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Sumatran Light Gravity, API° Gravity SG Sulfur, wt% Total Nitrogen, ppm Acid Number, mg KOH/g Pour Point, °C Charact. Factor (K-FACTOR) Viscosity, cSt at 40°C (104°F) Viscosity, cSt at 50°C (122°F) Vanadium, ppm Nickel, ppm MCR, wt% Ramsbottom Carbon, wt% Asphaltenes, (H.C7) wt%



Sumatran Light



Whole Crude Properties 33.94 0.86 0.09 1231.01 --33.64 12.49 12.17 9.72 0.06 12.43 3.52 3.20 0.62



SUMMARY OF MAJOR CUTS Whole



Light



Medium



Heavy



Crude



Naphtha



Naphtha



Naphtha



TBP Temp At Start, °C



Start



10



80



150



TBP Temp At End, °C



End



80



150



TBP Temp At Start, °F



Start



55



TBP Temp At End, °F



End



175



Yield at Start, vol%



Kero



Atm



Light



Gas Oil



VGO



200



260



340



200



260



340



450



175



300



400



500



650



300



400



500



650



850



0.2



2.9



9.7



17.0



25.7



40.6



Yield at End, vol%



2.9



9.7



17.0



25.7



40.6



63.7



Yield of Cut (wt% of Crude)



2.0



5.9



6.6



8.2



14.6



23.2



Yield of Cut (vol% of Crude)



2.6



6.8



7.3



8.7



15.0



23.1



Gravity, °API



33.9



80.8



60.2



51.5



43.1



38.5



33.2



Specific Gravity



0.86



0.67



0.74



0.77



0.81



0.83



0.86



Sulfur, wt%



0.09



0.00



0.00



0.00



0.01



0.06



0.08



Mercaptan Sulfur, ppm Nitrogen, ppm



0 1231



Hydrogen, wt%



1



1



1



0



0



0



2



37



307



16.2



15.0



14.5



14.1



13.9



13.8



Viscosity @ 40 °C (104 °F), cSt



12.17



0.48



0.69



1.06



1.77



3.83



14.65



Viscosity @ 50 °C (122 °F), cSt



9.72



0.45



0.62



0.93



1.52



3.14



10.81



Viscosity @ 100 °C (212 °F), cSt



4.21



0.34



0.43



0.58



0.85



1.45



3.63



Viscosity @ 135 °C (275 °F), cSt



2.76



0.30



0.37



0.47



0.65



1.00



2.14



Freeze Point, °C



60



-94



-76



-55



-30



9



43



Freeze Point, °F



140



-136



-105



-68



-22



48



109



Pour Point, °C



34



-99



-81



-58



-32



4



37



Pour Point, °F



93



-147



-114



-73



-26



39



99



Smoke Point, mm (ASTM)



5



35



31



27



22



18



10



Aniline Point, °C



96



71



62



65



69



81



102



Aniline Point, °F



205



160



143



150



157



179



216



Total Acid Number, mg KOH/g Cut : this property/stream pair cannot be evaluated for 0.0crude 'SUMLT339-M' 0.0



0.1



0.1



0.1



0.1



Cetane Index, ASTM D4737



49



54



67



Diesel Index



70



129



86



77



68



69



72



12.5



12.6



12.0



12.1



12.0



12.2



12.4



Research Octane Number, Clear



70.3



55.7



37.4



Motor Octane Number, Clear



69.4



56.4



Paraffins, vol%



85.9



58.6



52.7



50.6



Naphthenes, vol%



14.1



35.5



35.4



35.1



Aromatics, vol%



0.0



5.9



11.8



14.1



Characterization Factor (K Factor)



Thiophenes, vol% Molecular Weight



333



103



120



148



180



233



346



Gross Heating Value, MM BTU/bbl



5.91



4.86



5.26



5.46



5.66



5.78



5.93



Gross Heating Value, kcal/kg



10971



11577



11315



11207



11077



11018



10953



Gross Heating Value, MJ/kg



45.9



48.4



47.3



46.9



46.3



46.1



45.8



Heptane Asphaltenes, wt%



0.6



Micro Carbon Residue, wt%



3.5



Ramsbottom Carbon, wt%



3.2



Vanadium, ppm



0



Nickel, ppm



12



Iron, ppm



3



Heavy



Vacuum



Atm



VGO



Resid



Resid



450



570



340



570



End



End



850



1050



650



1050



End



End



63.7



79.2



40.6



79.2



100.0



100.0



15.9



23.3



62.5



15.4



20.8



59.4



28.5



16.2



25.7



0.88



0.96



0.90



0.10



0.20



0.13



713



4458



1960



6.76E+01



7.E+04



1.61E+02



4.44E+01



2.E+04



1.01E+02



9.95E+00



7.E+02



1.85E+01



5.02E+00



1.E+02



8.58E+00



61



79



68



141



175



154



13.2



56



53



44



132



128



112



5



2



3



116



122



113



240



251



235



0.1



0.1



0.1



68



41



60



12.6



12.7



12.6



482



938



457



6.06



6.40



6.14



10883



10602



10817



45.5



44.4



45.3



2.6



1.0



14.7



5.6



13.4



5.1



0



0



53



20



12



5



Date Assayed



9/16/2009



Sumatran Light



DISTILLATION SUMMARY Whole



Light



Medium



Heavy



Crude



Naphtha



Naphtha



Naphtha



TBP Temp At Start, °C



10



80



150



TBP Temp At End, °C



80



150



200



TBP Temp At Start, °F



55



175



300



TBP Temp At End, °F



175



300



400



Yield at Start, vol%



0.2



2.9



9.7



Yield at End, vol%



2.9



9.7



17.0



Yield of Cut (wt% of Crude)



0.2



2.2



8.1



Yield of Cut (vol% of Crude)



2.2



8.1



14.7



°C Start



10



79



150



°C



5%



28



90



152



°C 10%



28



92



155



°C 30%



50



101



165



°C 50%



63



120



175



°C 70%



69



132



185



°C 90%



72



145



195



°C 95%



72



147



198



°C End



79



150



200



°F Start



59



175



300



°F



5%



82



194



305



°F 10%



82



197



310



°F 30%



121



214



329



°F 50%



146



247



350



°F 70%



156



269



370



°F 90%



161



291



390



°F 95%



161



296



395



°F End



175



300



400



TBP Distillation, vol%



TBP Distillation, vol%



Kero



Atm



Light



Heavy



Vacuum



Atm



Gas Oil



VGO



VGO



Resid



Resid



200



260



340



450



570



340



260



340



450



570



End



End



400



500



650



850



1050



650



500



650



850



1050



End



End



17.0



25.7



40.6



63.7



79.2



40.6



25.7



40.6



63.7



79.2



100.0



100.0



14.7



22.9



37.5



60.7



76.7



37.5



22.9



37.5



60.7



76.7



100.0



100.0



200



260



340



450



570



340



203



264



347



454



580



357



207



268



353



457



591



375



220



284



379



474



636



431



232



300



402



495



694



487



244



316



422



522



776



594



255



332



441



553



922



779



257



336



445



562



987



877



260



340



450



570



End



End



400



500



650



850



1050



650



406



508



662



856



1069



681



411



515



674



863



1088



711



433



545



721



891



1170



810



453



574



762



926



1274



912



473



604



798



971



1423



1105



491



634



832



1023



1687



1437



496



642



841



1036



1806



1612



500



650



850



1050



End



End