SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP

Formaldehyde is the most im/wrtam derivative of methanol. This compound has become one cf the world's most important industrial and research chemicals. Its principal use today is in the production q f thermosetting resins by condensation with urea, phenol or melamine. Industrially, the oxidatio...

Full description

Saved in:
Bibliographic Details
Main Author: Misran, Erni
Format: Theses
Language:Indonesia
Online Access:https://digilib.itb.ac.id/gdl/view/3036
Tags: Add Tag
No Tags, Be the first to tag this record!
Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:3036
spelling id-itb.:30362005-10-11T13:01:24ZSIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP Misran, Erni Indonesia Theses INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/3036 Formaldehyde is the most im/wrtam derivative of methanol. This compound has become one cf the world's most important industrial and research chemicals. Its principal use today is in the production q f thermosetting resins by condensation with urea, phenol or melamine. Industrially, the oxidation process based on iron molvhdate catalysts has an effective importance for formaldehyde production. from methanol due to its improved activity, selectivity and resistance to poisoning. In indu.sirial application. oxidation reaction of methanol takes place in a nuultituhe fixed-bed reac or. The gas reaction takes place exothermically nosing iron molybdate catalyst in the fixed-bed. In this research, the reaction ?rill he observed in a system that is steady state, at a nor isothermal and non-adiabatic single tube fixed--bed reactor. The .simulation 1.s done by means of Ai 0-dimensional fixed-bed reactor model derived from mass and energv balance. The model is solved numerically fusing a semidicreliration method in MA7LAIi language. The result of computation shows a good agreement when it is verified with experimental data of l'anthe/. The variables that are used, namelt'.feed temperature (To). wall temperature (Th), methanol composition in the feed (Co). and, feed mass flo%vrate (m) give a significant effect to the distribution of concentration, temperature, pressure, and superficial velocity. 77w higher the To, 7µr. and Co, the higher the hot spot temperature achieved and its position is shifted to the entrance of the reactor. At higher Tw, the shift is not signniftcant. The reverse thing does happen at the higher feed mass flowrate (m). The outlet temperature increases at higher Tw and Co. but decreases at higher To and m. At higher Co the methanol conversion increases. The pressure drop (OP) is more it fluenced by Co and m: whereas the superficial velocity by To and m text
institution Institut Teknologi Bandung
building Institut Teknologi Bandung Library
continent Asia
country Indonesia
Indonesia
content_provider Institut Teknologi Bandung
collection Digital ITB
language Indonesia
description Formaldehyde is the most im/wrtam derivative of methanol. This compound has become one cf the world's most important industrial and research chemicals. Its principal use today is in the production q f thermosetting resins by condensation with urea, phenol or melamine. Industrially, the oxidation process based on iron molvhdate catalysts has an effective importance for formaldehyde production. from methanol due to its improved activity, selectivity and resistance to poisoning. In indu.sirial application. oxidation reaction of methanol takes place in a nuultituhe fixed-bed reac or. The gas reaction takes place exothermically nosing iron molybdate catalyst in the fixed-bed. In this research, the reaction ?rill he observed in a system that is steady state, at a nor isothermal and non-adiabatic single tube fixed--bed reactor. The .simulation 1.s done by means of Ai 0-dimensional fixed-bed reactor model derived from mass and energv balance. The model is solved numerically fusing a semidicreliration method in MA7LAIi language. The result of computation shows a good agreement when it is verified with experimental data of l'anthe/. The variables that are used, namelt'.feed temperature (To). wall temperature (Th), methanol composition in the feed (Co). and, feed mass flo%vrate (m) give a significant effect to the distribution of concentration, temperature, pressure, and superficial velocity. 77w higher the To, 7µr. and Co, the higher the hot spot temperature achieved and its position is shifted to the entrance of the reactor. At higher Tw, the shift is not signniftcant. The reverse thing does happen at the higher feed mass flowrate (m). The outlet temperature increases at higher Tw and Co. but decreases at higher To and m. At higher Co the methanol conversion increases. The pressure drop (OP) is more it fluenced by Co and m: whereas the superficial velocity by To and m
format Theses
author Misran, Erni
spellingShingle Misran, Erni
SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
author_facet Misran, Erni
author_sort Misran, Erni
title SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
title_short SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
title_full SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
title_fullStr SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
title_full_unstemmed SIMULASI DUA DIMENSI REAKS: OKSIDASI METANOL MENJADI FORMALDEHIDA PADA REAKTOR UNGGUN TETAP
title_sort simulasi dua dimensi reaks: oksidasi metanol menjadi formaldehida pada reaktor unggun tetap
url https://digilib.itb.ac.id/gdl/view/3036
_version_ 1820663326284185600