Macro Complete a Bml

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* note1 This worksheet contains all t * note 2 ABML key words are case insen * note 3 The number 1 through 53 at th * You can change them if you s * note 4 Cells in red are required fie * append the 3 character PIMS q * note 5 Cells in yellow are optional. * note 6 Correlations number 40 onward * They will have a reverse tran * * *TABLE ABML TEXT OPTION CORR1 DriveabilityIndex OPTION1 CORF1 F ENDOPT1 INPROP1 *PIMS tag ABML Tags T10 T50 T90 ENDIN1 OUTPRP1 DriveNdx ENDOUT1 ************** CORR2 D86ONE10BLEND OPTION2 CORF2 F ENDOPT2 INPROP2 *PIMS Tag ABML Tags T10NDX ENDIN2 OUTPRP2 T10 ENDOUT2 ************** CORR3 D86ONE90BLEND OPTION3 CORF3 F ENDOPT3 INPROP3 T90NDX ENDIN3 OUTPRP3 T90 ENDOUT3 ************** CORR4 POURPOINT1

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Transcript of Macro Complete a Bml

Page 1: Macro Complete a Bml

* note1 This worksheet contains all the available abml correlations exposed to PIMS. You can cut and paste the one you need into your worksheet.* note 2 ABML key words are case insensitive. The only exception is the key word OPTION in the column heading. Note that PIMS tags are still case sensitive * note 3 The number 1 through 53 at the end of the key words are there to by pass PIMS requirement of no duplicate row and column name. * You can change them if you so wish.* note 4 Cells in red are required field. You need to put your PIMSquality tag equivalent to the ABML quality tag. Don't forget to * append the 3 character PIMS quality tag with something that will make that row name unique.* note 5 Cells in yellow are optional.* note 6 Correlations number 40 onward are consider index type because they generate values that are blended linearly. * They will have a reverse transform in the set of correlations number 1 through 39.***TABLE ABML

TEXT OPTIONCORR1 DriveabilityIndexOPTION1CORF1 FENDOPT1INPROP1*PIMS tag ABML Tags

T10T50T90

ENDIN1OUTPRP1

DriveNdxENDOUT1**************CORR2 D86ONE10BLENDOPTION2CORF2 FENDOPT2INPROP2*PIMS Tag ABML Tags T10NDXENDIN2OUTPRP2 T10ENDOUT2**************CORR3 D86ONE90BLENDOPTION3CORF3 FENDOPT3INPROP3 T90NDXENDIN3OUTPRP3 T90ENDOUT3**************CORR4 POURPOINT1OPTION4CORF4 FENDOPT4

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INPROP4 PRPNTNDXENDIN4OUTPRP4 POURPNTENDOUT4**************CORR5 VISCOSITY1INPROP5 VISCNDXENDIN5OUTPRP5 VISCENDOUT5**************CORR6 VISCOSITY2INPROP6 VISCNDXENDIN6OUTPRP6 VISCENDOUT6**************CORR7 CETANEINDEX2OPTION7CORF7 FENDOPT7INPROP7 SPG T50ENDIN7OUTPRP7 CETANEENDOUT7**************CORR8 CETANEINDEX4OPTION8CORF8 FENDOPT8INPROP8 SPG T10 T50 T90ENDIN8OUTPRP8 CETANEENDOUT8**************CORR9 CETANEIMPROVEROPTION9CORF9 FP1_9P2_9

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P3_9P4_9P5_9P6_9P7_9ENDOPT9INPROP9 SPG T50 IMPVOLENDIN9OUTPRP9 CETIMPENDOUT9**************CORR10 CLOUDPOINT1OPTION10CORF10 FENDOPT10INPROP10 CPNTNDXENDIN10OUTPRP10 CLDPNTENDOUT10**************CORR11 CLOUDPOINT3OPTION11CORF11 FENDOPT11INPROP11 CPNTNDXENDIN11OUTPRP11 CLDPNTENDOUT11**************CORR12 FLASHPOINT1OPTION12CORF12 FENDOPT12INPROP12 FPNTNDXENDIN12OUTPRP12 FLSHPNTENDOUT12**************CORR13 DONINPROP13 RON MONENDIN13OUTPRP13

