Heat machine configured for realizing heat cycles and method for realizing heat cycles by means of such heat machine

Abstract

A heat machine for realizing a heat cycle, operating with a thermal fluid includes a drive unit. A first rotor and a second rotor, each having three pistons slidable in an annular chamber, wherein the pistons delimit six variable-volume chambers. The drive unit includes a transmission to convert the rotary motion with first and second periodically variable angular velocities of said first and second rotor, offset from each other, into a rotary motion at a constant angular velocity. The heat machine further includes a compensation tank, to accumulate the compressed fluid from the drive unit, a regenerator to preheat the fluid, a heater to superheat the fluid circulating in the serpentine coil, a burner, to supply the thermal energy to the heater; wherein the regenerator, in fluid communication with the drive unit, is configured to acquire energy-heat from the exhausted fluid and to preheat the fluid sent to the heater.

Claims

1. A heat machine for realizing a heat cycle, the heat machine operating with a thermal fluid and configured to function with a combined heat cycle using hot air and aqueous vapour, featuring unidirectional continuous motion of the thermal fluid, the heat machine comprising: a drive unit comprising: a casing delimiting therein an annular chamber and having dimensioned inlet or discharge openings in fluid communication with conduits external to the annular chamber, wherein each inlet or discharge opening is angularly spaced from the adjacent inlet and discharge openings so as to define an expansion/compression path for a working fluid in the annular chamber; a first rotor and a second rotor rotatably installed in said casing; wherein each one of the two rotors has three pistons that are slidable in the annular chamber; wherein the pistons of one of the rotors are angularly alternated with the pistons of the other rotor; wherein angularly adjacent pistons delimit six variable-volume chambers; a primary shaft operatively connected to said first and second rotor; a transmission that is operatively interposed between said first and second rotor and the primary shaft and configured to convert the rotational motion with respective first and second periodically variable angular velocities of said first and second rotor that are offset relative to each other into a rotational motion having a constant angular velocity of the primary shaft; wherein the transmission is configured to confer, on the periodically variable angular velocity of each of the rotors, six periods of variation for each complete revolution of the primary shaft; wherein said drive unit is a rotary volumetric expander operating with said thermal fluid; a first section of the drive unit, where, following the movement of the two pistons away from each other, the thermal fluid, passing through the inlet opening, is suctioned into the chamber; a second section of said drive unit, where, following the movement of the two pistons towards each other, the previously suctioned thermal fluid is compressed in the chamber and then, on passing through the discharge opening, a pipe and a check valve, it is conveyed into a compensation tank; a compensation tank configured to accumulate the compressed thermal fluid to make it available, via pipes and the check valve, for subsequent use thereof, in a continuous mode; a regenerator, in fluid communication via pipes with said drive unit and configured to preheat the thermal fluid prior to its entry in a heater; a heater configured to superheat the thermal fluid circulating in a serpentine coil, using the thermal energy produced by a burner; a burner with a combustion chamber attached thereto, said burner being apt for operating with various types of fuel and being capable of supplying the necessary thermal energy to the heater; a third section of said drive unit, in fluid communication with said heater, via pipes, and capable of receiving, via the inlet openings, the thermal fluid heated to a high temperature under pressure in the heater so as to have it expand in the chambers, which are delimited by the pistons, respectively, for the purpose of having said pistons rotate and produce work; a fourth section of said drive unit, in fluid communication with the regenerator through the discharge openings and pipes, and wherein, due to the reduction in volume of the two chambers brought about by the movement of the two pairs of pistons towards each other, the exhausted thermal fluid is forcedly expelled; wherein said regenerator, in fluid communication with said drive unit, is further configured to acquire heat-energy from the exhausted thermal fluid and to use it to preheat the thermal fluid to be sent to the heater.

2. The heat machine according to claim 1, wherein the first section of the drive unit is in fluid connection with the external environment via a pipe, so that the ambient air can be suctioned into the chamber, and wherein the heat machine comprises a metering pump in fluid connection with a distilled water tank and arranged so as to enable a predefined amount of distilled water to be injected in an air circuit by means of an injector, said predefined amount being capable of increasing the unit power of the drive unit and of ensuring lubrication of the cylinder.

3. The heat machine according to claim 1, comprising: a cooler that is operatively interposed between the low temperature outlet of the regenerator and the inlet of the heater, wherein the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section, and wherein, pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through and reaches an injector arranged so as to inject, in an air circuit, a predefined amount of condensate water, which is capable of increasing the unit power of the drive unit and of ensuring lubrication of the cylinder.

4. The heat machine according to claim 1, comprising: a cooler that is operatively interposed between the low temperature outlet of the regenerator and the inlet of the heater; wherein the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section, and wherein, pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through the pipes and reaches an evaporator that is configured to heat and vaporize the condensate water and send it to an injector arranged so as to inject, in an air circuit, a predefined amount of aqueous vapour, which is capable of increasing the unit power of the drive unit and of ensuring lubrication of the cylinder, wherein said evaporator is operatively interposed, with its high temperature side, between said high pressure pump and said injector, and wherein said evaporator is configured to receive as incoming fluid, on its low temperature side, the exhausted thermal fluid expelled from the outlet of the drive unit, so as to acquire residual heat-energy from this exhausted thermal fluid and to use it to preheat the thermal fluid to be sent to the heater.

5. The heat machine according to claim 1, comprising: a cooler that is operatively interposed between the low temperature outlet of the regenerator and the inlet of the heater; wherein the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section, and wherein, pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through the pipes and reaches an evaporator that is configured to heat and vaporize the condensate water and send it to a superheater, which, by extracting energy from the hot combustion fumes downstream of the burner, is configured to superheat the saturated vapour exiting from the evaporator, so as to supply energy thereto; wherein said superheater is configured to send the vaporized and superheated condensate water to an injector, which is arranged so as to enable injection, in an air circuit, of a predefined amount of superheated aqueous vapour, which is capable of further increasing the unit power of the drive unit and of ensuring lubrication of the cylinder, wherein said evaporator is operatively interposed, with its high temperature side, between said high pressure pump and said superheater, and wherein said evaporator is configured to receive as incoming fluid, on its low temperature side, the exhausted thermal fluid expelled from the outlet of the drive unit, so as to acquire residual heat-energy from this exhausted thermal fluid and to use it to preheat the thermal fluid to be sent to the heater.

