The abundance and composition of matrix compounds in fire debris samples undergoing ignitable liquid residue analysis frequently leads to inconclusive results, which can be diminished by applying comprehensive two-dimensional gas chromatography (GC × GC). Method development must be undertaken to fully utilize the potential of GC × GC by maximizing separation space and resolution.
Trang 1journalhomepage:www.elsevier.com/locate/chroma
chromatography
Nadin Boegelsacka,b,∗, Kevin Hayesa,c, Court Sandaua,d, Jonathan M Witheye,
Dena W McMartinb, Gwen O’Sullivana
a Department of Earth and Environmental Sciences, Mount Royal University, 4825 Mount Royal Gate SW, Calgary, AB Canada, T3E 6K6
b Department of Civil, Geological and Environmental Engineering, University of Saskatchewan, 57 Campus Drive, Saskatoon, SK Canada, S7N 5A9
c Manchester Metropolitan University, Ecology & Environment Research Centre, Chester Street, Manchester, U.K., M1 5GD
d Chemistry Matters Inc., 104-1240 Kensington Rd NW Suite 405, Calgary, AB Canada, T2N 3P7
e Department of Chemistry and Physics, Mount Royal University, 4825 Mount Royal Gate SW, Calgary, AB Canada, T3E 6K6
a r t i c l e i n f o
Article history:
Received 24 May 2021
Revised 29 July 2021
Accepted 23 August 2021
Available online 26 August 2021
Keywords:
Design of experiment (DoE)
Response surface methodology (RSM)
Multidimensional Analysis
GC × GC-TOFMS
Fire Debris
ILR
a b s t r a c t
Theabundanceandcompositionofmatrixcompoundsinfiredebrissamplesundergoingignitableliquid residueanalysisfrequentlyleadstoinconclusiveresults,whichcanbediminishedbyapplying compre-hensivetwo-dimensionalgaschromatography(GC× GC).Methoddevelopmentmustbeundertakento fullyutilizethe potentialofGC× GCbymaximizingseparationspaceandresolution Thethreemain areastoconsiderformethoddevelopmentarecolumnselection,modulatorsettingsandparameter opti-mization.Sevencolumncombinationswithdifferentstationaryphasechemistry,columndimensionsand orthogonality wereassessedforsuitabilitybasedontargetcompound selectivity, retention,resolution, andpeakshapes,aswellasoverallpeakcapacityandareause.UsingBox-Behnkendesignof experimen-tation(DoE),theeffectofmodulatorsettingssuchasflowratioandloopfillcapacitywereevaluated us-ingcarbonloadingpotential,dilutioneffect,aswellastargetpeakamplitudeandskewingeffect.Therun parametersexploredfor parameteroptimizationwereovenprogramming,inletpressure (columnflow rate),and modulationperiod.Comparing DoEapproaches,Box-Behnkenand Doehlertdesignsassessed sensitivity,selectivity, peakcapacity, andwraparound;alongside target peakretention,resolution, and shapeevaluation.Certifiedreferencestandardsandsimulatedwildfiredebriswereusedformethod de-velopmentandverification,andwildfiredebriscasesamplesscrutinizedformethodvalidation.Thefinal methodemployedalowpolaritycolumn(5%diphenyl)coupledtoasemi-polarcolumn(50%diphenyl) andresultedinanaverageSeparationNumber(SN)exceeding1inbothdimensionsafteroptimization SeparationNumbersof18.16forfirstand1.46forseconddimensionwithoutwraparoundforcompounds withatleastfouraromaticringssignifiedsuccessfulseparationofalltargetcompoundsfromvaried ma-trixcompositionsand allowedforeasyvisualcomparison ofextracted ionprofiles.Massspectrometry (MS)wasrequiredduringvalidation todifferentiateionswherenobaselineseparationbetweentarget compoundsandextraneousmatrixcompoundswaspossible.Theresultingmethodwasevaluatedagainst ASTME1618andfoundtobeanidealroutineanalysismethodprovidinggreatresolutionoftarget com-poundsfrominterferencesandexcellentpotentialforILRclassificationwithinacomplexsamplematrix
© 2021TheAuthors.PublishedbyElsevierB.V ThisisanopenaccessarticleundertheCCBY-NC-NDlicense (http://creativecommons.org/licenses/by-nc-nd/4.0/)
1 Introduction
Ignitable liquidresidue(ILR)analysisprovidescrucialevidence
for arson casesby determining thepresence, type, andsource of
∗ Corresponding author
E-mail address: nboegelsack@mtroyal.ca (N Boegelsack)
an ignitable liquid,which denotesthe remnantsof substancesor mixturesofsubstancesusedtoaidtheinitialdevelopmentor esca-lationofafire.ASTMissuesthemostwidelyusedstandard meth-ods forILRs, covering variousmethods of extractionandanalysis
by GC–MS.ASTME1618 basesILR classificationon their chemical composition,includingpresence ofanalytesofinterest (orgroups
of analytes),equivalent n-alkane carbon range, andboiling point (bp)ranges[1,2]
https://doi.org/10.1016/j.chroma.2021.462495
0021-9673/© 2021 The Authors Published by Elsevier B.V This is an open access article under the CC BY-NC-ND license ( http://creativecommons.org/licenses/by-nc-nd/4.0/ )
Trang 2Despite well-established ILR class profiles and standardized
methods of analysis, arson cases have amongst the lowest
con-viction ratesinNorthAmerica Theremnant natureofILRs,
com-binedwiththepresenceofcombustion,pyrolysis,andmatrix
com-poundsinlargeconcentrations,amplifiesthechallengeof
identify-ingandcharacterizingILRs,leadingtofrequentfalsenegatives[3]
ILR patternrecognitionisevenmore challenginginwildfire
sam-pleswherethephysico-chemicalcompositionofprominentmatrix
compounds is very similar to that of the ILR target compounds,
leadingto anincrease inhomologpeaks(compoundssharingthe
same spacein thechromatogram)[2].In addition,accelerant
ap-plication inwildfireeventscanbemoredispersive, without
pool-ing orother areas ofhigh ILR concentrationsto occur as is
pos-sible in structural fire scenarios, resulting in significantly greater
abundance of matrix interference.Homolog peakscan frequently
beseparatedbyselectionanalysisinMS,whichisoneofthe
rea-sonswhyMSisthepreferreddetectionsystemoverflame
ioniza-tion detectorfor ILRanalysis.However, if severalcompounds
oc-cupy thesamespace, andone ormoreofthesecompounds share
thesamemajorions,theILRsignalcannolongerbedistinguished
frommatrixinterferences
Comprehensive multidimensional gas chromatography
(GC × GC)hasbecomea populartool forhighresolution
separa-tion of complex organic mixtures by reducing the occurrence of
overlapping homologpeaks andemploying differentmechanisms
ofseparation inasingleanalysis.Recent studieshavehighlighted
the potential application for fire debris analysis [2,4,5,6,7] The
majority of these GC × GC studies have been performed on
thermally modulated (TM) systems [2,5,6], but flow-modulated
