Browse > Article

Phase Behavior of Poly(ethylene-co-norbornene) in $C_6$ Hydrocarbon Solvents: Effect of Polymer Concentration and Solvent Structure  

Kwon, Hyuk-Sung (Department of Chemical Engineering, Dong-A University)
Lee, Sang-Ho (Department of Chemical Engineering, Dong-A University)
Publication Information
Macromolecular Research / v.11, no.4, 2003 , pp. 231-235 More about this Journal
Abstract
Phase behavior information is necessary for accomplishing homogeneous copolymerization to obtain high yield of copolymers and prevent a fouling problem. Cloud-point data to $160^{\circ}C$ and 1,450 bar are presented for five $C_6$ hydrocarbon solvents, normal hexane, 2,2-dimethyl butane, 2,3-dimethyl butane, 2-methyl pentane, and 3-methyl pentane, with poly(ethylene-co-53 mol% norbornene) ($PEN_{53}$). The pressure-concentration isotherms measured for $PEN_{53}$/n-hexane have maximums that range between 5 and 12 wt% $PEN_{53}$. The cloud-point curves for $PEN_{53}$ all have negative slopes that decrease in pressure with temperatures. The single-phase region of $PEN_{53}$ in n-hexane is larger than the regions in 2,2-dimethyl butane, 2,3-dimethyl butane, 2-methyl pentane, and 3-methyl pentane. The cloud-point curve of $PEN_{53}$ in 2,2-dimethyl butane is located at higher temperatures and pressures than the curve in 2,3-dimethyl butane due to the reduced dispersion interactions with and limited access of 2,2-dimethyl butane to the copolymer. Similar cloud-point behavior is observed for $PEN_{53}$ in 2-methyl pentane and 3-methyl pentane.
Keywords
poly(ethylene-co-norbornene); phase behavior; high pressures;
Citations & Related Records

Times Cited By Web Of Science : 1  (Related Records In Web of Science)
Times Cited By SCOPUS : 1
연도 인용수 순위
1 M. T. Ratzscn, P. Wagner, C. Wohlfarth, and S. Gleditzsch, Acta Polymerica, 34, 340 (1983)
2 S.-H. Lee, M. A. LoStracco, B. M. Hasch, and M. A. McHugh, J. Phys. Chem., 98, 4055 (1994)
3 C. A. Irani and C. Cozewith, J. Appl. Polym. Sci., 31, 1879 (1986)
4 Cyclic Olefin Copolymers, 94/95S5, Chem. Systems Inc., New York, 1996, Chapter IV
5 M. T. Ratzsch, P. Wagner, C. Wohlfarth, and D. Heise, Acta Polymerica, 33, 463 (1982)
6 R. R. Lamonte and D. McNalley, Plastics Engineering, 56, 51 (2000)
7 J. A. Abara, D. W. Jennings, W. B. Kay, and A. S. Teja, J. Chem. Eng. Data, 33, 242 (1988)
8 G. Khanarian, Polym. Eng. Sci., 40, 2590 (2000)
9 T. Weller, D. Schulz, and D. McNally, Plastics Technology, 43, 58 (1997)
10 C.-K. Y. Thomas, H.-Y. T. Stanley, S.-F. Wang, and C.-C. Juan, Composition Sci. and Technol., 62, 655 (2002)
11 M. A. McHugh and V. J. Krukonis, Supercritical Fluid Extraction: Principles and Practice, 2nd ed., Butterworths, Stoneham, MA, U.S.A., 1994, pp 64
12 T. E. Daubert, J. Chem. Eng. Data, 41, 365 (1996)
13 G. Khanarian, Opt. Eng., 40, 1024 (2001)
14 R. C. Reid, J. M. Prausnitz, and B. E. Poling, The Properties of Gases and Liquids, 4th ed., McGraw-Hill, New York, U.S.A., 1987, pp 656