# Patent

## Title
Method of cleaning an industrial tank using electrical energy and critical fluid

## Abstract

A method of cleaning an industrial tank using electrical energy and critical fluid comprises the steps of transmitting electrical energy into an industrial tank to a first predetermined temperature, providing a critical fluid with a reactant or catalyst into the tank for diffusion into the contents of the tank at a predetermined pressure, transmitting electrical energy into the tank to heat the contents including the critical fluid to a second predetermined temperature to initiate reaction of a reactant in the critical fluid with a portion of the contents of the tank causing hydrocarbons and contaminants to be released for extraction as a vapor, liquid or dissolved in the critical fluid. A step of pressure cycling may be performed prior to a step of removing the contents of the tank including the hydrocarbons and contaminants. A further step includes separating the hydrocarbons, critical fluid, gases, and contaminants removed from the tank.

## Background
CROSS REFERENCE TO RELATED APPLICATIONS
This application is a divisional of application Ser. No. 11/314,857, filed Dec. 20, 2005, which is hereby incorporated herein by reference in its entirety.


BACKGROUND OF THE INVENTION
1. Field of the Invention
This invention relates generally to extraction of hydrocarbon fuels from a body of fixed fossil fuels in subsurface formations such as oil shale, heavy oil in aging wells, coal, lignite, peat and tar sands, and in particular to a method and apparatus for extraction of kerogen oil and hydrocarbon gas from oil shale in situ utilizing electrical energy and critical fluids (CF), and extraction of contaminants or residue from a body of fixed earth or from a vessel in situ utilizing electrical energy and critical fluids (CF).
2. Description of Related Art
Oil shale, also known as organic rich marlstone, contains organic matter comprised mainly of an insoluble solid material called kerogen. Kerogen decomposes during pyrolysis into kerogen oil and hydrocarbon gasses, which can be used as fuels or further refined into other transportation fuels or products. Shale oil and hydrocarbon gas can be generated from kerogen by a pyrolysis process, i.e. a treatment that consists of heating oil shale to elevated temperatures, typically 300 to 500° C. Prior to pyrolysis, kerogen products at room temperature have substantial portions of high viscosity non-transformed material such that they cannot be accessed within the rock/sand matrix. The shale oil is then refined into usable marketable products. Early attempts to process bodies of oil shale in situ by heating the kerogen in the oil shale, for example, injecting super-heated steam, hot liquids or other materials into the oil shale formation, have not been economically viable even if fundamentally feasible (which some were not). Early and current attempts to process bodies of oil shale above ground to obtain the kerogen oil and gas in the oil shale, for example, by mining, crushing and heating the shale in a retort type oven, have not been environmentally feasible nor economically viable.
It is well known to use critical fluids for enhanced oil and gas recovery by injecting naturally occurring carbon dioxide into existing reservoirs in order to maximize the output of oil and gas. By pumping carbon dioxide or air into the reservoirs, the existing oil or gas is displaced, and pushed up to levels where it is more easily extracted.
An article by M. Koel et al. entitled “Using Neoteric Solvents in Oil Shale Studies”, Pure Applied Chemistry, Vol. 73, No. 1, PP 153-159, 2001 discloses that supercritical fluid extraction (SFE) at elevated temperatures with carbon dioxide modified with methanol or water can be used to extract kerogen oil and gas from ground shale. This study was targeted at replacing analytical techniques using conventional solvents. Most of these solvents are not environmentally desirable and are impractical for use on a large scale.
In a paper by Treday, J. and Smith, J, JAIChE, Vol. 34, No. 4, pp 658-668, supercritical toluene is shown to be effective for the extraction of kerogen oil and gas from shale. This study used oil shale which was mined, carried to above ground levels, and ground to 1⁄4′′ diameter particles in preparation for the extraction. This labor intensive preparation process was to increase diffusivity, as the in-situ diffusivity reported would not support toluene's critical point of 320 degrees Celsius. “In-Situ” diffusivity of 5×10−9 M2/s was estimated, resulting in a penetration of a few centimeters per day which was insufficient. Furthermore the cost of toluene and the potential environmental impact of using toluene in-situ were prohibitive. Finally, maintaining the temperature of 320 degrees Celsius would be expensive in a toluene system.
In a paper by Willey et. al, “Reactivity Investigation of Mixtures of Propane on Nitrous Oxide”, scheduled for publication in December, 2005 in Process Safety Progress, the use of CO2 to inhibit an oxidation reaction from becoming a hazardous runaway reaction is demonstrated. However in this article it is not contemplated to use such a reactant for in-situ fossil fuel processing, shale heating, etc.
Critical fluids are compounds at temperatures and pressures approaching or exceeding the thermodynamic critical point of the compounds. These fluids are characterized by properties between those of gasses and liquids, e.g. diffusivities are much greater than liquids, but not as great as gasses and viscosity is lower than typical liquid viscosities. Density of critical fluids is a strong function of pressure. Density can range from gas to liquid, while the corresponding solvent properties of a critical fluid also vary with temperature and pressure which can be used to advantage in certain circumstances and with certain methods. Critical fluids were first discovered as a laboratory curiosity in the 1870's and have found many commercial uses. Supercritical and critical CO2 have been used for coffee decaffeination, wastewater cleanup and many other applications.
Many efforts have been attempted or proposed to heat large volumes of subsurface formations in situ using electric resistance, gas burner heating, steam injection and electromagnetic energy such as to obtain kerogen oil and gas from oil shale. Resistance type electrical elements have been positioned down a borehole via a power cable to heat the shale via conduction. Electromagnetic energy has been delivered via an antenna or microwave applicator. The antenna is positioned down a borehole via a coaxial cable or waveguide connecting it to a high-frequency power source on the surface. Shale heating is accomplished by radiation and dielectric absorption of the energy contained in the electromagnetic (EM) wave radiated by the antenna or applicator. This is superior to more common resistance heating which relies solely on conduction to transfer the heat. It is superior to steam heating which requires large amounts of water and energy present at the site.
U.S. Pat. No. 3,881,550 issued May 6, 1975 to Charles B. Barry and assigned to Ralph M. Parson Company, discloses a process for in situ recovery of hydrocarbons or heavy oil from tar sand formations by continuously injecting a hot solvent containing relatively large amounts of aromatics into the formations, and alternatively steam and solvents are cyclically and continuously injected into the formation to recover values by gravity drainage. The solvents are injected at a high temperature and consequently lie on top of the oil shale or tar sand and accordingly no complete mixing and dissolving of the heavy oil takes place.
U.S. Pat. No. 4,140,179 issued Feb. 20, 1979 to Raymond Kasevich, et al. and assigned to Raytheon Company discloses a system and method for producing subsurface heating of a formation comprising a plurality of groups of spaced RF energy radiators (dipole antennas) extending down boreholes to oil shale. The antenna elements must be matched to the electrical conditions of the surrounding formations. However, as the formation is heated, the electrical conditions can change whereby the dipole antenna elements may have to be removed and changed due to changes in temperature and content of organic material.
U.S. Pat. No. 4,508,168, issued Apr. 2, 1985 to Vernon L. Heeren and assigned to Raytheon Company, is incorporated herein by reference and describes an RF applicator positioned down a borehole supplied with electromagnetic energy through a coaxial transmission line whose outer conductor terminates in a choking structure comprising an enlarged coaxial stub extending back along the outer conductor. It is desirable that the frequency of an RF transmitter be variable to adjust for different impedances or different formations, and/or the output impedance of an impedance matching circuit be variable so that by means of a standing wave, the proper impedance is reflected through a relatively short transmission line stub and transmission line to the radiating RF applicator down in the formation. However, this approach by itself requires longer application of RF power and more variation in the power level with time. The injection of critical fluids (CF) will reduce the heating dependence, due solely on RF energy, simplifying the RF generation and monitoring equipment and reducing electrical energy consumed. The same is true if simpler electrical resistance heaters are used in place of the RF. Also, the injection of critical fluids (CF) as in the present invention increases the total output of the system, regardless of heat temperature or application method, due to its dilutent and carrier properties.
The process described in U.S. Pat. No. 4,140,179 and U.S. Pat. No. 4,508,168 and other methods using resistance heaters, require a significant amount of electric power to be generated at the surface to power the process and does not provide an active transport method for removing the products as they are formed and transporting them to the surface facilities. CO2, or another critical fluid, which also acts as an active transport mechanism, can potentially be capped in the shale after the extraction is complete thereby reducing greenhouse gases released to the atmosphere.
U.S. Pat. No. 5,065,819 issued Nov. 19, 1991 to Raymond S. Kasevich and assigned to KAI Technologies discloses an electromagnetic apparatus for in situ heating and recovery of organic and inorganic materials of subsurface formations such as oil shale, tar sands, heavy oil or sulfur. A high power RF generator which operates at either continuous wave or in a pulsed mode, supplies electromagnetic energy over a coaxial transmission line to a downhole collinear array antenna. A coaxial liquid-dielectric impedance transformer located in the wellhead couples the antenna to the RF generator. However, this requires continuous application and monitoring of the RF power source and the in-ground radiating hardware, to provide the necessary heating required for reclamation.
SUMMARY OF THE INVENTION
Accordingly, it is therefore an object of this invention to provide a method and apparatus for extraction of hydrocarbon fuel from a body of fixed fossil fuels using electrical energy and critical fluids (CF).
It is another object of this invention to provide a method and apparatus for in situ extraction of kerogen oil and gas from oil shale using a combination of RF energy and critical fluids.
It is a further object of this invention to provide a method and apparatus for effectively heating oil shale in situ using a combination of RF energy and a critical fluid.
It is a further object of this invention to provide a method and apparatus for effectively converting kerogen to useful production in-situ using RF energy and a critical fluid.
It is a further object of this invention to provide a method and apparatus for effectively obtaining gaseous and liquefied fuels from deep, otherwise uneconomic deposits of fixed fossil fuels using RF energy and critical fluids.
It is a further object of this invention to provide a method and apparatus for extraction of heavy oils from aging oil wells using electrical energy and critical fluids.
