Correction to “Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm”

IF 1.4 4区 工程技术 Q3 ENGINEERING, CHEMICAL Asia-Pacific Journal of Chemical Engineering Pub Date : 2024-11-04 DOI:10.1002/apj.3167
{"title":"Correction to “Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm”","authors":"","doi":"10.1002/apj.3167","DOIUrl":null,"url":null,"abstract":"<p>Ramalingam A, Banerjee T, Santhi VM, Mishra DK, Reji DJPM, Nagaraj S. Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm. <i>Asia-Pac J Chem Eng.</i> 2023; 18(2):e2875. doi:10.1002/apj.2875</p><p>Errors included in the original article may be due to the purity of individual components and experimental error, including sample bottle cleaning and the syringe used for density measurements. In addition, the apparent molar volume was calculated using a mathematical expression.</p><p>In Section 4.1, Para 1, Line 7: The following correction has been done.</p><p>“lesser than 0.02%” instead of “lesser than 0.23%”.</p><p>In Section 4.1, Equation (1): The equation was corrected as:</p><p>“\n<span></span><math>\n <msub>\n <mi>ρ</mi>\n <mtext>mixture</mtext>\n </msub>\n <mo>=</mo>\n <mi>a</mi>\n <mfenced>\n <mi>T</mi>\n </mfenced>\n <mo>+</mo>\n <mi>b</mi></math>” instead of “\n<span></span><math>\n <msub>\n <mi>ρ</mi>\n <mtext>mixture</mtext>\n </msub>\n <mo>=</mo>\n <mi>a</mi>\n <mo>+</mo>\n <mi>b</mi>\n <mfenced>\n <mi>T</mi>\n </mfenced>\n <mo>+</mo>\n <mi>c</mi>\n <msup>\n <mfenced>\n <mi>T</mi>\n </mfenced>\n <mn>2</mn>\n </msup></math>.</p><p>In Section 4.2, Para 2: The following correction has been done.</p><p>“[EMIM][EtSO<sub>4</sub>] &gt; [EMIM][HSO<sub>4</sub>] &gt; EtAc &gt; [ChCl][Gly] &gt; [ChCl][AA] &gt; EtOH &gt; HAc &gt; water”.</p><p>Use the above lines, instead of:</p><p>[EMIM][EtSO<sub>4</sub>] &lt; [EMIM][HSO4] &lt; EtAc &lt; [ChCl][Gly] &lt; [ChCl][AA] &lt; EtOH &lt; HAc &lt; water.</p><p>In Section 4.2, Para 3, Line 3: the following line has been corrected as:</p><p>“It can be observed that the \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values are positive for the binary mixtures of EtOH with EtAc, DES<sub>1</sub> {[ChCl][2AA]}, and DES<sub>2</sub> [ChCl][2Gly] over the entire composition range at all the studied temperatures”.</p><p>Use the above lines, instead of:</p><p>“It can be observed that the \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values are positive for the binary mixtures of EtOH with EtAc, [EMIM][HSO<sub>4</sub>], [EMIM][EtSO<sub>4</sub>], [ChCl][AA], and [ChCl][Gly] over the entire composition range at all the studied temperatures”.</p><p>In Section 4.2, Para 4, Line 7: The following line has been corrected as:</p><p>“The maximum of excess molar volume is 3.6466 cm<sup>3</sup> mol<sup>−1</sup> at <i>x</i><sub>1</sub> = 0.5014 for EtOH + [ChCl][2Gly], 1.2227 cm<sup>3</sup> mol<sup>−1</sup> at <i>x</i><sub>1</sub> = 0.5010 for EtOH+ [Ch-Cl][2AA], and EtOH + EtAc is 0.1102 cm<sup>3</sup> mol<sup>−1</sup> at <i>x</i><sub>1</sub> = 0.5013, respectively, at 293.15 K. The \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values follow the order: [Ch-Cl][Gly] &gt; [Ch-Cl][HAc] &gt; EtAc with ethanol”.</p><p>Use the above lines, instead of:</p><p>“The maximum of excess molar volume is 15.450 cm<sup>3</sup>/mol at x<sub>1</sub> = 0.5 for EtOH + [EMIM][EtSO<sub>4</sub>], 14.483 cm<sup>3</sup> mole<sup>−1</sup> at x<sub>1</sub> = 0.6 for EtOH+ [EMIM][HSO<sub>4</sub>], 5.714 cm<sup>3</sup> mole<sup>−1</sup> at x<sub>1</sub> = 0.4 for EtOH + [Ch-Cl][Gly], 1.785 cm<sup>3</sup> mole<sup>−1</sup> at x<sub>1</sub> = 0.4 for EtOH + [Ch-Cl][HAc], and EtOH + EtAc is 1.512 cm<sup>3</sup> mole<sup>−1</sup> at x<sub>1</sub> = 0.4, respectively. The \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values follow the order: [EMIM][EtSO<sub>4</sub>] &gt; [EMIM][HSO<sub>4</sub>] &gt; [Ch-Cl][Gly] &gt; [Ch-Cl][HAc] &gt; EtAc.”