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DONENDOUT13**************CORR14 MTMRINPROP14 TRON TMON OLE AROENDIN14OUTPRP14 RON MONENDOUT14**************CORR15 RVPOPTION15P1_15 1.25ENDOPT15INPROP15

RVPNDXENDIN15OUTPRP15

RVPENDOUT15**************CORR16 TVLOPTION16CORF16 FENDOPT16INPROP16

RVPT10T50

ENDIN16OUTPRP16

TVLENDOUT16**************CORR17 CFPPIMPROVEROPTION17CORF17 FP1_17P2_17P3_17ENDOPT17INPROP17 CLDPNT IMPDRATEENDIN17OUTPRP17 CFPPIMPENDOUT17**************

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CORR18 D86FromPercentOffOPTION18TYPCOR18 HC94CORF18 FP1_18 30P2_18 70P3_18 100P4_18 140P5_18 180P6_18 250P7_18 330P8_18 360P9_18 390P10_18 450ENDOPT18INPROP18

POFF1POFF2POFF3POFF4POFF5POFF6POFF7POFF8POFF9POFF10

ENDIN18OUTPRP18

IBPT10T30T50T70T90FBP

ENDOUT18**************CORR19 CARBOB2*OPTION19O2OPTRNDO2RNDRSTEOHAROEOHBNZEOHEHOEOHOLFEOHSULEOHSPGGASSPGEOHVOLENDOPT19INPROP19

ARO

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BNZOLFRVPSULT50T90

ENDIN19OUTPRP19

AROBNZEHOOLFOXYRVPSULT50T90

ENDOUT19**************CORR20 CARBOBOPTION20ESTRM20ENDOPT20INPROP20 OBSRVP OBST50 OBST90 VOLETOHENDIN20OUTPRP20 RVP T50 T90ENDOUT20**************CORR21 CT50BLENDINPROP21 T50ENDIN21OUTPRP21 OBST50ENDOUT21**************CORR22 CT90BLENDINPROP22 T90ENDIN22OUTPRP22 OBST90ENDOUT22**************CORR23 CD86ONE90BLENDINPROP23 T90NDX

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ENDIN23OUTPRP23 OBST90ENDOUT23**************CORR24 CD86FromPercentOffINPROP24

POFF1POFF2POFF3POFF4POFF5POFF6POFF7POFF8POFF9POFF10

ENDIN24OUTPRP24

OBSIBPOBST10OBST30OBST50OBST70OBST90OBSFBP

ENDOUT24**************CORR25 CRVPINPROP25

RVPNDXENDIN25OUTPRP25

OBSRVPENDOUT25**************CORR26 GNDXROUTPRP26

user defined corrENDOUT26**************CORR27 GPRPCALCOUTPRP27

user defined corrENDOUT27**************CORR28 TVL2OPTION28CORF28 FENDOPT28INPROP28

RVPT10T20

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T50ENDIN28OUTPRP28

TVLENDOUT28**************CORR29 VAPORLOCKINDEXINPROP29

RVPE70

ENDIN29OUTPRP29

VLIENDOUT29**************CORR30 EVAPORATIVEOPTION30P00_30P01_30P02_30P03_30P04_30P05_30P06_30P07_30P08_30P09_30P10_30P11_30ENDOPT30INPROP30

