ContentslistsavailableatSciVerseScienceDirect
Fluid
Phase
Equilibria
j o ur n a l ho m e p a g e :w w w . e l s e v i e r . c o m / l o c a t e / f l u i d
Effects
in
the
solubility
of
CaCO
3
:
Experimental
study
and
model
description
B.
Coto
a,∗, C.
Martos
a,
J.L.
Pe ˜
na
b,
R.
Rodríguez
a,
G.
Pastor
aaDepartmentofChemicalandEnergyTechnology,ESCET,UniversidadReyJuanCarlos,C/Tulipáns/n,28933Móstoles,Madrid,Spain bTechnologyCenterRepsol,28933Móstoles,Madrid,Spain
a
r
t
i
c
l
e
i
n
f
o
Articlehistory:
Received23December2011
Receivedinrevisedform13March2012 Accepted14March2012
Availableonline23March2012
Keywords:
Calciumcarbonate Scale
Solubility Electrolytes ELEC-NRTL
a
b
s
t
r
a
c
t
Crudeoilisusuallyco-producedwithreservoirwater,withincreasingcontentintheproductionfluid alongfieldlife.Changesintemperature,pressure,and/orchemicalcompositionmaycausesignificant precipitationofinorganicsalts(“scales”)duringproduction.Therefore,theknowledgeoftheinfluence thatdifferentvariablesmayhaveonsaltsolubilityiscriticaltoanticipateoridentifypotentialflow assur-anceproblemsrelatedtoscales.Thepresentworkisspecificallyfocusedinthestudyofcalciumcarbonate precipitateformationasamaincomponentof“scales”.Duetothenumberofvariablesinvolvedin cal-ciumcarbonateprecipitation(temperature,pressure,CO2partialpressure,othersaltcontent)andthe heterogeneityofreservoirconditions,thereareseriouslimitationstoperformafullexperimentalstudy coveringallthepossibleprecipitationscenarios.Solubilitydatapresentedinthiswork,bothpreviously reportedandexperimentallydetermined,coverawiderangeofexperimentalconditions.
Asimulationmodelthatallowsquantitativepredictionsindifferentscenariosisaninterestingtool. AversatilesimulationalgorithmwasdevelopedusingASPENPLUS®7.1fromAspenTechnology,Inc.,
thatallowsdifferentexperimentalconditionsandthequantificationoftheinfluenceoftemperature, pressureandpHinCaCO3solubility.Thissimulationschemewasappliedtodescribebothliteratureand newexperimentalsolubilitydata.Predictedresultswereinreasonableagreementwithexperimental information.Thesolubilityofcalciumcarbonatedecreaseswithtemperature,increaseswithpressure andshowsamaximuminpresenceofNaCl.TheCO2partialpressurehasstrongeffectbecauseitisdirect relationwithsolutionpHthatmodifytheamountofionicspeciespresentintheaqueoussolution,and henceincreasingthesolubilityofcalciumcarbonate.SpecialattentionwasdevotedtosuchpHeffect but,inordertohaveafullypredictivemodel,noparametersfitwascarriedout.Themainconclusionof thisworkisthesuitablesimulationschemetodescribeandpredictthesolubilityofcalciumcarbonate atdifferentconditions.
©2012ElsevierB.V.Allrightsreserved.
1. Introduction
Thestudyoftheeffectofdifferentvariablesonthesolubility
ofcalciumcarbonatein aqueoussolutionis importantto
antic-ipateand/ormitigatepotentialflow assuranceproblemsdueto
calciumcarbonatescaleformationanddepositionduringcrudeoil
andassociatedwaterproduction.Reliabledataofcalcium
carbon-atesolubilityasafunctionoftemperature,totalandpartialCO2
pressure,pHandothervariablesarerequiredtocalibrateaccurate
simulationmodelscapabletoreproducethiscomplexequilibrium.
Thesolubilityofcalciumcarbonateinwaterhasbeenpublished
indifferentsourcesatroomtemperatureandhighertemperatures
[1,2].
Ingeothermalfluids,significantamountsofcarbondioxidemay
existat reservoirpressure and temperatureconditions[2].This
∗Correspondingauthor.Tel.:+34914887089;fax:+34914887068.
