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The Petroleum Template defines defaults commonly used in the petroleum industry. It is also appropriate for petrochemical applications such as ethylene plants, which involve petroleum
fractions as feedstocks.
This table shows the defaults used:
Specification | English Default | Metric Default |
Units | F, psi, lb/hr, lbmol/hr, MMBtu/hr, bbl/day | C, bar, kg/hr, kmol/hr, MMkcal/hr, bbl/day |
Physical property method | None | None |
Free water | Yes | Yes |
Flow basis | Standard liquid volume | Mass |
Stream report composition | Standard liquid volume flow | Mass flow |
Because petroleum applications encompass a wide range of boiling fractions/ components and process conditions, this Template does not have a default physical property method. These methods are used most frequently:
BK10
CHAO-SEA
GRAYSON
RK-SOAVE
PENG-ROB
IDEAL
You should consider additional methods for various operations within a refinery (such as ELECNRTL for sour water strippers and amine treatment units, and UNIFAC for aromatic extraction).
Aspen Plus provides comprehensive methods for analyzing assay data and automatically generating pseudocomponents. You can select from five built-in pseudocomponent property methods to characterize pseudocomponents. You can also enter curves of petroleum properties, such as sulfur and metal contents. Aspen Plus tracks these properties throughout the flowsheet. You can use them in design specifications, optimization constraints, and objective functions.
The Aspen Plus PetroFrac model simulates a wide range of fractionation units within a refinery. PetroFrac can model a tower with any number of:
Side strippers, including the bottom liquid return to the main tower
Pumparounds and bypasses
Partial and total drawoffs
PetroFrac can model the feed furnace as an integral part of the tower, including the slop cut recycle for a vacuum unit. It lets you enter petroleum-specific property specifications, such as ASTM distillation temperatures, gaps, and overlaps. It also offers extensive column sizing and rating capabilities, including the ability to handle structured packings and integrated pressure drop calculations.
Petroleum Property Sets
In Aspen Plus, many properties can be used to characterize streams in a refinery. The Petroleum Template includes property sets for many widely used petroleum-related properties.
Property Set | Description |
CUTS-E | Standard liquid volume flow of petroleum cuts at 100º F intervals. Valuable for concise reporting of stream composition. |
CUTS-M D86-5 | Mass flow rate of petroleum cuts at 50º C intervals. Valuable for concise reporting of stream composition. ASTM D86 temperature at 5 liquid volume % |
D86-95 | ASTM D86 temperature at 95 liquid volume % |
GASPROPS | Vapor phase properties, including: Compressibility factor for a mixture Actual volume flow Standard vapor volume flow Heat capacity ratio (CP/CV) |
KINVISC | Kinematic viscosity at 100°F and 212°F or 40°C and 100°C (dry basis) |
LIGHT | Petroleum characteristics for light distillates (dry basis), including: Reid vapor pressure Flash point based on API method Aniline point |
MIDDLE | Petroleum characteristics for middle distillates (dry basis), including: Cetane number Flash point based on API method Pour point based on API method Aniline point |
PETRO † | General petroleum properties on dry basis, including: Standard liquid volume flow (bbl/day) and (bbl/hr) Standard API gravity Standard specific gravity Watson UOP K-factor True boiling point distillation curve ASTM D86 and D1160 distillation curves |
TBP-5 | True boiling point temperature at 5 liquid volume % |
TBP-95 | True boiling point temperature at 95 liquid volume % |
† | Default for stream results |
Petroleum Stream Report Options
The large number of pseudocomponents and distillation curves in a petroleum application can result in a lengthy stream report. The Petroleum Template defines several stream report format
(TFF) options so you can view or print subsets of stream information:
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