Dynamic modelling of crude distillation unit / (Record no. 4066)

MARC details
000 -LEADER
fixed length control field 02227nam a2200253 a 4500
001 - CONTROL NUMBER
control field vtls000075780
003 - CONTROL NUMBER IDENTIFIER
control field KUKTEM
005 - DATE AND TIME OF LATEST TRANSACTION
control field 20251114204545.0
008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION
fixed length control field 131029t2013 my da f abm 000 0 eng d
020 ## - INTERNATIONAL STANDARD BOOK NUMBER
International Standard Book Number THE0004829(Local)
039 #9 - LEVEL OF BIBLIOGRAPHIC CONTROL AND CODING DETAIL [OBSOLETE]
Level of rules in bibliographic description 201905161009
Level of effort used to assign nonsubject heading access points smfh
-- 201310291457
-- nabilah
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) TP690 .T36 2013 rs Bc.
100 1# - MAIN ENTRY--PERSONAL NAME
Personal name Tan, Weng Khim
245 10 - TITLE STATEMENT
Title Dynamic modelling of crude distillation unit /
Statement of responsibility, etc. by Tan Weng Khim
260 ## - PUBLICATION, DISTRIBUTION, ETC.
Place of publication, distribution, etc. Kuantan, Pahang :
Name of publisher, distributor, etc. UMP,
Date of publication, distribution, etc. 2013
300 ## - PHYSICAL DESCRIPTION
Extent xii, 70 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 – 2013
504 ## - BIBLIOGRAPHY, ETC. NOTE
Bibliography, etc. note Bibliography : p. 63-65
520 3# - SUMMARY, ETC.
Summary, etc. There is rapid growth in the usage and demand of crude oil in various industrial fields. Thus, the price of the petrol is rising due to the stronger-than-expected demand for petroleum products. With the available information, most of the modeling models used today is only steady state models. The procedure for this work was firstly forming a mathematical model for the theoretical stage of the column. Then based on the partial equation obtained, the relationship between input variable and output variable was studied. After that, Aspen Plus simulation of CDU was run in steady state mode and the results obtained was studied. Next, a dynamic simulation of CDU in Aspen Plus Dynamic was run and the dynamic behavior of CDU model was studied based on the results obtained. Based on the result obtained from steady state simulation, it was proven that the change of energy balance of the column lead to a change in the mass balance of the column. As the conclusion the dynamic simulation results shown on all the changes of process variable with respect to time until the system stability achieved. A good dynamic model is necessary to develop a proper control strategy. Thus, this work was very helpful in understanding dynamic behaviour of CDU and used to increase the efficiency of refining process which also increases the yield of the product.
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Petroleum
650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM
Topical term or geographic name entry element Distillation, Fractional
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   TP690 .T36 2013 rs Bc. 0000074717 04/09/2019 1 04/09/2019 Final Year Report
  Not lost   Not for loan UMPLIB GAMBANG UMPLIB GAMBANG 04/09/2019   CD 7058 | TP690 .T36 2013 rs Bc. 0000074718 04/09/2019 1 04/09/2019 Final Year Report

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