It is another object of this invention to provide a method and apparatus for extraction of hydrocarbon fuels, liquid and gaseous fuels, from coal, lignite, tar sands and peat using electrical energy or critical fluids.
It is a further object of this invention to provide a method and apparatus for remediation of oil and other hydrocarbon fuels from a spill site, land fill or other environmentally sensitive situation by using a combination of electrical energy and critical fluids and to recover liquid and gaseous fuels from same.
It is yet another object of this invention to provide a method and apparatus to remove material from any container with-out danger to an in-situ human, such as cleaning a large industrial tank of paint or oil sludge.
These and other subjects are further accomplished by a method of producing hydrocarbon fuel products from a body of fixed fossil fuels beneath an overburden comprising the steps of (a) transmitting electrical energy down a borehole to heat the body of fixed fossil fuels to a first predetermined temperature, (b) providing critical fluids with reactants or catalysts down the borehole for diffusion into the body of fixed fossil fuels at a predetermined pressure, (c) transmitting electrical energy down the borehole to heat the body of fixed fossil fuels and critical fluids to a second predetermined temperature, and (d) heating the critical fluids and the fixed fossil fuels with the electrical energy to the second predetermined temperature to initiate reaction of the reactants in the critical fluids with a fraction of the hydrocarbon fuel products in the body of fixed fossil fuels causing a portion of the remainder of the hydrocarbon fuel products to be released for extraction as a vapor, liquid or dissolved in the critical fluids. The method comprises the step of removing the hydrocarbon fuel products to a ground surface above the overburden. The method comprises the steps of pressure cycling in the borehole between 500 psi and 5000 psi and performing steps (b), (c) and (d) during each pressure cycling. The method comprises the step of separating the hydrocarbon fuel, critical fluids, gases and contaminants received from the product return line. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels includes the step of heating any one of the body of oil shale, tar sands, heavy petroleum from a spent well, coal, lignite or peat formation. The method comprises the step of monitoring the temperatures in an immediate region of the body of fixed fossil fuels to optimize producing the hydrocarbon fuel products, the temperature being sufficient to initiate oxidation reactions, such reactions providing additional heat required to efficiently release the hydrocarbon fuel products. The step of providing critical fluids with reactants or catalysts comprises the step of providing a mixture of carbon dioxide critical fluids such as carbon dioxide and an oxidant such as nitrous oxide or oxygen or a combination thereof. The step of providing critical fluids with reactants or catalysts down the borehole comprises the step of controlling the flow rate, pressure, and ratio of the critical fluids and reactants or catalysts into the borehole. The step of providing critical fluids down a borehole for diffusion into the body of fixed fossil fuels comprises the step of adding a modifier to the critical fluids, the modifier including one of alcohol, methanol, water or a hydrogen donor solvent. The step of heating the critical fluids and the fixed fossil fuels with the electrical energy initiating reaction of the critical fluids with the body of fixed fossil fuels comprises the step of raising the predetermined temperature to approximately 200 degrees Celsius. The method comprises the steps of providing a wellhead at the surface of the borehole for safely transferring the electrical energy and the critical fluids to the borehole and for receiving and connecting a product return line to means for separating gases, critical fluids, oil and contaminants. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels comprises the steps of generating electromagnetic energy with an RF generator, and providing a radiating structure in the borehole coupled to the RF generator to heat the body of fixed fossil fuels. The method further comprises the steps of performing steps (b), (c) and (d) for N cycles.
The objects are further accomplished by a method of producing hydrocarbon fuel products from a body of fixed fossil fuels beneath an overburden comprising the steps of (a) providing critical fluids with reactants or catalysts down the borehole for diffusion into the body of fixed fossil fuels at a predetermined pressure, (b) transmitting electrical energy down a borehole to heat the body of fixed fossil fuels and critical fluids to a predetermined temperature, and (c) heating the critical fluids and the fixed fossil fuels with the electrical energy to the predetermined temperature to initiate reaction of the reactants in the critical fluids with a fraction of the hydrocarbon fuel products in the body of fixed fossil fuels causing a portion of the remainder of the hydrocarbon fuel products to be released for extraction as a vapor, liquid or dissolved in the critical fluids. The method comprises the step of removing the hydrocarbon fuel products to a ground surface above the overburden. The method comprises the steps of pressure cycling in the borehole between 500 psi and 5000 psi and performing steps (a), (b) and (c) during each pressure cycle. The method comprises the step of separating the hydrocarbon fuel, critical fluids, gases and contaminants received from the product return line. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels includes the step of heating any one of the body of oil shale, tar sands, heavy petroleum from a spent well, coal, lignite or peat formation. The method comprises the step of monitoring the temperature in an immediate region of the body of fixed fossil fuels to optimize producing the hydrocarbon fuel products, the temperature being sufficient to initiate oxidation reactions, such reactions providing additional heat required to efficiently release the hydrocarbon fuel products. The step of providing critical fluids with reactants or catalysts comprises the step of providing a mixture of carbon dioxide critical fluids such as carbon dioxide and an oxidant such as nitrous oxide or oxygen or combinations thereof. The step of providing critical fluids with reactants or catalysts down the borehole comprises the step of controlling the flow rate, pressure, and ratio of the critical fluids and reactants or catalysts into the borehole. The step of providing critical fluids down a borehole for diffusion into the body of fixed fossil fuels comprises the step of adding a modifier to the critical fluids, the modifier including one of alcohol, methanol, water or a hydrogen donor solvent. The step of heating the critical fluids and the fixed fossil fuels with the electrical energy initiating reaction of the critical fluids with the body of fixed fossil fuels comprises the step of raising the predetermined temperature to approximately 200 degrees Celsius. The method comprises the steps of providing a wellhead at the surface of the borehole for safely transferring the electrical energy and the critical fluids to the borehole, and for receiving and connecting a product return line to means for separating gases, critical fluids, oil and contaminants. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels comprises the steps of generating electromagnetic energy with an RF generator, and providing a radiating structure in the borehole coupled to the RF generator to heat the body of fixed fossil fuels.
The objects are further accomplished by a method of producing hydrocarbon fuel products from a body of fixed fossil fuels beneath an overburden comprising the steps of (a) providing a carbon dioxide critical fluid down a borehole for diffusion into the body of fixed fossil fuels at a predetermined pressure, (b) transmitting electrical energy down the borehole to heat the body of fixed fossil fuels and the carbon dioxide critical fluid to a predetermined temperature, (c) pressure cycling in the borehole between 500 psi and 5000 psi, and (d) removing the hydrocarbon fuel products in the critical fluid with a product return line extending to a ground surface above the overburden. The method comprises the step of performing steps (a), (b), (c), and (d) during each predetermined pressure of the pressure cycling. The method comprises the step of separating the hydrocarbon fuel, critical fluids, gases and contaminants received from the product return line. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels and the critical fluids to a predetermined temperature comprises the step of setting the temperature to approximately 300 degrees Celsius. The step of transmitting electrical energy down a borehole to heat the body of fixed fossil fuels comprises the steps of generating electromagnetic energy with an RF generator, and providing a radiating structure in the borehole coupled to the RF generator to heat the body of fixed fossil fuels.
The objects are further accomplished by a method of producing hydrocarbon fuel products from an aging oil well having heavy oil comprising the steps of (a) transmitting electrical energy down a borehole to heat the heavy oil to a first predetermined temperature, (b) providing critical fluids with reactants or catalysts down the borehole for diffusion into the heavy oil at a predetermined pressure, (c) transmitting electrical energy down the borehole to heat the heavy oil and critical fluids to a second predetermined temperature, and (d) heating the critical fluids and the heavy oil with the electrical energy to the second predetermined temperature to initiate reaction of the reactants in the critical fluids with a portion of the hydrocarbon fuel products in the body of fixed fossil fuels causing the hydrocarbon fuel products to be released for extraction as a vapor, liquid or dissolved in the critical fluids. The method comprises the step of removing the hydrocarbon fuel products to a ground surface above the overburden. The method comprises the steps of pressure cycling the critical fluids in the oil well between 500 psi and 5000 psi and performing steps (b), (c) and (d) during each pressure cycle. The method comprises the step of separating the hydrocarbon fuel, critical fluids, gases and contaminants received from the product return line. The step of transmitting electrical energy down a borehole comprises the step of providing a radio frequency (RF) generator coupled to a transmission line for transferring electrical energy to an RF applicator positioned in the borehole.
The objects are further accomplished by a method of cleaning an industrial tank comprising the steps of (a) transmitting electrical energy into the tank to heat a contents of the tank to a first predetermined temperature, (b) providing critical fluids with reactants or catalysts into the tank for diffusion into the contents of the tank at a predetermined pressure, (c) transmitting electrical energy into the tank to heat the contents and critical fluids to a second predetermined temperature, and (d) heating the critical fluids and the contents of the tank with the electrical energy to the second predetermined temperature to initiate reaction of the reactants in the critical fluids with a portion of the contents of the tank causing hydrocarbons and contaminants to be released for extraction as a vapor, liquid or dissolved in the critical fluids. The method comprises the step of removing the hydrocarbons and contaminants from the tank. The method comprises the steps of pressure cycling in the tank between 500 psi and 5000 psi, and performing steps (b), (c) and (d) during each pressure cycling. The method comprises the step of separating the hydrocarbons, critical fluids, gases and contaminants removed from the tank.
Additional objects, features and advantages of the invention will become apparent to those skilled in the art upon consideration of the following detailed description of the preferred embodiments exemplifying the best mode of carrying out the invention as presently perceived.



