Changeset 490


Ignore:
Timestamp:
Apr 3, 2008, 8:38:09 PM (16 years ago)
Author:
gerson bicca
Message:

updated

Location:
trunk
Files:
3 edited

Legend:

Unmodified
Added
Removed

  • trunk/eml/heat_exchangers/HEX_Engine.mso

    r474 r490  
    166166hshell          as heat_trans_coeff     (Brief="Shell Side Film Coefficient",Default=1,Lower=1e-12, Upper=1e6);
    167167Phi     as positive                             (Brief="Phi Correction",Default=1,Lower=1e-3);
    168 Ji                      as constant                     (Brief="Shell Side Ji Factor",Default=0.05);
    169 Jr                      as positive                             (Brief="Shell Side Jr Factor",Lower=10e-6);
    170 Jl                      as positive                             (Brief="Shell Side Jl Factor",Lower=10e-6);
    171 Jb                      as positive                             (Brief="Shell Side Jb Factor",Lower=10e-6);
    172 Jc                      as positive                             (Brief="Shell Side Jc Factor",Lower=10e-6);
    173 Js                      as positive                             (Brief="Shell Side Js Factor",Lower=10e-6);
    174 Jtotal          as positive                             (Brief="Shell Side Jtotal Factor",Lower=10e-6);
    175 Sm              as area                                 (Brief="Shell Side Cross Flow Area",Default=0.05,Lower=10e-6);
    176 
    177168end
    178169
    … …  
    181172ATTRIBUTES
    182173        Pallete = false;
    183         Brief = "to be documented";
    184         Info =
    185         "to be documented";
    186        
    187 VARIABLES
    188 Ls              as length               (Brief="Central Baffle Spacing",Lower=1e-8);
    189 Lsi             as length               (Brief="Inlet Baffle Spacing",Lower=1e-8);
    190 Lso             as length               (Brief="Outlet Baffle Spacing",Lower=1e-8);
     174        Brief = "Main variables in the Baffle section of a shell and tube heat exchanger.";
     175
     176PARAMETERS
     177
     178BaffleCut                       as Integer      (Brief="Baffle Cut",Default=25,Lower=25);
     179NumberOfBaffles     as Real             (Brief="Number of Baffles", Symbol = "N_{baffles}", Lower=1);
     180
     181VARIABLES
     182
     183Inlet_Spacing                   as length               (Brief="Inlet Baffle Spacing",Lower=1e-8, Symbol = "L_{si}", DisplayUnit ='mm' );
     184Central_Spacing                 as length               (Brief="Central Baffle Spacing",Lower=1e-8, Symbol = "L_s", DisplayUnit ='mm' );
     185Outlet_Spacing          as length               (Brief="Outlet Baffle Spacing",Lower=1e-8, Symbol = "L_{so}", DisplayUnit ='mm' );
     186
     187end
     188
     189Model Clearances_Main
     190       
     191ATTRIBUTES
     192        Pallete = false;
     193        Brief = "Main parameters for diametral clearances in a shell and tube heat exchanger.";
     194
     195PARAMETERS
     196
     197SealStrip                               as Integer      (Brief="Number of Sealing Strips pairs",Lower=1);
     198Hinozzle_Shell          as length               (Brief="Height Under Shell Inlet Nozzle",Lower=1E-6);
     199Honozzle_Shell          as length               (Brief="Height Under Shell Outlet Nozzle",Lower=1E-6);
     200BundleToShell           as length               (Brief="Bundle-to-Shell Clearance", Symbol = "L_{cf}", Lower=1E-8);
     201BaffleToShell           as length       (Brief="Baffle-to-Shell Clearance", Symbol = "L_{cd}", Lower=1E-8);
     202TubeToBaffle            as length       (Brief="Tube-to-Baffle Clearance", Symbol = "L_{td}", Lower=1E-8);
    191203
    192204end
    … …  
    274286ATTRIBUTES
    275287        Pallete = false;
    276         Brief = "to be documented";
    277         Info =
    278         "to be documented";
    279        
    280 VARIABLES
    281 PressureDrop    as Tube_Pdrop                   (Brief="Tube Side Pressure Drop");
    282 HeatTransfer    as Tube_Heat_Transfer (Brief="Tube Side Heat Transfer");
    283 Properties      as Physical_Properties   (Brief="Tube Side Properties");
     288        Brief = "Main variables in the Tube Side section of a shell and tube heat exchanger.";
     289
     290PARAMETERS
     291
     292NumberOfTubes           as Integer                      (Brief="Total Number of Tubes in Shell",Default=100,Lower=1);
     293Tubepasses                      as Integer                      (Brief="Number of Tube Passes", Lower=1);
     294TubeLength                              as length                               (Brief="Effective Tube Length",Lower=0.1);
     295TubePitch                               as length                               (Brief="Tube Pitch",Lower=1E-8);
     296Kwall                                           as conductivity         (Brief="Tube Wall Material Thermal Conductivity");
     297TubeOD                                          as length                               (Brief="Tube Outside Diameter",Lower=1E-6);
     298TubeID                                  as length                               (Brief="Tube Inside Diameter",Lower=1E-6);
     299Fouling                                 as positive                     (Brief="Tubeside Fouling Resistance",Unit='m^2*K/kW', Symbol = "Rf_{tube}", Default=1E-6 , Lower=0);
     300InletNozzleID           as length                               (Brief="Inlet Nozzle Inside Diameter", Lower=1E-6);
     301OutletNozzleID                  as length                               (Brief="Outlet Nozzle Inside Diameter", Lower=1E-6);
     302
     303VARIABLES
     304
     305PressureDrop    as Tube_Pdrop                           (Brief="Tube Side Pressure Drop");
     306HeatTransfer    as Tube_Heat_Transfer   (Brief="Tube Side Heat Transfer");
     307Properties              as Physical_Properties          (Brief="Tube Side Properties");
    284308
    285309end
    … …  
    289313ATTRIBUTES
    290314        Pallete = false;
    291         Brief = "to be documented";
    292         Info =
    293         "to be documented";
    294        
    295 VARIABLES
    296 PressureDrop    as Shell_Pdrop                           (Brief="Shell Side Pressure Drop");
    297 HeatTransfer    as Shell_Heat_Transfer  (Brief= "Shell Side Heat Transfer");
    298 Properties      as Physical_Properties   (Brief="ShellSide Properties");
     315        Brief = "Main variables in the Shell Side section of a shell and tube heat exchanger.";
     316
     317PARAMETERS
     318
     319ShellID                         as length               (Brief="Inside Shell Diameter",Lower=1E-6);
     320Fouling                         as positive     (Brief="Shellside Fouling Resistance",Unit='m^2*K/kW', Symbol = "Rf_{shell}", Default=1E-6 , Lower=0);
     321InletNozzleID   as length               (Brief="Inlet Nozzle Inside Diameter", Lower=1E-6);
     322OutletNozzleID          as length               (Brief="Outlet Nozzle Inside Diameter", Lower=1E-6);
     323
     324VARIABLES
     325
     326PressureDrop    as Shell_Pdrop                                  (Brief="Shell Side Pressure Drop");
     327HeatTransfer    as Shell_Heat_Transfer          (Brief= "Shell Side Heat Transfer");
     328Properties              as Physical_Properties          (Brief="ShellSide Properties");
    299329
    300330end

  • trunk/eml/heat_exchangers/HeatExchangerDetailed.mso

    r420 r490  
    2222ATTRIBUTES
    2323        Pallete = false;
    24         Brief  = "Basic Model for Detailed Shell and Tubes Heat Exchangers";
     24        Brief  = "Basic Model for Detailed Shell and Tube Heat Exchanger.";
    2525        Info  =
    2626        "to be documented.";
    … …  
    2828PARAMETERS
    2929
    30 HotSide         as Switcher     (Brief="Hot Side in the Exchanger",Valid=["shell","tubes"],Default="shell");
     30HotSide                 as Switcher     (Brief="Hot Side in the Exchanger",Valid=["shell","tubes"],Default="shell");
