Ind. Eng. Chem. Process Des. Dev. 1983, 22, 401-409 40 1 Nomenclature C = conversion factor between partial pressure and concentration, mol/m3, Pa E = eddy diffusivity, m2/s H = height of an increment, m H,, = total bed height, m I = increment index J = gas component index, J = Hz, CO, CO2, CH4, HZS, H20, kl, k4 = constants, l / s k2: k3, k5, k6' = constants, 1/Pa k3 = constant, 1/Pa0.= k6 = constant, 1/Pa0.05 k7 = constant, mol/kg, s, Pa2 k8 = constant, dimensionless K H Kco KCO, K H = constants, 1/Pa P, $Azo, P&, PCO, $H2 = partial pressure, Pa R = production rate, mol/s rc = reaction rate of fixed carbon, mol/kg, s reo, = reaction rate of C02 in ri, i = 1-3 reaction rate of fied conversion rate of C02 in the shift reaction rpi, i = Hz, CO, COZ, CHI, H20, HzS; pyrolysis yield of component i, mol/kg of shale V = volumetric gas flow, m3/s uo = superficial gas velocity, m/s u = gas velocity, m/s y = dispersion parameter, dimensionlesse r a t u r e Cited Berggren, J.C.; Bjerle, I.; Eklund, H.; Karlsson, H.; Svensson, 0. Chem. Eng. Scl. 1980, 35, 448. BJerle, I.; Eklund, H.; Svensson, 0. I d . Eng. Chem. Process Des. Dev. 1980, 19, 345. Bjerle, I.; Eklund, H.; Llnn6, M.; Svensson. 0. I d . Eng. Chem. Process Des. Dev. 1982, 21, 141. Eklund, H.; Llnder, 0.; Svensson, 0. "A Klnetlc Study of the Heterogeneous Shlfi Reactlon over Shale Char and Kerogen Free Ash"; Report, Lund Instltute of Technology, Dept of Chemical Engineering, 1980. Qeldart, D. Powder Techno/. 1973, 7, 285. Kato, K.; Wen, C. Y. Chem. Eng. Scl. 1969, 24, 1351. Park, D.; Levensplel. 0.: FitzgeraM, T. J. Fuel 1981, 60, 295. 0 2Mixtures of two-, three-, and four-ring (naphthalene, phenanthrene, and pyrene) structures were hydrocracked over a nickel-tungsten sulfide uttrastable zeolite Y catalyst. The hydrocracking of tetralin and phenanthrene proceeds by elimination of butanes to form CB and Clo hydrocarbons primarily. Isomerization of saturated six-member rings to methyl-substituted five-member rings is also prominent. The presence of 1-cyclohexyl-2-phenylethane in the products from phenanthrene hydrocracking suggests an akematlve reaction path for the hydrocracking of structures containing adjacent saturated rings. Pyrene hydrocracking proceeds primarily by elimination of propane followed by butanes ellmination, Le., CIB -, C,, -Clo -Ce. The C13 intermediates are mostly h drogenated phenalenes.The zeolite-based catalyst was very active in hydrocracking pyrene (critical diameter = 9 Ay ) and smaller molecules.The perhydropyrene component of the feed mixture was relatively inert, but it could not be established whether this was due to a molecular sieve effect or intrinsic chemical kinetics factors.