4.7 Article

Fate of low molecular weight organic matters in reverse osmosis and vacuum ultraviolet process for high-quality ultrapure water production in the semiconductor industry

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JOURNAL OF CLEANER PRODUCTION
卷 423, 期 -, 页码 -

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ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2023.138714

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Low molecular weight organic matter; Semiconductor industry; Ultrapure water; Reverse osmosis; Vacuum ultraviolet

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Ultrapure water is crucial in the semiconductor industry, but the presence of low molecular weight organic matters (LMWOMs) in feed water sources can affect its quality. This study investigates the mechanisms of LMWOM removal in reverse osmosis (RO) and the performance of vacuum ultraviolet (VUV) for producing high-quality ultrapure water. It finds that RO primarily removes LMWOMs through size exclusion, but certain substances such as methanol, ethanol, and urea are not efficiently removed. Lab-scale and pilot-scale VUV experiments demonstrate the limitations in removing LMWOMs with low reactivity. The study discusses strategies for ultrapure water production using current water sources.
Ultrapure water (UPW) is essential in the semiconductor industry for rinsing and cleaning products. With the growing demand for UPW, various feed water sources such as tap water, surface water, and wastewater are utilized to produce UPW. However, these feed water sources contain various low molecular weight organic matters (LMWOMs), which can adversely affect the quality of semiconductors when present in treated UPW. Therefore, achieving the complete removal of LMWOMs is crucial in the UPW production process. However, the current reverse osmosis (RO) and vacuum ultraviolet (VUV) processes employed for UPW production have limitations in achieving complete LMWOM removal. Therefore, this study is conducted to investigate the mechanisms of LMWOM removal in RO and the performance of VUV for high-quality UPW production. Six LMWOMs found in the semiconductor industry were tested for lab- and pilot-scale experiments. The result showed that size exclusion is the main mechanism of LMWOM removal in the RO process. However, methanol, ethanol, and urea were not efficiently removed by RO membranes. In addition, a lab-scale VUV experiment was performed under accelerated conditions to examine the oxidation mechanism of LMWOM. The LMWOM with low reactivity to hydroxyl radicals, such as tetramethylammonium hydroxide (TMAH) and urea, were not removed perfectly within 60 min and 180 min, respectively. Furthermore, a pilot-scale VUV experiment was performed to examine the oxidation of LMWOM under real UPW production conditions. Despite observing a correlation in the pseudo-first-order rate constants between the lab-scale and pilot-scale experiments, the removal of TMAH and urea was still not achieved even with a lamp power of 320 W. As urea was not completely removed by either RO or VUV, strategies for UPW production using current water sources are discussed to develop future UPW technologies.

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