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DF 1 0 Pr bl m: Assume se yu de du distilesh n na 2 0 0 psia n 2 0 0 deg
DFPrblm: Assume se yu de du distileshn na psia n deg F we de rilizt di
flw separeshn inklud fd distilepsi tepsi n btm kmpnt f fl repsi t in kmolhr:
Komponent Distillat kmolhr Btm dn kmolhr
Mitan Di wan dn we de wok
Itan Di wan dn we de wok
Propan Di wan dn we de wok
nButan Di wan dn we de wok
nPntan
nHksan
a Gi di separeshn we de p we dn kin klas di bst as di layt ki n we na di ebi
ki
b Ditarmin di K valyu f dn kmpnnt ya na dn kndishn ya yuz di DePriester cht
bin gi
c Ditarmin di rilitiv volatility valyu dn bays pan di K valyu dn frm b
d Ditarmin di minimum nmba f di stej f dis separeshn
e Yu kleja dn de du di ndawd analisis, asum se na styuret likwid fid, n
ajst wan valyu we na Q Kalkul di minim riflks repsi shn
f Assuming se yu de rn di repsi fluks na oba di minimm gi di aktual repsi fluks repsi sh
g Kalkul di tiori nmba f di stej dn yuz di Eduljee iqwj
h Assume se yu de rn wan supafishal velositi we na ms wan vapour density we na kgm
n wan avrej vaypa mlikul wet we na Kalkul di aktif trey eria.
i Assume wan daunkam eria we na pan di trey eria, kl di klm dayamita.
j Assuming a trey spacing of inch, negligible trey tiknes n neglektin ayt biks f
di riboyla en di kondensa, aw bohku ayt nid fo di trey dem na dis kolm?
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