The present disclosure concerns embodiments of a heating assembly that incorporates one or more plasma generators for heating a fluid.
A heat exchanger is a device designed to transfer heat from a first substance to a second, thereby decreasing the heat content of the first substance and increasing the heat content of the second. Heat exchangers have various industrial and commercial applications, including use in power plants, refrigerators, automobile radiators, etc., and various configurations of heat exchangers are known in the art. Methods of heating fluids have various specific applications which include heating cleaning fluids for treating a well bore or pipeline, and heating gases or liquids for use in fracking operations. In at least some of these applications, fluid-heating devices may need to be used in remote and/or numerous locations in a short time span. While many configurations of heat exchangers and devices for heating fluids are known, there is always a need for improvements in efficiency, capacity, portability, and other relevant characteristics of these devices.
Plasma is a state of matter distinct from the traditionally known liquid, gas, and solid states. Generally speaking, it is a gas whose particles have been ionized. Plasma can be created by various natural and artificial methods, including by the exposure of a gas to extreme heat and/or magnetic fields. Methods of generating and using plasma include, as examples, plasma globes, plasma television screens, fluorescent lamps, neon signs, and arc welding. In arc welding, an electric current is passed through the air between two spaced apart pieces of conductive material, thereby creating an electric arc (a very high temperature plasma) between them. Thus, in arc welding, an electric current is used to create a high temperature plasma which can heat and melt the materials to be welded.
Accordingly, it would be desirable to provide improved methods of generating high temperature plasma. Additionally, it would be advantageous to provide improved methods and devices for heating fluids utilizing the heat of high temperature plasma. Improvements in efficiency, capacity, and portability of such methods and devices would all be valuable.
Disclosed herein are embodiments of an invention allowing the generation of high-temperature plasma and its use for heating a fluid by heat exchange. In some embodiments, a plasma generator comprises an anode and a cathode between which an electrical potential difference can be established. A gas, such as air, is passed between the anode and the cathode, and an electric arc (a high temperature plasma) is created between the electrodes and through the gas. The high temperature plasma and/or high temperature exhaust gases can extend through a conduit over which a fluid to be heated flows, thereby allowing a heat exchange between the plasma and the fluid. Certain embodiments provide a coolant to flow within the anode and/or the cathode to protect against overheating. Certain embodiments utilize a plurality of plasma generators and a plurality of conduits. Certain embodiments utilize supplementary heat exchangers which use engine coolant, engine exhaust, or plasma exhaust to pre-heat the fluid to be heated before it flows over the conduit.
In one embodiment, a heating apparatus includes plural plasma generators and plural conduits, each conduit extending from a plasma generator and configured to receive plasma and/or plasma exhaust therefrom. Each conduit can comprise a burn chamber and a coil, with each burn chamber extending from a respective plasma generator and each coil extending from a respective burn chamber. A conduit housing can be provided which surrounds the conduits, and through which a fluid to be heated can flow. In some embodiments, an insert extends through the coils within the conduit housing such that a smaller volume of water passes through the conduit housing.
In another embodiment, a method comprises generating plasma within a burn chamber that is surrounded by a housing. A fluid is allowed to flow through the housing and over the burn chamber, thereby receiving heat from the plasma. The generation of plasma may be cyclical or periodic, such that the plasma generator is not constantly generating plasma. If multiple plasma generators are utilized, their cycles may be coordinated such that plasma is constantly generated by at least one of the generators.
In yet another embodiment, a plasma generator comprises a casing, an outer insulator positioned coaxially within the casing, a cathode positioned coaxially within the outer insulator, an inner insulator positioned coaxially within the cathode, and an anode positioned coaxially within the inner insulator. A difference in electrical potential can be established between the anode and the cathode, and thus an electric arc can be generated when a gas is passed between them. The inner insulator can have air channels extending along its length to allow a gas to be provided to the gap between the electrodes. The cathode and the anode can be provided with ducts or channels for allowing a coolant fluid (e.g., water) to flow through, in order to protect against overheating of the various components. Materials, components, and configurations can additionally be selected to increase the transfer of heat from the electrodes to the coolant fluid to further protect against overheating.
The disclosed embodiments should not be construed as limiting in any way. Instead, the present disclosure is directed toward all novel and nonobvious features and aspects of the various disclosed embodiments, alone or in various combinations and sub-combinations with one another.
The heating assembly 10 can be used to heat any type of fluid, including without limitation, liquids, such as water, diesel fuel, or kerosene, and gases, such as nitrogen, to name a few. For purposes of description, the heating assembly 10 will be described in the context of heating water, although the assembly can be used to heat other fluids.