6. The heat machine according to claim 5, and provided with a cooling circuit comprising: a first recuperator, located upstream of the burner, where combustion air is drawn from the environment; a cooling unit (interspace) associated with the drive unit; a second recuperator, located downstream of the burner and the heater, along the exit path of the hot combustion fumes; a plurality of cooling pipes connecting in series said first recuperator, said cooling unit and said second recuperator, so as to form a circular path, and bearing an amount of cooling fluid; a cooling pump located in said circuit and that is operatively active on one pipe of said plurality of cooling pipes so as to bring about circulation of said cooling fluid in the cooling circuit; wherein: said first recuperator is configured to cool said cooling fluid by surrendering heat-energy to said combustion air; said cooling unit is configured to cool the drive unit by transfer of heat-energy from the drive unit to the cooling fluid, which undergoes an increase in temperature; said second recuperator is configured to heat said cooling fluid by acquiring heat-energy from the hot combustion fumes.

7. The heat machine according to claim 1, and equipped with an auxiliary hydraulic circuit comprising: an auxiliary recuperator, located downstream of the burner and the heater, along the exit path of the hot combustion fumes; a plurality of auxiliary pipes configured to pass through said auxiliary recuperator and to be connected with one or more auxiliary uses, an auxiliary pump, located in said circuit and that is operatively active on one pipe of said plurality of auxiliary pipes so as to bring about circulation in said auxiliary circuit; wherein said auxiliary recuperator is configured to recover energy from the combustion fumes and to transmit it to the fluid circulating in said auxiliary circuit, said energy thus being available for said auxiliary uses.

8. The heat machine according to claim 1, further comprising: a fan located upstream of the burner and configured to draw combustion air from the environment and to send it forcedly to said burner to feed the combustion process; and/or one or more check vales located along the pipes of the heat machine and configured to facilitate circulation of the thermal fluid in a unidirectional manner and prevent the outflow of the thermal fluid in the opposite direction.

9. A method for realizing a heat cycle, the method operating with a thermal fluid and being configured to function with a combined heat cycle using hot air and aqueous vapour, featuring unidirectional continuous motion of the thermal fluid, the method comprising the steps of: arranging a heat machine, according to claim 1, carrying out the following steps: starting up the primary shaft and the transmission of the drive unit, setting the pistons into motion; activating the burner and starting up the combustion process; when the thermal fluid circulating in the heat machine has reached a pre-established minimum operating state, the drive unit produces the work needed to be able to turn independently; following the movement of the two pistons away from each other, the thermal fluid is suctioned into the chamber through the suctioning opening; following the movement of the two pistons towards each other, the previously suctioned thermal fluid is compressed in the chamber, undergoes an increase in temperature from T1′ to T2, passes through the discharge opening and reaches the compensation tank; with the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings, the thermal fluid flows out from the tank and passes through the regenerator, where it undergoes an increase in temperature from T2 to T2′; the thermal fluid passes through the heater, where it receives heat-energy and increases in temperature from T2″ to T3; rotating in the annular cylinder, when the pistons open the inlet openings, the superheated thermal fluid is admitted into the expansion chambers where it expands, with a decrease in its temperature from T3 to T4 and, as it makes the pistons rotate, it produces useful work; following the movement of the pistons towards each other, the chambers diminish in volume, the exhausted thermal fluid is expelled from the drive unit, passes through the discharge openings, and through the regenerator, where it surrenders part of the heat-energy still possessed and undergoes a decrease in temperature from T4 to T4′.

10. The method according to claim 9, wherein in the step of suctioning the thermal fluid into the chamber, said thermal fluid is air suctioned from the environment at temperature T1′, and wherein the method comprises the steps of: drawing distilled water from the tank; activating the metering pump and introducing a given amount of distilled water into the circuit by means of the injector; thereby bringing about a decrease in the temperature of the resulting thermal fluid from T2′ to T2″; and wherein, following the step of passing through the regenerator, the exhausted thermal fluid is discharged into the atmosphere.

11. The method according to claim 9, further comprising the following steps: the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section; pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through pipes and reaches an injector arranged so as to enable injection, in an air circuit, of a predefined amount of condensate water, which is capable of increasing the unit power of the drive unit and of ensuring lubrication of the cylinder.

12. The method according to claim 9, further comprising the following steps: the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section; pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through the pipes and reaches an evaporator that is configured to heat and vaporize the condensate water and to send it to an injector arranged so as to enable injection, in air circuit, of a predefined amount of aqueous vapour, which is capable of increasing the unit power of the drive unit and of ensuring lubrication of the cylinder; wherein said evaporator is configured to receive as incoming fluid, on its low temperature side, the exhausted thermal fluid expelled from the outlet of the drive unit, so as to acquire residual heat-energy from this exhausted thermal fluid and to use it to preheat the thermal fluid to be sent to the heater.

13. The method according to claim 9, further comprising the following steps: the thermal fluid, exiting from the cooler at temperature T1, passes into a pipe, passes through a condensate trap, where the water in the thermal fluid is condensed and separated from the air, passes into a pipe at temperature T1′, passes through the suctioning opening and following the movement of the two pistons away from each other, is suctioned into the chamber of said first section; pushed by a high-pressure pump, the condensate water previously extracted from the air by the trap travels through the pipes and reaches an evaporator that is configured to heat and vaporize the condensate water and to send it to a superheater, which, by extracting energy from the hot combustion fumes downstream of the burner, is configured to superheat the saturated vapour exiting from the evaporator, so as to supply energy thereto; wherein said superheater is configured to send the superheated aqueous vapour to an injector, which is arranged so as to enable injection, in an air circuit, of a predefined amount of said superheated aqueous vapour, which is capable of further increasing the unit power of the drive unit, of increasing the overall yield and of ensuring lubrication of the cylinder, and wherein said evaporator is configured to receive as incoming fluid, on its low temperature side, the exhausted thermal fluid expelled from the outlet of the drive unit, so as to acquire residual heat-energy from this exhausted thermal fluid and to use it to preheat the thermal fluid to be sent to the heater.

