All crude and other streams (not originating from blocks located elsewhere in the flowsheet) must be defined by user. In addition, estimates for recycle streams must be provided. All streams are defined using the Stream Input form accessed by right clicking on the respective stream.
Stream Type
The Stream Type field indicates that the type of stream represented. Options include Crude and Non Crude.
Each stream name may contain a maximum of ten characters. If the stream is a crude oil, the name must be chosen from the offered list. The list includes all crudes with assays defined in the file bearing the same name as the crude (with the suffix.mod) and in the directory identified by the File | Model Dir menu.
In order to create a new crude assay file, use the Edit | Submodel/Crude menu command prior to entering stream data.
A volume (RateV) or a weight (RateW) basis must be specified for each block.
The specific gravity (SG) or API density (API) must be entered except for crude oil streams.
The Properties field may be left blank for crude streams. However, the Properties must be specified for Non Crude streams. The list of properties available is presented at the end of this topic. Additional properties may be defined by using General Input form. Property names must be spelled verbatim for the blender input and submodels.
PropX and PropY are any user-defined properties that may be calculated based on linear mixing rules by weight basis (for example, thepercentage weight iron in a mixture). The process submodels that incorporate the properties for calculations must be consistent in the interpretation of the values. PropA and PropB are similar in function but defined for volume blending properties.
Certain stream properties must be defined if the simulator is to perform the block calculations. For process submodels, if the feed properties required to calculate product yields (and SG) are missing, a fatal error is indicated. Many properties have default values of zero. This is usually true for contaminants (such as SUL and NIT). Other properties, such as viscosity and RON, have no default values. Such properties must be defined for blocks whose submodels use the properties during calculations.
A list of properties that are supported by PetroPlanâ is presented. Additional properties may be defined using the General Input form. The units of measure must be consistent with those used by the process submodels (for example, RVP may be in psia, kPa or KgCm2).
· RateV Volume flow rate per day
· RateW Weight flow rate
· SG Specific gravity
· API API density
· VABP Volume average boiling point
· SUL Weight percentage sulfur
· OXY Weight percentage oxygen
· RVP Reid Vapor Pressure
· FLSH Flash Point
· RON Research Octane Number
· MON Motor Octane Number
· RM2(R+M)/2 If RON and MON both provided, RM2 will be calculated automatically.
· PAR Volume percentage of paraffins
· OLE Volume percentage of olefins
· NAPH Volume percentage of naphthenes
· ARO Volume percentage of aromatics
· BENZ Volume percentage of benzene
· SMK Smoke point
· FRZ Freeze point
· POR Pour point
· CET Cetane index
· ANL Aniline point
· CS122 Viscosity, CS at 122°F
· CS210 Viscosity, CS at 210°F
· NIT Weight percentage of nitrogen
· NI Nickel, wppm
· VAN Vanadium, wppm
· C5I C5 insoluble
· CCR Weight percentage of Conradson Carbon
· PROPA User defined volume blending property
· PROPB User defined volume blending property
· PROPX User defined weight blending property
· PROPY User defined weight blending property
· V150 Volumepercentage evaporated at 150°F
· V200 Volumepercentage evaporated at 200°F
· V300 Volumepercentage evaporated at 300°F
· V400 Volumepercentage evaporated at 400°F
· V500 Volumepercentage evaporated at 500°F
· V650 Volumepercentage evaporated at 650°F