Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange

博士 === 國立臺灣科技大學 === 化學工程系 === 101 === Due to the rise in thin-film transistor liquid crystal display and semiconductor manufacturing, amount of chemicals extensively used in production process have increased as well. Tetramethylammonium hydroxide (TMAH) is one the chemicals, widely used as a major i...

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Main Authors: Hening Marlistya Citraningrum, 施佳鋭
Other Authors: Liu Jhy Chern
Format: Others
Language:en_US
Published: 2013
Online Access:http://ndltd.ncl.edu.tw/handle/29167971054658297114
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spelling ndltd-TW-101NTUS53421372016-08-22T04:17:27Z http://ndltd.ncl.edu.tw/handle/29167971054658297114 Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange Hening Marlistya Citraningrum 施佳鋭 博士 國立臺灣科技大學 化學工程系 101 Due to the rise in thin-film transistor liquid crystal display and semiconductor manufacturing, amount of chemicals extensively used in production process have increased as well. Tetramethylammonium hydroxide (TMAH) is one the chemicals, widely used as a major ingredient of photoresist developer in light emitting diode (LED) production, as well as an alkaline etchant and cleaning solution in semiconductor manufacturing. TMAH is a strong base and highly toxic, thus TMAH-containing wastewater has to be properly treated before it is discharged to the environment. In this study, ion exchange process using commercial ion exchange resin was selected. Two cation exchange resins, namely strong acid (SAC) and weak acid (WAC) cation exchange resin were used to remove TMAH from aqueous solution. Both resins showed high TMA+ ion removal. Ion exchange process was completed within 20 minutes when using SAC and 40 minutes when using WAC. Pseudo second order kinetics model was chosen to represent experimental data, which showed that SAC has faster exchange rate compared to WAC. Investigation on the effect of solution pH revealed WAC was more predominantly affected, and equilibrium pH above 6.5 needs to be maintained. Freundlich and Langmuir adsorption isotherm showed that adsorption was favorable; with Langmuir parameters implied that WAC has stronger interaction with TMA+ compared to SAC. Desorption study using HCl suggested that ion exchange resins used in this study can performed well after 5 cycles. Calculated selectivity coefficient for TMA+ uptake using SAC and WAC was 5.16 and 46.28, respectively. The presence of interfering ions, both simple and more complex ones, affected TMA+ uptake. When amines were present in solution, the extent of TMA+ uptake decrease was as high as 37%, due to strong interaction between resin matrix with amine molecule Liu Jhy Chern 劉志成 2013 學位論文 ; thesis 120 en_US
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language en_US
format Others
sources NDLTD
description 博士 === 國立臺灣科技大學 === 化學工程系 === 101 === Due to the rise in thin-film transistor liquid crystal display and semiconductor manufacturing, amount of chemicals extensively used in production process have increased as well. Tetramethylammonium hydroxide (TMAH) is one the chemicals, widely used as a major ingredient of photoresist developer in light emitting diode (LED) production, as well as an alkaline etchant and cleaning solution in semiconductor manufacturing. TMAH is a strong base and highly toxic, thus TMAH-containing wastewater has to be properly treated before it is discharged to the environment. In this study, ion exchange process using commercial ion exchange resin was selected. Two cation exchange resins, namely strong acid (SAC) and weak acid (WAC) cation exchange resin were used to remove TMAH from aqueous solution. Both resins showed high TMA+ ion removal. Ion exchange process was completed within 20 minutes when using SAC and 40 minutes when using WAC. Pseudo second order kinetics model was chosen to represent experimental data, which showed that SAC has faster exchange rate compared to WAC. Investigation on the effect of solution pH revealed WAC was more predominantly affected, and equilibrium pH above 6.5 needs to be maintained. Freundlich and Langmuir adsorption isotherm showed that adsorption was favorable; with Langmuir parameters implied that WAC has stronger interaction with TMA+ compared to SAC. Desorption study using HCl suggested that ion exchange resins used in this study can performed well after 5 cycles. Calculated selectivity coefficient for TMA+ uptake using SAC and WAC was 5.16 and 46.28, respectively. The presence of interfering ions, both simple and more complex ones, affected TMA+ uptake. When amines were present in solution, the extent of TMA+ uptake decrease was as high as 37%, due to strong interaction between resin matrix with amine molecule
author2 Liu Jhy Chern
author_facet Liu Jhy Chern
Hening Marlistya Citraningrum
施佳鋭
author Hening Marlistya Citraningrum
施佳鋭
spellingShingle Hening Marlistya Citraningrum
施佳鋭
Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
author_sort Hening Marlistya Citraningrum
title Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
title_short Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
title_full Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
title_fullStr Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
title_full_unstemmed Removal of Tetramethylammonium Hydroxide (TMAH) from Aqueous Solution Using Ion Exchange
title_sort removal of tetramethylammonium hydroxide (tmah) from aqueous solution using ion exchange
publishDate 2013
url http://ndltd.ncl.edu.tw/handle/29167971054658297114
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