In-situ methanotrophic bioremediation of ground water contaminated wit
h petroleum hydrocarbons and chlorinated aliphatic hydrocarbons (CAHs)
often require the addition of O-2 for compound oxidation. The purpose
of this research was to test the feasibility of a down-well gas-trans
fer apparatus for adding O-2 directly into recirculating ground water.
At times it may be desirable to add other gases as well, such as meth
ane for CAH cometabolism. A high downward velocity of water through th
e inlet tube of an inverted cone prevented upward movement of injected
O-2 bubbles. The addition of gas-liquid mixing cones within the trans
fer section of the inverted cone increased the turbulence below the in
let. Complete dissolution of gases is possible. The relationships betw
een O-2 transfer rate and system variables such as pressure loss, wate
r flow rate, and N-2 content in the influent water were evaluated. A s
ignificant factor affecting O-2 mass transfer was the total dissolved
gas content in the water entering the transfer device. From the result
s of this study, a design for practical conditions of operation was de
veloped.