VACUUM APPARATUS AND PROCESS FOR IN-SITU REMOVING UNDERGROUND LIQUIDS AND VAPORS

Abstract: An apparatus for removing underground contaminants from a contaminated subsurface area (16) is provided. The apparatus includes releasing and/or recovering means in the form of a wellbore (12), which is aligned in the contaminated subsurface area (16) for releasing predetermined substances into selected areas of the contaminated subsurface area (16) so that the substances and contaminants are intermixed and for recovering the intermixture of substances and contaminants from selected areas of the contaminated subsurface area (16). A means (83) is provided for rotating and sliding an inner housing (68) of the wellbore (12). Predetermined substances are injected into the wellbore (12) and vacuum is applied to the wellbore (12) so that the intermixture of substances and contaminants can be extracted from the contaminated area. The intermixture of substances and contaminants are then collected and/or stored for subsequent removal in a tank (28).

Description: VACUUM APPARATUS AND PROCESS FOR IN-3ITU REMOVING UNDERGROUND LIQUIDS AND VAPORS TECHNICAL FIELD: The present invention relates to a system that is designed to completely remove liquid contaminants from landfills and subsur¬ face areas. More particularly a system is provided which, by se¬ lectively and sequentially using a vacuum alone and/or in con¬ junction with heat, water, chemicals or microbes, the removal of contaminants is facilitated from discreet "zones" throughout the entire length and breadth of a contaminated subsurface area. The contamination of the subsurface area known as the vadose zone, which is the zone between the ground and underground water tables or aquifers, is a major problem throughout the world. Many of these contaminants have been indentified as carcinogens. The contamination of the vadose zone is normally the result of the leaking of waste dumps; or because of chemical or oil spills. This contamination can also be caused by leaking chemi- cals or oil from underground storage tanks. The threat to human health occurs when these contaminants are carried by rain water into the underground water supply. Volatile liquid contaminants are often removed from subsurface areas by excavating the contaminated area and then decontaminat¬ ing it on the surface. There are significant drawbacks and dis¬ advantages to this method, however. Not only are these excava¬ tion-based methods extremely expensive, they have an even grea¬ ter disadvantage in that residents of areas near the contami- nated sites often raise objections to the above ground exca¬ vation of polluted soil in their neighborhoods. Another more recent problem is associated with landfills to which toxic-chemicals are transported for burial after they have been excavated. These chemicals normally include some very mo¬ bile contaminants and often these mobile contaminants will dif¬ fuse into the barriers of the landfills thereby breaking through into the vadose zone over drinking water aquifers. Because of this additional problem, it now makes it even more difficult to excavate contaminated sites and ship them off for reburial in supposedly secure landfill sites. Because of these problems, re- clamation will have to be done on or in the site, that is, "in- situ". It also means that the landfills themselves, most of which are very deep, will have to be decontaminated "in situ". Clearly, what is needed is a reliable and efficient method of cleaning up the toxic chemicals, oil and gasoline "in situ". DESCRIPTION OF PRIOR ART: There have been a number of systems and methods developed for in situ removal of pollutants. One such system is disclosed in U.S. Patent 4,163,973. In this patent, a system and method are disclosed which includes flushing the pollutants into a water removal well and then pumping them therefrom onto the surface. This process is not only inefficient, but the flushing can ac¬ tually force the contaminants into the ground water. Another system and method is disclosed in U.S. Patent No. 3,980,138. This system provides for the large scale recovery of liquid and vaporized contaminants from the vadose zone using suction. The patented apparatus has limited applicability be- cause the suction is taken from just one point in the polluted zone. As a result the device is decreasingly effective with con¬ taminants that are twenty feet or more from the single recovery ' point. There is an additional problem that plagues "single point" suction recovery systems. As air, gas and liquids are pumped to a single suction point, they soon create air and water channels that by-pass the contamination. An even greater problem is that the single point recovery system tends to pull air from the sur- face and bypass the target pollutants. U.S. Patent No. 4,026,355, attempts to solve the problems inherent with single- point recovery wells by using multiple wells to pull gas from several subsurface points through a series of wells. However, this system has the drawback of requiring the expense of an ex¬ cessive number of wells. U.S. Patent No. 4,183,407 represents another attempt to remove the volatile liquid contaminants from the entire sub-surface zone, rather than the immediate vicinity of the vacuum wellbore. This invention attempts to create a mul¬ titude of recovery points by running horizontal piping out from the base of the well. The drawback to this unit is that it is difficult and expensive to install and it diffuses its vacuum effect through a multitude of openings. Still another system is disclosed in U.S. Pat. No. 4,183,407. However this system only serves to increase the relative pres¬ sure differential pulling the contaminants to the recovery point and does not improve the recovery point or the vacuum recovery balance of the entire unit. What it does, instead, is to in¬ crease the pressure differential at a point that is distant from the wellbore. This is done at the expense of the vacuum drag on the area that is near to the "hub" of the spokes of the "wheel design" of that system. - __> DISCLOSURE OF THE INVENTION: An apparatus for removing underground contaminants from a conta¬ minated subsurface area is provided. The apparatus preferably includes means positioned in the contaminated subsurface area for releasing predetermined substances into selected areas of the contaminated subsurface area so that the substances and con¬ taminants are intermixed. This same means may also be adapted to recover the contaminants, eventually in intermixture with the predetermined substances, from selected areas of the contami¬ nated subsurface area, or alternatively a special recovering means is positioned in the contaminated subsurface area. The re¬ leasing and/or recovering means is provided with means for rota¬ ting and/or for sliding a portion of the positioned means. The apparatus is provided with means for injecting the sub¬ stances into the releasing means. Means for applying pressure to __._%__. the