(FM) GC × GC has been gaining increased popularity due to its
financial accessibility and robust peak parameters in the second
dimensionandefficientmodulationofallvolatilities[8,9,10,11,12]
Integration of GC × GC into routine analysis and commercial
laboratories has been slow due to the perceived complexity of
GC× GCfunctionalityanddataanalysis,aswellastheassumption
that method development will be costly and require training as
it is considered far more complicated than in single dimension
systems
MethoddevelopmentandoptimizationinGC× GCsystemsare
drivenlargelybythedesiretofullyexploitseparationpotential.A
number ofstudies havedescribedGC× GC method optimization
[5,6,10,13,14], including method comparisons [9,11,13] as well as
the applicationofGC× GC toindustrialfires[6].However,much
oftheliterature pertainstoTMsystems,explorestheoretical
con-cepts, such asnumericalmodeling [15],andparameter
optimiza-tion[16]ordonotincludepotentialmatrixeffectsduringmethod
development [5,9,17] Although the 2D separation potential is a
majoradvantageofGC× GC,existingmethoddevelopmentstudies
rarelyprovideadetaileddiscussiononcolumnselection, whichis
oftenperformedonatrialanderrorbasisuntilasuitable
combina-tionisfound[5,6,8,9,11,13],oroptimizetheactualspatial
distribu-tion inthe chromatogram.Instead,thesestudies favortheoretical
peak capacity,which assumes an evenly randomized distribution
of peaks across the available space Lack of spatial optimization
can be partially attributedto the choice ofcolumn combination,
non-optimizedcolumnconditionornon-optimizedmodulator
set-tings Relevant hardwarechoices,such ascolumn combinationor
flowmodulatorsettings,arerarelydiscussedindetailandstill
pri-marilydeducedthroughtrialanderror
Complex method development with a high number of
vari-ables or highlyinteractive variables, asis thecasefor
chromato-graphic analyses, benefits fromdesign of experiments (DoE).The
two main advantages ofDoE are reduction in numberof
experi-mental runsnecessary andsimultaneous investigation of
interac-tion effects Evaluationof responses is oftencoupledto response
surfacemethodology (RSM),which plotspredictedresponses ina
Fig 1 Visualisation of Box-Behnken (A) and Doehlert (B) matrix with center point
(0) in dark gray and sampling points in light gray Two of the three sampling planes for Box-Behnken are shown in light blue Doehlert model is represented as three- dimensional model (top) and two-dimensional model as viewed from above (bot- tom)
multidimensionalmatrixandallowsdeterminationofoptimum re-gionsforvariablesettingsataglance
Awidevarietyofexperimentaldesignsexistandhavebeen ap-pliedtoGCandGC× GCmethoddevelopment, includingfull fac-torial,centralcomposite,Box-Behnken,andDoehlertuniformshell design [14,18,19].Each designhas its own advantagesand disad-vantages In this study, Box-Behnken (sampling pointsvisualized
inFig.1A) andDoehlert(sampling pointsvisualizedin Fig.1Bas 3Dmodel(top)and2Dmodelasviewedfromabove(bottom)) de-signswereusedforanalysis,withacomparativeevaluationofboth models for the final parameter optimization.With the exception
ofmodelcomparisons[18],Box-Behnkenhasbeenappliedto sam-plepreparationstepsmostfrequently[14,20]whereasDoehlerthas beenpredominantly appliedto GCseparation parameters[20,21] Bothdesigns are compatiblewithRSMandhave asimilar model efficiencyandaccuracyforthreevariables[18]
In this paper, we introduce a systematic workflow for FM
GC× GC methoddevelopmentutilizing thebenefits of DoE,and describingindetailthemostimportantGC× GCset-updecisions (columnchoice&modulatorsettings)andparameteroptimization basedonILRanalysis.Inadditiontoreferencestandard materials, simulatedandactual wildfiresampleswereinvestigatedto evalu-ate theproposed ILRanalysis method inrelation to ASTM E1618 [1]undermatrixinterferenceeffects
2 Materials & methods
2.1 Standards and reagents
Benzene(99.9%),carbondisulfide(CS2,99.9%), d8-naphthalene (Cat#: AC174960010), d10-ethylbenzene (AC321360010), dichloromethane (DCM, 99.9%), methanol (99.9%) and toluene (99.9%) were obtained from Fisher Scientific (Ottawa, ON, Canada) A C7–C30 saturated alkanes certified reference mate-rial (Cat#: 49,451-U), PAH Mix 3 certified reference material (Cat#:861,291), and d12–1,3,5-trimethylbenzene (Cat#: 372,374–
1 G) were purchased from Sigma Aldrich (Supelco, Bellefonte,
PA, USA) Deuterated Kovats-Lee retention index mix (KLI mix, consisting of d22-decane, d32-pentadecane, d42-eicosane,
Trang 3d50-tetracosane, d8-toluene, d8-naphthalene, d10-phenanthrene,
d12-chrysene and d12-benz(a)pyrene) was acquired from Cambridge
Isotope Laboratories, Inc (Tewksbury, MA, USA) and
d14–1,2,4,5-tetramethylbenzene (Cat#: d-0269) was purchased from CDN
isotopes(Pointe-Claire,QC,Canada)
Arecoverystandardwascreatedbycombiningd8-naphthalene,
d10-ethylbenzene, d12–1,3,5-trimethylbenzene and
d14–1,2,4,5-tetramethylbenzene inmethanol ata concentration of200 ng/ml
each A 1 ppm aromatic standard mixture containing alkanes
(49,451-U),benzene,PAHs(861,291),andtolueneinDCMwas
pre-paredforthedeterminationofRIvaluesincomparisontoa1ppm
standardofthedeuteratedKovats-Leeretentionindexmix
AccelerantswerepurchasedinCalgary,AB,Canadaandincluded
acompositesampleofgasolineanddiesel.Thecompositegasoline
sample wascreatedby combining 21 gasolinesof various octane
rating 87 (n = 6), 89 (n = 7), 91 (n = 6), 94 (n = 2) collected
fromsevenstations.Thedieselcompositewascreatedby
combin-ingfourdieselsamplescollectedfromfourstations
Controlled burns were conducted on pine and cedar blend
woodchips (Pestell, New Hamburg, ON, Canada), charring them
to a 50% burn Metal quart cans (Uline, Edmonton, AB, Canada)
were filled to approximately 80% with controlled burn material
(41.5 g ± 1.5g) and spiked with250 μl recovery standard
Sim-ulated ILR samples were created by additionally spiking 50 μl
each ofthegasoline anddiesel compositesamples.Allcanswere
extracted in accordance with ASTM guidelines [22] at 90 °C for
16hours
2.2 Analytical system overview
AllanalyseswereperformedonanAgilent7890AGC(PaloAlto,
CA),retrofittedwithanInsightflowmodulator(Sepsolve,
Peterbor-ough, UK) andcoupled to a Markes BenchTOF-Select mass
spec-trometer(Llantrisant, UK).Throughoutthestudy,theinjector was
operated at 250 °C in split mode with a 25:1 ratio and1 μl of
