astronautix.com | LOX/LH2 |
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J-2 - Credit: © Mark Wade. 29,661 bytes. 304 x 445 pixels. |
Liquid oxygen was the earliest, cheapest, safest, and eventually the preferred oxidiser for large space launchers. Its main drawback is that it is moderately cryogenic, and therefore not suitable for military uses where storage of the fuelled missile and quick launch are required. Liquid oxygen, as normally supplied, is of 99.5 percent purity and is covered in the United States by Military Specification MIL-P-25508. High purity liquid oxygen has a light blue colour and is transparent. It has no characteristic odour. Liquid oxygen does not burn, but will support combustion vigorously. The liquid is stable; however, mixtures of fuel and liquid oxygen are shock-sensitive. Gaseous oxygen can form mixtures with fuel vapours that can be exploded by static electricity, electric spark, or flame. Liquid oxygen is obtained from air by fractional distillation. The 1959 United. States production of high-purity oxygen was estimated at nearly 2 million tonnes. The cost of liquid oxygen, at that time, ex-works, was $ 0.04 per kg. By the 1980's NASA was paying $ 0.08 per kg.
Liquid hydrogen was identified by all the leading rocket visionaries as the theoretically ideal rocket fuel. It had big drawbacks, however - it was highly cryogenic, and it had a very low density, making for large tanks. The United States mastered hydrogen technology for the highly classified Lockheed CL-400 Suntan reconnaissance aircraft in the mid-1950's. The technology was transferred to the Centaur rocket stage program, and by the mid-1960's the United States was flying the Centaur and Saturn upper stages using the fuel. It was adopted for the core of the space shuttle, and Centaur stages still fly today.
In Russia hydrogen fuelled upper stages were designed and developed by the mid-1970's, but the Russians never seem to have found the extra performance to be worth the extra cost. Europe and China developed liquid oxygen/liquid hydrogen engines for upper stages of the Ariane and Long March launch vehicles.
The equilibrium composition of liquid hydrogen is 99.79 per cent parahydrogen and 0.21 per cent orthohydrogen. The boiling point of this composition is -253 deg C. Liquid hydrogen is transparent and without a characteristic odour. Gaseous hydrogen is colourless. Hydrogen is not toxic but is an extremely flammable material. The flammable limits of gaseous hydrogen in air are 4.0 to 75 volume percent.
Hydrogen is produced from by-product hydrogen from petroleum refining and the partial oxidation of fuel oil. The gaseous hydrogen is purified to 99.999+ per cent, and then liquefied in the presence of paramagnetic metallic oxides. The metallic oxides catalyse the ortho-para transformation of freshly liquefied hydrogen. Freshly liquefied hydrogen which has not been catalysed consists of a 3:1 ortho-para mixture and cannot be stored for any length of time because of the exothermic heat of conversion. The delivered cost of liquid hydrogen in 1960 was approximately $ 2.60 per kg. Large-scale production was expected to reduce the cost to $ 1.00 per kg. In the 1980's NASA was actually paying $ 3.60 per kg.