In use, water to be heated in the plasma heat exchanger 12 enters the assembly via an inlet conduit 22 (e.g., pipe). A portion of the inlet water can be directed to flow through respective conduits 24, respective plasma exhaust heat exchangers 20, and respective conduits 26, and then into the plasma heat exchanger 12. Hot exhaust gases from the plasma heat exchanger 12 flow through respective conduits 32, respective plasma exhaust heat exchangers 20, and then through an exhaust manifold 34 that exhausts the gases to atmosphere. Inlet water flowing through plasma exhaust heat exchangers 20 therefore is pre-heated by the hot exhaust gas from the plasma heat exchanger.
A portion of the inlet water also can be directed to flow through a conduit 28, the engine exhaust heat exchanger 16, a conduit 30, and then into the plasma heat exchanger 12. Hot exhaust gases from the generator's engine flows through conduit 36, the engine exhaust heat exchanger 16, and then an exhaust conduit 38, which vents the exhaust gases to atmosphere. Inlet water flowing through the engine exhaust heat exchanger 16 therefore is preheated by the hot exhaust gases from the generator's engine.
A portion of the inlet water also can be directed to flow through a conduit 40, the engine coolant heat exchanger 18, a conduit 42, and then into the plasma heat exchanger 12. The engine coolant from the generator's engine (e.g., water or a water/antifreeze mixture) circulates through the engine coolant heat exchanger 18 via conduits 44, 46 to be cooled by the inlet water flowing into the plasma heat exchanger. Inlet water directed into the plasma heat exchanger via conduits 26, 30, and 42 is heated by plasma inside the plasma heat exchanger 12, as described in detail below. Heated water exits the plasma heat exchanger through an outlet conduit 48, from which the heated water can be directed to one or more users or processes requiring heated water.
The heating assembly 10 can also include an air compressor 52 (e.g., a rotary screw compressor or reciprocating compressor) that serves as a source of gas supplied to the plasma heat exchanger 12 for generating plasma. The compressed air from compressor 52 can flow through a conventional air/water separator 56, and into a compressed air storage tank 54. As best shown in
In an alternative embodiment not shown in
The heating assembly 10 can also include water pumps 58 placed in the inlet water conduits 22. As best shown in
The nozzle plate 100 includes one or more apertures 128, each of which is sized to receive and support a respective plasma generator 114. As best shown in
Each plasma generator 114 receives compressed air from the compressor 52 (or compressed gas from another source) and electrical current from the generator 14 (or another current source) to generate plasma, which is directed into respective burn chambers 122. Each burn chamber 122 is in fluid communication with a respective coil 124 that receives plasma and/or heated exhaust gases from the burn chamber. Each coil 124 can have an end portion 138 that extends through a corresponding aperture 140 in end plate 108 and is fluidly connected to a respective conduit 32 (
The burner housing 102 includes one or more inlet openings 130 (three in the illustrated embodiment) spaced in the circumferential direction around the outer surface of the housing. Each opening 130 is fluidly connected to a respective conduit 26 (
Referring to
The air injection cap 162 can be secured to the nozzle 166 by a plurality of bolts 174 that extend through corresponding openings in the cap 162 and are tightened into corresponding openings in an end flange 178 of the nozzle 166. The electrode 168 can be secured to air injection cap 162 by a central bolt 176 that extends through an opening in the cap 162 and is tightened in a central opening in the electrode 168. As best shown in
The air injection cap 162 includes an inlet conduit 180 that is fluidly connected to a source of compressed gas (e.g., compressed air). In the illustrated embodiment, for example, the inlet conduit 180 is connected to a compressed air line 64 that supplies compressed air from tank 54 to the plasma generator 114. As best shown in
The air injection cap 162 can further include a slot 194 that extends all the way through the side wall of the air injection cap. A conductor bar 196 (
As best shown in
As best shown in
In one specific embodiment, the various components of the heat exchanger 12 and the nozzle generator 114 are made of the following materials. The air injection cap 162 and the end plate 164 are made of polytetrafluoroethylene (PTFE). The nozzle 166 and the electrode 168 are made of a copper-tungsten alloy. The inner and outer insulators 172, 170, respectively, are made of 99% alumina. The housing 160 is made of 316L stainless steel. The conductor bar 194 is made of copper. The burner housing 102, the coil housing 104, the diverter 106, the burn chambers 122, the coils 124, the outlet pipe 112, and the heat sinks 118 are made of stainless steel, such as 316L or 310L stainless steel.
