SELF-CONTAINED ENERGY CENTER FOR PRODUCING MECHANICAL, ELECTRICAL, AND HEAT ENERGY

Abstract: Various forms of energy, such as mechanical, electrical, and/or heat energy are produced by an energy conversion mechanism (10) which includes a spool (16), the spool (16) including a shaft (22) on which a compressor (18) and turbine (20) are mounted. A generator (23) is operably connected to the energy conversion mechanism (10) for converting mechanical energy into electrical energy. Fuel and air are supplied separately to the compressor (18). A regenerator type heat exchanger (28) has a cold side for conducting compressed air traveling from an outlet of a compressor (18) to an inlet of the turbine (20), a hot side for conducting hot waste gas from the energy conversion mechanism (10), and a rotary core movable sequentially through the cold and hot sides for absorbing heat in the hot side and giving up heat in the cold side. A catalytic combustor (30) combusts the fuel at a location upstream of the turbine (20). During start-up, the catalytic combustor (30) is preheated independently of the heat exchanger (28) by an electric heater (40).

Description: SELF-CONTAINED ENERGY CENTER FOR PRODUCING MECHANICAL, ELECTRICAL, AND HEAT ENERGY Related Invention This is a continuation-in-part of Serial No. 08/934,217 filed September 19, 1997 and now abandoned. Background of the Invention The present invention relates to a self-contained energy center which can convert chemical energy into mechanical, electrical and heat energy, and methods for carrying this out. Such self-contained energy centers or cogeneration systems have been proposed, wherein chemical fuel is combined with compressed air from a compressor and is combusted. The resulting hot, high pressure air is delivered to a turbine which powers the compressor as well as electrical generating equipment. There are thus provided mechanical energy, electrical energy, and heat energy (i.e. waste heat from the turbine) which can be utilized to satisfy various needs such as heating, cooling, ventilating, lighting, etc. in a building. Such a system is disclosed, for example, in U.S. Patent No. 4,754,607 wherein fuel and air are combined in a mixer. The resulting mixture is delivered to the inlet of a compressor which compresses the mixture and outputs the compressed mixture to the cold side of a recuperator-type heat exchanger in which it becomes heated. The heated, high-pressure mixture is then delivered to the combustion chamber of a catalytic combustor. The resulting products of combustion are directed to the inlet of an expansion turbine mounted on the compressor shaft. After powering the turbine, the hot combustion gases are directed through the hot side of the heat exchanger. Accordingly, heat from those gases is transferred to the cooler air/fuel mixture passing through the cold side of the heat exchanger. The hot combustion gases exiting the hot side of the heat exchanger are delivered to heat-utilizing devices 99/14071 such as a hot water heater. Meanwhile, the turbine drives an electric generator mounted on the compressor shaft for producing electric power. During start-up of the system, the combustion chamber of the catalytic combustor is too cold to combust an air/fuel mixture. Therefore, a preheat burner, disposed in the conduit which conducts combustion gases from the turbine to the hot side of the heat exchanger, is supplied with fuel to create combustion gases. Those gases are then supplied to the hot side of the heat exchanger for preheating air delivered to the cold side of the heat exchanger from the compressor (which is being motored-over during start-up). The air preheated in the cold side of the heat exchanger is then conducted through the catalytic combustor to heat the latter. Once the catalytic combustor has been sufficiently heated to support combustion, the startup phase is over, and fuel is mixed with air fed to the compressor. That air/fuel mixture is then preheated in the heat exchanger before being delivered to the catalytic combustor for combustion therein. The above-described system exhibits certain shortcomings, especially as regards the start-up operation. In that regard, the start-up procedure requires that heat be transferred from a preheat burner to cold air traveling through a recuperator, and a subsequent transfer of that heat from the air to the catalytic reactor. That procedure is highly time consuming. Also, the need for both a catalytic reactor and a preheat burner complicates the system and increases its cost. Furthermore, the premixing of air and fuel prior to introduction into the compressor requires die use of a separate mixer, which involves added cost and complexity, as well as a potential source of an energy-diminishing pressure drop which increases the parasitic load on the system, causing the compressor to work harder. Also, during operation of the system, energy demands will vary, calling for changes in temperature of gas delivered to the turbine. To that end, die amount of fuel supplied to the catalytic combustor can be varied. Also, the system provides a valved by-pass whereby some of the exhaust gases can bypass me hot side of the 99/14071 recuperator, whereby the amount of heat being transmitted to the air/fuel mixture passing through the cold side of the recuperator can be varied. However, a recuperator utilizes a relatively massive heat transfer medium, so there is an appreciable delay before a temperature change at the hot side of the recuperator is realized at the cold side. As a result, the reaction time of me system is slower than would be desired. Accordingly, it is an object of the invention to provide a highly efficient, low cost, simplified cogeneration system which can be rapidly started. Summary of the Invention One aspect of the invention relates to an energy producing apparatus comprising a compressor side for compressing air/fuel, and a turbine side for driving the compressor side. An air supply conduit and a fuel supply conduit conduct air and fuel separately into a compressor of the compressor side to be compressed and mixed therein. An electrical generator is operably connected to the turbine side to be driven thereby for producing electrical energy. A heat exchanger has a first passage for conducting compressed air/fuel traveling from an outlet of the compressor side, and a second passage for conducting hot waste gas from an outlet gas from an outlet of the turbine side in heat exchange relationship with the compressed air/fuel in the first passage. A catalytic combustor is disposed between an outlet of the first passage of die heat exchanger and an inlet of die turbine side for reacting compressed air/fuel mixture received from the first passage prior to entry ±ereof into me turbine side. A preheating device is preferably provided for heating me catalytic combustor to a start-up temperature during start-up of the system. The preheating device, for example an electrical heater, is preferably operable to heat the catalytic combustor independently of the heat -exchanger. The preheater could comprise a fuel-burning start-up combustor disposed adjacent to the catalytic combustor. 