AGBADAOLA ADEKUNLE GABRIEL MATRIC NO: 2003/14933EH

Similar documents
Transcription:

COMPUTER AIDEDS DESIGN AND SIMULATION OF DOUBLE EFFECT EVAPORATOR FOR CONCERTRATION OF SUCROSE SOLUTION. BY AGBADAOLA ADEKUNLE GABRIEL MATRIC NO: 2003/14933EH DEPARTMENT OF CHEMICAL ENGINEERING FEDERAL UNIVERSITY OF TECHNOLOGY, MINNA NIGER STATE, NIGERIA NOVEMBER, 2008

COMPUTER AIDED DESIGN AND SIMULATION OF DOUBLE EFFECT EVAPORATOR FOR CONCERTRATION OF SUCROSE SOLUTION. BY AGBADAOLA ADEKUNLE GABRIEL MATRIC. NO. 2003/14933EH A RESEARCH PROJECT SUBMITTED TO THE DEPARTMENT OF CHEMICAL ENGINEERING, SCHOOL 0F ENGINEERING AND ENGINEERING TECHNOLOGY, FEDERAL UNIVERSITY OF TECHNOLOGY, MINNA, NIGER STATE 11

DECLARATION I, Agbadaola Adekunle Gabriel with matriculation number 03/14933EH declare that this research project report is my original work and has not been presented elsewhere to the best of my knowledge. AGADAOLA ADEKUNLE G. DATE 111

CERTIFICATION This resarch project by Agbadaola Adekunle Gabriel has been examined and certified under the supervision ofprof.k.r onifade to be adequate in scope and quality for the partial fulfillment of the requirement for the Award of Bachelor of Engineering in chemical Engineering. ----~------------- (PROF. K.RONIFADE) PROJECT SUPERVISOR { o1 11log --------- -- --------------- DATE DR. M.O EDOGA (HOD) DATE EXTERNAL SUPERVISOR DATE IV

DEDICATION To the glory of God and to my late Father Surveyor Ayodele Agbadaola of blessed memories. v

ACKNOWLEDGEMENT I want to use this medium to thank my mother Mrs. Margaret Agbadaola. Whose contributions to my educational pursuit cannot be quantified? I will like to acknowledge the support of my supervisor, professor K.O onifade My good friends Richard Oyatekwa, Ellis Oshokha Alegieuno, Malcolm Esekhile, Nsikan Uboho lekan joks, raph banji, femi,bada bola and my younger brothers Alabi Olubumni, Oshadola Opeyemi. I seize this opportunity to show my appreciation to the entire family member of Mr. and Mrs. Ayodele Lawrence the family of dare clement and the family of Engineer TEE. for their unquantifiable contribution and assistance to the successful completion of my program. Above all I wish to express my gratitude especially to the following people My big brother Mr. omoregie and my dearly friend ogundipe olalekan bright i will not forget my sweet younger sister Tolu Agbadaola. And my sweat lovely angel kemi omoniyi. Finally, I give thanks to God for granting me all it takes for the successful completion of my program. VI

ABSTRACT This research work is concerned with the computer aided design of a double effect evaporator for the concentration f sucrose solution using HYSYS process simulator. The purpose of this work is to get sucrose solution concentration. It was found the feed enter the pump at a temperature of 25 C and the pressure of 120kPa and the feed in pumped to the first effect evaporator and heat is applied giving a top product a the top of the evaporator with temperature 110.0 c and pressure of 130.0 kpa, and the bottom product from the evaporator having a temperature of 11 O.O c and pressure of 130.0 kpa. The remaining sucrose from the first evaporator enters the second effect evaporator the vapour (top product) from the evaporator comes out at a temperature of 325.2 c and pressure of 139.0 kpa. The sucrose (the bottom product) from the evaporator comes out at temperature of325.2 c and presure of 139.0 kpa. Vll

