fig1 illustrates one preferred embodiment of the invention . a well or borehole with a perforated liner has been made in a region that has been contaminated by a spill or leak of a petroleum product such as motor oil , transmission oil or gasoline . the well has been drilled in a formation 12 in which the soil contains groundwater within a few feet of the surface . the water table is indicated at 14 . the soil 16 above the water level 14 may contain some water . the surface is indicated at 18 . the region below water table 14 , of course , comprises soil saturated with water and containing organic material . the region also contains many different types of naturally occurring bacteria , some of which are capable of consuming the foreign organic material . usually such bacteria require a supply of oxygen to metabolize the oil -- typically three to four times the weight of the contaminant to be consumed . therefore , it is necessary to inject oxygen into the soil and water if the effort of the natural organisms is to proceed at any practical rate . further the oxygen , or other remediation assisting gas , must be introduced in an amount that can be dissolved in the water if it is not to simply bubble up out of the ground . as seen in fig1 a gas injection device 22 is placed in the well liner 20 to contain oxygen or other gas under pressure as it permeates from the device 22 into the water . the body of the device is preferably a tube or hose 24 , preferably of silicone rubber . silicone tubing and hose , reinforced and unreinforced , is commercially available . such hose is available , for example , from pure fit , inc ., allentown , pa . under the trade designation smp hose . smp hose is extruded tubes of platinum - cured silicone rubber . the hose is cloudy , nearly transparent and is reinforced with four - ply wrapped nomex aramid fiber . the hose is formed by extruding a first tube over which an aramid fiber wrap or braid is applied . an outer tube is applied over the wrapped inner tube . a hose of one to three and one - half inch internal diameter is suitable for application in this invention depending upon the desired inner diameter of the well . the thickness of the wall including reinforcement is typically about 0 . 4 inch . the tube 24 is shown suspended in well 10 . the tubing 24 is cut to a desired length for treatment of the ground water in a specific application . the tubing ends are sealed with suitable end caps . the lower end of tube 24 is sealed with end cap 26 and clamp 41 , and the upper end is closed with a cap 28 , clamp 41 and valve 30 ( shown closed ) for filling with oxygen or other remediation enhancing gas . if tube 24 does not contain internal reinforcement ( or if additional support is desired ), it may be enclosed in a flexible or rigid porous supporting mesh 34 with end caps 36 ( lower ) and 38 ( upper ) with clamps 40 . fastened to upper end cap 38 is a support line 32 for suspending the tube at a desired depth in the well 10 . mesh 34 can be used to place the hollow injection device 22 in the well . the mesh 34 can be weighted by means not shown to help sink the injection device 22 and then to provide support against the high pressure to which the tube 24 will be subjected . the mesh 34 may be formed of metal such as copper or brass or of a suitable polymer . the use of a copper containing alloy can provide protection against fouling of the gas injection site by bacteria . when the gas injection device is in place in the well liner 20 , the tube 24 can be evacuated of air . then one or more gases are introduced into the tube under pressure . oxygen is introduced at a pressure of 40 to 100 psig for aerobic bacterial activity . methane , ethane or ethylene and oxygen are supplied in combination to increase the methanotropic bioremediation of chlorinated compounds including trichloroethene , dichloroethene and vinyl chloride . ammonia and nitrous oxide are used as nutrients to supply nitrogen for bacterial growth to promote biodegradation processes . to a similar purpose , triethylphosphate vapor can be used to supply phosphorus . with the exception of ammonia , the above - named gases have limited solubility in groundwater and the use of the subject apparatus permits the slow , efficient diffusion of the gases from the silicone tube into the water in amounts that can be dissolved . diffusion rates of 0 . 6 g / day to 3 . 7 g / day per foot of length through a silicone rubber tube have been measured to demonstrate the utility of the subject apparatus . a silicone rubber tube one foot in length with a 1 . 5 inch inside diameter and a 0 . 25 inch wall thickness was tested in 1 . 2 liter closed recirculating water bath . the tube was pressurized with oxygen at pressures from 35 psig to 100 psig . dissolved oxygen concentration in the water was measured to determine the rate of oxygen transfer through the tubing or bladder wall . the results are shown in the following table . ______________________________________applied pressure total oxygen diffusion rate k . sub . p ( psig ) capacity ( g ) ( mg / day ) ( barrer )* ______________________________________35 33 562 16058 54 . 6 1579 210 100 94 3696 272______________________________________ * 1 barrer = 1 × 10 . sup .- 10 ml /( s cm cm . sup . 2 cm hg ) the diffusion rate , j , of gases through membranes can be calculated using fick &# 39 ; s law : j = k p x pressure gradient . in principle , the diffusivity constant , k p , is independent of pressure . however , in the above experiment k p increased as the pressure on the tube increased . this may have resulted from the fact the tube expanded as the pressure increased and the diffusion area increased rather than the diffusivity value . in any event the delivery rate of a gas utilizing the subject apparatus is readily controlled by controlling the pressure of the gas inside the bladder . fig2 shows a second preferred embodiment of the apparatus 122 of this invention . in fig2 a combination of well pipe 120 and well screen 121 is used as support for the inflated oxygen injection device 122 . the spacing between device 122 and the well pipe 120 and screen 121 is exaggerated for clarity of illustration . the tube 124 , end caps 126 , 128 and clamps 141 assembly is inserted in the well pipe 120 and well screen 121 before the tube 124 is inflated . only about half of the tube 124 extends below the water table 114 , and most of the oxygen diffusion occurs through the portion of the tube within the well screen 121 . inflation of the tube through valve 130 and refill pipe 131 expands the tube 120 and forces it out against well pipe 120 and screen 121 . since the well pipe is not perforated , oxygen diffusion is retarded in that region of the bladder . the portion of the bladder contained within the well pipe can be formed of a lower cost material that is less permeable to the oxygen or other remediation assisting gas . well pipe 120 contains a removable sealer cap 134 with suspending wires 132 for injection apparatus 122 . the top of the well 110 is closed with a flush mounted well cap 136 at ground level 118 . in the preferred embodiments described , the gas introduction apparatus has included a fabric - reinforced silicone rubber ( or other suitable polymeric ) gas - permeable tube fitted with suitable end closures . obviously , other gas container structures could be employed . instead of a tube , a long cylindrical bag or bladder could be used where the bottom is integral with the walls . the bag may be blow molded , e . g ., like a bottle so that only a small closure and valve need be applied . other structures may also be used . while the invention has been described in terms of specific embodiments thereof it will be apparent that other forms could readily be adapted by one skilled in the art . accordingly , the scope of the invention is to be limited only by the following claims .