14. The method according to claim 13, further comprising the following steps: arranging a cooling circuit, comprising: a first recuperator, located upstream of the burner, where combustion air is drawn from the environment; a cooling unit associated with the drive unit; a second recuperator, located downstream of the burner and the heater, along the exit path of the hot combustion fumes; a plurality of cooling pipes connecting in series said first recuperator, said cooling unit and said second recuperator, so as to form a circular path, and bearing an amount of cooling fluid; a cooling pump located in said circuit and that is operatively active on one pipe of said plurality of cooling pipes so as to bring about circulation of said cooling fluid in the cooling circuit; carrying out the following steps: cooling the cooling fluid by means of said first recuperator by surrendering heat-energy to said combustion air; cooling, by means of said cooling unit, the drive unit by transfer of heat-energy from the drive unit to the cooling fluid, which undergoes an increase in temperature; heating, by means of said second recuperator, said cooling fluid by acquiring heat-energy from the hot combustion fumes.

15. The method according to claim 9, further comprising the following steps: arranging an auxiliary hydraulic circuit, comprising: an auxiliary recuperator, located downstream of the burner and the heater, along the exit path of the hot combustion fumes; a plurality of auxiliary pipes configured to pass through said auxiliary recuperator and to be connected with one or more auxiliary uses; an auxiliary pump, located in said circuit and that is operatively active on one pipe of said plurality of auxiliary pipes so as to bring about circulation in said auxiliary circuit; carrying out the following steps: recovering energy from the combustion fumes, by means of said auxiliary recuperator; transmitting said energy to the fluid circulating in said auxiliary circuit; making said energy available for auxiliary uses.

Description

DESCRIPTION OF THE DIAGRAMS AND DRAWINGS

(1) With reference to the accompanying diagrams and drawings, it is noted that the same are provided solely by way of illustration and not by way of limitation; in them:

(2) FIG. 1 shows a schematic front view of a drive unit utilizable in the present invention;

(3) FIG. 2a illustrates a side sectional view of the central body of the drive unit of FIG. 1;

(4) FIG. 2b is a side sectional view of a variant of the central body of the drive unit of FIG. 1, with a section of the motion transmission system;

(5) FIG. 3 illustrates a front view of the train of three-lobe gears forming part of the motion transmission system of the drive unit of FIG. 1;

(6) FIG. 4 illustrates the operating diagram of the closed-circuit Ericsson cycle carried out with an engine provided with pistons with reciprocating motion;

(7) FIG. 5 illustrates the operating diagram of a heat machine with a closed-circuit Joule cycle carried out with a single-shaft turbine;

(8) FIG. 6 schematically illustrates a first possible embodiment of a heat machine according to the present invention in an “open-circuit” configuration characterized by the use of a thermal fluid composed of air with the injection of water;

(9) FIG. 7 schematically illustrates a second possible embodiment of a heat machine according to the present invention, in a “closed-circuit” configuration, characterized by the use of a thermal fluid composed of air with the injection of condensate of aqueous vapour;

(10) FIG. 8 schematically illustrates a third possible embodiment of a heat machine according to the present invention, in a “closed-circuit” configuration, characterized by the use of a thermal fluid composed of air with the injection of saturated aqueous vapour;

(11) FIG. 9 illustrates a functional diagram that shows the energy recovery obtainable through the vaporization of condensed water;

(12) FIG. 10 illustrates a functional diagram that shows the increase in energy obtainable through the vaporization of condensed water and with the use of superheated aqueous vapour in the cycle;

(13) FIG. 11 schematically illustrates a fourth possible embodiment of a heat machine according to the present invention, in a “closed-circuit” configuration, characterized by the use of a thermal fluid composed of air with the injection of superheated aqueous vapour;

(14) FIG. 12 schematically illustrates a fifth possible embodiment of a heat machine according to the present invention, in a “closed-circuit” configuration, characterized by the use of a thermal fluid composed of air with the injection of superheated aqueous vapour and provided with an energy recovery system with thermal stabilization of the drive unit;

(15) FIG. 13 shows an enlargement of a portion of the heat machine according to the present invention; this portion is identical for the configurations shown in FIGS. 6, 7, 8, 11 and 12.

DETAILED DESCRIPTION OF THE DRIVE UNIT EMPLOYED IN THE HEAT MACHINE

(16) With reference to FIGS. 1, 2a, 2b, 3, (1) denotes in its entirety the “drive unit” employed as “compressor/expander” in a new “pulsating heat cycle” operating preferably with hot air and aqueous vapour.

(17) The drive unit 1 comprises a casing 2 which internally delimits a seat 3.

(18) In the non-limiting embodiment illustrated, the casing 2 is made up of two half-parts 2a, 2b joined together.

(19) Housed in the seat 3 there is a first rotor 4 and a second rotor 5, which rotate around a same axis “X-X”.

(20) The first rotor 4 has a first cylindrical body 6 and three first elements 7a, 7b, 7c which extend radially from the first cylindrical body 6 and are rigidly connected or integral therewith.

(21) The second rotor 5 has a second cylindrical body 8 and three second elements 9a, 9b, 9c which extend radially from the second cylindrical body 8 and are rigidly connected or integral therewith.

(22) The elements 7a, 7b, 7c of the rotor 4 are angularly equidistant from one another, i.e. each element is spaced apart from the adjacent element on average by an angle “a” of 120° (measured between the planes of symmetry of each element).

(23) The elements 9a, 9b, 9c of the rotor 5 are angularly equidistant from one another, i.e. each element is spaced apart from the adjacent element on average by an angle “a” of 120° (measured between the planes of symmetry of each element).

(24) The first and second cylindrical bodies 6, 8 are set side by side at respective bases 10, 11 and are coaxial.

(25) The three first elements 7a, 7b, 7c of the first rotor 4 moreover extend along an axial direction and have a projecting portion disposed in a position that is radially external to the second cylindrical body 8 of the second rotor 5.

(26) The three second elements 9a, 9b, 9c of the second rotor 5 moreover extend along an axial direction and have a projecting portion disposed in a position that is radially external to the first cylindrical body 6 of the first rotor 4.