E-mailaddress:baudilio.coto@urjc.es(B.Coto).
compoundhasastronginfluenceintheequilibriumofcalcium
car-bonatesolutions,andthesaltsolubilityisstronglyconditionedby
thepresenceofthisgas.
Thecomplexityofthedescriptionofthesolubilityofcalcium
carbonateinwaterisduetothepresenceofsimultaneous
chem-icalequilibriaofa highnumber ofspecies(CO32−,HCO3−,CO2,
etc.)involvedinthisprocessbetweensolid,liquidandgasphases.
Furthermore,ifhydrocarbonphasesarealsopresentinreservoir
conditions, CO2 willalso be present in the liquid hydrocarbon
phase, addinganotherphase totheequilibriatobeconsidered.
Accordingtothesecomplexequilibria,theeffectofbothCO2
par-tialpressureandpHcanmodifythedistributionofdifferentionic
species,affectingthedepositionorthesolubilizationofthecalcium
carbonate[3].
Theeffectofpressurealoneonthesupersaturationof
carbon-ate mineralsin water solutions hasusually minor significance.
More important is the effect on the calcium carbonate
sol-ubility of carbon dioxide and the related chemical reactions
that lead to the formation of CaCO3 precipitate. Firstly, the
precipitationofCaCO3 iscontrolledbythefollowingequilibrium
(1):
Ca2++2HCO
3−CaCO3(s)+CO2+H2O (1)
Thusaspressuredecreases,CO2iseffectivelylostfromsolution
tothegasphase.Consequently,thedrivingforceleadingtothe
pre-cipitationofCaCO3isincreasedaccordingtotheaboveequilibrium
[4].
Secondly,thelossofCO2fromthesolutionresultsina
reduc-tionintheconcentrationofcarbonicacidbythefollowingchemical
equilibrium(2),whichconsequentlyresultsinanincreaseinbrine
pH[2,3,5–7].
CO2+H2OH2CO3 HCO3−+H+ (2)
On theotherhand, thehighnumber of ionic species which
appearinthesolutionofcalciumcarbonatemakestheavailability
oftheinteractionparametermatrixofelectrolytethermodynamic
modelapriorityforpropersimulationmodels.
Formationwaters containedin sedimentaryrocksmay have
salinityvaluesinarangeofapproximatelyfiveordersof
magni-tude[8],fromdilutemeteoricwaters,withtypicalvaluesofsalinity
below10gl−1,towaterswithsalinityhigherthan600gl−1.
Consid-erableprogresshasbeenmadeinpredictingthesolubilityofmany
commonreservoirminerals,likecalciumcarbonate,insolutions
withhighionicstrengthbyapplyingthePitzer virial-coefficient
approachtoestimateionactivities[9–12].AswellasPitzer
thermo-dynamicmodel,localcompositionmodelsthatexpresstheexcess
Gibbsfreeenergyduetoshortrangeintermolecularinteractions
suchastheWilson,NRTLandUNIQUACmodelshavebeenused
asactivitycoefficientmodelsinthepredictionofsaltprecipitation
[13–15].
Asmentionedabove,calciumcarbonateisoneofthemainsalts
whichmaycauseflowassuranceproblems,creatingdepositsonthe
productionflowlines.Inthiscase,theslowkineticofthesolubility
processofcalciumcarbonateandtheinfluenceofpH,temperature,
pressure,etc.[16]maychangetheequilibriumofthissalt.Asall
thementionedvariableshaveabigeffectontheprecipitationof
calciumcarbonate,itisachallengetocarryoutafullexperimental
studycoveringallthepossibleconditionsandtodevelopsimulation
modelsabletodescribealltheexperimentalinformation.
Thecalculationofactivitycoefficients ofsaltsin a saturated
solutionisthemain probleminorder topredictthescale
pre-cipitation.ThePitzerandTheElectrolyteNon-RandomTwoLiquid
(ELEC-NRTL)modelsarethemostwidelyusedmodelstoestimate
theactivitycoefficientsforaqueouselectrolytesystems[17].
