Vapor–Liquid Equilibria Prediction and Validation of Binary Systems Containing SiCl4 by Using the MOSCED Model
The measurement of olyzed VLE data of some binary system containing a deliquescent constituent is often difficult and time consuming. The MOSCED model was employed to predict the phase equilibria of the SiCl 4 –CS 2 and SiCl 4 –C 2 H 4 Cl 2 binary systems, which are easily hydrolyzed during the meas...
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Veröffentlicht in: | Journal of solution chemistry 2021-08, Vol.50 (8), p.1037-1050 |
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creator | Xiang, Xiaoyan Liu, Hao Shao, Yufeng Xia, Wentang Yuan, Xiaoli |
description | The measurement of olyzed VLE data of some binary system containing a deliquescent constituent is often difficult and time consuming. The MOSCED model was employed to predict the phase equilibria of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems, which are easily hydrolyzed during the measuring process. The infinite dilution activity coefficients and activity coefficients of components of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were calculated. Then, VLE data and the VLE phase diagram of these binary systems were calculated using the trial-and-error method based on the obtained activity coefficients of the components of these binary systems. The calculated results are consistent with the experimental data within the allowable error. The result shows that the SiCl
4
–CS
2
binary mixtures have closer bubble and dew point curves than SiCl
4
–C
2
H
4
Cl
2
binary mixtures in the
T
–
x
–y phase diagram, which means that the SiCl
4
–C
2
H
4
Cl
2
system is much more easily separated by distillation. Meanwhile, the VLE data and VLE phase diagram of SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were used to guide the process of separating high-quality SiCl
4
from liquid waste originating from the titanium metallurgical industry. |
doi_str_mv | 10.1007/s10953-021-01096-1 |
format | Article |
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4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems, which are easily hydrolyzed during the measuring process. The infinite dilution activity coefficients and activity coefficients of components of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were calculated. Then, VLE data and the VLE phase diagram of these binary systems were calculated using the trial-and-error method based on the obtained activity coefficients of the components of these binary systems. The calculated results are consistent with the experimental data within the allowable error. The result shows that the SiCl
4
–CS
2
binary mixtures have closer bubble and dew point curves than SiCl
4
–C
2
H
4
Cl
2
binary mixtures in the
T
–
x
–y phase diagram, which means that the SiCl
4
–C
2
H
4
Cl
2
system is much more easily separated by distillation. Meanwhile, the VLE data and VLE phase diagram of SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were used to guide the process of separating high-quality SiCl
4
from liquid waste originating from the titanium metallurgical industry.</description><identifier>ISSN: 0095-9782</identifier><identifier>EISSN: 1572-8927</identifier><identifier>DOI: 10.1007/s10953-021-01096-1</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Activity coefficients ; Binary mixtures ; Binary system ; Binary systems ; Chemistry ; Chemistry and Materials Science ; Condensed Matter Physics ; Dew point ; Dilution ; Distillation ; Geochemistry ; Hygroscopicity ; Industrial Chemistry/Chemical Engineering ; Inorganic Chemistry ; Liquid wastes ; Liquid-vapor equilibrium ; Mathematical models ; Metallurgy ; Oceanography ; Phase diagrams ; Phase equilibria ; Physical Chemistry ; Silicon tetrachloride ; Titanium ; Trial and error methods</subject><ispartof>Journal of solution chemistry, 2021-08, Vol.50 (8), p.1037-1050</ispartof><rights>The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2021</rights><rights>The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2021.