Cell Width

at192a.txt Abid (1991) [1]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.5-12 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at192b.txt Abid (1991) [1]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.2-14 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at33a.txt Anderson (1992) [4]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	26.3-56.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at33b.txt Anderson (1992) [4]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	26.3-56.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at33c.txt Anderson (1992) [4]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	26.3-56.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	0.75

at58a.txt Barthel (1974) [8]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.7-53.3 kPa	Diluent:
Initial Temperature:	298 K	Equivalence Ratio:	1

at58b.txt Barthel (1974) [8]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.7-53.3 kPa	Diluent:	Ar
Initial Temperature:	298 K	Equivalence Ratio:	1

at58c.txt Barthel (1974) [8]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.7-53.3 kPa	Diluent:	Ar
Initial Temperature:	298 K	Equivalence Ratio:	1

at176a.txt Beeson (1991) [11]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at19.txt Benedick (1984) [14]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	82.7 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	.5-.7

at157j.txt Bull (1982) [25]  

Category:	cell size	Fuel:	C2H6
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at157e.txt Bull (1982) [25]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at14.txt Ciccarelli (1994) [27]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	100 kPa	Diluent:
Initial Temperature:	300 K	Equivalence Ratio:	.5-3.3

at15.txt Ciccarelli (1994) [27]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	100 kPa	Diluent:
Initial Temperature:	500 K	Equivalence Ratio:	.35-2.4

at16.txt Ciccarelli (1994) [27]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	100 kPa	Diluent:
Initial Temperature:	650 K	Equivalence Ratio:	.26-2.4

at198d.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at187a.txt Desbordes (1988) [31]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2.5-18.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at187b.txt Desbordes (1988) [31]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4.1-13.2 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at187c.txt Desbordes (1988) [31]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4.1-45.6 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at187d.txt Desbordes (1988) [31]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.1-0.4 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at166c.txt Desbordes (1986) [34]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2.5-16.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at166b.txt Desbordes (1986) [34]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4.1-12.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at197a.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at197b.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at197c.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	Kr
Initial Temperature:	293 K	Equivalence Ratio:	1

at198a.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at198b.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at198c.txt Desbordes (1993) [33]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	0.13-1 kPa	Diluent:	Kr
Initial Temperature:	293 K	Equivalence Ratio:	1

at166a.txt Edwards (1978) [37]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2-9.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

H2-Air1.txt Guirao (1982) [42]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.54 - 2.03

at182a.txt Knystautas (1988) [47]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Cl2
Initial Pressure:	2.1-24.0 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.56

at182b.txt Knystautas (1988) [47]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Cl2
Initial Pressure:	2.1-24.0 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.67

at182c.txt Knystautas (1988) [47]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Cl2
Initial Pressure:	2.1-24.0 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1.5

at182d.txt Knystautas (1988) [47]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Cl2
Initial Pressure:	2.1-24.0 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at13a.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at13f.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C4H10
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.7 - 1.5

at13e.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C3H8
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.6 - 1.7

at13d.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C2H6
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.8 - 1.3

at157d.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.5 - 2.2

at13b.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.5 - 2.2

js13c.txt Knystautas (1984) [46]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.4 - 3

at149a.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at148a.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at154b.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C4H10
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	6.7-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at150a.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2-12 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	2.5

at150b.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2-12 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	2.5

at151.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2.7-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.625

at152.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C2H6
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at153.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C3H6
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4-12 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at154a.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	C3H8
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	2.7-13.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at74.txt Knystautas (1982) [48]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	5.3-20 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at35a.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at35b.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at37.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	Deuterium
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at38a.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	1.5H2+CO2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	295 K	Equivalence Ratio:	1

at38b.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	2.7H2+CO2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	295 K	Equivalence Ratio:	1

at38c.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	6H2+CO2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	295 K	Equivalence Ratio:	1

at39a.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	H2+H2O
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	353 K	Equivalence Ratio:	1

at39b.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	1.6H2+H2O
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	353 K	Equivalence Ratio:	1

at39c.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	2.7H2+H2O
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	353 K	Equivalence Ratio:	1

at39d.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	6H2+H2O
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	106.6 kPa	Diluent:	He
Initial Temperature:	353 K	Equivalence Ratio:	1

at42a.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	20-150 kPa	Diluent:	He
Initial Temperature:	295 K	Equivalence Ratio:	1

at42b.txt Kumar (1990) [51]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	20-150 kPa	Diluent:	He
Initial Temperature:	295 K	Equivalence Ratio:	1

at199a.txt Laberge (1993) [52]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	8-26.7 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at199c.txt Laberge (1993) [52]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-13.3 kPa	Diluent:
Initial Temperature:	K	Equivalence Ratio:	1

at199d.txt Laberge (1993) [52]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-13.3 kPa	Diluent:
Initial Temperature:	K	Equivalence Ratio:	2.5

at47a.txt Lee (1977) [57]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	5.1-30.4 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at47b.txt Lee (1977) [57]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	20.3-40.5 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at57b.txt Denisov (1959) [28]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	10.1-101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at57a.txt Manzhalei (1974) [67]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	10.1-1013 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at57d.txt Manzhalei (1974) [67]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	30.4-912 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at157h.txt Moen (1984) [71]  