    3131ShellType       as Switcher     (Brief="TEMA Designation",Valid=["Eshell","Fshell"],Default="Eshell");
    3232
     33Pattern                                 as Switcher                     (Brief="Tube Layout Characteristic Angle",Valid=["Triangle","Rotated Square","Square"],Default="Triangle");
     34
    3335VARIABLES
    3436
    35 in  InletTube   as stream               (Brief="Inlet Tube Stream", PosX=0.08, PosY=0, Symbol="_{inTube}");
    36 out OutletTube  as streamPH     (Brief="Outlet Tube Stream", PosX=0.08, PosY=1, Symbol="_{outTube}");
    37 in  InletShell  as stream               (Brief="Inlet Shell Stream", PosX=0.2237, PosY=0, Symbol="_{inShell}");
    38 out OutletShell as streamPH     (Brief="Outlet Shell Stream", PosX=0.8237, PosY=1, Symbol="_{outShell}");
    39        
    40         Details         as Details_Main         (Brief="Details in Heat Exchanger");
    41         Tubes           as Tube_Side_Main       (Brief="Tube Side");   
    42         Shell           as Shell_Side_Main      (Brief="Shell Side");
    43         Baffles         as Baffles_Main         (Brief="Baffles");
    44 
     37        Tubes                   as Tube_Side_Main               (Brief="Tube Side Section");   
     38        Shell                   as Shell_Side_Main      (Brief="Shell Side Section");
     39        Baffles                 as Baffles_Main                         (Brief="Baffle Section", Symbol=" ");
     40        Clearances      as Clearances_Main      (Brief="Diametral Clearances", Symbol=" ");
     41       
     42in  InletTube           as stream                                       (Brief="Inlet Tube Stream", PosX=0.08, PosY=0, Symbol="_{inTube}");
     43out OutletTube  as streamPH                             (Brief="Outlet Tube Stream", PosX=0.08, PosY=1, Symbol="_{outTube}");
     44in  InletShell          as stream                                       (Brief="Inlet Shell Stream", PosX=0.2237, PosY=0, Symbol="_{inShell}");
     45out OutletShell as streamPH                             (Brief="Outlet Shell Stream", PosX=0.8237, PosY=1, Symbol="_{outShell}");
     46        Details                         as Details_Main                         (Brief="Details in Heat Exchanger");
     47       
    4548#+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    4649#                               Auxiliar Variables - Must be hidden                                             
    4750#+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    48         Nc              as Real         (Brief = "Number of Tube rows Crossed in one Crossflow Section",Lower=1);
    49         Ncw     as Real         (Brief = "Number of Effective Crossflow rows in Each Window",Lower=1);
    50         a               as Real         (Brief = "Variable for calculating Ji heat transfer correction Factor",Lower=1e-3);
    51         b               as Real         (Brief = "Variable for calculating shell side pressure drop friction Factor",Lower=1e-3);
    52         Rb              as Real         (Brief = "ByPass Correction Factor for Pressure Drop",Lower=1e-3);
    53         Rss     as Real         (Brief = "Correction Factor for Pressure Drop",Lower=1e-3);
    54         Rspd    as Real         (Brief = "Pressure Drop Correction Factor for Unequal Baffle Spacing",Lower=1e-3);
    55         mw              as Real         (Brief = "Mass Velocity in Window Zone", Unit='kg/m^2/s');
    56        
     51        Nc              as Real                                 (Brief = "Number of Tube rows Crossed in one Crossflow Section", Hidden = true, Lower=1);
     52        Ncw     as Real                                 (Brief = "Number of Effective Crossflow rows in Each Window", Hidden = true, Lower=1);
     53        a                       as Real                                 (Brief = "Variable for calculating Ji heat transfer correction Factor", Hidden = true, Lower=1e-3);
     54        b                       as Real                                 (Brief = "Variable for calculating shell side pressure drop friction Factor", Hidden = true, Lower=1e-3);
     55        Rb              as Real                                 (Brief = "ByPass Correction Factor for Pressure Drop", Hidden = true, Lower=1e-3);
     56        Rss             as Real                                 (Brief = "Correction Factor for Pressure Drop", Hidden = true, Lower=1e-3);
     57        Rspd    as Real                                 (Brief = "Pressure Drop Correction Factor for Unequal Baffle Spacing", Hidden = true, Lower=1e-3);
     58        mw              as Real                                 (Brief = "Mass Velocity in Window Zone", Hidden = true, Unit='kg/m^2/s');
     59        Ji                      as constant                     (Brief="Shell Side Ji Factor", Hidden = true, Default=0.05);
     60        Jr                      as positive                     (Brief="Shell Side Jr Factor", Hidden = true, Lower=10e-6);
     61        Jl                      as positive                     (Brief="Shell Side Jl Factor", Hidden = true, Lower=10e-6);
     62        Jb                      as positive                     (Brief="Shell Side Jb Factor", Hidden = true, Lower=10e-6);
     63        Jc                      as positive                     (Brief="Shell Side Jc Factor", Hidden = true, Lower=10e-6);
     64        Js                      as positive                     (Brief="Shell Side Js Factor", Hidden = true, Lower=10e-6);
     65        Jtotal  as positive                     (Brief="Shell Side Jtotal Factor", Hidden = true, Lower=10e-6);
     66        Sm              as area                                 (Brief="Shell Side Cross Flow Area", Hidden = true, Default=0.05,Lower=10e-6);
     67
    5768PARAMETERS
    58 outer PP            as Plugin           (Brief="External Physical Properties",Type = "PP");
     69outer PP                        as Plugin               (Brief="External Physical Properties",Type = "PP");
    5970outer NComp     as Integer      (Brief="Number of Components");
    6071       
    61         Pi                      as constant    (Brief="Pi Number",Default=3.14159265);
    62         M(NComp)        as molweight    (Brief="Component Mol Weight");
    63 
    64 TubeFlowRegime            as Switcher   (Brief="Tube Side Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar");
    65 ShellFlowRegime           as Switcher   (Brief="Shell Side Flow Regime ",Valid=["deep laminar","laminar","turbulent"],Default="deep laminar");
    66 ShellRange                as Switcher   (Brief="Shell Side Flow Regime Range for Correction Factor",Valid=["range1","range2","range3", "range4","range5"],Default="range1");
    67 Side                              as Switcher   (Brief="Flag for Fluid Alocation ",Valid=["shell","tubes"],Default="shell");
    68 LaminarCorrelation    as Switcher       (Brief="Tube Heat Transfer Correlation in Laminar Flow",Valid=["Hausen","Schlunder"],Default="Hausen");
    69 TransitionCorrelation as Switcher       (Brief="Tube Heat Transfer Correlation in Transition Flow",Valid=["Gnielinski","ESDU"],Default="Gnielinski");
    70 TurbulentCorrelation  as Switcher       (Brief="Tube Heat Transfer Correlation in Turbulent Flow",Valid=["Petukhov","SiederTate"],Default="Petukhov");
     72M(NComp)        as molweight (Brief="Component Mol Weight");
     73
     74TubeFlowRegime           as Switcher            (Brief="Tube Side Flow Regime ",Valid=["laminar","transition","turbulent"],Default="laminar");
     75ShellFlowRegime                 as Switcher             (Brief="Shell Side Flow Regime ",Valid=["deep laminar","laminar","turbulent"],Default="deep laminar");
     76ShellRange                              as Switcher             (Brief="Shell Side Flow Regime Range for Correction Factor",Valid=["range1","range2","range3", "range4","range5"],Default="range1");