TheELEC-NRTLmodelwasoriginallyproposedbyChenetal.
[18,19], for aqueous electrolyte systems and later extended to
mixedsolventelectrolytesystems[5,20].TheELEC-NRTLmodelis
aversatilemodelfor thecalculationof activitycoefficients that
canbeappliedforalltheconcentrationrangeusingexclusively
binaryparameters,whilePitzermodelisrestrictedtoelectrolyte
concentrationuptoapproximately6m.
Despitethelimitationsofthemodels(absenceofbinary
inter-actionparametersofsomeelectrolytes),theirapplicabilitytothe
calculationofthethermodynamicequilibriumofelectrolyte
solu-tionshavebeentestedbymanyauthors[5–7,10,11].
Duetothechallengesandcomplexityofthecalciumcarbonate
system,thepresentworkisfocusedonthecompilationofreliable
experimentaldatatoevaluatethesolubilityofcalciumcarbonate
inaqueoussolutioninawiderangeofoperatingconditionsandthe
validationofathermodynamicmodelforcalciumcarbonate
solu-bilityevaluation.Theinfluenceofparameterssuchastemperature,
pressure,andpresenceofNaClinthesolutionwillbestudiedbya
simulationmodelunderASPENPLUS® v7.1software.Thisstudy
focusesinpredictingrealistic oilfieldwatersystems,and
there-fore,thecalciumcarbonatesolubilitywasevaluatedathighvalues
ofionicstrengthusingbothexperimentalandtheoretical
proce-dures.Noliteraturedatawerefoundatthesamerangeofionic
strengthvalues.Thevalidationofthismodelwascarriedoutwith
calciumcarbonatesolubilitydataalreadyreportedintheliterature
andexperimentaldataobtainedinthepresentwork.
2. Experimental
Table1summarizesCaCO3 solubilitydatareportedinthe
lit-eraturebydifferentauthors[1,12,21–47]atdifferentconditions
oftemperature,ionicstrength,etc.Theexistingreporteddataare
relativelyscarce,and notalltheexperimentalconditionsofthe
describedexperimentswerereported.
Thesolubilityofcalciteishighlyinfluencedbytheamountof
carbonicacidpresentinthesolution(CaCO3 solubilityincreases
withCO2concentration).Inthatcase,calcitesolubilitystudiescan
bedividedintodifferentgroupsaccordingtotheamountofcarbon
dioxideemployed.Manystudiesarefocusedoncalcitesolubilityin
purewater,withoutthepresenceofCO2[21–25].Toachievethat
purpose,alltheCO2dissolvedinthewateriseliminatedbyusing
vigorousboiling.
Ontheotherhand,otherauthorsstudythecalciumcarbonate
solubilitywithdissolvedCO2.Forthatpurpose,pureCO2 is
bub-bledintothesolutionkeepingconstanttheamountofCO2,while
thetemperatureand/orpressurearechanged [15,26–37].Many
oftheseauthorsmeasuredcalcitesolubilityinCO2–H2Omixtures
(CO2concentrationislowerthansaturationvalue).Anotherstudies
usedagasphaseconstitutedbycarbondioxideandN2orairin
dif-ferentproportions.Wehaveusedliteraturedatawithexperimental
conditionssimilartoourwork.
Thesolubilityofcalciumcarbonatewasexperimentally
deter-mined in aqueous solution at different ionic strengths and
temperature.Purecalciumcarbonateandsodiumchloridereagent
gradeACS,providedbySCHARLAB,wereused.Thesolutionswere
preparedwithdeionizedandultrapurewater(MilliQ).
TheexperimentalsystemisaRADLEYScarrouselwithsix
her-meticclosedsphericalglassreactors(250mLeachone)thatcan
bestabilizedatthesameconditionsofpressureandtemperature
(temperaturewas controlled within±0.1◦C). An excess of
cal-ciumcarbonateinwaterorinaNaClsolutionwasstirredat95◦C
andatmosphericpressureineachreactoruntilphaseand
chemi-calequilibriawerereached(approximately4days)asdenotedby
conductivity,pHandcalciumconcentrationvalueswereanalyzed
along timeand usedas equilibriaindicators.A continuous
stir-ringof650rpmwasmaintainedduringalltheexperiment.Every2
days(stabilizationtime)asmallaliquotofsupernatantliquidwas
removed(∼1mL),weightedandfilteredthrougha0.45mfilter.
