PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI

<b>Abstract :</b><p align=\"justify\"> Modeling of electrolysis process has been conducted for water treatment contained ferrous was used artificial raw water with controllable level and type of ferrous. The influence of some parameters in electrolysis process can be pred...

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Main Author: Irwan Bagyo Santoso (NIM : 25397021), R.
Format: Theses
Language:Indonesia
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Online Access:https://digilib.itb.ac.id/gdl/view/4831
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Institution: Institut Teknologi Bandung
Language: Indonesia
id id-itb.:4831
spelling id-itb.:48312006-06-30T14:43:20ZPEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI Irwan Bagyo Santoso (NIM : 25397021), R. Teknik (Rekayasa, enjinering dan kegiatan berkaitan) Indonesia Theses Modelling, Electrolysis, Water treatment, Reactor INSTITUT TEKNOLOGI BANDUNG https://digilib.itb.ac.id/gdl/view/4831 <b>Abstract :</b><p align=\"justify\"> Modeling of electrolysis process has been conducted for water treatment contained ferrous was used artificial raw water with controllable level and type of ferrous. The influence of some parameters in electrolysis process can be predicted by experiment used model of electrolysis process reactor. <br /> <br /> The experiment used batch model , some parameters that influence process are : current , initial concentration , area of electrode , type of ferrous , and distance of electrode. On the other hand , the experiment used reactor model with continous flow , the parameters that influence the process are : current, area of electrode , flow and type of ferrous . <br /> <br /> The results of experiment are process equation for batch reactor as follow : <br /> Zero orde reaction ( initial process) : <br /> Ct=Co-Kl.t <br /> where : <br /> KI = -2.1027.10<sup<-3</sup>- 1.3526.10<sup>-1</sup>.I-I.8351.10<sup>-5</sup>.Co-1.4412:10<sup>-6</sup>.A+ 2.5537.10<sup>-4</sup>.x+2.0567,10<sup>-3</sup>.n <br /> First orde reaction ( after zero orde ) <br /> In Ct = In C\' - (K2.(t-t\')) <br /> where : <br /> K2 = -1.4347.10<sup>-4</sup> -6.9085.10<sup>-4</sup>.I+ 1.6117 .10<sup>-5</sup>.lnCo - <br /> 8.7714. 10<sup>-9</sup>. A+3 . 3 927.10<sup>-5</sup>. n <br /> <br /> The results of experiment are process equation for continous flow reactor as follow : <br /> Cout = Cin ( e<sup>(KL.A/Q</sup>)<sup>-1</sup> <br /> where <br /> K<sub>L</sub>= 1.7323.10<sup>-4</sup> + 8.1060.10<sup>-4</sup>.1- 2.2717.10<sup>-5</sup>.1nCin - -2.0216.10<usp>-5</sup>, n-1.4067.10<sup>-8</sup>.A+1.1735.10<sup>1</sup>.Q 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
topic Teknik (Rekayasa, enjinering dan kegiatan berkaitan)
spellingShingle Teknik (Rekayasa, enjinering dan kegiatan berkaitan)
Irwan Bagyo Santoso (NIM : 25397021), R.
PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
description <b>Abstract :</b><p align=\"justify\"> Modeling of electrolysis process has been conducted for water treatment contained ferrous was used artificial raw water with controllable level and type of ferrous. The influence of some parameters in electrolysis process can be predicted by experiment used model of electrolysis process reactor. <br /> <br /> The experiment used batch model , some parameters that influence process are : current , initial concentration , area of electrode , type of ferrous , and distance of electrode. On the other hand , the experiment used reactor model with continous flow , the parameters that influence the process are : current, area of electrode , flow and type of ferrous . <br /> <br /> The results of experiment are process equation for batch reactor as follow : <br /> Zero orde reaction ( initial process) : <br /> Ct=Co-Kl.t <br /> where : <br /> KI = -2.1027.10<sup<-3</sup>- 1.3526.10<sup>-1</sup>.I-I.8351.10<sup>-5</sup>.Co-1.4412:10<sup>-6</sup>.A+ 2.5537.10<sup>-4</sup>.x+2.0567,10<sup>-3</sup>.n <br /> First orde reaction ( after zero orde ) <br /> In Ct = In C\' - (K2.(t-t\')) <br /> where : <br /> K2 = -1.4347.10<sup>-4</sup> -6.9085.10<sup>-4</sup>.I+ 1.6117 .10<sup>-5</sup>.lnCo - <br /> 8.7714. 10<sup>-9</sup>. A+3 . 3 927.10<sup>-5</sup>. n <br /> <br /> The results of experiment are process equation for continous flow reactor as follow : <br /> Cout = Cin ( e<sup>(KL.A/Q</sup>)<sup>-1</sup> <br /> where <br /> K<sub>L</sub>= 1.7323.10<sup>-4</sup> + 8.1060.10<sup>-4</sup>.1- 2.2717.10<sup>-5</sup>.1nCin - -2.0216.10<usp>-5</sup>, n-1.4067.10<sup>-8</sup>.A+1.1735.10<sup>1</sup>.Q
format Theses
author Irwan Bagyo Santoso (NIM : 25397021), R.
author_facet Irwan Bagyo Santoso (NIM : 25397021), R.
author_sort Irwan Bagyo Santoso (NIM : 25397021), R.
title PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
title_short PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
title_full PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
title_fullStr PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
title_full_unstemmed PEMODELAN PROSES ELEKTROLISIS UNTUK PENGOLAHAN AIR YANG MENGANDUNG BESI
title_sort pemodelan proses elektrolisis untuk pengolahan air yang mengandung besi
url https://digilib.itb.ac.id/gdl/view/4831
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