     77Side                                                            as Switcher             (Brief="Flag for Fluid Alocation ",Valid=["shell","tubes"],Default="shell");
     78LaminarCorrelation      as Switcher             (Brief="Tube Heat Transfer Correlation in Laminar Flow",Valid=["Hausen","Schlunder"],Default="Hausen");
     79TransitionCorrelation   as Switcher             (Brief="Tube Heat Transfer Correlation in Transition Flow",Valid=["Gnielinski","ESDU"],Default="Gnielinski");
     80TurbulentCorrelation    as Switcher             (Brief="Tube Heat Transfer Correlation in Turbulent Flow",Valid=["Petukhov","SiederTate"],Default="Petukhov");
    7181
    7282#+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    73 #                               Shell Geometrical Parameters                                           
     83#                               Auxiliar Parameters     - Must be hidden                                                       
    7484#+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    75 Tpass                                   as Integer              (Brief="Number of Tube Passes",Lower=1);
    76 Nss                                     as Integer              (Brief="Number of Sealing Strips pairs",Lower=1);
    77 Dishell                                 as length               (Brief="Inside Shell Diameter",Lower=10e-6);
    78 Donozzle_Shell          as length               (Brief="Shell Outlet Nozzle Diameter",Lower=10e-6);
    79 Dinozzle_Shell          as length               (Brief="Shell Inlet Nozzle Diameter",Lower=10e-6);
    80 Aonozzle_Shell          as area                 (Brief="Shell Outlet Nozzle Area",Lower=10e-6);
    81 Ainozzle_Shell          as area                 (Brief="Shell Inlet Nozzle Area",Lower=10e-6);
    82 Aeonozzle_Shell         as area                 (Brief="Shell Outlet Escape Area Under Nozzle",Lower=10e-6);
    83 Aeinozzle_Shell         as area                 (Brief="Shell Inlet Escape Area Under Nozzle",Lower=10e-6);
    84 Hinozzle_Shell          as length               (Brief="Height Under Shell Inlet Nozzle",Lower=10e-6);
    85 Honozzle_Shell          as length               (Brief="Height Under Shell Outlet Nozzle",Lower=10e-6);
    86 Lcf                                     as length               (Brief="Bundle-to-Shell Clearance",Lower=10e-8);
    87 
    88 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    89 #                               Tubes Geometrical Parameters                                           
    90 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    91 Ntt                                     as Integer                      (Brief="Total Number of Tubes in Shell",Default=100,Lower=1);
    92 Pattern                 as Switcher             (Brief="Tube Layout Characteristic Angle",Valid=["Triangle","Rotated Square","Square"],Default="Triangle");
    93 Ltube                                   as length                       (Brief="Effective Tube Length",Lower=0.1);
    94 pitch                           as length                       (Brief="Tube Pitch",Lower=1e-8);
    95 Kwall                                   as conductivity         (Brief="Tube Wall Material Thermal Conductivity");
    96 Dotube                                  as length                       (Brief="Tube Outside Diameter",Lower=10e-6);
    97 Ditube                          as length                       (Brief="Tube Inside Diameter",Lower=10e-6);
    98 Donozzle_Tube   as length                       (Brief="Tube Outlet Nozzle Diameter",Lower=10e-6);
    99 Dinozzle_Tube   as length                       (Brief="Tube Inlet Nozzle Diameter",Lower=10e-6);
    100 Aonozzle_Tube   as area                         (Brief="Tube Outlet Nozzle Area",Lower=10e-6);
    101 Ainozzle_Tube   as area                         (Brief="Tube Inlet Nozzle Area",Lower=10e-6);
    102 Kinlet_Tube             as positive                     (Brief="Tube Inlet Nozzle Pressure Loss Coeff",Default=1.1);
    103 Koutlet_Tube    as positive                     (Brief="Tube Outlet Nozzle Pressure Loss Coeff",Default=0.7);
    104 
    105 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    106 #                               Baffles Geometrical Parameters                                         
    107 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    108 Bc      as Integer      (Brief="Baffle Cut",Default=25,Lower=25);
    109 Nb      as Real         (Brief="Number of Baffles",Lower=1);
    110 Lcd     as length       (Brief="Baffle-to-Shell Clearance",Lower=10e-8);
    111 Ltd             as length       (Brief="Tube-to-Bafflehole Clearance",Lower=10e-8);
    112 
    113 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    114 #                               Fouling                                         
    115 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    116 Rfi                     as positive     (Brief="Inside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0);
    117 Rfo             as positive     (Brief="Outside Fouling Resistance",Unit='m^2*K/kW',Default=1e-6,Lower=0);
    118 
    119 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    120 #                               Auxiliar Parameters - Must be hidden                                           
    121 #+++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++++#
    122 Ods     as Real                 (Brief="Baffle Cut Angle in Degrees");
    123 Octl    as Real                 (Brief="Baffle Cut Angle relative to the centerline in Degrees");
    124 Ftw     as Real                 (Brief="Fraction of Number of Tubes in Baffle Window");
    125 Scd     as area         (Brief="Shell to Baffle Leakage Area");
    126 Std     as area         (Brief="Tube to Baffle Hole Leakage Area");
    127 Rs              as Real                 (Brief="Ratio of the shell to baffle leakage area");
    128 Dw    as length         (Brief="Hydraulic diameter of the baffle window");
     85Pi                                                      as constant   (Brief="Pi Number", Hidden = true, Default=3.14159265);
     86Aonozzle_Shell          as area                 (Brief="Shell Outlet Nozzle Area", Hidden = true, Lower=1E-6);
     87Ainozzle_Shell          as area                 (Brief="Shell Inlet Nozzle Area", Hidden = true, Lower=1E-6);
     88Aeonozzle_Shell         as area                 (Brief="Shell Outlet Escape Area Under Nozzle", Hidden = true, Lower=1E-6);
     89Aeinozzle_Shell         as area                 (Brief="Shell Inlet Escape Area Under Nozzle",Hidden = true, Lower=1E-6);
     90Aonozzle_Tube   as area                 (Brief="Tube Outlet Nozzle Area", Hidden = true, Lower=1E-6);
     91Ainozzle_Tube           as area                 (Brief="Tube Inlet Nozzle Area", Hidden = true, Lower=1E-6);
     92Kinlet_Tube             as positive     (Brief="Tube Inlet Nozzle Pressure Loss Coeff", Hidden = true, Default=1.1);
     93Koutlet_Tube            as positive     (Brief="Tube Outlet Nozzle Pressure Loss Coeff",Hidden = true, Default=0.7);
     94Ods                                             as Real                 (Brief="Baffle cut angle in degrees", Symbol = "\theta _{ds}", Hidden = true);
     95Octl                                    as Real                 (Brief="Baffle cut angle relative to the centerline in degrees", Symbol = "\theta _{ctl}", Hidden = true);
     96Ftw                                             as Real                 (Brief="Fraction of number of tubes in baffle window", Symbol = "F _{tw}", Hidden = true);
     97Scd                                             as area                 (Brief="Shell to baffle leakage area", Symbol = "S _{cd}", Hidden = true);
     98Std                                             as area                 (Brief="Tube to baffle hole leakage area", Symbol = "S _{td}", Hidden = true);