Thefiltermustbewarmedpreviouslyattheexperimental
temper-aturetoavoidanyprecipitationorsolutionofsolid.Afterwards,the
glassreactorstemperaturewasdecreased10◦Candthementioned
experimentalprocedurewasrepeatedagainuntilthetemperature
reached25◦C.Inordertostudytherepeatabilityoftheprocedure,
threedifferentsamplesweretakenateachtemperature.ThepHof
thesampleswasmeasureddirectlyfromeachreactoratevery
tem-peraturewithaCRISONMM40multi-meter,calibratedpreviously
withtwobuffersolutionofpH7and4.01.
Theamountofcalciumindissolutionwasanalyzedby
Induc-tivelyCoupledPlasmaAtomicEmissionSpectroscopy(ICP-AES)on
aVARIANVistaAXAxialCCDSimultaneousICP-AES
spectrome-ter.Calciumwasanalyzedattwowavelengths,315.887nm−1and
317.933nm−1,andtheaveragevaluewasused.Calibrationcurve
wasobtainedfromStandardcalciumsolutions(concentrationof
1000mg/L,providedbySCHARLAB).Twodifferentlinear
Table1
Literaturecalciumcarbonatesolubilitydataandexperimentalconditions.
Author Year Reference T(◦C) PCO2(bar) CNaCl(moldm−3)
Segnitetal. 1962 1 75–200 40 0
Segnitetal. 1962 1 100 1–60 0
Miller 1952 27 0–105 1–100 0–0.5
Ellis 1963 31 100–300 2–150 0
Milleroetal. 1984 12 25 – 0.1–6
Ponizovskiietal. 1980 41 25 0.02 –
ShterminaandFrolova 1945 43 – – –
ShterminaandFrolova 1957 42 – – –
Kaasaetal. 2005 44 – – –
Nagy 1988 45 – – –
FrearandJohnston 1929 36 25 1 –
Hastingsetal. 1927 46 38 – 0.024–0.2
Yanatéva 1955a 28 0–55 1 –
MacDonaldandNorth 1974 24 1–25 25.3–962.6 –
Weyl 1959 37 10–70 1 –
Mitchell 1923 26 25 1–24 –
LeatherandSen 1909 33 15–40 1 –
Johnston 1915 34 16 1 –
LyashchenkoandChuragulov 1981 25 25 1–1000 –
Kindyakovetal. 1958 22 25–75 1 –
Kendall 1912 21 25–100 1 –
Morey 1962 23 25–350 200 –
Yanatéva 1960 30 70 1 –
Ellis 1959a 29 98–302 1.9–142.3 –
Malinin 1963 32 100–300 2–150 –
SharpandKenedy 1965 38 197–300 20–1000 –
Nakayama 1968 47 25 0.01–1 –
Plummeretal. 1982 39 0.1–90 0.30–0.98 –
Wolfetal. 1989 40 10–60 0.01 0–6
3. Simulationmodel
Thesolubilityequilibriumofcalciumcarbonatewassimulated bymeansofflash separator (Fig.1)using ASPENPLUS®,which
allowstheeffectofthedifferentparametersintheCaCO3solubility
tobeevaluated.
Theflashseparatorisfedbytwostreamscontainingvapourand
liquidphases.Theinletliquidstream(LIQ-IN)containscalcium
car-bonatesaturatedwater(introducedinthesystemasCaCO3solidin
excesspluswater).Theinletvapourstream(V-IN)canbeformed
bycarbondioxideand/orair,andmaybesaturatedwithH2Oat
thesamepressureand temperatureconditionsofthefirstflash
separator.
Pressure,temperatureandstreamcompositionsaresetupin
thisfirstflashseparator.Attheseconditions,thechemicalis
sim-ulatedandthreephasesequilibrium(liquid,gasandsolidCaCO3).
