• Bilag 7 Sammenligninger
  • Håndberegning
  • Syntesegass
  • Inn på reaktor
  • Ut av reaktor
  • Purge
  • Resirkulasjon
  • Råmetanol
  • HYSYS-flytskjema, reformingsanlegg




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    HYSYS-flytskjema, reformingsanlegg


    Bilag 7 Sammenligninger


    Tabell B7.1: Sammenligning mellom håndberegninger og flytskjema



      1. Håndberegning

      1. Flytskjema


























    F1
    1. Syntesegass














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    Kg/h

    CO2

    8.2%

    918.4

    40418.8

    8.2%

    918.4

    40418.8

    CO

    21.1%

    2363.2

    66193.2

    21.1%

    2363.2

    66193.2

    H2

    68.9%

    7716.8

    15587.9

    68.9%

    7716.8

    15587.9

    CH4

    1.4%

    156.8

    2516.6

    1.4%

    156.8

    2516.6

    N2

    0.2%

    22.4

    627.6

    0.2%

    22.4

    627.6

    Ar

    0.1%

    11.2

    447.4

    0.1%

    11.2

    447.4

    H2O

    0.1%

    11.2

    201.8

    0.1%

    11.2

    201.8

    CH3OH

    0.0%

    0

    0.0

    0.0%

    0

    0.0




    100.0%

    11200

    125993.5

    100.0%

    11200

    125993.5

























    F4
    1. Inn på reaktor














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    Kg/h

    CO2

    6.7%

    3338.0

    146903.6

    6.7 %

    3349.9

    147430.6

    CO

    6.8%

    3358.7

    94076.9

    7.2 %

    3599.9

    100834.0

    H2

    69.0%

    34155.6

    68994.4

    68.4 %

    34199.3

    69082.6

    CH4

    14.4%

    7127.3

    114392.7

    13.5 %

    6749.9

    108335.3

    N2

    2.1%

    1018.2

    28529.5

    2.5 %

    1250.0

    35024.3

    Ar

    1.0%

    509.1

    20338.2

    1.5 %

    750.0

    29961.9

    H2O

    0.0%

    11.2

    201.8

    0.04%

    20.0

    360.4

    CH3OH

    0.0%

    0.0

    0.0

    0.13%

    65.0

    2082.6




    100.0%

    49518.0

    473437.0




    49999.0

    493111.6

























    F5
    1. Ut av reaktor














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    Kg/h

    CO2

    5.8%

    2524.5

    111102.2

    5.8 %

    2532.5

    111455.9

    CO

    2.4%

    1017.9

    28510.9

    2.9 %

    1266.3

    35467.8

    H2

    62.6%

    27033.6

    54607.8

    61.9 %

    27028.0

    54596.6

    CH4

    16.5%

    7127.3

    114392.7

    15.5 %

    6767.9

    108625.1

    N2

    2.4%

    1018.2

    28529.5

    2.9 %

    1266.3

    35480.5

    Ar

    1.2%

    509.1

    20338.2

    1.7 %

    742.3

    29654.4

    H2O

    1.9%

    824.7

    14860.8

    2.0 %

    873.3

    15736.5

    CH3OH

    7.3%

    3154.3

    101063.4

    7.3 %

    3187.5

    102126.6




    100.0%

    43209.4

    473405.5




    43664.0

    493143.4

























    F10
    1. Purge














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    Kg/h

    CO2

    6.3%

    54.4

    2395.4

    6.3 %

    47.1

    2071.7

    CO

    2.6%

    22.4

    627.2

    3.1 %

    23.2

    648.8

    H2

    69.0%

    594.7

    1201.4

    68.3 %

    510.3

    1030.9

    CH4

    18.2%

    156.8

    2516.6

    17.0 %

    127.0

    2038.7

    N2

    2.6%

    22.4

    627.6

    3.2 %

    23.9

    670.0

    Ar

    1.3%

    11.2

    447.4

    1.9 %

    14.2

    567.2

    H2O

    0.0%

    0.0

    0.0

    0.02%

    0.1

    2.7

    CH3OH

    0.0%

    0.0

    0.0

    0.18%

    1.3

    43.1




    100.0%

    862.0

    7815.7




    747.2

    7073.0

























    F11
    1. Resirkulasjon














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    Kg/h

    CO2

    6.3%

    2419.6

    106484.8

    6.3 %

    2444.3

    107572.5

    CO

    2.6%

    995.5

    27883.6

    3.1 %

    1202.7

    33688.7

    H2

    69.0%

    26438.8

    53406.4

    68.3 %

    26499.0

    53528.0

    CH4

    18.2%

    6970.5

    111876.1

    17.0 %

    6595.7

    105860.3

    N2

    2.6%

    995.8

    27901.8

    3.2 %

    1241.5

    34787.8

    Ar

    1.3%

    497.9

    19890.7

    1.9 %

    737.2

    29449.6

    H2O

    0.0%

    0.0

    0.0

    0.02%

    7.8

    139.8

    CH3OH

    0.0%

    0.0

    0.0

    0.18%

    69.8

    2237.6




    100.0%

    38318.0

    347443.5




    38798.0

    367264.4

























    F13
    1. Råmetanol














    Fraksjon

    kmol/h

    kg/h

    Fraksjon

    kmol/h

    kg/h

    CO2

    1.3%

    50.5

    2222.0

    1.2 %

    49.3

    2171.1

    CO

    0.0%

    0.0

    0.0

    0.1 %

    2.5

    69.1

    H2

    0.0%

    0.0

    0.0

    0.7 %

    28.8

    58.1

    CH4

    0.0%

    0.0

    0.0

    0.6 %

    24.7

    395.9

    N2

    0.0%

    0.0

    0.0

    0.04%

    1.6

    46.1

    Ar

    0.0%

    0.0

    0.0

    0.04%

    1.6

    65.7

    H2O

    20.5%

    824.7

    14860.8

    20.4 %

    838.6

    15112.4

    CH3OH

    78.3%

    3154.3

    101063.4

    76.8 %

    3157.2

    101158.2




    100.0%

    4029.5

    118146.3




    4111.0

    119076.6

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    HYSYS-flytskjema, reformingsanlegg

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