     99Rs                                              as Real                 (Brief="Ratio of the shell to baffle leakage area", Symbol = "R_s", Hidden = true);
     100Dw                                      as length               (Brief="Hydraulic diameter of the baffle window", Symbol = "D _w", Hidden = true);
    129101
    130102SET
    131103
    132         M                                               = PP.MolecularWeight();
    133         Pi                                              = 3.14159265;
    134 
    135 #"comments"
    136         Ods     = (360/Pi)*acos(1-0.02*Bc);
    137 
    138 #"comments"
    139         Octl    = (360/Pi)*acos((Dishell/(Dishell - Lcf - Dotube))*(1-0.02*Bc));
    140 
    141 #"comments"
     104#"Molecular weight"
     105        M       = PP.MolecularWeight();
     106       
     107#"Pi Number"
     108        Pi      = 3.14159265;
     109
     110#"Baffle cut angle in degrees"
     111        Ods     = (360/Pi)*acos(1-0.02*Baffles.BaffleCut);
     112
     113#"Baffle cut angle relative to the centerline"
     114        Octl    = (360/Pi)*acos((Shell.ShellID/(Shell.ShellID - Clearances.BundleToShell - Tubes.TubeOD))*(1-0.02*Baffles.BaffleCut));
     115
     116#"Fraction of number of tubes in baffle window"
    142117        Ftw     = (Octl/360)-sin(Octl*Pi/180)/(2*Pi);
    143118
    144 #"comments"
    145         Scd     = Pi*Dishell*Lcd*((360-Ods)/720);
    146 
    147 #"comments"
    148         Std     = Pi*0.25*((Ltd + Dotube)^2-Dotube*Dotube)*Ntt*(1-Ftw);
     119#"Shell to baffle leakage area"
     120        Scd     = Pi*Shell.ShellID*Clearances.BaffleToShell *((360-Ods)/720);
     121
     122#"Tube to baffle hole leakage area"
     123        Std     = Pi*0.25*((Clearances.TubeToBaffle + Tubes.TubeOD)^2-Tubes.TubeOD*Tubes.TubeOD)*Tubes.NumberOfTubes*(1-Ftw);
    149124
    150125#"comments"
    … …  
    152127
    153128#"comments"
    154         Dw      = (4*abs((Pi*Dishell*Dishell*((Ods/360)-sin(Ods*Pi/180)/(2*Pi))/4)-(Ntt*Pi*Dotube*Dotube*Ftw/4)))/(Pi*Dotube*Ntt*Ftw+ Pi*Dishell*Ods/360);
     129        Dw      = (4*abs((Pi*Shell.ShellID*Shell.ShellID*((Ods/360)-sin(Ods*Pi/180)/(2*Pi))/4)-(Tubes.NumberOfTubes*Pi*Tubes.TubeOD*Tubes.TubeOD*Ftw/4)))/(Pi*Tubes.TubeOD*Tubes.NumberOfTubes*Ftw+ Pi*Shell.ShellID*Ods/360);
    155130
    156131#"Tube Side Inlet Nozzle Area"
    157         Ainozzle_Tube = (Pi*Dinozzle_Tube*Dinozzle_Tube)/4;
     132        Ainozzle_Tube = 0.25*Pi*Tubes.InletNozzleID^2;
    158133
    159134#"Tube Side Outlet Nozzle Area"
    160         Aonozzle_Tube = (Pi*Donozzle_Tube*Donozzle_Tube)/4;
     135        Aonozzle_Tube = 0.25*Pi*Tubes.OutletNozzleID^2;
    161136
    162137#"Tube Inlet Nozzle Pressure Loss Coeff"
    … …  
    167142
    168143#"Shell Outlet Nozzle Area"
    169         Aonozzle_Shell  = (Pi*Donozzle_Shell*Donozzle_Shell)/4;
     144        Aonozzle_Shell  = 0.25*Pi*Shell.OutletNozzleID^2;
    170145
    171146#"Shell Inlet Nozzle Area"
    172         Ainozzle_Shell  = (Pi*Dinozzle_Shell*Dinozzle_Shell)/4;
     147        Ainozzle_Shell  = 0.25*Pi*Shell.InletNozzleID^2;
    173148
    174149#"Shell Outlet Escape Area Under Nozzle"
    175         Aeonozzle_Shell = Pi*Donozzle_Shell*Honozzle_Shell + 0.6*Aonozzle_Shell*(1-(Dotube/pitch));
     150        Aeonozzle_Shell = Pi*Shell.OutletNozzleID*Clearances.Honozzle_Shell + 0.6*Aonozzle_Shell*(1-(Tubes.TubeOD/Tubes.TubePitch));
    176151
    177152#"Shell Inlet Escape Area Under Nozzle"
    178         Aeinozzle_Shell = Pi*Dinozzle_Shell*Hinozzle_Shell + 0.6*Ainozzle_Shell*(1-(Dotube/pitch));
     153        Aeinozzle_Shell = Pi*Shell.InletNozzleID*Clearances.Hinozzle_Shell + 0.6*Ainozzle_Shell*(1-(Tubes.TubeOD/Tubes.TubePitch));
    179154
    180155EQUATIONS
    … …  
    348323       
    349324"Jc Factor"
    350         Shell.HeatTransfer.Jc = 0.55+0.72*(1-2*Ftw);
     325        Jc = 0.55+0.72*(1-2*Ftw);
    351326
    352327"Jl Factor"
    353         Shell.HeatTransfer.Jl = 0.44*(1-Rs)+(1-0.44*(1-Rs))*exp(-2.2*(Scd + Std)/Shell.HeatTransfer.Sm);
     328        Jl = 0.44*(1-Rs)+(1-0.44*(1-Rs))*exp(-2.2*(Scd + Std)/Sm);
    354329
    355330"Total J Factor"
    356         Shell.HeatTransfer.Jtotal = Shell.HeatTransfer.Jc*Shell.HeatTransfer.Jl*Shell.HeatTransfer.Jb*Shell.HeatTransfer.Jr*Shell.HeatTransfer.Js;
     331        Jtotal = Jc*Jl*Jb*Jr*Js;
    357332
    358333"Mass Velocity in Window Zone"
    359         mw      = Shell.Properties.Inlet.Fw/sqrt(abs(Shell.HeatTransfer.Sm*abs((Pi*Dishell*Dishell*((Ods/360)-sin(Ods*Pi/180)/(2*Pi))/4)-(Ntt*Pi*Dotube*Dotube*Ftw/4))));
     334        mw      = Shell.Properties.Inlet.Fw/sqrt(abs(Sm*abs((Pi*Shell.ShellID*Shell.ShellID*((Ods/360)-sin(Ods*Pi/180)/(2*Pi))/4)-(Tubes.NumberOfTubes*Pi*Tubes.TubeOD*Tubes.TubeOD*Ftw/4))));
    360335
    361336switch TubeFlowRegime
    … …  
    374349
    375350"Nusselt Number in Laminar Flow - Hausen Equation"
    376         Tubes.HeatTransfer.Nu = 3.665 + ((0.19*((Ditube/Ltube)*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR)^0.8)/(1+0.117*((Ditube/Ltube)*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR)^0.467));
     351        Tubes.HeatTransfer.Nu = 3.665 + ((0.19*((Tubes.TubeID/Tubes.TubeLength)*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR)^0.8)/(1+0.117*((Tubes.TubeID/Tubes.TubeLength)*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR)^0.467));
    377352       
    378353        case "Schlunder":
    379354       
    380355"Nusselt Number in Laminar Flow - Schlunder Equation"
    381         Tubes.HeatTransfer.Nu = (49.027896+4.173281*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR*(Ditube/Ltube))^(1/3);
     356        Tubes.HeatTransfer.Nu = (49.027896+4.173281*Tubes.HeatTransfer.Re*Tubes.HeatTransfer.PR*(Tubes.TubeID/Tubes.TubeLength))^(1/3);
    382357
    383358end
    … …  
    441416
    442417"Shell Side Cross Flow Area"
    443         Shell.HeatTransfer.Sm= Baffles.Ls*(Lcf+((Dishell-Lcf-Dotube)/pitch)*(pitch-Dotube));
     418        Sm= Baffles.Central_Spacing*(Clearances.BundleToShell+((Shell.ShellID-Clearances.BundleToShell-Tubes.TubeOD)/Tubes.TubePitch)*(Tubes.TubePitch-Tubes.TubeOD));
    444419
    445420"Number of Tube rows Crossed in one Crossflow Section"
    446         Nc      = Dishell*(1-0.02*Bc)/(0.866*pitch);
     421        Nc      = Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.866*Tubes.TubePitch);
    447422
    448423"Number of Effective Crossflow rows in Each Window"
    449         Ncw = 0.8*(Dishell*0.01*Bc-(Lcf + Dotube)*0.5)/(0.866*pitch);
     424        Ncw = 0.8*(Shell.ShellID*0.01*Baffles.BaffleCut-(Clearances.BundleToShell + Tubes.TubeOD)*0.5)/(0.866*Tubes.TubePitch);
    450425
    451426"Variable for calculating Ji heat transfer correction Factor"
    … …  
    456431
    457432"Correction Factor for Pressure Drop"
    458         Rss     = Nss/(Dishell*(1-0.02*Bc)/(0.866*pitch)) ;
     433        Rss     = Clearances.SealStrip/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.866*Tubes.TubePitch)) ;
    459434       
    460435"Ideal Shell Side Pressure Drop"
    461         Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Dishell*(1-0.02*Bc)/(0.866*pitch))*(Shell.Properties.Inlet.Fw/Shell.HeatTransfer.Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
     436        Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.866*Tubes.TubePitch))*(Shell.Properties.Inlet.Fw/Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
    462437
    463438"Shell Pressure End Zones"
    464         Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Dishell*(1-0.02*Bc)/(0.866*pitch))))*Rb*Rspd;
     439        Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.866*Tubes.TubePitch))))*Rb*Rspd;
    465440
    466441switch ShellRange
    … …  
    469444       
    470445"Ji Factor"
    471         Shell.HeatTransfer.Ji =1.40*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^0.667;
     446        Ji =1.40*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^0.667;
