User`s Manual - Manual del Usuario
Contents
1. of B in still pot Accumulated mass of A distilled X axis horizontal Ef Total mass distilled Total moles distilled Total mass distilled Total moles distilled Total mass in still pot Total moles in still pot MAd Accumulated mass of A distilled tMd Total mass distilled Fig 3 Main window X vs Progress graph 29 Number of the current distillation stage Allows us to select the current distillation stage 30 Y axis parameters Allows us to select one of the following Y axis parameters Accumulated mass of A distilled Mass of A in still pot Accumulated mole fraction of A distilled Mole fraction of A in still pot Mass of B in still pot Mole fraction of B in still pot Accumulated mass of B distilled Accumulated mole fraction of B distilled Mass of A in still pot Mass of B in still pot Moles of A in still pot Moles of B in still pot Accumulated mass of A distilled Accumulated mass of B distilled Accumulated moles of A distilled Accumulated moles of B distilled Mole fraction of A in distilled vapor 10 31 X axis parameters Allows us to select one of the following X axis parameters Total mass distilled Total moles distilled Total mass distilled Total moles distilled Total mass in still pot Total moles in still pot 32 Copy button Copy the graph to the clipboard 33 Scale of values of X axis Shows the scale of values of X axis 34 X axis tit2. 427 Mass distilled progress 35 Allows us to open a Binary Distillation File bdf Save mm gt Saves the current distillation data as a Binary Distillation File bdf Save as 21 16 18 15 13 14 12 Asks us for a filename and saves the current data as a Binary Distillation File bdf Print Open the Print window to print one of the following items when it s visible VLE graph Vapor Liquid Equilibrium graph X vs Progress graph Exit Close the application Edit menu Copy Copies either ELV graph or X vs Progress graph or X vs Progress table to the clipboard View menu Main Shows the Main panel ELV graph Shows the VLE graph Vapor Liquid Equilibrium graph X vs Progress graph Shows the X vs Progress graph X parameter vs distillation progress X vs Progress table Shows the X vs Progress table X parameter vs distillation progress Liquid color Allows us to select the color of the simulated liquid Help menu User s manual PDF document Shows this manual Application registration Shows the registration form window to register the application Disabled functions in the unregistered version Shows the list of disabled functions when the application is not registered Home page www vaxasoftware com Connects to VaxaSoftware home page An active Internet connection and a browser are required About Shows the Splash wind
3. E window 4 Press Open button to open the table Ethanol water vie that is in Example subfolder located in the directory where the application was installed 5 Press OK button to close the window and return to main window 6 In the main window we enter the following data mass of A 15 Initial mass of binary mixture 2500g Number of stages 2 7 We enter the percentage progress of each stage of distillate mass Stage 1 40 Stage 2 60 8 Finally we get the following results for the second stage in the distillate flask Total mass 600 g A component Mass 358 48 g mass 59 75 Moles 7 7811 mol Mole fraction of A Xa 0 3672 15 Main window F5 Calculate Ctrl O Open Ctrl S Save Ctrl P Print Ctrl F4 Exit Alt F4 Exit Ctrl C Copy Page Up Show the next distillation stage Page Down Show the previous distillation stage F1 Help Show User s Manual PDF document Mayus F1 About 16 Description License Unregistered version restrictions Decimal separator Thousands separator Binary mixture distillation file extension VLE Vapor Liquid Equilibrium data input Azeotrope support Maximum number of consecutive stages Maximum number of parameters in the X vs Progress table Number of X axis parameters for the X vs Progress graph Number of Y axis parameters for the X vs Progress graph Number of col
4. User s Manual SDEN Version 1 9 0 Chemical software Single multi stage distillation simulator Windows XP Windows Vista Windows 7 Windows 8 Windows 10 WALA SOFTWARE Reference SDEN www vaxasoftware com ENGLISH neten 2MD222222 0 2 __ w22m57 xymJyggg PPm D rrperm m mm 3 TEMS EE 3 Main window Main TEE 4 Main window TE E EE 8 Main window X vs WE E 10 Main window X vs Progress table EE kk kk kk k k ke 12 Windows VLE Vapor Liquid Equilibrium table uEE kek Re 14 lt 2 gg E 15 lie Gerd 16 SEENEN 17 Registered HESE eschen 18 SDEN is a single multi stage binary distillation simulator for Windows using Rayleigh equation SDEN can simulate distillations from 1 to 6 consecutive stages This manual isn t about single multi stage binary distillation theories Please read this manual carefully in order to learn all the capabilities of the application In no event shall VaxaSoftware be liable to anyone for direct indirect special collateral incidental or consequential damages by the use or impossibility of use of the software nor by the effects in the operation of other software or the operating system Before the installation we recommended to make backup of your data and create a restoration point You will be able freely to evaluate the software during the time that considers necessary Passed this period of evaluation you would have or to re
