Method of and apparatus for producing power in remote locations

Abstract

A system for producing power at remote locations comprises: a closed cycle vapor turbine unit having an evaporator containing liquid working fluid, a turbine receiving vapor of the evaporated working fluid for producing power by way of an electrical generator coupled to the turbine, a condenser and means for returning the working fluid condensate from the condenser to the evaporator; a biomass furnace associated with the evaporator for heating working fluid present in the evaporator and evaporating a portion of the working fluid; and a controller for controlling the amount of biomass fuel supplied to the biomass furnace in accordance with energy requirements of a customer load. Further, a method for producing power using the system is also provided.

Description

BACKGROUND OF THE INVENTION

[0001] 1. Field of the Invention

[0002] The present invention relates to a method of and apparatus for the operation of a closed cycle vapor turbine unit by biomass only, or combined with solar energy, and more particularly, a method of and apparatus for the operation of a closed cycle vapor turbine based on an organic Rankine cycle with biomass only or combined with solar energy.

[0003] 2. Description of the Prior Art

[0004] Many communities in remote locations are living on agriculture products. Such products in most cases are partially processed in the fields or near the farmer's home or in the village. There are large quantities of unused biomass wastes that remain to rot or decompose on site.

[0005] At the same time, many of such rural communities are not connected to the electric grid, but they need electrification to improve the quality of life.

[0006] The present invention overcomes the above deficiencies by the use of units for remote operation which may not have enough biomass supply for continuous operation and utilize solar energy during the day and biomass during the night or during periods of low solar radiation.

[0007] Many of the locations that require remote electrification are in the region of intense solar radiation and the addition of the option of utilization of solar energy as an alternatative contributes to successful installation.

BRIEF SUMMARY OF THE INVENTION

[0008] The present inventive subject matter is drawn to a system for producing power at remote locations comprising: a closed cycle vapor turbine unit having an evaporator containing liquid working fluid, a turbine receiving vapor of the evaporated working fluid for producing power by way of an electrical generator coupled to the turbine, a condenser and means for returning the working fluid condensate from the condenser to the evaporator; a biomass furnace associated with the evaporator for heating working fluid present in the evaporator and evaporating a portion of the working fluid; and a controller for controlling the amount of biomass fuel supplied to the biomass furnace in accordance with energy requirements of a customer load.

[0009] Preferably, the controller for controlling the amount of fuel supplied to the biomass furnace further controls the amount of biomass fuel supplied to the biomass furnace also in accordance with a control signal from a buffer load connected to the output of the generator. Also preferably, the controller for controlling the amount of biomass fuel supplied to the biomass furnace additionally controls the amount of biomass fuel supplied to the biomass furnace also in accordance with a monitored evaporator temperature. More preferably, the system includes a solar parabolic concentrating system for providing heat to the working fluid

[0010] The present inventive subject matter is further drawn to a method for producing power in remote locations comprising the steps of: providing a closed cycle vapor turbine unit having an evaporator containing liquid working fluid, a turbine receiving vapor of the evaporated working fluid for producing power by way of an electrical generator coupled to the turbine, a condenser and means for returning the working fluid condensate from the condenser to the evaporator; heating the working fluid present in the evaporator and evaporating portion of the working fluid using a biomass furnace associated with the evaporator; and controlling the amount of biomass fuel supplied to the biomass furnace in accordance with energy requirements of a customer load.

[0011] Preferably, the step of controlling the amount of biomass fuel supplied to the biomass furnace further includes the step of controlling the amount of biomass fuel supplied to the biomass furnace also in accordance with a control signal from a buffer load connected to the output of the generator. Also preferably, the step of controlling the amount of biomass fuel supplied to the biomass furnace additionally includes the step of controlling the amount of biomass fuel supplied to the biomass furnace also in accordance with a monitored evaporator temperature. More preferably, the method includes the step of providing heat to the working fluid using a solar parabolic concentration system.

[0012] Three options of operation with solar and two intallations of biomass are brought up here as magor installation examples although additional features can be added which are not the issues of the present proposal such as use of heat recovery by recuperators after the condenser etc.

[0013] A closed cycle vapor turbine (CCVT) unit is based on an organic Rankine cycle and comprises an evaporator, turbine, condenser and circulation pump.

[0014] Heat is supplied to the evaporator that is filled with organic fluid. The organic liquid temperature and pressure rises and part of the liquid is evaporated and flows out at the top of the evaporator. A turbine that is installed on the vapor path will utilize the energy of the expanding vapors, thus operating a generator for the generation of electric power.

[0015] A droplet separator is preferably installed at the vapors exit path to collect any liquid droplets that may enter the high pressure flow path, reach the turbine and damage the blades.

