Nitric acid/UDMH
Agena Engine
Credit - Bell
Propellant Formulation: IRFNA/UDMH. Optimum Oxidiser to Fuel Ratio: 3.00. Temperature of Combustion: 3,225 deg K. Ratio of Specific Heats: 1.23. Density: 1.25 g/cc. Characteristic velocity c: 1,675 m/s (5,495 ft/sec). Isp Shifting: 277 sec. Isp Frozen: 268 sec. Pp Isp Shifting: 346. Mol: 22.00 M (72.00 ft). Isp (sl): 276. Isp (vac): 323.
Oxidiser: Nitric Acid. Oxidiser Density: 1.510 g/cc. Oxidiser Freezing Point: -42 deg C. Oxidiser Boiling Point: 86 deg C.

Drawing on the German World War II Wasserfall rocket, nitric acid (HNO3) became the early storable oxidiser of choice for missiles and upper stages of the 1950's. To overcome various problems with its use, it was necessary to combine the nitric acid with N2O4 and passivation compounds. These formulae were considered extremely secret at the time. The propellant combinations WFNA/ JP-4 and later IRFNA/JP-4 were the first storable systems given serious consideration in the United States. Problems which caused the abandoning of these propellants were the absence of reliable hypergolic ignition and unstable combustion. IRFNA/UDMH and IRFNA/JP-X finally did prove satisfactory.

By the late 1950's it was apparent that N2O4 by itself was a better oxidiser. Therefore nitric acid was almost entirely replaced by pure N2O4 in storable liquid fuel rocket engines developed after 1960. The composition of propellant-grade nitric acids is covered by Military Specification MIL-N-7254. The nitric acids are fuming liquids which vary from colorless to brown, depending on the amount of dissolved N2O4. The vapours from these acids have a characteristic pungent odour. They are highly corrosive, toxic, oxidising agents and attack most metals. They react with most organic materials violently enough to cause fire. The acids are soluble in water in all proportions, with an accompanying evolution of heat. They cannot be made to explode. Approximately 90 per cent of the nitric acid is made by the catalytic oxidation of ammonia with air or oxygen to yield nitric oxide (NO). The latter is oxidised to N2O4 which, when treated with water, yields nitric acid (HNO3) and may be concentrated by distillation with sulphuric acid. Red fuming nitric acids may be produced by passing gaseous N2O4 into nitric acid, a slight modification of the above process. Production of nitric acid was estimated at 3 million tonnes in 1959. The price of RFNA was $ 0.20 per kg in drum lots; IRFNA was slightly higher. The varieties of nitric acid propellants include:

  • WFNA - White fuming nitric acid is based on anhydrous nitric acid (HNO3), a colourless corrosive liquid which fumes in moist air. They contain a maximum of 2 per cent water and 0.5 per cent nitrogen dioxide, and decompose to yield amounts of water, nitrogen dioxide, and oxygen which are in chemical equilibrium.

  • IWFNA - Inhibited white fuming nitric acid. Since container materials are attacked by WFNA and equilibrium products, 0.6 per cent HF is added for passivation by deposition of a protective metallic fluoride coating.

  • RFNA - Red fuming nitric acid. Since WFNA or IWFNA exhibit excessive equilibrium decomposition pressures, reaching 75 bar at 700 deg C. To suppress the high pressure through a mass-action effect, some 13 per cent N2O4 and 3 per cent H20 are added, in order to reduce equilibrium pressures to 2 bar at 700 deg C. The colour of the resulting red fuming nitric acid is imparted by N204.

  • IRFNA - Inhibited red fuming nitric acid. Addition of 0.6 per cent HF to RFNA produces inhibited RFNA (IRFNA). The IRFNA specification was published in 1954 and thereafter Russian rocket engines using the same fuel appeared.

  • AK20 - Russian formulation consisting of 80% nitric acid + 20% N2O4 (AK = Azotna Kislota = Nitric Acid)

  • AK20F - Russian formulation consisting of 80% nitric acid + 20% N2O4 + fluorine passivant

  • AK20I - Russian formulation consisting of 80% nitric acid + 20% N2O4 + iodine passivant

  • AK20K - Russian formulation consisting of 80% nitric acid + 20% N2O4 + unknown additive

  • AK27I - Russian formulation consisting of 73% nitric acid + 27% N2O4 + iodine passivant

  • AK-27P - Russian formulation consisting of 73% nitric acid + 27% N2O4 + unknown additive

Fuel: UDMH. Fuel Density: 0.793 g/cc. Fuel Freezing Point: -57 deg C. Fuel Boiling Point: 63 deg C.

