US2023028449A1PendingUtilityA1
Compositions and methods of producing rocket propellants with enhanced cryogenic cooling, thermal stability, and thrust efficiency performance
Est. expiryDec 30, 2039(~13.4 yrs left)· nominal 20-yr term from priority
Inventors:Anton HuntCynthia Natalie GinestraJoanna Margaret BauldreayPaul Franciscus BogersElise Marie Miner
C06D 5/08C06B 47/12
47
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Claims
Abstract
The present disclosure relates to a rocket propellant composition comprising (a) a liquid oxygen; and (b) a hydrocarbon mixture comprising: (i) a hydrogen content from about 14.0 mass % to about 16.0 mass %, by mass of the hydrocarbon mixture; (ii) a kinematic viscosity of from about 5 mm 2 /s to about 8 mm 2 /s at a temperature ranging from about −35° C. to about −33° C.; and (iii) a sulfur content of from about 0 ppm to about 0.1 ppm, by mass of 0 the hydrocarbon mixture.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A rocket propellant composition comprising:
(a) a liquid oxygen; and (b) a hydrocarbon mixture comprising:
(i) a hydrogen content from about 14.0 mass % to about 16.0 mass %, by mass of the hydrocarbon mixture;
(ii) a kinematic viscosity of from about 5 mm 2 /s to about 8 mm 2 /s at a temperature ranging from about −35° C. to about −33° C.; and
(iii) a sulfur content of from about 0 01 ppm to about 0.1 ppm, by mass of the hydrocarbon mixture.
2 . The rocket propellant composition according to claim 1 , wherein a mixture ratio of the liquid oxygen to the hydrocarbon mixture ranges from about 1.8 to about 3.2.
3 . The rocket propellant composition according to claim 1 , wherein a mixture ratio of the liquid oxygen to the hydrocarbon mixture ranges from about 1 to about 4.
4 . The rocket propellant composition according to claim 1 , wherein the hydrogen content ranges from about 15.3 mass % to about 15.9 mass %, by mass of the hydrocarbon mixture.
5 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon mixture further comprises one or more of a branched paraffin, a straight chain paraffin, a cyclo-paraffin, and combinations thereof.
6 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon further comprises a flash point according to ASTM D93 of at least about 60° C. at 1 ATM.
7 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon mixture further has a distillation initial boiling point of at least about 180° C.
8 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon mixture further has a density ranging from about 0.7 kg/m3 to about 0.9 kg/m3 at a temperature of about 15° C.
9 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon mixture further comprises a freezing point that is lower than about −45° C.
10 . The rocket propellant composition according to claim 1 , wherein the hydrocarbon mixture is a Fischer-Tropsch product.
11 . The rocket propellant composition according to claim 1 , wherein the rocket propellant composition comprises a c* value of at least about 1% gain versus RP-1/RP-2 under set operating conditions.
12 . A method for producing a rocket propellant composition, the method comprising:
(a) providing a liquid oxygen; and (b) providing a hydrocarbon mixture comprising:
(i) a hydrogen content from about 15.0 mass % to about 16.0 mass %, by mass of the hydrocarbon mixture;
(ii) a kinematic viscosity of from about 5 mm 2 /s to about 7 mm 2 /s at a temperature ranging from about −35° C. to about −33° C.; and
(iii) a sulfur content of from about 0.01 ppm to about 0.1 mass %, by mass of the hydrocarbon mixture.
13 . The method according to claim 12 , wherein a mixture ratio of the liquid oxygen to the hydrocarbon mixture ranges from about 1 to about 4.
14 . The method according to claim 12 , wherein a mixture ratio of the liquid oxygen to the hydrocarbon mixture ranges from about 1.8 to about 3.2.
15 . The method according to claim 12 , further comprising combining the liquid oxygen and the hydrocarbon mixture at a burner plate.
16 . The method according to claim 12 , wherein the hydrogen content ranges from about 15.3 mass % to about 15.9 mass %, by mass of the hydrocarbon mixture.
17 . The method according to claim 12 , wherein the hydrocarbon further comprises a flash point according to ASTM D93 of at least about 60° C. at 1 ATM.
18 . The method according to claim 12 , wherein the hydrocarbon mixture further comprises a distillation initial boiling point of at least about 190° C.
19 . The method according to claim 12 , wherein the rocket fuel composition further comprises a density ranging from about 0.7 kg/m3 to about 0.8 kg/m3 at a temperature of about 15° C.
20 . The method according to claim 12 , wherein the hydrocarbon mixture is a Fischer-Tropsch product.
21 . The method according to claim 12 , wherein the rocket propellant composition comprises a c* value of at least about 1% gain versus RP-1/RP-2 under set operating conditions.Join the waitlist — get patent alerts
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