Ke Yuan, Tao Zhang, Li Lv, Yan Wang, Zongpeng Zou, Shengwei Tang
{"title":"Correction to “Intensification Mechanism of Acidic Imidazole-Based Ionic Liquids on the Synthesis of 1,3,5-Trioxane Catalyzed by Sulfuric Acid”","authors":"Ke Yuan, Tao Zhang, Li Lv, Yan Wang, Zongpeng Zou, Shengwei Tang","doi":"10.1021/acs.iecr.5c01119","DOIUrl":null,"url":null,"abstract":"The authors regret to report that they have identified two errors in the article published in 2024. Based on these errors, the corrigendum to the original article is as follows: <b>Corrigendum to Abstract:</b> “The yield of TOX was increased from 13.84 to 16.95% with the addition of 0.5 mol [PS<sub>2</sub>Im]HSO<sub>4</sub> per kilogram of FA solution” is corrected to “The yield of TOX was increased from 4.21 to 5.14% with the addition of 0.5 mol [PS<sub>2</sub>Im]HSO<sub>4</sub> per kilogram of FA solution”. <b>Corrigendum to eq 3:</b> Equation 3 is corrected as shown below. The second sentence of paragraph two in Section 2.2.2, “The number 5.35 is the calibration coefficient of the GC analysis” was corrected to “The number 4.87 is the calibration coefficient of the GC analysis”. <b>Corrigendum to the Supporting Information:</b> The new version of the standard curve for TOX quantification is corrected as Figure SC2 of Supporting Information with this Correction. <b>Corrigendum to Figure 3:</b> Figure 3 is corrected as shown below. Figure 3. Variation of TOX concentrations in reaction liquids with reaction time. (a) H<sub>2</sub>SO<sub>4</sub> (0.6 mol/kg) + ILs (0.1 mol/kg) and (b) H<sub>2</sub>SO<sub>4</sub> (0.6 mol/kg) + ILs (0.5 mol/kg) (The FA concentration in the feed stream was 50 wt %, and the reaction temperature was 100 °C. Lines were fitted by eq 9. Dots were experimental results.) <b>Corrigendum to Table 1:</b> Table 1 in original article is corrected as shown below. mol/kg = molality [mol × (kg FA aqueous solution)<sup>−1</sup>]. The equilibrium concentration of TOX in reaction solutions. <i>k</i><sub>1</sub> and <i>k</i><sub>2</sub> are, respectively, the rate constants of the forward and the reverse reactions with a 50 wt % FA solution at 100 °C. <i>K</i> is the equilibrium constant of reaction in eq 1. <b>Corrigendum to description of the experimental results in Section 3.2:</b> Lines 4–13 of paragraph two in Section 3.2, the sentences “When 0.1 mol/kg of [PMIm]HSO<sub>4</sub>, [PSMIm]HSO<sub>4</sub> and [PS<sub>2</sub>Im]HSO<sub>4</sub> were respectively added, the equilibrium yields of TOX were 14.35, 15.04, and 15.58%, respectively. Compared with 13.84%, which was the equilibrium yield of TOX with H<sub>2</sub>SO<sub>4</sub> as catalyst, the relative increments were 3.7, 8.7, and 12.6%, respectively. When the ILs dosages were increased to 0.5 mol/kg, the equilibrium yields of TOX were increased to 16.19, 16.49, and 16.95%, respectively. Compared with the equilibrium yield of TOX with H<sub>2</sub>SO<sub>4</sub> as catalyst, the increments were 16.9, 19.1, and 22.5%, respectively” are changed to “When 0.1 mol/kg of [PMIm]HSO<sub>4</sub>, [PSMIm]HSO<sub>4</sub> and [PS<sub>2</sub>Im]HSO<sub>4</sub> were respectively added, the equilibrium yields of TOX were 4.35, 4.56, and 4.72%, respectively. Compared with 4.21%, which was the equilibrium yield of TOX with H<sub>2</sub>SO<sub>4</sub> as catalyst, the relative increments were 3.3, 8.3, and 12.1%, respectively. When the IL dosages were increased to 0.5 mol/kg, the equilibrium yields of TOX were increased to 4.91, 5.01, and 5.14%, respectively. Compared with the equilibrium yield of TOX with H<sub>2</sub>SO<sub>4</sub> as catalyst, the increments were 16.6, 19.0, and 22.1%, respectively”. <b>Corrigendum to Figure 7:</b> Figure 7 is corrected as shown below. Figure 7. Relationship between the water activity of composite catalyst aqueous solutions (25 °C and 96.3 kPa) and the equilibrium yield of TOX in different reaction systems. <b>Corrigendum to sentence in</b> <b>Conclusions:</b> The sentence “And the yield of TOX increased from 13.84 to 16.95% with an increment of 22.5%” is corrected to “And the yield of TOX increased from 4.21 to 5.14% with an increment of 22.1%”. The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acs.iecr.5c01119. Standard curve for TOX quantification (PDF) Correction to “Intensification\nMechanism of\nAcidic Imidazole-Based Ionic Liquids on the Synthesis of 1,3,5-Trioxane\nCatalyzed by Sulfuric Acid” <span> 0 </span><span> views </span> <span> 0 </span><span> shares </span> <span> 0 </span><span> downloads </span> Most electronic Supporting Information files are available without a subscription to ACS Web Editions. Such files may be downloaded by article for research use (if there is a public use license linked to the relevant article, that license may permit other uses). Permission may be obtained from ACS for other uses through requests via the RightsLink permission system: http://pubs.acs.org/page/copyright/permissions.html. We would like to thank the editors for their handling of this Correction. This article has not yet been cited by other publications.","PeriodicalId":39,"journal":{"name":"Industrial & Engineering Chemistry Research","volume":"73 1","pages":""},"PeriodicalIF":3.8000,"publicationDate":"2025-04-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Industrial & Engineering Chemistry Research","FirstCategoryId":"5","ListUrlMain":"https://doi.org/10.1021/acs.iecr.5c01119","RegionNum":3,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