99/14071 The heat exchanger preferably comprises a regenerator having a movable (e.g., rotatable) core sequentially passing tihrough the first and second passages for absorbing heat in die second passage and giving up heat in the first passage. A humidifier could be provided for introducing moisture into d e compressed air/fuel prior to entry diereof into the combustor. A steam generator could be provided to introduce steam into me inlet of die turbine side for starting me turbine side. A fuel pressurizing mechanism could be provided in me form of a roto cell device which includes a rotor having a plurality of cells spaced circumferentially around an outer periphery thereof for receiving fuel. The roto cell device would be operably connected to the spool to be rotated diereby. A take-off conduit would divert compressed air from the compressor side and introduce me diverted compressed air into me cells for pressurizing die fuel. Other aspects of the invention relate to various combinations of the above, and omer, features. For example, an aspect of the invention relates to a cogeneration apparatus which comprises an energy conversion mechamsm including a turbine for convening chemical fuel into energy. An electric generator is operably connected to me energy conversion mechanism for generating electricity. A diagnostic mechanism senses the operating conditions in me energy conversion mechanism. A transmitting mechanism connected to me diagnostic mechanism transmits signals to a central monitoring station. The invention also involves method aspects. For example, the invention relates to a mediod of varying a heat-to-electric ratio of a cogeneration system by varying me rate of heat transfer to the compressed gas in me first passage of die heat exchanger. Another method aspect involves employing a compressor as an air fuel mixer, i.e., the air and fuel are supplied separately mereto. Anomer method aspect involves a mediod of starting a multi-spool energy generating mechanism which includes a plurality of shafts, an expansion turbine mounted on each shaft, and a compressor mounted on at least two of die shafts, die compressors interconnected fluidly in series, and the turbines connected fluidly in series. The method comprises me steps of: A) causing the compressed air to expand in the upstream mrbine for rotating die shaft and compressor associated merewith; B) venting at least some of die exhaust gas discharged from the upstream turbine, prior to the entry thereof into a turbine disposed downstream of the upstream mrbine as the upstream turbine accelerates; and diereafter C) conducting all of the waste gas from the upstream mrbine to me downstream turbine after die energy generating mechanism reaches a predetermined operating state. Another method aspect involves a method of starting a cogeneration system wherein a catalytic reactor is preheated independently of me heat exchanger. Another method aspect of the invention comprises the provision of a catalytic reactor and a fuel-burning combustor, wherein fuel is combusted in the catalytic combustor during normal operation, and fuel is combusted in the combustor in the event of a failure of me catalytic reactor, in order to supply hot gas to die second passage of die heat exchanger which heats compressed air from die compressor. Brief Description of the Drawings The objects and advantages of the invention will become apparent from die following detailed description of preferred embodiments iereof in connection widi d e accompanying drawing in which like numerals designate like elements, and in which: FIG. 1 is a schematic view of a cogeneration system according to die present invention; 99/14071 FIG. 2 is a schematic view of a first embodiment of an energy conversion mechanism of me system depicted in FIG. 1; FIG. 3 is a view similar to FIG. 2 of a second embodiment of an energy conversion mechanism according to me invention; FIG. 4 is a view similar to FIG. 2 of yet another embodiment of an energy conversion mechanism according to me invention; FIG.5 is a schematic perspective view of a regenerator-type of heat exchanger usable in die present invention; FIG. 6 is a schematic view of a multi-spool type of energy conversion mechamsm according to die present invention: FIG. 7 is a schematic view of another embodiment of energy conversion mechanism according to d e invention, wherein a roto cell device is utilized to pressurize fuel; FIG. 8 is a schematic perspective view of roto cell device for pressurizing fuel; and FIG. 9 is a block diagram depicting a control mechamsm according to die present invention. Detailed Description of Preferred Embodiments of the Invention Depicted in Fig. 1 is an automated self-contained energy center or cogeneration system including an energy conversion mechanism 10 which converts chemical energy (e.g., combusted fuel) to mechanical and heat energy, a heat utility section 12 for utilizing or storing die heat energy, an electrical utility section 14 for converting some of me mechanical energy into electrical energy for immediate use or storage, and a mechanical utility section 15 (e.g., a flywheel) for immediate use or storage of mechanical energy. The system is ideally suitable for use in small facilities, such as, for example, a residence, a commercial site, or a light industrial site. The energy conversion mechanism comprises a compressor/turbine spool 16, also shown in Fig. 2, comprising a compressor 18 and an expansion turbine 20 interconnected by a shaft 22. During normal operating conditions, air is introduced into me compressor via main duct 24. Fuel is introduced via conduit 26 dirough