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Table 1. Typical LFG Composition

| By Mary Bailey

LFG components Wet LFG during peak production Flaring/direct-use during peak LFG production Pipeline-grade specifications
CH4 ~55 vol% (typical)  ~55 vol% (typical)  96 vol% min.
CO2 ~45 vol% (typical)  ~45 vol% (typical)  3 vol% max.
Pressure 40-60 inWC vacuum to the blower 5 psig 200 psig (min.)
Temperature ~90°F ~110°F 50°F (min.)
105°F (max.)
H2S 17 ppmv (average) Sulfur removal requirements based on concentration, local environmental regulations, gas generator specifications as well as CapEx vs. OpEx analysis 4 ppmv max.
700 ppmv (typical max.)
Mercaptans 11 ppmv (average) 5 ppmv max.
30 ppmv (typical max.)
Total Sulfur 18 ppmv (average) 12 ppmv max.
735 ppmv (typical max.)
Non-methane volatile organic compounds (nmVOCs) / hazardous substances 465 ppmv (average) < 155 ppmv (typical) after condensate knockout None 

0.6 mol% (max.)  

(~1 gph condensed nmVOCs in KO drum / 100 SCFM LFG)

nmVOC removal requirements based on concentration, local environmental regulations, gas generator specifications as well as CapEx vs. OpEx analysis
   
NH3 < 1 vol% < 1 vol% None
N2 < 5 vol% < 5 vol% * see inerts
O2 < 1 vol% < 1 vol% 0.2 mol% max.
LHV ~550 Btu/SCF  550 Btu/SCF 990 Btu/SCF
Moisture 100% R.H. (~7 gph condensate in KO drum / 100 SCFM LFG) 100% R.H. 7 ppmv max.
Siloxanes < 100 ppmwt (typical) Siloxane removal optional None
1000 ppmwt (max.)