Boron and metal removal technology from PGMEA and NMP

Boron in organic solvent is one of the impurities which was difficult to remove by sub-boiling distillation as a result of our pre-evaluation. On the other hand, ion exchange reaction using Ion Exchange Resin (IER) treatment was effective to remove boron in comparison to the result of sub-boiling distillation. In this presentation, we evaluated the combination of three type of ion exchange resins; chelating (C-IER), strong acid (SA-IER), and strong base (SB-IER) to remove the metal impurities and boron from organic solvents. Propylene Glycol Monomethyl Ether Acetate (PGMEA) and N-Methyl-2-Pyrrolidone (NMP) were highlighted as target organic solvents. The target concentration level of each metal impurities was 1 ng/L. As a result, C-MB system consisted of two step treatment, C-IER followed by the mixture of SB-IER and SA-IER was effective for removing metal impurities from both PGMEA and NMP. In order to reduce the hydrolysis of PGMEA when contacting SB-IER, HCO<sub>3</sub> form SB-IER was adopted for the treatment.

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Published
2025-02-21
DOI
https://doi.org/10.1117/12.3049988
Primary Topic
Extraction and Separation Processes
Type
article
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article

Boron and metal removal technology from PGMEA and NMP

Noriko Hisano
2 links
Extraction and Separation Processes
article

Boron and metal removal technology from PGMEA and NMP

Noriko Hisano
article en

Abstract

Boron in organic solvent is one of the impurities which was difficult to remove by sub-boiling distillation as a result of our pre-evaluation. On the other hand, ion exchange reaction using Ion Exchange Resin (IER) treatment was effective to remove boron in comparison to the result of sub-boiling distillation. In this presentation, we evaluated the combination of three type of ion exchange resins; chelating (C-IER), strong acid (SA-IER), and strong base (SB-IER) to remove the metal impurities and boron from organic solvents. Propylene Glycol Monomethyl Ether Acetate (PGMEA) and N-Methyl-2-Pyrrolidone (NMP) were highlighted as target organic solvents. The target concentration level of each metal impurities was 1 ng/L. As a result, C-MB system consisted of two step treatment, C-IER followed by the mixture of SB-IER and SA-IER was effective for removing metal impurities from both PGMEA and NMP. In order to reduce the hydrolysis of PGMEA when contacting SB-IER, HCO<sub>3</sub> form SB-IER was adopted for the treatment.

Organ Technologies (Japan) (JP)
Openalex Percentile: Top 97%
Extraction and Separation Processes
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