samplewasinjected viaAgilentG4567A(PaloAlto, CA)
autosam-pler.Heliumwasusedascarriergaswithanaveragelinearvelocity
of4.0cm − 1.The MStransferlineandionsourcewere heldat
250 °C The electron energyapplied was70 eV andthe scanned
mass range was 50–400 m/z in electron ionization mode Data
was acquired and processed using the ChromSpace software (V
1.5.1, Sepsolve, Peterborough, UK)and MicrosoftExcel(Microsoft,
Redmond, WA) Adeconvolution algorithm wasused for
integra-tion,withaminimumioncount300,minimumabsoluteareaand
heightof1000,andpeakmergingat10%overlap
The modulatoristhe“heart” ofa multidimensionalsystem,its
primary functionistotrap,refocus,andinjectsequentiallythe
ef-fluentfromtheprimarycolumnontothesecondarycolumn.Flow
modulators are valve-based andusedifferential flowsto ‘fill’ and
‘flush’ a sampleloop (Fig.2) [23].Hardware components include
first and second dimension columns (1D & 2D), a sample loop,
controlled supplyofheliumfromauxiliarylines(regulatedbythe
PneumaticControlModule(PCM)),andcapillarybleedandtransfer
lines During theloading step,the effluentfromthe first column
fills the sample loop When the modulation valve switches the
auxiliary flow, this reinjects the content of the sampleloop into
theseconddimension.Thetimetakentocompleteonemodulation
or‘cut’ofthefirstdimensioniscalledthemodulationperiod(PM)
Typically, effluent from the first dimension are cut by the
mod-ulator into2–5modulation sliceswithseparationon the
second-dimensioncolumnoccurringveryfast,normallywithin38s
Fig 2 FM modulator hardware setup with column and loop dimensions Loop fill
and flush flow directions are depicted as solid and dashed arrows respectively
Method development in GC × GC is challenging but can be achievedby selectingappropriatecolumnsandinstrumentset-up, andoptimizingmodulatorandparametersettings.Mainelements
to consider before method development include composition of analytesof interest andprominentmatrix compounds aswell as employingtargetedversusnon-targetedanalysis.Theseinformthe practical requirements of methoddevelopment andoptimization, such asstationary phase chemistry,column dimensions, modula-torsetup, andoptimizationofovenanddetectorparameters (e.g flow,temperatureprogrametc.).Aschematicoverviewispresented
inFig.3.Theoverallgoalformethoddevelopmentistomaximize selectivity andsensitivity accordingto the application, which for ILR analysis translates to the separation of all target compounds [1]fromothertargetcompoundsaswellascommoninterferences
to allow foraccurate detection andquantification, pattern recog-nition to differentiate ILR classes[1], detector split for optimum
MSsensitivity,andappropriateruntimeforroutineanalysis(<90 mins).Withinthefollowingsectionsweoutlinethestepstakento develop an appropriate GC× GCmethod forILRanalysisusing a flowmodulator
Column selection and changes to the modulator hardware were consideredfirst astheserelate toinstrumental setup ofthe
GC × GC and concern the most important and difficult choices Modulatorandparameter optimizationwere completed following instrumentsetup
2.3.1 Selection of column set
Choice of column sets is one of the most important steps in method development Dictating selectivity of the method, it is drivenbythepropertiesofthesample,includingtargetandmatrix compounds,andtheobjectiveoftheanalysis.Aneffectivepairing shouldhaveappropriateretention,resolution,selectivity,andpeak shape.Themainchoicestoconsiderinachievingthisarestationary phasechemistry,columndimensionsandorder,aswellas orthog-onalityandfilmthickness
Trang 4Elements to consider:
Selectivity, Retention, Resolution, Peak Capacity / Area Usage, Peak Shape
Achieved by:
Stationary Phase Chemistry, Column Dimensions, Orthogonality
Elements to consider:
Sensitivity, Peak Skewing / Amplitude, Carbon Loading, Dilution Effect
Achieved by:
Flow Ratio, Loop Fill, Detector Efficiency
Elements to consider:
Sensitivity, Selectivity, Retention, Resolution, Peak Capacity / Area Usage, Peak Shape, Wraparound
Achieved by:
Oven Programming, Inlet Pressure (Column Flow), Modulation Period
Analytical Question,
Target Compounds,
Sample Matrix
Analytical Answer, Separation of Targets, Resolution Interference
Column Selection Modulator Settings Parameter Optimization
phase length
i.d
film thickness
column order
loop bleed line
transferline detector 2
transferline detector 1
detector settings
PM
column flow oven
settings
injector settings
auxiliary pressure
Fig 3 Workflow steps applied to method development from left to right, detailing practical considerations underneath each step
Table 1
Column pairings installed in first and second dimension including physical dimensions, station- ary phase, and stationary phase orthogonality
Combination 1 D (length m x
i.d mm x f.t μm)
2 D (length m x i.d mm x f.t μm)
Orthogonality
(25 m x 0.15 mm
x 0.25 μm)
BPX50 (5 m x 0.25 mm
x 0.15 μm)
Non-polar × semi-polar
(30 m x 0.25 mm
x 0.5 μm)
BPX50 (5 m x 0.25 mm
x 0.15 μm)
Non-polar × semi-polar
(30 m x 0.25 mm
x 0.25 μm)
BPX50 (5 m x 0.25 mm
x 0.15 μm)
Polar × semi-polar
(30 m x 0.25 mm
x 0.15 μm)
BPX50 (5 m x 0.25 mm
x 0.15 μm)
Polar × semi-polar
(30 m x 0.25 mm
x 0.25 μm)
BPX50 (5 m x 0.25 mm
x 0.15 μm)
Non-polar × semi-polar
(25 m x 0.18 mm
x 0.18 μm)
Mega Wax HT (5 m x 0.25 mm
x 0.15 μm)
Non-polar × polar
(25 m x 0.18 mm
x 0.18 μm)
Mega-5MS (5 m x 0.25 mm
x 0.5 μm)
Non-polar × non-polar
Based on expected analytes and maximum column
tempera-tures,severalcolumncombinationswere tested(Table1).The
in-vestigation was divided into two steps, wherecombinations 1–5
(Table1)werecomparedwiththesame2Dcolumntochoosethe
most appropriate 1D column The chosen column wasthen
cou-pled withadditional2Dcolumns(combinations 6&7) toexplore
whichcolumncouplingmaximizedthepotentialperformance.The
majority of applications start with a non-polar 1D column (5%
diphenyl/95% dimethyl polysiloxane) connected to a more polar
2D column (50% diphenyl/dimethylpolysiloxane) as this column
set separates analytes based on two mechanisms; boiling points
(1D) and polarity ranges (2D) Columns selected for comparison
(Table1) were chosen based oncommoncomposition ofwildfire
samples[2],systemrequirementsforflowequilibration(see2.3.2.),
andcurrentroutinecolumnsusedinGC–MS(non-polar,commonly
30mlength,0.25mminternaldiameter(i.d.))