5. ble X Mole fraction of most volatile component in liquid phase Y Mole fraction of most volatile component in vapor phase 0 0 0952381 0 181818 0 26087 0 333333 0 4 0 461538 0 518519 0 571429 0 62069 0 666667 0 709677 Fig 5 Window VLE Vapor Liquid Equilibrium table 42 Data table Allows us to enter the values of X and Y of a VLE Vapor Liquid Equilibrium X is the mole fraction of most volatile component A in liquid phase Y is the mole fraction of most volatile component A in equilibrium in vapor phase 43 Buttons Ok button Checks the table closes the dialog window and returns to the main window The edited data table will be used Cancel button Closes the window The edited data is not used Open button Allows us to open a file of table vle or import a Binary Distillation File BDF Save as button Asks us for a filename and saves the current table as a file vle Clear button Clears the table 14 We want to make a double distillation of 2500 g of ethanol water solution of 15 ethanol by mass In the first stage we distillate 1000 g 40 of the initial solution In the second stage we distillate 600 g 60 Find out the concentration of ethanol in the second distillate solution Procedure 1 Set the number of distillation stages as 2 2 Select Table in Vapor Liquid Equilibrium section 3 Press Edit table button to open the VL
6. distilled tMd Total mass distilled g tMd MAd XAd tMd 0 0 0 0 5 57 448 0 61427 0 25 10 56 837 0 60835 0 5 LS 56 189 0 60204 0 75 20 55 505 0 59538 3 KA 54 783 0 58833 2 25 30 54 021 0 58087 1 5 35 53 215 0 57296 1 2 40 LF gees tok 0 56454 2 4s 51 451 0 55557 2 25 50 50 483 0 54599 2 5 55 49 449 0 53572 2 19 60 48 342 0 52469 3 65 47 155 0 5128 3 525 70 45 878 0 49998 E 15 44 503 0 4861 3 735 8 43 022 0 47109 4 41 431 0 45487 4 25 a Fig 4 Main window X vs Progress table Accumulated mole fraction of A distilled Mole fraction of A in still pot Total mass distilled Total moles distilled Mass of B in still pot Mole fraction of B in still pot Accumulated mass of B distilled Accumulated mole fraction of B distilled 38 Number of the current distillation stage Allows us to select the current distillation stage Allows us to select one of the following parameters Total mass in still pot Total moles in still pot Mass of A in still pot Mass of B in still pot Moles of A in still pot Moles of B in still pot Accumulated mass of A distilled Accumulated mass of B distilled Accumulated moles of A distilled Accumulated moles of B distilled Mole fraction of A in distilled vapor 12 40 Numbers of rows Allows us to select the numbers of rows in the table 41 Copy button Copy the table to the clipboard 42 Table Shows us the table 13 Ed vLE Vapor Liquid Equilibrium ta
7. e can cause the VaxaSoftware s software or third party software may not work correctly VaxaSoftware will try to resolve these conflicts in a reasonable manner despite its satisfactory resolution is not guaranteed Design products specifications and prices are for information purposes only VaxaSoftware reserves the right to change or modify design products specifications and prices at any time without prior notice 10 11 19 ZS aso are gle ge d ato ato File Edit View Help VLE graph X v progress graph A Most volatile component Name Molar mass benzene 78 1121 g mol B Less volatile component Name Molar mass toluene 92 14 g mol Initial concentration of A Mole fraction Xo mass ofA Total mass 3 25 g 0 4 36 109 Sr A component 0 8742 g 26 9 o 0 011192 mol Vapor liquid equilibrium Be Relative volatility alpha B component SES Relative volatility 2 3758 g 73 1 VLE Table 0 025785 mol Xb 0 6973 Initial mass of binary mixture g Oky Ooz Om Number of consecutive stages of distillation Gi O02 O03 Ou O5 O86 Fig 1 Main window Main panel 1 Menu bar It contains the menus File Edit View and Help File menu Calculate Calculates output values from input values Open 17 20 X vs progress table Stage 1 Total mass 1 75g A component 0 93125 g 53 21 0 011922 mal Xa 0 573 B component 0 81875 g 46 79 8 8859E 3 mol Xb 0