Thefluidoutletfromthefirstseparatorisfedintothesecondflash,
inwhichadifferenttemperatureisfixedatthesamepressure
con-ditions.
ThepHoftheoutletliquidstreamfedintothesecondflash,is
adjustedmodifyingthemolarflowofapureCO2streamuntilthe
experimentalpHvalueisreached.
Thisschemeisrepeatedtoreproduceexperimentalconditions
fromthehighesttemperature95◦Ctothelowest25◦C.Thestreams
atthermodynamicequilibriumthatleavethelastflashseparator
areconstitutedbytheCO2 and asmallamountofH2O(vapour
phase)andbyatwophasesstreamthatcontainsallionicspecies
insolution(liquidphase)andtheprecipitatedcalciumcarbonate
(solidphase)ateverypressureandtemperaturevalues.
Thechemical reactionstakeninto accountin thesimulation
processarethefollowing:
CaCO3(s) CO32−+Ca2+ (3)
CaCO3→ CO32−+Ca2+ (4)
H2O OH−+H3O+ (5)
2H2O+CO2HCO3−+H3O+ (6)
H2O+HCO3−CO32−+H3O+ (7)
CaOH+Ca2++OH− (8)
NaCl→ Cl−+Na+ (9)
TheNRTLactivitycoefficientmodelmodifiedfor electrolytes
systems(ELEC-NRTL)wasusedforthesimulations.Thecalcium
carbonatesolubilitywascalculatedascalciummolarconcentration
consideringallthecalciumspeciesinaqueoussolutiononcethepH
wasadjustedateachtemperaturestep.
4. Resultsanddiscussion
Initially,theinfluenceoftemperatureontheCaCO3 solubility
processwasevaluatedforbothexperimentalandliteraturedata,
comparingtheavailableCaCO3solubilityprovidedbythe
simula-tionmodel.Table2showsthevalueofpHandcalciumcarbonate
solubilityin the differentcases studied,thetemperature range
studiedwasbetween25and95◦Cat1barofpressureanddifferent
concentrationsofNaClfrom0to2.4moldm−3werestudied.The
thermodynamicmodelwasusedtosimulatetheexperimentaldata
attheconditionsdescribedinSection2(differenttemperaturesand
atmosphericpressure).Fig.2illustratesthiscomparativestudy.As
itisshown,thethermodynamicmodelsimulatesthe
experimen-taldataofthecalciumcarbonatesolubilityinwateraccurately,the
errorsassociatedwiththemeasureofcalciumconcentrationwas
calculatedbydifferentrepetitionsofthesameexperimentinthe
sameconditions,inFig.2areplottingthedifferenterrorsobtained
ineachpointandaswecanseeinthisfigurethevaluesof
cal-ciumcarbonatesolubilityobtainedineachpointareveryaccurately
withthethermodynamicmodelused.Fig.3showsthe
compar-isonbetweensimulatedcalciumcarbonatesolubility(expressed
ascalciummolarconcentration)withdatareportedinthe
liter-ature [1,27,31].In thesimulation scheme,thetemperaturewas
variedfrom10to170◦Catafixedpressureof40barofCO2 by
usingELEC-NRTLmodel.Strongtemperaturedependenceforthe
Fig.1.ASPENsimulationmodelforthesystem.V-IN=inletvapourstream;LIQ-IN=inletcalciumcarbonatesolution;V-OUT=outletequilibriumvapourstream; LIQ-OUT=outletequilibriumliquidstream(calciumcarbonatesolution);CO2-IN=inletCO2supporttofixedpHvalue;LIQ-PH=obtainedcalciumcarbonatesolutionwithpH
adjustedtoexperimentalvalues.
seen,theseresultsarein reasonableagreementwiththose
ref-erencedinliterature.Afteranalyzingbothfigures(Figs.2and3)
itisremarkablethatthesolubilityofthissaltdecreaseswiththe
temperature,andtherefore,adecreaseofthisvariablereducesthe
precipitationofcalciumcarbonate,asexpected[14].Theeffectof
pressureintheCaCO3illustratedbythesetwofiguresshowsthatif
thepressureincreasesthesolubilityofcalciumcarbonateincreases
too.