IBPT10T30T50T70T90FBP

ENDIN30OUTPRP30

EVP0EVP1EVP2EVP3EVP4EVP5EVP6EVP7EVP8EVP9EVP10EVP11

ENDOUT30**************

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CORR40 D86ONE10INDEXOPTION40CORF40 FENDOPT40INPROP40 T10ENDIN40OUTPRP40 T10NDXENDOUT40**************CORR41 D86ONE90INDEXOPTION41CORF41 FENDOPT41INPROP41 T90ENDIN41OUTPRP41 T90NDXENDOUT41**************CORR42 POURPOINTINDEX1OPTION42CORF42 FENDOPT42INPROP42 POURPNTENDIN42OUTPRP42 PRPNTNDXENDOUT42**************CORR43 VISCOSITYINDEX1OPTION43CORF43 FENDOPT43INPROP43 VISCENDIN43OUTPRP43 VISCNDXENDOUT43**************CORR44 VISCOSITYINDEX2OPTION44CORF44 FENDOPT44INPROP44 VISCENDIN44OUTPRP44 VISCNDXENDOUT44

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**************CORR45 CLOUDPOINTINDEX1OPTION45CORF45 FENDOPT45INPROP45 CLDPNTENDIN45OUTPRP45 CPNTNDXENDOUT45**************CORR46 CLOUDPOINTINDEX3OPTION46CORF46 FENDOPT46INPROP46 CLDPNTENDIN46OUTPRP46 CPNTNDXENDOUT46**************CORR47 FLASHPOINTINDEX1OPTION47CORF47 FENDOPT47INPROP47 FLSHPNTENDIN47OUTPRP47 FPNTNDXENDOUT47**************CORR48 T10INDEXOPTION48CORF48 FENDOPT48INPROP48 T10 T50 T90ENDIN48OUTPRP48 T10BVENDOUT48**************CORR49 T50INDEXOPTION49CORF49 FENDOPT49INPROP49 T10 T50

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T90ENDIN49OUTPRP49 T50BVENDOUT49**************CORR50 T90INDEXOPTION50CORF50 FENDOPT50INPROP50 T10 T50 T90ENDIN50OUTPRP50 T90BVENDOUT50**************CORR51 MTMFINPROP51 RON MON OLE AROENDIN51OUTPRP51 TRON TMONENDOUT51**************CORR52 RVPINDEXINPROP52

RVPENDIN52OUTPRP52

RVPNDXENDOUT52**************CORR53 D86toPercentOffOPTION53TYPCOR53 HC94CORF53 FP1_53 30P2_53 70P3_53 100P4_53 140P5_53 180P6_53 250P7_53 330P8_53 360P9_53 390P10_53 450ENDOPT53

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INPROP53IBPT10T30T50T70T90FBP

ENDIN53OUTPRP53

POFF1POFF2POFF3POFF4POFF5POFF6POFF7POFF8POFF9POFF10

ENDOUT53**************CORR54 GBLNVALOUTPRP54

user defined corrENDOUT54**************CORR31 ND86FROMPERCENTOFFOPTION31TYPCOR31 HC94CORF31 FP1_31 30P2_31 70P3_31 100P4_31 140P5_31 180P6_31 250P7_31 330P8_31 360P9_31 390P10_31 450P11_31P12_31P13_31P14_31P15_31P16_31P17_31P18_31P19_31P20_31T1_31 0T2_31 10T3_31 30

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T4_31 50T5_31 70T6_31 90T7_31 100T8_31T9_31T10_31T11_31T12_31T13_31ENDOPT31INPROP31

P1P2P3P4P5P6P7P8P9P10P11P12P13P14P15P16P17P18P19P20

ENDIN31OUTPRP31

T1T2T3T4T5T6T7T8T9T10T11T12T13

ENDOUT31**************CORR55 ND86TOPERCENTOFFOPTION55TYPCOR55 HC94CORF55 FP1_55 30

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P2_55 70P3_55 100P4_55 140P5_55 180P6_55 250P7_55 330P8_55 360P9_55 390P10_55 450P11_55P12_55P13_55P14_55P15_55P16_55P17_55P18_55P19_55P20_55T1_55 0T2_55 10T3_55 30T4_55 50T5_55 70T6_55 90T7_55 100T8_55T9_55T10_55T11_55T12_55T13_55ENDOPT55INPROP55

