Method of generating power from a vapor

Claim 3

A process for generating power comprising the steps of: generating a superheated vapor from a working fluid; supplying the superheated vapor to a high pressure zone to maintain the high pressure zone at a substantially constant high pressure; imparting work to a working shaft rotatably coupled to a high pressure piston by constantly exposing the lower face of the high pressure piston to the vapor in the high pressure zone while selectively exposing the upper face of the high pressure piston to the vapor in the high pressure zone as the high pressure piston approaches upper dead center in relation to the working shaft, said upper face of the high pressure piston forming a first variable volume with the high pressure cylinder wall; and concurrently therewith intermittently discharging vapor from the first variable volume to a larger second variable volume formed of the lower face of a low pressure piston linked directly to the high pressure piston and a low pressure cylinder wall while constantly exposing the upper face of the low pressure piston to low pressure vapor in a low pressure zone and intermittently exposing the second variable volume to the low pressure zone, said second variable volume being allowed to increase more rapidly than the first variable volume decreases as the high and low pressure pistons move from bottom dead center to top dead center in relation to the working shaft.

Claim 4

A process for generating power comprising the steps of: generating a superheated vapor from a working fluid; supplying the superheated vapor to a high pressure zone to maintain the high pressure zone at a substantially constant high pressure; imparting work to a working shaft rotatably coupled to a high pressure piston by constantly exposing the lower face of the high pressure piston to the vapor in the high pressure zone while selectively exposing the upper face of the high pressure piston to the vapor in the high pressure zone as the high pressure piston approaches upper dead center in relation to the working shaft, said upper face of the high pressure piston forming a first variable volume with the high pressure cylinder wall; and concurrently therewith intermittently discharging vapor from the first variable volume to a larger second variable volume formed of the lower face of a low pressure piston linked directly to the high pressure piston and a low pressure cylinder wall while constantly exposing the upper face of the low pressure piston to low pressure vapor in a low pressure zone and intermittently exposing the second variable volume to the low pressure zone, said second variable volume being allowed to increase more rapidly than the first variable volume decreases as the high and low pressure pistons move from bottom dead center to top dead center in relation to the working shaft.

Claim 5

A process according to claim 2 wherein high pressure vapor in the first variable volume generally undergoes an adiabatic isentropic expansion as the vapor is intermittently discharged from the first variable volume to the second variable volume.

Claim 6

A process according to claim 2 wherein vapor in the high pressure zone impacting the lower face of the high pressure piston performs a generally isobaric work process as the vapor is intermittently discharged from the first variable volume to the second variable volume.

Claim 7

A process according to claim 2 wherein the working shaft is operably connected to the high pressure piston by a crank mechanism rotating through 360 degrees and wherein the work imparted is imparted as the crank mechanism rotates from approximately 181 degrees to 360 degrees.

Claim 8

A process according to claim 5 wherein the high pressure piston attains a minimum pressure differential within at least a few degrees of the end of the power stroke.

Claim 9

A process according to claim 6 wherein the high pressure piston attains high mean effective pressure as the crank mechanism recedes within no more than a few degrees from the optimum angle for exerting force on the crank mechanism.

Claim 10

A process according to claim 7 wherein the high pressure piston attains highest net torque as the crank mechanism approaches an angle of approximately 300 degrees based on a rotation of 181 degrees through 360 degrees.

Claim 11

A process according to claim 5 wherein the low pressure piston attains a maximum pressure differential at the beginning of the power stroke.

Claim 12

A process according to claim 9 wherein the low pressure piston attains high mean effective pressure as the crank mechanism approaches within a few degrees of the optimum angle for exerting force on the crank mechanism.

Claim 13

A process according to claim 10 wherein the low pressure piston attains its highest net torque as the crank mechanism approaches an angle of approximately 240 degrees based on a rotation of 181 degrees to 360 degrees.

Claim 14

A process according to claim 11 wherein the high pressure piston and the low pressure piston attain their highest net combined torque as the crank mechanism approaches an angle of approximately 260 degrees based on a rotation of 181 degrees to 360 degrees.

