Two-phase thermal energy conversion system

Claim 2

A two-phase energy conversion system comprising: (a) a source of a first fluid which is evaporable within a predetermined range of temperatures and pressures; (b) a source of a second fluid consisting of a gas which is not liquefiable within said range; (c) means for heating at least one of said fluids; (d) means for mixing said fluids; (e) means for supplying the fluids under pressure to the mixing means; (f) a prime mover coupled to be driven by said mixture; (g) sensing means for monitoring at least one operating condition of the prime mover; and (h) control means responsive to the sensing means for controlling the ratio of flow rates of the first and second fluids to the mixing means so as to substantially saturate the second fluid with the first fluid over a pressure range up to twice the absolute pressure of the prime mover exhaust at equilibrium temperature.

Claim 3

An energy conversion system as defined in claim 1 wherein said first fluid consists of water and said second fluid consists of air.

Claim 4

An energy conversion system as defined in claim 2 wherein said prime mover comprises a turbine.

Claim 5

An energy conversion system as defined in claim 2 wherein said prime mover comprises a reciprocating piston engine.

Claim 6

An energy conversion system as defined in claim 2 wherein said water is heated to a temperature not greater than its boiling point.

Claim 7

An energy conversion system as defined in claim 1 wherein the prime mover comprises one having substantially constant volume.

Claim 8

An energy conversion system as defined in claim 3 wherein the turbine has substantially constant axial cross-sectional area from inlet to outlet.

Claim 9

An energy conversion system as defined in claim 2 wherein the water consists of salt water, whereby the exhaust of said prime mover is fresh water.

Claim 10

The system of claim 1 wherein the sensing means are coupled to monitor the load demand on the prime mover and the temperature of discharge water from the mixing means, respectively, and wherein the control means are operative to control the rate of flow of at least one of said fluids to the mixing means in accordance with signals from the sensing means.

Claim 11

The system of claim 9 further comprising first and second valves of respectively controlling the rate of flow of the first and second fluids to the mixing means such that the rate of flow of the second fluid is proportional to prime mover load demand while the rate of flow of the first fluid is varied inversely with the temperature of discharge water from the mixing means.

Claim 12

The system of claim 1 wherein the mixing means is incorporated with the prime mover.

Claim 13

The system of claim 11 wherein the sensing means is connected to monitor the rate of flow of the first fluid to the prime mover for mixing therein, and wherein the control means controls the rate of flow of the second fluid to the prime mover in accordance with signals from the sensing means.

Claim 14

The system of claim 11 wherein the sensing means is connected to monitor the rate of flow of the second fluid to the prime mover for mixing therein, and wherein the control means varies the rate of flow of the first fluid to the prime mover in accordance with signals from the sensing means.

Claim 15

A two-phase thermal energy conversion system comprising: (a) a source of hot water; (b) a first pump connected to said source for pumping the hot water; (c) a first controllable valve connected to said pump for controlling the rate of flow of water; (d) an evaporator connected to said controllable valve to receive hot water therefrom; (e) a second pump for pumping ambient air; (f) a second controllable valve connected to said second pump for supplying a predetermined rate of air flow to said evaporator, said evaporator having means for mixing the air and water pumping thereto, thereby to evaporate the water and to provide moist air at an increased pressure; (g) a prime mover connected to said evaporator for receiving the mixture of hot moist air and vapor, thereby to extract energy from the mixture; (h) first means for sensing the temperature of water discharged from the evaporator; (i) second means for sensing the load on the prime mover; and (j) means responsive to said sensing means for controlling said first and second controllable valves to control the rates of water and air supplied for mixing in the evaporator to develop an equilibrium mixture for application to said prime mover.

