Process simulation for electronic-grade methanethiol synthesis via H

This study proposes an integrated process for producing electronic-grade methanethiol (EMT) from H2S-rich Rectisol tail gas (RTS) through three stages: H2S purification, methanethiol (MT) synthesis, and MT refining. First, a two-stage methyl diethanolamine absorption-desorption process selectively recovers H2S from RTS, achieving 92 mol% H2S purity. Subsequently, MT is synthesized via methanol and H2S over a K2WO4/Al2O3 catalyst in a fixed-bed reactor optimized at 380°C, 10 bar, and a mass hourly space velocity (MHSV) of 2 h−1, achieving 90% methanol conversion and 92% MT selectivity. Finally, the crude product is separated via a optimized distillation sequence, with a pressure-swing distillation to break the methanol-dimethyl sulfide azeotrope, yielding EMT with 99.99 wt% purity. Rigorous Aspen Plus simulations demonstrate the process's economic viability, leveraging H2S valorization to produce high-value EMT while meeting stringent emission standards (<0.03 mg/m3 H2S).

Authors

Publication Details

Journal
Springer Link (Chiba Institute of Technology)
Published
2025-05-16
DOI
https://doi.org/10.1051/e3sconf/202562801014/pdf
Primary Topic
Industrial Gas Emission Control
Type
article
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article

Process simulation for electronic-grade methanethiol synthesis via H

Peijie Zhou, Yaqi Liu, Lulu Ma, Guangheng Wang
Springer Link (Chiba Institute of Technology)
Industrial Gas Emission Control
article

Process simulation for electronic-grade methanethiol synthesis via H

Peijie Zhou, Yaqi Liu, Lulu Ma, Guangheng Wang
article en

Abstract

This study proposes an integrated process for producing electronic-grade methanethiol (EMT) from H2S-rich Rectisol tail gas (RTS) through three stages: H2S purification, methanethiol (MT) synthesis, and MT refining. First, a two-stage methyl diethanolamine absorption-desorption process selectively recovers H2S from RTS, achieving 92 mol% H2S purity. Subsequently, MT is synthesized via methanol and H2S over a K2WO4/Al2O3 catalyst in a fixed-bed reactor optimized at 380°C, 10 bar, and a mass hourly space velocity (MHSV) of 2 h−1, achieving 90% methanol conversion and 92% MT selectivity. Finally, the crude product is separated via a optimized distillation sequence, with a pressure-swing distillation to break the methanol-dimethyl sulfide azeotrope, yielding EMT with 99.99 wt% purity. Rigorous Aspen Plus simulations demonstrate the process's economic viability, leveraging H2S valorization to produce high-value EMT while meeting stringent emission standards (<0.03 mg/m3 H2S).

Springer Link (Chiba Institute of Technology)
Openalex Percentile: Top 40%
Industrial Gas Emission Control
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