Claim 15

A process according to claim 2 wherein the lower face of the high pressure piston is substantially constantly exposed to a maximum high pressure and the upper face of the low pressure piston is substantially constantly exposed to a minimum low pressure whereby the maximum pressure differential may be maintained across the high pressure and low pressure pistons as they impart work to the working shaft.

Claim 16

A process according to claim 2 wherein the low pressure cylinder diameter is at least twice the diameter of the high pressure cylinder diameter.

Claim 17

A process according to claim 14 wherein the low pressure cylinder diameter is at least three times the diameter of the high pressure cylinder diameter.

Claim 18

A process according to claim 2 wherein the vapor in the low pressure zone is condensed.

Claim 19

A process according to claim 16 wherein the step of generating a superheated vapor comprises heating the condensed vapor from the low pressure zone using a low grade heat source sufficiently to cause the condensed vapor to undergo a phase change to saturated vapor and thereafter by additionally heating under constant pressure the saturated vapor while exposing it to another heat source to form the superheated vapor.

Claim 20

A process according to claim 2 further comprising the step of thermally insulating the high and low pressure zones.

Claim 21

A process according to claim 2 wherein the temperature of the superheated vapor is less than about 400 degrees F.

Claim 22

A process according to claim 2 wherein the working fluid is at a maximum pressure of no more than about 700 psig.

Claim 23

A process according to claim 20 wherein the working fluid is at a maximum pressure in the range of about 300 to 400 psig.

Claim 24

A process according to claim 2 wherein the working shaft is rotatable and rotates at a speed of less than about 450 revolutions per minute.

Claim 25

A process according to claim 22 wherein the working shaft rotates at a speed of less than about 120 revolutions per minute.

Claim 26

A process according to claim 2 wherein the working fluid comprises a refrigerant capable of undergoing a phase change within the desired thermal operating range.

Claim 27

A process according to claim 24 wherein the working fluid is Freon.

Claim 28

A process according to claim 24 wherein the working fluid is water.

Claim 29

A process according to claim 2 wherein the working shaft is operably connected to the high pressure piston by a crank mechanism rotating through 360 degrees and wherein the high and low pressure pistons attain a combined high mean effective pressure as the crank mechanism approaches within at least a few degrees of the optimum angle for exerting force on the crank mechanism.

Claim 30

A process according to claim 2 wherein the working shaft is operably connected to the high pressure piston by a crank mechanism rotating through 360 degrees and wherein the high pressure piston attains high mean effective pressure as the crank mechanism recedes no more than a few degrees from the optimum angle for exerting force on the crank mechanism.

Claim 31

A process according to claim 2 wherein the temperature of the vapor drops such that the expansion of vapor is completed in the low pressure zone before the second variable volume has expanded to a maximum by movement of the low pressure piston and further comprising the step of selectively exposing the second variable volume to the low pressure zone to prevent a vacuum from being drawn in the second variable volume.

Claim 32

A process according to claim 2 wherein the temperature of vapor increases such that the expansion of vapor is limited in the low pressure zone and further comprising the step of selectively exposing the first and second variable volumes to the high and low pressure zones, respectively, to permit the required expansion of the vapor discharge from the first to the second variable volumes.

Claim 33

A process according to claim 2 wherein the mass flow of vapor is reduced during operation by extending of the time that the first variable volume is in fluid communication with the high pressure zone and extending of the time the second variable volume is in fluid communication with the low pressure zone prior to the transfer of mass from the first variable volume to the second variable volume.

Claim 34

A process according to claim 2 wherein the efficiency of the process is at least about 90 percent as compared to a Carnot cycle.

Claim 35

A process for generating power comprising the steps of: generating a superheated vapor from a working fluid; supplying a superheated vapor to a high pressure zone to maintain the high pressure zone at a substantially constant high pressure; first imparting work to a working shaft coupled to an enclosed high pressure piston by placing a first variable volume comprising the lower face of the high pressure piston and the high pressure cylinder walls in fluid communication with the high pressure zone while allowing discharge of working fluid from a second variable volume formed from the upper face of the high pressure piston and the high pressure cylinder walls to a third variable volume formed by the lower face of an enclosed low pressure piston linked to the high pressure piston and low pressure cylinder walls while concurrently therewith placing a fourth variable volume comprising the upper face of the low pressure piston and the low pressure cylinder walls to a low pressure zone, the low pressure zone being maintained at a substantially constant low pressure; and thereafter imparting further work to the working shaft by placing the second variable volume in fluid communication with the high pressure zone while allowing discharge of working fluid from the first variable volume to the fourth variable volume while concurrently placing the third variable volume in fluid communication with the low pressure zone.