</p><p>In Section 4.2, Para 5, Line 1: The following line has been corrected as:</p><p>“EtOH + AA, EtOH + water, EtAc + AA, EtOH + [EMIM][EtSO<sub>4</sub>], and EtOH + [EMIM][HSO<sub>4</sub>] exhibit negative deviations from ideality over the whole composition range at all the studied temperatures. The minimum of \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> shift from the mole fraction range, <i>x</i><sub>1</sub> = 0.5003 (−1.1830 cm<sup>3</sup> mol<sup>−1</sup>) for EtOH + water, <i>x</i><sub>1</sub> = 0.4021 (−1.4196 cm<sup>3</sup> mol<sup>−1</sup>) for EtAc + AA, −0.6036 cm<sup>3</sup> mol<sup>−1</sup> at <i>x</i><sub>1</sub> = 0.7011 for EtOH + [EMIM][EtSO<sub>4</sub>], −1.588 cm<sup>3</sup> mol<sup>−1</sup> at <i>x</i><sub>1</sub> = 0.4022 for EtOH + [EMIM][HSO<sub>4</sub>], and <i>x</i><sub>1</sub> = 0.5017 (−0.5035 cm<sup>3</sup> mol<sup>−1</sup>) for EtOH + AA, respectively. Here, the \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values of the binary micture of EtOH + water are more negative when compared to the mixture of EtOH + AA and EtAc + AA”.</p><p>Use the above lines, instead of;</p><p>“EtOH + HAc, EtOH + water and EtAc + HAc exhibit negative deviations from ideality over the whole composition range at all the studied temperatures. The minimum of \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> shift from the mole fraction range 0.5 (−3.485 cm<sup>3</sup> mole<sup>−1</sup>) for EtOH + water, EtAc + HAc (−1.763 cm<sup>3</sup> mole<sup>−1</sup>) and 0.3 (−0.489 cm<sup>3</sup> mole<sup>−1</sup>) for EtOH + HAc, respectively. Here, the \n<span></span><math>\n <msup>\n <mi>V</mi>\n <mi>E</mi>\n </msup></math> values of the binary micture of EtOH + water are more negative when compared to the mixture of EtOH + HAc and EtAc + HAc”.</p><p>Figures 2, 3, and 4 have been revised. The following figures should be used in place of the original Figures 2, 3, and 4.</p><p>Table 4 has been revised. The following table should be used in place of the original Table 4.</p><p>Table 5 has been revised for EtOH + EtAc, ethanol (1) + [EMIM][EtSO<sub>4</sub>] (2), and ethanol + water mixtures of RK fitting values. The following table should be used in place of the original Table 5.</p><p>Table 6 has been revised. The following table should be used in place of the original Table 6.</p><p>Table S1 has been revised. The following table should be used in place of the original Table S1.</p><p>Table S1: The density correlation parameters a, b, and R<sup>2</sup> for all the studied systems.\n\n </p><p>Table S4 has been revised. The following table should be used in place of the original Table S4.</p><p><b>Table S4:</b> Excess molar volume of ethanol(1)+water(2), ethanol (1) +acetic acid (2), ethyl Acetate (1) + Acetic Acid (2), ethanol (1) +ethyl acetate (2), ethanol (1) + DES-1(AA) (2), ethanol (1) + DES-2(Gly), ethanol (1) + [EMIM][EtSO<sub>4</sub>] (2) and ethanol (1) + [EMIM][HSO<sub>4</sub>] (2) over the entire mole fractions and at different temperatures.\n\n </p><p>Table S5 has been revised. The following table should be used in place of the original Table S5.</p><p><b>Table S5:</b> The partial molar volume (cm<sup>3</sup>/mole), excess partial molar volume (cm<sup>3</sup>/mole) and apparent molar volume (cm<sup>3</sup>/mole) of individual compounds at different temperatures and 1 atm.\n\n </p><p>Standard uncertainty: u (T) = 0.01 K, u(p)=0.01MPa, u (ρ) = 0.0001 g cm<sup>−3</sup> and for \n<span></span><math>\n <mover>\n <msub>\n <mi>V</mi>\n <mi>i</mi>\n </msub>\n <mo>¯</mo>\n </mover></math>, \n<span></span><math>\n <msubsup>\n <mover>\n <mi>V</mi>\n <mo>¯</mo>\n </mover>\n <mi>i</mi>\n <mi>E</mi>\n </msubsup>\n <mo>,</mo>\n <msub>\n <mi>V</mi>\n <mrow>\n <mo>∅</mo>\n <mi>i</mi>\n </mrow>\n </msub></math>, = 0.002 cm<sup>3</sup> mole<sup>−1</sup> (0.95 level of confidence).</p>","PeriodicalId":49237,"journal":{"name":"Asia-Pacific Journal of Chemical Engineering","volume":"19 6","pages":""},"PeriodicalIF":1.4000,"publicationDate":"2024-11-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://onlinelibrary.wiley.com/doi/epdf/10.1002/apj.3167","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Asia-Pacific Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://onlinelibrary.wiley.com/doi/10.1002/apj.3167","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENGINEERING, CHEMICAL","Score":null,"Total":0}
引用次数: 0