die wall at die compressor moutii. The air and fuel are drawn separately into die compressor 18 where they are compressed and mixed, and die compressed air/fuel mixmre exiting die compressor is then heated by being passed dirough die cold side of a heat exchanger 28, which can be of any suitable type, but preferably is a regenerator type of heat exchanger. The mrbine 20, and all turbines used herein, is preferably a conventional turbine, most preferably a mrbine having a power output no greater than one megawatt. The heated air/fuel mixmre from die heat exchanger 28 is combusted in a conventional catalytic combustor or reactor 30, such as the type manufactured by Precision Combustion, Inc. of New Haven, CT, wherein fuel oxidizes on a catalyst surface, and brings die gas temperature to the required operating temperature of the mrbine inlet. That gas is tiien expanded in die mrbine 20. Exhaust gas from the mrbine 20 is expanded in a power mrbine 32 to which an electrical generator 23 is connected. Exhaust gas from the power mrbine 32 is tiien conducted dirough die hot side of die heat exchanger in heat exchange relationship with air/fuel mixmre passing dirough die cold side of die heat exchanger 28. The heating of die air/fiiel mixture in the heat exchanger 28 will have brought die air/fuel mixmre to the threshold temperature necessary for oxidation to occur in the catalytic combustor 30. For example, d e above-mentioned catalytic combustor of Precision Combustion Inc. needs to be heated to approximately 500°C. The use of a catalytic combustor is beneficial because it only needs an air/fuel molar ratio of about 100, in contrast to a typical non-catalytic combustor which requires an air/fuel molar ratio of about 18. A catalytic combustor is relatively clean burning, emitting less tiian approximately 1 ppm NO x and 10 ppm CO. An additional benefit is tiiat d e air/fuel mixmre will never be in a regime where there will be a fire or explosion danger in the compressor or anywhere in die system. The system may also include a back-up fuel-burning combustor 34 (optional) located downstream of the power mrbine 32 to operate die system in die event that the catalytic combustor 30 malfunctions. Exhaust gas from the back-up combustor would pass dirough die hot side of die heat exchanger 28 to heat the compressed air/fuel to a sufficient temperature to operate die turbine during an interim period until the catalytic combustor has been repaired. The heat exchanger can comprise any suitable type, but preferably comprises a regenerator which is schematically depicted in Fig. 6 and described in greater detail in concurrentiy filed application Serial No. (Attorney Docket No. 031064-009), die disclosure of which is incorporated by reference herein. The regenerator forms two separate paths in a housing, namely a hot path HP through which hot gases flow, and a cold path CP through which a cold air/fuel mixmre flows. A porous heat-transfer core C rotates within die housing such that each portion of the core sequentially travels through die two pati s. Thus, the portions of the core traveling through die hot path are heated and subsequently give up tiiat heat to the cold air/fuel flow when traveling through the cold patii. Suitable seals are provided to resist leakage between die hot and cold gas flows. Such a regenerator type of heat exchanger 28 is highly effective, and the rate of heat transfer can be conveniently controlled merely by varying the rate of rotation of the core. The mass of die core is relatively low (e.g., as compared to tiiat of a recuperator). Therefore, me time required to heat such a regenerator is short as compared to a recuperator type of heat exchanger. Principles of operation of a regenerator have been previously known, and regenerators are commercially available, e.g., from Allison Engine Co. of Indianapolis, IN. The regenerator disclosed in above-referenced Serial No. involves a novel sealing arrangement. O 99/14071 The above description has characterized die post start-up state operation of die system, i.e., die state when the catalytic combustor 30 is sufficiently hot to support combustion of me fuel. However, at the imtiation of start-up, die catalytic combustor is below its activation temperature. Accordingly, there is provided an electric heater 40, or any otiier suitable heat generator, which supplies heat to die catalytic combustor to rapidly bring it to its start-up temperature. A conventional heater for a catalytic combustor is disclosed in U.S. Patent No. 4,065,917, the disclosure of which is incorporated herein by reference. The start-up phase continues until the catalytic combustor 30 reaches a temperature (i.e., a start-up temperature) which is hot enough to combust fuel. Once a start-up temperature is reached in the catalytic combustor 30, a starter motor 36 is actuated to rotate the shaft 22, causing fuel and air to be drawn into the compressor 18 and conducted to the catalytic combustor 30. An alternative way of starting the system involves turning the spool 16 by d e starter motor to circulate air (but no fuel) through d e cold side of die regenerator while rotating the regenerator. The back-up combustor 34 would be actuated to supply hot gas to the regenerator for heating the air passing dirough d e cold side. That heated air would d en pass dirough, and heat, die catalytic combustor 30. When the catalytic combustor 30 reaches a start-up temperature, fuel would be introduced to the compressor 30, and die resulting compressed air/fuel would be combusted in die catalytic combustor 30. In lieu of driving d e electrical generator 23 by a separate power mrbine 32, the generator could be driven by the shaft 22, as depicted in Fig. 3. Yet anodier arrangement is depicted in Fig. 4 wherein a conventional hybrid fuel combustor 44 is employed. The hybrid combustor includes a catalytic reactor downstream part 44A, and an upstream burner 44B. Only die burner part 44B would be employed during start-up, in order to heat die catalytic reactor part 44 A by conduction, radiation and convection. Fuel would be supplied to die burner 44B during start-up, via line 42. After start-up, fuel would be cut off from die burner and introduced into the compressor via line 26. Alternatively, the burner part could be disposed downstream of die catalytic part. During normal start-up of die Fig. 4 arrangement, the compressor is motor-driven