    472447       
    473448"Shell Side Pressure Drop Friction Factor"
    474         Shell.PressureDrop.fi=48*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-1;
     449        Shell.PressureDrop.fi=48*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-1;
    475450       
    476451        when Shell.HeatTransfer.Re > 10 switchto "range2";
    … …  
    479454       
    480455"Ji Factor"
    481         Shell.HeatTransfer.Ji =1.36*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.657;
     456        Ji =1.36*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.657;
    482457       
    483458"Shell Side Pressure Drop Friction Factor"
    484         Shell.PressureDrop.fi=45.10*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.973;
     459        Shell.PressureDrop.fi=45.10*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.973;
    485460       
    486461        when Shell.HeatTransfer.Re > 100 switchto "range3";
    … …  
    489464
    490465"Ji Factor"
    491         Shell.HeatTransfer.Ji =0.593*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.477;
     466        Ji =0.593*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.477;
    492467       
    493468"Shell Side Pressure Drop Friction Factor"
    494         Shell.PressureDrop.fi=4.570*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.476;
     469        Shell.PressureDrop.fi=4.570*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.476;
    495470       
    496471        when Shell.HeatTransfer.Re > 1000 switchto "range4";
    … …  
    499474
    500475"Ji Factor"
    501         Shell.HeatTransfer.Ji =0.321*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.388;
     476        Ji =0.321*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.388;
    502477       
    503478"Shell Side Pressure Drop Friction Factor"
    504         Shell.PressureDrop.fi=0.486*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.152;
     479        Shell.PressureDrop.fi=0.486*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.152;
    505480
    506481        when Shell.HeatTransfer.Re > 10000 switchto "range5";
    … …  
    509484
    510485"Ji Factor"
    511         Shell.HeatTransfer.Ji =0.321*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.388;
     486        Ji =0.321*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.388;
    512487
    513488"Shell Side Pressure Drop Friction Factor"
    514         Shell.PressureDrop.fi=0.372*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.123;
     489        Shell.PressureDrop.fi=0.372*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.123;
    515490       
    516491        when Shell.HeatTransfer.Re < 10000 switchto "range4";
    … …  
    521496
    522497"Shell Side Cross Flow Area"
    523         Shell.HeatTransfer.Sm= Baffles.Ls*(Lcf+((Dishell-Lcf-Dotube)/(0.707*pitch))*(pitch-Dotube));
     498        Sm= Baffles.Central_Spacing*(Clearances.BundleToShell+((Shell.ShellID-Clearances.BundleToShell-Tubes.TubeOD)/(0.707*Tubes.TubePitch))*(Tubes.TubePitch-Tubes.TubeOD));
    524499
    525500"Number of Tube rows Crossed in one Crossflow Section"
    526         Nc      = Dishell*(1-0.02*Bc)/(0.707*pitch);
     501        Nc      = Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.707*Tubes.TubePitch);
    527502
    528503"Number of Effective Crossflow rows in Each Window"
    529         Ncw = 0.8*(Dishell*0.01*Bc-(Lcf + Dotube)*0.5)/(0.707*pitch);
     504        Ncw = 0.8*(Shell.ShellID*0.01*Baffles.BaffleCut-(Clearances.BundleToShell + Tubes.TubeOD)*0.5)/(0.707*Tubes.TubePitch);
    530505
    531506"Variable for calculating Ji heat transfer correction Factor"
    … …  
    536511
    537512"Correction Factor for Pressure Drop"
    538         Rss     = Nss/(Dishell*(1-0.02*Bc)/(0.707*pitch)) ;
     513        Rss     = Clearances.SealStrip/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.707*Tubes.TubePitch)) ;
    539514
    540515"Ideal Shell Side Pressure Drop"
    541         Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Dishell*(1-0.02*Bc)/(0.707*pitch))*(Shell.Properties.Inlet.Fw/Shell.HeatTransfer.Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
     516        Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.707*Tubes.TubePitch))*(Shell.Properties.Inlet.Fw/Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
    542517
    543518"Shell Pressure End Zones"
    544         Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Dishell*(1-0.02*Bc)/(0.707*pitch))))*Rb*Rspd;
     519        Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/(0.707*Tubes.TubePitch))))*Rb*Rspd;
    545520
    546521switch ShellRange
    … …  
    549524
    550525"Ji Factor"
    551         Shell.HeatTransfer.Ji =1.550*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^0.667;
     526        Ji =1.550*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^0.667;
    552527
    553528"Shell Side Pressure Drop Friction Factor"
    554         Shell.PressureDrop.fi=32*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-1;
     529        Shell.PressureDrop.fi=32*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-1;
    555530       
    556531        when Shell.HeatTransfer.Re > 10 switchto "range2";
    … …  
    559534
    560535"Ji Factor"
    561         Shell.HeatTransfer.Ji =0.498*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^0.656;
     536        Ji =0.498*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^0.656;
    562537
    563538"Shell Side Pressure Drop Friction Factor"
    564         Shell.PressureDrop.fi=26.20*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.913;
     539        Shell.PressureDrop.fi=26.20*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.913;
    565540       
    566541        when Shell.HeatTransfer.Re > 100 switchto "range3";
    … …  
    569544
    570545"Ji Factor"
    571         Shell.HeatTransfer.Ji =0.730*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^0.500;
     546        Ji =0.730*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^0.500;
    572547
    573548"Shell Side Pressure Drop Friction Factor"
    574         Shell.PressureDrop.fi=3.50*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.476;
     549        Shell.PressureDrop.fi=3.50*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.476;
    575550       
    576551        when Shell.HeatTransfer.Re > 1000 switchto "range4";
    … …  
    579554       
    580555"Ji Factor"
    581         Shell.HeatTransfer.Ji =0.370*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.396;
     556        Ji =0.370*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.396;
    582557       
    583558"Shell Side Pressure Drop Friction Factor"
    584         Shell.PressureDrop.fi=0.333*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.136;
     559        Shell.PressureDrop.fi=0.333*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.136;
    585560
    586561        when Shell.HeatTransfer.Re > 10000 switchto "range5";
    … …  
    589564
    590565"Ji Factor"
    591         Shell.HeatTransfer.Ji =0.370*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.396;
     566        Ji =0.370*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.396;
    592567       
    593568"Shell Side Pressure Drop Friction Factor"
    594         Shell.PressureDrop.fi=0.303*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.126;
     569        Shell.PressureDrop.fi=0.303*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.126;
    595570       
    596571        when Shell.HeatTransfer.Re < 10000 switchto "range4";
    … …  
    601576
    602577"Shell Side Cross Flow Area"
    603         Shell.HeatTransfer.Sm= Baffles.Ls*(Lcf+((Dishell-Lcf-Dotube)/pitch)*(pitch-Dotube));
     578        Sm= Baffles.Central_Spacing*(Clearances.BundleToShell+((Shell.ShellID-Clearances.BundleToShell-Tubes.TubeOD)/Tubes.TubePitch)*(Tubes.TubePitch-Tubes.TubeOD));
    604579
