Simulation of catalytic cracking process

Claim 2

In the catalytic cracking of a feed stream having a multiplicity of hydrocarbons having various boiling ranges by contacting such hydrocarbons with an active hydrocarbon cracking catalyst under catalytic cracking conditions to convert said hydrocarbons to cracked product and to contaminate said catalyst with coke deposited thereon; and controlling the product produced responsive to the boiling range of said multiplicity of hydrocarbons; the improvement which comprises lumping said hydrocarbons both kinetically and according to boiling range as: P l = Wt. % paraffinic molecules, (mass spec analysis), 430°-650°F N l = Wt. % naphthenic molecules, (mass spec analysis), 430°-650°F C al = Wt. % carbon atoms among aromatic rings, (n-d-M method), 430°-650°F A l = Wt. % aromatic substituent groups (430°-650°F) P h = Wt. % paraffinic molecules, (mass spec analysis), 650°F + N h = Wt. % naphthenic molecules, (mass spec analysis), 650°F + C ah = Wt. % carbon atoms among aromatic rings, n-d-M method, 650°F + A h = Wt. % aromatic substituent groups (650°F + ) and wherein the yields of said products are lumped as: G = g lump (C 5 + - 430°F) C = c lump (C 1 -C 4 + coke) and controlling the reaction conditions of said catalytic cracking reaction responsive to the invariant predetermined simultaneous and consecutive reactions characteristic of said proportions in said lumps to maximize yields therefrom.

Claim 3

The invention recited in claim 1 wherein said yields are gasoline, light fuel oil, and light ends + coke (C lump).

Claim 4

The invention recited in claim 1 wherein the lumps of hydrocarbons react in accordance with the following reaction rate constants: MATRIX OF RATE CONSTANTS K P.sub.h N.sub.h ______________________________________ P.sub.h -(K.sub.phpl +K.sub.phg +K.sub.phc) N.sub.h -(K.sub.nhnl +K.sub.nhg +K.sub.nhc) A.sub.h C.sub.Ah P.sub.l V.sub.hl K.sub.phpl N.sub.l V.sub.hl K.sub.nhnl A.sub.l C.sub.Al G V.sub.hg K.sub.phg V.sub.hg K.sub.nhg C V.sub.hc K.sub.phc V.sub.hc K.sub.nhc ______________________________________ A.sub.h C.sub.Ah ______________________________________ A.sub.h -(K.sub.ahal +K.sub.ahg +K.sub.ahc +K.sub.ahcal) C.sub.Ah -(K.sub.cahcal +K.sub.cahc) P.sub.l N.sub.l A.sub.l V.sub.hl K.sub. ahal C.sub.Al V.sub.hl K.sub.ahcal V.sub.hl K.sub.cahcal G V.sub.hg K.sub.ahg o C V.sub.hc K.sub.ahc V.sub.hc K.sub.cahc ______________________________________ P.sub.l N.sub.l A.sub.l ______________________________________ P.sub.l -(K.sub.plg +K.sub.plc) N.sub.l -(K.sub.nlg +K.sub.nlc) A.sub.l - (K.sub.alg +K.sub.alc) C.sub.Al G V.sub.lg K.sub.plg V.sub.lg K.sub.nlg V.sub.lg K.sub.alg C V.sub.lc K.sub.plc V.sub.lc K.sub.nlc V.sub.lc K.sub.alc ______________________________________ C.sub.Al G C ______________________________________ C.sub.Al -K.sub.calc G o -K.sub.gc C V.sub.lc K.sub.cala V.sub.gc K.sub.gc o ______________________________________ where, V hl = Stoichiometric coefficient (Mol. Wt. of heavy fuel oil/Mol. Wt. of light fuel oil) V hg = Stoichiometric coefficient (Mol. Wt. of heavy fuel oil/Mol. Wt. of gasoline) V hc = Stoichiometric coefficient (Mol. Wt. of heavy fuel oil/Mol. Wt. of C lump) V lg = Stoichiometric coefficient (Mol. Wt. of light fuel oil/Mol. Wt. of gasoline) V lc = Stoichiometric coefficient (Mol. Wt. of light fuel oil/Mol Wt. of C lump) V gc = Stoichiometric coefficient (Mol. Wt. of gasoline/Mol. Wt. of C lump).

Claim 5

The invention recited in claim 1 wherein the decay of the catalyst is dependent only on the concentration of the lump C AH = Wt. % carbon atoms among aromaic rings, n-d-M method, 650°+ and on the catalyst residence time.

Claim 6

The invention recited in claim 1 wherein said yields include the detailed composition of the light and heavy fuel oil fractions of the lumps P l , N l , C Al , A l , P h , N h , C Ah , and A h .

Claim 7

The invention recited in claim 1 further comprising lumping said hydrocarbons both kinetically and according to boiling range in a linear combination which produces an indication of the amount of coke deposited on the catalyst independent of the hydrocarbon composition of the feed stock.