releasing and/or recovering means is provided so that the intermixture of substances and contaminants can be extracted from the contaminated subsurface area. Means is provided and coupled to the pressure applying means for collecting and/or storing the intermixture of substances and contaminants as the intermixture is extracted from the contaminated subsurface area. A method for removing underground contaminants from a contamina¬ ted subsurface area in accordance with the principles of the in- vention includes the first steps of positioning a releasing and/or recovering means in the contaminated subsurface area and then activating a rotating and sliding means to sequentially and selectively open and close succesive ports of the releasing and/or recovering means. A vacuum pressure is sequentially and selectively applied to each open port in the releasing and/or recovering means to reco¬ ver contaminants from an adjacent area of the contaminated sub¬ surface area. The rotating and sliding means is then activated to close each of the successive open ports in the releasing and recovering means before the next port thereof is opened. As a result upon the application of vacuum pressure to the successive opened ports recovery of the contaminants in the entire contaminated subsurface area can be accomplished. 3RIΞF DESCRIPTION OF THE DRAWING: The details of the invention will be described in connection with the accompanying drawing in which: Fig.1 is a diagrammatic view of a surface mounted vacuum appa¬ ratus for removing underground contaminated liquids and vapors in accordance with the principles of the inven- tion; Fig.2 is a partial cross-sectional side view of a wellbore ta¬ ken along lines 1-1, of Figure 1 in accordance with the principles of the invention; Fig.3 is a cross-sectional view of the wellbore taken along lines 2-2 of Figure 1 in accordance with the principles of the invention; Fig.4 is an exposed side view of the wellbore of Figure 1 il¬ lustrating the movement of the inner housing and driving means of the wellbore in accordance with the principles of the invention; Fig.5 is a cross-sectional top view of the wellbore taken along lines 4-4 of Figure 4 in accordance with the prin¬ ciples of the invention; Fig.6 is a diagrammatic view of a single well configuration of the vacuum apparatus during an injection made in accor¬ dance with the principles of the invention; Fig.7 is another diagrammatic view of the single well configu¬ ration during the injection mode in accordance with the principles of the invention; Fig.8 is a diagrammatic view of a multiwell configuration of the vacuum apparatus illustrating vertical parallel well- bores which can be used and operated to inject substances such as toxiphilic microbes throughout the contaminated vadose zone in accordance with the principles of the in- vention; Fig.9 is another diagrammatic view of the multiwell configu¬ ration of the vacuum apparatus illustrating vertical par¬ allel wellbores which can be used to further disperse microbes and recover contaminants in accordance with the principles of the invention; Fig.10 is a top view of a schematic diagram illustrating another multiwell vacuum apparatus which can be used to inject and disperse substances such as toxiphilic bac¬ teria throughout the vadose zone so as to recover conta- minants in accordance with the principles of the inven¬ tion and Fig.11 is a block diagram of an automatic control system. SUBSTITUTE SHEET DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS: Referring now to Figure 1 , there is shown a vacuum apparatus, generally designated by the numeral 10, for removing underground contaminants and vapors from a contaminated subsurface area 16. The vacuum apparatus 10 is provided with an extraction well or wellbore, generally designated by the numeral 12, which extends from a surface area 1 into the contaminated subsurface target area 16 which is above aquifers (water tables) 18. The wellbore 12 is coupled at an input junction 20 to an injection system, and at an output junction 24 thereof to an extraction or reco¬ very system, generally designated ba the numeral 26. The recovery system is provided with a vacuum tank 28, which serves as a condenser and container for water vapor and contami¬ nants. The vacuum tank 28 is coupled to the output 24 of the wellbore 12 by piping 30. The vacuum tank 28 is provided with a drain valve 32 which allows the removal of recovered contamina¬ ted water and vapors. The vacuum tank 28 is supported on the surface area 1 by support posts 34. A motor 36 is coupled to drive a vacuum pump 38 by a shaft 48. This permits the creation of a vacuum in the tank 28 through a coupling pipe 42. The va¬ cuum pump 38 is also provided with an exhaust member 44 which leads to a suitable collection point (not shown) for extracting air and vapors that must be removed to create the vacuum in the vacuum tank 28. The exhaust member 44 is suitable to reduce the pressure in vacuum tank 28 to less than 50 percent of that of the atmosphere. The injection system of the vacuum apparatus 10 is coupled at input injunction 20 to a pump 45 through pipe 46 and a valve 48. The pump 44 is controlled by a motor 50 coupled thereto by a shaft 52. The pump 44 and motor 50 are supported above the sur¬ face area 14 by a platform member*«>-5 which includes supports 55. A steam generator 56, heater 58, chemical storage tank 60 and water supply 61 are coupled to the pump 44 by piping 62 and con¬ trol valves 64. The chemical storage tank 60 is for providing UTE SHEET such chemical additives or microbes as are necessary to enhance the- recovery of volatile liquid contaminants from the polluted contaminated subsurface area 16. The control valves 64 are used to control the flow of the contents of the generator 56, heater 5 58, tank 60 and water supply 61. The wellbore 12 is illustrated in detail in Figure 2, 3, 4 and 5. The wellbore 12 is provided with an outer screen or housing 66 and an inner pipe or housing 68. The inner housing 68 is pro- 10 vided with holes 69 and slots 70 for receiving sealing rings 72. The sealing rings 72 position the inner housing 68 in spaced re¬ lationship to the outer housing 66. This creates a space or an- nulus 74 between the inner housing 68 and outer housing 66. The sealing rings 72 prevent the loss of vacuum in the wellbore in 15 the same way that piston rings prevent loss of pressure in the piston chamber of an internal combustion engine. The sealing rings 72 are provided with holes 76. Additionally, a diagonal slot (not shown) may be provided which allows the 20 sealing ring 72 to expand tightly against the outer housing 66. The outer housing 66 is -provided with holes 80 formed therein. The holes 69 in the inner housing are alignable with the holes 76 in the sealing ring 72 and the holes 80 in the outher housing 25 66 when they are not blocked by non-perforated portions of the sealing rings. When this occurs, a conduit 82 is formed through which gases and fluids can pass in and out of the wellbore 12 (Figure 3) . 