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Abstract
The authors regret to report that they have identified two errors in the article published in 2024. Based on these errors, the corrigendum to the original article is as follows: Corrigendum to Abstract: “The yield of TOX was increased from 13.84 to 16.95% with the addition of 0.5 mol [PS2Im]HSO4 per kilogram of FA solution” is corrected to “The yield of TOX was increased from 4.21 to 5.14% with the addition of 0.5 mol [PS2Im]HSO4 per kilogram of FA solution”. Corrigendum to eq 3: Equation 3 is corrected as shown below. The second sentence of paragraph two in Section 2.2.2, “The number 5.35 is the calibration coefficient of the GC analysis” was corrected to “The number 4.87 is the calibration coefficient of the GC analysis”. Corrigendum to the Supporting Information: The new version of the standard curve for TOX quantification is corrected as Figure SC2 of Supporting Information with this Correction. Corrigendum to Figure 3: Figure 3 is corrected as shown below. Figure 3. Variation of TOX concentrations in reaction liquids with reaction time. (a) H2SO4 (0.6 mol/kg) + ILs (0.1 mol/kg) and (b) H2SO4 (0.6 mol/kg) + ILs (0.5 mol/kg) (The FA concentration in the feed stream was 50 wt %, and the reaction temperature was 100 °C. Lines were fitted by eq 9. Dots were experimental results.) Corrigendum to Table 1: Table 1 in original article is corrected as shown below. mol/kg = molality [mol × (kg FA aqueous solution)−1]. The equilibrium concentration of TOX in reaction solutions. k1 and k2 are, respectively, the rate constants of the forward and the reverse reactions with a 50 wt % FA solution at 100 °C. K is the equilibrium constant of reaction in eq 1. Corrigendum to description of the experimental results in Section 3.2: Lines 4–13 of paragraph two in Section 3.2, the sentences “When 0.1 mol/kg of [PMIm]HSO4, [PSMIm]HSO4 and [PS2Im]HSO4 were respectively added, the equilibrium yields of TOX were 14.35, 15.04, and 15.58%, respectively. Compared with 13.84%, which was the equilibrium yield of TOX with H2SO4 as catalyst, the relative increments were 3.7, 8.7, and 12.6%, respectively. When the ILs dosages were increased to 0.5 mol/kg, the equilibrium yields of TOX were increased to 16.19, 16.49, and 16.95%, respectively. Compared with the equilibrium yield of TOX with H2SO4 as catalyst, the increments were 16.9, 19.1, and 22.5%, respectively” are changed to “When 0.1 mol/kg of [PMIm]HSO4, [PSMIm]HSO4 and [PS2Im]HSO4 were respectively added, the equilibrium yields of TOX were 4.35, 4.56, and 4.72%, respectively. Compared with 4.21%, which was the equilibrium yield of TOX with H2SO4 as catalyst, the relative increments were 3.3, 8.3, and 12.1%, respectively. When the IL dosages were increased to 0.5 mol/kg, the equilibrium yields of TOX were increased to 4.91, 5.01, and 5.14%, respectively. Compared with the equilibrium yield of TOX with H2SO4 as catalyst, the increments were 16.6, 19.0, and 22.1%, respectively”. Corrigendum to Figure 7: Figure 7 is corrected as shown below. Figure 7. Relationship between the water activity of composite catalyst aqueous solutions (25 °C and 96.3 kPa) and the equilibrium yield of TOX in different reaction systems. Corrigendum to sentence inConclusions: The sentence “And the yield of TOX increased from 13.84 to 16.95% with an increment of 22.5%” is corrected to “And the yield of TOX increased from 4.21 to 5.14% with an increment of 22.1%”. The Supporting Information is available free of charge at https://pubs.acs.org/doi/10.1021/acs.iecr.5c01119. Standard curve for TOX quantification (PDF) Correction to “Intensification
Mechanism of
Acidic Imidazole-Based Ionic Liquids on the Synthesis of 1,3,5-Trioxane
Catalyzed by Sulfuric Acid” 0 views 0 shares 0 downloads Most electronic Supporting Information files are available without a subscription to ACS Web Editions. Such files may be downloaded by article for research use (if there is a public use license linked to the relevant article, that license may permit other uses). Permission may be obtained from ACS for other uses through requests via the RightsLink permission system: http://pubs.acs.org/page/copyright/permissions.html. We would like to thank the editors for their handling of this Correction. This article has not yet been cited by other publications.
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ndustrial & Engineering Chemistry, with variations in title and format, has been published since 1909 by the American Chemical Society. Industrial & Engineering Chemistry Research is a weekly publication that reports industrial and academic research in the broad fields of applied chemistry and chemical engineering with special focus on fundamentals, processes, and products.