I've never seen air being added. The problem is in fact usually the opposite in that gas from the well heads contain more Btu's than the average pipeline blend and the excess heavier HCs contributing to the higher Btu contents being removed. That also saves them from condensing in the pipeline as temperatures cool. What is left is pretty much methane with very small quantities <5% of ethane, butane plus a few other limited impurities normally yielding around 1050 Btu/cf. Pure CH4 has only 980 Btu/lbm, so you can see that nobody is purposely adding air to lower the Btu content, all that is needed is to remove the richer heavier compounds, which are sold separately. Neither is anyone adding air to a heavier blend just so they can transport that air cross country only to sell the gas at a lesser volumetric price, since gas you know is bought and sold by Btu content.
BTW Adding H2 to methane reduces the volumetric energy content. A 30% H2 blend into methane results in a CF having 863 Btu, 80% that of pipeline quality methane. Adding air will drop it a bit more, so no point in that.
Table 3-1. Typical Pipeline Gas Specifications
Characteristic Specification
Water content 4–7 lbm H2O/MMscf of gas
Hydrogen sulfide content 0.25–1.0 grain/100 scf
Gross heating value 950–1200 Btu/scf
Hydrocarbon dewpoint 14–40 °F at specified pressure
Mercaptans content 0.25–1.0 grain/100 scf
Total sulfur content 0.5–20 grain/100 scf
Carbon dioxide content 2–4 mol%
Oxygen content 0.01 mol% (max)
Nitrogen content 4–5 mol%
Total inerts content (N2 + CO2) 4–5 mol%
Sand, dust, gums, and free liquid None
Typical delivery temperature Ambient
Typical delivery pressure 400–1200 psig