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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

DF10"Prblm: Assume se yu de du distileshn na 200 psia n 200\deg F, we de rilizt di...
flw separeshn, inklud fd, distil\epsi t,\epsi n btm kmpnt f fl r\epsi t in kmol/hr:
Komponent Distillat (kmol/hr) Btm dn (kmol/hr).
Mitan 1000. Di wan dn we de wok
Itan 2000100. Di wan dn we de wok
Propan 2002000. Di wan dn we de wok
n-Butan 02500. Di wan dn we de wok
n-Pntan 0500
n-Hksan 0500
(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=1.44. Kalkul di minim riflks r\epsi shn.
(f) Assuming se yu de rn di r\epsi fluks na 50% oba di minimm, gi di aktual r\epsi fluks r\epsi 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 0.300 m/s, wan vapour density we na 30 kg/m3,.
n wan avrej vaypa mlikul wet we na 30.6. Kalkul di aktif trey eria.
(i) Assume wan daunkam eria we na 15% pan di trey eria, kl di klm dayamita.
(j) Assuming a trey spacing of 18 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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