Claim 36

A process for generating power comprising the steps of: generating a superheated vapor from a working fluid; supplying a superheated vapor to a high pressure zone to maintain the high pressure zone at a substantially constant high pressure; first imparting work to a working shaft coupled to an enclosed high pressure piston by placing a first variable volume comprising the lower face of the high pressure piston and the high pressure cylinder walls in fluid communication with the high pressure zone while allowing discharge of working fluid from a second variable volume formed from the upper face of the high pressure piston and the high pressure cylinder walls to a third variable volume formed by the lower face of an enclosed low pressure piston linked to the high pressure piston and low pressure cylinder walls while concurrently therewith placing a fourth variable volume comprising the upper face of the low pressure piston and the low pressure cylinder walls to a low pressure zone, the low pressure zone being maintained at a substantially constant low pressure; and thereafter imparting further work to the working shaft by placing the second variable volume in fluid communication with the high pressure zone while allowing discharge of working fluid from the first variable volume to the fourth variable volume while concurrently placing the third variable volume in fluid communication with the low pressure zone.

Claim 37

A process according to claim 33 wherein high pressure vapor in the second variable volume generally undergoes an adiabatic isentropic expansion as the vapor is intermittently discharged from the second variable volume to the third variable volume, and thereafter undergoes a similar process between the first and fourth variable volumes.

Claim 38

A process according to claim 33 wherein vapor in the high pressure zone impacting the lower face of the high pressure piston performs a generally isobaric work process as the vapor is intermittently discharged from the second variable volume to the third variable volume, and thereafter undergoes a similar process wherein vapor in the high pressure zone impacting the upper face of the high pressure piston performs a generally isobaric work process as the vapor is intermittently discharged from the first variable volume to the fourth variable volume.

Claim 39

A process according to claim 33 wherein the pressure differential that occurs across the high and low pressure pistons results from a single mass that flows between the second and third variable volumes and alternately between the first and fourth variable volumes.

Claim 40

A process according to claim 33 wherein the working shaft is operably connected to the high pressure piston by a crank mechanism rotating through 360 degrees and wherein the work first imparted is imparted as the crank mechanism rotates from approximately 0 to 180 degrees in a first power stroke and wherein the work thereafter imparted is imparted as the crank mechanism rotates from approximately 181 to 360 degrees in a second power stroke.

Claim 41

A process according to claim 37 wherein a maximum pressure differential exists across the high pressure piston as it approaches within at least a few degrees of the end of each of the first and second power strokes.

Claim 42

A process according to claim 38 wherein the high pressure piston attains high mean effective pressure as the crank mechanism is receding within no more than a few degrees from the optimum angle for exerting force on the crank mechanism as it passes through each of the first and second power strokes.

Claim 43

A process according to claim 39 wherein the high pressure piston attains its highest net torque as the crank mechanism approaches an angle of approximately 120 degrees during the first power stroke and 300 degrees during the second power stroke.

Claim 44

A process according to claim 37 wherein the low pressure piston attains a maximum pressure differential across the low pressure piston as the low pressure piston is within at least a few degrees of the beginning of each power stroke.

Claim 45

A process according to claim 41 wherein the low pressure piston attains high mean effective pressure as the crank mechanism approaches at least within a few degrees of the optimum angle for exerting force on the crank mechanism.

Claim 46

A process according to claim 42 wherein the low pressure piston attains the highest net torque as the crank mechanism approaches an angle of approximately 60 degrees during the first power stroke and approximately 240 degrees during the second power stroke.

Claim 47

A process according to claim 37 wherein the high and low pressure pistons attain a combined high mean effective pressure as the crank mechanism approaches within at least a few degrees of the optimum angle for exerting force on the crank mechanism.