BRIEF DESCRIPTION OF THE DRAWINGS
The appended claims particularly point out and distinctly claim the subject matter of this invention. The various objects, advantages and novel features of this invention will be more fully apparent from a reading of the following detailed description in conjunction with the accompanying drawings in which like reference numerals refer to like parts, and in which:
FIG. 1 is a flow chart of a method of producing hydrocarbon fuel products from a body of fixed fossil fuels according to the present invention.
FIG. 2A and FIG. 2B in combination illustrate the system apparatus of the present invention including a sectional view of a wellhead and borehole RF applicator.
FIG. 3A illustrates a first apparatus for obtaining thermocouple data using an RF choke to decouple RF energy from the thermocouple lines.
FIG. 3B illustrates a second apparatus for obtaining thermocouple data using the thermocouple wires to form a hollow RF choke to decouple RF energy from the thermocouple lines.
FIG. 4 is a plan view of a wellhead illustrating a ground plane at the surface having a surface grounding screen close to the wellhead to eliminate electromagnetic radiation for personnel safety and radial ground wires.
FIG. 5 is a flow chart of a first alternate embodiment of the method of producing hydrocarbon fuel products from a body of fixed fossil fuels without preheating according to the present invention.
FIG. 6 is a flow chart of a second alternate embodiment of the method of producing hydrocarbon fuel products from a body of fixed fossil fuels having repetitive cycles according to the present invention.
FIG. 7 is a flow chart of a third alternate embodiment of the method of producing hydrocarbon fuel products from a body of fixed fossil fuels without the use of reactants or catalysts according to the present invention.
FIG. 8 is a block diagram of an auxiliary well apparatus.
FIG. 9 is a simplified diagram of the system in FIGS. 2A and 2B showing the well head, borehole and RF applicator positioned in the ground at a predetermined angle.
FIG. 10 is an illustration of the application of the system of the present invention as shown in FIGS. 2A and 2B in an aging oil well comprising heavy oil.
FIG. 11 is a plan view of a plurality of systems of FIGS. 2A and 2B showing a central RF generator and a control station.
FIG. 12 is an illustration of a method of cleaning an industrial tank using a critical fluid and electrical energy.
FIG. 13 is a flow chart of the method of cleaning an industrial tank using a critical fluid and electrical energy.