(27) The three first elements 7a, 7b, 7c are alternated with the three second elements 9a, 9b, 9c along the circumferential extent of the annular chamber 12.

(28) Each of the first and second elements 7a, 7b, 7c, 9a, 9b, 9c has, in a radial section (FIG. 1), a substantially trapezoidal profile which converges toward the rotation axis “X-X” and, in a axial section (FIG. 2a,2b), a substantially circular or rectangular profile.

(29) Each of the first and second elements 7a, 7b, 7c, 9a, 9b, 9c has an angular size, given purely by way of approximation and not by way of limitation, of about 38°.

(30) Peripheral surfaces that are radially external to the first and second cylindrical bodies 6, 8 delimit, together with an inner surface of the seat 3, an annular chamber 12.

(31) The annular chamber 12 is therefore divided into variable-volume “rotating chambers” 13′, 13″, 13′″, 14′, 14″, 14′″ by the first and second elements 7a, 7b, 7c, 9a, 9b, 9c. In particular, each variable-volume “rotating chamber” is delimited (besides by the surface radially internal to the casing 2 and the surface radially external to the cylindrical bodies 6, 8) by one of the first elements 7a, 7b, 7c and one of the second elements 9a, 9b, 9c.

(32) In the first FIG. 2a, each of the first and second elements 7a, 7b, 7c, 9a, 9b, 9c has, in an axial section thereof, a substantially circular profile and the annular chamber 12 likewise has a circular cross section defined as “toroidal”.

(33) In the variant in FIG. 2b, each of the first and second elements 7a, 7b, 7c, 9a, 9b, 9c has, in a axial section thereof, a rectangular (or square) profile and the annular chamber 12 likewise has a rectangular (or square) cross section.

(34) Between inner walls of the annular chamber 12 and each of the aforesaid first and second elements 7a, 7b, 7c, 9a, 9b, 9c there remains an interspace such as to permit the rotary movement of the pistons 4, 5 and sliding of the elements 7a, 7b, 7c, 9a, 9b, 9c in the chamber 12 itself.

(35) The first and second elements 7a, 7b, 7c, 9a, 9b, 9c are the pistons of the drive unit 1 illustrated and the variable-volume rotating chambers 13′, 13″, 13′″, 14′, 14″, 14′″ are the chambers for the compression and/or expansion of the working fluid of said drive unit 1.

(36) The inlet or discharge openings 15′, 16′, 15″, 16″, 15′″, 16′″ (of suitable size and shape) are fashioned in a wall radially external to the casing 2; they open into the annular chamber 12 and are in fluid communication with conduits external to the annular chamber 12, illustrated further below.

(37) Each inlet or discharge opening 15′, 16′, 15″, 16″, 15′″, 16′″ is angularly spaced in an appropriate way so as to adapt to the requirements of each different individual functional configuration of the drive unit 1.

(38) The drive unit 1 further comprises a primary shaft 17 parallel to and distanced from the rotation axis “X-X” and rotatably mounted on the casing 2 and a transmission 18 mechanically interposed between the primary shaft 17 and the rotors 4, 5.

(39) The transmission 18 comprises a first auxiliary shaft 19 onto which the first rotor 4 is keyed and a second auxiliary shaft 20 onto which the second rotor 5 is keyed. The first and second auxiliary shafts 19, 20 are coaxial with the rotation axis “X-X”. The second auxiliary shaft 20 is tubular and houses within it a portion of the first auxiliary shaft 19. The first auxiliary shaft 19 can rotate in the second auxiliary shaft 20 and the second auxiliary shaft 20 can rotate in the casing 2.

(40) A first three-lobe gear 23 is keyed onto the primary shaft 17. A second three-lobe gear 24 is keyed onto the primary shaft 17 next to the first. The second three-lobe gear 24 is mounted on the primary shaft 17 angularly offset relative to the first three-lobe gear 23 by an angle “A” of 60°. The two three-lobe gears 23 and 24 rotate together jointly with the primary shaft 17.

(41) A third three-lobe gear 25 is keyed onto the first auxiliary shaft 19 (so as to rotate integrally therewith) and the teeth thereof precisely enmesh with the teeth of the first three-lobe gear 23.

(42) A fourth three-lobe gear 26 is keyed onto the second auxiliary shaft 20 (so as to rotate integrally therewith) and the teeth thereof precisely enmesh with the teeth of the second three-lobe gear 24.

(43) Each of the above-mentioned three-lobe gears 23, 24, 25, 26 has approximately the profile of an equilateral triangle with rounded vertices 27 and connecting portions 28, interposed between the vertices 27, which can be concave, flat or convex.

(44) Changing the shape of the vertices 27 and connecting portions 28 of the gears makes it possible to pre-establish the value of the angular periodic movement of the auxiliary shafts 19, 20 during their rotary motion.

(45) The structure of the transmission 18 is such that during a complete revolution of the primary shaft 17 the two rotors 4, 5 also carry out a complete revolution, but with periodically variable angular velocities, offset from each other, which induce the adjacent pistons 7a, 9a; 7b, 9b; 7c, 9c to move away and toward one another three times during a complete 360° revolution. Therefore, each of the six variable-volume chambers 13′, 13″, 13′″, 14′, 14″, 14′″ expands three times and contracts three times at each complete revolution of the primary shaft 17.

(46) In others words, pairs of adjacent pistons of the six pistons 7a, 7b, 7c; 9a, 9b, 9c are movable, during their rotation at a periodically variable angular velocity in the annular chamber 12, between a first position, in which the two faces of the adjacent pistons lie substantially next to each other, and a second position, in which the same faces are angularly spaced apart by the maximum allowed. Purely by way of example, in the first position the two faces of the adjacent pistons are angularly spaced apart from each other by about 1°, whereas in the second position the two same faces are angularly spaced apart from each other by about 81°.

(47) The six variable-volume chambers 13′, 13″, 13′″, 14′, 14″, 14′″ are made up of a first group of three chambers 13′, 13″, 13′″ and a second group of three chambers 14′, 14″, 14′″. When the three chambers 13′, 13″, 13′″ of the first group have the minimum volume (pistons next to each other at the minimum reciprocal distance) the other three chambers 14′, 14″, 14′″ (of the second group) have the maximum volume (pistons at the maximum reciprocal distance).