30 The inner housing can be rotated and slid up or down in the ou¬ ter housing 66 so fluids and gases can flow through the bottom portions of the wellbore 12 when the bottom row or rows of holes 69, 76 and 80 are opened to form a conduit 82. If the inner hou¬ sing 68 is raised, it would close off that bottom port 82 and 35 depending on how it was rotated it could open up one or more of the other ports 82 also. The rotation and slidable movement of the inner housing is ac¬ complished by a drive apparatus, which is illustrated in Figures 4 and 5. The drive apparatus 83 is provided with a first drive member generally designated by the numeral 84. The drive member 84 is formed with a recessed groove 86 in in¬ termediate portions thereof and a plurality of teeth 88 (Figure 5) formed on an internal surface thereof. The drive member 84 is provided to drivingly engage the inner housing 68 by aligning the teeth 88 in locking engagement around the inner housing. The drive member 84 is provided with a hinge 90 and lock 92 to allow the drive member 84 to be placed around and locked onto the in¬ ner housing 68. The drive apparatus 83 is provided also with a second drive mem¬ ber, generally designated by the numeral 94. The drive member 94 includes a recessed groove 96 formed therein. A belt 98 is pro¬ vided which is aligned in the groove 96 of the drive member 94 and the groove 86 of the drive member 84. The belt 98 drivingly couples the drive member 94 to the drive member 84. A shaft 100 is rotatabiy coupled to the drive member 94. A motor 102 is coupled to a gear 106 which in turn drives a gear 108. The gear 108 is coupled to rotate a shaft 110. The shaft 110 drivingly engages a gear 112 which is coupled to rotate the shaft 100. This in turn, rotates the drive members 94 and 84 and thus rota¬ tion of the inner housing 68 is accomplished. The drive apparatus is provided with a third drive member, which is provided with a first arm 116 having a shaft 118 coupled to one end thereof. The other end ot the arm 116 is pivotably coupled to a second arm 120 by a pivot pin 121. The arm 120 has a coupling member 122 formed thereon which is attached to the first drive member 84. A first piston assembly is provided having a piston housing 124 and a piston 125 seated in the housing. The piston 125 is coupled to the shaft 118 of the arm 116 by a coupler 115. A second piston assembly is provided having a piston housing 127 and a piston 128 seated in the housing. The piston 128 is coupled to the shaft 100 by a coupler 129. A pneumatic control device 130 is coupled through pneumatic lines 131 to pneumatically drive the piston assemblies. As a re¬ sult, the drive member 94 can be raised or lowered by the sli¬ ding movement of the piston 128 and the drive member 84 can be raised and lowered by the sliding movement of the piston 125 and movement of the drive member. This, in turn, raises and lowers the inner housing 68, in the outer housing 66 of the wellbore 12. This, along with the rotation of the inner housing facili¬ tates the opening and closing of ports 82 in the wellbore. This is accomplished with slidable up and down movement of the inner housing 66 of two to three feet and rotation thereof of three hundred sixty degrees (360) in either direction. The primary recovery process using the present invention in¬ volves lining up, say, holes 69, 76 and 80 to create conduit 82 to vacuum out the volatile pollutants in the stratum closest to outer port 80. This is continued until no traces of the target pollutants can be detected. Then the inner housing 68 is raised and/or rotated to close conduits 80 and to open up another con- duits(s) to allow another stratum to be vacuumed to the point that no further pollutants can be detected. The apparatus 10 shown in Figure 6, illustrates the operation of another a single-well configuration of the invention. This is a second recovery process. As illustrated, steam and surfactants (chemicals), if any, are released from the tanks 56 and 58 by releasing the appropriate valves 64. This allows a steam and chemical jet 132 to be injected into the contaminated subsurface ■ area 16. The inner housing 68 of the wellbore is positioned so only top ports 134 in an upper zone 136 of the contaminated sub¬ surface area 16 are opened to release the steam and chemicals . The steam and chemical jet 132 move along the upper zone 136 of contaminated subsurface area 16, and gravity causes the con¬ densed steam and chemicals to disburse throughout the subsurface area. This heats the contaminants and creates a chemical-in- water emulsion. As illustrated in Figure 7, once this is accomplished, top ports 134 are closed and bottom ports 140 are opened so the steam and chemical jet 132 pressurizes the base of the contaminated sub- surface area. This causes movement on a parallel path in a lower zone 142 away from ports 140. When the pressure is at the maxi¬ mum, then lower ports 140 are closed and upper ports 134 are reopened as recovery ports. The result is a flow of steam and surfactants towards upper ports 134, thereby creating turbulence and providing necessary energy to create a chemical-in-water or oil-in-water emulsion throughout the entire contaminated subsur¬ face area 16. When the contra-flow is completed, the next step is to open the bottom ports 140 of the well and concentrate a full vacuum drag on the bottom of the vadose zone and to pull the micellized chemical or oil-in-water emulsion from the upper stratas of the vadose zone where it will be drawn by the vacuum from upper ports 134 to the bottom strata thereby further saturating the vadose with chemicals. This is repeated over and over again, zone by zone and port by port until the recovery of the contami¬ nants in the contaminated subsurface area 16 is completed. The purpose of the "steam soak" with the steam 132 is to heat and chemically treat the contaminated subsurface area 16 thereby expediting the recovery of the liquid volatile contaminants through the increased vaporization that occurs with all such contaminants when heated. The heat and turbulence in conjunction with surfactants effectuates the total solubilization of the contaminants in the water in the vadose zone as chemical-in-wa¬ ter emulsions, which are pumped from recovery well 12. The following table shows the temperature required to boil vola¬ tile liquid contaminants before and after being mixed with water. Mixture Pure component Lb. steam/ Component boiling temp.