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Unified Supply Chain Assay

Correlations

  • Last UpdatedAug 14, 2026
  • 5 minute read

Assay offers you the powerful ability to enter correlations between properties, to be used when measurements are not available for particular properties. These correlations are specified in terms of input properties and calculation steps.

The correlation manager offers you the necessary functionality to enter these correlations. See Add new correlations.

The possible mathematical operations which may be used in the correlation functions are described in Writing Formulae.

The following correlations are industry standard, and may be included in your version of the product.

Note: Your version of the product may have additional correlations defined.

Correlation

Unit Category

Properties involved

Calculation Steps

4-ring+ Aromatics

Proportion (%)

  • A4 — 4-ring+ Aromatics

  • A0 — Aromatics by weight %

  • A1 — Aromatics (1-ring) by weight %

  • A2 — Aromatics (2-ring) by weight %

  • A3 — Aromatics (3-ring) by weight %

  • A4 = A0 - A1 - A2 - A3

API gravity

None

  • API — API gravity

  • SG — Specific gravity at 60°F

  • API = 141.5 / SG - 131.5

Aromatics from 1-ring to 4-ring+

Proportion (%)

  • A — Aromatics from 1-ring and 2-ring+

  • A1 — Aromatics (1-ring) by weight %

  • A2 — Aromatics (2-ring) by weight %

  • A3 — Aromatics (3-ring) by weight %

  • A4PLUS — Aromatics (4-ring+) by weight %

  • A = A1 + A2 + A3 + A4PLUS

Aromatics from 1-ring and 2-ring+

Proportion (%)

  • A — Aromatics from 1-ring and 2-ring+

  • A1 — Aromatics (1-ring) by weight %

  • MRA — Multiring aromatics by weight %

  • A = A1 + MRA

Butene

Proportion (%)

  • BU — Butene

  • 1BU — 1-Butene by weight %

  • ISOB — iso-butene by weight %

  • T2B — trans-2-butene by weight %

  • CIS2B — cis-2-butene by weight %

  • Bu = 1BU + ISOB + T2B + CIS2B

C/H ratio from PNA

Proportion

  • CH — C/H ratio from PNA

  • CHP — Carbon to hydrogen ratio for paraffins

  • CHN — Carbon to hydrogen ratio for naphthenes

  • CHA — Carbon to hydrogen ratio for aromatics

  • PAR — Paraffins by weight %

  • NAP — Naphthenes by weight %

  • ARO — Aromatics by weight %

  • CH = (PAR * CHP) + (NAP * CHN) + (ARO * CHA)

C10 paraffins from iso and normal

Proportion (%)

  • C10 — C10 paraffins from iso and normal

  • ISOC10 — C10 iso-paraffins by weight %

  • NC10 — n-decane by weight %

  • C10 = ISOC10 + NC10

C11 paraffins from iso and normal

Proportion (%)

  • C11 — C11 paraffins from iso and normal

  • ISOC11 — C11 iso-paraffins by weight %

  • NC11 — n-undecane by weight %

  • C11 = ISOC11 + NC11

C12 paraffins from iso and normal

Proportion (%)

  • C12 — C12 paraffins from iso and normal

  • ISOC12 — C12 iso-paraffins by weight %

  • NC12 — n-dodecane by weight %

  • C12 = ISOC12 + NC12

C4 paraffins

Proportion (%)

  • C4 — C4 paraffins

  • IBU — Isobutane by weight %

  • NBU — n-butane by weight %

  • C4 = IBU + NBU

Carbon/Hydrogen ratio

Proportion

  • CH — Carbon/Hydrogen ratio

  • C — Carbon by weight %

  • H — Hydrogen by weight %

  • CH = C / H

Cetane index (ASTM-D976) SI

None

  • CI — Cetane index (ASTM-D976) SI

  • den — Density at 15°C

  • t50 — TBP in °C at yield by volume of 50% measured using D86 and converted to standard barometric pressure.