Column dimensions were chosen with expected acceptability for routine analysis in mind This included column lengths not longer than 30 m to reduce sample analysistime, andthin film thickness (< 0.5μm) asmost ILR compounds are not extremely volatile.Narrowtomedium i.d.(0.15 mmto0.25mm)were con-sideredaslargeri.d.columnsrequirehigherflowrates,whichcan
bedifficulttobalanceinflowmodulation.Orthogonality combina-tions,separationresultingfromindependentretentionmechanisms [24], were investigated for stationary phases It is generally as-sumedthathighlyorthogonalcolumnsetsincreasetheseparation space occupied in the second dimension butinstances of seem-ingly non-orthogonal sets performing better have been reported [24].Although stationaryphaseis traditionallythemain measure
as it relates to selectivity and therefore separation mechanisms, severaldefinitionsfororthogonalityexistintheliterature [25,26] Forthispurpose,orthogonalitywashereinusedasthetraditional
Trang 5eval-uatedusingpeakcapacityassuggestedinSchure&Davis[26]
to-getherwiththeactualpercentageofchromatographicareautilized
Performance betweencolumn combinations wascompared by
evaluating peak capacity betweenthe solvent peak and eicosane
/ naphthalene,separation efficiency, and total percentageof area
used Flow rates were changed for individual columns in order
to keep the flow ratio stable for comparable results (see 2.3.2)
As minimumrequirementformethoddevelopment, eicosane was
chosen as representative for the latest eluting compound in the
firstdimension basedonthetestmixturedetailedinASTME1618
[1] Naphthalenewaschosen as representative approximation for
thelatestelutingcompoundintheseconddimensionbasedonthe
targetcompoundslistedinASTME1618[1]
Theareacoveredinbothretentionspaceswascalculatedin
ac-cordancewiththeCorderomethodincludingwraparoundpeaksas
outlinedinEqs.(1)and(2)[27]:
With l representing the length in minutes (1D) and w
repre-sentingthewidthinseconds(2D)
A%= A co v ered
WithAcovereddescribing the areapertaining to the column
com-binationandApotentialasthetotalareainthechromatogramas
cal-culatedbyEq.(1)respectively.Incaseswhereruntimeswere
insuf-ficienttoelutetargetpeaksuptoKI12400,A%wasmultipliedwith
thepercentageoftargetKI1coveredandannotatedasA%adj
Separation efficiency was compared by tabulating separation
numbers acrosstheKLImix componentsaccordingtothe
separa-tionnumber(SN)asshowninEq.(3):
SN= t R ( j+1) − t R ( j )
W h ( j+1)+W h ( j )− 1 (3)
With tR(j) andtR(j+1) representing retentiontimes of two
con-secutive compounds ofinterest and their respective peak widths
at half height shownas Wh(j) andWh(j+1) Alkanes were used as
referencepointsforSN1,whereasSN2 wasbasedonLI2 reference
compounds SinceWh wasnot readilyavailable inthesecond
di-mension,widthatbasepeakwasusedinsteadforSN2
After calculatingretentionindicesforcompoundsofinterestin
accordance withBoegelsack etal.[7],individual peak resolutions
fortargetcompoundswerecalculatedaccordingtoEq.(4):
R S =1.177(R I2− R I1) (SN+1) (4)
WhereRI1 andRI2areretentionindexnumbersoftwo
consec-utivecompoundsofinterestinasingledimension
Thepeakcapacity(n)wascalculatedbasedonGrushka[28]as
outlinedinEqs.(5)and(6):
N=5.54t
R
W h
2
(5)
WhereNistheplatenumber,tRistheretentiontimeandWh
isthewidthathalfpeakheightofagivencompound
1n=1+N41/ 21nt n
Where 1n is the peak capacity of the first dimension, tn is
the retention time ofeicosane andtS representsthe solvent
elu-tiontime.Theoutputofthepeakcapacityrepresentsthepotential
numberofcompounds thatcan befullyseparatedwithinits
spa-tial boundariesin the firstdimension To account forthe second
dimension,Eqs.(5)&6wereappliedtonaphthaleneforvalues
re-latingtothe seconddimension toyield2n Finally,thetotalpeak
capacity(n)wascalculatedasshowninEq.7:
Using the total peak capacity, the number of possible distin-guishedpeakspinachromatogramwiththesameboundarieswas calculated as Eq (8) in accordance with Bertsch [29], assuming
RS=0.5:
Whereprepresentsthenumberofpeaksappearingassinglets, and m is the number of components in the sample, which was averaged to 3000for a typical diesel on wood matrixsample to simplifythecomparison
2.3.2 Modulator settings
FMsystemsareconsideredmorecomplextooptimizethanTM systems,duetotheprincipaloftheiroperationsandrestrictionsin hardware [13,23] Despite the importance of optimizing modula-torperformance,methoddevelopmentstudiesoftenfocusonlyon the“soft” parameters,solely includingmodulationperiod (PM) in their considerationsforFM systems[11,23].Instead,PM was con-sideredpartoftheparameteroptimizationinthisstudyand mod-ulator settings concentrated onoptimizing flow ratio andcarbon loadinginlightofthedilutioneffect
Flow ratiowasshown tohave a major effecton peak shapes, which in turn affects the ability for consistent integration [10] Calculating the flush: fill volumetric ratio (see Fig 2) in accor-dancewithHarvey &Shellie [10], peak skewingandpeak ampli-tude were evaluated in relation to 2D separation and resolution potential Harvey & Shellie [10] recommended a flow ratio > 30 duringmethoddevelopmenttominimizetheeffectofpeak skew-ing,whereas thispaperassumes flowratios < 40assub-optimal basedonobserveddifferencesduringcolumnselection(2.3.1) Carbon loading was investigated two-fold: by calculating the balancebetweenPCMpressureandbleedlineflowtoensure con-sistentloopfill,andby applyingaBoxBehnkenmodel(see2.3.3.)
