Process Intensification and Integration for Sustainable Design. Группа авторов

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Process Intensification and Integration for Sustainable Design - Группа авторов

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255 21 Residue gas 900

      2.C

      Table 2.C.1 Fractionation train column parameters for the base case (Feed #3).

Column Feed flow rate (MMSCFD) T (°F) P (psig) Number of trays Light/heavy key
Deethanizer 27.1 38.8–159 285–292 35 Ethane/propane
Depropanizer 17.9 104–187 190–193 36 Propane/i‐butane
Debutanizer 8.09 163–219 135–140 60 n‐Butane/pentane
C4 splitter 5.74 147–179 120–140 60 i‐Butane/n‐butane

      Feed flow rate is a standard vapor volumetric flow rate.

      2.D

      Table 2.D.1 Acid gas removal column parameters.

Column Feed flow rate (MMSCFD) T (°F) P (psig) Number of trays
Contactor 150 100–110 796–800 7
Regenerator 150.18 210 8–12 10

      Feed flow rate is a standard vapor volumetric flow rate.

      Table 2.D.2 Makeup composition.

Stream Water (mass%) MDEA (mass%) Piperazine (mass%)
18 – Makeup 55 40 5.0

      Table 2.D.3 Key heat exchange equipment outlet temperatures.

Stream T (°F)
8 210
22 110 a

      a Set at 10 °F warmer than inlet gas.

      Abbreviations

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AFC annualized fixed cost (depreciation)
AOC annual operating cost
Btu British thermal unit
CO2 carbon dioxide
images purchased cost of equipment q
FCI fixed capital investment
FCIi fixed capital investment for a given processing unit
FCIS salvage value of the fixed capital investment
ΔFLmix average explosiveness of a mixture
images Hand factor for equipment q
gal gallons
GJ gigajoules
h hours
H2S hydrogen sulfide
HA high acid
HVm average mass heating value
IROI incremental return on investment
kWh kilowatt hours
lb pounds
LFLmix lower flammability level of a mixture
images mass flow rate
MDEA methyl diethanolamine
MM$ million dollars
MMBtu million British thermal units
MMSCFD million standard cubic feet per day
MSCF thousand standard cubic feet
N plant lifetime (number of years)