane +30.1 80.7 +85.1 hydrogen sulphide +18.7 -60.4 +87.9 methane +8.18 -161.5 +73.2 water +40.7 100.0 +109.1
ΔvapH0BoilingpointoCΔvapS0[J/(molK)]
Trouton’sobserva5on:ΔvapS0iscloseforawiderangeofsubstancesandTvap.Thereforefromaboilingtemperaturewecanes5mateenthalpyloss:ΔvapH0
BoilingT
FrederickThomasTrouton,Physicist,1963-1922
0=Δ−Δ
−=−
STHTSHTSH
trstrs
ggll
Excep5onsfromTrouton’srule
• Thevaporiza5onentropyranges– from73J/(Kmol)(CH4)– to109J/(Kmol)forwater– normallyΔS=85-89J/(Kmol)or10.5R
• Waterismoreorderedthanotherliquidsbecauseofthehydrogenbondingstructure
• Methaneisunusuallyround
Waterismoreorderedthanotherliquids
Therela5veincreaseinanumberofstatespermoleculeingas:
ΔvapS ≈ 4.5R+ R lnT ≈10.5R
ΔvapS = R lnngnl
#
$%
&
'(
lna− lnb = ln(a / b)ln(ng / nl ) =10.5
ng / nl = e10.5 ≈ 36,500 ~ 30•1200
Halothanevapor
• Halothanevapor(akaFluothane)isaninhala5onalgeneralanaesthe5c(mixedwithO2)
• Itboilsat50C(s5llaboveroomtemperaturebutenoughforhighconcentra5on)
• @20CP=244mmHg(~0.3atm)• Q:ishalothaneagoodpropellant?
DrugDelivery:Aerosols• Gas is thevaporsofa liquidwithboiling
po int s l ight ly lower than roomtemperature. Thismeans that inside thepressurized can, the vapor can exist inequilibrium with its bulk liquid. As gasescapes it is immediately replaced bymore evapora5ng liquid. Since thepropellant exists in liquid form it isdesirable that it be miscible with ordissolvedinthedrug
• Medicinalaerosolssuchasasthmainhalersusehydrofluoroalkanes(HFA),food:nitrousoxide(whippedcream).
BoilingT
AerosolPropellants• Heavypropellants:Deathof21oldArinRugefromaerosol(“Huffing”fromcompressedair)
• Temperature-sensi5vity– ToostrongathighT,stopsatlow
Propellants:FromChlorofluorocarbons(bannedduetoozonedepleHon)toHydrofluoroalkanes(HFA)
Tb=8.92°C-26.3°C
TetrafluoromethaneTb=-127.8°C
PhaseTransi5onsinPureSubstances
• Phaseboundaries–coexistencecurves(twophasescoexist)
• Triplepoint–3phasescoexist
• Beyondcri2calpoint,liquidandgasarefusedtoformsupercri2calfluid
• Solid,Liquid,Gas• Phases–notonlysolid/liquid/gas,butalsoallotropes,• Usually,atgivenP,Tonlyonephaseofpuresubstanceis
thermodynamicallystable
water
CrystalsandAllotropes
Graphite Diamond Theenthalpyandentropyofforma5onofallotropes
H,kcal/molS,cal/molK
Graphite0.001.36Diamond0.450.58But:Graphiteislighter
• Whichformis“forever”?
Crystals
• MostDrugsinthetabletformaremicrocrystals
• Crystalsnaturallypurifythedrugfromthemixture
• Manydrugsorcontrastagentsexcretedintheurinehavethepoten5altoformcrystals.Highconcentra5onanddifferentpHmaybefactors
Crystal-Methmethamphetamine
Purifica5onandslowdeliveryofinsulin
• Oneofthemostimportanthumanproteintherapeu5cagentisinsulin.
• Roleofcrystalsforproteins– 3Dstructuredetermina5on– Purifica5onmethod– Slowdelivery(dependsonacrystalform.3formswithdifferentrateofrelease) Insulincrystals
Thekine5csdependsonthesizethetypeofcrystals
TypicalPhaseDiagrams:CarbonDioxide
• Basicfacts,CO2:0.039%• DryIce:Cooling(leavesnotrace)• Blood:
– 70%to80%isconvertedtobicarbonateionsHCO−3bycarbonicanhydraseintheredbloodcells
– CO2+H2O→H2CO3→H++HCO−3.
– ~10%dissolvedintheplasma– ~10%isboundtohemoglobin
• Solid-liquidboundaryhasaposi2veslope,asformostsubstances
• Thetriplepoint:P=5bar>1atm⇒– liquidCO2doesnotexistat1atm⇒
“dryice”– Phasetransi5on:sublima2on
CarbonMonoxide
• HemoglobincanexchangeO2andCO2• CarbonMonoxidebindsTOOTIGHTLYtohemoglobin
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ImportantPhaseDiagrams:Water• Waterismoredensethaniceat00C,
• Tetrahedralarrangementinice
Deriva5on.Vaporpressuresatvarioustemperatures
• Alongacoexistencecurve:Gα(T,P)=Gβ(T,P)
Gα(T+dT,P+dP)=Gβ(T+dT,P+dP)dGα=dGβ
Vα,⋅dP–Sα,⋅dT=Vβ⋅dP–Sβ⋅dT
• whichrearrangesto:
Clapeyron Equation
dPdT
=Sα − SβVα −Vβ
=ΔStrsΔVtrs
Theexactslopeofphaseboundaryforanyphaseequilibriumofanypuresubstance!
Note:waterP373K=1atm
α
β
Fromthe1stLawanddefofG,q:dG=V⋅dP–S⋅dT
dGgas
dGliquid
Appendix.Deriva5on
VaporPressurevsTemperatureAnalterna5veformofClausius-Clapeyroneq:where• T1andP1areacorrespondingabsolutetemperatureandvaporpressure,samefortheT2andP2pressure• ΔHvapisthemolarenthalpyofvaporiza5on
€
ln P2P1
"
# $
%
& ' = −
ΔHvap
R1T2−1T1
"
# $
%
& '
dPdT
=ΔStrsΔVtrs
=ΔHtrs
TΔVtrs≈ΔHtrs
TVgas=
ΔHtrs
T RTP
#
$%
&
'(
dPP=ΔHtrs
RT 2 ; ln(P) 21 = −ΔHtrs
R1T#
$%
&
'( 21
ln P2P1
#
$%
&
'(= −
ΔHvap
R1T2−1T1
#
$%
&
'(
dGgas
Deriva5on:TheGaslawfor1mole:
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Appendix
Mixtures,Equilibrium&ChemicalPoten5alµ
Singlecompartment• TotalG->minumum
equlibrium
Twocompartments• Chemicalpoten5alµΑofeachcomponentisequalinbothcompartmentsinequilibrium
A(gas)
A(liquid)
• SoluHons• Suspensions• Colloids(milk,
nanopar5cles,colloidalsilver,sulphur,gold)
ChemicalPotenHalµ• G = H-TSisanextensivevariable• ForapuresubstanceJthechemicalpoten5al is
defined asmolarGibbs energy: µJ≡Gm= G/n
• ChemicalPoten7alis molarFreeEnergyof a par7cular chemical ingredient in amixture
• Inamixtureofn1,n2,..,nJ
JinTpJJ n
G
≠
⎟⎟⎠
⎞⎜⎜⎝
⎛
∂
∂=
,,
µ