T1T2T3T4T5T6T7T8T9T10T11T12T13

ENDIN55OUTPRP55

P1P2P3P4P5

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P6P7P8P9P10P11P12P13P14P15P16P17P18P19P20

ENDOUT55**************CORR34 RBOB*OPTION34EOHARO_EOHBNZ_EOHEHO_EOHOLF_EOHSUL_EOHSPG_GASSPG_EOHVOL_P1_34P2_34P3_34P4_34P5_34P6_34ENDOPT34INPROP34

AROBNZOLFRVPSULT50T90

ENDIN34OUTPRP34

AROBNZEHOOLFRVPSULT50T90

E200

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E300ENDOUT34**************CORR32 E200E300EPA*OPTION32P1_32P2_32P3_32P4_32ENDOPT32INPROP32

T50T90

ENDOUT32OUTPRP32

E200E300

ENDOUT32**************CORR33 CETANEINDEX5OPTION33CORF33 FENDOPT33INPROP33

SPGT10T50T90

ENDIN33OUTPRP33

CETANE ENDOUT33**************CORR35 EPAINPROP35

MTOETOEHOTMOSULRVPE20E30AROOLFBNZ

ENDIN35OUTPRP35

VOCTOXNOXEXBEXT

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ENDOUT35**************CORR36 CARBINPROP36

RVPT50T90AROOLFOXYSULBNZ

ENDIN36OUTPRP36

CNXTHCPOT

ENDOUT36**************CORR37 CARB3INPROP37

RVPT50T90AROOLFOXYEHOSULBNZ

ENDIN37OUTPRP37

CNXTHCPOT

ENDOUT37**************CORR38 T20GAUSSINPROP38

T10T30

ENDIN38OUTPRP38

T20ENDOUT38**************CORR39 VISCOSITY3INPROP39 VISCNDXENDIN39OUTPRP39 VISCENDOUT39**************

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CORR56 VISCOSITYINDEX3OPTION56CORF56 FENDOPT56INPROP56 VISCENDIN56OUTPRP56 VISCNDXENDOUT56**************

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This worksheet contains all the available abml correlations exposed to PIMS. You can cut and paste the one you need into your worksheet.ABML key words are case insensitive. The only exception is the key word OPTION in the column heading. Note that PIMS tags are still case sensitive The number 1 through 53 at the end of the key words are there to by pass PIMS requirement of no duplicate row and column name. You can change them if you so wish.Cells in red are required field. You need to put your PIMSquality tag equivalent to the ABML quality tag. Don't forget to append the 3 character PIMS quality tag with something that will make that row name unique.

Correlations number 40 onward are consider index type because they generate values that are blended linearly. They will have a reverse transform in the set of correlations number 1 through 39.

*CommentsDriveability correlation

Celsius or Fahrenheit

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Pour Point index

Pour Point

Viscosity index

Viscosity

Viscosity index

Viscosity

Cetane Index

Cetane Index

Correlation Coefficients See Appendix A.Correlation Coefficients See Appendix A.

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Correlation Coefficients See Appendix A.Correlation Coefficients See Appendix A.Correlation Coefficients See Appendix A.Correlation Coefficients See Appendix A.Correlation Coefficients See Appendix A.

Improver vol %

Cloud Point Index

Cloud Point

Cloud Point Index

Cloud Point

Flash Point Index

Flash Poiont

Research OctaneMotor Octane

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Road Octane

Transformed Research OctaneTransformed Motor OctaneOlefin vol %Aromatic vol %

Research OctaneMotor Octane

Exponent.

Reid Vapor Pressure Index

Reid Vapor Pressure

ASTM D4814 Linear version.

