Temperature Calculation Using Polynomial Eqn

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    Estimating Temperatures in the primary reformer using K-Polynomials:

    There are two major reactions taking place in the Primary reformer.

    1. Reforming reaction : CH4 (g)+ H2O(g)CO(g)+ 3H2(g) (Equilibrium constantK1)

    2.

    Shift conversion : CO(g) + H2O(g)CO2 (g)+ H2 (g) (Equilibrium constantK2)

    K1=()(

    )

    ()()[P]2 and K2=

    ()()

    ()()[P]0

    Where Pi is the partial pressure of component i and P is thetotal pressure.

    From the Wet-Analysis of the outlet of primary reformer, we get the composition of the gas stream as :

    Component Dry Analysis (mol%) Flow rates (Nm3

    /hr) Wet Analysis (mol%)H2 66.51 59792.49 37.26

    N2 0.82 737.18 0.46

    CO 7.67 6895.33 4.3

    CO2 10.86 9763.14 6.08

    Ar 0.01 8.99 0.0056

    CH4 14.13 12702.87 7.915

    H2O 70585.76 44

    Also, we know that,

    Pi= xi * P where xi is the mole % of component i

    Here, in the primary reformer, Ptotal= 33 kg/cm2 gauge.

    And since the components in the outlet stream are in equilibrium, we take those compositions to calculate

    the equilibrium partial pressures.

    = 0.07195 x Ptotal

    = 0.44 x Ptotal

    = 0.043 x Ptotal

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    = 0.0608 x Ptotal

    = 0.3726 x ptotal

    Kreforming= K1=()()

    ()()[P]2 =

    ()()

    ()()(

    ) = 74.87

    And Kshift = K2=()()

    ()()[P]0 =

    ()()

    ()() = 1.197

    K-Polynomials for calculating the Equilibrium Constant

    K = exp (K1x InT + K2/T + K3 + T (K4+ T (K5+ K6x T)))

    T = Temperature in Kelvin

    Shift Reaction Ammonia Reforming Reaction

    CO+H2OH2+CO2 3H2+N22NH3 CH4+ H2OCO+3H2

    K1 -3.161655 x 10-1 -8.047466 8.611141

    K2 5.016493 x 103 9.109037 x 103 -2.264800 x 104

    K3 -4.104398 2.714340 x 101 -2.898262 x 101

    K4

    2.139622 x 10-3 4.730516 x 10-3 -4.980093 x 10-3

    K5 -6.044361 x 10-7 -4.355303 x 10-7 3.977486 x 10-7

    K6 7.582492 x 10-11 -6.422945 x 10-12 2.013355 x 10-11

    Reforming reaction:

    Given, K = (

    ( ( )))

    lnK = K1lnT +

    + K3+ K4T + K5T

    2+ K6T3

    We have,

    Kref= 74.87 ,

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    And from the above table, for reforming reactions,

    ln(74.87) = 8.611141lnT -

    - 28.98262 - 0.004980093T + (3.977486x10-7)T2+ (2.013355 x 10-11)T3

    Solving the above equation, we get,

    Tref= 1039.037K = 766.0370C 7670C (as given in the data sheet)

    Similarly, using the data given in the table for Shift reactions, we get,

    Tshift= 766.7670C 767

    0C

    Thus, we can verify the operating values by theoretical methods.