    605580"Number of Tube rows Crossed in one Crossflow Section"
    606         Nc      = Dishell*(1-0.02*Bc)/pitch;
     581        Nc      = Shell.ShellID*(1-0.02*Baffles.BaffleCut)/Tubes.TubePitch;
    607582       
    608583"Number of Effective Crossflow rows in Each Window"
    609         Ncw = 0.8*(Dishell*0.01*Bc-(Lcf + Dotube)*0.5)/pitch;
     584        Ncw = 0.8*(Shell.ShellID*0.01*Baffles.BaffleCut-(Clearances.BundleToShell + Tubes.TubeOD)*0.5)/Tubes.TubePitch;
    610585
    611586"Variable for calculating Ji heat transfer correction Factor"
    … …  
    616591
    617592"Correction Factor for Pressure Drop"
    618         Rss     = Nss/(Dishell*(1-0.02*Bc)/pitch) ;
     593        Rss     = Clearances.SealStrip/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/Tubes.TubePitch) ;
    619594
    620595"Ideal Shell Side Pressure Drop"
    621         Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Dishell*(1-0.02*Bc)/pitch)*(Shell.Properties.Inlet.Fw/Shell.HeatTransfer.Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
     596        Shell.PressureDrop.Pideal= 2*Shell.PressureDrop.fi*(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/Tubes.TubePitch)*(Shell.Properties.Inlet.Fw/Sm)^2/(Shell.Properties.Average.rho*Shell.HeatTransfer.Phi);
    622597
    623598"Shell Pressure End Zones"
    624         Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Dishell*(1-0.02*Bc)/pitch)))*Rb*Rspd;
     599        Shell.PressureDrop.PdEndZones = Shell.PressureDrop.Pideal*(1+ (Ncw/(Shell.ShellID*(1-0.02*Baffles.BaffleCut)/Tubes.TubePitch)))*Rb*Rspd;
    625600
    626601switch ShellRange
    … …  
    629604
    630605"Ji Factor"
    631         Shell.HeatTransfer.Ji =0.970*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.667;
     606        Ji =0.970*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.667;
    632607       
    633608"Shell Side Pressure Drop Friction Factor"     
    634         Shell.PressureDrop.fi=35*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-1;
     609        Shell.PressureDrop.fi=35*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-1;
    635610
    636611        when Shell.HeatTransfer.Re > 10 switchto "range2";
    … …  
    639614
    640615"Ji Factor"
    641         Shell.HeatTransfer.Ji =0.900*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.631;
     616        Ji =0.900*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.631;
    642617
    643618"Shell Side Pressure Drop Friction Factor"     
    644         Shell.PressureDrop.fi=32.10*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.963;
     619        Shell.PressureDrop.fi=32.10*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.963;
    645620
    646621        when Shell.HeatTransfer.Re > 100 switchto "range3";
    … …  
    649624
    650625"Ji Factor"
    651         Shell.HeatTransfer.Ji =0.408*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.460;
     626        Ji =0.408*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.460;
    652627
    653628"Shell Side Pressure Drop Friction Factor"     
    654         Shell.PressureDrop.fi=6.090*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.602;
     629        Shell.PressureDrop.fi=6.090*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.602;
    655630
    656631        when Shell.HeatTransfer.Re > 1000 switchto "range4";
    … …  
    659634       
    660635"Ji Factor"
    661         Shell.HeatTransfer.Ji =0.107*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.266;
     636        Ji =0.107*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.266;
    662637
    663638"Shell Side Pressure Drop Friction Factor"     
    664         Shell.PressureDrop.fi=0.0815*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^0.022;
     639        Shell.PressureDrop.fi=0.0815*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^0.022;
    665640
    666641        when Shell.HeatTransfer.Re > 10000 switchto "range5";
    … …  
    669644       
    670645"Ji Factor"
    671         Shell.HeatTransfer.Ji =0.370*((1.33*Dotube/pitch)^a)*Shell.HeatTransfer.Re^-0.395;
     646        Ji =0.370*((1.33*Tubes.TubeOD/Tubes.TubePitch)^a)*Shell.HeatTransfer.Re^-0.395;
    672647
    673648"Shell Side Pressure Drop Friction Factor"     
    674         Shell.PressureDrop.fi=0.391*((1.33*Dotube/pitch)^b)*Shell.HeatTransfer.Re^-0.148;
     649        Shell.PressureDrop.fi=0.391*((1.33*Tubes.TubeOD/Tubes.TubePitch)^b)*Shell.HeatTransfer.Re^-0.148;
    675650
    676651        when Shell.HeatTransfer.Re < 10000 switchto "range4";
    … …  
    685660
    686661"Jr Factor"     
    687         Shell.HeatTransfer.Jr = (10/((Nc +Ncw)*(Nb+1)))^0.18;
     662        Jr = (10/((Nc +Ncw)*(Baffles.NumberOfBaffles+1)))^0.18;
    688663
    689664"Js Factor"
    690         Shell.HeatTransfer.Js = (Nb-1+(Baffles.Lsi/Baffles.Ls)^0.7 + (Baffles.Lso/Baffles.Ls)^0.7)/(Nb-1+(Baffles.Lsi/Baffles.Ls) + (Baffles.Lso/Baffles.Ls));
     665        Js = (Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing)^0.7 + (Baffles.Outlet_Spacing/Baffles.Central_Spacing)^0.7)/(Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing) + (Baffles.Outlet_Spacing/Baffles.Central_Spacing));
    691666
    692667"Jb Factor"
    693         Shell.HeatTransfer.Jb = exp(-1.35*( Lcf+ Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm*(1-(2*(Nss/Nc)^(1/3))));
     668        Jb =    exp(-1.35*( Clearances.BundleToShell+ Tubes.TubeOD)*Baffles.Central_Spacing/Sm*(1-(2*(Clearances.SealStrip/Nc)^(1/3))));
    694669
    695670"ByPass Correction Factor for Pressure Drop"
    696         Rb      = exp(-4.7*((Lcf + Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm)*(1-(2*Rss)^(1/3)));
     671        Rb      = exp(-4.7*((Clearances.BundleToShell + Tubes.TubeOD)*Baffles.Central_Spacing/Sm)*(1-(2*Rss)^(1/3)));
    697672
    698673"Pressure Drop Correction Factor for Unequal Baffle Spacing"
    699         Rspd = (Baffles.Ls/Baffles.Lso) + (Baffles.Ls/Baffles.Lsi);
     674        Rspd = (Baffles.Central_Spacing/Baffles.Outlet_Spacing) + (Baffles.Central_Spacing/Baffles.Inlet_Spacing);
    700675
    701676"Shell Pressure Drop Baffle Window"
    702         Shell.PressureDrop.Pdwindow    = Nb*((26/Shell.Properties.Average.rho)*mw*Shell.Properties.Average.Mu*(Ncw/(pitch-Dotube)+ Baffles.Ls/(Dw*Dw))+ 0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Shell.HeatTransfer.Sm)^(-0.15*(1+Rs) + 0.8));
     677        Shell.PressureDrop.Pdwindow    = Baffles.NumberOfBaffles*((26/Shell.Properties.Average.rho)*mw*Shell.Properties.Average.Mu*(Ncw/(Tubes.TubePitch-Tubes.TubeOD)+ Baffles.Central_Spacing/(Dw*Dw))+ 0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Sm)^(-0.15*(1+Rs) + 0.8));
    703678
    704679        when Shell.HeatTransfer.Re > 20 switchto "laminar";
    … …  
    707682
    708683"Jr Factor"     
    709         Shell.HeatTransfer.Jr = (10/((Nc +Ncw)*(Nb+1)))^0.18 + (0.25-0.0125*Shell.HeatTransfer.Re)*((10/((Nc +Ncw)*(Nb+1)))^0.18 - 1);
     684        Jr = (10/((Nc +Ncw)*(Baffles.NumberOfBaffles+1)))^0.18 + (0.25-0.0125*Shell.HeatTransfer.Re)*((10/((Nc +Ncw)*(Baffles.NumberOfBaffles+1)))^0.18 - 1);
    710685
    711686"Js Factor"
    712         Shell.HeatTransfer.Js = (Nb-1+(Baffles.Lsi/Baffles.Ls)^0.7 + (Baffles.Lso/Baffles.Ls)^0.7)/(Nb-1+(Baffles.Lsi/Baffles.Ls) + (Baffles.Lso/Baffles.Ls));
     687        Js = (Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing)^0.7 + (Baffles.Outlet_Spacing/Baffles.Central_Spacing)^0.7)/(Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing) + (Baffles.Outlet_Spacing/Baffles.Central_Spacing));
    713688
    714689"Jb Factor"
    715         Shell.HeatTransfer.Jb = exp(-1.35*( Lcf+ Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm*(1-(2*(Nss/Nc)^(1/3))));
     690        Jb =    exp(-1.35*( Clearances.BundleToShell+ Tubes.TubeOD)*Baffles.Central_Spacing/Sm*(1-(2*(Clearances.SealStrip/Nc)^(1/3))));
    716691
    717692"ByPass Correction Factor for Pressure Drop"