Referring to
The outer insulator 306 is generally cylindrically shaped and comprises an insulating material. As best seen in
As best illustrated in
In the illustrated configuration, pressurized water can be provided to and withdrawn from the various ducts in the anode and the cathode via conduits through the injection cap 304. The provision of flowing water helps insulate and protects against overheating of the anode 312 and cathode 308, which carry electric current for the generation of plasma. Also in this configuration, air for generating plasma is provided via conduits through the injection cap 304 to the air channels 314, which carry the air through the plasma generator.
In one specific embodiment, the components of the plasma generator 300 are made of the following materials. The injection cap 304 is made of PTFE. The cathode 308 and anode 312 are made of a copper-chromium alloy. The inner insulator 310 and the outer insulator 306 are made of 99% alumina, and the housing 302 is made of stainless steel such as grade 303 stainless steel.
Referring again to
The frequency of the power supply to the plasma generators can be adjusted to vary the electric arc between the electrode 168 and the nozzle 166. In particular, increasing the frequency above 60 Hz, to about 80-85 Hz or greater, can increase the frequency of sparks across the gap 214 to form a substantially annular electric arc extending between the electrode 168 and the nozzle 166, which promotes the generation of plasma from the air crossing the electric arc. The frequency of the power supply can be increased in some embodiments to at least 100 kHz, and in some embodiments up to 50 GHz.
The assembly 10 can further include a controller to control the operation of the various components of the assembly, including the generator 14, the air compressor 52, the pumps 58, and the plasma generators 114. The controller can be programmed (such as by user input) to set various operating parameters, such as the voltage, current and frequency of power supplied to each plasma generator and the operating sequence of each plasma generator. For example, each plasma generator 114 can be cycled on and off in a predetermined sequence with the other plasma generators to avoid overheating of the generators. In a specific implementation, for example, only one plasma generator is cycled on while the other two are cycled off. Initially, each plasma generator is cycled on for a period of about 5-7 seconds and then for a period of about 3 seconds for each subsequent cycle. It should be noted that the operating parameters of the generators 114 (including the operating sequence and frequency) can be varied depending on the specific application.
In a specific application, the heating assembly 10 is used to heat a cleaning fluid for treating a well bore or pipeline used in the transfer of hydrocarbon fluids, such as oil and gas. In the transfer and production of hydrocarbon fluids, well bores, pipelines and other conduits become clogged and/or fouled from accumulation of various compounds. A known technique for cleaning well bores and pipelines involves heating a solution and injecting the solution into the well bore and/or pipeline. A known heating system used for this purpose utilizes friction heating to heat about 4,800 gallons of water per hour to about 250 degrees F. The assembly 10 of the present disclosure can be used to heat about 18,000 gallons of water per hour from ambient (about 68 degrees F.) to about 290 degrees F. The heating assembly 10 can also be used to heat any of various other fluids, such as diesel fuel and kerosene, for cleaning well bores and pipelines. The heated fluid can also be used for fracking in which the fluid is injected into a well bore under pressure to create fractures in underground rock formations, such as shale rock and coal beds.
In another application, the heating assembly can be used to heat nitrogen for use in fracking. In such an application, liquid nitrogen stored in a tank (which can be on or adjacent the heating assembly) is supplied to an expansion chamber, which allows the nitrogen to expand into a gas. From the expansion chamber, the nitrogen flows into the plasma heat exchanger and is heated to at least about 85 degrees F. The heated nitrogen exiting the heat exchanger can be pressurized and injected into a well bore for fracking, as known in the art. In another embodiment, the nitrogen can be fed into the plasma generators 114 (instead of the compressed air) to create high temperature plasma from the nitrogen. The nitrogen cools to an appropriate working temperature and then can be pressurized and injected into a well bore.
The heating assembly 10 can also be used in a variety of other applications. For example, the heating assembly can be used in a variety of different industrial processes requiring a relatively large supply of a heated fluid, for heating a building, or for rapidly boiling water. In alternative embodiments, a plasma generator 114 can be used apart from the heat exchanger 12 for a variety of applications where heat from plasma can be utilized. For example, the plasma generator 114 can be used as a plasma torch for cutting metal, burning or incinerating material, such as trash or waste, or for various other uses.
In view of the many possible embodiments to which the principles of the disclosed invention may be applied, it should be recognized that the illustrated embodiments are only preferred examples of the invention and should not be taken as limiting the scope of the invention. Rather, the scope of the invention is defined by the following claims. I therefore claim as my invention all that comes within the scope and spirit of these claims.
This application claims the benefit of U.S. Provisional Patent Application No. 61/558,949, filed Nov. 11, 2011, which is hereby incorporated herein by reference.
Number | Date | Country | |
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61558949 | Nov 2011 | US |