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Miscellaneous Fuel

at143a.txt Knystautas (1982) [56]  

Category:	critical tube	Fuel:	C2H6
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1

at137h.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C2H6
Sub-Category:		Oxidizer:	O2
Initial Pressure:	30-203 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at137i.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C3H8
Sub-Category:		Oxidizer:	O2
Initial Pressure:	23-96 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at137j.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C3H6
Sub-Category:		Oxidizer:	O2
Initial Pressure:	20-132 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at66d.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C2H6
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1.4

at66e.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C3H8
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1.43

at66f.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	C3H6
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1.5

mk22e.txt Moen (1984) [84]  

Category:	critical tube	Fuel:	C2H6
Sub-Category:		Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1.05, 1.25

Edited Last: May 27, 2002
jeshep@galcit.caltech.edu