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><cites>FETCH-LOGICAL-c270t-ed64cc107f36e16d2c3aed4bb4d87fa149b67a3694775df851e1e24a306f24bc3</cites><orcidid>0000-0002-7080-7980</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://link.springer.com/content/pdf/10.1007/s10953-021-01096-1$$EPDF$$P50$$Gspringer$$H</linktopdf><linktohtml>$$Uhttps://link.springer.com/10.1007/s10953-021-01096-1$$EHTML$$P50$$Gspringer$$H</linktohtml><link.rule.ids>314,780,784,27922,27923,41486,42555,51317</link.rule.ids></links><search><creatorcontrib>Xiang, Xiaoyan</creatorcontrib><creatorcontrib>Liu, Hao</creatorcontrib><creatorcontrib>Shao, Yufeng</creatorcontrib><creatorcontrib>Xia, Wentang</creatorcontrib><creatorcontrib>Yuan, Xiaoli</creatorcontrib><title>Vapor–Liquid Equilibria Prediction and Validation of Binary Systems Containing SiCl4 by Using the MOSCED Model</title><title>Journal of solution chemistry</title><addtitle>J Solution Chem</addtitle><description>The measurement of olyzed VLE data of some binary system containing a deliquescent constituent is often difficult and time consuming. The MOSCED model was employed to predict the phase equilibria of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems, which are easily hydrolyzed during the measuring process. The infinite dilution activity coefficients and activity coefficients of components of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were calculated. Then, VLE data and the VLE phase diagram of these binary systems were calculated using the trial-and-error method based on the obtained activity coefficients of the components of these binary systems. The calculated results are consistent with the experimental data within the allowable error. The result shows that the SiCl
4
–CS
2
binary mixtures have closer bubble and dew point curves than SiCl
4
–C
2
H
4
Cl
2
binary mixtures in the
T
–
x
–y phase diagram, which means that the SiCl
4
–C
2
H
4
Cl
2
system is much more easily separated by distillation. Meanwhile, the VLE data and VLE phase diagram of SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were used to guide the process of separating high-quality SiCl
4
from liquid waste originating from the titanium metallurgical industry.</description><subject>Activity coefficients</subject><subject>Binary mixtures</subject><subject>Binary system</subject><subject>Binary systems</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Condensed Matter Physics</subject><subject>Dew point</subject><subject>Dilution</subject><subject>Distillation</subject><subject>Geochemistry</subject><subject>Hygroscopicity</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Inorganic Chemistry</subject><subject>Liquid wastes</subject><subject>Liquid-vapor equilibrium</subject><subject>Mathematical models</subject><subject>Metallurgy</subject><subject>Oceanography</subject><subject>Phase diagrams</subject><subject>Phase equilibria</subject><subject>Physical Chemistry</subject><subject>Silicon tetrachloride</subject><subject>Titanium</subject><subject>Trial and error methods</subject><issn>0095-9782</issn><issn>1572-8927</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp9kM1OAyEUhYnRxFp9AVckrlFgGJhZ6lh_kjY1qe2WMANTaabDFKaL7nwH39AnkbYm7twAJ5xzbu4HwDXBtwRjcRcIztMEYUoQjk-OyAkYkFRQlOVUnIIBjv8oFxk9BxchrHDUWc4GoFuozvnvz6-x3WythqN4Nrb0VsE3b7SteutaqFoNF6qxWh2kq-GDbZXfwdku9GYdYOHaXtnWtks4s0XDYLmD87CX_YeBk-msGD3CidOmuQRntWqCufq9h2D-NHovXtB4-vxa3I9RRQXukdGcVRXBok64IVzTKlFGs7JkOhO1IiwvuVAJz5kQqa6zlBhiKFMJ5jVlZZUMwc2xt_NuszWhlyu39W0cKWnKIyOacRZd9OiqvAvBm1p23q7jZpJguScrj2RlJCsPZCWJoeQYCtHcLo3_q_4n9QPOqnyW</recordid><startdate>20210801</startdate><enddate>20210801</enddate><creator>Xiang, Xiaoyan</creator><creator>Liu, Hao</creator><creator>Shao, Yufeng</creator><creator>Xia, Wentang</creator><creator>Yuan, Xiaoli</creator><general>Springer US</general><general>Springer Nature B.V</general><scope>AAYXX</scope><scope>CITATION</scope><orcidid>https://orcid.org/0000-0002-7080-7980</orcidid></search><sort><creationdate>20210801</creationdate><title>Vapor–Liquid Equilibria Prediction and Validation of Binary Systems Containing SiCl4 by