CRE:010117Initial rates (1,1,2),(2,1,8),(1,3,6): m=2, n=1, k=2; CB=2, CA 0.50 to 0.25 in 0.50 minCre Initial Rate Order TableCre Constant B Second Order BatchPrivateLabels unavailablePrivate saving unavailableRate laws, mechanisms, and parameter inferenceChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010118Closed A<->B, CT=1.20, kf=0.30, kr=0.10: Aeq=0.30, A=0.30+0.90 e^{-0.40 t}Cre Reversible First Order BatchCre Equilibrium Relaxation TimePrivateLabels unavailablePrivate saving unavailableRate laws, mechanisms, and parameter inferenceChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010219Isobaric PFR A->2B, v0=10, k=0.20, X=0.50: kV/v0=2 ln 2-0.5, V=100 ln 2-25 LCre Variable Density Pfr ExpansionCre First Order Pfr Design IntegralPrivateLabels unavailablePrivate saving unavailableBatch, CSTR, and PFR design equationsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010220Recycle PFR R=1, q=1/2: Cin=2, Cout=1, overall X=2/3, fresh removal 8 mol/minCre Recycle Pfr Mixer BalanceCre Overall Versus Single Pass ConversionPrivateLabels unavailablePrivate saving unavailableBatch, CSTR, and PFR design equationsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010221Inert-fed batch V=1+0.5t, nA=2 e^{-0.5 t}: at t=2, CA=1/e, reacted 1-e^{-1}, dCA/dt=-3/(4e)Cre Fed Batch Mole BalanceCre Dilution Versus ConversionPrivateLabels unavailablePrivate saving unavailableBatch, CSTR, and PFR design equationsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010322Linear-cooling batch: theta=100(e^{-t}-e^{-2t}), unique peak t=ln 2, T=325 KCre Linear Batch Energy Integrating FactorCre Batch Thermal Peak Generation LossPrivateLabels unavailablePrivate saving unavailableEnergy coupling, multiplicity, and thermal stabilityChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010323Adiabatic PFR, k=k0 T/T0: atanh X = k0 V/v0, X=0.60 gives V=20 ln 2, Tout=480 KCre Adiabatic Pfr Linear K OF TCre Atanh First Order Pfr VolumePrivateLabels unavailablePrivate saving unavailableEnergy coupling, multiplicity, and thermal stabilityChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010424Consecutive A->B->C: B=2(e^{-t/2}-e^{-t}), peak t=2 ln 2, (A,B,C)=(1/4,1/2,1/4)Cre Consecutive First Order B ProfileCre Intermediate Maximum Rate BalancePrivateLabels unavailablePrivate saving unavailableMultiple reactions, selectivity, and yieldChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010425Stoich left-null: A+C+D=2, B+C=3; extents (1.2,0.4) give (0.8,2.2,0.8,0.4)Cre Stoich Left Null InvariantsCre Extent Nonnegative RegionPrivateLabels unavailablePrivate saving unavailableMultiple reactions, selectivity, and yieldChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010426Autocatalytic A+B->2B: B=1/(1+9 e^{-2t}), B=1/2 at t=ln 3, max rate 1/2Cre Autocatalytic Logistic ReductionCre Logistic Half Time Max RatePrivateLabels unavailablePrivate saving unavailableMultiple reactions, selectivity, and yieldChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010527Two equal tanks tau_s=2: E=t/4 e^{-t/2}, mean 4, var 8, first-order X=3/4View access optionsCre Two Tank Gamma Rtd MomentsCre Tanks IN Series First Order SurvivalPrivateLabels unavailablePrivate saving unavailableResidence-time distributions and nonideal reactorsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010528Uniform window E=1/2 on [1,3]: mean 2, var 1/3, k=ln 2, X=0.72949468View access optionsCre Uniform Window Rtd MomentsCre First Order Laplace OF WindowPrivateLabels unavailablePrivate saving unavailableResidence-time distributions and nonideal reactorsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010529Bypass 1/4 plus exp tau=4: E has a delta, mean 3, var 15, first-order X=1/2View access optionsCre Bypass Dirac Exponential RtdCre Bypass First Order SurvivalPrivateLabels unavailablePrivate saving unavailableResidence-time distributions and nonideal reactorsChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010630Symmetric slab phi=ln3/2: eta=1/ln3, C(0)/Cs=sqrt(3)/2, wall slope ln3/4View access optionsCre Slab Thiele ProfileCre Slab Effectiveness FactorPrivateLabels unavailablePrivate saving unavailableHeterogeneous catalysis and reaction-diffusionChemical Reaction Engineering · Mixed reviewProgress not loaded
CRE:010631Nonporous kg=3, ks=6: Cs/Cb=1/3, K=2, film drop 2 Cb/3, resistances 2/3 and 1/3View access optionsCre Film Surface Series BalanceCre Overall Coefficient Resistance SplitPrivateLabels unavailablePrivate saving unavailableHeterogeneous catalysis and reaction-diffusionChemical Reaction Engineering · Mixed reviewProgress not loaded