Detonation Database -- Critical Tube Diameter

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Critical Tube Diameter

at161a.txt Bauer (1984) [10]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 400-2200 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.08

at161b.txt Bauer (1984) [10]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 200-1200 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.09

at161c.txt Bauer (1984) [10]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 200-1100 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.15

at161d.txt Bauer (1984) [10]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 500-1900 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.09

at162a.txt Bauer (1984) [10]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 350-880 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 3

at162b.txt Bauer (1984) [10]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 150-600 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 3

at162c.txt Bauer (1984) [10]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 100-400 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 3

at163a.txt Bauer (1984) [10]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 100 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.05

mk23a.txt Guirao (1982) [42]

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) [42]

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

at71a.txt Knystautas (1982) [48]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at72a.txt Knystautas (1982) [48]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

mk142a.txt Knystautas (1982) [48]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at143a.txt Knystautas (1982) [48]

Category: critical tube Fuel: C2H6

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at147a.txt Knystautas (1982) [48]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at147b.txt Matsui (1979) [68]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1.3

at147c.txt Matsui (1979) [68]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.3

at147d.txt Matsui (1979) [68]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.3

at31c.txt Rinnan (1982) [87]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 0.6-.78

at56a.txt Makris (1994) [65]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: .6-1.2

at56c.txt Makris (1994) [65]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: K Equivalence Ratio: .5-2.7

at137g.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 14.6-101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

at75a.txt Matsui (1979) [68]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

at22a4.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1.67

at66b.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.67

at66a.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at137h.txt Matsui (1979) [68]

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) [68]

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) [68]

Category: critical tube Fuel: C3H6

Sub-Category: Oxidizer: O2

Initial Pressure: 20-132 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

mk137k.txt Matsui (1979) [68]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 101-184 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

at56d.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

at80b.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1.5

at80c.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 2

at72c.txt Matsui (1979) [68]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

at66d.txt Matsui (1979) [68]

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) [68]

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) [68]

Category: critical tube Fuel: C3H6

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.5

at66c.txt Matsui (1979) [68]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1.5

at75b.txt Moen (1985) [74]

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) [74]

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) [74]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 80 kPa Diluent: CO2

Initial Temperature: 293 K Equivalence Ratio: 1

at22a1.txt Moen (1984) [71]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 0.6

at22b.txt Moen (1984) [71]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 0.6

at22c.txt Moen (1982) [72]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: .7-1

at77a.txt Moen (1985) [74]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent: CF4

Initial Temperature: 293 K Equivalence Ratio: 0.88

at77b.txt Moen (1985) [74]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent: CF3Br

Initial Temperature: 293 K Equivalence Ratio: 0.88

at77c.txt Moen (1985) [74]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent: CF3Br

Initial Temperature: 293 K Equivalence Ratio: 0.88

at77d.txt Moen (1985) [74]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent: CO2

Initial Temperature: 293 K Equivalence Ratio: 0.88

at20a.txt Rinnan (1982) [87]

Category: critical tube Fuel: C2H2

Sub-Category: Oxidizer: Air

Initial Pressure: 101.3 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 0.45-0.75

at43.txt Plaster (1991) [84]

Category: critical tube Fuel: H2

Sub-Category: Oxidizer: O2

Initial Pressure: 100 kPa Diluent:

Initial Temperature: 100 K Equivalence Ratio: 0.25-3

at200c.txt Moen (1981) [70]

Category: critical tube Fuel: C2H4

Sub-Category: Oxidizer: O2

Initial Pressure: 101.3 kPa Diluent: N2

Initial Temperature: 293 K Equivalence Ratio: 1

att2.txt Zeldovich (1956) [112]

Category: critical tube Fuel: CH4

Sub-Category: Oxidizer: O2

Initial Pressure: 106.7 kPa Diluent:

Initial Temperature: 293 K Equivalence Ratio: 1

mikek@galcit.caltech.edu

Category:	critical tube	Fuel:	CH4
Sub-Category:		Oxidizer:	O2
Initial Pressure:	400-2200 kPa	Diluent:	N2
Initial Temperature:	293 K	Equivalence Ratio:	1.08