at a relatively low speed, so mere is not a high pressure at die fuel inlet of me burner part 44B which would inhibit the inflow of fuel. If it were instead desired to motor-drive die compressor at a high speed, a dirottle 44 for air flow would be provided at die compressor inlet. By dirottling- down, the pressure at die fuel inlet of the start-up combustor can be reduced, in order to facilitate the injection of fuel. Although a gaseous type of fuel is preferred in die present invention, liquid or solid fuel could be used. For example, die liquid fuel could be atomized, gasified or vaporized. Liquid fuels which can be used include gasoline, naphtiias, No. 2 heating oils, diesel, and kerosene. Any solid fuel which is capable of being gasified could be used. Suitable gaseous fuels include natural gas, propane, acetylene, process and refinery gases, and all manner of hydrocarbon mixtures, as well as low-BTU gas. Since the present invention utilizes an adjustable heat exchanger, i.e. , a regenerator 28, the amount of heat transferred from the high-temperature mrbine exhaust to the low-temperature compressor discharge can be regulated, and changes in heat transfer at die hot side can be realized almost instantaneously at the cold side. That is, when die core C of the regenerator is spinning at die optimum speed, a maximum amount of exhaust heat is recycled into die mrbine to yield die lowest heat- to-electric ratio. At a certain minimum rotation speed of die core C, there will occur a maximum heat-to-electric ratio. Thus, by varying die rate of spinning of the regenerator core, the heat-to- electric ratio can be varied between die two extremes. The efficiency of the heat exchanger can be monitored by temperamre sensors located upstream and downstream diereof, enabling die heat transfer rate to be automatically controlled to achieve die desired effectiveness. The ability to adjust the rate of heat transfer in die heat exchanger provides anodier advantage, namely me ability to provide, in effect, an instantaneous reduction O 99/14071 11 in load. Typical recuperator-type heat exchangers have substantial dieπnal mass. That means that die gases in the machine stay hot for a long period after there has been a command to reduce die load output. In contrast, since the efficiency of the regenerator in die presently claimed invention can be instantiy spoiled, die gases can be more rapidly cooled to provide a rapid response to a load reduction command. Conventional features can be employed to increase shaft power and efficiency in systems of die type disclosed in connection witii Figs. 2-4. That is, as shown in Figs. 4, water can be supplied via conduit 52 to be combined witii die compressed air/fuel mixmre traveling to the heat exchanger. The water can be mixed with die compressed air/fuel mixmre in a conventional samrator 54. This humidification of the air increases die mass flow of the mrbine 20 while making the heat collected by die water prior to its introduction into the samrator available for utilization in he expansion process within the mrbine. Thus, me added water increases shaft power and efficiency. When this shaft power is transformed into electrical energy, the electric-to-heat ratio is increased. By varying the water flow rate to die samrator, or altering the ratio of water to air in the samrator, or changing e place where moismre is injected into the samrator, the degree of humidification of die air can be varied to produce an optimum electric-to-heat ratio. Although only shown in connection with Fig. 4, die samrator 54 could be utilized in d e systems described in connection witii Figs. 2 and 3. It will be appreciated tiiat due to die combination of the above-described techniques for varying die electric-to-heat ratio, i.e., varying the amount of heat • transferred in die regenerator 28 and varying the amount of humidification applied in the samrator 54, a high degree of control over me electric-to-heat ratio can be achieved. By tiius momtoring the electric and heat loads in die building and automatically correspondingly varying the electric-to-heat ratio, an optimum fuel utilization can be achieved by adjusting d e spinning rate of the heat exchanger core and/or die amount of humidification of die compressed air. Depicted in Fig. 6 is a multi-spool embodiment of die invention which realizes the advantages explained earlier in connection witii the low-pressure fuel introduction. As explained earlier herein, the start-up mode of a conventional multi- spool arrangement is time-consuming and also is costly from a fuel expenditure standpoint. In addition, it requires significantly more power from the starter motor or starting device to turn d e multiple shafts of a multi-spool machine during startup. The present invention alleviates those shortcomings by providing a valve, or so-called waste gate 60 in conjunction witii at least one (but preferably botii) of the turbines 20A, 20B of the lower compressor/turbine spools 16A, 16B, and also die power mrbine 20C (if such an optional power mrbine 20C is used). Such a waste gate 60 enables some or all of the high pressure gas to be vented to atmosphere thereby minimizing the occurrence of pressure build-up in die upstream mrbine, or starter mrbine 20. That makes die starter mrbine easier to operate. The waste gate could be installed at, or upstream of, the mrbine inlet. It is noted tiiat waste gates per se are conventional and have typically been used on turbochargers of reciprocating internal combustion engines for venting some of the mrbine inlet air when the exit pressure at the compressor is too high for the strength of die combustion engine construction. By thus venting some of tiie air that would otherwise drive die mrbine of the turbocharger, the compressor is driven more slowly, so the exit pressure is reduced to a safe level. The use of a waste gate in the present invention achieves a different result, i.e., to keep the downstream turbines at low pressure until die upstream turbines speed up. During start-up, the electric heater 40 heats the catalytic combustor as described earlier herein (no fuel as yet being supplied via conduit 26). At this time, the waste gates 60 associated with either or both of the lower turbines 20A, 20B are fully or partially opened for venting the incoming air. Once the catalyst is heated to its light-off temperamre, the starter motor is started