Fig.4depictstheinfluenceofthepartialpressureofCO2onthe
solubilityprocessofcalciumcarbonate.Thisfigurecompares
refer-enceddata[1,27]at100◦Canddifferentpressurestothesimulated
values.Asitisshown,thesimulationoftheprocessvaryingthe
pressureintherangeof1–70baratafixedtemperatureof100◦C
yieldsanincreaseofthesolubilitycurveofcalciumcarbonatein
agreementtodatareferencedintheliterature.
The variation in the CaCO3 solubility with pressure can be
explainedbythesimultaneousequilibriumsinvolvedinthis
pro-cess.Asstatedabove,thepresenceCO2isofhighimportanceas
itmodifiestheamountofthespeciespresentinaqueoussolution.
Thus,calciumcarbonateisslightlysolubleinpurewater,butthe
solubilityincreaseswhencarbondioxideispresentinthesolution
[3].Therefore,higherpartialCO2 pressuresmaketheamountof
calciuminthesolutionincrease[1].
Fig.5plotsthesimultaneousinfluenceofthetemperatureand
thepressureofCO2onthesolubilityofcalciumcarbonatevalues
wereobtainedbysimulation.Themostimportanteffectobservedis
theincreaseoncalciumcarbonatesolubilityintwoordersof
mag-nitudeinpresenceofCO2,asstatedabove.Theeffectoftemperature
oncalciumcarbonatesolubility,seemstoincreaseathigherpartial
pressureofCO2,decreasingastemperatureincreases.
AsitismentionedinSection1,thepresenceofcarbondioxide
inthegasphaseisassociatedinadditiontochangesinpHchanges.
Fig.6showstherelationshipbetweenCaCO3solubilityandpHin
theaqueoussolutioncomparingbothsimulationandliteraturedata
reportedbyNakayama[47]atafixedtemperaturevalueof25◦Cat
afixedpressureof1bar.AqueoussolutionpHisofagreat
impor-tanceaslowervaluesofpH(highPCO2)modifiestheamountofthe
speciespresentintheaqueoussolution(increasingtheamountof
Table2
Experimentalcalciumcarbonatesolubilitydataandexperimentalconditionsdeterminedinthiswork.
Experiment T(◦C) P(bar) CNaCl(moldm−3) pHa C
Ca2+b×104(moldm−3)
1 25 1 0.0 8.31 5.26±0.65
2 35 1 0.0 8.34 4.53±0.36
3 45 1 0.0 8.31 3.7±0.43
4 55 1 0.0 8.34 3.34±0.43
5 65 1 0.0 8.35 2.75±0.22
6 75 1 0.0 8.33 2.39±0.27
7 85 1 0.0 8.35 2.27±0.27
8 95 1 0.0 8.34 1.83±0.22
9 25 1 0.6 9.34 9.23±0.37
10 25 1 1.2 9.41 11.01±0.07
11 25 1 1.8 9.67 10.70±0.30
12 25 1 2.4 9.95 10.10±0.46
13 95 1 0.6 8.43 7.92±0.40
14 95 1 1.2 8.54 9.11±0.56
15 95 1 1.8 8.80 8.16±0.33
16 95 1 2.4 9.00 7.40±0.15
aı
100 90 80 70 60 50 40 30 20 0,0 5,0x10-5 1,0x10-4 1,5x10-4 2,0x10-4 2,5x10-4 3,0x10-4 3,5x10-4 4,0x10-4 4,5x10-4 5,0x10-4 5,5x10-4 6,0x10-4
MCa
2+
T(ºC)
Prediction
Experimental data (this work)
Fig.2. InfluenceofthetemperatureontheCaCO3solubility(P=1bar).
200 180 160 140 120 100 80 60 40 20 0,0 5,0x10-3 1,0x10-2 1,5x10-2 2,0x10-2 2,5x10-2 3,0x10-2
MCa
2+
T (ºC)
Experimental data [1] Experimental data [27] Prediction
Fig.3. InfluenceofthetemperatureontheCaCO3solubility(P=40bar).