(48) For the purpose of better clarifying and highlighting the innovative aspects of the present invention, the five main functional configurations will be described below in a precise and detailed manner.

(49) In order to describe the operation of the new heat machine (121), configured to operate with a “pulsating heat cycle” according to the present invention, it is necessary to start off by noting that in the drive unit (1), in each of the six periodically variable-volume chambers (13′,13″,13′″,14′,14″,14′″), each delimited by the two pistons adjacent to each other and rotating inside the annular cylinder, the diversified suction, compression, expansion and expulsion functions are performed periodically.

(50) FIG. 13 shows an enlargement of a portion of the heat machine according to the present invention; this portion relates to the drive unit employed, identically, in the five configurations that are shown in FIGS. 6, 7, 8, 11 and 12, and are the subject matter of the following five descriptions (A, B, C, D, E). The reference numbers included in FIG. 13, used to identify elements of the drive unit 1 and its connection to the components of the heat machine 121, are applicable to the corresponding elements shown in FIGS. 6, 7, 8, 11 and 12.

(51) For the sake of simplicity, in the following five descriptions (A, B, C, D, E), the path followed by the thermal fluid in the different sections of the heat engine (121) will be explained as if a single complete heat cycle were involved. In reality, for each revolution of the drive shaft (corresponding to a revolution angle of) 360° no fewer than six complete heat cycles are carried out.

(52) A. Detailed Description of the Heat Machine 121 Operating According to the Functional Configuration Represented in the FIG. 6.

(53) Compared to the Joule-Ericsson cycles on their own and the sole “drive unit”, the novelty introduced with this configuration regards the realization of a “combined” operating cycle, where the thermal fluid is a mixture of air and water (transformed into vapour); this ensures the lubrication of the cylinder (where the pistons slide) and enables a higher unit power to be obtained, albeit with a slight decrease in overall efficiency.

(54) With reference to FIG. 6, in the position where the pistons are located, the following main steps of the cycle can be identified:

(55) A1_Setting into Motion.

(56) Noting first of all that all control and regulating devices are powered via a specific auxiliary electric line (not represented), the start-up of the heat machine 121 takes place in the following manner: the primary shaft 17 (visible in FIG. 2b) and the whole transmission system that moves the six pistons 7a,7b,7c,9a,9b,9c are set in rotation via the starter motor, thus creating the preliminary condition for start-up of the cycle; the metering pump for metering distilled water 97b is activated; the fan 92 is activated; the burner is activated by acting on the regulation valve 91 (which controls the injection of fuel F) 40 and the combustion process is started; when the circulating thermal fluid has reached the predetermined minimum operating condition, the drive unit 1 will be capable of producing the work necessary in order to be able to run autonomously.
A2_Start of the Cycle, Starting from the Step of Suctioning Ambient Air.

(57) The air suctioned from the environment at temperature T1′, passes into the pipe 93, passes through the suctioning opening 15′″ and, following the movement of the two pistons 9c-7c away from each other, it is suctioned into the chamber 13′″.

(58) A3_Step of Compression and Recovery of the Suctioned Air.

(59) Following the movement of the two pistons 7c-9a towards each other, the previously suctioned air is compressed in the chamber 14′″ (up to the limit, which is normally preset with a minimum ratio of 1:4 and a maximum ratio of 1:20), undergoes an increase in temperature from T1′ to T2, passes through the discharge opening 16′″, the pipe 44′ and the check valve 44a and ends up in the compensation tank 44, where it remains available for immediate use.

(60) A4_Step of Preheating the Compressed Thermal Fluid.

(61) With the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings 15,15″, the air flows out from the tank 44, passes through the pipe 44″ and the check valve 44b, travels through the pipe 44″, and passes into the regenerator 42 (where it undergoes an increase in temperature from T2 to T2′).

(62) A5_Step of Injecting Distilled Water into the Air Conduit.

(63) The air, exiting from the regenerator 42, travels through the pipe 42′, passes through the check valve 42a and passes into the pipe 42′″.

(64) The distilled water is drawn from the tank 97a, travels through the pipe 97″, is brought to a high pressure in the metering pump 97b and, at temperature Tc, is conveyed into the pipe 97′″ and, by means of the injector 97, it is introduced into the pipe 42′″ where, as a result of mixing, the mixture thus formed undergoes a decrease in temperature from T2′ to T2″.

(65) A6_Step of Superheating the Circulating Thermal Fluid.

(66) The mixed thermal fluid travels through the pipe 97′, passes through the heater 41 (adjacent to the combustion chamber 40A and provided with the multi-fuel burner 40), where it receives heat-energy and increases in temperature from T2″ to T3.

(67) A7_Step of Expanding the Superheated Thermal Fluid and Producing Useful Work.

(68) When the pistons 7a-7b, by rotating in the annular cylinder in the direction of motion indicated by the arrows, open the inlet openings 15-15″, the superheated thermal fluid flowing through the pipes 41′-41″-41′″ is introduced into the expansion chambers 13′ and 13″, where it is expanded (decreasing in temperature from T3 to T4) and, by making the pistons rotate, produces useful work.

(69) A8_Step of Expulsion and of Recovering Energy from the Exhausted Thermal Fluid.

(70) Following the movement of the pistons 7a-9b and 7b-9c towards each other, the chambers 14′ and 14″ diminish in volume, the exhausted thermal fluid (already expanded in the previous cycle) is expelled from the drive unit 1, passes through the two discharge openings 16′-16″, flows through the pipes 45′-45″-45″, passes through the regenerator 42 (where it surrenders part of the energy-heat still possessed and undergoes a decrease in temperature from T4 to T4′) and then, on passing through the pipe 42″, is discharged into the atmosphere, the heat cycle thus being concluded.

(71) A9_Recovery of Energy with a Reduction in the Temperature of the Combustion Fumes.