and fuel is added. Because the downstream spools have open waste gates, die first mrbine 20 can be started relatively easily, quickly, and efficiently. Once the starter mrbine 20 of the spool 16 99/14071 13 is at a predetermined speed (or die downstream compressor of the spool 16 reaches a predetermined discharge pressure) and die starter motor 27 has been shut off, the waste gate on die next turbine 20B is closed. Hence, die spool 16B starts to spin and eventually reaches the predetermined speed, whereupon the waste gate 60 of the next turbine 20A is closed and it, too, begins to spin. It will be appreciated that the use of waste gates in tiiat fashion will enable the start-up operation of a multi-spool arrangement to be carried out relatively easily and quickly, with reduced fuel costs. In addition, this procedure could be carried out with conventional (non-catalytic) combustors and witiiout the heat exchanger 28. It should be noted that mechanical energy from any or all of the spools 16, 16A, 16B, or a spool of the power mrbine 20C, can be utilized, e.g., to generate electric energy. The systems described thus far have relied upon a starter motor 27 (e.g. , an electric motor) for the start-up procedure. It will be appreciated that there may occur the need to start the system when there is no connection available to a working electric grid (e.g. , during a power black-out) or an external fuel source. One way of achieving this is to utilize a storage battery 70 as shown in Fig. 1 for driving d e starter motor. Another way of providing for a total black start capability is through the use of a steam generator 72, shown in Fig. 6, which can be used in combination witii, or in lieu of, the storage battery/starter motor arrangement. The steam boiler is connected to an in-house fuel supply such as a tank 74 of liquid fuel or natural gas supplied dirough a pipeline. The steam generator is pre-supplied with water which, when necessary, is heated by a burner connected to die fuel tank, to supply steam for driving die mrbine 20. The steam could be introduced to the turbine inlet, or it could be injected directly into die mrbine via nozzles to impinge directly against the mrbine blades. This rotates die mrbine which in turn drives die compressor to begin the air flow and start die system. Once die system is up and running at full speed, die 14 electrical utility section 14 produces electrical power to assist with normal operations, such as powering the onboard control and communication system. The steam generator 72 is shown in combination with die multi-spool arrangement of Fig. 7, but it could be used with the single-spool arrangements of Figs. 2-4 as well. When used in a multi-spool arrangement, wherein die turbines are equipped with the previously described waste gates 60, the black start can be further facilitated by opening the waste gates 60 in die previously described manner. Other ways of producing steam, in lieu of die boiler 72, include die catalytic decomposition of stored hydrogen peroxide, and die use of energy released by absorbing hydrogen gas onto a palladium surface or other suitable surface. As noted earlier herein, die present invention envisions that no means will be necessary to highly pressurize the fuel being supplied to the system since me fuel is introduced at low-pressure locations. In die event however, that it should prove necessary to pressurize the fuel to a level above tiie inlet pressure (up to the compressor discharge pressure), a highly efficient system for doing so is depicted in Figs. 7 and 8. In tiiat system, there is provided a conventional roto cell compressor 80 of the type sold by ASEA Brown Boveri (ABB) and described in SAE Technical Paper 830-234, March 1983, which is incorporated herein by reference. That compressor includes a rotor 81 forming circumferentially spaced cells 82 on its outer periphery. The rotor is rotated by a shaft 84 which is operably connected to die shaft 22 of the spool, and low pressure gaseous fuel is introduced sequentially into die cells via conduit 42. Some of the high-pressure air from the compressor is diverted to the cells via conduit 88 following the introduction of die fuel, whereby the air expands in the cells and pressurizes the fuel which is supplied to die catalytic combustor via conduit 92. The spent air-is men routed via conduit 90 to the inlet to preclude any leakage of fuel gas to the atmosphere. An advantage of such an arrangement is that the small mechanical force for rotating the rotor, and the high-pressure air for compressing die fuel are generated by die highly efficient spool mechanism 16, whereby no additional fuel pressurizing devices are necessary. 14071 15 It will be appreciated tiiat the present invention provides a self-contained energy center which is smaller, and less complex and costly tiian conventional cogeneration systems, and can be quickly started. The energy center can be safely and efficiently operated by many types of readily available chemical fuels. Accordingly, die center is highly suitable for use in small facilities where it can be driven by natural gas received from low pressure delivery pipes. Accordingly, a home or other small facility can generate all of its energy needs independently of traditional electric utilities which may be characterized by periodic outages. In the event that it proves necessary to pressurize the fuel before it is introduced into die air stream, a method for doing so is provided which avoids using a gas compressor separate from the existing hardware. Furthermore, he electric-to- fuel ratio produced by the system can be adjusted in order to match die fluctuating electric and heating loads of die building. The invention enables a multi-spool system to be started more quickly and efficiently. This also is useful when the need arises for a total black start, e.g. by die use of steam power or the like for operating the spool. The present invention also envisages a control system which provides die energy center witii a high degree of control and reliability. The control system, depicted in Fig. 9, includes suitable computing devices 100 to which are connected numerous on-board sensors for continuously supplying data associated witii the operating components of the energy center. For example, a sensor 102 senses compressor output pressure, a sensor 104 senses combustor inlet temperamre. a sensor 106 