100 90 80 70 60 50 40 30 20 10 0 0,0 2,0x10-3 4,0x10-3 6,0x10-3 8,0x10-3 1,0x10-2 1,2x10-2
MCa
2+
P (bar)
Experimental data [1] Experimental data [27] Experimental data [31] Prediction
Fig.4. InfluenceofthepressureontheCaCO3solubility(T=100◦C).
HCO3−andCO32−),causingthesolubilityofcalciumcarbonateto
increase.ThesimulateddatausingELEC-NRTLmodelaresimilar
tothetheoreticalvaluesreportedbyNakayama[47].Theseresults
ofcalciumconcentrationareobtainedknowingCO2partial
pres-sureandthermodynamicconstantsinthesameconditionsused
intheASPENsystem.BothresultsemphasizetheinfluenceofpH
(asafunctionoftheamountofCO2inthesystem)inthechemical
equilibriainvolvedatthesolubilityprocess.
Increasesofthesolubilityofasaltincreaseswhenothersaltis
presentisamaintopicinordertosimulaterealformationwater
systems,withsignificantamountsofNa+andCl−ions.The
influ-enceofthepresenceofNaClintheCaCO3solubilitywasstudiedin
thiswork.Table2showsthevalueofpHandcalciumcarbonate
sol-ubilityatdifferentNaClconcentrations.Fig.7showsthevariation
ofCaCO3solubilityagainstthemolarconcentrationofaddedNaCl
atapressurevalueof1barandthreedifferenttemperatures(T=25
and 95◦C) bothexperimentaland simulatedvalues areplotted.
Asitisshown,thethermodynamicmodelaccuratelyreproduces
experimentaldatawhenpHisfittedtoexperimentalvalue.
More-over,analyzingFig.8it canbeseenthat,asexpected,solubility
valuesarehigherforthesimulationsperformedwithaddedNaCl.
AmaximumsolubilityvalueisobtainedforanapproximateNaCl
7,2 7,0 6,8 6,6 6,4 6,2 6,0 0,0 2,0x10-3 4,0x10-3 6,0x10-3 8,0x10-3 1,0x10-2 1,2x10-2 1,4x10-2
MCa
2+
pH
Prediction
Experimental data [47]
Fig.6.EffectofthepHontheCaCO3solubilityat25◦Cand1barairpressure.
concentrationof1.25moldm−3insolutionforallthetemperatures.
ThatNaClconcentration,atwhichsolubilityreachesthemaximum
value,issimilartotheseawatersalinity.Therefore,itisinteresting
toremarkthattheextractionofthecrudeoilwithhighsalinity
for-mationwaterisprobablycarriedoutatmaximumCaCO3solubility
conditions.Thepresenceofmaximumvaluesforallthe
tempera-turesinFig.7leadstotheconclusionthatnoanincreaseofthe
solubilitycanbe reachedalthoughhigher amounts of NaClare
addedtothesolution.
Additionally,thethermodynamicmodelwasusedtopredictthe
solubilityresultsreportedbyMilleroetal.[12]atdifferentNaCl
concentrationatafixedpressureof1barasillustratedinFig.8and
sothecomparisonwithMilleroetal.[12]datacouldonlybemade
todescribetheionicstrengthinfluence.Afteranalyzingsimulated
andexperimentalresultsreportedinthis figure,nomeaningful
differencesamongthesecurvesareshownatlowconcentration
values,until1moldm−3ofsodiumchlorideconcentration,whereas
athighervaluesofionicstrength (NaClconcentration)the
sim-ulationcurveshowsadeviationprobablyduetothedifficultyof
theELEC-NRTLtoreproducehighNaClconcentrations,closetothe
solubilitylimit.
