LAB 4 ASPEN

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    UNIVERSITI TEKNOLOGI MARA

    FAKULTI KEJURUTERAAN KIMIA

    CHEMICAL ENGINEERING LABORATORY IV

    (CPE613)

    No. Tit! Ao"#t!$ M#%&' () M#%&'

    1 Procedure 10

    2 Process Flow Diagram (PFD) 20

    3 Workbook/Stream Summary 30

    4 uestio!s " Discussio!s 40

    TOTAL MARKS 1

    R!*#%&'+

    C,!"&!$ -+ R!",!"&!$ -+

    ############################## ###############################

    ( ) ( )/#t!+ /#t!+

    NAME : ADDISON JUTTIE ANAK BANGGASTUDENT I.D : 2014259348

    EXPERIMENT : PRODUCTION OF ACETIC ANHDRIDE

    DATE PERFORMED : 22 OCTOBER 2015

    SEMESTER : 5

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    PROCE/URE

    1$ Firstly% t&e 'se! lus user i!terace is oe!ed a!d t&e reacta!ts a!d roducts are

    selected$

    Figure 1* Selectio! o como!e!ts

    2$ +e,t% t&e tye o reactio! is e!tered by usi!g Wilso! roerty ackage$ -&e

    i!ormatio! regardi!g t&e ki!etics (Forward* ' . $2 , 1014% . 2$ , 10 k/kmol%

    eerse* ' . 0% . 0) stoic&iometry coeicie!ts a!d reactio! &ase are also i!serted$

    Figure 2* eactio! ki!etic tab

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    3$ -&e!% t&e reactio! set is c&ose!$

    Figure 3* 5&oosi!g reactio! set

    4$ +e,t% t&e simulatio! is started$

    $ 6aterial stream 1 is t&e! added a!d t&e i!ormatio! is added i!to t&e stream suc& as

    temerature (780o5)% ressure (10 kPa)% mass low rate (000 kg/&) are e!tered$

    Figure 4* 5o!ditio!s o material stream 1

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    8$ +e,t% t&e comositio! o t&e eed stream is added wit& t&e eed o!ly &ai!g aceto!e$

    Figure * 5omositio! o material stream 1

    7$ +e,t% a lug low reactor is added$ 6aterial stream 1 is added to t&e reactor as a!

    i!ut a!d t&e outut is !amed as material stream 2$

    Figure 8* 5o!!ectio!s o lug low reactor 

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    $ +e,t% t&e ressure dro (0 kPa) is i!serted i!to t&e arameters o t&e lug low

    reactor$

    Figure 7* Parameters o lug low reactor 

    9$ :! t&e rati!g tab% t&e dime!sio!s o t&e reactor is added% wit& le!gt& 30m a!d i!!er 

    diameter 0$m$ -&e le!gt& was ad;usted to ac&iee a desired co!ersio! o 20

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    10$ 'ter a ew trial a!d errors% t&e co!ersio! was obtai!ed$

    Figure 9* 5o!ersio! results o lug low reactor 

    Figure 10* 5o!ditio!s o material stream 2

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    Figure 11* 5omositio! o material stream 2

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    PROCESS FLO0 /IAGRAM

    Figure 12* Process low diagram o roductio! o acetic a!&ydride

    -&e lug low reactor model is a model used to describe c&emical reactio!s i!

    co!ti!uous% lowi!g systems o cyli!drical geometry$ -&e PF model is used to redict

    t&e be&aiour o c&emical reactors o suc& desig!% so t&at key reactor ariables% suc& as

    t&e dime!sio!s o t&e reactor% ca! be estimated$ >! t&is lab e,erime!t% o!e o t&e routes

    to roduce acetic a!&ydride is by t&e aour &ase cracki!g o aceto!e to roduce kete!e

    a!d met&a!e by usi!g a PF$ So% i! t&e e,erime!t% t&e eed i!let is o!ly aceto!e$ -&e

    outlet o t&e reactor is &ai!g t&e roducts w&ic& are kete!e a!d met&a!e$ For t&is

    e,erime!t% it is set wit& a set#oi!t o ac&iei!g a co!ersio! o 20< o!ly% t&us t&e

    reactor is desig!ed wit& diere!t le!gt& a!d i!ter!al diameter to ac&iee t&e re?uired

    co!ersio!% wit& i!itial arameters o t&e reactor already gie!$ ' PF is robably c&ose!

    due to its ability to &ae a better co!ersio! comared to ot&er reactors suc& as a

    co!ti!uous stirred ta!k reactor% 5S-$

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    0ORKBOOK 

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    /ISCUSSION

    -&e ob;ecties o t&e e,erime!t o roductio! o acetic a!&ydride is to i!stall a!d

    co!erge a lug low reactor a!d simulate a rocess i!oli!g reactio!$ >! t&is

    e,erime!t% kete!e a!d met&a!e is roduced by aour &ase cracki!g o aceto!e% wit&

    t&e gie! co!ditio!s$ 's taug&t i! t&e course 5&emical eactio!s% t&e olume o a lug

    low reactor is V  PFR=∫0

     X  F 

     A0

    −r A

    dX  $ From &ere% it ca! be said t&at t&e olume o reactor is

    dee!de!t o! t&e low rate a!d rate o reactio!$ -&e low rate ca! be said is aected by

    t&e desig! o t&e reactor% w&ic& are t&e dime!sio!s o t&e reactor$ >! t&is e,erime!t% t&e

    aim is to determi!e t&e relatio!s&i betwee! t&e dime!sio!s o reactor a!d t&e

    co!ersio!$ For t&is% t&e co!ersio! is set as t&e reso!di!g ariable a!d t&e ma!iulated

    ariables are eit&er reactor le!gt& or i!ter!al diameter o t&e reactor$ -&e c&ose!

    ma!iulated ariable or t&is e,erime!t is le!gt& o reactor wit& t&e i!itial le!gt& gie!

    as 30 meters$ >t is t&e! reduced as t&e co!ersio! at 30 meters is 24$17

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