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Showing results 1 to 9 of 9

Issue DateTitleAuthor(s)
1996-12-23Catalytic performance of Cs2.5Fe0.08H1.26PVMo11O40 for direct oxidation of lower alkanesMizuno, N; Suh, DJ; Han, W; Kudo, T
2001-06Comparison of protonated zeolites with various dimensionalities for the liquid phase alkylation of i-butane with 2-buteneYoo, K; Burckle, EC; Smirniotis, PG
2016-01Effect of oxychlorination treatment on the regeneration of Pt-Sn/Al2O3 catalyst for propane dehydrogenationKim, Ga Hee; Jung, Kwang-Deog; Kim, Won-Il; Um, Byung-Hwan; Shin, Chae-Ho; Oh, Kyeongseok; Koh, Hyoung Lim
2004-07Measurement of vapor-liquid equilibria for the binary mixture of pentafluoroethane (HFC-125)+propane (R-290)Lim, JS; Park, JY; Lee, KS; Kim, JD; Lee, BG
2002-01-30Phase equilibria of 1,1,1-trifluoroethane (HFC-143a)+1,1,1,2-tetrafluoroethane (HFC-134a), and +1,1-difluoroethane (HFC-152a) at 273.15, 293.15, 303.15, and 313.15 KLim, JS; Park, JY; Lee, BG; Lee, YW
2001-11Phase equilibria of CFC alternative refrigerant mixtures. Binary systems of trifluoromethane (HFC-23)+1,1,1,2-tetrafluoroethane (HFC-134a) and trifluoromethane (HFC-23)+1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) at 283.15 and 293.15 KLim, JS; Park, KH; Lee, BG; Kim, JD
2002-05Phase equilibria of HFC mixtures: Binary mixtures of trifluoromethane plus 1,1-difluoroethane and trifluoromethane plus 1,1,1-trifluoroethane at 283.15 and 293.15 KLim, JS; Park, KH; Lee, BG
2007-11Vapor-liquid equilibria for propane (R-290)+1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) at various temperaturesLim, Jong Sung; Seong, Gimyeong; Roh, Hee-Kook; Lee, Byung Gwon
2003-07Vapor-liquid equilibria for the binary system difluoromethane (HFC-32) plus propane (HC-290) at seven temperatures [(268.15, 278.15, 283.15, 288.15, 298.15, 308.15, and 318.15) K]Lee, BG; Yang, WJ; Kim, JD; Lim, JS

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