Eng-engineslink | Thrust(vac)-kgf | Thrust(vac)-kN | Isp-sec | Isp (sea level)-sec | Designed for | Status | RS-52 | 11 | 405 | RM-1500H | 680 | 400 | YF-73 | 1,125 | 11.00 | 425 | Upper Stages | In Production | RS-71 | 3,174 | 430 | RD-0126 | 3,997 | 39.20 | 476 | Upper Stages | Design concept 1993- | HM7-A | 6,289 | 61.70 | 443 | 308 | Upper Stages | Out of Production | HM-10 | 6,300 | 61.80 | 443 | Upper Stages | Developed 1990's | HM7-B | 6,394 | 62.70 | 446 | 310 | Upper Stages | In Production | RL-10A-3 | 6,690 | 65.60 | 444 | Upper Stages | Out of Production | RL-10A-5 | 6,696 | 64.70 | 373 | 316 | First Stages | Out of Production | AEC | 6,801 | 481 | RL-10A-1 | 6,804 | 66.70 | 425 | 10 | Upper Stages | Out of Production | RL-10 | 6,804 | 66.70 | 410 | 10 | Upper Stages | Out of Production | RD-56 | 7,100 | 69.60 | 462 | Upper Stages | Developed 1960-77 | RL-10A-3A | 7,485 | 73.40 | 444 | Upper Stages | In Production | RD-56M | 7,503 | 73.58 | 461 | Upper Stages | Developed 1994- | YF-75 | 8,000 | 78.50 | 440 | Upper Stages | In Production | AMPS-1 | 8,161 | 468 | ASE | 9,068 | 473 | RL-10A-4 | 9,433 | 92.50 | 449 | Upper Stages | In Production | RL-10B-X | 9,524 | 93.40 | 470 | Upper Stages | Design concept 1994 | RD-0132 | 10,000 | 98.00 | 469 | Upper Stages | Design concept 1996- | RD-0126A | 10,000 | 98.00 | 476 | Upper Stages | Design concept 1996- | RD-0131 | 10,000 | 98.00 | 467 | Upper Stages | Design concept 1996- | RD-0133 | 10,000 | 98.00 | 467 | Upper Stages | Design concept 1996- | RD-0128 | 10,000 | 98.00 | 474 | Upper Stages | Design concept 1996- | RL-10A-4-2 | 10,110 | 99.10 | 451 | Upper Stages | In Production | RL-10A-4-1 | 10,110 | 99.10 | 451 | Upper Stages | In Production | RD-0146 | 10,197 | 100.00 | 470 | Upper Stages | Design concept 1998- | RL-10A-5KA | 10,247 | 398 | 352 | First Stages | Design 1992 | LE-5 | 10,500 | 103.00 | 450 | Upper Stages | In Production | RL-10B-2 | 11,222 | 110.00 | 462 | Upper Stages | In Production | RL-10C-X | 11,300 | 110.80 | 450 | Upper Stages | Design concept 1994 | LE-5A | 12,390 | 121.50 | 452 | Upper Stages | In Production | HIMES | 14,000 | 137.30 | 452 | 340 | Upper Stages | Study -1998 | LE-5B | 14,000 | 137.00 | 447 | Upper Stages | In Production | Truax LH2 | 15,000 | 147.10 | 425 | 306 | Upper Stages | Design concept 1982 | RL-10C | 15,873 | 155.70 | 450 | Upper Stages | In Production | MB-60 | 27,200 | 467 | RL-50 | 29,500 | 290.00 | 472 | Upper Stages | Development | LH2-80k | 36,274 | 355.70 | 425 | 306 | Upper Stages | Study 1959 | RD-57 | 40,000 | 392.00 | 457 | Upper Stages | Developed 1960-77 | RD-54 | 40,000 | 392.00 | 440 | Upper Stages | Developed 1960-75 | RD-57A-1 | 40,279 | 395.00 | 460 | Upper Stages | Developed 1995-98 | RD-57M | 40,483 | 397.00 | 461 | Upper Stages | Developed 1960-74 | MBB-ATC500 | 45,000 | 441.30 | 460 | 409 | First Stages | Study 1980 | LR-87 LH2 | 68,000 | 667.00 | 350 | Upper Stages | Out of Production | J-2T-200K | 90,686 | 889.30 | 435 | 300 | Upper Stages | Study NASA 1966 | J-2-SL | 101,634 | 996.70 | 390 | 275 | First Stages | Study 1966 | J-2 | 105,352 | 1,033.10 | 421 | 200 | Upper Stages | Out of Production | Vulcain | 109,619 | 1,075.00 | 431 | 326 | First Stages | In Production | LE-7 | 109,925 | 1,078.00 | 446 | 349 | First Stages | In Production | LE-7A | 112,000 | 1,098.00 | 440 | 338 | First Stages | In Development | Aerospike Annular Booster | 113,358 | 450 | J-2T-250K | 113,358 | 1,111.60 | 441 | 290 | Upper Stages | Study NASA 1966 | J-2S | 121,066 | 1,187.00 | 426 | 200 | Upper Stages | Developed 1965-1969 | XRS-2200 | 121,600 | 1,192.00 | 439 | 339 | First Stages | In Production | ATCRE | 130,524 | 1,280.00 | 490 | 409 | Upper Stages | Study -1985 | Vulcain 2 | 132,563 | 1,300.00 | 440 | 318 | First Stages | Developed 1990's | HG-3-SL | 141,500 | 1,387.00 | 450 | 360 | First Stages | Study 1966 | HG-3 | 142,831 | 1,400.70 | 451 | 280 | Upper Stages | Developed 1960's | SSME Study | 156,550 | 1,535.20 | 459 | 359 | First Stages | Study 1970 | Plug-Nozzle SASSTO | 160,600 | 1,574.90 | 459 | 359 | First Stages | Study 1966 | Helios Stage 1 | 170,000 | 1,667.00 | 400 | 340 | First Stages | Study, Ehricke, 1960 | Toroidal 400k | 181,400 | 1,778.00 | 447 | 200 | Upper Stages | Design concept 1990's | RD-0120M | 200,000 | 1,961.00 | 455 | 372 | First Stages | Hardware | RD-0120 | 200,000 | 1,961.00 | 455 | 359 | First Stages | Out of Production | NK-35 | 200,000 | 1,960.00 | Upper Stages | Design 1972 | NK-15VM | 200,000 | 1,960.00 | Upper Stages | Developed 1965 | Mustard | 220,000 | 2,157.40 | 405 | 300 | First Stages | Study 1967 | RS-2200 | 224,540 | 2,201.00 | 455 | 347 | Upper Stages | In Production | SSME | 232,301 | 2,278.00 | 453 | 363 | First Stages | In Production | RD-0122 | 235,860 | 2,313.00 | 461 | Upper Stages | Developed 1990- | SSME Demonstrator Booster | 249,400 | 465 | Toroidal 560k | 254,020 | 2,491.00 | 447 | 200 | Upper Stages | Design concept 1990's | STME | 294,703 | 2,890.00 | 431 | 365 | First Stages | Developed -1990 | RS-68 | 337,807 | 3,312.00 | 420 | 365 | First Stages | In Production | SSME Plus | 380,221 | 3,728.70 | 467 | 385 | First Stages | Study 1970 | Plug-Nozzle SSME | 380,221 | 3,728.70 | 485 | 412 | First Stages | Study 1970 | PW 1000000 lb LH2 | 454,500 | 4,457.00 | 425 | 354 | First Stages | Study 1988 | M-1 | 544,118 | 5,335.90 | 428 | 310 | Upper Stages | Developed 1960's | HP-1 | 666,541 | 6,536.00 | 451 | 379 | First Stages | Study 1963 | Plug-Nozzle J-2 | 700,000 | 6,864.60 | 425 | 330 | First Stages | Study 1993 | CD Module | 750,708 | 7,361.00 | 420 | 377 | First Stages | Design concept 1960's | Chamber/single nozzle | 1,349,250 | 13,231.00 | 455 | 365 | First Stages | Design concept 1960's | Toroid FD | 2,041,000 | 20,015.00 | 455 | Upper Stages | Study 1963 | Plug-Nozzle Pegasus | 2,440,000 | 23,928.00 | 459 | 359 | First Stages | Study 1966 | L-5.25H | 2,789,000 | 27,350.00 | 410 | 350 | First Stages | Study General Dynamics 1963 | L-5.00H | 3,129,000 | 30,684.00 | 428 | 310 | First Stages | Study General Dynamics 1963 | Plug-Nozzle SERV | 3,261,105 | 31,980.20 | 455 | 367 | First Stages | Study 1970 | 5 mlbf | 4,217,750 | 41,361.00 | 410 | 345 | First Stages | Study 1963 | Plug-Nozzle Rombus | 10,400,000 | 101,988.00 | 459 | 359 | First Stages | Study 1966 | L6H | 12,517,000 | 122,748.00 | 439 | 382 | First Stages | Study 1963 |