Unsymmetrical Dimethylhydrazine ((CH3)2NNH2) became the storable liquid fuel of choice by the mid-1950's. Development of UDMH in the Soviet Union began in 1949. It is used in virtually all storable liquid rocket engines except for some orbital manoeuvring engines in the United States, where MMH has been preferred due to a slightly higher density and performance. Unsymmetrical dimethylhydrazine (UDMH) is 98 to 99 per cent pure and is described by Military Specification MIL-D-25604. The normally expected impurities are dimethylamine and water. UDMH is a clear, hygroscopic liquid which yellows on exposure to air. It absorbs oxygen and carbon dioxide. UDMH is a toxic volatile liquid. It exhibits the sharp ammoniacal or fishy odour which is characteristic of organic amines. It is completely miscible with water, ethanol, and most petroleum fuels. It is not shock sensitive. The vapours are flammable in air over 2.5 to 95 per cent concentration range. UDMH can be produced commercially by nitrosation of dimethylamine, to N-nitro-sodimethylrtmine, followed by reduction of the intermediate to UDMH and subsequent purification. UDMH can be prepared, also, by a modification of the Raschig process (see discussion of hydrazine), in which the chloramine intermediate is with dimethylamine rather than with ammonia. The price in 1959 for tank-car quantities was under $ 1.00 per kg. Engineering studies indicated a price of $ 1.00 per kg with large scale sustained production. But due to its toxic nature, production and transport costs soared in response to environmental regulations. By the 1980's NASA was paying $ 24.00 per kg.


Engines Using Nitric acid/UDMH
Engine
engineslink
Thrust(vac)
kN
Thrust(sl)
kN
Isp
sec
Isp (sea level)
sec
Designed for Status
YLR63AJ-3         JATO Out of Production
AJ10-118J            
P8E-9   205.440   238    
45LR-35000   159.583       Out of Production
RD-216M         First Stages Out of Production
RM-100B 0.441   283      
KDU-414 1.961   272   Upper Stages Out of Production
Isayev DOS-3/4 3.920       Upper Stages Out of Production
KTDU-53 4.089   280   Upper Stages Out of Production
KTDU-35 4.090   280   Upper Stages Out of Production
KTDU-66 4.090   280   Upper Stages Out of Production
KTDU-417 18.920   314   Upper Stages Out of Production
RD-851 32.480   279 243 First Stages Out of Production
AJ10-118D 33.700   278   Upper Stages  
AJ10-118 33.800   271   Upper Stages Out of Production
AJ10-101 34.300 30.500 270 240 Upper Stages  
AJ10-104 35.100   278   Upper Stages  
AJ10-118E 35.100   278   Upper Stages  
AJ10-118F 41.400   306   Upper Stages  
AJ10-118G 43.414   314      
AJ10-118H 43.414   319      
RD-852 48.250   255   Upper Stages Out of Production
RD-69 49.200       First Stages Out of Production
Bell 8048 68.900   276   Upper Stages Out of production
Bell 8096 71.200   293   Upper Stages Out of production
Bell 8081 71.200   285   Upper Stages Out of production
Bell 8247 71.200   291   Upper Stages Out of Production
Nodong 144.000   255 232 First Stages Out of production
11D49 157.500   303   Upper Stages  
YF-2A 306.100 275.300 268 241 First Stages Out of production
RD-68 380.000       First Stages Out of Production
Von Braun-3 392.300 315.500 286 230 Upper Stages Study 1952
Von Braun-2 461.500 371.100 286 230 Upper Stages Study 1952
RD-853 467.600   301   Upper Stages Developed 1960-63
U102-000 468.000   307   Upper Stages Out of production
AJ10-33 509.000          
RD-215 864.000   291 248 First Stages Out of Production
RD-217 865.000   289 246 First Stages Out of Production
RD-219 883.000   293   Upper Stages  
RD-225 889.000   294 251 First Stages Out of Production
RD-220 1,074.000   306 270 First Stages Developed 1960-
RD-221 1,118.000   318   Upper Stages Developed 1960-
RD-222 1,634.000   302 272 First Stages Developed 1960-61
RD-223 1,697.000   314   Upper Stages Developed 1960-61
RD-216 1,728.000 1,469.200 291 248 First Stages  
RD-224 1,778.000   294 251 First Stages Out of production
S5.45 1,961.000   267   Upper Stages Out of Production
RD-218 2,592.000 2,220.000 289 246 First Stages  
Von Braun-1 3,057.300 2,458.700 286 230 First Stages Study 1952
 
 
 
 
 
 
 
 
 

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