(°C) boiling point (°C) Lb.component Benzene 68.3 80.1 0.092 Toluene 83.9 110.6 0.236 Bromoform 94.3 150.0 0.311 Chlorobenzene 91.0 112.5 0.405 Hexachloro- ethane 98.7 186.0 1.57 The first column in the above table shows the temperature at which the contaminants will boil off in the presence of steam and hot water. The second column shows the heat that would be required if the contaminants were not intermixed with the hot water and steam. Note that all of these contaminants can be boiled and thereby recovered by vacuum through wellbore 12 with¬ out necessarily having to suspend the chemicals in a micellar emulsion. The purpose of using surfactants (chemicals) in conjunction with this process is to miscellize the chemical and oil contaminants into the hot water from the steam drive as it is used according to the above description and thereby recover pollutants with boiling points over 100 °C. After the contaminants have been fully miscellized (suspended in water), they can be vacuumed out of the formation through the wellbore as described. As a further benefit, this invention can be used to recover certain volatile liquid contaminants, especially PCBs, which have extremely high boiling points (above 700 °C) and have a low solubility rate in water. In the case of these pollutants, specialized surfactants are used in the present invention to create chemical-in-water or oil-in-water emulsions within the polluted zones, thereby enab¬ ling the emulsions to be vacuumed out of the formation. SUBSTITUTE SHEET There are three generic groups of chemicals that are currently best suited to create the chemical-in-water and oil-in-water emulsions which are integral to the decontamination methods, that can be effectuated by and in conjunction with the methods and apparatus of the present invention. The first of these groups are the alcohol-ether-sulfates. These have passed the various ecological safety tests to the point that they have been cleared for human consumption by the U.S. F.D.A. The second of these, which is also non-toxic, is the alpha-olefin sulfonate class of chemicals and the third non- toxic candidate is the linear alkyl-benzene class sulfonates. In a variation on the single well configurations that are des- cribed above, water can be injected into the contaminated zone along with the micelle-generating surfactants and then allowed to soak. Following the optimal "soak time", the micellized che¬ mical contaminants can be drawn from the formation by vacuuming them either from one port of the wellbore, or from several ports, either together or individually. The preferred embodiment is to use the ports individually in a sequence which causes the maximum intermixing of the surfactant and the contaminants thus maximizing recovery. A third recovery process involves the drying out of the contami¬ nated area with hot air. This is accomplished by injecting su¬ perheated steam or hot air into the contaminated subsurface area 16. The hot air serves to volatilize chemical pollutants, inclu- ding those remaining after a steam sweep has removed most of the contaminants and lowered the boiling points on the others. The hot air that is injected in the single-well configuration can either be recovered on the surface (which must be insulated from the atmosphere), or back through the wellbore in a "huff'n puff" process which is explained in more detail below. Dry heating is accomplished by injecting air that has been heated to a level that is sufficiently high to vaporize all of the volatile liquid contaminants (superheated air) in the targeted vadose zone. This heat treatment can either be applied to the entire area or pre¬ ferentially it can be applied to discrete layers or zones within the area by sequentially opening and blocking the ports in the wellbore. Upon the completion of the heat treatment, the injection of su¬ per-heated air is stopped and the heated zone can then be "vacuumed" clean. This process is repeated "zone" by "zone" from the top of the contaminated area to the center of that area and then from the bottom up to the center. At all times a vacuum drag is kept on the bottom of the vadose zone to prevent the leakage of any contaminants into the atmosphere or aquifer. This process is repeated until all traces of the contaminants have been removed. This is know as a "huff'n puff" process to petro¬ leum engineers . A fourth recovery process is similar to the second an third pro¬ cess in that it uses the opening and closing of holes in a weli- bore to direct fluids through a vadose zone so as to effectuate the complete recovery of all pollutants. It differs from those processes in that it uses two or more wells to do what is done with a single well in the second and third process. With a single well process the steam and/or chemicals that are injected into the bottom strata from ports 140 are recovered through ports 134 in the same well. In a multi-well configuration the recovery would be done from ports 140 in a parallel well or wells thus assuring more distribution through the vadose zone. Figure 8 illustrates a multi-wellbore embodiment of the inven¬ tion, generally designated by the numeral 210. This embodiment can be used very effectively, for example, as a bioremediation embodiment of the invention. In this embodiment, two vertical parallelly spaced wellbores 212 and 214, are provided. It shall be understood that each wellbore 212 and 214 is provided with the injection, recovery and drive systems, as is illustrated in Figure 1. The wellbore 212 in Figure 8 is shown in temporary SUBSTITUTE SHEET usage as an injection well. Wellbore 214 is in use as a vacuum suction well. When wellbore 212 is rotated and/or slid to open up top port 2 6, simultaneously with top port 218 of wellbore 214 being opened, high pressure steam and chemicals can be dri- ven from port 216 to port 218. This causes a communication chan¬ nel 220 to be opened between the two wellbores 212 and 214 and serves to eliminate indigeous bacteria which might otherwise threaten the survival of the injected bacteria. After the communication channel 220 has been opened, cold water is pumped through the communication channel 220 to cool off the area. Next, a gel or acqueous polymer solution is injected which will tend to adhere to the circumference of the channel and thereby minimize the absorption of the injected chemicals. When the chemicals have traversed the channel between port 216 and port 218, port 216 and 218 are closed, the injection of steam and chemicals is continued to be between those two ports as is shown taking place between port 230 and port 232. In this example used the continued injection will fill zone 222 as shown. When zone 222 has been saturated, the ports 230 and 232 are closed and ports 234 and 236 are opened and the procedure is repeated until zone 138 is completely saturated. The contaminated subsurface area 16 can be also saturated with surfactants or toxiphilic bacteria as described above. The con¬ taminated subsurface area 16 can be also saturated with surfac¬ tants or toxiphilic bacteria by forming diagonal channels, such as channels 250, 252, 254, 256, 258 and 260, as shown in Figure 9. Communication between ports 216 and 236 would facilitate the sa¬ turation of zone 222 and the opening of a communication path between ports 230 and 242 would facilitate the saturation of zone 238. For example after toxiphilic microbes are injected, they will be supplied by air through the same patterns