toevaluate thex-line lengthsanddiameters (seeFig 2)for opti-mizingdetectorsplitflow
The flow calculator provided by Sepsolve (Peterborough, UK) wasusedto calculatethe requiredsettings tobalance PCM pres-sure and bleed line flow, as well as calculate flow rate results forFID andMS x-lines forthe 4-factor Box Behnken model (see Table 2) Only one detector was in use for this setup as ASTM E1618 [1] prescribes the use of MS as detection method There-fore,thesecond x-line(Fig 2)actedasbleedlineforthe2D col-umn, and holdup time, which is a necessary consideration in a setupwithtwodetectors,couldbedisregardedinthemodel Base-linesettingsassumedforthemodelwereuseofHeliumascarrier gas, 40°C oven temperature, PCM pressure 27.5 psi, 1Dflowrate 0.5ml/min,2D flowrate16 ml/min,anddimensions asshownin Fig.2
Rootmeansquarederrorofprediction(RMSEP)wascalculated
inaccordancewithEq.9:
RMSEP=
1
I
I
i =1
ˆ
y i − y i 2
(9)
Where Irepresents the number ofcompounds presentin the mixture, y is the predicted average resolution and y is the ex-perimentallyrecordedaverageresolutionineachdimension Two-way analysis of variance (ANOVA) with 95% level of confidence wasused toevaluatestatisticalsignificance.Standardmodel eval-uations(multiplelinearregressionsanderrorestimates)were per-formedinJMPTrial16.0.0(SASInstituteInc.,Cary,NC,USA) RSM was also performed in JMP Trial 16.0.0 using desired flowrateoutputsasoptimalregions
2.3.3 Run parameter optimization
Optimization wascompleted usingDoE due tothe interactive nature andnumberofvariables considered Runparameters
Trang 6cho-Table 2
Corresponding coded and actual values used for calculating flow rates of FID and MS x-lines in 4-factor Box Behnken model
Coded value l FID x-line (m) l MS x-line (m) i.d FID x-line (mm) i.d MS x-line (mm)
senasvariablesforthemodelsweremodulationperiod(PM),flow
rate(asafunctionofinletpressure),andovenramp,astheseare
generallyconsideredto havethehighestimpactonGC× GC
per-formance[13,30]
The columnsetconsistedof anon-polar, 5%diphenyl, column
(30 m × 0.18 μm i.d × 0.18 μm film thickness) in the first
di-mensionandasemi-polar,50%diphenyl,column(5m× 0.25μm
i.d× 0.18μmfilmthickness)intheseconddimension.Actual
val-uesasusedforcalculationscanbeseeninTable3,whereascoded
values were standard for Box-Behnken (−1, 0, 1) and based on
the prescribed uniform shell design simplex laid out inDoehlert
[31]forthreevariables
2.3.4 In addition to the evaluation tools described in 2.3.1., average
Sn and Rs for both dimensions were calculated for modeling using
based on their RMSEP for results as given by eq (9)
RSMwasappliedtoresultsofthemodelstodeterminethe
op-timum performancezonesforthethreevariablesunder
investiga-tion,usingmaximaforA%adj.andtheaveragepeakresolutions(RS)
ofeachdimensionasdesiredoutputs.RSMandmodelevaluations
wereperformedinJMPTrial16.0.0
3 Results & discussion
3.1 Column selection
The comparative results of all column combinations are
pre-sented in Table 4 Comparing first-dimension columns
(combina-tions 1 to5), combinations1& 3showed thegreatestresolution
potential inboth dimensionswith thehighest peakcapacity and
potentialnumberofdistinguishablepeaks.Althoughcolumn3had
a higherarea usage andpeak capacity,iteluted lessthan70% of
target compounds in thesame time frame asthe other columns
andresultedinextensivewraparoundstartingbetweenmono-and
diaromaticcompounds.Wraparoundcomplicatesdataanalysisasit
requiresmanual integrationofdata,makingitunsuitablefor
rou-tineanalysis.Timelyelutionisanotherkeyfactorforroutine
anal-ysis;thus,column1wasselectedfor2Dcomparison
As column 1 had a narrow i.d., an equivalent column was usedwitha shorterlength toreduce solventdelayandaslightly largeri.d.topreserveplatepotential.Amediumfilmthicknesswas electedtoraisethetheoreticalplatenumberwhilesimultaneously keepingthecolumnbleedandretentiontimelow forcleanerand fasteranalysis.Comparingseconddimensionperformance(column combinations1,6and7),columncombination7showedthe great-estresolutionpotentialintheseconddimension,leadingtoan in-creasedarea usage.However,thepotentialnumberof distinguish-able peaks performed the worst out of all three combinations Withcolumn combination6 providing the bestresolution in the firstdimensionbuttheworst resolutioninthesecond dimension, column combination1 offered the best overall result for further methoddevelopment
3.2 Stationary phase chemistry
Table4 showsthat combinations1,2 & 5(non-polar × semi-polar)haveagreateraverageresolutionin1Dthancombinations3
&4(polar× semi-polar).Sincepolarityandselectivityofthephase determineretentionandinteractivityofcompoundgroups,thiscan
beattributedtothestationaryphase(5%phenylagainstwax) Ad-ditionally,the maximum operatingtemperature forwax columns
islowerthanthatfor5%phenylcolumns.Thisrestrictsthe poten-tialresolutionforhighbpcompounds,whichisproblematicwhen identifyingheavierILRsinfiredebrissamples
Separation in the first dimension is very important and pri-oritizedin methoddevelopmentasthe second dimensioncannot makeupforanyresolutionlostin1D.One-dimensionalGCmethod developmentprinciplesapply; therefore,linearvelocityshouldbe operated as closely as possible to the optimum indicated from thevanDeemtercurve.Otherexamplesincludeoventemperature rates contributing to the balance between peak shapes and co-elutions,orinletsplitratiosbeingconsideredinconjunctionwith columni.d.toavoidoverloading
Looking closely at the second dimension, negative results for
SN2 avg (combinations 2& 4to 6)indicate that target compounds elutedonthesameplanein2D,asthedifferencebetweentR2was smallerthantheaveragepeakwidth.Consideringthatthebaseline
Table 3
