This is the completed case for part 5 of the Alph Tutorial.
Browse this page with the web browser on your iPhone. Tap and hold in the gray area below to select the whole region and and then tap the copy button that appears. Run Alph and use the Load Case command to load this case from the paste board.
{ "SelectedFluidIndex" : 7, "PropPkg" : "APRNGL", "Tools" : [ { "Type" : "Hydrate", "HydrateVariable" : "P", "name" : "hydrate", "DiagramX" : 93, "DiagramY" : 3, "Feed" : "feed" }, { "Source" : "feed.v", "QualityLineSpec" : "1. 0.75 0.5 .95", "name" : "envelope", "DiagramX" : 185, "Type" : "Phase Envelope", "DiagramY" : 11, "StartPressure" : "500 kPa" }, { "minInnerStep" : 0.0001, "Pressures" : [ { "Spec" : "700 kPa", "Stage" : 0 }, { "Spec" : "750 kPa", "Stage" : -1 } ], "ovhdFormula" : "140 kgmole/h", "DiagramX" : 211.6708, "Feeds" : [ { "Stage" : 4, "Fluid" : "feed.l" }, { "Stage" : 7, "Fluid" : "lts.l" } ], "maxOuterError" : 0.0001, "viewPage" : 2, "maxOuterLoops" : 20, "nStages" : 15, "refluxRatio" : "1.0", "attemptRestart" : false, "dampingFactor" : 1, "maxInnerLoops" : 50, "name" : "stab", "Description" : "liquid stabilizer", "Type" : "Tower", "Draws" : [], "Energies" : [ { "Spec" : "(@vpcheck.t -{fromunit \"f\" \"t\" 100}) / 500", "Stage" : 0 }, { "Stage" : -1 } ], "Temperatures" : [ { "Spec" : "20 C", "Stage" : 0 }, { "Spec" : "150 C", "Stage" : -1 } ], "DiagramY" : 204.5386, "maxInnerError" : 0.0001 } ], "diagramX" : -110.3843, "SelectedToolIndex" : 2, "Program" : "Alph", "NextFluidNumber" : 10, "Fluids" : [ { "CompFormula" : "[ 70,20,10,9,8,7,6,5 ]", "Retrograde" : false, "FlowFormula" : "10 mmscfd", "SecondPropFormula" : "4000 kPa", "name" : "feed", "DiagramX" : 12, "TwoLiquids" : false, "SumCompForFlow" : false, "FirstPropType" : "T", "SecondPropType" : "P", "DiagramY" : 52, "FirstPropFormula" : "10 C" }, { "CompFormula" : "@feed.v", "Retrograde" : false, "FlowFormula" : "@feed.v", "SecondPropFormula" : "@feed - 2 * $dp", "name" : "lts", "DiagramX" : 126, "TwoLiquids" : false, "SumCompForFlow" : false, "FirstPropType" : "T", "SecondPropType" : "P", "DiagramY" : 50, "FirstPropFormula" : "-10 C" }, { "CompFormula" : "@lts.v", "Retrograde" : false, "FlowFormula" : "@lts.v", "SecondPropFormula" : "1", "name" : "dewpt", "DiagramX" : 227, "TwoLiquids" : false, "SumCompForFlow" : false, "FirstPropType" : "P", "SecondPropType" : "Vf", "DiagramY" : 40, "FirstPropFormula" : "800 psig" }, { "CompFormula" : "@lts.v", "Retrograde" : false, "FlowFormula" : "@lts.v", "SecondPropFormula" : "@lts - $dp", "name" : "salesgas", "DiagramX" : 211, "TwoLiquids" : false, "SumCompForFlow" : false, "FirstPropType" : "T", "SecondPropType" : "P", "DiagramY" : 84, "FirstPropFormula" : "@feed - $dt" }, { "FlowFormula" : "@feed.v", "SumCompForFlow" : false, "DiagramX" : 119, "Retrograde" : false, "FirstPropType" : "P", "CompFormula" : "@feed.v", "SecondPropType" : "H", "FirstPropFormula" : "@feed - $dp", "TwoLiquids" : false, "SecondPropFormula" : "(@feed.v.Q - $ggduty) / @feed.v.F", "name" : "chillfeed", "Description" : "Chiller Feed", "DiagramY" : 256 }, { "FlowFormula" : "#stab.0.v.f", "SumCompForFlow" : false, "DiagramX" : 288.5555, "Retrograde" : false, "FirstPropType" : "P", "CompFormula" : "#stab.0.v.x", "SecondPropType" : "Vf", "FirstPropFormula" : "#stab.0.p", "TwoLiquids" : true, "SecondPropFormula" : "1", "name" : "stabovhd", "Description" : "Stabilizer Overhead", "DiagramY" : 189.5869 }, { "FlowFormula" : "#stab._1.l.f", "SumCompForFlow" : false, "DiagramX" : 286.1607, "Retrograde" : false, "FirstPropType" : "P", "CompFormula" : "#stab._1.l.x", "SecondPropType" : "Vf", "FirstPropFormula" : "#stab._1.p", "TwoLiquids" : false, "SecondPropFormula" : "0", "name" : "stabbtms", "Description" : "Stabilizer Bottoms", "DiagramY" : 230.2954 }, { "FlowFormula" : "@stabbtms", "SumCompForFlow" : false, "DiagramX" : 219.4816, "Retrograde" : false, "FirstPropType" : "P", "CompFormula" : "@stabbtms", "SecondPropType" : "Vf", "FirstPropFormula" : "1 atm", "TwoLiquids" : false, "SecondPropFormula" : "0", "name" : "vpcheck", "Description" : "Check vapour pressure of stabilizer bottoms", "DiagramY" : 267.5058 } ], "Hypotheticals" : [], "diagramY" : -79.00694, "CompoundNames" : [ "METHANE", "ETHANE", "PROPANE", "n-BUTANE", "n-PENTANE", "n-HEXANE", "n-HEPTANE", "n-OCTANE" ], "SelectedVariableIndex" : 2, "Variables" : [ { "PropertyType" : "DeltaP", "name" : "dp", "DiagramX" : 10, "DiagramY" : 92, "PropertyFormula" : "50 Kpa" }, { "PropertyType" : "DeltaT", "name" : "dt", "DiagramX" : 12, "DiagramY" : 137, "PropertyFormula" : "5 C" }, { "PropertyType" : "Q", "name" : "ggduty", "DiagramX" : 209, "DiagramY" : 123, "PropertyFormula" : "@salesgas - @lts.v" } ], "CaseName" : "tutorial5", "CurrentUnitSet" : 1, "NextVariableNumber" : 8, "Version" : 1.101, "diagramScale" : 1.307424, "DisplayedProperties" : { "-4" : "y", "8" : "y", "-2" : "y", "-1" : "y", "10001" : "y", "-6" : "y", "9" : "y" } }