8. f A Mole fraction Xo mass of A 04 36 109 DI Vapor liquid equilibrium Relative volatility alpha 2 45 Relative volatility OVLE Table SSS SS SSS Initial mass of binary mixture 5 Ga Ok Ox Ob Number of consecutive stages of distillation One e 2 OS O4n Te fe Calculate Clears X Mole fraction of benzene in liquid phase 0 6 0 7 0 8 0 9 Fig 2 Main window VLE graph 22 Scale of values of X axis Shows the scale of values of X axis 23 X axis title Shows the X axis title 24 Scale of values of Y axis Shows the scale of values of Y axis 25 Y axis title Shows the Y axis title 26 Mouse coordinates Shows x y coordinates of the mouse 27 y x line Shows the y x line 28 VLE curve Vapor liquid equilibrium curve Shows the VLE Vapor Liquid Equilibrium curve We can modify the curve with the mouse when using constant relative volatility The relative volatility is changed while we move the curve If we use a table of VLE we can double click on the curve to edit the VLE table Y axis vertical 1 Mass of A in still pot Accumulated mole fraction of A distilled O Mole fraction of A in still pot Mass of B in still pot O Mole fraction of B in still pot Accumulated mass of B distilled O Accumulated mole fraction of B distilled Mass of A in still pot Mass of B in still pot Moles of A in still pot O Moles
9. gister it or uninstall it To register the software please see the option REGISTER APPLICATION in the help menu of the software After paying the registry fee you will receive by email the REGISTRATION KEY of the software Once registered the software it will be able to use the options that were disabled until that moment The REGISTRATION KEY is UNIQUE for EACH COMPUTER You cannot use the same REGISTRATION KEY for multiple computers You can freely distribute unaltered copies of the installation system of the software to other users You cannot decompile the software nor use no type of reverse engineer for its analysis or modification You cannot use part or the totality of the software to create a new software COOKIES VaxaSoftware only uses cookies during the registration process If you want to register the software without using cookies please contact us at info vaxasoftware com Conflicts of shared files VaxaSoftware assumes no liability for conflicts due to the incompatibility of shared files dll ocx and other files VaxaSoftware s software use shared files dll ocx and other files It is possible that the shared file already exists and whether or not previously replaced by a different version during the installation of the VaxaSoftware s software This can cause the installed software may not work and or a third party software that shares the same file does not Also the installation of a third party softwar
10. le Shows the X axis title 35 Scale of values of Y axis Shows the scale of values of Y axis 36 Y axis title Shows the Y axis title 37 Curve Shows the curve of Y axis parameter vs X axis parameter 11 Zi axaSo a g age d File Edit View Help Main VLE graph 38 Number of the stage 1 Select items M Total mass distilled O Total moles distilled 39 v Accumulated mass of A distilled Mass of A in still pot V Accumulated mole fraction of A distilled C Mole fraction of A in still pot O Total moles distilled O Mass of B in still pot Mole fraction of B in still pot C Accumulated mass of B distilled Accumulated mole fraction of B distilled C Total mass in still pot Total moles in still pot DMass of A in still pot O Mass of B in still pot U Moles of A in still pot 1 Moles of B in still pot C Accumulated mass of A distilled P Number of rows ball em Oon O20 O50 100 200 41 EE El ss 39 Parameters Total mass distilled Total moles distilled Accumulated mass of A distilled Mass of A in still pot 42 X vs progress graph Distillation of binary mixture of benzene A and toluene B i Initial mass of mixture 5 g Molar mass of benzene A 78 142 g mol Molar mass of toluene B 92 14 g mol Number of the current stage of djstillation i 1 tMd Total mass distilled MAd Accumulated mass of A distilled XAd Accumulated mole fraction of A
11. ors for the liquid simulation SDEN is a single multi stage distillation simulator for Windows using Rayleigh equation Trialware Initial mole fraction of A is locked Point or comma You may use spaces to separate the thousands However the output results are displayed without a separator BDF Relative volatility Table of VLE or files vle bdf Yes 6 23 parameters 17 parameters 6 parameters 5 colors 17 VaxaSoftware and VaxaSoftware logo are trademarks of VaxaSoftware Microsoft Windows Windows XP Windows Vista Windows 7 Windows 8 Windows 10 and logos are registered trademarks or trademarks of Microsoft Corporation in the United States of America and or other countries Adobe Adobe logo PDF and Reader are registered trademarks or trademarks of Adobe Systems Incorporated in the United States of America and or other countries PayPal and PayPal logo are registered trademarks or trademarks of PayPal Inc and or eBay Inc in the United States of America and or other countries YouTube and YouTube logo are registered trademarks or trademarks of YouTube LLC and or Google Inc in the United States of America and or other countries Google and Google logo are registered trademarks or trademarks of Google Inc in the United States of America and or other countries Visa and Visa logo are registered trademarks or trademarks of Visa Inc in the United States of America and or other countrie