TABLE OF CONTENTS TITLE ]>~(;E----------------------------------------------------------------------------------i-ii ])ECLE~TION-------------------------------------------------------------------------------iii CEIlTIFIC~TION-----------------------------------------------------------------------------i" ]) E]) I C~ TI 0 N -----------------------------------------------.. ----------------------------------" ~C~O~LE])(;E~EN~T-----------------------------------------------------------------"i ~]JST~CT------------------------------------------------------------------------------------"ii CH~]>TEIl ONE 1.0 INTIlO])lJCTION-------------------------------------------------------------------------1 1.1 CO~]>lJTEIl ~I])E])/ COM]>lJTEIl ~I])E]) ~~NlJF~CTlJIlEIN(;---------l 1.2 ]>1l0(;~~~IN(; L~N(;lJ~(;E-------------------------------------------------------2 1.3 ]>1l0CESS SYNTHESIS FLO~SHEET ----------------------------------------------3 1.4 SI~lJL~TION ]>~CI(j\(;E--------------------------------------------------------------4 1.5 ]>ru~~ily ]>1l0]JLE~ IN EVE~]>O~TOIl ])ESI(;N--------------------------4. CH~]>TEIl T~O 2.0 LITE~TlJllE IlEVIE~----------------------------------------------------------------5 2.1 EV ~]>O~TOIl TY]>ES ~N]) ~]>]>LIC~TION------------------------------------5 2.2 HE~T T~NSFEIl IN EV ~]>O~TOIlS---------.. ---------------------------------6 2.2.1]>ru~~IlY ]>1l0]JLE~ IN EV ~]>O~~TOIl ])ESI(;N-------------------------6 2.2.2V~]>OlJll LI~lJI]) SE]>E~IlTION---------------------------------------------------6 2.2.3SELECTION ]>1l0]JLE~--------------------------------------------------------------7 2.2.4]>1l0])lJCT ~lj~lity------------------------------------------------------------------8 2.3HE~ T T~NSFEIl COEFFI CIENT ----.. ----------------------------------------------8 2.4.1 ]JO ILIN (; ~ T SlJM~EIl(;E SlJllF ~CE-----------------------------------------1 0

2.4.2 ]{()It<:~]) <:()~"~<:1fI()~ ]J()1~1~(;---------------------------------------------13 2.5 SI~ (;~~ ~]{]{~<:1f ~" AP() RA 1f()t--------------------------------------------------14 2.6 MULI1fPL~ ~]{]{~<:1f ~" AP()RA 1f()ItS--------------------------------------------15 2. 7 ~Q UIPM~~1f ]{()It ~" AP()RA 1f()ItS----------------------------------------------16 2.7.1 ~" AP() RA 1f1t() It S ~L~<:1f1 () ~ ----------------------------------------------------16 2.7.2 ~"AP()It1fA1f()ItS WI1fH ])11tE<:1f H~A1fI~(;--------------------------------17 2.7.3 ]{()It<:~]) <:11t<:ULA 1f1 ()~ ~" AP() RA 1f1t()ItS---------------------------------18 2.7.4 ~ A 1fURAL <:11t<:ULA 1f1 ()~ ~" AP() RAIt1f()ItS------------------------------19 <:HAP1f~1t 1fHItE~ 3. 0 M~ 1fH ()])() L ()(;Y -----------------------------------------------------------------------24 3.1 SAMPL~,PIt()]JL~M-------------------------------------------------------------------24 3.1.1 <:ItEA 1f1~ (; A ]{L UI]) P A <: KA (;~-------------------------------------------------24 3.1.2S~L~<:1fI~ (; <:() MP() ~~ ~1f --------------------------------------------------------24 3.1.3PIt()<:~])UItE---------------------------------------------------------------------------24 3.1.4SIMULA 1f1 ()~ ~~"IIt()~M~~1f ---------------------------------------------------25 3.2 PIt()<:~S S ]) ~S<:ruP1f1 () ~ -------------------------------------------------------------25 <:HAP1f~1t ]{()UIt 4.0 ItESUL1f----------------------------------------------------------------------------------26 4.1 SUMMAItY ()]{ MA1f~ruAL ~ ~~~It(;Y ]JALA~<:~ A<:It()SS 1fH~ ]{IItS1f A~]) S~<:()~]) ~]{]{~<:1fS----------------------------------------26 4.2 D ISS<:U S I () ~ ()]{ ItE S UL 1fS----------------------------------------------------------30 <:HAP1f~1t ]{I"~ 5.1 <:() ~ <:L U SI () ~ S--------------------------------------------------------------------------31 5.2 1tE<:()MM~~DA1fI()~-----------------------------------------------------------------31 1tE]{~ItE~<:~-----------------------------------------------------------------------------32