Abstract

In-situ methanotrophic bioremediation of ground water contaminated with 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-transfer apparatus for adding O 2 directly into recirculating ground water. At times it may be desirable to add other gases as well, such as methane for CAH cometabolism. A high downward velocity of water through the inlet tube of an inverted cone prevented upward movement of injected O 2 bubbles. The addition of gas-liquid mixing cones within the transfer section of the inverted cone increased the turbulence below the inlet. Complete dissolution of gases is possible. The relationships between O 2 transfer rate and system variables such as pressure loss, water flow rate, and N 2 content in the influent water were evaluated. A significant factor affecting O 2 mass transfer was the total dissolved gas content in the water entering the transfer device. From the results of this study, a design for practical conditions of operation was developed.

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