Interim Presentation

[nur faiqa]

Presentation Process Flow

#	Subject	PIC	Allocated Time (minutes)
1	Introduction	Ilmi	5
2	Product Market Study	Muchapa	5
3	Plant Location	Ilmi	5
4	Process Screening	Tamil	10
5	Synthesis before Rev		6
6	Pre-treatment	Faiqa n Balqees
7	Reactor 1	Muchapa
8	Absorption	Ilmi
9	Flash distillation	Muchapa
10	Reactor 2	Tamil
11	Distillation	Zul
12	Synthesis after Revision	Muchapa	2
13	Mass Balance	Muchapa	5
14	Before HEN	Faiqa	5
15	After HEN	Balqees	5
16	Economic Potential	Zul	5
17	Conclusion	Zul
	Total		53

[TAMILARASAN MUNIANDY]

this is the old revisions

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Warm Regards

Tamilarasan Muniandy

Tel: (6017) 457 1573

Email: ara...@gmail.com

Bachelor of Engineering (Hons) Chemical
Universiti Teknologi PETRONAS
Perak Darul Ridzuan
Malaysia.

[General Grievous]

tomorrow we show rev1. Rev 3 and the Before HEN diagrams as the 3 versions.

Felisberto Muchapa
Universiti Teknologi PETRONAS
Chemical Engineering Department
H/P No:+60149048782
Proudly MY_MOZ.

[nur faiqa]

my friend said that there is case where the internal examiner said that its not practical to have heat integration with reboiler and condenser stream.

so my opinion, maybe we should avoid focusing on reboiler and condenser stream

[Balqees Zailani]

Ok, i wont go in detail each stream extracted as well as the heat exchanger.. but if khashayar sharp enough to notice that.. haha idk. help me later on :P

[nur faiqa]

before we forget much of it, maybe we should point out things that need to be improved. Anything else besides this guys?

Subject	To recheck	PIC
Heat Integration	Utilities selection	Faiqa n Balqees
Economic potential	Compressor cost calculation	Zul
PFD	Add stream to show temp change (energy balance) and reprint	Tamil

[Zul Gmie]

wah thanks... good reminder 

MUHAMMAD ZULHILMI BIN MAHARI
B.Eng.(Hons.) of Chemical.
Universiti Teknologi PETRONAS,
Bandar Seri Iskandar,
31750 Tronoh,
Perak Darul Ridzuan.