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H2 Fuel

mk23a.txt Guirao (1982) [48]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.85-1.86

mk23b.txt Guirao (1982) [48]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.85-1.86

at72a.txt Knystautas (1982) [56]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1

at56a.txt Makris (1994) [77]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	.6-1.2

at75a.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at72c.txt Matsui (1979) [80]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	101.3 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1

at75b.txt Moen (1985) [87]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	40-80 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at75d.txt Moen (1985) [87]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	40-80 kPa	Diluent:	CF3Br
Initial Temperature:	293 K	Equivalence Ratio:	1

at75c.txt Moen (1985) [87]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	80 kPa	Diluent:	CO2
Initial Temperature:	293 K	Equivalence Ratio:	1

at43.txt Plaster (1991) [99]  

Category:	critical tube	Fuel:	H2
Sub-Category:		Oxidizer:	O2
Initial Pressure:	100 kPa	Diluent:
Initial Temperature:	100 K	Equivalence Ratio:	0.25-3

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