Correction to “Intensification Mechanism of Acidic Imidazole-Based Ionic Liquids on the Synthesis of 1,3,5-Trioxane Catalyzed by Sulfuric Acid”

IF 3.9 3区 工程技术 Q2 ENGINEERING, CHEMICAL Industrial & Engineering Chemistry Research Pub Date : 2025-04-01 DOI:10.1021/acs.iecr.5c01119
Ke Yuan, Tao Zhang, Li Lv, Yan Wang, Zongpeng Zou, Shengwei Tang
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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":3.9000,"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 in Conclusions: 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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对“酸性咪唑基离子液体对硫酸催化合成1,3,5-三氧环的强化机理”的修正
作者很遗憾地报告说,他们在2024年发表的文章中发现了两个错误。根据这些错误,对原文的更正如下:摘要更正:“TOX的产率从13.84%提高到16.95%,每公斤FA溶液中添加0.5 mol [PS2Im]HSO4”更正为“TOX的产率从4.21%提高到5.14%,每公斤FA溶液中添加0.5 mol [PS2Im]HSO4”。公式3的更正:将公式3更正如下。将2.2.2节第二段第二句“The number 5.35 is The calibration coefficient of The GC analysis”改为“The number 4.87 is The calibration coefficient of The GC analysis”。支持信息的更正:新版TOX定量标准曲线在此更正后被更正为支持信息的图SC2。图3的勘误表:图3更正如下。图3。反应液中TOX浓度随反应时间的变化。(a) H2SO4 (0.6 mol/kg) + ILs (0.1 mol/kg)和(b) H2SO4 (0.6 mol/kg) + ILs (0.5 mol/kg)(进料流中FA浓度为50 wt %,反应温度为100℃)。用eq 9拟合直线。圆点是实验结果。)表1的更正:原文表1更正如下。mol/kg =质量摩尔浓度[mol × (kg FA水溶液)−1]。反应溶液中TOX的平衡浓度。k1和k2分别为在50 wt % FA溶液中,在100°C条件下正反反应的速率常数。K是方程1中反应的平衡常数。3.2节实验结果描述的更正:3.2节第二段第4-13行,“分别加入0.1 mol/kg的[PMIm]HSO4、[PSMIm]HSO4和[PS2Im]HSO4时,TOX的平衡产率分别为14.35%、15.04和15.58%。”与以H2SO4为催化剂的TOX的平衡产率13.84%相比,相对增量分别为3.7、8.7和12.6%。当il用量增加到0.5 mol/kg时,TOX的平衡产率分别提高到16.19%、16.49%和16.95%。当添加0.1 mol/kg的[PMIm]HSO4、[PSMIm]HSO4和[PS2Im]HSO4时,TOX的平衡产率分别为4.35%、4.56%和4.72%。与以H2SO4为催化剂的TOX的平衡产率4.21%相比,相对增量分别为3.3、8.3和12.1%。当IL用量增加到0.5 mol/kg时,TOX的平衡产率分别提高到4.91、5.01和5.14%。与以H2SO4为催化剂的TOX的平衡产率相比,分别增加了16.6%、19.0%和22.1%。图7的勘误:图7被更正如下。图7。复合催化剂水溶液(25℃,96.3 kPa)的水活度与不同反应体系中TOX平衡产率的关系结论句更正:将“And The yield of TOX从13.84增加到16.95%,增量为22.5%”修改为“And The yield of TOX从4.21增加到5.14%,增量为22.1%”。支持信息可在https://pubs.acs.org/doi/10.1021/acs.iecr.5c01119免费获取。TOX定量标准曲线(PDF)对“双基咪唑离子液体对硫酸分析合成1,3,5-三氧化合物的强化机理”的修正0查看0分享0下载大多数电子支持信息文件无需订阅ACS网络版即可获得。这些文件可以通过文章下载用于研究用途(如果相关文章有公共使用许可链接,该许可可以允许其他用途)。如有其他用途,可通过RightsLink权限系统http://pubs.acs.org/page/copyright/permissions.html向ACS申请。我们要感谢编辑们对这次更正的处理。这篇文章尚未被其他出版物引用。
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来源期刊
Industrial & Engineering Chemistry Research
Industrial & Engineering Chemistry Research 工程技术-工程:化工
CiteScore
7.40
自引率
7.10%
发文量
1467
审稿时长
2.8 months
期刊介绍: 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.
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