Reid Vapor Pressure

Temp @ V/L = 20

Cloud PointImprover dosing rate (ppm)

Cold Filter Plug Point

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Points at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculated

% off at P1% off at P2% off at P3% off at P4% off at P5% off at P6% off at P7% off at P8% off at P9% off at P10

D86 initial boiling point

D86 final boiling point

The volume percent of ethanol in this version of CARBOB is an input parameter. This correlation calculates the blend properites if the userspecified amount of ethanol is added to a blend stock. This correlation is for putting specs on blend stocks that will eventually be blended with ethanol and must meet CARB phase3 specs.Handle rounding and oxygen discontinuity problem 0=off 1=on default = 1 (see documentation)Above and round OXY to 1 decimal place 0=off, 1= on default = 0 (see documentation)Above and round BNZ to 2 decimal place SUL to 0 decimal place 0 = off, 1 = on default = 0 (see documentatio)Volume % of aromatics in ethanol ( default 1.7)Volume % of benzene in ethanol (default 0.06)Weight % Oxygen in ethanol from ethanol (default 34.7)Volume % of olefins in ethanol (default 0.5)Weight ppms of sul in ethanol (default 10.0)Specific gravity of ethanol (default 0.788)Specific gravity of gasoline (default 0.718)Volume % of ethanol in the final blend (default 5%)

Volume % aromatics

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Volume % benzeneVolume % olefinsReid Vapor Pressure w/o Ethanol (PSI)Weight ppms of sul

Volume % aromatics in blendVolume % benzene in blendWeight % of oxygen from ethanol in blendVolume % of olefins in blendWeight % of total oxygen in blendReid Vapor Pressure of blend (PSI)Weight ppms of sul in blend

PIMS's Tag of the ethanol stream

RVP of CARBOB blend stock w/o EthanolT50 of CARBOB blend stock w/o EthanolT90 of CARBOB blend stock w/o EthanolVolume % (4 to 10) of Ethanol to be blended

Blended RVPBlended T50Blended T90

This correlation is used inconjuction with CARBOB. It is used to calculate the T50 of the blend without ethanol.This correlation assumes that the T50 can be blended linearly and all this does is to strip the ethanol contribution to T50Note since T50 is assumed to blend linearly this should be PIMS T50 Tag.

The corresponding PIMS tag should be the one passed to CARBOB.

This correlation is used inconjuction with CARBOB. It is used to calculate the T90 of the blend without ethanol.This correlation assumes that the T90 can be blended linearly and all this does is to strip the ethanol contribution to T90Note since T90 is assumed to blend linearly this should be PIMS T90 Tag.

The corresponding PIMS tag should be the one passed to CARBOB.

This correlation is used inconjuction with CARBOB. It is used to calculate the T90 of the blend without ethanol.

D86 T50 w/o Ethanol (oF)

D86 T90 w/o Ethanol (oF)

D86 T50 of blend (oF)

D86 T90 of blend (oF)

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The corresponding PIMS tag should be the one passed to CARBOB.

This correlation is used inconjuction with CARBOB. It is used to calculate the Temperature of the blend without ethanol.It takes the percent off minus the ethanol contribution and calls the D86FromPercentOff to calculate the ASTM% off at P1% off at P2% off at P3% off at P4% off at P5% off at P6% off at P7% off at P8% off at P9% off at P10

D86 initial boiling point

The corresponding PIMS tag should be the one that is passed to CARBOB.

The corresponding PIMS tag should be the one that is passed to CARBOB.D86 final boiling point

This correlation is used in conjuction with CARBOB. It is used to calculate the RVP of the blend without ethanol.

Reid Vapor Pressure Index

Reid Vapor Pressure

This is a set of generic Property/Index relationship defined by user in T. Index or Property calculator. Must be one to one relationship.Just place the property in the OUTPRP section. Input tags are automatically picked up from T. Index or Property Calculator Properties defined in Table Index or Property Calculator

This is a set of second order correlations (property from another property of the blend) defined through Property calculator Property can be function of more than one other property. Input tags automatically picked up from Property calculator sheet.Properties defined in Property Calculator

ASTM D4814 TVL method. More complicated non-linear version of TVL.