Claim 48

A process according to claim 44 wherein the high pressure piston and the low pressure piston attain the highest net combined torque as the crank mechanism approaches an angle of approximately 80 degrees during the first power stroke and approximately 260 degrees during the second power stroke.

Claim 49

A process according to claim 33 wherein the vapor in the low pressure zone is condensed.

Claim 50

A process according to claim 33 wherein the lower face of the high pressure piston is substantially constantly exposed to a maximum high pressure in the high pressure zone and the upper face of the low pressure piston is substantially constantly exposed to a minimum low pressure in the low pressure zone whereby the maximum pressure differential may be maintained across the high and low pressure pistons as they impart work to the working shaft.

Claim 51

A process according to claim 33 wherein the low pressure cylinder diameter is at least twice the diameter of the high pressure cylinder diameter.

Claim 52

A process according to claim 48 wherein the low pressure cylinder diameter is at least five time the diameter of the high pressure cylinder diameter.

Claim 53

A process according to claim 33 wherein the step of generating a superheated vapor comprises heating the condensed vapor from the low pressure zone using a low grade heat source sufficiently to cause the condensed vapor to undergo a phase change to saturated vapor during an isobaric heat addition process and thereafter increasing the heat content of the saturated vapor while exposing it to another heat source to form the superheated vapor.

Claim 54

A process according to claim 33 further comprising the step of thermally insulating the high and low pressure zones.

Claim 55

A process according to claim 33 wherein the temperature of the superheated vapor is no more than approximately 400 degrees F.

Claim 56

A process according to claim 33 wherein the working fluid is at a maximum pressure of about 700 psig.

Claim 57

A process according to claim 33 wherein the working shaft is rotatable and rotates at a speed of no more than about 450 revolutions per minute.

Claim 58

A process according to claim 33 wherein the working fluid comprises a refrigerant capable of undergoing a phase change within the desired thermal operating range.

Claim 59

A process according to claim 55 wherein the working fluid comprises Freon.

Claim 60

A process according to claim 55 wherein the working fluid comprises water.

Claim 61

A process according to claim 33 wherein the temperature of the vapor drops such that the expansion of vapor is completed in the low pressure cylinder before the third variable volume has expanded to a maximum by movement of the low pressure piston and further comprising a step of selectively exposing the third variable volume to the low pressure zone to prevent a vacuum from being drawn in the third variable volume.

Claim 62

A process according to claim 33 wherein the temperature of the vapor drops such that the expansion of vapor is completed in the low pressure cylinder before the fourth variable volume has expanded to a maximum by movement of the low pressure piston and further comprising a step of selectively exposing the fourth variable volume to the low pressure zone to prevent a vacuum from being drawn in the fourth variable volume.

Claim 63

A process according to claim 33 wherein the temperature of the vapor increases such that the expansion of vapor is limited in the low pressure cylinder and further comprising the step of selectively exposing the second and third variable volumes to the high and low pressure zones, respectively, to permit the required expansion of vapor discharged from the second to the third variable volumes.

Claim 64

A process according to claim 33 wherein the temperature of the vapor increases such that the expansion of vapor is limited in the low pressure cylinder and further comprising the step of selectively exposing the first and fourth variable volumes to the high and low pressure zones, respectively, to permit the required expansion of vapor discharged from the first to the fourth variable volumes.

Claim 65

A process according to claim 33 wherein mass flow of vapor is reduced during operation by extending the time that the first variable volume is in fluid communication with the high pressure zone and extending the time the fourth variable volume is in fluid communication with the low pressure zone prior to the transfer of mass flow from the first variable volume to the fourth variable volume.

Claim 66

A process according to claim 33 wherein mass flow of vapor is reduced during operation by extending the time that the second variable volume is in fluid communication with the high pressure zone and extending the time the third variable volume is in fluid communication with the low pressure zone prior to the transfer of mass flow from the second variable volume to the third variable volume.

Claim 67

A process according to claim 33 wherein the overall efficiency is at least about 90 percent as compared to a Carnot cycle.