by which they were injected. An example of this process is where injected water is used in a criss-cross pattern through channels 250 and 256 patterns to move the chemicals (microbes) and facilitate the process of the microbes digesting the contaminants. After a co¬ lony of toxophilic bacteria is established in a contaminated area like this, the wellports in both wellbores can be closed and opened selectively to allow released gases to move the microbes throughout the formation. The contaminated subsurface area 16 can then be selectively vacuumed utilizing wellbores 212 and 214 to remove the contaminants to the surface. Figure 10 is a schematic of another multi-wellbore variation of the invention. This is considered a sixth recovery process. It should be understood that the wellbores discussed in this confi¬ guration of the invention are the same as previously disclosed herein. The wellbore pattern in Figure 10 is circular and com- posed of a plurality of wellbores 270 through 300 that are used as injection wellbores in the contaminated subsurface area 16. A wellbore or wellbores 310 (one shown) in the center of the pat¬ tern is the recovering wellbore. This recovering means 310 is used to create the low pressure zone from which the contaminants are recovered in the contaminated subsurface area 16 which is shown by dashed lines 312. The injection wellbores 270 through 300 are set at points around the recovering wellbore 310 to create communication channels such as channel 314 between injec¬ tion wellbores 270 and 272 to recovery wellbore 310. Additional channels can then be created using this technique such as chan¬ nel 316 between the injection wellbore 278 and wellbore 298. This particular configuration is not limited to injecting steam and/or water with chemicals. It can also be used to inject hot air into the contaminated subsurface area 16 to boil off the contaminants and drive them towards the recovery wellbore 310. With this configuration, the wellbores can be used alternately as injection and recovering wellbores by alternating the ports to create a multitude of paths or channels for recovery of con¬ taminants. This allows a systematic sweeping of the entire con- taminated subsurface area allowing the total recovery of the contaminants in the typical polluted vadose zone. TITUTE SHEET Another variation of the multiple well configuration is the use of four or more wellbores which are put in a horizontal, paral¬ lel array so as to bound a specific area. This embodiment invol¬ ves the use of two or more rows of parallel wellbores in which each row is composed of two or more wellbores so as to create a rectangular "box" which encompasses part or all of the contami¬ nated subsurface area. In this configuration, the water and sur¬ factant solution is flushed back and forth between the two rows in such a way as to micellize all of the contaminants into the chemical-in-water or oil-in-water emulsion. This cross-flushing and vacuuming process is continued until there are no traces of the contaminants in the vacuumed effluent. Certain of the steps that were described above for the single well configuration can also be used in the multi-well embodiment of the present invention. For instance, the entire polluted sub¬ surface area can be "soaked" with hot air or steam prior to in¬ itiating the drive operation. In addition, all of the wellbores can be used as producers after "the steam soak" treatment has been completed. An additional embodiment of the present invention involves the use of certain toxiphilic (toxin-degrading aerobic bacteria) that have proven useful in degrading liquid toxic contaminants into CO2 and benign and/or useful chemicals. This is the seventh recovery process. This recovery stage can utilize toxiphilic aerobic bacteria in conjunction with the above described multi-well configurations. First, either toxiphilic bacterial spores (the preferable embo¬ diment) or toxiphilic bacteria are injected in water (or suspen¬ ded in a polymerous solution), and are pumped under high pres¬ sure through a previously created "communication channel" from one wellbore port to its opposing port in another wellbore. As soon as the production wellbore shows evidence that the in¬ jected spores have migrated from the injector, the process is terminated only for the two ports that have been used for that specific layer or zone. The process is repeated on a "zone" by "zone" basis until the entire contaminated area between the two wellbores is saturated with the toxiphilic spores. The spores are then "shocked" to "life" in one of several ways. One way is to flush hot water through their "zone". Another is to use a nu¬ trient to "shock" them to life. A third way is to blow hot air across their zone. When the spores are activated, they become full-fledged bacteria who will proceed to consume the toxins around them. The reason for using spores in the particular process, instead of the actual bacteria, is that the spores are smaller and can be more easily driven deep into the polluted zone. The spores will normally be injected into the formation in a polymerous so- lution (preferably xanthan gum), to reduce their "fallout" rate in their voyage form the injection to the producing well. When they are suspended in the polymerous solution, they are far less apt to be adsorbed onto particles of sand and clay. After the bacteria are dispersed throughout the contaminated subsurface area and "shocked" to life, they can be further dis¬ bursed throughout the vadose zone by air and water which has been heated to the optimum temperature and controlled as to its movement by systematically opening and closing ports in the par¬ allel wellbores. The multiple port arrangement further allows oxigen and additional nutrients to be injected into the vadose zone in criss-crossing horizontal and diagonal patterns that will evenly dispense the toxiphilic microbes throughout the zone thereby effectuating total recovery of the pollutants. In certain locations, the soil may be so impermeable that it will require that microbes be injected in between the wells that are disclosed in this invention. This injection process can be accomplished by a slim-hole water jet drill that jets microbe- carrying water radically outward from the verticle drill. The process is repeated in this matter until the periodic "washing" of the formerly contaminated subsurface area fails to reveal any evidence of oil of toxic chemicals. At that time, the final step in the process will be taken which is to eradicate the baterial colony by terminating its nutrient supply. Each of the processes described can also be carried out with the aid of at least one wellbore (not shown) which is laid horizon¬ tally in the soil and is connected at least at one end with a wellbore which extends vertically or obliquely into the contami¬ nated subsurface and forms a connection to the vacuum apparatus or to the injection system. The laying of such pipe systems is known in particular from