senses combustor outlet temperamre, a sensor 108 senses catalyst surface temperature, a sensor 110 senses regenerator inlet temperamre, a sensor 112 senses regenerator outlet temperamre, a sensor 114 senses oil pressure, a sensor 116 senses oil temperature, a sensor 118 senses generator output voltage, a sensor 120 senses generator output current, a sensor 122 senses generator output waveform, a sensor 124 senses exhaust gas temperature, a sensor 126 senses mrbine RPM, and a sensor 128 senses mrbine load (e.g., by sensing torque). The control system is also 99/14071 16 connected to the operable components of the energy center, including, but not limited to, die starter motor 27, the fuel valve 31, a regenerator motor 130, an oil pump 132, wastegates 60, and a central monitoring station 134. The control system controls all aspects of machine operation, including die start-up sequence, wastegate operation, fuel metering, and regenerator rotation speed, for example. In the event tiiat a building contains multiple cogeneration systems of die above-disclosed type, the control system would selectively mm units on and off and control the fuel to each unit in response to the load. In addition, die control system will keep track of part-load operation history in a multi-system configuration, to be able to cycle individual machines to evenly distribute die wear between them. The control system also contains conventional diagnostic software capable of determining if there is a fault on board, and taking necessary remedial action. For example, if oil pressure were sensed as being low, die control system could operate die oil pump at a faster speed to boost oil pressure. Also, the control system could communicate the existence of such a fault to the central monitoring station 134. That would alert service personnel who could respond to the simation. Moreover, the service personnel could call up the status of a particular energy center twenty four hours per day and receive a full report on the status and performance history thereof. In addition, die control system will allow die operation of die energy center to be remotely controlled by an operator communicating over a communications network. If the energy center were used in conjunction with other "smart" technology, such as LONWorks (available from Echelon, Inc.), the control system would process requests for additional power and ramp the turbine(s) to meet tiie load while controlling which power requests are satisfied at a given point in time. This is known as "demand-side" management. For example, upon the starting of a refrigerator compressor, which typically requires a large power input, the control system would control the energy center to increase die power output. Once the power output was matched to the requirement of e new load, die control system would mm the refrigerator compressor on. Alternatively, if the control system were instructed by die user that the refrigerator compressor was an "essential" load, die control system would divert power from inessential loads to meet die refrigerator compressor load immediately. The self-contained energy center can be combined witii a local or wide-area network which employs, or is independent of, the present electrical infrastructure. An integrated digital communication and control system (DCCS) 90 can be provided which supplies load regulation, energy management fuel control, and in some embodiments, communication and integration with loads served, witii other centers, with dispatch centers, witii monitoring, diagnostic, and maintenance centers. The DCCS may serve in load following or in load control modes. For example, in load following, a dispatch demand signal may be received, and electrical load increased or decreased at a rate and to a level appropriate for the signal. In load control, die DCCS may anticipate the need for an essential electrical load (lighting for example) and may postpone a non-essential load such as refrigeration or water heating to manage fuel demand. The DCCS will interface and be compatible with, distributed controller technology, and other "smart building" technology. Possible methods that can be employed will be apparent to tiiose skilled in the art, including, but not limited to: (1) feedback, (2) multivariable, (3) expert system, and (4) fuzzy logic. The DCCS is capable of interacting with individual component loads at die served site to smooth peaking requirements and optimize energy usage. The system could be made self- diagnostic, and able to communicate its condition to central locations using modems, communication via die electrical supply system, radio, and other means. The energy center can be used in a residence, a commercial site, or a light industrial site for satisfying die usual needs such as heating, ventilation and air conditioning. The invention can satisfy heating needs by, for example, (a) tiie generation of electricity which is converted to heat energy, or (b) the use of waste gas from the heat exchanger. Ventilation needs can be satisfied by fans driven by the generated electricity. Air conditioning or otiier cooling needs can be satisfied by, for example, (a) generation of electricity which is then converted to mechanical energy 99/14071 18 (shaft rotation, reciprocation, etc.) for mechanical refrigeration or heat energy which, in turn, drives refrigeration cycles such as vaporization/condensation cycles or heat absorption chillers, (b) conversion of fuel chemical energy to mechanical energy which is input to a refrigeration cycle, and (c) recovery of heat energy from direct firing or from exhaust heat recovery by an absorption chiller or vaporization/condensation refrigeration cycle. In addition, hot water needs may be served by, for example, (a) generation of electricity which is then converted to heat energy, (b) recovery of energy from a refrigeration cycle, and (c) recovery of heat energy from direct firing or from exhaust heat recovery. All of these may be used for on-demand water heating or for heating water to be used as thermal energy. Altiiough the present invention has been described in connection with preferred embodiments diereof, it will be appreciated by those skilled in the art that additions, deletions, modifications, and substitutions not specifically described may be made widiout departing from the spirit and scope of die invention as defined in die appended claims.