    718         Rb      = exp(-4.7*((Lcf + Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm)*(1-(2*Rss)^(1/3)));
     693        Rb      = exp(-4.7*((Clearances.BundleToShell+ Tubes.TubeOD)*Baffles.Central_Spacing/Sm)*(1-(2*Rss)^(1/3)));
    719694
    720695"Pressure Drop Correction Factor for Unequal Baffle Spacing"
    721         Rspd = (Baffles.Ls/Baffles.Lso) + (Baffles.Ls/Baffles.Lsi);
     696        Rspd = (Baffles.Central_Spacing/Baffles.Outlet_Spacing) + (Baffles.Central_Spacing/Baffles.Inlet_Spacing);
    722697
    723698"Shell Pressure Drop Baffle Window"
    724         Shell.PressureDrop.Pdwindow    = Nb*((26/Shell.Properties.Average.rho)*mw*Shell.Properties.Average.Mu*(Ncw/(pitch-Dotube)+ Baffles.Ls/(Dw*Dw))+ 0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Shell.HeatTransfer.Sm)^(-0.15*(1+Rs) + 0.8));
     699        Shell.PressureDrop.Pdwindow    = Baffles.NumberOfBaffles*((26/Shell.Properties.Average.rho)*mw*Shell.Properties.Average.Mu*(Ncw/(Tubes.TubePitch-Tubes.TubeOD)+ Baffles.Central_Spacing/(Dw*Dw))+ 0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Sm)^(-0.15*(1+Rs) + 0.8));
    725700
    726701        when Shell.HeatTransfer.Re < 20 switchto "deep laminar";
    … …  
    730705
    731706"Jr Factor"     
    732         Shell.HeatTransfer.Jr = 1;
     707        Jr = 1;
    733708
    734709"Js Factor"
    735         Shell.HeatTransfer.Js = (Nb-1+(Baffles.Lsi/Baffles.Ls)^0.4 + (Baffles.Lso/Baffles.Ls)^0.4)/(Nb-1+(Baffles.Lsi/Baffles.Ls) + (Baffles.Lso/Baffles.Ls));
     710        Js = (Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing)^0.4 + (Baffles.Outlet_Spacing/Baffles.Central_Spacing)^0.4)/(Baffles.NumberOfBaffles-1+(Baffles.Inlet_Spacing/Baffles.Central_Spacing) + (Baffles.Outlet_Spacing/Baffles.Central_Spacing));
    736711
    737712"Jb Factor"
    738         Shell.HeatTransfer.Jb = exp(-1.25*( Lcf+ Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm*(1-(2*(Nss/Nc)^(1/3))));
     713        Jb =    exp(-1.25*( Clearances.BundleToShell+ Tubes.TubeOD)*Baffles.Central_Spacing/Sm*(1-(2*(Clearances.SealStrip/Nc)^(1/3))));
    739714
    740715"ByPass Correction Factor for Pressure Drop"
    741         Rb      = exp(-3.7*((Lcf + Dotube)*Baffles.Ls/Shell.HeatTransfer.Sm)*(1-(2*Rss)^(1/3)));
     716        Rb      = exp(-3.7*((Clearances.BundleToShell + Tubes.TubeOD)*Baffles.Central_Spacing/Sm)*(1-(2*Rss)^(1/3)));
    742717
    743718"Pressure Drop Correction Factor for Unequal Baffle Spacing"
    744         Rspd = (Baffles.Ls/Baffles.Lso)^1.8 + (Baffles.Ls/Baffles.Lsi)^1.8;
     719        Rspd = (Baffles.Central_Spacing/Baffles.Outlet_Spacing)^1.8 + (Baffles.Central_Spacing/Baffles.Inlet_Spacing)^1.8;
    745720
    746721"Shell Pressure Drop Baffle Window"
    747         Shell.PressureDrop.Pdwindow    = Nb*((2+0.6*Ncw)*0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Shell.HeatTransfer.Sm)^(-0.15*(1+Rs) + 0.8));
     722        Shell.PressureDrop.Pdwindow    = Baffles.NumberOfBaffles*((2+0.6*Ncw)*0.5*mw*mw/Shell.Properties.Average.rho)*exp(-1.33*(1+Rs)*((Scd + Std)/Sm)^(-0.15*(1+Rs) + 0.8));
    748723       
    749724        when Shell.HeatTransfer.Re < 100 switchto "laminar";
    … …  
    752727
    753728"Shell Pressure Drop Cross Flow"
    754         Shell.PressureDrop.PdCross = Shell.PressureDrop.Pideal*Rb*(Nb-1)*exp(-1.33*(1+Rs)*((Scd + Std)/Shell.HeatTransfer.Sm)^(-0.15*(1+Rs) + 0.8));
     729        Shell.PressureDrop.PdCross = Shell.PressureDrop.Pideal*Rb*(Baffles.NumberOfBaffles-1)*exp(-1.33*(1+Rs)*((Scd + Std)/Sm)^(-0.15*(1+Rs) + 0.8));
    755730
    756731"Shell Side Phi correction"
    … …  
    767742
    768743"Tube Side Pressure Drop"
    769         Tubes.PressureDrop.PdTube       = 2*Tubes.PressureDrop.fi*Ltube*Tubes.Properties.Average.rho*(Tubes.HeatTransfer.Vtube^2)*Tpass/(Ditube*Tubes.HeatTransfer.Phi);
     744        Tubes.PressureDrop.PdTube       = 2*Tubes.PressureDrop.fi*Tubes.TubeLength*Tubes.Properties.Average.rho*(Tubes.HeatTransfer.Vtube^2)*Tubes.Tubepasses/(Tubes.TubeID*Tubes.HeatTransfer.Phi);
    770745
    771746"Pressure Drop Tube Side Inlet Nozzle"
    … …  
    806781
    807782"Tube Side Velocity"
    808         Tubes.HeatTransfer.Vtube        = Tubes.Properties.Inlet.Fw*Tpass/((Pi*Ditube*Ditube/4)*Tubes.Properties.Average.rho*Ntt);
     783        Tubes.HeatTransfer.Vtube        = Tubes.Properties.Inlet.Fw*Tubes.Tubepasses/((Pi*Tubes.TubeID*Tubes.TubeID/4)*Tubes.Properties.Average.rho*Tubes.NumberOfTubes);
    809784
    810785"Tube Side Reynolds Number"
    811         Tubes.HeatTransfer.Re           = (Tubes.Properties.Average.rho*Tubes.HeatTransfer.Vtube*Ditube)/Tubes.Properties.Average.Mu;
     786        Tubes.HeatTransfer.Re           = (Tubes.Properties.Average.rho*Tubes.HeatTransfer.Vtube*Tubes.TubeID)/Tubes.Properties.Average.Mu;
    812787       
    813788"Tube Side Prandtl Number"
    … …  
    815790
    816791"Tube Side Film Coefficient"
    817         Tubes.HeatTransfer.htube= (Tubes.HeatTransfer.Nu*Tubes.Properties.Average.K/Ditube)*Tubes.HeatTransfer.Phi;
     792        Tubes.HeatTransfer.htube= (Tubes.HeatTransfer.Nu*Tubes.Properties.Average.K/Tubes.TubeID)*Tubes.HeatTransfer.Phi;
    818793
    819794"Shell Side Prandtl Number"
    … …  
    821796
    822797"Overall Heat Transfer Coefficient Dirty"
    823         Details.Ud=1/(Dotube/(Tubes.HeatTransfer.htube*Ditube)+Rfo+Rfi*(Dotube/Ditube)+(Dotube*ln(Dotube/Ditube)/(2*Kwall))+(1/(Shell.HeatTransfer.hshell)));
     798        Details.Ud=1/(Tubes.TubeOD/(Tubes.HeatTransfer.htube*Tubes.TubeID)+Shell.Fouling+Tubes.Fouling*(Tubes.TubeOD/Tubes.TubeID)+(Tubes.TubeOD*ln(Tubes.TubeOD/Tubes.TubeID)/(2*Tubes.Kwall))+(1/(Shell.HeatTransfer.hshell)));
    824799
    825800"Overall Heat Transfer Coefficient Clean"
    826         Details.Uc=1/(Dotube/(Tubes.HeatTransfer.htube*Ditube)+(Dotube*ln(Dotube/Ditube)/(2*Kwall))+(1/(Shell.HeatTransfer.hshell)));
     801        Details.Uc=1/(Tubes.TubeOD/(Tubes.HeatTransfer.htube*Tubes.TubeID)+(Tubes.TubeOD*ln(Tubes.TubeOD/Tubes.TubeID)/(2*Tubes.Kwall))+(1/(Shell.HeatTransfer.hshell)));
    827802
    828803"Exchange Surface Area"
    829         Details.A=Pi*Dotube*Ntt*Ltube;
    830 
    831 "Baffles Spacing"
    832         Ltube = Baffles.Lsi+Baffles.Lso+Baffles.Ls*(Nb-1);
     804        Details.A=Pi*Tubes.TubeOD*Tubes.NumberOfTubes*Tubes.TubeLength;
     805
     806"Baffle Spacing Constraint"
     807        Tubes.TubeLength = Baffles.Inlet_Spacing+Baffles.Outlet_Spacing+Baffles.Central_Spacing*(Baffles.NumberOfBaffles-1);
    833808
    834809"Shell Side Reynolds Number"
    835         Shell.HeatTransfer.Re = (Dotube*Shell.Properties.Inlet.Fw/Shell.HeatTransfer.Sm)/Shell.Properties.Average.Mu;
     810        Shell.HeatTransfer.Re = (Tubes.TubeOD*Shell.Properties.Inlet.Fw/Sm)/Shell.Properties.Average.Mu;
    836811
    837812"Shell Heat Transfer Coefficient"
    838         Shell.HeatTransfer.hshell                       = Shell.HeatTransfer.Ji*(Shell.Properties.Average.Cp/Shell.Properties.Average.Mw)*(Shell.Properties.Inlet.Fw/Shell.HeatTransfer.Sm)*(Shell.HeatTransfer.PR^(-2/3))*Shell.HeatTransfer.Jtotal*Shell.HeatTransfer.Phi;
     813        Shell.HeatTransfer.hshell                       = Ji*(Shell.Properties.Average.Cp/Shell.Properties.Average.Mw)*(Shell.Properties.Inlet.Fw/Sm)*(Shell.HeatTransfer.PR^(-2/3))*Jtotal*Shell.HeatTransfer.Phi;
    839814
    840815end
    … …  
    856831
    857832"Number of Units Transference"
    858         Method.NTU*Method.Cmin = Details.Ud*Pi*Dotube*Ntt*Ltube;
     833        Method.NTU*Method.Cmin = Details.Ud*Pi*Tubes.TubeOD*Tubes.NumberOfTubes*Tubes.TubeLength;
    859834
    860835"Minimum Heat Capacity"
    … …  
    947922
    948923"Exchange Surface Area"
    949         Details.Q   = Details.Ud*Pi*Dotube*Ntt*Ltube*Method.LMTD*Method.Fc;
     924        Details.Q   = Details.Ud*Pi*Tubes.TubeOD*Tubes.NumberOfTubes*Tubes.TubeLength*Method.LMTD*Method.Fc;
    950925
    951926switch HotSide

