Open the form by double clicking on it and type in P-T envelope under the comments section. Two-phase Envelope form in the Main WinProp interface. We would also like to generate a pressure-temperature phase diagram. The input value of saturation pressure estimate is used as an initial guess by WinProp during the iteration processes for calculating the actual saturation pressure.ĩ. Also, input the reservoir temperature and saturation pressure estimate as 180 F and 1000 Psia respectively. Double click and open the saturation pressure calculation form. Perform a saturation pressure calculation at the reservoir temperature. Insert Saturation pressure calculation Form" into the WinProp Interface to The two-phase flash calculation form should look like as shown in Figure 3.ħ. The feed composition is subjected to mixed i.e. Leave other calculation options as default. We are planning to perform a flash at 14.7 Psia and 60 deg.F.
Open thisįorm by double clicking on it and under the comments section type Standard condition flash. Insert two phase flash calculation form" into the WinProp interface. The secondary corresponds to the injection fluid (if applicable).Ħ. Open the "composition form" and input the mole fractions of the primary composition as mentioned in the file: Five Fluid Types Data.xls. Your component definition form should look like Figure1 for Dry gas and Figure 2 in case of other fluid types.įigure1: Component definition for case of Dry Gasĥ. Use the properties given in the file: Five Fluid Types Data.xls. Click on options button in the component definition form and select insert own component based on specific gravity (SG), boiling point (TB) and molecular weight (MW). Pseudocomponent by inserting a user defined component. In all cases except Dry Gas also, characterize the C7+ fraction with a single
(The order of selection in important!).Ĥ. Open component selection form and insert the library components in theįollowing order: CO2, N2, C1, C2, C3, IC4, NC4, IC5, NC5, and FC6. Select PR 1978 and the equation of state to be used in characterizing the fluid model, select Psia & deg F as the units and Feed as mole. Double click on Titles/EOS/Units and write Dry gas/Wet gas/GasĬondensate/Volatile oil/Black oil in the comments and the Title1 section depending on the case you are modelling. Double click on the WinProp icon in the Launcher and open the WinProp interface.Ģ. Dry gas, wet gas, Gas condensate, volatile oil and Black oil.ġ. (Dry Gas, Wet Gas, Gas Condensate) (Volatile Oil, Black Oil, Heavy Oil)Įxercise 1 (Required File: Five Fluid Types Data.xls) Objective: Modelling of five fluid type i.e. Building, Running and Analyzing Different Types of Fluid Models
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