Claims: WHAT IS CLAIMED IS: 1. An energy producing apparatus comprising: an energy conversion mechanism comprising a compressor side for compressing air/fuel, and a mrbine side for driving the compressor side; an air supply conduit and a fuel supply conduit for conducting air and fuel separately into a compressor of the compressor side to be compressed and mixed tiierein; an electrical generator operably connected to die mrbine side to be driven thereby for producing electrical energy; a heat exchanger having a first passage for conducting compressed air/fuel traveling from an outlet of the compressor side, and a second passage for conducting hot waste gas from an outlet of the mrbine side in heat exchange relationship with the compressed air/fuel in the first passage; and a catalytic combustor disposed between an outlet of the first passage of the heat exchanger and an inlet of the mrbine side for reacting compressed air/fiiel mixmre received from die first passage prior to entry thereof into the mrbine side. 2. The apparatus according to claim 1, further including preheating means for heating the catalytic combustor to a start-up temperamre during start-up. 3. The apparatus according to claim 2, wherein die preheating means is operable to heat the catalytic combustor independently of die heat exchanger. 99/14071 20 4. The apparatus according to claim 3 wherein tiie preheating means comprises an electric heater. 5. The apparatus according to claim 1 wherein die preheating means comprises a fuel burning start-up combustor disposed adjacent to the catalytic combustor. 6. The apparatus according to claim 1, further including a blow-off valve communicating with an outiet of the mrbine side for conducting mrbine waste gas away from die heat exchanger during start-up. 7. The apparatus according to claim 1 further including a fuel burning back-up combustor located between an outlet of tiie mrbine side and an inlet of the second passage of the heat exchanger. 8. The apparatus according to claim 1 wherein die heat exchanger comprises a regenerator having a movable core sequentially passing dirough he first and second passages for absorbing heat in die second passage and giving up heat in the first passage. 9. The apparatus according to claim 8 wherein a speed of die core of the regenerator is adjustable to vary an amount of heat tt-ansferred to compressed air/fuel traveling dirough the first passage. 10. The apparatus according to claim 8 wherein the core of the regenerator is rotatable about an axis of rotation. 11. The apparatus according to claim 1 wherein die turbine side constitutes a first mrbine mounted on a common shaft with a compressor of the compressor side, and a second turbine having an inlet fluidly connected to an outlet of the first mrbine; the generator operably connected to the second turbine; the second passage of the heat exchanger connected to a waste gas outlet of die second mrbine. 12. The apparatus according to claim 1, further including a humidifier for introducing moismre into the compressed air/fuel prior to entry diereof into the catalytic combustor. 13. The apparatus according to claim 12 wherein the humidifier comprises an adjustable humidifier for varying the moismre introduced into the compressed air/fuel. 14. The apparatus according to claim 1 further including a steam generator arranged to introduce steam into die inlet of die mrbine side for starting die mrbine side. 15. The apparatus according to claim 1 further comprising a fuel pressurizing mechanism for pressurizing fuel delivered to die compressor side, the fuel pressurizing mechanism comprising a roto cell device including a rotor having a plurality of cells spaced circumferentially around an outer periphery thereof for receiving fuel, the roto cell device operably connected to die spool to be rotated diereby, and a take-off conduit for diverting compressed air from the compressor side and introducing die diverted compressed air into the cells for pressurizing the fuel. 16. The apparatus according to claim 1 wherein the mrbine has a power output no greater than one megawatt. 17. The apparatus according to claim 1 further comprising diagnostic means for sensing operating conditions in die energy conversion mechanism; transmitting means connected to die diagnostic means for transmitting signals to a central monitoring station; and means for local and/or remote station monitoring and operation. 18. The apparatus according to claim 1 further including a heat utilization device connected to the second passage for recovering heat from the waste gas exiting die heat exchanger. 19. An energy producing apparams comprising: an energy conversion mechanism comprising a compressor side for compressing air/fuel, and a mrbine side for driving the compressor side; an air and fuel supply for conducting air and fuel into a compressor of the compressor side to be compressed and mixed tiierein; an electrical generator operably connected to die mrbine side to be driven thereby for producing electrical energy; a regenerator heat exchanger having a first passage for conducting compressed air/fiiel ϋ:aveling from an outiet of the compressor side, a second passage for conducting hot waste gas from an outiet of the turbine side in heat exchange relationship with the compressed air/fuel in the first passage, and a movable core passing through sequentially through the first and second passages for being heated in the second passage and transferring heat to the compressed air/fuel passing through the first passage; 99/14071 23 a catalytic combustor disposed between an outlet of the first passage of the regenerator heat exchanger and an inlet of die turbine side for reacting compressed air/fiiel mixmre received from the first passage prior to entry thereof into the mrbine side; and preheating means for preheating the catalytic combustor independently of die regenerator during start-up. 20. The energy producing apparatus according to claim 19, further comprising diagnostic means for sensing operating conditions in the energy conversion mechanism; transmitting means connected to the diagnostic means for transmitting signals to a central monitoring station; and means for local and/or remote station monitoring and operation. 21. The apparatus according to claim 19 further including a heat utilization device connected to the second passage for recovering heat from the waste gas exiting the heat exchanger. 22. The apparatus according to claim 19 wherein the air and fuel supply is arranged to introduce the air and fuel separately into die compressor side. 23. An energy producing apparatus comprising: an energy conversion mechanism comprising a compressor side for compressing air/fuel, and a mrbine side for driving die compressor side; an electrical generator operably connected to the turbine side to be driven tiiereby for producing electrical energy; 99/14071 24 a heat exchanger having a first passage for conducting compressed air/fuel traveling from an outlet of the compressor side, and a second passage for conducting hot waste gas from an outlet of the mrbine side in heat exchange relationship with the compressed air/fuel in the first passage; a combustor disposed between an outlet of die first passage of the heat exchanger and an inlet of die mrbine side for reacting compressed air/fuel mixmre received from the first passage prior to entry thereof into the mrbine side; and a fuel supply mechanism for supplying pressurized fuel downstream of the compressor side, the fuel supply mechanism comprising a roto cell device having a driven rotor forming a plurality of cells spaced circumferentially around an outer periphery diereof for receiving fuel, and a take-off conduit for diverting compressed air from die compressor side and introducing die diverted compressed air into the cells for pressurizing the fuel. 24. The energy producing apparatus according to claim 23 further including a conduit for conducting the pressurized fuel into mixing relationship with compressed air from the compressor, at a location upstream of the combustor. 