  • trunk/sample/heat_exchangers/sample_Detailed.mso

    r382 r490  
    6262#       Shell Geometrical Parameters
    6363#=====================================================================       
    64 exchanger.Tpass                 = 2;
    65 exchanger.Dishell               = 0.75  *'m';
    66 exchanger.Lcf                   = 0.043  *'m';
    67 exchanger.Nss                   = 2;
    68 exchanger.Donozzle_Shell    = 0.1937    *'m';
    69 exchanger.Dinozzle_Shell    = 0.1937    *'m';
    70 exchanger.Honozzle_Shell    = 0.0225    *'m';
    71 exchanger.Hinozzle_Shell    = 0.02155   *'m';
     64exchanger.Tubes.Tubepasses                      = 2;
     65exchanger.Shell.ShellID                 = 0.75  *'m';
     66exchanger.Clearances.BundleToShell                      = 0.043  *'m';
     67exchanger.Clearances.SealStrip                  = 2;
     68exchanger.Shell.InletNozzleID    = 0.1937       *'m';
     69exchanger.Shell.OutletNozzleID    = 0.1937      *'m';
     70exchanger.Clearances.Honozzle_Shell    = 0.0225         *'m';
     71exchanger.Clearances.Hinozzle_Shell    = 0.02155        *'m';
    7272#=====================================================================
    7373#       Tubes Geometrical Parameters
    7474#=====================================================================
    75 exchanger.Ntt                   = 500;
     75exchanger.Tubes.NumberOfTubes                   = 500;
    7676exchanger.Pattern                       = "Triangle";
    77 exchanger.pitch                         = 0.0254        *'m';
    78 exchanger.Ltube                 = 5.5           *'m';
    79 exchanger.Ditube                = 0.013395  *'m';
    80 exchanger.Dotube                = 0.015875  *'m';
    81 exchanger.Kwall                         = 0.057         *'kW/m/K';
    82 exchanger.Donozzle_Tube     = 0.203     *'m';
    83 exchanger.Dinozzle_Tube         = 0.203         *'m';
     77exchanger.Tubes.TubePitch                       = 0.0254        *'m';
     78exchanger.Tubes.TubeLength                      = 5.5           *'m';
     79exchanger.Tubes.TubeID                  = 0.013395  *'m';
     80exchanger.Tubes.TubeOD                  = 0.015875  *'m';
     81exchanger.Tubes.Kwall                           = 0.057         *'kW/m/K';
     82exchanger.Tubes.InletNozzleID    = 0.203        *'m';
     83exchanger.Tubes.OutletNozzleID          = 0.203         *'m';
    8484#=====================================================================
    8585#       Baffles Geometrical Parameters
    8686#=====================================================================
    87 exchanger.Lcd           = 0.0047        *'m';
    88 exchanger.Bc            = 30;
    89 exchanger.Ltd           = 0.00039  *'m';
    90 exchanger.Nb            = 6;
     87exchanger.Clearances.BaffleToShell              = 0.0047        *'m';
     88exchanger.Baffles.BaffleCut             = 30;
     89exchanger.Clearances.TubeToBaffle       = 0.00039  *'m';
     90exchanger.Baffles.NumberOfBaffles               = 6;
    9191
    9292#=====================================================================
    9393#       Fouling
    9494#=====================================================================
    95 exchanger.Rfi = 0.001*'m^2*K/kW';
    96 exchanger.Rfo = 0.001*'m^2*K/kW';
     95exchanger.Tubes.Fouling = 0.001*'m^2*K/kW';
     96exchanger.Shell.Fouling = 0.001*'m^2*K/kW';
    9797
    9898SPECIFY
    … …  
    114114#       Baffle Spacing
    115115#=====================================================================
    116         exchanger.Baffles.Ls     = 0.622  *'m';
    117         exchanger.Baffles.Lsi = 0.807  *'m';
     116        exchanger.Baffles.Central_Spacing        = 0.622  *'m';
     117        exchanger.Baffles.Inlet_Spacing= 0.807  *'m';
    118118
    119119OPTIONS
    … …  
    153153        exchanger.ShellType  = "Eshell";
    154154       
    155 exchanger.LMTDcorrection  = "Fakeri";
     155exchanger.LMTDcorrection  = "Bowmann";
    156156
    157157#   Heat Transfer Correlation
    … …  
    163163#       Shell Geometrical Parameters
    164164#=====================================================================       
    165 exchanger.Tpass                 = 2;
    166 exchanger.Dishell               = 0.75  *'m';
    167 exchanger.Lcf                   = 0.043  *'m';
    168 exchanger.Nss                   = 2;
    169 exchanger.Donozzle_Shell    = 0.1937    *'m';
    170 exchanger.Dinozzle_Shell    = 0.1937    *'m';
    171 exchanger.Honozzle_Shell    = 0.0225    *'m';
    172 exchanger.Hinozzle_Shell    = 0.02155   *'m';
     165exchanger.Tubes.Tubepasses                      = 2;
     166exchanger.Shell.ShellID                 = 0.75  *'m';
     167exchanger.Clearances.BundleToShell                      = 0.043  *'m';
     168exchanger.Clearances.SealStrip                  = 2;
     169exchanger.Shell.InletNozzleID    = 0.1937       *'m';
     170exchanger.Shell.OutletNozzleID    = 0.1937      *'m';
     171exchanger.Clearances.Honozzle_Shell    = 0.0225         *'m';
     172exchanger.Clearances.Hinozzle_Shell    = 0.02155        *'m';
    173173#=====================================================================
    174174#       Tubes Geometrical Parameters
    175175#=====================================================================
    176 exchanger.Ntt                   = 500;
     176exchanger.Tubes.NumberOfTubes                   = 500;
    177177exchanger.Pattern                       = "Triangle";
    178 exchanger.pitch                         = 0.0254        *'m';
    179 exchanger.Ltube                 = 5.5           *'m';
    180 exchanger.Ditube                = 0.013395  *'m';
    181 exchanger.Dotube                = 0.015875  *'m';
    182 exchanger.Kwall                         = 0.057         *'kW/m/K';
    183 exchanger.Donozzle_Tube     = 0.203     *'m';
    184 exchanger.Dinozzle_Tube         = 0.203         *'m';
     178exchanger.Tubes.TubePitch                       = 0.0254        *'m';
     179exchanger.Tubes.TubeLength                      = 5.5           *'m';
     180exchanger.Tubes.TubeID                  = 0.013395  *'m';
     181exchanger.Tubes.TubeOD                  = 0.015875  *'m';
     182exchanger.Tubes.Kwall                           = 0.057         *'kW/m/K';
     183exchanger.Tubes.InletNozzleID    = 0.203        *'m';
     184exchanger.Tubes.OutletNozzleID          = 0.203         *'m';
    185185#=====================================================================
    186186#       Baffles Geometrical Parameters
    187187#=====================================================================
    188 exchanger.Lcd           = 0.0047        *'m';
    189 exchanger.Bc            = 30;
    190 exchanger.Ltd           = 0.00039  *'m';
    191 exchanger.Nb            = 6;
     188exchanger.Clearances.BaffleToShell              = 0.0047        *'m';
     189exchanger.Baffles.BaffleCut             = 30;
     190exchanger.Clearances.TubeToBaffle       = 0.00039  *'m';
     191exchanger.Baffles.NumberOfBaffles               = 6;
    192192
    193193#=====================================================================
    194194#       Fouling
    195195#=====================================================================
    196 exchanger.Rfi = 0.001*'m^2*K/kW';
    197 exchanger.Rfo = 0.001*'m^2*K/kW';
     196exchanger.Tubes.Fouling = 0.001*'m^2*K/kW';
     197exchanger.Shell.Fouling = 0.001*'m^2*K/kW';
    198198
    199199SPECIFY
    … …  
    215215#       Baffle Spacing
    216216#=====================================================================
    217         exchanger.Baffles.Ls     = 0.622  *'m';
    218         exchanger.Baffles.Lsi = 0.807  *'m';
     217        exchanger.Baffles.Central_Spacing        = 0.622  *'m';
     218        exchanger.Baffles.Inlet_Spacing= 0.807  *'m';
    219219
    220220OPTIONS
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