Reid Vapor Pressure

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Temp @ V/L = 20

Reid Vapor Pressure (kPa)

Vapor Lock Index

Does a linear interpolation of the the blended D86 curve to obtain the % evaporative.

Up to 12 D86 temperature at which to interpolate for the percent evaporative.The temperature units must be the same as the D86 curve temperature units of the input properties below.You must have at least one and the number of entries in the option section must equal the number of entries inthe OUTPRP section.

The following D86 temperature must be in the same units as the temperature in above.D86 IBPD86 T10D86 T30D86 T50D86 T70D86 790D86 FBP

A list of up to 12 percent evaporative. They are the percent off at the corresponding temperature in the optionsection. The first on this list is at the first temperature in the option list. The second is at the second temperatureetc. The correspondence in the last digit before the _ has absolutely no bearing on the mapping between the this list and the option list. It is strictly by order.

Volume percent off at 70 oC

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Pour Point

Pour Point Index

Viscosity

Viscosity Index

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Cloud Point

Cloud Point Index

Cloud Point

Cloud Point Index

Flash Point

Flash Point Index

T10 Blend Value

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T50 Blend Value

T90 Blend Value

Research OctaneMotor OctaneOlefin vol %Aromatic vol %

Transformed Research OctaneTransformed Motor Octane

Reid vapor pressure

Reid vapor pressure index

Points at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculated

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% off at P1% off at P2% off at P3% off at P4% off at P5% off at P6% off at P7% off at P8% off at P9% off at P10

This is a set of blend value correlations (essentially index after blending requires no reverse transform) defined through Property calculator Blend Value can be function of more than one other property. Input tags automatically picked up from Property calculator sheet.Blend values defined in Property Calculator

This version of D86 curve method allows up to 20 percent off points and if TYPCOR = NONE up to 13 D86 points. If no P1-P20 value defined, PIMS assumes 10 points with the default value shown. If no T1-T13 defined PIMS assumes standard 7 points as shown.Delete any points not needed. Make sure there is a correspondence between the points defined in the option section and in the input/output section.Please see PIMS documentation for further details.Points at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculated

IBPT10T30

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T50T70T90FBP

%off at P1%off at P2%off at P3%off at P4%off at P5%off at P6%off at P7%off at P8%off at P9%off at P10%off at P11%off at P12%off at P13%off at P14%off at P15%off at P16%off at P17%off at P18%off at P19%off at P20

Temperature at T1Temperature at T2Temperature at T3Temperature at T4Temperature at T5Temperature at T6Temperature at T7Temperature at T8Temperature at T9Temperature at T10Temperature at T11Temperature at T12Temperature at T13

This version of D86 curve method allows up to 20 percent off points and if TYPCOR = NONE up to 13 D86 points. If no P1-P20 value defined, PIMS assumes 10 points with the default value shown. If no T1-T13 defined PIMS assumes standard 7 points as shown.Delete any points not needed. Make sure there is a correspondence between the points defined in the option section and in the input/output section.Please see PIMS documentation for further details.Points at which % off is to be calculated

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Points at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculatedPoints at which % off is to be calculated

IBPT10T30T50T70T90FBP

Temperature at T1Temperature at T2Temperature at T3Temperature at T4Temperature at T5Temperature at T6Temperature at T7Temperature at T8Temperature at T9Temperature at T10Temperature at T11Temperature at T12Temperature at T13

%off at P1%off at P2%off at P3%off at P4%off at P5

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%off at P6%off at P7%off at P8%off at P9%off at P10%off at P11%off at P12%off at P13%off at P14%off at P15%off at P16%off at P17%off at P18%off at P19%off at P20

