Penguapan Pengembunan 5 2

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    Penguapan-pengembunan

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    Kesetimbangan materi

    • Komposisi ---------- tekanan parsial

    • Diketahui tititk embun air dalam gas Tekanan parsial uap air

    dalam gas

    • Gas jenuh didinginkan pada tekanan tetap, fraksi mol uap air dan

    gas tetap konstan sampai tercapai titik embun, pada pendinginan

    selanjutnya semakin banyak air yang mengembun. Pada saatpendinginan dihentikan , gas tersebut masih jenuh dengan titik

    embunnya yang baru 

    P!G"#!G

    $D%"% &%'%(

    K%)$ K"#!G

    $D%"% P*+&%&

    K%)$ &%'%(

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    #nput output

    • +assain . +olfraksiin  %  +assaout . +olfraksiout  % 

    • +assain . Pi/P in  %  +assaout . Pi/P out  %

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    0ontoh-1

    •  %ir saturated 2ith 2ater 3apor at 4567 and 89:.5 mm (gabs. is passed through an air compressor and thenstored in a tank at ;:.5 psig and 4567.

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    Step 5 'e3eral basis can be considered> 7 155 lb mol, P 155 lb mol,

    < 155 lb mol, 7 89: lb mol, and so on, but 2e 2ill take

    a tie component as a con3enient basis

      &asis> 7 1.55 lb mol

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    0ontoh-;

    • Toluene is e3aporated into dry air. The

    resulting mi?ture at 9560 and a pressure

    of 151.@kPa has a percentage saturation

    of :5A. #t is desired to condense 45A of

    the toluene in the mi?ture by a process ofcooling and compressing. #f the

    temperature is reduced to :60, determine

    the pressure to 2hich gas must becompressed.

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    0ontoh-@

    •  % constant-3olume 3essel contains dry air atBB67 and ;1.; psia. Cne pound of liuid 2ateris introduced into the 3essel. The 3essel isthen heated to a constant temperature of14567. %fter euilibrium is reached, the

    pressure in the 3essel is @1.5 psia. The 3aporpressure of 2ater at 14567 is 8.:1 psia.• a. Did all of the 2ater e3aporate=• b. 0ompute the 3olume of the 3essel in cubic

    feet.• c. 0ompute the humidity of the air in the3essel at the final conditions in pounds of2ater per pound of air.

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    0ontoh-9

    •  % silica gel drier remo3es 1555 kg of 2ater

    per hour. %ir is supplied at a temperature

    of ::60 and a de2 point of ;B.:60. The air

    lea3es the drier at a temperature of @;60

    and a de2 point of 8.;60. The pressure in

    the system is constant at 155.5 kPa.

    0alculate the 3olume of the 2et air at theinitial conditions 2hich is supplied per

    hour.

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    ?ercise

      % 1555 kg batch of a pharmaceutical

    po2der containing : A by 2t 2ater is

    dried in a double cone drier. %fter drying

    E5 A of the 2ater has been remo3ed.0alculate the final batch composition and

    the 2eight of 2ater remo3ed.