petroleum engineering. The horizontal wellbore should be essentially parallel to the groundwater zone or to other water-conveying strata. The horizontal wellbore cor¬ responds in its design and function to the extraction wells de¬ scribed above; the displacement or rotation of an inner housing within an outer housing can take place via coupling members - in particular flexible ones - as is likewise known from petroleum engineering. Such an arrangement has the great advantage that the contaminants present in the already contaminated area are prevented form migrating toward the water-conveying region, and poisoning or contamination of the water can thus be anticipated. For this reason, such a horizontally laid wellbore should be operated in particular during and after rainfalls. It proves to be particularly advantageous, especially in more extensively contaminated areas, to provide a "network" of horizontal wellbo¬ res which are arranged in parallel, in the form of a star or in the form of a circle, and can be operated in accordance with the process variants described above. To ensure that the contaminants can also be disposed of satis¬ factorily in practice, it is preferable to provide a control system for the recovered intermixture of substances and contami- nants (see above) . Thus, disposal from the contaminated area will be satisfactory if, in the stepwise decontamination pro¬ cess, it is ensured that disposal from the next stratum is in- itiated only when pollutants are no longer detectable in the stratum from which disposal is to be carried out first. It is therefore necessary for samples to be taken continuously from the recovered intermixture during the disposal process. Such a control system is described in, for example, the co-pending U.S. Patent Application, Serial No. 07/743,815 (Javadi et al. ) , the content of which is herewith considered disclosed. A sample to be analysed is taken, and the sample is routed through a sensor for determining the precise concentration of the contaminants. The concentration is then analysed by using computer software in a controller, and a signal is sent from the controller either into the injection system for further injecting a specified quantity of substances or into the means for rotating and/or sliding the inner housing of the wellbore. This control system may also have sensors which are to be coor¬ dinated with the particular open ports of the wellbore or can be coordinated with said ports. Thus, it is possible to provide a positioning means for the sensor(s), which should preferably be coupled with the positioning means effecting the displacement or rotation of the inner housing, so that this sensor tests the contaminants - and only these - extracted through the particular open port. If a contaminant is no longer detected, the next port and hence the next position of the sensor can be selected. The provision of a sensor coordinated with a particular open port can be effected in a particularly simple manner when in each case only one port of the wellbore is opened. It is then pos¬ sible to manage with one sensor only to be provided in or on top of the inner housing, which sensor need not be moved indepen- dently of the inner housing. The sensors might also be pushed up and down easily when posi¬ tioned on poles that are guided within the inner housing. Thereby the sensoring can be effected step by step over the ' whole length of the wellbore. If contaminants are detected in a certain area, it is possible to align the apertures of the inner housing with those of the outer housing in this area. As soon as the sensor detects the contamination, the sensor will send a signal to the controller; the controller will rotate the inner housing and align one of its holes with the hole of the outer housing where the contamination has been detected. If this is done by a rotational motion only, the inner housing is easier and better controllable. The block diagram shown in Fig.11 is a general description of the control system that is going to be used. The input set point 324 activates the system 320 - that contains the releasing and recovering means - in its normal condition, which is rotating and sliding up and down. H is the feedback sent by the sensors 321. Y is the output signal sent to the sensors 321 to have a complete controllability over the system 320. The controller 322 will rotate and/or axially move the inner housing to align one or more of its apertures with the apertures of the outer housing at the precise point where the contamina¬ tion has been detected by the moving sensor. The reason for using a moving sensor within the inner housing is to get the most accurate possible reading. If the reading were to be done at the vacuum tank on " the surface, the dilution by any leakage into the entire length of the inner housing would tend to dis¬ tort the readings by showing lower concentrations of contami- nants then is actually the case. This means that the apertures of the inner housing are aligned with those of the outer housing according to the signal sent by the sensors 321. Different kinds of sensors 321 may be used. For instance, since most of the contaminants 323 in the ground are a combination of hydrocarbons, sensors could be installed that detect hydrocar¬ bons and send signals to the controller. This is done by instal¬ ling a carbon resistor in the sensing element which is very sen¬ sitive to hydrocarbons. When a carbon resistor is exposed to hy- drocarbons, its resistivity decreases. Decreasing the resisti¬ vity of the resistor increases the current, that will notify the controller 322 to align the inner housing within the outer hou- sing so as to suck out the hydrocarbons. From the process variants described above by way of example and with reference to the Figures, it is clear that the number, po¬ sitioning and, where relevant, also the size of the holes in the two housings - but in particular in the inner housing - should be chosen according to the type of process chosen. Thus, depen¬ ding on whether the process in question involves flooding with steam, flushing and/or vacuuming of the contaminated area - in particular stratum by stratum or in the form of a criss-cross pattern - or is a "huff'n puff" process described using the third recovery process as an example, it is possible to provide interchangeable housings having the hole pattern adapted to the desired use. It is possible to relinquish the sealing means, especially the sealing rings, in case the inner housing is made of a different metal or alloy than the outer housing. For example, using alumi- num alloy for the inner housing and steel for the outer housing, the inner housing will have a higher thermal expansion coeffi¬ cient than the outer housing so that as it is heated the inner housing will form an airtight bond with the outer housing. The purpose of this is to allow the unheated inner housing to be freely rotated and moved axially so as to line up an inner hou¬ sing aperture with