DESCRIPTION OF THE PREFERRED EMBODIMENTS
Referring to FIG. 1, FIG. 2A and FIG. 2B, FIG. 1 shows the steps of a method 19 of producing hydrocarbon fuel products, such as kerogen oil 98 and gas, from a body of fixed fossil fuels, such as oil shale 14, or tar sand beneath an overburden 12, or heavy petroleum from a spent well, or hydrocarbon fuels from coal, lignite or peat. FIGS. 2A and 2B together illustrate a system 10 for accomplishing the method of FIG. 1.
The method 19 comprises a step 21 of transmitting electrical energy to heat a body of fixed fossil fuels, such as oil shale 14, to a first predetermined temperature such as 150 degrees Celsius to begin the kerogen 98 pyrolysis process, fracturing and modifying of the shale sufficiently to allow the critical fluids to easily penetrate deep into the formation and to reduce the total energy input required in some instances.
Step 21 is a preheating step to increase the speed of the critical fluid diffusion and depth of the critical fluids penetration into the body of fixed fossil fuels. The electrical energy down a borehole is provided by an RF generator 44 which generates electromagnetic energy and known to one skilled in the art.
The next step 23 provides critical fluids (CF), such as carbon dioxide (CO2), with reactants, such as nitrous oxide (N2O) or oxygen (O2), and catalysts may be added such as nano-sized iron oxide (Fe2O3), silica aerogel, and nano-sized Alumina (Al2O3) aerogel, down the borehole 16 for diffusion into the body of fixed fossil fuel or oil shale 14. However, in addition to the oxidants and catalysts, other modifiers can be added to the critical fluids to enhance the extraction of kerogen oil and gas. Materials such as water or alcohols (e.g. methanol), can be added to modify the polarity and solvent characteristics of the critical fluid. Modifiers can also participate in reactions improving the product quality and quantity by the addition of hydrogen to kerogen (known as hydrogen donor solvents). Tetralin and methanol are examples of hydrogen donor solvents.
The introduction of critical fluids may be at various pressures, from 300 PSI to 5000 PSI. In the preferred embodiment of FIG. 1, the critical fluids are introduced at 700 psi prior to a second heating in step 25; in step 25 further heating of the critical fluids (CO2) and the fixed fossil fuels occurs by transmitting electrical energy down the borehole 16 to reach a second predetermined temperature, in the range of 200 to 250 degrees Celsius. The lower initiation temperature uses less electrical energy and increases the overall process return on energy invested. This heating initiates an oxidation reaction, heating the critical fluids (CO2) reactants, catalysts and the fixed fossil fuels with an oxidation of a small fraction of the fixed fossil fuels causing the temperature to rise further to approximately 450 degrees Celsius and converts the kerogen to hydrocarbon fuel products such as kerogen oil and gas 98 to be released and extracted as a vapor, liquid, or dissolved in the critical fluids. In step 27 a decision is made as to whether or not to perform pressure cycling by proceeding to step 33 where cycling pressure occurs in the borehole 16 between 500 psi and 5000 psi. Also, the pressure of the critical fluids may be increased at this point to 5000 PSI to assist in the removal of the fuel products; in step 29, removing the hydrocarbon fuel products in the critical fluid occurs with a product return line 54 or lines extending from down in the borehole 16 or other boreholes to the ground surface above the overburden 12. In step 31, when the hydrocarbon fuel products in the critical fluids leave the wellhead 34 via the product return line 40, they pass to a gas/liquid separator 42 for separating the critical fluid (CO2) from the products and return the critical fluid to the borehole 16 or to storage.
Referring to FIG. 2A, a wellhead 34 is shown on top of a borehole 16 which has been drilled from the ground surface through the overburden 12, through the oil shale 14 and into a substrate 15. Overburden 12 may be sedimentary material forming a substantially gas tight cap over the oil shale 14 region. A seal to the overburden 12 is formed by a steel casing 18 extending from above the surface downwardly in borehole 16 to a point beneath the loose surface material, and the steel casing 18 is sealed to the walls of the borehole 16 by concrete region 20 surrounding the steel casing 18 which is well known to those of ordinary skill in the art. A lower portion of the wellhead 34, referred to as the wellhead casing 12 extends within the steel casing 18 and is attached to the steel casing 18, for example, by welding. The steel casing 18 design and application is determined by the condition of the specific site and formation and is known to one skilled in the art.
A critical fluid, such as carbon dioxide (CO2), is provided in a CO2 storage tank 70, and CO2 may also be provided from the gas/liquid separator 42 which separates gases and liquids obtained from the external product return line 40 provided by the system 10. A pump or compressor 72 moves the CO2 from the separator 42 to an in-line mixer 78. A nitrous oxide (N2O) storage tank 74 and an oxygen (O2) storage tank 76 are provided and their outputs are connected to the in-line mixer 78. Additional tanks 73 may be provided containing modifiers other reactants and other catalysts, such as nano-sized iron oxide (Fe2O3), silica aerogel or nano-sized Alumina (Al2O3). The mixture of the critical fluid, carbon dioxide (CO2), the nitrous oxide (N2O) and oxygen (O2) are provided by the in-line mixer 78 into the wellhead 34, down the borehole 16 and into the body of fixed fossil fuels for enhanced extracting, for example, of kerogen oil and gas 98 from oil shale 14.
Still referring to FIG. 2A, a center conductor 50 of a coaxial transmission line 53 is supported by the wellhead 34 being suspended via a landing nipple 30 and a support ring 28, from an insulator disk 26 and extending down to the center portion of the borehole 16. A ground shield or pipe 52 of the coax transmission line 53 provides a ground return path through a center conductor support 24. An RF generator 44, which provides electrical or electromagnetic energy in the frequency range between 100 KHZ and 100 MHZ, is coupled to an impedance matching circuit 46, and an RF coax line 48 from the impedance matching circuit 46 connects through a pressure window 49 to an input coax line 51 in the wellhead 34. The upper frequency of 100 MHZ is a practical limit based on the wavelength in shale. Oil Shale has a dielectric constant from 4 to 20 depending on the amount of kerogen and other materials in the shale. At 100 MHZ and lower, the wavelength in shale will be 1 meter and greater, resulting in sufficient penetration of the RF energy for efficient heating. The wavelength is inversely proportional to the frequency making lower frequencies even more effective. The input coax line 51 connects to the coax center conductor 50 via the landing nipple 30.
The product return line 54 is located within the coax center conductor 52, and it is supported by the landing nipple 30 in the wellhead 34. A ceramic crossover pipe 36 or other non-conductive pressure capable pipe isolates an external product return line 40 from RF voltage in the wellhead 34. A flexible coupling hose 38 is used to make up tolerances in the product return line 40 and to reduce strain on the ceramic crossover pipe 36. A feed port 41 is provided at the top of the wellhead 34 in the external product return line 40 for a gas lift line.
Referring to FIG. 2A and FIG. 2B, FIG. 2B shows a sectional view of an RF applicator 100. The coaxial transmission line 53 comprises several lengths of pipe (or coaxial ground shield) 52 joined together by a threaded couplings 60, and the upper end of the upper length of pipe 52 is threaded into an aperture in the center of the wellhead casing 22. The lower length of pipe 52 is threaded into an adapter coupling 112 which provides an enlarged threaded coupling to an upper coaxial stub 110 extending back up the borehole 16 for a distance of approximately an electrical eighth of a wavelength of the frequency to be radiated into the body of fixed fossil fuel or oil shale 14 by a radiator 102. A lower stub 108 of the same diameter as upper coaxial stub 110 extends downwardly from adapter coupling 112 for a distance equal to approximately an electrical quarter wavelength of the selected frequency band. If desired, a ceramic sleeve 106 having perforations may be placed in the fixed fossil fuel or oil shale 14 to prevent caving of the oil shale during the heating process.
