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000 nam k
001 2210080166958
005 20140714130605
007 ta
008 920309s1991 bnka FB 000 kor
040 a221008
041 akorbeng
056 a570.32424
100 a정상훈
245 00 a2-프로판올-물-용매계에서의 첨가제의 영향에 관한 연구 /d鄭祥勳
260 a부산:b東亞大學校 大學院,c1991
300 a56 장:b삽도;c26 cm
502 a학위논문(석사)--b東亞大學校 大學院:c化學工學科,d1991. 2
520 b영문초록 : The ternary liquid-liquid equilibria and the salt effect on ternary liquid-liquid equilibria were studied as following. Binodal curve, tie line, plait point, distribution coefficient, and selectivity in the equilibrium of quarternary liquid-liquid system with calcium chloride salt at 25℃ were determined to find the extraction effect, experimental data of phase equilibrium were correlated with NRTL and UNIQUAC model, and parameters in the models were calculated. The following results were obtained for the utilization of the basic data in the design of extraction apparatus. 1. As the temperature of system increased, the binodal corves rose and the effect of solvent extraction was improved. 2. Consistency of experimental tie line data for ternary systems were examined using Othmer Tobias and Eisen-Joffe equations. 3. As the concentration of CaCl_(2) increased, the binodal curve rose plait point disappeared, and solvent extraction was well done around plait point. 4. The calculated phase equilibrium data were satisfactory within RMSD values as shown in table 5. 5. When the concentration of CaCl_(2) increased, the distribution coefficient and selectivity increased, and the effect of solvent was improved.
650 a용매추출
856 adonga.dcollection.netuhttp://donga.dcollection.net/jsp/common/DcLoOrgPer.jsp?sItemId=000002141657
940 a이-프로판올-물-용매계에서의 첨가제의 영향에...
950 a비매품b₩2600c(추정가)
950 aFB
2-프로판올-물-용매계에서의 첨가제의 영향에 관한 연구
Material type
학위논문 동서
Title
2-프로판올-물-용매계에서의 첨가제의 영향에 관한 연구
Author's Name
Publication
Physical Description
56 장: 삽도; 26 cm
학위논문주기
학위논문(석사)-- 東亞大學校 大學院: 化學工學科, 1991. 2
Keyword
영문초록 : The ternary liquid-liquid equilibria and the salt effect on ternary liquid-liquid equilibria were studied as following. Binodal curve, tie line, plait point, distribution coefficient, and selectivity in the equilibrium of quarternary liquid-liquid system with calcium chloride salt at 25℃ were determined to find the extraction effect, experimental data of phase equilibrium were correlated with NRTL and UNIQUAC model, and parameters in the models were calculated. The following results were obtained for the utilization of the basic data in the design of extraction apparatus. 1. As the temperature of system increased, the binodal corves rose and the effect of solvent extraction was improved. 2. Consistency of experimental tie line data for ternary systems were examined using Othmer Tobias and Eisen-Joffe equations. 3. As the concentration of CaCl_(2) increased, the binodal curve rose plait point disappeared, and solvent extraction was well done around plait point. 4. The calculated phase equilibrium data were satisfactory within RMSD values as shown in table 5. 5. When the concentration of CaCl_(2) increased, the distribution coefficient and selectivity increased, and the effect of solvent was improved.
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Call no. : 570.324 정51이
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