(72) Given that the function envisaged for the heat machine is also to provide energy-heat to be destined to auxiliary uses (space heating and/or production of domestic hot water, etc.), before the hot fumes are discharged into the atmosphere (through the conduit 102), all their residual energy is recovered by reducing their temperature as much as possible (it also being possible to recover further energy through their possible condensation). To achieve this purpose, use is made of a specific hydraulic circuit, where the following mode of conveyance is adopted: the incoming thermal fluid (normally water) from the auxiliary uses 103 passes into the pipe 103′ and, pushed by the circulation pump 104, passes into the pipe 104′, reaches the recuperator 101 at the low temperature Tf and then, on passing through it, thanks to the reduction in the temperature of the fumes S from Th7 to Th2, acquires energy-heat and heats up to the higher temperature Tg, so as to be made available, via the pipe 101′, for the auxiliary uses 130, and for the intended purpose.

(73) B. Detailed Description of the Heat Machine 121 Operating According to the Functional Configuration Represented in FIG. 7.

(74) Compared to the Joule-Ericsson cycles on their own and the sole “drive unit”, the novelty introduced with this configuration regards the realization of a “combined” operating cycle, where the thermal fluid is a mixture of air and water (transformed into vapour); this ensures the lubrication of the cylinder (where the pistons slide) and enables a higher unit power to be obtained, albeit with a slight decrease in overall efficiency.

(75) With reference to FIG. 7, in the position where the pistons are located, the following main steps of the cycle can be identified:

(76) B1_Setting into Motion the Heat Machine 121.

(77) Noting first of all that all control and regulating devices are powered via a specific auxiliary electric line (not represented), the start-up of the heat machine 121 takes place in the following manner: the primary shaft 17 (visible in FIG. 2b) and the whole transmission system that moves the six pistons 7a,7b,7c,9a,9b,9c are set in rotation via the starter motor, thus creating the preliminary condition for start-up of the cycle; the condensate water pump 94 is activated; the fan 92 is activated; the burner 40 is activated by acting on the regulation valve 91 (which controls the injection of fuel F) and the combustion process is started; when the circulating thermal fluid has reached the predetermined minimum operating condition, the drive unit 1 will be capable of producing the work necessary in order to be able to run autonomously.
B2_Start of the Cycle, Starting from the Step of Suctioning the Cooled Thermal Fluid.

(78) The thermal fluid, exiting from the cooler 43 at temperature T1, passes into the pipe 43′, passes through the condensate trap 93 (where the water in the thermal fluid is condensed and separated from the air), passes into the pipe 93′ at temperature T1′, passes through the suctioning opening 15′″ and, following the movement of the two pistons 9c-7c away from each other, is suctioned into the chamber 13′″.

(79) B3_Step of Compression and Recovery of the Suctioned Thermal Fluid.

(80) Following the movement of the two pistons 7c-9a towards each other, the previously suctioned air is compressed in the chamber 14′ (up to the limit, which is normally preset with a minimum ratio of 1:4 and a maximum ratio of 1:20), undergoes an increase in temperature from T1′ to T2, passes through the discharge opening 16′″, the pipe 44′ and the check valve 44a and ends up in the compensation tank 44, where it remains available for immediate use.

(81) B4_Step of Preheating the Compressed Thermal Fluid.

(82) With the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings 15,15″, the air flows out from the tank 44, passes through the pipe 44″ and the check valve 44b, travels through the pipe 44″, and passes into the regenerator 42 (where it undergoes an increase in temperature from T2 to T2′).

(83) B5_Step of Drawing Condensate Water.

(84) Pushed by the high pressure pump 94, the condensate water previously extracted from the air by the trap 93, flows through the pipes 93″ and 94′ (at temperature T1″).

(85) B6_Step of Injecting the Condensate Water into the Air Conduit.

(86) The air, exiting from the regenerator 42, travels through the pipe 42′, passes through the check valve 42a and passes into the pipe 42′″ where, via the injector 97, the condensate water is introduced. As a result of the mixing of the air with the condensate water, the mixture undergoes a decrease in temperature from T2′ to T2″.

(87) B7_Step of Superheating the Circulating Thermal Fluid.

(88) The mixed thermal fluid travels through the pipe 97′, passes through the heater 41 (adjacent to the combustion chamber 40A and provided with the multi-fuel burner 40), where it receives heat-energy and increases in temperature from T2″ to T3.

(89) B8_Step of Expanding the Superheated Thermal Fluid and Producing Useful Work.

(90) When the pistons 7a-7b, by rotating in the annular cylinder in the direction of motion indicated by the arrows, open the inlet openings 15-15″, the superheated thermal fluid flowing through the pipes 41′-41″-41′″ is introduced into the expansion chambers 13′ and 13″, where it is expanded (decreasing in temperature from T3 to T4) and, by making the pistons rotate, produces useful work.

(91) B9_Step of Expulsion and of Recovering Energy from the Exhausted Thermal Fluid.

(92) Following the movement of the pistons 7a-9b and 7b-9c towards each other, the chambers 14′ and 14″ diminish in volume, the exhausted thermal fluid (already expanded in the previous cycle) is expelled from the drive unit 1, passes through the two discharge openings 16′-16″, flows through the pipes 45′-45″-45′″, passes through the regenerator 42 (where it surrenders part of the energy-heat still possessed and undergoes a first decrease in temperature from T4 to T4′).

(93) B10_Conclusion of the Cycle with Further Cooling of the Exhausted Thermal Fluid.

(94) The thermal fluid passes into the pipe 42″ and reaches the cooler 43, from where the cycle can continue and repeat itself in a continuous mode.

(95) B11_Recovery of Energy with the Optimization of the Process of Preheating the Combustion Air.

(96) The combustion air drawn from the environment is pushed by the fan 92 and passes into the cooler 43, where it acquires energy and increases in temperature from Th1 to Th3, thus facilitating the combustion process.

(97) B12_Recovery of Energy with a Reduction in the Temperature of the Combustion Fumes.