Claim 68

A process for generating power comprising the steps of: generating a superheated vapor with a temperature no greater than 400 degrees F. by heating condensed vapor from a low pressure zone in a superheating zone using a low grade heat source to cause the condensed vapor to undergo a phase change to saturated vapor during generally isobaric heat addition and thereafter increasing the heat content of the saturated vapor by exposing it to another heat source to form the superheated vapor; supplying the superheated vapor to a high pressure zone thermally separated from the low pressure zone to maintain the vapor in the high pressure zone at a substantially constant high pressure of no more than 700 psig; imparting work to a working shaft operably connected by a crank mechanism rotatable through 360 degrees to a high pressure piston by constantly exposing the lower face of the high pressure piston to the vapor in the high pressure zone while selectively exposing the upper face of the high pressure piston to the vapor in the high pressure zone as the high pressure piston approaches upper dead center in relation to the working shaft, said upper face of the high pressure piston forming a first variable volume with the high pressure cylinder wall; concurrently therewith intermittently discharging vapor from the first variable volume to a larger second variable volume formed of the lower face of a low pressure piston linked directly to the high pressure piston and a low pressure cylinder wall while constantly exposing the upper face of the low pressure piston through low pressure vapor in a low pressure zone to thereby obtain a maximum pressure differential between the high and low pressure pistons and intermittently exposing the second variable volume to the low pressure zone, said second variable volume being allowed to increase more rapidly than the first variable volume decreases as the high and low pressure pistons move from bottom dead center to top dead center in relation to the working shaft, said working shaft operating at a rotational speed of no more than about 450 revolutions per minute; wherein high pressure vapor in the first variable volume generally undergoes an adiabatic isentropic expansion as the vapor is intermittently discharged from the first variable volume to the second variable volume and wherein vapor in the high pressure zone impacting the lower face of the high pressure piston performs a generally isobaric work process as the vapor is intermittently discharged from the first variable volume to the second variable volume; intermittently discharging vapor from the second variable volume to the low pressure zone; and condensing discharged vapor from the second variable volume in the low pressure zone for recycle to the superheating zone.

Claim 69

A process for generating power comprising the steps of: generating a superheated vapor with a temperature no greater than 400 degrees F. by heating condensed vapor from a low pressure zone in a superheating zone using a low grade heat source to cause the condensed vapor to undergo a phase change to saturated vapor during generally isobaric heat addition and thereafter increasing the heat content of the saturated vapor by exposing it to another heat source to form the superheated vapor; supplying the superheated vapor to a high pressure zone thermally separated from the low pressure zone to maintain the vapor in the high pressure zone at a substantially constant high pressure of no more than 700 psig; imparting work to a working shaft operably connected by a crank mechanism rotatable through 360 degrees to a high pressure piston by constantly exposing the lower face of the high pressure piston to the vapor in the high pressure zone while selectively exposing the upper face of the high pressure piston to the vapor in the high pressure zone as the high pressure piston approaches upper dead center in relation to the working shaft, said upper face of the high pressure piston forming a first variable volume with the high pressure cylinder wall; concurrently therewith intermittently discharging vapor from the first variable volume to a larger second variable volume formed of the lower face of a low pressure piston linked directly to the high pressure piston and a low pressure cylinder wall while constantly exposing the upper face of the low pressure piston through low pressure vapor in a low pressure zone to thereby obtain a maximum pressure differential between the high and low pressure pistons and intermittently exposing the second variable volume to the low pressure zone, said second variable volume being allowed to increase more rapidly than the first variable volume decreases as the high and low pressure pistons move from bottom dead center to top dead center in relation to the working shaft, said working shaft operating at a rotational speed of no more than about 450 revolutions per minute; wherein high pressure vapor in the first variable volume generally undergoes an adiabatic isentropic expansion as the vapor is intermittently discharged from the first variable volume to the second variable volume and wherein vapor in the high pressure zone impacting the lower face of the high pressure piston performs a generally isobaric work process as the vapor is intermittently discharged from the first variable volume to the second variable volume; intermittently discharging vapor from the second variable volume to the low pressure zone; and condensing discharged vapor from the second variable volume in the low pressure zone for recycle to the superheating zone.