Using the MOSCED Model</title><author>Xiang, Xiaoyan ; Liu, Hao ; Shao, Yufeng ; Xia, Wentang ; Yuan, Xiaoli</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c270t-ed64cc107f36e16d2c3aed4bb4d87fa149b67a3694775df851e1e24a306f24bc3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2021</creationdate><topic>Activity coefficients</topic><topic>Binary mixtures</topic><topic>Binary system</topic><topic>Binary systems</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Condensed Matter Physics</topic><topic>Dew point</topic><topic>Dilution</topic><topic>Distillation</topic><topic>Geochemistry</topic><topic>Hygroscopicity</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Inorganic Chemistry</topic><topic>Liquid wastes</topic><topic>Liquid-vapor equilibrium</topic><topic>Mathematical models</topic><topic>Metallurgy</topic><topic>Oceanography</topic><topic>Phase diagrams</topic><topic>Phase equilibria</topic><topic>Physical Chemistry</topic><topic>Silicon tetrachloride</topic><topic>Titanium</topic><topic>Trial and error methods</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Xiang, Xiaoyan</creatorcontrib><creatorcontrib>Liu, Hao</creatorcontrib><creatorcontrib>Shao, Yufeng</creatorcontrib><creatorcontrib>Xia, Wentang</creatorcontrib><creatorcontrib>Yuan, Xiaoli</creatorcontrib><collection>CrossRef</collection><jtitle>Journal of solution chemistry</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Xiang, Xiaoyan</au><au>Liu, Hao</au><au>Shao, Yufeng</au><au>Xia, Wentang</au><au>Yuan, Xiaoli</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Vapor–Liquid Equilibria Prediction and Validation of Binary Systems Containing SiCl4 by Using the MOSCED Model</atitle><jtitle>Journal of solution chemistry</jtitle><stitle>J Solution Chem</stitle><date>2021-08-01</date><risdate>2021</risdate><volume>50</volume><issue>8</issue><spage>1037</spage><epage>1050</epage><pages>1037-1050</pages><issn>0095-9782</issn><eissn>1572-8927</eissn><abstract>The measurement of olyzed VLE data of some binary system containing a deliquescent constituent is often difficult and time consuming. The MOSCED model was employed to predict the phase equilibria of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems, which are easily hydrolyzed during the measuring process. The infinite dilution activity coefficients and activity coefficients of components of the SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were calculated. Then, VLE data and the VLE phase diagram of these binary systems were calculated using the trial-and-error method based on the obtained activity coefficients of the components of these binary systems. The calculated results are consistent with the experimental data within the allowable error. The result shows that the SiCl
4
–CS
2
binary mixtures have closer bubble and dew point curves than SiCl
4
–C
2
H
4
Cl
2
binary mixtures in the
T
–
x
–y phase diagram, which means that the SiCl
4
–C
2
H
4
Cl
2
system is much more easily separated by distillation. Meanwhile, the VLE data and VLE phase diagram of SiCl
4
–CS
2
and SiCl
4
–C
2
H
4
Cl
2
binary systems were used to guide the process of separating high-quality SiCl
4
from liquid waste originating from the titanium metallurgical industry.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s10953-021-01096-1</doi><tpages>14</tpages><orcidid>https://orcid.org/0000-0002-7080-7980</orcidid></addata></record> |
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subjects | Activity coefficients Binary mixtures Binary system Binary systems Chemistry Chemistry and Materials Science Condensed Matter Physics Dew point Dilution Distillation Geochemistry Hygroscopicity Industrial Chemistry/Chemical Engineering Inorganic Chemistry Liquid wastes Liquid-vapor equilibrium Mathematical models Metallurgy Oceanography Phase diagrams Phase equilibria Physical Chemistry Silicon tetrachloride Titanium Trial and error methods |
title | Vapor–Liquid Equilibria Prediction and Validation of Binary Systems Containing SiCl4 by Using the MOSCED Model |
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