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Thermophysical Properties of Petroleum Fractions and Crude Oils
Introduction • Design of Petroleum Refinery requires the
knowledge of certain Thermophysical properties
Introduction
• Crude oil has complex composition of petroleum fractions
• Calculation methods for pure hydrocarbons are not applicable
• Correlations are developed to estimate the properties of petroleum fractions
Basic Input Data
Such correlations require basic input data from LAB experiments:
Specific Gravity (SG)
Boiling Point Curve (ASTM or True Boiling Point Distillation)
Refractive Index (n)
Molecular Weight (M)
True Boiling Point Distillation
• More detailed characterization of petroleum fractions
• Performed in column with 15 plates and reflux ratio of 5
• Higher degree of separation than ASTM distillation
• IBP is Lower than that of ASTM distillation
• FBP is higher than that of ASTM distillation
Conversion between ASTM & TBP Distillation
Both Temperatures are in Rankin T(R)=(T(C)+273)*1.8 Or T(R) = (1.8T(C)+32)+460
Excel Example
Pseudo-Components
• Calculations involving crude oil and petroleum fractions require composition of each process stream
• Since the actual components are not known, petroleum fractions are characterized as mixture of pseudo components
Pseudo-Components
• They are defined over boiling point range over the TBP distillation curve.
• Each pseudo-component corresponds to several unknown actual compounds.
Pseudo Components
• Each pseudo-component is characterized by
– Normal Boiling Point (NBP, treated as MABP)
– Specific Gravity
– Molecular Weight
• Once this parameters are characterized, Pseudo-component can be treated as any defined component for the Thermophysical parameters Calculations
Breaking of TBP Curve to Pseudo-components
• The following cut-points are reasonable for most refining calculations
TBP range is defined by (IBP-FBP)
• General Guideline for determining the number of Pseudo-Components:
Breaking of TBP Curve to Pseudo-components
• Divide the TBP curve into 20 pseudo-components. Calculate the liquid volume percentage of each pseudo-component.
Breaking of TBP Curve to Pseudo-components
Note that: TBP curve extends to 95 volume percent distilled only. To Obtain the NBP of the final cuts, it has to be extrapolated to 100 % distilled; by fitting polynomial curve using Excel and extrapolating it.
Breaking of TBP Curve to Pseudo-components
Excel Continued
Calculation of Pseuodo-components SG
• The K factor is assumed constant for all fractions, and equal to its value for the whole Crude Oil.
• K= 𝑀𝐴𝐵𝑃
3
𝑆𝐺
• For the pseudo-components; MABP = NBP in Ranking
• Knowing K & NBP, SG can be obtained easily.
• Knowing K = 11.94, calculate the API of the Pseudo-components.
Calculation of Pseuodo-components SG
• The molecular weight is obtained from the following correlation
• Where M is the Mwt
• Tb is the NBP in K
• SG is the specific gravity
Calculation of Pseuodo-components Molecular Weight