Actual values for chosen parameters (modulation period, inlet pressure, oven ramp) used in model development
Run
P M (s) Inlet pressure (psi) Oven ramp ( °C/min) P M (s) Inlet pressure (psi) Oven ramp ( °C/min)
Trang 7Table 4
Overview of column combination performance including area percentage covered (A%), av- erage separation (SN) and resolution (R S ) in both dimensions, total peak capacity for the system (n) and the potential number of distinguishable peaks (p) appearing as singlets in
an average gasoline/diesel mix + wood matrix sample
Column combination A% SN 1
avg R S1avg SN 2
avg R S2avg n P
widthhadtobeusedforthiscalculation,negativeresultswere
ex-pectedinlightoftherelativelyshorttimeframeformodulation
Columnorderbetween1Dand2Disanimportantfactorforany
GC × GC system Each column characteristics (phase, film
thick-ness, i.d.andlength)isindependentlyimportantforoptimal
sep-arationbutmustalsobeconsideredinrelationtothepairing
col-umn.ThisisparticularlyimportantinFMsystems,whereitis
cru-cial to have an appropriate flow ratio betweenthe columns (see
3.2.1.).Eachflowisaffectedbylengthandi.d.ofitsrespective
col-umn While TM-GC × GC followsthe traditionalrule ofa longer
columnequaling betterseparationalbeitlonger runtime,FM
im-posesadditionalrestrictions.Alongercolumnstillcorrespondstoa
highertheoreticalplatenumber;butalsoleadstohigherpressures
andcomplications inflow balancing.As a result,it isuncommon
to seecolumns exceeding 30min FM systems.When appliedto
ILRanalysis,shorterlengthsupto30mprovedtobesufficientfor
targetcompoundseparations
Balancing i.d.s,TMsystemmethoddevelopmentoftensuggests
usingthesamei.d.infirstandsecond dimensiontoheighten
the-oretical platenumberandoptimizeflow[32],thisisnot thecase
in FMsystems asevident fromTable4.The 0.25mm i.d
combi-nations(2, 4&5) donotshow agreat advantageintheRS1,and
comparepoorlyinareausageandRS2sincethesecond-dimension
i.d.isthesamediameter.This,inturn,negativelyaffectstheir
abil-ity to fully separate large numbers of peaks (see p, Table 4) In
additiontotheregularconsiderationsrelatingtoinjectionmethod,
phaseratio,orretention;i.d hasalargeimpactonflowratioand
related pressure restrictions In FM systems, a smalleri.d inthe
first dimensionwillspeedup analysisandallowforeasier
equili-brationofflow(see3.2.)
3.4 Orthogonality and film thickness
Looking at area usage and resolution in both dimensions for
column combinations in Table 4, combination 7, which had no
orthogonality, outperformed all others in regard to area and 2D
resolution, whereas combination 6 with high orthogonality
out-performed all others inpeak capacity, number ofdistinguishable
peaks and 1D resolution Therefore, it appears that the
orthogo-nality of stationary phases is not the primary factor influencing
separation in the second dimension, confirmingthat true system
orthogonalityisaffectedbyanumberoffactors[25,27].An
impor-tant factor inthe second dimension appearsto be film thickness
basedoncombination7
In theory,film thickness directlyaffects retention (the thicker
thefilm,thelongercompoundsareretained).Thiswasnotevident
from average retention in 1D (Table 4) where the difference
be-tweenvariousthinfilmsoverthelengthofthefirst-dimension
col-umnwasnotapparent.Asfilmthicknessshouldalwaysbe
consid-Fig 4 Comparison of the flow ratio effect on peak skewing (black dotted line) and
amplitude enhancement as shown on naphthalene with flow ratios of 60 (A) and
30 (B)
eredinconjunctionwiththeinternaldiameter,whichplaysavery importantroleforflow-regulatedGC× GC,columnlengthandi.d betweencombinations1,6&7werekeptconstant.Giventhe dif-ferenceinlengthbetween1Dand2D,andthesubsequentamount
oftimecompoundsspendineach dimension,itmakessense that filmthickness hadamuch largerimpact onthe 2Dseparation.A film thickness of 0.15 μm wasselected in 2D to reduce the po-tentialforearlywraparoundduringparameteroptimization.Since filmthicknessoftheseconddimensionhasasignificanteffectonly
on2Dseparation,thiscanbeincreasedatalaterpointasrequired withoutaffectingotherdevelopmentparameters
Area usage inthe second dimension isfrequently not consid-eredimportantinmethoddevelopment.Instead,phase orthogonal-ityisfavoured.Table4illustrates thatpeak capacityandarea us-agearecloselylinked Usingthesevariables asa measureoftrue systemorthogonality assuggestedby Schure &Davis [26], wasa betterapproachforevaluatingcolumnperformancethansolely re-lyingonphaseorthogonality
3.5 Modulator settings 3.5.1 Flow ratio
Fig.4depictstheeffectofflowratioonnaphthalene.Thepeak skewingeffectisrepresentedbytheblackdottedlineandisclearly enhanced in Fig.4B (flow ratio= 30) compared to Fig 4A(flow ratio=60).Theeffectonpeakamplitudecanalsobeobservedas thepeakheightinAismoreconcentrated,whichisrepresentedby darkredarea, andlessdrawnout, whichisshownby adecrease
ingreen&blueareas
As Harvey & Shellie [10]highlighted, sub-optimal flow equili-bration leads to an increase in observed modulation effects, i.e
a higherdegree ofpeak skewingandlower peak amplitudes Al-though they concluded that a flow ratio > 30 was appropriate, Fig.4Bshowedpronouncedartifactsofmodulationeffects.In gen-eral, non-focusing modulation displays broader peak widths in comparisontofocusingmodulation,whichmeans asmaller theo-reticalresolutionpotential butincreasedrobustnessoverlong pe-riodsoftime[12].Avoidanceofmodulationeffectsisthereforean important undertaking to ensure consistently well-shaped peaks
Trang 8Table 5
Dependency table summarizing the impact of increasing the length and internal diameter of transfer lines to MS and FID on the carbon loading to the detector (dilution effect)
Carbon Loading / x-line Flowrate
Impact Quantifier
