HETEROPOLY ACID AS NEW LIQUID REDOX ABSORBENT FOR LOW SULFUR CONTAINING GAS SWEETENING
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概要
- 論文の詳細を見る
Using as absorbent the aqueous solution of heteropoly compound, namely H<SUB>3</SUB>PW<SUB>10</SUB>Mo<SUB>2</SUB>O<SUB>40</SUB>, a new approach to low sulfur containing gas desulfurization and sulfur recovery was developed. The dependence of the desulfurization efficiency on factors including the absorbent concentration, absorption temperature and the feed gas H<SUB>2</SUB>S concentration were experimentally investigated, whereby the favourable operation conditions were recommended. For the gas stream with H<SUB>2</SUB>S concentration below 1000mg/m<SUP>3</SUP>, flowing at a rate of 0.368L/min, the favourable concentration of 200mL of H<SUB>3</SUB>PW<SUB>10</SUB>Mo<SUB>2</SUB>O<SUB>40</SUB> is ca. 5×10<SUP>-3</SUP>mol/L. Within the temperature range of beyond 30°C as investigated, the increase of the absorption temperature tends to decrease the desulfunzation efficiency of H<SUB>3</SUB>PW<SUB>10</SUB>Mo<SUB>2</SUB>O<SUB>40</SUB> solution. However, within the temperature range of below 30°C, the reverse effect can be found. Hence, ambient temperature of around 30°C is favourable for desulfurization. The desulfurization efficiency of H<SUB>3</SUB>PW<SUB>10</SUB>Mo<SUB>2</SUB>O<SUB>40</SUB> solution decreases with the increase of H<SUB>2</SUB>S concentration in the feed gas stream, which can be found remarkably when the absorption time exceeds 20min. Some additives having positive effect on the desulfurization performance of H<SUB>3</SUB>PW<SUB>10</SUB>Mo<SUB>2</SUB>O<SUB>40</SUB> solution were found, with the effect decreasing in the order CuS>NaCl>NH<SUB>4</SUB>VO<SUB>3</SUB> at low dosage.
- 日本マクロエンジニアリング学会の論文
著者
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WANG RUI
Chem. Eng. Department, Hainan University
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GAO HANG
State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences
関連論文
- HETEROPOLY ACID AS NEW LIQUID REDOX ABSORBENT FOR LOW SULFUR CONTAINING GAS SWEETENING
- DEVELOPMENT OF HPA-BASED NEW REGENERABLE LIQUID REDOX ABSORBENT SYSTEM FOR SO2 REMOVAL FROM GAS STREAMS