BINARY CYCLE POWER SYSTEM

Abstract

The application relates to a binary cycle power system for generating electrical power. The system comprises a heat exchanger for evaporating a first fluid, a turbine converter, an electrical generator, and a first condenser for condensing the evaporated first fluid. The turbine converter converts energy of the evaporated first fluid to mechanical energy and the electrical generator generates the electrical power from the mechanical energy. The heat exchanger is a second condenser, which is a part of a heat pump that transfers heat from a second fluid circulating in the heat pump to the first fluid so that the first fluid evaporates.

Claims

1. A binary cycle power system for generating electrical power comprising a heat exchanger for evaporating a first fluid, a turbine converter, an electrical generator, and a first condenser for condensing the evaporated first fluid, wherein the turbine converter converts energy of the evaporated first fluid to mechanical energy and the electrical generator generates the electrical power from the mechanical energy, characterized in that the heat exchanger is a second condenser, which is a part of a heat pump that transfers heat from a second fluid circulating in the heat pump into the first fluid so that the first fluid evaporates.

2. The system according to claim 1, wherein the heat pump is an air-source heat pump that extracts the heat from surrounding air to the second fluid.

3. The system according to claim 1, wherein the heat pump comprises an evaporator, where heat energy transfers into the second fluid and causes an evaporation of the second fluid.

4. The system according to claim 1, wherein a part of a channel system of the heat pump is positioned into water of a river or lake system, or into seawater, and the heat pump extracts the heat from the water to the second fluid, which circulates in the channel system of the heat pump, whereupon heat energy transfers into the second fluid and causes an evaporation of the second fluid.

5. The system according to claim 4, wherein the heat pump comprises a compressor that compresses the evaporated second fluid so that its pressure and temperature increases.

6. The system according to claim 1, wherein the heat pump comprises an expander that expands the second fluid, which has condensed and cooled when transferring the heat to the first fluid inside the second condenser, so that its pressure and temperature decreases.

7. The system according to claim 1, which comprises a liquid pump for circulating the first fluid towards the second condenser.

8. A generating method for generating electrical power in the binary cycle power system according to claim 1, comprising at least steps of transferring, by the second condenser, the heat from the second fluid to the first fluid so that the first fluid evaporates, converting, by the turbine converter, energy of the evaporated first fluid to the mechanical energy, condensing, by the first condenser, the evaporated first fluid, and generating, by the electrical generator, the electrical power from the mechanical energy.

Description

DESCRIPTION OF THE FIGURE

[0011] The FIGURE presents a binary cycle power system 100 for generating electrical power clean and sufficiently effective way.

[0012] The system 100 comprises at least two cycles 102, 104, wherein one fluid 106. 108 circulates in each cycle 102, 104 in order to provide heat transfer between fluids 106, 108 and, of course, between the cycles 102, 104. The fluids 106, 108 are arranged so that a first fluid 106 circulates in the first cycle 102 and a second fluid 108 circulates in the second cycle 108.

[0013] Both first and second cycles 102, 104 comprise a channel system, which are not marked with separate reference numbers in the FIGURE, and the first and second fluids 106, 108 circulate along these channel systems in the first and second cycles 102, 104.

[0014] The second cycle 104 comprises a heat pump 110, wherein the second fluid 108 circulates in order to receive heat (energy) 111 from outside the heat pump 110 and to transfer it to the first fluid 106 in the first cycle 102.

[0015] The second fluid 108 is chosen so that its boiling point, when it is in a liquid form, is optimal to a condensing process where a heat energy of a gas is condensed into a smaller volume. The second fluid 108 comprises e.g. propylene glycol or ethyl alcohol.

[0016] The heat pump 110 comprises an evaporator 112, wherein the heat energy 111 received from outside the heat pump 110, and the system 100, transfers into the second fluid 108 and the heat 111 causes an evaporation of second fluid 108, which flows through the evaporator 112.

[0017] The heat pump 110 may be an air-source heat pump that extracts the heat 111 from surrounding air to the second fluid 108 in accordance with the FIGURE.