Length of FID x-line
Internal Diameter
of FID x-line
Length of MS x-line
Internal Diameter
of MS x-line Carbon loading to
FID
loading/flowrate
ing/flowrate
–
Carbon loading to
MS
Low ↑ load-
ing/flowrate
ing/flowrate
–
andmaximumresolution,andaminimumflowratioof40was
re-quiredforthissetup.Althoughhigherflowratiosbetweencolumns
leadtobetterpeakshapes,theymustbebalancedbychoosing
ap-propriatemodulatordimensionstoensureconsistencyofflowratio
andcarbonloadingofthedetector[13]
3.5.2 Carbon loading & dilution affect
InFMsystems,optimizationofcarbonloadinganddetector
ef-ficiency is achieved by balancing flows across the 7- and3-port
valves(seeFig.2)
Basedontheflowcalculator,a2-mlengthwassufficientto
bal-ance flowsacrossthe7-portvalveforthecolumnsetupchosen in
3.1.witha0.1-mmi.d.bleedlinetoensureconsistentcarbon
load-ingin2D.Establishedstandard1Dcolumnflows,whichneedtobe
balanced withbleed lineflow forconsistent loop fill(see Fig.2),
are<1ml/minforcapillarycolumns.Whencalculatingbleedline
flow, thechoice of bleed linei.d was prioritized asit is directly
relatedtoflowrate,whereaslengthisinverselyrelated.Therefore,
choosing a 0.1-mm diameter bleed line i.d prevented the need
forextremelength,whichinturnminimizedpotential carriergas
waste.An imbalanceinflowratioequilibriuminthe 7-portvalve
canleadtoovershootingorundershootingtheloop,whichinturn
negatively affectscarbonloadingandcausesloss of2Dresolution
viapeakskewing(depictedinFig.4)
Table 5 summarizes the variables toconsider when balancing
flows across the 3-port valve and the respective impact of their
changes on each detector flow rate Fig 5 shows an RSM graph
as one example of the relationships outline in Table 5,
specifi-cally therelationshipbetweenMSx-linelengthandFIDx-linei.d
to FID andMS flowrates.The FID flowrate isrepresented by the
yellow-red mesh, whereas the MS flowrate is displayed as light
purple-greenmeshwiththeoptimumregionwheretheyintersect
(11 ml/min and 4 ml/min respectively) The relationship shown
in Fig.5correlates to thebleed lineoptimization.FID flowis
di-rectlyrelatedtoFIDdiameterasshownonthey-axis,resultingin
thehighestflow(redarea)forthelargesti.d.,whereas MSlength
is indirectly related to MS flow, resulting in the lowest MS flow
(grayarea)forthelongestx-line.Theseprinciplesworkviceversa,
meaning that alongerFID x-line resultsindecreasedflow tothe
FIDandincreasedflowtotheMS.Finaldimensionsusedtoachieve
theoptimumratioarelistedinFig.2
The model showed significance for all individual parameters,
aswell astheinteractionbetweeni.d.s,andinteractions between
each x-line length andrespectively opposing x-line i.d The
RM-SEP ofthe modelwas 1.7with 2 = 0.98andhomogenous error
distribution Although resulting calculatednumbers were not
ex-act whencompared totheactual valueoutput ofthesystem,the
evaluationwasperformedrelativetothebaselinesettingsandthe
finaldilutionfactorwasadjustedaccordinglytomaketheuseofa
flowcalculatorsuitable
The desireddetectorsplit flow, alsoreferred toasdilution
ef-fect, regulates how much ofthe total 2Dflow is sent to the
de-tector A 1:4 ratio is considered ideal for MS detector efficiency
topreservemaximumsensitivitywithoutoverloadingthefilament
Fig 5 Flow model RSM displaying relationship between FID x-line i.d and MS x-
line length with effect on MS x-line flow (light purple-dark green, optimum region displayed in light purple) and FID x-line flow (light yellow-red, optimum region displayed in red & dark orange)
andintroducingdetectornoise,whichtranslatedtothesetoptima aftertakingintoaccountthedifferencebetweencalculatedand ac-tualvalues
3.5.3 Parameter optimization
Fig.6showsallRSMgraphsfor“soft” parameteroptimization, comparingBoxBehnken(top)andDoehlertuniformshell(bottom) design The RSM graphs show that area usage isoptimized with shortermodulationtimes(Fig.6A& D).InFMsystems,longerPM risk introducing pressure inconsistencies, which lead to poor re-peatability.RelatingA%andPM,favouringshortermodulationwas expectedasthisgreatly reduces thepotential area to filland in-creasespeakstability.However,aconsiderabledownsideisan in-creaseinwraparound,whichwasnotaccountedforinthisanalysis butwasevaluated manually outsideofmodels.The Box Behnken model(Fig.6A)only showsoneoptimum (whichheavily featured wraparoundfromLI2>150),whereasDoehlert(Fig.6D)displaysa secondoptimumregionwhichdidnotincludewraparoundforLI2
≤ 450.Asimilareffectcanbeseeninrelationtotheinletpressure andareausage (A/D),aswell asthesecond-dimensionresolution andinlet pressure (C/F) Doehlert matricesinvestigate values be-sidesthemodelextremathatBox-Behnkenmodelsexamine,which could explainwhyDoehlert pickedup morecomplexcorrelations withouttheneedforadditionaldatamanipulation
Fig 6B & E shows that a lower temperature ramp increased
1Dresolution.Inagreement withgeneralchromatographytheory,
Trang 9Fig 6 Response surface plots for Box Behnken (A-C) and Doehlert (D-F) models showing responses for adjusted area% against modulation and inlet pressure (A, D), average
first-dimension resolution (R S1avg ) against temperature ramp and inlet pressure (B, E), and average second-dimension resolution (R S2avg ) against temperature ramp and inlet pressure (C, F)
it confirmedthat the firstdimension can be optimizedlike most
traditional GCsystems.The optimum rangefor 1Dseparationlay
between−0.5and−1forbothmodels,whichtranslatestoa
tem-perature ramp of 5°C/min to 1 °C/min.Within thisrange,
feasi-bilityofthetotal runtime woulddictatethechosen rampspeed
Havinga120+minruntime,forinstance,wouldnotbeacceptable
foracommercialthroughputofsamples
Therelationbetweenseparationandinletpressure(asflowrate
equivalent)showedthattheentirerangeinvestigatedcanbe