an outer housing aperture and then secured at that location by heating the inner housing by about 18 °C more than the normal temperature of the ground to expand the inner housing to form an airtight seal that prevents any undesirable leakage from the outer housing apertures to the inner. An alternate method is to utilize an inner housing which shrinks when flushed with cold water. With this technique - after a va¬ cuuming phase has been completed - the inner housing is flushed with water at about 17 °C less than the normal temperature of the ground which causes the inner housing to shrink thereby un- locking it. At normal temperatures a tight fit within the outer housing is formed. The choice between which of these two systems will be used will normally be based on the ambient ground temperatures. In cold climates, it will normally be advisable to use the system in which the inner housing is expanded with heat to fit flush against the outer housing. In tropical and semi-tropical clima¬ tes, the chilled water system should be used. SUBSTITUTE SHI=ET

Claims: CLAIMS 1. Method for removing underground contaminants from a contami¬ nated subsurface area (16) including the steps of: positioning at least one means (12) in the contaminated subsurface area (16) for recovering said contaminants and eventually - before said recovery - for releasing a predeter mined substance into said subsurface area; activating at least one rotating and sliding means (83) to sequentially and selectively open and close selected, pre ferably successive, ports (82) of the at least one positione means (12); applying a vacuum pressure selectively, preferably se¬ quentially, through open port (82) in the positioned means (12) to recover contaminants from an adjacent area of the contaminated subsurface area (16); and activating the rotating and sliding means (83) to selec¬ tively, preferably successively, close each open port (82) in the positioned means (12) before or while the next port (82) thereof is opened so that upon the application of vacuum pressure the contaminants in the entire contaminated subsur¬ face area (16) are recovered through said open ports (82) . 2. Method according to claim 1 , wherein said predetermined sub¬ stance is injected into at least one port (82) of the posi¬ tioned means (12), preferentially into sequentially and se- lectively opened successive ports (82) of the positioned means (12), so that the predetermined substance moves into - and eventually intermixes with the contaminants in - selected areas of the contaminated subsurface area (16). 3. Method for removing underground contaminants from a contami- nated subsurface area (16) including the steps of: SUBSTITUTE SHEET positioning at least one first means (212; 270, 272, 274, ...,300) in the contaminated subsurface area (16) - even¬ tually in a spaced circular configuration - for releasing a predetermined substance and/or for recovering said conta i- na ts; positioning at least one second means (214; 310) in the contaminated subsurface area (16) for recovering said conta¬ minants and/or for releasing a predetermined substance, in spaced relationship to the first positioned means (212; 270, 272, 274,...,300) - preferably in a respective center of a circularly configured plurality of the first positioned means (212; 270, 272, 274, ... ,300); activating at least one of first rotating and sliding means to open and close selected, preferably successive, ports of the first positioned means; activating at least one of second rotating and sliding means to open selective, preferably successive, ports of the second positioned means (214; 310) while at the same time at least one adjacently aligned port of the first positioned means is opened; injecting a predetermined substance into at least o e open port of the first positioned means (212; 270, 272,...,300) while applying a vacuum pressure to the at least one adjacently aligned opened port of the at least one second positioned means (214; 310) so that the predetermined sub¬ stance is pulled along a predetermined path (250, 252,...,260) between the aligned ports in the first (212; 270, 272,...,300) and the second positioned means (214; 310); activating the at least one first and second rotating and sliding means to close each of the successively opened ports in the first and the second positioned means before or while the next ports between the first and the second positioned means are open. 4. Method according to claim 3, including the steps of: activating the first and second rotating and sliding means to close all the ports of the first (212) and the se¬ cond (214) positioned means; activating the first and second rotating and sliding means to open the bottom ports of the first (212) and the se¬ cond (214) positioned means; applying a vacuum pressure selectively, preferably se¬ quentially, to each port in the first (212) and the second (214) positioned means beginning with the bottom ports the¬ reof until recovery of the contaminants in the entire contaminated subsurface area (16) is completed. 5. Method according to claim 3 or 4, wherein - preferaoly a plurality of - the first and the second means for recovering and/or releasing are positioned vertically, horizontally and/or obliquely - especially m a parallel configuration - in, eventually beneath, the contaminated subsurface area (16). 6. Method according to anyone of the preceding claims, wnerein said predetermined substance is selected from the group con¬ sisting of hot air, steam, surfactants and microorganisms, such as toxiphilic bacteria. 7. Method according to anyone of the preceding claims, inclu¬ ding the steps of at least once selectively heating and/or cooling at least one part (68, 66) of at least one of the po¬ sitioned means (12). 8. Method according to anyone of the preceding claims, wnerein before activating the rotating and sliding means and/or be¬ fore applying the vacuum pressure the kind and/or quantity of the contaminants are detected by sensormg means, especially by moving the sensormg means step by step up and/or down in¬ side the positioned means (12). 9. Method according to anyone of the preceding claims, inclu¬ ding the steps of: injecting the predetermined substance into at least one top port (134) of at least one positioned means (12); activating the at least one rotating and sliding means (83) to close said top port(s) (134) and to open at least one bottom port (140) of the at least one positioned means (12); injecting the predetermined substance into said bottom port(s) (140); activating said rotating and sliding means (83) to close said bottom port(s) (140) and open said top port(s) (134); applying a vacuum pressure to said top port(s) (134) so that the predetermined substance flows toward said top port(s) (134); activating said rotating and sliding means (83) to close said top ρort(s) (134) and open said bottom port(s) (140); and applying a vacuum pressure selectively, preferably se¬ quentially, to each open port in the positioned means (12), preferably beginning with the bottom port(s) (140) thereof, until recovery of the contaminants in the entire contaminated subsurface area is completed. 