TY - GEN
T1 - High-pressure phase behaviour of the system linear low density polyethylene + N-hexane + ethylene
T2 - Experimental results and modelling
AU - Krenz, Ryan
AU - De Loos, Theo W.
AU - Heidemann, Robert A.
PY - 2005
Y1 - 2005
N2 - Experimental bubble point curves, cloud point curves, and liquid-liquid-vapor boundary curves are presented for the linear low density polyethylene (LLDPE) + n-hexane + ethylene system. The experiments were conducted at process conditions (360-510 K and up to 15 MPa). The liquid-liquid-vapor boundary was measured up to a temperature where a three phase transition was no longer observed near a liquid-vapour critical point. The experiments were modeled with the modified Sanchez-Lacombe (MSL) EOS. Linearly temperature dependent binary interaction parameters were found for LLDPE + ethylene and LLDPE + n-hexane. The LLDPE + n-hexane binary interaction parameters were used to calculate the cloud points of two LLDPE + n-hexane systems reported by others. The LLDPE samples in these other systems had similar molecular structures but different molar mass distributions. The MSL equation provided a qualitative representation of the phase behavior of all three systems. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).
AB - Experimental bubble point curves, cloud point curves, and liquid-liquid-vapor boundary curves are presented for the linear low density polyethylene (LLDPE) + n-hexane + ethylene system. The experiments were conducted at process conditions (360-510 K and up to 15 MPa). The liquid-liquid-vapor boundary was measured up to a temperature where a three phase transition was no longer observed near a liquid-vapour critical point. The experiments were modeled with the modified Sanchez-Lacombe (MSL) EOS. Linearly temperature dependent binary interaction parameters were found for LLDPE + ethylene and LLDPE + n-hexane. The LLDPE + n-hexane binary interaction parameters were used to calculate the cloud points of two LLDPE + n-hexane systems reported by others. The LLDPE samples in these other systems had similar molecular structures but different molar mass distributions. The MSL equation provided a qualitative representation of the phase behavior of all three systems. This is an abstract of a paper presented at the AIChE Annual Meeting and Fall Showcase (Cincinnati, OH 10/30/2005-11/4/2005).
UR - http://www.scopus.com/inward/record.url?scp=33646746663&partnerID=8YFLogxK
M3 - Conference contribution
AN - SCOPUS:33646746663
SN - 0816909962
SN - 9780816909964
T3 - AIChE Annual Meeting Conference Proceedings
BT - 05AIChE
PB - American Institute of Chemical Engineers
ER -