The coaxial transmission line 53 (FIG. 2A) has the inner or center conductor 50 made, for example, of steel pipe lengths. The upper end of the upper section is attached to the support ring 28 and an insulator 32 spaces the inner conductor 50 electrically from the outer conductor 52. The inner conductor 50 extends downwardly through outer conductor 52 to a point beyond the lower end of tubular stub 108. An enlarged ceramic spacer 114 surrounds the inner conductor pipe 50 adjacent to a lower end of tubular stub 108 to space the inner conductor pipe 50 centrally within coaxial lower stub 108.
The region from the upper end of the upper stub or tubular member 110 to the lower end of lower stub or tubular member 108 is made an odd number of quarter wavelengths effective in oil shale in the operating frequency band of the device and forms an impedance matching section 104. More specifically, the distance from the adapter coupling 112 to the lower end of tubular member 108 is made approximately a quarter wavelength effective in air at the operating frequency of the system 10. The impedance matching section 104 of RF applicator 100 comprising lower stub 108 together with portions of the inner conductor 50 adjacent thereto act as an impedance matching transformer which improves the impedance match between coaxial transmission line 53 and the RF radiator 102.
The RF radiator 102 is formed by an enlarged section of a pipe or tubular member 88 threadably attached to the lower end of the lowest inner conductor 50 by an enlarging coupling adapter 86 and the lower end of enlarged tubular member 88 has a ceramic spacer 92 attached to the outer surface through to space member 88 from the borehole 16 surface (FIG. 2B). The RF radiator 102 is a half wave monopulse radiator and part of the RF applicator 100; it is described in U.S. Pat. No. 4,508,168 which, is incorporated herein by reference.
Still referring to FIG. 2B, the radiator 102 is shown in three positions within the borehole 16. When the kerogen oil and gas extraction is completed to the desired level in the lowest position in the borehole 16, the radiator 102 is raised so that it is in the position of radiator 102a, and likewise it may be raised again to the position of radiator 102b and so on to other desired locations. At each position a sequence of heating cycles 1, 2, 3, etc. described hereinafter occurs for penetration of the oil shale 14 located at greater distances from the radiator 102.
Referring to FIGS. 2A and 2B, an auxiliary well pipe 66 is provided spaced apart from the borehole 16 for providing an additional means for removing the fuel products, such as kerogen oil and gas, from beneath the overburden 12. The lower portion of the auxiliary well pipe 66 comprises perforations 65 to allow the fuel products to enter the well pipe 66 and be removed.
Referring to FIGS. 2A, 2B and FIG. 8, FIG. 8 is a block diagram of an auxiliary well apparatus 64 from which the auxiliary well pipe 66 extends downward. The auxiliary well apparatus 64 comprises an auxiliary well head 69 on top of the auxiliary well pipe 66, a pump 68 for bringing the fuel products to the surface and a gas/liquid separator 67 which is similar to the gas/liquid separator 42 in FIG. 2A and separates the oil, gas, critical fluids and contaminants.
Referring to FIGS. 2A, 2B, 3A and 3B, FIG. 2A shows the thermocouple bundle 37 in the upper portion of wellhead 34 supported by the landing nipple 30, and are accessible through the thermocouple output connector 39 of the RF wellhead 34. In this arrangement RF voltage is present on the thermocouple lines 56 when transmitting RF energy down hole. FIG. 3A shows a first embodiment for obtaining thermocouple data using RF chokes to decouple the thermocouple bundle 37 from the RF voltage in the wellhead 34. FIG. 3B shows a second embodiment for obtaining thermocouple data using the thermocouple bundle 37 to form a hollow RF choke 140 to decouple RF energy for the thermocouple lines or wires 56 in the bundle 37. The thermocouple lines 56 extend down the borehole within the outer conductor 52.
Referring to FIG. 3A, the individual thermocouple wires or lines 56 in thermocouple bundle 37 are insulated from the wellhead 34, and they are connected to RF chokes 134 that are insulated from ground. Filter capacitors 132 are connected to the chokes 134 to eliminate radio frequency interference (RFI) in the thermocouple measurement system. The thermocouple output is at the connector 39a that terminates the wires from point A at the junction between the RF chokes 134 and the filter capacitors 132.
Referring to FIG. 3B, a special hollow RF choke 140 is wound using the insulated thermocouple bundle 37 which comprises the insulated thermocouple wires inside of it, and the RF choke 140 is used to decouple the RF energy. The end of choke 140 is grounded to the RF wellhead 34 by a clamp 144 and the thermocouple wires 56 are connected at points B to filter capacitors 142 and an output connector 39b. 
Referring now to FIG. 4, a plan view of a wellhead having a surface grounding screen 152 positioned close to and around the wellhead 34 forming a ground plane to eliminate electromagnetic radiator for personnel and equipment safety. The ground screen 152 comprises a small mesh (i.e. 2 inches×3 inches). In addition to or instead of the grounding screen 152, ground wires 150 may be used extending radially a distance of one wavelength (minimum) from the wellhead 34 at intervals of 15 degrees. When the grounding wires 151 are used in combination with the grounding screen 152, the grounding wires 151 are welded to the edges 153 of the grounding screen 152 to insure good RF contact. In an array of wellheads 34, the ground should be continuous from wellhead to wellhead with the radial grounding wires extending outward from the perimeter of the wellhead field.
Referring now to FIG. 5, a flow chart of a first alternate embodiment is shown of the method 200 of producing hydrocarbon fuel products from a body of fixed fossil fuels without preheating the body of fixed fossil fuels. In step 202, critical fluids such as carbon dioxide (CO2), a reactant such as nitrous oxide (N2O), and a catalyst such as nano-sized iron oxide (Fe2O3) are provided down the borehole 16 via wellhead 34 for diffusing into a body of fixed fossil fuels such as oil shale 14 at a predetermined pressure in the range of 300 to 5000 psi. The use of reactants and catalysts improves the overall efficiency and effectiveness of the method or process. In Step 204, electrical energy is provided by the RF generator 44 down the borehole 16 to heat the body of fixed fossil fuels and critical fluid (CO2) to a predetermined temperature in the range of 200 to 250 degrees Celsius which causes a reaction of the reactant (N2O) with hydrocarbon fuel products in the body of fixed fossil fuels raising the temperature to approximately 350 to 450 degrees Celsius at which point hydrocarbon fuel products are produced, such as kerogen oil and gas 98 from the oil shale 14, which may be extracted as a vapor, liquid or dissolved in the critical fluid.
Still referring to FIG. 5, in step 206 a decision is made whether or not to cycle pressure. If a pressure cycle is performed, the cycling of pressure in the borehole 16 between 500 psi and 5000 psi is performed, and steps 202 and 204 are performed again as the pressure in the borehole 16 is cycled. However, during each cycle the pressure is controlled at the injection point. In step 208 removing the hydrocarbon fuel products in the critical fluid occurs continuously via the product return line 54 which extends to the ground surface above the overburden 12. In step 210 separating the critical fluid from the products is performed by the gas/liquid separator 42 (FIG. 2A), and the critical fluid (CO2) is returned to the borehole 16 or to the CO2 storage tank 70.