25. The energy producing apparatus according to claim 23 wherein die rotor is operably connected to a driven shaft of the energy conversion mechamsm to be driven tiiereby. 26. The energy producing apparatus according to claim 23 including a conduit for conducting the diverted compressed air from the rotor to the combustor. 99/14071 25 27. The apparatus according to claim 23 further including a heat utilization device connected to die second passage for recovering heat from the waste gas exiting the heat exchanger. 28. The apparatus according to claim 23 wherein the heat exchanger comprises a regenerator having a movable core sequentially passing through the first and second passages for absorbing heat in the second passage and giving up heat in the first passage. 29. A cogeneration apparatus comprising: an energy conversion mechanism including a mrbine arrangement for converting chemical fuel into energy; an electric generator operably connected to the energy conversion mechamsm for generating electricity; diagnostic means for sensing operating conditions in die energy conversion mechamsm; transmitting means connected to die diagnostic means for transmitting signals to a central monitoring station; and means for local and/or remote station monitoring and operation. 99/14071 26 30. Apparatus for producing a compressed air/fiiel mixture, comprising: a spool including a shaft, a compressor mounted on die shaft to be driven tiiereby, and an expansion mrbine operably connected to die shaft for driving the compressor; an air conduit connected to die compressor for conducting air into the compressor; and a fuel conduit connected to the compressor for conducting fuel into the compressor separate from die air. 31. A method of varying a heat-to-electric ratio of a cogeneration system comprising a shaft; an energy conversion mechamsm comprising a spool including a compressor and expansion turbine connected to the shaft; a heat exchanger having a first passage for conducting compressed gas traveling from an outlet of the compressor to an inlet of the turbine, a second passage for conducting hot waste gas received from the energy conversion mechamsm in heat exchange relationship with the compressed gas in die first passage, and a core movable sequentially through the first and second passages for being heated in the second passage and giving up that heat in the first passage; an electric generator operably connected to the energy conversion mechanism; and a heat-utilizing device connected to die heat exchanger for receiving waste gas therefrom; the method comprising die step of varying die speed of movement of d e core to adjust d e rate of heat transfer to the compressed gas in die first passage of the heat exchanger to alter the heat-to-electric ratio. 99/14071 27 32. A method of starting a multi-spool energy generating mechanism comprising a plurality of shafts; an expansion turbine mounted on each shaft, and a compressor mounted on at least one of the shafts, die compressors interconnected fluidly in series, and die turbines connected fluidly in series, the method comprising the steps of: A) causing die compressed air to expand in die upstream mrbine for rotating the shaft and compressor associated therewith; B) venting at least some of the exhaust gas discharged from the upstream mrbine, prior to die entry thereof into a mrbine disposed downstream of the upstream mrbine as the upstream mrbine accelerates; and thereafter C) conducting all of die exhaust gas from he upstream mrbine to die downstream mrbine after the energy generating mechanism reaches a predetermined operating state. 33. The method according to claim 32 wherein step C is performed when die upstream turbine reaches a predetermined speed. 34. The method according to claim 32 wherein step C is performed when die downstream compressor reaches a predetermined discharge pressure. 35. A method of starting a cogeneration system comprising an energy conversion mechanism including a spool formed by a shaft and a compressor and expansion turbine arrangement connected to the shaft; a heat exchanger having a first passage for conducting compressed air traveling from an outiet of the compressor to an inlet of the mrbine, and a second passage for conducting hot exhaust gas received 99/14071 28 from the energy conversion mechamsm; a catalytic reactor disposed downstream of the heat exchanger; and an electric generator operably connected to the energy conversion mechanism; the method comprising the step of preheating the catalytic reactor independently of the heat exchanger. 36. The method according to claim 35 wherein die catalytic reactor is disposed upstream of the mrbine arrangement. 37. The method according to claim 35 wherein die preheating step comprises actuating a fuel-burning combustor disposed between the heat exchanger and an inlet of the catalytic reactor. 38. The method according to claim 37 further including the step of throttling down an air inlet of the compressor to reduce pressure in the combustor and facilitate the introduction of fuel thereto. 39. The method according to claim 35 wherein the preheating step comprises actuating an electric heater which directly heats the catalytic reactor. 40. The method according to claim 35, wherein the heat exchanger is a regenerator including a movable core, tiie method including moving portions of the core sequentially tiirough the first and second passages, whereby die core absorbs heat in the second passage and gives up heat in die first passage. 99/14071 29 41. A method of operating a cogeneration system comprising an energy conversion mechamsm including a spool formed by a shaft and a compressor and expansion mrbine arrangement including a turbine connected to the shaft; a heat exchanger having a first passage for conducting compressed air/fuel traveling from an outlet of the compressor to an inlet of the mrbine, and a second passage for conducting hot waste gas received from the energy conversion mechanism; a catalytic combustor disposed between the first passage of the heat exchanger and an inlet of the mrbine arrangement; a fuel-burning combustor disposed between an outlet of the mrbine arrangement and die second passage of the heat exchanger; and an electric generator operably connected to the energy conversion mechanism; tiie method comprising the steps of: A) combusting fuel in the catalytic combustor to supply hot gas to the mrbine; and B) combusting fuel in the fuel-burning combustor in response to a failure of the catalytic combustor, to supply hot gas to the second passage of die heat exchanger which heats compressed air/fuel from the compressor.

Inventors: DIBBLE ROBERT W, LAGOD MARTIN L, MONGIA RAJIV K, TOUCHTON GEORGE L, DIBBLE, ROBERT, W., LAGOD, MARTIN, L., MONGIA, RAJIV, K., TOUCHTON, GEORGE, L.
Applicants: DIBBLE ROBERT W, LAGOD MARTIN L, MONGIA RAJIV K, SOLO ENERGY CORP, TOUCHTON GEORGE L, DIBBLE, ROBERT, W., LAGOD, MARTIN, L., MONGIA, RAJIV, K., SOLO ENERGY CORPORATION, TOUCHTON, GEORGE, L.
Application year: 1998
Main classification: B60L1
IPC codes: F01K21, F02C3, F02C6, F02C7, F23R3