2022
DOI: 10.1016/j.cej.2021.132707
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Study on removing NO from simulated marine diesel engine exhaust gas using the novel composite system of Ozone-Na2SO3/(NH2)2CO

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Cited by 2 publications
(6 citation statements)
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“…After 2 h of treatment, the removal rates of NO 2 and NO x decreased from 85 to 68% and from 80 to 58%, respectively. Owing to the large consumption of Na 2 S 2 O 5 and the reduction in the SO 3 2– concentration, eqs and shifted to the left, and the removal rates of NO x and NO 2 were markedly reduced Na 2 normalS 2 normalO 5 + normalH 2 normalO 2 Na normalH normalS normalO 3 2 Na normalH normalS normalO 3 Na 2 SO 3 + normalH 2 normalO + SO 2 2 normalN O 2 + SO 3 2 + normalH 2 normalO SO 4 2 + 2 normalN normalO 2 + 2 normalH + 2 normalN normalO 2 + 4 normalS normalO 3 2 …”
Section: Resultsmentioning
confidence: 99%
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“…After 2 h of treatment, the removal rates of NO 2 and NO x decreased from 85 to 68% and from 80 to 58%, respectively. Owing to the large consumption of Na 2 S 2 O 5 and the reduction in the SO 3 2– concentration, eqs and shifted to the left, and the removal rates of NO x and NO 2 were markedly reduced Na 2 normalS 2 normalO 5 + normalH 2 normalO 2 Na normalH normalS normalO 3 2 Na normalH normalS normalO 3 Na 2 SO 3 + normalH 2 normalO + SO 2 2 normalN O 2 + SO 3 2 + normalH 2 normalO SO 4 2 + 2 normalN normalO 2 + 2 normalH + 2 normalN normalO 2 + 4 normalS normalO 3 2 …”
Section: Resultsmentioning
confidence: 99%
“…This is because, in addition to Na 2 S 2 O 5 that needs to be consumed to remove NO 2 and NO x , the etching waste gas contains a large amount of O 2 , Cl 2 , and acidic waste gases such as HF, which can also oxidize SO 3 2– to SO 4 2– . This may explain why the SO 3 2– concentration required to reduce marine exhaust gas is high . The oxidation–reduction potential (ORP) of E SO 4 2– /SO 3 2– is −0.94 mV, and the ORP of the Na 2 S used for current etching waste gas treatment is −0.48 mV higher than that of E SO 4 2– /SO 3 2– .…”
Section: Resultsmentioning
confidence: 99%
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