Referring to FIG. 6, a flow chart of a second alternate embodiment is shown of the method 220 of producing hydrocarbon fuel products from a body of fixed fossil fuels having repetitive cycles N. The addition of repetitive cycle N allows for penetration of the heat and critical fluids to provide additional extraction at each elevation of the fixed fossil fuels, or for the movement of the RF radiator 102 and entire process up and down elevations within a borehole 16 at a fixed level of penetration. In step 222, electrical energy, which is provided by the RF generator 44, is transmitted down the borehole 16 to heat the body of fixed fossil fuels to a first predetermined temperature of approximately 150 degrees Celsius. In step 224, critical fluids such as carbon dioxide (CO2), a reactant such as nitrous oxide (N2O), and a catalyst such a nano-sized metal oxide aerogel are provided down the borehole 16 at a predetermined pressure of between 300 and 5000 psi. The predetermined pressure is formation dependant, taking into account variables such as depth of the borehole, richness of the shale deposit, local geothermal conditions and the specific processing objectives. These objectives are a combination of technical factors such as the solubility of the shale oil and economic factors such as optimum amount of oil to recover. They include variables that the operator may choose to optimize the process. An example includes a process optimized to recover a lower percentage of total recoverable fuel in a rapid fashion. Such a quick recovery of a low percentage of fuels would have shorter cycle times and fewer cycles than a process optimized to recover a high percentage of the fuel from a specific borehole area. Each site specific iteration of the process can use a different combination of temperature and pressure of the incoming critical fluid. For example, a 1 mhz RF transmitter may be used to heat the formation to 150 degree Celsius. A 50 meter area around the RF transmitter will reach 150 degrees Celsius in approximately 6 to 10 days. This preheating step in some situations increases the permeability of the shale, increasing the effectiveness and permeation distance and reducing the time required for permeation of the critical fluids. Still referring to this example, the critical fluids would then be allowed to penetrate and react with the shale for a period of 21 to 90 days, depending on site specifics such as temperature, richness and porosity and depending on the parameters desired for that particular extraction, such as depth of penetration and cycle time. In a similar example, without the use of RF preheating, the critical fluids may be allowed to penetrate and react for a longer period of time, for example 120 days, also depending on site specifics and extraction parameters and goals. In some instances, the critical fluid can be pressurized and preheated. For example, if the critical fluids are preheated to 200 degrees Celsius, they would typically be injected into the borehole at about 3000 psi. If the critical fluids are injected with no preheating, and remain at their typical storage temperature of −20 degrees Celsius, they could be injected at the storage pressure of 300 psi, if that temperature/pressure combination meets favorably with the other variables at that site. Naturally, the actual temperature and pressure of the critical fluids at the bottom of the borehole 16 vary, being affected by several local conditions including depth, porosity of the shale, and geothermal temperatures.
Still referring to FIG. 6, in step 226 electrical energy from the RF generator 44 is provided down borehole 16 to further heat the critical fluids and the fixed fossil fuels to a second predetermined temperature in the range of 200 to 250 degrees Celsius which causes a reaction of the reactant (N2O) with hydrocarbon fuel products in the body of fixed fossil fuels raising the temperature to approximately 400 degrees Celsius at which point hydrocarbon fuel products are produced, such as kerogen oil and gas 98 from the oil shale 14. In step 228, a decision is made whether or not to cycle pressure. If pressure cycling is performed, the cycling of pressure in borehole 16 occurs between 500 psi and 5000 psi, and steps 224 and 226 are performed again as the pressure in borehole 16 is cycled. However, during each cycle the pressure is controlled at the injection point. During step 226, hydrocarbon fuel products are produced, and in step 230, removing the hydrocarbon fuel products in the critical fluid occurs continuously via the product return line 54 which extends to the ground surface. Cycling back to step 224 and then step 226 N times, where the RF energy initiates oxidation with the hydrocarbon fuel products, and performing pressure cycling while performing step 224 and 226 produces additional hydrocarbon fuel products. In step 232, separating the critical fluid from the products is performed by the gas/liquid separator 42 and the critical fluid (CO2) is returned to the borehole 16 or to the CO2 storage tank 70. The gas/liquid separator 42 may be embodied by a Horizontal Longitudinal Flow Separator (HLF) manufactured by NATCO Group, Inc., of 2950 North Loop West, Houston, Tex. 77092.
Referring to FIG. 7, a flow chart of a third alternate embodiment is shown of the method 240 of producing hydrocarbon fuel products from a body of fixed fossil fuels without the use of reactants or catalysts, which may be more cost effective or environmentally acceptable, for certain site specific applications. In step 242, a CO2 critical fluid is provided down the borehole 16 for diffusion into the body of fixed fossil fuels at a predetermined pressure in the range of 300 to 5000 psi. In step 244, electrical energy is transmitted down the borehole 16 by RF generator 44 to heat the body of fixed fossil fuels and critical fluid to a predetermined temperature of 300 to 400 degrees Celsius. For example, a 1 mhz RF transmission will heat 50 meters of surrounding area to 280 degrees Celsius in approximately 12-14 days, and to 380 degrees Celsius in 3 to 4 weeks depending on local site conditions. In step 246, cycling pressure in borehole 16 is performed between 500 psi and 5000 psi. In step 248, removing the hydrocarbon fuel products in the critical fluid occurs continuously via the product return line 54 which extends up to the ground surface and through the wellhead 34. As the hydrocarbon fuels products are removed, the method 240 cycles back to step 242 and repeats steps 242, 244 and 246 N times producing more products until a reduction in such products occurs.
Referring to FIG. 9, an alternate embodiment representation of system 10 of FIGS. 2A and 2B is shown simplified with only the well head 34, borehole 16, and applicator 102, positioned in the ground through the overburden 12 at a predetermined angle relative to vertical (as shown in FIGS. 2A and 2B). This angular arrangement of system 10 is used to provide desired heating and distribution of the critical fluids in various applications and compositions, such as a landfill or peat bog. Angular borehole arrangements may also be necessary to avoid various underground obstacles such as foundations or aquifers when a vertical borehole will meet with interference. The use of angular boreholes is well known to those skilled in the art and can be applied to both this apparatus and method. The RF applicator 102 is utilized in much the same fashion as in FIGS. 2A and 2B with the angular arrangement of the borehole being determined by the local conditions at the site, so as to extract the maximum contaminants or fuels using the fewest number of boreholes (16) and the least amount of electrical energy and the least volume of critical fluids to accomplish the goals of that particular project. The predetermined angle, pressure and temperature is site dependant.
The predetermined pressure is formation dependant, taking into account variables such as depth of the borehole, richness of the shale deposit or concentration of contaminants, local geothermal conditions and the specific processing objectives. The objectives are a combination of technical factors such as the solubility of the shale oil and economic factors such as optimum amount of oil to recover or the amount of hydrocarbon fuels or contaminants to recover from a peat bog, remediation site, etc. They include variables that the operator may choose to optimize the process. An example includes a process optimized to recover a lower percentage of total recoverable fuel in a rapid fashion. Such a quick recovery of a low percentage of fuels would have shorter cycle times and fewer cycles than a process optimized to recover a high percentage of the fuel from a specific borehole area. Each site specific iteration of the process can use a different combination of temperature and pressure of the incoming critical fluid. In some instances, the critical fluid can be pressurized and preheated, for example, if the critical fluids are preheated to 200 degrees Celsius, they would typically be injected into the borehole at about 3000 psi. If the critical fluids are injected with no preheating, and remain at their typical storage temperature of −20 degrees Celsius, they could be injected at the storage pressure of 300 psi if that temperature/pressure combination meets favorably with the other variables at that site. Naturally, the actual temperature and pressure of the critical fluids at the bottom of the borehole 16 vary, being affected by several local conditions including depth, porosity of the site, and geothermal temperatures.