10. Apparatus for removing underground contaminants from a con¬ taminated subsurface area (16) including: at least one recovering means (12; 310) aligned in the contaminated subsurface area for recovering said contaminants from selected areas of the contaminated subsurface area (16); at least one means (83) for rotating and/or sliding por¬ tions (66, 68) of said recovering means (123; 310); at least one means (26) for applying vacuum pressure to said recovering means so that said contaminants can be ex¬ tracted from the contaminated area (16); and at least one means (28) for collecting and/or storing said contaminants as they are extracted from the contaminated subsurface area (16). 11. Apparatus for removing underground contaminants from a con¬ taminated subsurface area including: at least one releasing means (212; 270, 272, ..., 300) aligned in the contaminated subsurface area (16) for re¬ leasing predetermined substances into selected areas of the contaminated subsurface area (16); at least one recovering means (214; 310) for recovering the contaminants - eventually in intermixture with said sub- stances - from selected areas of the contaminated subsurface area (16); at least one means (83) for rotating and/or sliding por¬ tions (66, 68) of said releasing and recovering means; at least one means for injecting said predetermined sub- stances into said releasing means; at least one means (26) for applying vacuum pressure to said recovering means so that the contaminants - eventually in intermixture with said substances - can be extracted from the contaminated area (16); and at least one means (28) for collecting and/or storing the contaminants - eventually in intermixture with said substan¬ ces - as they are extracted from the contaminated subsurface area (16). 12. Apparatus according to claim 11 , wherein at least one re- leasing means (12; 214, 212) is adapted to act as recovering means (12; 212, 214) before, during or after the predeter- mined substances are released into selected areas of the con¬ taminated subsurface area (16). 13. Apparatus according to anyone of the claims 10 to 12, where¬ in the at least one releasing and/or recovering means (12; 212, 214) includes: an outer housing (66) having a plurality of apertures (80) formed therein; an inner housing (68) having a plurality of apertures (69) at least partly alignable with the apertures (80) in the outer housing (66) by rotating and/or sliding the inner hou¬ sing (68) relatively to the outer housing (66). 14. Apparatus according to claim 13, wherein the inner housing (68) is made of a material with a different thermal expansion coefficient from that of the outer housing (66) and wherein means for heating and/or cooling the inner housing (68) and/or the outer housing (66) are provided. 15. Apparatus according to claim 13 or 14, wherein a sealing means - preferably a plurality of sealing rings (72) - is aligned between the outer housing (66) and the inner housing (68) in spaced relationship - preferably in at least one re¬ cess (70) formed in the inner housing (68) -, and has a plu¬ rality of apertures (76) formed therein which are alignable with the apertures (69) in the inner housing (68) and outer housing (66) so that upon selective movement of the inner housing (68) predetermined ones of the apertures in the outer housing (66), in the sealing means (72), and in the inner housing (68) can be moved into direct alignment with each other. 16. Apparatus according to anyone of the claims 13 to 15, where- in the rotating and sliding means (83) includes: SUBSTITUTESHEET at least one first drive member (84) coupled to the inner housing (68) for sliding the inner housing (68) of the at least one releasing and/or recovering means (12) up and down at least one second drive member (94) for rotating the inner housing (68) of the at least one releasing and/or reco vering means (12) - preferentially coupled to the first driv member (84) . 17. Apparatus according to anyone of the claims 13 to 16, com¬ prising at least one piston member (125) - preferably a pneu matic member - coupled to the inner housing (68) and means for activating the at least one piston member to move along predetermined path. 18. Apparatus according to anyone of the claims 11 to 17, fur¬ ther including means - especially in the form of tanks (60) ' for storing at least one predetermined substance and pre¬ ferably at least one vacuum pump for extracting the substan¬ ces from the storing means (60) and feeding them to the re¬ leasing means (12). 19. Apparatus according to anyone of the claims 10 to 18, where- in the at least one means for applying a vacuum pressure (26) to the at least one recovering means (12) includes means for condensing and/or storing (28) the contaminants - eventually in intermixture with the predetermined substances - and for creating a predetermined suction pressure applicable to the at least one recovering means (12). 20. Apparatus according to anyone of the claims 11 to 19, inclu¬ ding at least two releasing and/or recovering means (212, 214), which are aligned with and spaced from each other to allow communication channels (250, 252, ..., 260) to be formed therebetween, and wherein further means for applying pressure to at least one releasing and/or recovering means (212, 214) is included for forcing the predetermined substances from the first means (212, 214) to the second means (214, 212) thereby SUBSTITUTESHEET selectively creating communication channels (250, 252,...,260) therebetween by and for extracting the contami¬ nants - eventually in intermixture with the substances - from the contaminated area (16). 21. Apparatus according to anyone of the claims 11 to 19 with a plurality of releasing and/or recovering means (270, 272,...,300, 310) whereby at least a part of the means (27, 272,...,300) is aligned in the contaminated subsurface area in at least one spaced circular configuration and whereby preferentially at least one means (310) is aligned respecti¬ vely in the center thereof. 22. Apparatus according to anyone of the claims 11 to 21 , where¬ by at least one releasing and/or recovering means is aligned essentially horizontally, preferably underneath the contami- nated area. 23. Apparatus according to anyone of the claims 10 to 22, com¬ prising at least one means for monitoring any contaminants especially comprising a controller (322) and related soft¬ ware, preferably at least one gas sensor (321 ) for the conta- minants - preferentially related to the apertures (69) of the inner housing (68) - and eventually comprising a means .of po¬ sitioning the sensor next to an aligned aperture (82). T

Inventors: SAVERY WIN, SAVERY, WIN
Applicants: TECHNOLIZENZ ETS, TECHNOLIZENZ ESTABLISHMENT
Application year: 1991
Main classification: B09B3
IPC codes: B09B3, B09C1, B65D88, B65G5, E21B34, E21B43