WhenFigs.2,4and8areconsideredtogether,important
dif-ferencesin Ca2+concentration canbeobserved. Fig.2 shows a
calciumcarbonatesolubilityvalue around5×10−4moldm−3 at
25◦C and 1bar of air pressure whereas in Fig. 8 solubility is
2.5 2.0
1.5 1.0
0.5 0.0
0.0 1.0x10-4 2.0x10-4 3.0x10-4 4.0x10-4 5.0x10-4 6.0x10-4 7.0x10-4 8.0x10-4 9.0x10-4 1.0x10-3 1.1x10-3 1.2x10-3
MCa
2+
MNaCl Prediction
Experimental data T = 25 ºC (This work) Experimental data T = 95 ºC (This work)
Fig.7. InfluenceofthepresenceofNaClontheCaCO3solubilityat1barairpressure.
6 5 4 3
2 1 0 1,5x10-4 2,0x10-4 2,5x10-4 3,0x10-4 3,5x10-4 4,0x10-4 4,5x10-4 5,0x10-4 5,5x10-4 6,0x10-4 6,5x10-4
MCa
2+
MNaCl
Prediction
Experimental data [12]
Fig.8. InfluenceofthepresenceofNaClontheCaCO3solubilityat25◦Cand0.97atm
CO2pressure.
around9×10−3moldm−3at25◦Cand1barofCO2pressurewhen
MNaCl=0moldm−3. On theother hand,Fig.4 shows a value of
solubilityaround2×10−3moldm−3at100◦Cand1barofCO2
pres-sure.Thisdifferentmagnitudeorderinsolubilityvaluecannotbe
explainedintermsofpressureortemperaturechanges.A
signifi-cantdifferenceisobtainedbyanalyzingpHvaluesinthesethree
cases.FordataplottedinFig.2,theinvolvedpHwas8.33
deter-minedexperimentallyandreproducedbysimulation.However,for
dataplottedinFigs.4and8,theinvolvedpHwere5.48and6.07,
respectively,bothdeterminedbysimulationfromthe
experimen-talconditionsreportedinliterature.Therefore,thepresenceofCO2
isamainvariablebecauseitmodifiessignificantlythepHofthe
solutionwhichhasastrongeffectonsolubilityvalueinagreement
withthatshowninFig.6.
Asithasbeendemonstratedduringthesimulationstudy,this
thermodynamicmodelmaybeappliedtorealcrudeoilproduction
schemes,beingausefultooltopredictpotentialscalingproblems.
Consequentlythetestedmodelcanbesatisfactorilyconsideredto
describetherealCaCO3solubilitychemistryandbeusedtoevaluate
conditionstoavoidorminimizeoilformationrisk.
5. Conclusions
In the present work,a thermodynamicmodel under ASPEN
PLUSsimulationenvironmentwasconsideredtoevaluateCaCO3
solubilityinwater.ELEC-NRTLmodelandseveralionicequilibria
wereconsidered.Inthisschemeasimplephaseseparatorwasused,
beingthesystempressureiscontrolledbyintroducingavapour
phasestreamwheretheamountofCO2canbemodified.The
influ-enceof pressure, temperature,NaCl concentrationand pH was
studiedforbothliteratureandexperimentaldata.Theincreaseof
solubilityofCaCO3withthedecreaseoftemperature,aswellasthe
increaseofpressureandincreaseofCO2partialpressure,arewell
describedandinagreementwithexperimentalvalues.Solubility
showsamaximumagainstNaCltestedconcentrationforsalinity
valuessimilartothathighsalinityformationwaters.The
relation-shipbetweenCO2partialpressureandpHisalsodescribed,leading
totheexpecteddecreaseinsolubilityofcalciumcarbonatewith
increasingpH.
Simulationresultsarealsoinreasonableagreementwiththose
reportedinliterature.However,theeffectofNaClispoorly
pre-dictedbythismodelprovidinghighersolubilityvaluesthanthose
reportedbyMilleroetal.[12].However,themainconclusionofthis
workisthesuitablesimulationschemetodescribeandpredictthe
The application of this model could beused topredict the
amount of calcium carbonate deposited in equilibrium at any
conditions of pressure, temperature, etc. in realistic conditions
during crude oil production, and should be a valuable tool
for flow assurance risk assessment studies to minimize scale
formation.
Acknowledgment
The authors thank REPSOL S.A. for their financial support
throughtheresearchproject“Aseguramientodeflujodecrudos
depetróleo:Estudiodelacompatibilidaddeaguas”.
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