Modeling of crude distillation unit (CDU) / (Record no. 3510)

MARC details
000 -LEADER
fixed length control field 01996nam a2200241 a 4500
001 - CONTROL NUMBER
control field vtls000066679
003 - CONTROL NUMBER IDENTIFIER
control field KUKTEM
005 - DATE AND TIME OF LATEST TRANSACTION
control field 20251114204525.0
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 121121t2012 my a f m 000 0 eng d
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number THE0004235(Local)
039 #9 - LEVEL OF BIBLIOGRAPHIC CONTROL AND CODING DETAIL [OBSOLETE]
Level of rules in bibliographic description 201905152111
Level of effort used to assign nonsubject heading access points farhana
Level of effort used to assign subject headings 201211210914
Level of effort used to assign classification ida
-- 201211210900
-- ida
040 ## - CATALOGING SOURCE
Original cataloging agency UMP
090 ## - LOCALLY ASSIGNED LC-TYPE CALL NUMBER (OCLC); LOCAL CALL NUMBER (RLIN)
Classification number (OCLC) (R) ; Classification number, CALL (RLIN) (NR) TP159.D5 S24 2012 rs Bc.
100 0# - MAIN ENTRY--PERSONAL NAME
Personal name Muhammad Safwan Taharim
245 10 - TITLE STATEMENT
Title Modeling of crude distillation unit (CDU) /
Statement of responsibility, etc. Muhammad Safwan Taharim
260 ## - PUBLICATION, DISTRIBUTION, ETC.
Place of publication, distribution, etc. Kuantan, Pahang :
Name of publisher, distributor, etc. UMP,
Date of publication, distribution, etc. 2012
300 ## - PHYSICAL DESCRIPTION
Extent xv, 68 p. :
Other physical details ill. ;
Dimensions 30 cm. +
Accompanying material 1 CD-ROM
502 ## - DISSERTATION NOTE
Dissertation note Project paper (Bachelor of Chemical Engineering) -- Universiti Malaysia Pahang - 2012
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc. note Bibliography : p. 65-66
520 3# - SUMMARY, ETC.
Summary, etc. Crude distillation unit (CDU) is a complex process in the field of separation which produces wide range of products at different stages under different conditions. The products of the process were heavy naphtha, kerosene, diesel, atmospheric gas oil and reduced crude. However, the dynamic and multivariable nature with strict quality was makes it difficult to operate the process units steadily. More, the dynamics of CDU are complex due to its complex vapor-liquid equilibrium relationships. It is necessary to predict the new steady-state values for any changes in the operating conditions. This research aims to develop a steady-state model for CDU based on the fundamental modeling approach. The simulation was carried out in Aspen Plus. The effect of feed flow rate, feed composition and steam flow rate on product compositions and tray temperatures were studied. The results were compared with the data available in the literature and the accuracy of the model has been proved.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Distillation apparatus
General subdivision Design and construction
Holdings
Withdrawn status Lost status Damaged status Not for loan Home library Current library Date acquired Total checkouts Full call number Barcode Date last seen Copy number Price effective from Koha item type
  Not lost   Not for loan UMPLIB GAMBANG UMPLIB GAMBANG 04/09/2019   TP159.D5 S24 2012 rs Bc. 0000068260 04/09/2019 1 04/09/2019 Final Year Report
  Not lost   Not for loan UMPLIB GAMBANG UMPLIB GAMBANG 04/09/2019   CD 6422 | TP159.D5 S24 2012 rs Bc. 0000068261 04/09/2019 1 04/09/2019 Final Year Report

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