(98) Given that the function envisaged for the heat machine is also to provide energy-heat to be destined to auxiliary uses (space heating and/or production of domestic hot water, etc.), before the hot fumes are discharged into the atmosphere (through the conduit 102), all their residual energy is recovered by reducing their temperature as much as possible (it also being possible to recover further energy through their possible condensation). To achieve this purpose, use is made of a specific hydraulic circuit, where the following mode of conveyance is adopted: the incoming thermal fluid (normally water) from the auxiliary uses 103 passes into the pipe 103′ and, pushed by the circulation pump 104, passes into the pipe 104′, reaches the recuperator 101 at the low temperature Tf and then, on passing through it, thanks to the reduction in the temperature of the fumes S from Th7 to Th2, acquires energy-heat and heats up to the higher temperature Tg, so as to be made available, via the pipe 101′, for the auxiliary uses 130, and for the intended purpose.

(99) C. Detailed Description of the Heat Machine 121 Operating According to the Functional Configuration Represented in FIG. 8.

(100) Compared to the Joule-Ericsson cycles on their own and the sole “drive unit”, the novelty introduced with this configuration regards the realization of a “combined” operating cycle, where the thermal fluid is a mixture of air and water (transformed into vapour); this ensures the lubrication of the cylinder (where the pistons slide) and enables a higher unit power to be obtained and an improvement in the overall efficiency.

(101) With reference to FIG. 8, in the position where the pistons are located, the following main steps of the cycle can be identified:

(102) C1_Setting into Motion the Heat Machine 121.

(103) Noting first of all that all control and regulating devices are powered via a specific auxiliary electric line (not represented), the start-up of the heat machine 121 takes place in the following manner: the primary shaft 17 (visible in FIG. 2b) and the whole transmission system that moves the six pistons 7a,7b,7c,9a,9b,9c are set in rotation via the starter motor, thus creating the preliminary condition for start-up of the cycle; the condensate water pump 94 is activated; the fan 92 is activated; the burner 40 is activated by acting on the regulation valve 91 (which controls the injection of fuel F) and the combustion process is started; when the circulating thermal fluid has reached the predetermined minimum operating condition, the drive unit 1 will be capable of producing the work necessary in order to be able to run autonomously.
C2_Start of the Cycle, Starting from the Step of Suctioning the Cooled Thermal Fluid.

(104) The thermal fluid, exiting from the cooler 43 at temperature T1, passes into the pipe 43′, passes through the condensate trap 93 (where the water in the thermal fluid is condensed and separated from the air), passes into the pipe 93′ at temperature T1′, passes through the suctioning opening 15′″ and, following the movement of the two pistons 9c-7c away from each other, is suctioned into the chamber 13′″.

(105) C3_Step of Compression and Recovery of the Suctioned Thermal Fluid.

(106) Following the movement of the two pistons 7c-9a towards each other, the previously suctioned air is compressed in the chamber 14′ (up to the limit, which is normally preset with a minimum ratio of 1:4 and a maximum ratio of 1:20), undergoes an increase in temperature from T1′ to T2, passes through the discharge opening 16′″, the pipe 44′ and the check valve 44a and ends up in the compensation tank 44, where it remains available for immediate use.

(107) C4_Step of Preheating the Compressed Thermal Fluid.

(108) With the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings 15,15″, the air flows out from the tank 44, passes through the pipe 44″ and the check valve 44b, travels through the pipe 44′, and passes into the regenerator 42 (where it undergoes an increase in temperature from T2 to T2′).

(109) C5_Step of Vaporizing/Superheating the Condensate Water.

(110) Pushed by the high pressure pump 94, the condensate water previously extracted from the air by the trap 93, flows through the pipes 93″ and 94′, passes through the evaporator 95, where it is heated/vaporized (changing in state from a liquid to a vapour, with an increase in temperature from T1″ to Ta).

(111) C6_Step of Injecting the Saturated Vapour into the Air Conduit.

(112) The air, exiting from the regenerator 42, travels through the pipe 42′, passes through the check valve 42a and passes into the pipe 42′ where, via the injector 97, the saturated vapour conveyed in the pipe 95′ is introduced. As a result of the mixing of the air with the saturated vapour, the thermal fluid undergoes an increase in mass and decrease in temperature from T2′ to T2″.

(113) C7_Step of Superheating the Circulating Thermal Fluid.

(114) The mixed thermal fluid travels through the pipe 97′, passes through the heater 41 (adjacent to the combustion chamber 40A and provided with the multi-fuel burner 40), where it receives heat-energy and increases in temperature from T2″ to T3.

(115) C8_Step of Expanding the Superheated Thermal Fluid and Producing Useful Work.

(116) When the pistons 7a-7b, by rotating in the annular cylinder in the direction of motion indicated by the arrows, open the inlet openings 15-15″, the superheated thermal fluid flowing through the pipes 41′-41″-41′″ is introduced into the expansion chambers 13′ and 13″, where it is expanded (decreasing in temperature from T3 to T4) and, by making the pistons rotate, produces useful work.

(117) C9_Step of Expulsion and of Recovering Energy from the Exhausted Thermal Fluid.

(118) Following the movement of the pistons 7a-9b and 7b-9c towards each other, the chambers 14′ and 14″ diminish in volume, the exhausted thermal fluid (already expanded in the previous cycle) is expelled from the drive unit 1, passes through the two discharge openings 16′-16″, flows through the pipes 45′-45″-45′″, passes through the regenerator 42 (where it surrenders part of the energy-heat still possessed and undergoes a first decrease in temperature from T4 to T4′), then passes into the pipe 42″, passes through the evaporator 95, where it again surrenders part of the energy-heat possessed and undergoes a second decrease in temperature from T4′ to T4″, enabling the recovery of useful energy, which is schematically represented in the area Q95 in FIG. 9.

(119) C10_Conclusion of the Cycle with Further Cooling of the Exhausted Thermal Fluid.

(120) The thermal fluid passes into the pipe 95″ and reaches the cooler 43, from where the cycle can continue and repeat itself in a continuous mode.

(121) C11_Recovery of Energy with the Optimization of the Process of Preheating the Combustion Air.

(122) The combustion air drawn from the environment is pushed by the fan 92 and passes into the cooler 43, where it acquires energy and increases in temperature from Th1 to Th3, thus facilitating the combustion process.

(123) C12_Recovery of Energy with a Reduction in the Temperature of the Combustion Fumes.

