MARC details
| 000 -LEADER |
|---|
| fixed length control field |
02423nam a2200241 a 4500 |
| 001 - CONTROL NUMBER |
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| control field |
vtls000031308 |
| 003 - CONTROL NUMBER IDENTIFIER |
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| control field |
KUKTEM |
| 005 - DATE AND TIME OF LATEST TRANSACTION |
|---|
| control field |
20251114204412.0 |
| 008 - FIXED-LENGTH DATA ELEMENTS--GENERAL INFORMATION |
|---|
| fixed length control field |
080828t2008 my a f m 000 0 eng|d |
| 020 ## - INTERNATIONAL STANDARD BOOK NUMBER |
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| International Standard Book Number |
THE0003932(Local) |
| 039 #9 - LEVEL OF BIBLIOGRAPHIC CONTROL AND CODING DETAIL [OBSOLETE] |
|---|
| Level of rules in bibliographic description |
201905141027 |
| Level of effort used to assign nonsubject heading access points |
fauzi |
| Level of effort used to assign subject headings |
201107132226 |
| Level of effort used to assign classification |
VLOAD |
| Level of effort used to assign subject headings |
200908141514 |
| Level of effort used to assign classification |
VLOAD |
| Level of effort used to assign subject headings |
200908141444 |
| Level of effort used to assign classification |
VLOAD |
| -- |
200808281617 |
| -- |
ida84 |
| 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) |
TP156.D5 U54 2008 rs Thesis |
| 100 0# - MAIN ENTRY--PERSONAL NAME |
|---|
| Personal name |
Ungku Emmy Rina Ungku Ali |
| 245 10 - TITLE STATEMENT |
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| Title |
Simulationof salt-added batch distillation using superpro simulator / |
| Statement of responsibility, etc. |
Ungku Emmy Rina Ungku Ali |
| 246 3# - VARYING FORM OF TITLE |
|---|
| Title proper/short title |
Simulationof salt-added batch distillation using superpro simulator |
| Medium |
[electronic resource] |
| 260 ## - PUBLICATION, DISTRIBUTION, ETC. |
|---|
| Place of publication, distribution, etc. |
Kuantan, Pahang : |
| Name of publisher, distributor, etc. |
UMP, |
| Date of publication, distribution, etc. |
2008 |
| 300 ## - PHYSICAL DESCRIPTION |
|---|
| Extent |
64 p. : |
| Other physical details |
ill. (some col.) ; |
| Dimensions |
30 cm. + |
| Accompanying material |
1 computer disc |
| 502 ## - DISSERTATION NOTE |
|---|
| Dissertation note |
Project paper (Bachelor of Chemical Engineering) --- Universiti Malaysia Pahang - 2008 |
| 520 3# - SUMMARY, ETC. |
|---|
| Summary, etc. |
Batch distillation has received renewed interest in world wide market for small volume, high value, and specialty chemicals has increased. While Batch Distillation is more flexible than continuous distillation because the same equipment can be used for several product and operating conditions, Batch Distillation can be less flexible when azeotropes are present in the mixture to be separated. Azeotropes can form Batch Distillation regions where the types of feasible separations can be more limited than in continuous distillation. The problem of azeotropic mixture by-products which is isopropanol-water has been studied quite extensively. The technique used in breaking azeotropes that of extractive distillation, in which one feeds a heavy component, called an entrainer, close to the column. SuperPro simulator was used to study the performance of simulation separation an azeotrope mixture, isopropanol-water. In this study, Calcium nitrate, Ca(N03)2 has been used as an entrainer. This component changes the relative volatilities of the azeotrope-forming species and pulls some of the components down the column that normally show up in the distillate. In order to separate azeotropic mixtures in general, a simulation of Salt-Added Batch Distillation via SuperPro simulator has been simulated to determine the concentration of salt that are need to break down the azeotrope point. -Author |
| 650 #0 - SUBJECT ADDED ENTRY--TOPICAL TERM |
|---|
| Topical term or geographic name entry element |
Distillation |