Claim 16

A two-phase thermal energy conversion system comprising: (a) a source of hot water; (b) a first pump connected to said source for pumping the hot water; (c) a first controllable valve connected to said pump for controlling the rate of flow of water; (d) an evaporator connected to said controllable valve to receive hot water therefrom; (e) a second pump for pumping ambient air; (f) a second controllable valve connected to said second pump for supplying a predetermined rate of air flow to said evaporator, said evaporator having means for mixing the air and water pumping thereto, thereby to evaporate the water and to provide moist air at an increased pressure; (g) a prime mover connected to said evaporator for receiving the mixture of hot moist air and vapor, thereby to extract energy from the mixture; (h) first means for sensing the temperature of water discharged from the evaporator; (i) second means for sensing the load on the prime mover; and (j) means responsive to said sensing means for controlling said first and second controllable valves to control the rates of water and air supplied for mixing in the evaporator to develop an equilibrium mixture for application to said prime mover.

Claim 17

A system as defined in claim 14 wherein an electric generator is coupled to said prime mover.

Claim 18

A system as defined in claim 14 wherein said first and second pumps are coupled to be driven by said prime mover.

Claim 19

A system as defined in claim 14 wherein an additional sensor is provided to sense the level of water in said evaporator for controlling the outflow of water from said evaporator.

Claim 20

A system as defined in claim 14 wherein the rate of flow of air is controlled proportionally to the load on the prime mover and wherein the rate of flow of hot water is controlled inversely to the temperature of the evaporator discharge water.

Claim 21

The system of claim 14 wherein the controlling means are operated to develop substantial saturation of the mixture of air and vapor.

Claim 22

A two-phase energy conversion system comprising: (a) a source of a first fluid which is evaporable within a predetermined range of temperatures and pressures; (b) a source of a second fluid consisting of a gas which is not liquefiable within said range; (c) means for heating at least one of said fluids; (d) means for pressurizing the fluids; (e) means for mixing the vapor of said first fluid with said second fluid; (f) a prime mover of substantially constant volume coupled to be driven by the resulting mixture; and (g) means for selectively adjusting the ratio of first fluid vapor mixed with the second fluid in accordance with selected operating conditions of the prime mover to maintain the second fluid substantially saturated with vapor of the first fluid.

Claim 23

A two-phase energy conversion system comprising: (a) a source of a first fluid which is evaporable within a predetermined range of temperatures and pressures; (b) a source of a second fluid consisting of a gas which is not liquefiable within said range; (c) means for heating at least one of said fluids; (d) means for pressurizing the fluids; (e) means for mixing the vapor of said first fluid with said second fluid; (f) a prime mover of substantially constant volume coupled to be driven by the resulting mixture; and (g) means for selectively adjusting the ratio of first fluid vapor mixed with the second fluid in accordance with selected operating conditions of the prime mover to maintain the second fluid substantially saturated with vapor of the first fluid.

Claim 24

A two-phase energy conversion system comprising: (a) a source of a first fluid which is evaporable within a predetermined range of temperatures and pressures; (b) a source of a second fluid consisting of a gas which is not liquefiable within said range; (c) means for heating at least one of said fluids; (d) means for pressurizing the fluids; (e) means for mixing vapor of said first fluid with said second fluid; (f) a prime mover coupled to be driven by the resulting mixture, the prime mover being of substantially constant volume so as to preclude significant expansion of the fluid mixture therein; and (g) means for recycling the exhaust components from the prime mover to supplement the first and second fluids introduced to the mixing means.

Claim 25

A two-phase energy conversion system comprising: (a) a source of a first fluid which is evaporable within a predetermined range of temperatures and pressures; (b) a source of a second fluid consisting of a gas which is not liquefiable within said range; (c) means for heating at least one of said fluids; (d) means for pressurizing the fluids; (e) means for mixing vapor of said first fluid with said second fluid; (f) a prime mover coupled to be driven by the resulting mixture, the prime mover being of substantially constant volume so as to preclude significant expansion of the fluid mixture therein; and (g) means for recycling the exhaust components from the prime mover to supplement the first and second fluids introduced to the mixing means.