The volume percent of ethanol is an input parameter. This correlation calculates the blend properites if the userspecified amount of ethanol is added to a blend stock. This correlation is for putting specs on blend stocks that will eventually be blended with ethanol and must meet EPA RFG specs.Volume % of aromatics in ethanol ( default 1.7)Volume % of benzene in ethanol (default 0.06)Weight % Oxygen in ethanol from ethanol (default 34.7)Volume % of olefins in ethanol (default 0.5)Weight ppms of sul in ethanol (default 10.0)Specific gravity of ethanol (default 0.788)Specific gravity of gasoline without ethanol (default 0.718) . This is fixed in CARB's spreadsheet.Volume % of ethanol in the final blend (default 5%)Coefficient 1 (default 147.91) Adjusts the predicted E200 (E200 = P1 - P2 * T50)Coefficient 2 (default 0.49) Adjusts the predicted E200Coefficient 3 (default 155.47) Adjusts the predicted E300 (E300 = P3 - P4 * T90)Coefficient 4 (default 0.22) Adjusts the predicted E300Calculated RVP offset (default 0.0)Calculated RVP scale factor (default 1.0)

Volume % aromaticsVolume % benzeneVolume % olefinsReid Vapor Pressure w/o Ethanol (PSI)Weight ppms of sul

Volume % aromatics in blendVolume % benzene in blendWeight % of oxygen from ethanol in blendVolume % of olefins in blendReid Vapor Pressure of blend (PSI)Weight ppms of sul in blend

D86 T50 w/o Ethanol (oF)

D86 T90 w/o Ethanol (oF)

D86 T50 of blend (oF)

D86 T90 of blend (oF)

Percent Off at 200 oF

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Predicts the E200 and E300 from T50 and T90 for gasolineCoefficient 1 (default 147.91) Adjusts the predicted E200 E200 = P1 - P2 * T50Coefficient 2 (default 0.49) Adjusts the predicted E200Coefficient 3 (default 155.47) Adjusts the predicted E300 E300 = P3 - P4 * T90Coefficient 4 (default 0.22) Adjusts the predicted E300

Cetane Index

Percent Off at 300 oF

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Viscosity index

Viscosity

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Viscosity

Viscosity Index

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ABML key words are case insensitive. The only exception is the key word OPTION in the column heading. Note that PIMS tags are still case sensitive !^FR

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The volume percent of ethanol in this version of CARBOB is an input parameter. This correlation calculates the blend properites if the user

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This correlation assumes that the T50 can be blended linearly and all this does is to strip the ethanol contribution to T50

This correlation assumes that the T90 can be blended linearly and all this does is to strip the ethanol contribution to T90

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This correlation is used inconjuction with CARBOB. It is used to calculate the Temperature of the blend without ethanol.

The corresponding PIMS tag should be the one that is passed to CARBOB.

This is a set of generic Property/Index relationship defined by user in T. Index or Property calculator. Must be one to one relationship.Just place the property in the OUTPRP section. Input tags are automatically picked up from T. Index or Property Calculator

This is a set of second order correlations (property from another property of the blend) defined through Property calculator Property can be function of more than one other property. Input tags automatically picked up from Property calculator sheet.

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This is a set of blend value correlations (essentially index after blending requires no reverse transform) defined through Property calculator Blend Value can be function of more than one other property. Input tags automatically picked up from Property calculator sheet.

This version of D86 curve method allows up to 20 percent off points and if TYPCOR = NONE up to 13 D86 points. If no P1-P20 value defined, PIMS assumes 10 points with the default value shown. If no T1-T13 defined PIMS assumes standard 7 points as shown.Delete any points not needed. Make sure there is a correspondence between the points defined in the option section and in the input/output section.

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This version of D86 curve method allows up to 20 percent off points and if TYPCOR = NONE up to 13 D86 points. If no P1-P20 value defined, PIMS assumes 10 points with the default value shown. If no T1-T13 defined PIMS assumes standard 7 points as shown.Delete any points not needed. Make sure there is a correspondence between the points defined in the option section and in the input/output section.

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