Referring to FIG. 10, the system 10 of FIGS. 2A and 2B is shown having borehole 16 extending through the overburden 12 down into an aging oil well where most of an oil deposit 123 was removed and heavy oil 124 remains. Critical fluids in combination with RF energy (system 10) are used to extract the heavy oil to the surface via the product return line 54 in system 10, or via the auxiliary well pipe 66 and auxiliary well apparatus 64, or via the original oil well apparatus 120 and borehole 122. The method described in FIG. 1, FIG. 5, FIG. 6 and FIG. 7 with or without the use of reactants in the critical fluids may be used to recover the remaining heavy oil 124.
The methods of FIGS. 1, 5, 7, 9 and 11 and the apparatus of FIGS. 2A and 2B may be used for remediation of oil, other hydrocarbon fuels and contaminants from a spill site, land fill or other environmentally sensitive situations by using a combination of electrical energy and critical fluids. As described in FIG. 1, step 23, FIG. 5, Step 202 and FIG. 6, Step 224, critical fluids are supplied to the formation via the borehole 16. These critical fluids may have reactants or catalysts specifically chosen to physically or chemically bind or chemically neutralize or dissolve various hydrocarbon fuels, chemicals or undesired contaminants at the site. These reactants or catalysts provide additional cleansing, working with the natural dilutent and scrubbing and transport properties of the critical fluids. Some of these reactants may be heat activated by the RF, and some may not require heat activation. Some may be designed to be delivered and remain in-situ in the case of neutralizers and some may be designed to bind and carry undesired or desired compounds out of the site along with the critical fluids. For example, transuranic elements are a typical contaminate left behind by weapons manufacturing processes. These are difficult to remove by conventional methods, however the addition of nano-sized chelating agents to the critical fluids helps suspend the Uranium in the CO2 for transport. The RF heat adds additional efficiency and thermal gradient movement to the process for this type of difficult site remediation. Another example is the trichloroethane cleaning solvents many factories and municipalities used and dumped into the environment in years past, or creosotes which were typically deposited by town gas plants. These contaminants are easily diluted and scrubbed with the natural properties of critical CO2 and more thoroughly removed with the addition of RF heating.
Referring now to FIG. 11, a plan view of a plurality of systems 10a-10d of FIGS. 2A and 2B in a well field are shown having a central RF generator 44 connected to a control station 43. A plurality of boreholes 16a-16d are spaced apart in the well field by distances as much as several hundred feet and connected by a coax cabling 45a-45d through impedance matching circuits 46a-46d to the central RF generator 44, that is slaved to the control station 43. Critical fluids are provided to the boreholes 16a-16d via piping from in-line mixers 78a-78d which connect to the O2 storage tank 76, the N2O storage tank 74 and the CO2 storage tank 70. Product from the boreholes 16a-16d is routed to the gas/liquid separators 42a-42d where oil, gas and CO2 products and contaminants are derived. The RF power from central RF generator 44 may be shifted sequentially in any desired pattern to different radiators in different boreholes 16a-16d from a single RF generator based on input I1-I4 received from the control station 43. Similarly, the critical fluids may be shifted from one borehole to another as desired, based on inputs from the control station 43. Signals I1-I4 are fed to the control station 43 from the impedance matching circuits 46a-46d, as well as temperature monitoring signals T1-T4 measured in the boreholes 16 at subsurface layers. These inputs are used to monitor and/or adjust the frequency and impedance matching of the central RF generator 44 via control signals C1-C4 from the control station 43, and also to control the injection of critical fluids into the boreholes 16a-16d. The number of systems 10a-10d may be increased or decreased depending on the size of the well field being worked to obtain the oil, gas or CO2.
Referring to FIG. 12 and FIG. 13, FIG. 12 shows an illustration of a method 300 of cleaning an industrial tank 262 using critical fluid 268, electrical energy 278, and a settling tank 284 for separating the tank contents including hydrocarbons, contaminants, critical fluid, vapor, liquids and solids, and FIG. 13 is a flow chart of the method for cleaning the industrial tank 262. The method 300 comprises the step 302 of transmitting electrical energy 278 via an input into the tank 262 to heat the contents of the tank 262 to a first predetermined temperature up to approximately 150° C. (as described previously herein), step 304 of providing a critical fluid 268 with a reactant or catalyst into the tank 262 for diffusion into the contents of the tank 262 at a predetermined pressure, step 306 of transmitting electrical energy 278 into the tank 262 to heat the contents and critical fluid to a second predetermined temperature up to approximately 250° C. (as described previously herein), and step 308 of heating the critical fluid 268 and the contents of the tank 262 with the electrical energy 278 to the second predetermined temperature in order to initiate reaction of the reactant in the critical fluid with a portion of the contents of the tank causing hydrocarbons and contaminants to be released for extraction as a vapor, liquid or dissolved in the critical fluid. The critical fluid may be embodied by carbon dioxide (CO2). The reactant may be embodied by nitrous oxide (N2O) and the catalyst may be embodied by nano-sized iron oxide (Fe2O3) or other known critical fluids, reactants and catalysts may be used as described previously herein.
The method 300 comprises the optional step 310 of pressure cycling in the tank between 500 psi and 5000 psi, or proceeding directly to the step 312 of removing the contents of the tank 262 including the hydrocarbons and contaminants from the tank 262. The method 300 further comprises the option of performing steps 304, 306 and 308 during each pressure cycling (CYCLE N). The method 300 comprises the step 314 of separating the hydrocarbons, critical fluid, gas and contaminants removed from the tank 262 to a container such as a settling tank 284 commonly known in the art for the post processing of waste. The method 300 comprises the further step of repeating steps 304, 306 and 308 during each predetermined pressure cycle. Further, the method 300 further comprises the step of repeating step 304 for more complete cleaning of the industrial tank 262.
As shown in FIG. 3B, the temperature within the tank may be monitored by thermocouple 275 having wires 274 extending outside the tank 262 for obtaining the thermocouple data and monitoring when the first predetermined temperature and the second predetermined temperature are reached.
Further, a plurality of auxiliary production or extraction wells comprising pipes 66 and well apparatus 64 shown in FIGS. 2A and 2B may be added to the well field to increase the extraction of fuel products or contaminants. For example, in a remediation application, these additional auxiliary extraction wells, spaced at 50 meters or so from each RF/CF system 10, may help create a “flow” of contaminants out of a spoiled zone, while the RF/CF are left “on” and in the “pressure” mode, and the simple extraction wells are left in the “on” low pressure (extract) mode so that the critical fluids “flow” from the pump 72 high pressure side to the extraction well low pressure side and bring the contaminants with them. This operation may operate with or without the use of aerogels and catalysts. The extraction wells may be turned “off” for a period of time to allow pressure to build and to allow the CF to dilute and scrub, then turned back “on” to encourage the flow.
In a particular embodiment, the carbon dioxide critical fluid comprises a mixture of carbon dioxide (CO2) and an oxidant, the CO2 having a concentration of 80-100%, the oxidant comprising a mixture of nitrous oxide (N2O) having a concentration of 0 to 20% and oxygen (O2) having a concentration of 0 to 20%.
This invention has been disclosed in terms of certain embodiment. It will be apparent that many modifications can be made to the disclosed methods and apparatus without departing from the invention. Therefore, it is the intent of the appended claims to cover all such variations and modification as come within the true spirit and scope of this invention.