  • CI = 454.74 - 1641.416*den + 774.74*den^2 - 0.554*t50 + 97.803*(log t50)^2

Cetane index (D4737-90)

None

  • CI — Cetane index (D4737-90)

  • T10 — D86 in °C at yield by volume of 10%

  • T50 — D86 in °C at yield by volume of 50%

  • T90 — D86 in °C at yield by volume of 90%

  • T10N — Intermediate variable

  • T50N — Intermediate variable

  • T90N — Intermediate variable

  • DN — Density number

  • B — Intermediate variable

  • DEN — Density at 15°C in kg/m³

  • DN = DEN - 0.85

  • B = exp(-3.5 * DN) - 1

  • T10N = T10 - 215

  • T50N = T50 - 260

  • T90N = T90 - 310

  • CI = 45.2 + 0.0892 * T10N + 0.131 * T50N + 0.0523 * T90N + 0.901 * B * T50N - 0.420 * B * T90N + 4.9E-4 * (T10N^2 - T90N^2) + 107 * B + 60 * B^2

Cetane index (IP218)

None

  • CI — Cetane index (IP218)

  • API — API gravity

  • TBP50 — TBP in °F at yield by volume of 50%

  • T50 — Intermediate variable

  • X — Intermediate variable

  • T50 = (TBP / 0.8718)^(1/1.0258)

  • X = 97.833 * (log10(T50))^2 + 2.2088 * API * log10(T50) + 0.01247 * API^2 - 423.51 * log10(50) - 4.7808 * API + 419.59

  • CI = 0.49083 + 1.06577 * X - 0.0010552 * X^2

Flash point

Temperature (°C)

  • FP — Flash point

  • MBP — Mean boiling point by volume in °C

  • FP = 1.23 * MBP - 97.0

Isoparaffins

Proportion (%)

  • ISOPAR — Isoparaffins

  • TOTPAR — Paraffins by weight %

  • NPAR — n-paraffins by weight %

  • ISOPAR = TOTPAR - NPAR

Isoparaffins to n-paraffins

Proportion (%)

  • ITON — Isoparaffins to n-paraffins

  • ISOPAR — isoparaffins by weight %

  • NPAR — n-paraffins by weight %

  • ITON = ISOPAR / NPAR

Luminometer Number

Dimensionless

  • LN — Luminometer number

  • S — Smoke point in mm

  • LN = -12.03 + 3.009 * S - 0.0104 * S^2

Meta-xylene + para-xylene

Proportion (%)

  • X — meta-xylene + para-xylene

  • META — meta-xylene by weight %

  • PARA — para-xylene by weight %

  • X = META + PARA

Methane + ethane

Proportion (%)

  • ME — methane + ethane

  • M — methane by weight %

  • E — ethane by weight %

  • ME = M + E

Molecular Weight

mole

  • MW — methane + ethane

  • DEN — Density in g/cc at 15°C

  • E — Mean boiling point by weight in Rankines

  • X1 — Intermediate variable

  • X2 — Intermediate variable

  • X3 — Intermediate variable

  • X4 — Intermediate variable

  • X5 — Intermediate variable

  • X1 = 4.6523 - 3.3287 * DEN

  • X2 = 1 + DEN * (-0.77074 - DEN * 0.02058)

  • X3 = 1.3437e7 - 720.97e7 / MBP

  • X4 = 1 + DEN * (-0.80882 + DEN * 0.2226)

  • X5 = 1.8828e12 - 181.98e12 / MBP

  • MW = max(60, -12272.6 + 9486.4 * DEN + X1 * MBP + X2 * X3 / MBP + X4 * X5 / MBP^3)

N+2A

Proportion (%)

  • N2A — N+2A

  • N — Naphthenes by weight %

  • A — Aromatics by weight %

  • N2A = N + 2 * A

n-Paraffins

Proportion (%)

  • NPAR — n-paraffins

  • TOTPAR — Paraffins by weight %

  • ISOPAR — iso-paraffins by weight %

  • NPAR = TOTPAR - ISOPAR

Olefins

Proportion (%)

  • O — Olefins

  • C2E — Ethene by weight %

  • PRP — Propene by weight %

  • NC4E — 1-butene by weight %

  • IC4E — iso-butene by weight %

  • T2C4E — trans-2-butene by weight %

  • C2C4E — cis-2-butene by weight %

  • BD12 — 1-2-butadiene by weight %

  • C2C4E — 1-3-butadiene by weight %

  • O = C2E + PRP + NC4E + IC4E + T2C4E + C2C4E + BD12 + BD13

Paraffins

Proportion (%)

  • PAR — Paraffins

  • ISOPAR — iso-paraffins by weight %

  • NPAR — n-paraffins by weight %

  • PAR = ISOPAR + NPAR

Pour point index

Dimensionless

  • PPI — Pour point index

  • PPT — Pour point in °F

  • PPI = exp(0.03 * PPT)

Saturates

Proportion (%)

  • S — Saturates

  • PAR — Paraffins by weight %

  • NAP — Naphthenes by weight %

  • S = PAR + NAP

Watson K

Dimensionless

  • K — Watson K

  • VABP — Volume averaged mean boiling point

  • SG — Specific gravity at 60°F

  • K = VABP^(1/3)/SG