[0016] The expanding vapors, after expanding through the turbine, are condensed in a water or air-cooled condenser in which the pressure is lower according to the condensation temperature.

[0017] The condensed liquid is collected below the condenser and is pumped back to the evaporator to repeat the cycle. The liquid may be pumped by a mechanical driving force, turbine shaft-bearing centrifugal forces or gravity.

[0018] It is common practice to keep the cycle that uses organic fluid closed, for fear of losing material and air pollution because of the nature of such liquids.

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] Embodiments of the present inventive subject matter are described by way of example and with reference to the accompanying drawings wherein:

[0020] FIG. 1 is a schematic diagram of one embodiment of the apparatus of the present inventive subject matter.

[0021] FIG. 2 is a schematic diagram of another embodiment of the present inventive subject matter.

[0022] FIG. 3 is a schematic diagram of still another embodiment of the present inventive subject matter.

[0023] FIG. 4 is a schematic diagram of a yet further embodiment of the present inventive subject matter.

[0024] FIG. 5 is a schematic diagram of a yet still further embodiment of the present inventive subject matter.

[0025] FIG. 6 is a block diagram of another embodiment of the present inventive subject matter.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0026] Two types of systems are presented here, but in both cases the biomass furnace is directly heating the organic liquid. The difference between the two cases is that in one case, solar energy is introduced by way of a thermal fluid while in the other the organic fluid is also directly heated by the solar energy.

[0027] An additional option is shown in FIG. 2 in which the flue gas is optionally turned back to the biomass feeding silo to help dry the biomass, thus increasing the furnace combustion efficiency since biomass may contain high moisture levels that would reduce the heat value of the fuel if it was not dried before combustion.

[0028] An expansion tank is shown in both cases; however, in the case of usage of thermal fluid some means for fluid expansion and short or long term storage is a technical necessity due to the large difference in the fluid temperature between non-heated or heated modes, but in the case of direct heating of the organic liquid the evaporator itself can serve as the expansion tank, but the additional tank shown may serve as storage in cases when solar heat is available and there is no immediate need for electricity.

[0029] The following should be pointed out. A single controller can control all operation modes. Solar energy is continuously connected during the day or if the expansion or storage tank has a high enough level of stored energy. Biomass is used automatically to help the evaporator achieve evaporation temperature or supply energy to the buffer. In the case of buffer load control, the buffer load is connected to the power outlet of the turbine generator before the connection to the customer loads. When the buffer load is empty, due to customer's use, for example, the furnace receives a signal to increase the biomass flow and when the buffer load is full, the furnace receives a signal to decrease the biomass flow. In the case of temperature related control, the controller monitors the evaporator temperature and controls the fuel supply accordingly. The rate of fuel is controlled by the temperature difference between the boiler instantly monitored temperature and the desired temperature.

[0030] Air supply is controlled and optimized by an oxygen sniffer in the furnace exit, or preferably in the boiler exit, i.e., the chimney side. Small battery storage is necessary for start-up; large battery storage is optional.

[0031] In the case of solar operation, which is optional, a flash tray may be introduced into the evaporator to improve flashing of the solar heated liquid and the liquid level may be modified during such mode and/or use of different inlet tubes operated by the controller.

[0032] In case flue gas is used for drying of biomass fuel, the lid of the supply silo must be equipped with a safety relief valve to let of extra pressure created by the steam produced in the silo container—such drying will not only provide improved fuel to the combustion chamber, but also create higher pressure in the feeding compartment, thus reducing the chances for return fire from the furnace to the fuel silo.

[0033] In case the unit is vertical and high-condensed organic liquid returns to the evaporator by gravity, part goes directly and the other part goes through the turbine bearing to lubricate it. In the case of a low unit-horizontal design unit, the turbine shaft rotation in the bearing produces pressure that pushes the lubricating liquid (the organic fluid) through designed peripheral holes in the housing to a downstream tank that can be the evaporator.

[0034] Referring now to FIG. 6 describing the operation of the biomass-fueled power unit, The systems are capable of supplying the required power output from zero to the maximum rated power output. In order to do this, the system identifies the desired power output and controls the furnace to supply the required thermal energy to produce this power output, by doing so the system uses only the biomass quantities required and saves large amounts of biomass.

[0035] This is accomplished with the help of a buffer load, preferably using a Pulse Width Modulator (PWM) which is connected to the power outlet of the turbine generator before the connection to the customer loads. When the buffer is empty, due to customer's use, for example, the furnace receives a signal to increase the biomass flow, and when the buffer is full, the furnace receives a signal to decrease the biomass flow.