## Claims

1. A method of cleaning an industrial tank comprising the steps of:
(a) transmitting a first RF signal into the tank to heat contents of the tank to a first predetermined temperature;
(b) providing a carbon dioxide critical fluid into the tank;
(c) transmitting a second RF signal into the tank to heat the contents and critical fluid to a second predetermined temperature in the range of 200 to 250 degrees Celsius; and
(d) heating the critical fluid and the contents of the tank to the second predetermined temperature in order to initiate a reaction of an oxidant in the critical fluid with a portion of the contents of the tank thereby causing hydrocarbons and contaminants to be released from the contents of the tank for extraction as a vapor, liquid or dissolved in the critical fluid;
wherein the carbon dioxide critical fluid comprises a mixture of carbon dioxide (CO2) and the oxidant, the CO2 having a concentration of 80-100%, the oxidant comprising a mixture of nitrous oxide (N2O) having a concentration of greater than 0% but less than or equal to 20%, and oxygen (O2) having a concentration of greater than 0% but less than or equal to 20%.

2. The method as recited in claim 1 further comprising the step of removing hydrocarbons and contaminants from the tank.

3. The method as recited in claim 1 the steps of pressure cycling in the tank between 500 psi and 5000 psi, and performing steps (b), (c) and (d) during each pressure cycling.

4. The method as recited in claim 2 the step of separating hydrocarbons, critical fluids, gases and contaminants removed from the tank.

5. The method as recited in claim 1 further comprising the step of repeating steps (b), (c) and (d).

6. The method as recited in claim 2 further comprising the step of repeating step (b).

7. A method of extracting hydrocarbon fuel from an industrial tank, comprising:
(a) generating a first RF signal with an RF generator;
(b) transmitting the first RF signal into the industrial tank to heat contents of the industrial tank to a first temperature up to approximately 150 degrees Celsius;
(c) providing a carbon dioxide critical fluid into the industrial tank for diffusing into the contents of the industrial tank;
(d) generating a second RF signal with the RF generator;
(e) transmitting the second RF signal into the industrial tank to heat the contents of the industrial tank and carbon dioxide critical fluid to a second temperature in the range of 200 to 250 degrees Celsius to initiate a reaction between the contents of the industrial tank and the carbon dioxide critical fluid, thereby causing hydrocarbons and contaminants to be released from the contents of the tank for extraction; and
(f) removing the hydrocarbons and contaminants from the tank;
wherein the carbon dioxide critical fluid comprises a mixture of carbon dioxide (CO2) and an oxidant, the CO2 having a concentration of 80-100%, the oxidant comprising a mixture of nitrous oxide (N2O) having a concentration of greater than 0% but less than or equal to 20%, and oxygen (O2) having a concentration of greater than 0% but less than or equal to 20%.