Category:	cell size	Fuel:	C2H6
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1.0-1.3

at157c.txt Moen (1984) [71]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.55-1.1

at157b.txt Moen (1984) [71]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	.5-1

at157f.txt Moen (1984) [71]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

mk157g.txt Moen (1984) [71]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	.5-.7

at157a.txt Moen (1984) [71]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at184b.txt Pedley (1988) [83]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-13 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at184a.txt Pedley (1988) [83]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	7-13 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at5a.txt Stamps (1991) [90]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	25.3 - 152.0 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at5b.txt Stamps (1991) [90]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	20.2 - 253.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.5

at128a.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	15.2-50.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at128b.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4.1-15.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at128c.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	4.1-35.5 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at128d.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	12.2-70.9 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at129c.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.5-101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at129d.txt Voitsekhovskii (1966) [108]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.5-18.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at129e.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.5-18.2 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	0.625

at129f.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	20.3-40.5 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at69a.txt Strehlow (1967) [94]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.1-40.5 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at69b.txt Strehlow (1967) [94]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	6.1-40.5 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

mk61a.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	13.2-32.4 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	0.36

at61b.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	13.2-32.4 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	2.12

at61c.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	13.2-32.4 kPa	Diluent:	3.75Ar+N2
Initial Temperature:	293 K	Equivalence Ratio:	1

at62a.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	5.6-32.4 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at62f.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	18.2-45.6 kPa	Diluent:	He
Initial Temperature:	293 K	Equivalence Ratio:	1

at62c.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	9.1-50.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at62d.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	10.1-55.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at62e.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	10.1-55.7 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at62g.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	23.3-45.6 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at62b.txt Strehlow (1969) [92]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	9.1-40.5 kPa	Diluent:	Ar
Initial Temperature:	293 K	Equivalence Ratio:	1

at65.txt Strehlow (1969) [95]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	1.3-7.3 kPa	Diluent:	Ar
Initial Temperature:	600 - 800 K	Equivalence Ratio:	1

at3a.txt Tieszen (1986) [96]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	150 - 304 kPa	Diluent:
Initial Temperature:	373 K	Equivalence Ratio:	0.35 - 3

at3b.txt Tieszen (1986) [96]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	150 - 304 kPa	Diluent:	steam
Initial Temperature:	373 K	Equivalence Ratio:	.5 - 2

at3c.txt Tieszen (1986) [96]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	150 - 304 kPa	Diluent:	steam
Initial Temperature:	373 K	Equivalence Ratio:	.8 - 2

at3d.txt Tieszen (1986) [96]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	150 - 304 kPa	Diluent:	steam
Initial Temperature:	373 K	Equivalence Ratio:	.93 - 1.04

at4.txt Tieszen (1986) [96]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	298 K	Equivalence Ratio:	0.4 - 5

at172a.txt Tieszen (1991) [97]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	373 K	Equivalence Ratio:	1

at171b.txt Tieszen (1991) [97]  

Category:	cell size	Fuel:	C2H6
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	373 K	Equivalence Ratio:	1

at172d.txt Tieszen (1991) [97]  

Category:	cell size	Fuel:	C2H4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	373 K	Equivalence Ratio:	1

at171a.txt Tieszen (1991) [97]  

Category:	cell size	Fuel:	CH4
Sub-Category:	width	Oxidizer:	Air
Initial Pressure:	101.3 kPa	Diluent:
Initial Temperature:	373 K	Equivalence Ratio:	1

at148c.txt Voitsekhovskii (1966) [108]  

Category:	cell size	Fuel:	C2H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	3.0-30.4 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at21a.txt Desbordes (1990) [32]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	50.7-101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at21b.txt Zitoun (1995) [113]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	50.7-101.3 kPa	Diluent:
Initial Temperature:	293 K	Equivalence Ratio:	1

at21c.txt Zitoun (1995) [113]  

Category:	cell size	Fuel:	H2
Sub-Category:	width	Oxidizer:	O2
Initial Pressure:	50.7-101.3 kPa	Diluent:
Initial Temperature:	123 K	Equivalence Ratio:	1