Abstract

Ramalingam A, Banerjee T, Santhi VM, Mishra DK, Reji DJPM, Nagaraj S. Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm. Asia-Pac J Chem Eng. 2023; 18(2):e2875. doi:10.1002/apj.2875

Errors included in the original article may be due to the purity of individual components and experimental error, including sample bottle cleaning and the syringe used for density measurements. In addition, the apparent molar volume was calculated using a mathematical expression.

In Section 4.1, Para 1, Line 7: The following correction has been done.

“lesser than 0.02%” instead of “lesser than 0.23%”.

In Section 4.1, Equation (1): The equation was corrected as:

ρ mixture = a T + b” instead of “ ρ mixture = a + b T + c T 2 .

In Section 4.2, Para 2: The following correction has been done.

“[EMIM][EtSO4] > [EMIM][HSO4] > EtAc > [ChCl][Gly] > [ChCl][AA] > EtOH > HAc > water”.

Use the above lines, instead of:

[EMIM][EtSO4] < [EMIM][HSO4] < EtAc < [ChCl][Gly] < [ChCl][AA] < EtOH < HAc < water.

In Section 4.2, Para 3, Line 3: the following line has been corrected as:

“It can be observed that the V E values are positive for the binary mixtures of EtOH with EtAc, DES1 {[ChCl][2AA]}, and DES2 [ChCl][2Gly] over the entire composition range at all the studied temperatures”.

Use the above lines, instead of:

“It can be observed that the V E values are positive for the binary mixtures of EtOH with EtAc, [EMIM][HSO4], [EMIM][EtSO4], [ChCl][AA], and [ChCl][Gly] over the entire composition range at all the studied temperatures”.

In Section 4.2, Para 4, Line 7: The following line has been corrected as:

“The maximum of excess molar volume is 3.6466 cm3 mol−1 at x1 = 0.5014 for EtOH + [ChCl][2Gly], 1.2227 cm3 mol−1 at x1 = 0.5010 for EtOH+ [Ch-Cl][2AA], and EtOH + EtAc is 0.1102 cm3 mol−1 at x1 = 0.5013, respectively, at 293.15 K. The V E values follow the order: [Ch-Cl][Gly] > [Ch-Cl][HAc] > EtAc with ethanol”.

Use the above lines, instead of:

“The maximum of excess molar volume is 15.450 cm3/mol at x1 = 0.5 for EtOH + [EMIM][EtSO4], 14.483 cm3 mole−1 at x1 = 0.6 for EtOH+ [EMIM][HSO4], 5.714 cm3 mole−1 at x1 = 0.4 for EtOH + [Ch-Cl][Gly], 1.785 cm3 mole−1 at x1 = 0.4 for EtOH + [Ch-Cl][HAc], and EtOH + EtAc is 1.512 cm3 mole−1 at x1 = 0.4, respectively. The V E values follow the order: [EMIM][EtSO4] > [EMIM][HSO4] > [Ch-Cl][Gly] > [Ch-Cl][HAc] > EtAc.”