con-sideredoptimalfor1D(Fig 6B& E),whereas atendencyfortwo
localized optima was expressed in 2D (Fig 6C & F) This trend
was expressed more clearly in the Doehlert model (F) than the
Box Behnken model (C) Although the low point existed around
themediumflowrate,itwasstillconsideredpartoftheoptimum
rangebasedonthecolouring.Astheflow/pressureratiowaskept
constantbetweencolumns,anincreasein1Disdirectlycorrelated
to an increase in 2D While a higher inlet pressure compresses
peaks and improves their peak shape, which in turn favours
in-creased resolution, it can also lead to more frequent co-elutions
andadeclineinp
Both models showed the sameaverage variance of prediction
at 0.4, but Doehlert expressed more correlations whereas Box
Behnken calculated higher model efficiencies Model analysis
re-quires resultsdatatobe distributednormally, whichwasnotthe
caseforthisstudyandmadetheresults statisticallyinsignificant
Critical values for both models were outside of the set
parame-ters, whichcan eithermean that the trueoptimum isoutside of
thesetparametersorthattheentirerangewithintheparameters
is a local optimum,since modeling requires an obvious“fail”
re-sult to be able to calculate optima In this case, the latter took
place as parameters were chosen close to the theoretical
recom-mendations andwithsystematicrestrictions.Atheoreticalsuccess
forseparationisachievediftheseparationnumber(SN)isgreater
than1,whichwasmetbyallmodelpoints.Statisticalinsignificance
ofbothmodelsshowsthatchromatographicexperiencecannegate thenecessityformodelingwhenconcentratingonaverage resolu-tionandefficientuseofchromatographic areaasresults.Alotof variables relatedto flow, oven andinjector settings alreadyhave
anoptimumrangerecommendedbasedoncolumnchoiceandare readilyavailableonline.Theseincludesplitratioormaximumoven temperature or may simply be dependent on target compounds whichimpact filamentdelayorstartingoven temperaturefor in-stance
3.4 Method development & ASTM standards
Afteroptimization,thefinal methodverificationresultedinan averageSN>1inbothdimensionswith18.16forfirstand1.46for seconddimensionwithoutwraparoundforcompoundswithLI2of
atleast 450.The goalof thismethod developmentwas to allow for ILR classification based on ASTM E1618, i.e to provide suffi-cientseparationofallrelevantEIPsandtargetcompounds[1]from eachother aswell asseparation fromcommoninterferences The formerwassuccessfullyachievedduringverification, whereas the latterwasachievedduringvalidation
Fig 7 shows the relationship between the method validation andASTME1618classification requirements,wherelight,medium andheavyrefertobp-basedsubclasses;andalkanes,cycloalkanes, aromaticsandcondensedringaromaticsrefertotheoverallgroup compositionsofeachclass [1,7].Identifiedtargetcompounds cov-eringawiderangeofbpandpolarityarehighlightedbynumbers, exceptfornumerousn-alkanesandalkyl-cyclohexanes, aswellas trans-decalin,whichwereomittedforimageclarity
Achievingclassification in ASTME1618 [1]isbased onthe vi-sual comparison of a reference ignitable liquid to the total ion chromatogram(TIC),extractedionprofiles(EIP)foralkane,alkene, alcohol,aromatic,cycloalkane,ester, ketone, andpolynuclear aro-matic compoundtypes,and/or a target compound chromatogram
Trang 10Fig 7 TIC of two wildfire samples used to validate the developed method highlighting ASTM E1618 ILR classification scheme groups within matrix Target compounds iden-
tified include n-alkanes (along solid line), toluene (1), Three Musketeers including p-xylene (2), Castle Group including o- & m-ethyltoluene (3) and 1,3,5-trimethylbenzene (4), indane (5), Gang of Four (1,3-&1,4-diethylbenzene, 3-&4-propyltoluene, n-butylbenzene, 1-ethyl-3,5-dimethylbenzene, 6), tetramethylbenzenes (Tetris, 7), methylindanes (8), naphthalene (9), methylnaphthalenes (Twin Towers, 10), and Five Fingers including ethylnaphthalenes (11), and dimethylnaphthalenes (12)
(TCC) of the sample[1].All EIP groups andrelevant target
com-poundsareclearlyseparatedinFig.7,signifyingsuccessfulmethod
validation
Additional considerations specific to ILR method development
pertain to missing compounds, suitability of method evaluation,
andextraneous components.Missingcompounds are notunusual
in ILR analysis, asthe exposure to heat can resultin lossof
tar-get compounds on thelighter end, and samplepreparation
tech-niques mayexhibit preferentialrecovery ranges[1]orother
func-tions such as competitive absorption ASTM E1618 only refers to
their test mixture composed ofa selectfew compounds to
eval-uate method suitability While this may suffice for smaller
ad-justmentson anestablished method,theresultspresentedherein
clearlyshowthatthisapproachisnotsufficientformethod
devel-opment asinterferences are not considered Interferences via
ex-traneouscomponentscanconsistofoxygenatedcompounds, paraf-finic,cycloparaffinic,aromatic,orcondensedring aromatic hydro-carbons[1].As showninFig.7,their abundancecan varygreatly betweencompoundgroupsdependingonthematrixcomposition Whilethey cannot beexcluded fromtherespectiveEIPs, their2D retention allows for easier distinction between target compound andextraneous interference,asis shownby the separationof n-alkanes,branched alkanes andalkenes addressingthe exampleof polyolefinorasphaltdecompositioninASTME1618[1]
WhilealltargetcompoundslistedinASTME1618[1]were sat-isfactorily separated in the verification samples, some potential forextraneousinterferencespersistedinthemethodvalidationon wildfiresamples.Fig.8 displaysthree prominentinstances where compounds from an actual wildfire sample matrixcould still in-terferewiththemethod.Withtheseexamplesofincomplete