[0036] The furnace is able to operate at thermal loads of 20% of the maximum load with desired ratio between the biomass flow and the air supply for efficient combustion. Air supply is controlled and optimized by an oxygen sensor in the furnace exit or preferably in the boiler exit side, i.e., chimney side.

[0037] The controller establishes the desired furnace output and sends furnace output and sends a linear signal to the furnace and to the air blower. The air supply to the combustion influences the oxygen level in the exhaust gases, the feeder supplies the required biomass to enable combustion with the desired air/fuel ratio. The air/fuel ration set point changes according to the power demand from the boiler, to optimize the furnace performance.

[0038] The operation of the system starts with power supply to the furnace and to the control system from a battery, when the turbine is turning, the generator charges the battery and disconnects the battery from the system. From here on, the furnace receives the power it requires from the turbine generator. In case of planned use of battery storage, the rate of produced power that will be used for charging from the total production can be controlled by the controller.

[0039] The system recognizes customer's request according to the buffer load condition, when the buffer load is full, the system will connect the customers and decrease the request from the furnace. When the buffer load is empty, the furnace receives a signal to work at full load and the customers are connected automatically only when the buffer load is full.

[0040] The inventive subject matter being thus described, it will be obvious that the same may be varied in many ways. Such variations are not to be regarded as a departure from the spirit and scope of the inventive subject matter, and all such modifications are intended to be included within the scope of the following claims.

Claims

1. A system for producing power at remote locations comprising: (a) a closed cycle vapor turbine unit having an evaporator containing liquid working fluid, a turbine receiving vapor of the evaporated working fluid for producing power by way of an electrical generator coupled to said turbine, a condenser and means for returning the working fluid condensate from the condenser to the evaporator; (b) a biomass furnace associated with said evaporator for heating working fluid present in the evaporator and evaporating a portion of said working fluid; and (c) a controller for controlling the amount of biomass fuel supplied to said biomass furnace in accordance with energy requirements of a customer load.

2. A system for producing power according to claim 1 wherein said controller for controlling the amount of fuel supplied to said biomass furnace further controls the amount of biomass fuel supplied to said biomass furnace also in accordance with a control signal from a buffer load connected to the output of said generator.

3. A system for producing power according to claim 2 wherein said controller for controlling the amount of biomass fuel supplied to said biomass furnace additionally controls the amount of biomass fuel supplied to the biomass furnace also in accordance with a monitored evaporator temperature.

4. A system for producing power according to claim 2 wherein said buffer load comprises a pulse width modulator.

5. A system for producing power according to claim 1 including an oxygen sensor located at the exit of said evaporator for controlling the air/fuel ratio in the biomass furnace.

6. A system for producing power according to claim 1 wherein said working fluid is an organic fluid.

7. A system for producing power according to claim 1 wherein said means for returning the working fluid from the condenser to the evaporator comprises a pump.

8. A system for producing power according to claim 1 further comprising a line for supplying flue gases exiting said evaporator to biomass fuel for drying said biomass fuel.

9. A system for producing power according to claim 1 further comprising a solar parabolic concentrating system for providing heat to the working fluid.

10. A method for producing power in remote locations comprising the steps of: (a) providing a closed cycle vapor turbine unit having an evaporator containing liquid working fluid, a turbine receiving vapor of the evaporated working fluid for producing power by way of an electrical generator coupled to said turbine, a condenser and means for returning the working fluid condensate from the condenser to the evaporator; (b) heating said working fluid present in the evaporator and evaporating portion of said working fluid using a biomass furnace associated with said evaporator; and (c) controlling the amount of biomass fuel supplied to said biomass furnace in accordance with energy requirements of a customer load.

11. A method according to claim 10 wherein the step of controlling the amount of biomass fuel supplied to said biomass furnace further includes the step of controlling the amount of biomass fuel supplied to said biomass furnace also in accordance with a control signal from a buffer load connected to the output of said generator.

12. A method according to claim 11 wherein the step of controlling the amount of biomass fuel supplied to said biomass furnace additionally includes the step of controlling the amount of biomass fuel supplied to said biomass furnace also in accordance with a monitored evaporator temperature.

13. A method according to claim 11 wherein the step of controlling the amount of biomass fuel supplied to said biomass furnace also in accordance with a control signal from a buffer load connected to the output of said generator is carried out using a pulse width modulator.

14. A method according to claim 10 including the step of controlling the air/fuel ration in the biomass furnace using an oxygen sensor located at the exit of said evaporator.

15. A method according to claim 10 including the step of using an organic fluid for the working fluid.

16. A method according to claim 10 wherein flue gases exiting said evaporator are used to dry the biomass fuel.

17. A method according to claim 10 further including the step of providing heat to the working fluid using a solar parabolic concentration system.