Claim 26

A process for converting thermal energy to mechanical power in a prime mover comprising the steps of: (a) a mixing vapor of a first fluid consisting of a liquid which is evaporable over a predetermined range of temperatures and pressures with a second fluid consisting of a gas which is not liquefiable over said range; (b) controlling the ratio of the first and second fluids to establish a substantially saturated mixture within a pressure range up to twice the exhaust pressure of the prime mover; (c) pressurizing the fluid mixture and supplying it to the prime mover; (d) maintaining the volume of the mixture substantially constant through the prime mover; (e) condensing the first fluid within the prime mover; and (f) converting the heat of condensation of the first fluid to mechanical power within the prime mover.

Claim 27

A process for converting thermal energy to mechanical power in a prime mover comprising the steps of: (a) a mixing vapor of a first fluid consisting of a liquid which is evaporable over a predetermined range of temperatures and pressures with a second fluid consisting of a gas which is not liquefiable over said range; (b) controlling the ratio of the first and second fluids to establish a substantially saturated mixture within a pressure range up to twice the exhaust pressure of the prime mover; (c) pressurizing the fluid mixture and supplying it to the prime mover; (d) maintaining the volume of the mixture substantially constant through the prime mover; (e) condensing the first fluid within the prime mover; and (f) converting the heat of condensation of the first fluid to mechanical power within the prime mover.

Claim 28

The process of claim 22 wherein the prime mover is a turbine.

Claim 29

The process of claim 22 wherein the first fluid is water and the second fluid is air.

Claim 30

The process of claim 24 further comprising the step of directing the condensed water and exhaust gas from the prime mover to be repressurized and mixed for recycling into the prime mover.

Claim 31

The process of claim 22 further comprising the step of heating the first fluid prior to mixing with the second fluid.

Claim 32

The process of claim 22 further comprising the step of heating the second fluid prior to mixing with the first fluid.

Claim 33

The process of claim 26 wherein the first fluid is water and the heating step comprises heating the water to a point not exceeding its boiling point at ambient pressure.

Claim 34

A process for converting thermal energy to mechanical power within a prime mover comprising the steps of: (a) mixing vapor of a first fluid comprising a liquid which is evaporable over a predetermined range of temperatures and pressures with a second fluid comprising a gas which is not liquefiable over said range, the first fluid being heated to provide the preponderance of the heat of vaporization thereof; (b) pressurizing the fluids; (c) collecting and removing excess liquid from the mixing step; (d) supplying the resulting mixture to a prime mover; (e) sensing at least one of the operating conditions of the prime mover; and (f) controlling the rate of flow of at least one of the fluids in accordance with signals from the sensing of the prime mover to establish a saturated mixture within the prime mover.

Claim 35

A process for converting thermal energy to mechanical power within a prime mover comprising the steps of: (a) mixing vapor of a first fluid comprising a liquid which is evaporable over a predetermined range of temperatures and pressures with a second fluid comprising a gas which is not liquefiable over said range, the first fluid being heated to provide the preponderance of the heat of vaporization thereof; (b) pressurizing the fluids; (c) collecting and removing excess liquid from the mixing step; (d) supplying the resulting mixture to a prime mover; (e) sensing at least one of the operating conditions of the prime mover; and (f) controlling the rate of flow of at least one of the fluids in accordance with signals from the sensing of the prime mover to establish a saturated mixture within the prime mover.

Claim 36

The process of claim 29 wherein the sensing step comprises sensing the load demand on the prime mover and the temperature of the excess liquid from the mixing step; and wherein the controlling step comprises controlling the rate of flow of the first fluid to vary inversely with the temperature of the excess liquid from the mixing step and controlling the rate of flow of the second fluid to be proportional to prime mover load demand.

Claim 37

The process of claim 29 wherein the mixing step is performed within the prime mover.

Claim 38

The process of claim 31 wherein the sensing step comprises sensing the rate of flow of the first fluid; and the controlling step comprises controlling the rate of flow of the second fluid to the prime mover.

Claim 39

The process of claim 31 wherein the sensing step comprises sensing the rate of flow of the second fluid; and the controlling step comprises controlling the rate of flow of the first fluid to the prime mover.