In Section 4.2, Para 5, Line 1: The following line has been corrected as:

“EtOH + AA, EtOH + water, EtAc + AA, EtOH + [EMIM][EtSO4], and EtOH + [EMIM][HSO4] exhibit negative deviations from ideality over the whole composition range at all the studied temperatures. The minimum of V E shift from the mole fraction range, x1 = 0.5003 (−1.1830 cm3 mol−1) for EtOH + water, x1 = 0.4021 (−1.4196 cm3 mol−1) for EtAc + AA, −0.6036 cm3 mol−1 at x1 = 0.7011 for EtOH + [EMIM][EtSO4], −1.588 cm3 mol−1 at x1 = 0.4022 for EtOH + [EMIM][HSO4], and x1 = 0.5017 (−0.5035 cm3 mol−1) for EtOH + AA, respectively. Here, the V E values of the binary micture of EtOH + water are more negative when compared to the mixture of EtOH + AA and EtAc + AA”.

Use the above lines, instead of;

“EtOH + HAc, EtOH + water and EtAc + HAc exhibit negative deviations from ideality over the whole composition range at all the studied temperatures. The minimum of V E shift from the mole fraction range 0.5 (−3.485 cm3 mole−1) for EtOH + water, EtAc + HAc (−1.763 cm3 mole−1) and 0.3 (−0.489 cm3 mole−1) for EtOH + HAc, respectively. Here, the V E values of the binary micture of EtOH + water are more negative when compared to the mixture of EtOH + HAc and EtAc + HAc”.

Figures 2, 3, and 4 have been revised. The following figures should be used in place of the original Figures 2, 3, and 4.

Table 4 has been revised. The following table should be used in place of the original Table 4.

Table 5 has been revised for EtOH + EtAc, ethanol (1) + [EMIM][EtSO4] (2), and ethanol + water mixtures of RK fitting values. The following table should be used in place of the original Table 5.

Table 6 has been revised. The following table should be used in place of the original Table 6.

Table S1 has been revised. The following table should be used in place of the original Table S1.

Table S1: The density correlation parameters a, b, and R2 for all the studied systems.

Table S4 has been revised. The following table should be used in place of the original Table S4.

Table S4: Excess molar volume of ethanol(1)+water(2), ethanol (1) +acetic acid (2), ethyl Acetate (1) + Acetic Acid (2), ethanol (1) +ethyl acetate (2), ethanol (1) + DES-1(AA) (2), ethanol (1) + DES-2(Gly), ethanol (1) + [EMIM][EtSO4] (2) and ethanol (1) + [EMIM][HSO4] (2) over the entire mole fractions and at different temperatures.

Table S5 has been revised. The following table should be used in place of the original Table S5.

Table S5: The partial molar volume (cm3/mole), excess partial molar volume (cm3/mole) and apparent molar volume (cm3/mole) of individual compounds at different temperatures and 1 atm.

Standard uncertainty: u (T) = 0.01 K, u(p)=0.01MPa, u (ρ) = 0.0001 g cm−3 and for V i ¯ , V ¯ i E , V i , = 0.002 cm3 mole−1 (0.95 level of confidence).

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期刊介绍: Asia-Pacific Journal of Chemical Engineering is aimed at capturing current developments and initiatives in chemical engineering related and specialised areas. Publishing six issues each year, the journal showcases innovative technological developments, providing an opportunity for technology transfer and collaboration. Asia-Pacific Journal of Chemical Engineering will focus particular attention on the key areas of: Process Application (separation, polymer, catalysis, nanotechnology, electrochemistry, nuclear technology); Energy and Environmental Technology (materials for energy storage and conversion, coal gasification, gas liquefaction, air pollution control, water treatment, waste utilization and management, nuclear waste remediation); and Biochemical Engineering (including targeted drug delivery applications).
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Issue Information Correction to “Investigation of molecular interaction, performance of green solvent in esterification of ethanol and acetic acid at 298.15 K and at 1 atm” Issue Information Experimental studies on mechanism whereby premixed chamber length and equivalence ratio collaboratively influence self-excited thermoacoustic instability Experimental study on sloshing mechanical characteristics in a partially filled storage tank
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