[0018] Alternatively, the heat pump 110 may be manufactured without connecting the channel system of second cycle 104 to the evaporator 112. The second cycle 104 is also in this embodiment a closed loop, where the second fluid 108 circulates. A part of the channel system of second cycle 104, e.g. the channel part that is presented inside the structure of evaporator 112 in the FIGURE, is positioned (immergered) into water of a river or lake system, or into seawater. The heat pump 110 extracts the heat 111 from the water (seawater) to the second fluid 108, whereupon the heat energy 111 received outside the heat pump 110 (the system 100), i.e. from the water, transfers into the second fluid 108, when it flows through the immergered part of channel system of second cycle 104. This causes the evaporation of second fluid 108 correspondingly as in the evaporator 112. Otherwise, the operation of this alternative embodiment complies with the embodiment of the FIGURE.

[0019] Irrespective of how the heat pump 110 receives the heat 111, the system 100 enables clean energy and limitless energy resources for the production of electrical energy.

[0020] The heat pump 110 further comprises a compressor 114. The evaporated second fluid 108 flows along the channel system from the evaporator 112 or from the immergered part of channel system to the compressor 114, which compresses the evaporated second fluid 108 so that its pressure and temperature increases.

[0021] The heat pump 110 further comprises a second condenser (heat exchanger) 116. The pressurized and hot second fluid 108 flows along the channel system from the compressor 114 to the condenser 116 and, when the second fluid 108 flows along the second condenser 116, the heat, which is in the second fluid 108, transfers into the first fluid 106, which circulates in the first cycle 102, so that the first fluid 106 evaporates.

[0022] The second fluid 108 condenses and cools down when transferring the heat to the first fluid 106.

[0023] The heat pump 110 further comprises an expander 118. After the second fluid 108 has released its heat in the condenser 116, it flows along the channel system to the expander 118 that expands the second fluid 108 so that its pressure and temperature decreases.

[0024] Then, after the expander 118, the expanded second fluid 108 completes its cycle by returning back along the channel system to the evaporator 112 or to the immergered part of channel system, where it is ready to receive again the heat 111 from outside.

[0025] Similarly as the second cycle 104, the first cycle 102 also comprises the condenser 116 that operates as a heat exchanger in the first cycle 102. So, the heat exchanger (second condenser) 116 is shared by the heat pump 110 and the first cycle 102.

[0026] The heat exchanger 116 transfer the heat from the second fluid 108 into the first fluid 106 so that the first fluid evaporates as above has been explained.

[0027] The first fluid 106 is chosen so that its boiling point, when it is in a liquid form, is slightly higher than an ambient temperature. The first fluid 106 comprises e.g. pentane or isobutane.

[0028] An absolute pressure inside the closed loop systems 100, 110 may be controlled so that the boiling points are optimized for the available temperature, i.e. the heat 111.

[0029] The first cycle 102 further comprises a turbine converter 120. The evaporated first fluid 106 flows along a channel system of first cycle 102 from the heat exchanger 116 (from the heat pump 110) into the turbine converter 120, which converts energy of the evaporated first fluid 106 to a form of mechanical energy, i.e. rotation movement R.

[0030] The first cycle 102 further comprises an electrical generator 122. The rotation movement R, i.e. the produced mechanical energy, is used to generate electrical power in the electrical generator 122.

[0031] The first cycle 102 further comprises a (first) condenser 124. The first fluid 106, which caused the turbine converter 120 to rotate R, flows along the channel system from the turbine converter 120 towards the condenser 124, where the evaporated first fluid 106 is condensed.

[0032] The first cycle 102 further comprises a liquid pump 126. The condensed first fluid 106 flow from the condenser 124 along the channel system to the liquid pump 126, which circulates the first fluid 106 in the first cycle 102 and, thus, directs the first fluid 106 towards the heat exchanger 116.

[0033] Finally, after the liquid pump 126, the first fluid 106 completes its cycle by returning back along the channel system to the heat exchanger 116, where it is ready to receive again the heat from the second fluid 108 (from the heat pump 110).

[0034] The invention is not only restricted to these above-explained embodiments but it comprises all possible embodiments within the scope of following claims.