12. ow with the version and description of the application 2 Tab bar It contains the following tabs Main tab Shows the Main panel ELV graph tab Shows the VLE graph Vapor Liquid Equilibrium graph X vs Progress graph tab Shows the X vs Progress graph X parameter vs distillation progress X vs Progress table tab Shows the X vs Progress table X parameter vs distillation progress 3 Name and molar mass of the most volatile component A Allows us to enter the name and the molar mass of the most volatile component of the binary mixture The most volatile component is denoted as A 4 Name and molar mass of the less volatile component B Allows us to enter the name and the molar mass of the less volatile component of the binary mixture The less volatile component is denoted as B 5 Initial composition of A component most volatile component Allows us to enter the initial mole fraction or initial percentage by mass of A component Note 1 Decimal separator We can use either point or comma as decimal separator Note 2 Scientific notation The scientific notation is used to show very big or very small numbers A scientific notation number has a mantissa and a power of 10 To enter a scientific notation number we use letter E to input the exponent of 10 Examples 5 67 x 10 isenteredas 5 67 E 89 1 23 x 10 isenteredas 1 23 E 34 6 Relative volatility Allows
13. s Amex American Express Amex logo and American Express logo are registered trademarks or trademarks of American Express Company in the United States of America and or other countries MasterCard and MasterCard logo are registered trademarks or trademarks of MasterCard Incorporated and or MasterCard Worldwide in the United States of America and or other countries All the other product names company names or logos on this site are either trademarks or registered trademarks of their respective owners 18
14. t 18 Distillate flask Shows us a simulation of liquid in the distillate flask 19 Information about liquid in the still pot Shows us the following data about the liquid in the still pot Total mass Mass of most volatile component A Percentage by mass of A Moles of A Mole fraction of A Mass of less volatile component B Percentage by mass of B Moles of B Mole fraction of B 20 Information about liquid in the distillate flask Shows us the following data about the liquid in the distillate flask Total mass Mass of most volatile component A Percentage by mass of A Moles of A Mole fraction of A Mass of less volatile component B Percentage by mass of B Moles of B Mole fraction of B 21 Window control buttons These are the classic buttons of the windows of MS Windows Minimize button Minimizes the application to an icon on the desktop Maximize Restore button Maximizes restores the application s window size Close button Closes the application Also we can press Alt F4 keys on our keyboard E VaxaSoftware Single Multi stage distillation si nulator DER File Edit View Help Main VLE gre a vs progress graph X vs progress tabje A Most volatile component x 0 3073 y 0 6126 4 Name Molar mass Y Mole fraction of benzene in vapor phase benzene 78 1121 B Less volatile component Name Molar mass toluene 92 14 Initial concentration o
15. us to enter the relative volatility o alpha 7 Vapor liquid equilibrium Allows us to select the following method for vapor liquid equilibrium VLE Relative volatility Use this option if the vapor liquid equilibrium has a constant relative volatility Table Use this option if the vapor liquid equilibrium has a variable relative volatility and or there is azeotrope Click the Edit table button to edit the Vapor Liquid Equilibrium table 8 Initial mass of binary mixture Allows us to enter the mass of binary mixture for the first distillation stage We can select one of the following mass units g gram kg kilogram oz ounce Ib pound 9 Number of consecutive stages of distillation Allows us to select the number of stages of distillation We can select between 1 and 6 stages 10 Calculate button Calculates output values from input values 11 Clear button Clears all the input output values 12 13 Scroll buttons Allows us to select each stage of distillation 14 Percentage of distillation progress scroll bar Allows us to set the percentage of progress for the current stage of distillation 15 Percentage of distillation progress textbox Shows us the percentage of progress for the current stage of distillation and allows us to set it 16 Number of the current distillation stage Shows us the number of the current distillation stage 17 Still pot Shows us a simulation of liquid in the still po
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