(124) Given that the function envisaged for the heat machine is also to provide energy-heat to be destined to auxiliary uses (space heating and/or production of domestic hot water, etc.), before the hot fumes are discharged into the atmosphere (through the conduit 102), all their residual energy is recovered by reducing their temperature as much as possible (it also being possible to recover further energy through their possible condensation). To achieve this purpose, use is made of a specific hydraulic circuit, where the following mode of conveyance is adopted: the incoming thermal fluid (normally water) from the auxiliary uses 103 passes into the pipe 103′ and, pushed by the circulation pump 104, passes into the pipe 104′, reaches the recuperator 101 at the low temperature Tf and then, on passing through it, thanks to the reduction in the temperature of the fumes S from Th7 to Th2, acquires energy-heat and heats up to the higher temperature Tg, so as to be made available, via the pipe 101′, for the auxiliary uses 130, and for the intended purpose.

(125) D. Detailed Description of the Heat Machine 121 Operating According to the Functional Configuration Represented in FIG. 11.

(126) Compared to the Joule-Ericsson cycles on their own and the sole “drive unit”, the novelty introduced with this configuration regards the realization of a “combined” operating cycle, where the thermal fluid is a mixture of air and water (transformed into superheated vapour); this ensures the lubrication of the cylinder (where the pistons slide) and enables a higher unit power to be obtained and an improvement in the overall efficiency.

(127) With reference to FIG. 11, in the position where the pistons are located, the following main steps of the cycle can be identified:

(128) D1_Setting into Motion the Heat Machine 121.

(129) Noting first of all that all control and regulating devices are powered via a specific auxiliary electric line (not represented), the start-up of the heat machine 121 takes place in the following manner: the primary shaft 17 (visible in FIG. 2b) and the whole transmission system that moves the six pistons 7a,7b,7c,9a,9b,9c are set in rotation via the starter motor, thus creating the preliminary condition for start-up of the cycle; the condensate water pump 94 is activated; the fan 92 is activated; the burner 40 is activated by acting on the regulation valve 91 (which controls the injection of fuel F) and the combustion process is started; when the circulating thermal fluid has reached the predetermined minimum operating condition, the drive unit 1 will be capable of producing the work necessary in order to be able to run autonomously.
D2_Start of the Cycle, Starting from the Step of Suctioning the Cooled Thermal Fluid.

(130) The thermal fluid, exiting from the cooler 43 at temperature T1, passes into the pipe 43′, passes through the condensate trap 93 (where the water in the thermal fluid is condensed and separated from the air), passes into the pipe 93′ at temperature T1′, passes through the suctioning opening 15′″ and, following the movement of the two pistons 9c-7c away from each other, is suctioned into the chamber 13′″.

(131) D3_Step of Compression and Recovery of the Suctioned Thermal Fluid.

(132) Following the movement of the two pistons 7c-9a towards each other, the previously suctioned air is compressed in the chamber 14′ (up to the limit, which is normally preset with a minimum ratio of 1:4 and a maximum ratio of 1:20), undergoes an increase in temperature from T1′ to T2, passes through the discharge opening 16′″, the pipe 44′ and the check valve 44a and ends up in the compensation tank 44, where it remains available for immediate use.

(133) D4_Step of Preheating the Compressed Thermal Fluid.

(134) With the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings 15′,15″, the air flows out from the tank 44, passes through the pipe 44″ and the check valve 44b, travels through the pipe 44′, and passes into the regenerator 42 (where it undergoes an increase in temperature from T2 to T2′).

(135) D5_Step of Vaporizing/Superheating the Condensate Water.

(136) Pushed by the high pressure pump 94, the condensate water previously extracted from the air by the trap 93, flows through the pipes 93″ and 94′, passes through the evaporator 95, where it is heated/vaporized (changing in state from a liquid to a vapour, with an increase in temperature from T1″ to Ta), travels through the pipe 95′, passes through the superheater 96 (where acquires further energy and increases in temperature from Ta to Tb).

(137) D6_Step of Injecting the Superheated Vapour into the Air Conduit.

(138) The air, exiting from the regenerator 42, travels through the pipe 42′, passes through the check valve 42a and passes into the pipe 42′ where, via the injector 97, the superheated vapour conveyed in the pipe 96′ is introduced. As a result of the mixing of the air with the superheated vapour, the thermal fluid undergoes an increase in energy and increases in temperature from T2′ to T2″, enabling the recovery of useful energy, which is schematically represented in the area Q96 in FIG. 10.

(139) D7_Step of Superheating the Circulating Thermal Fluid.

(140) The mixed thermal fluid travels through the pipe 97′, passes through the heater 41 (adjacent to the combustion chamber 40A and provided with the multi-fuel burner 40), where it receives heat-energy and increases in temperature from T2″ to T3.

(141) D8_Step of Expanding the Superheated Thermal Fluid and Producing Useful Work.

(142) When the pistons 7a-7b, by rotating in the annular cylinder in the direction of motion indicated by the arrows, open the inlet openings 15′-15″, the superheated thermal fluid flowing through the pipes 41′-41″-41′″ is introduced into the expansion chambers 13′ and 13″, where it is expanded (decreasing in temperature from T3 to T4) and, by making the pistons rotate, produces useful work.

(143) D9_Step of Expulsion and of Recovering Energy from the Exhausted Thermal Fluid.

(144) Following the movement of the pistons 7a-9b and 7b-9c towards each other, the chambers 14′ and 14″ diminish in volume, the exhausted thermal fluid (already expanded in the previous cycle) is expelled from the drive unit 1, passes through the two discharge openings 16′-16″, flows through the pipes 45′-45″-45′″, passes through the regenerator 42 (where it surrenders part of the energy-heat still possessed and undergoes a first decrease in temperature from T4 to T4′), then passes into the pipe 42″, passes through the evaporator 95, where it again surrenders part of the energy-heat possessed and undergoes a second decrease in temperature from T4′ to T4″, enabling the recovery of useful energy, which is schematically represented in the area Q95 in FIG. 10.

(145) D10_Conclusion of the Cycle with Further Cooling of the Exhausted Thermal Fluid.

(146) The thermal fluid passes into the pipe 95″ and reaches the cooler 43, from where the cycle can continue and repeat itself in a continuous mode.

(147) D11_Recovery of Energy with the Optimization of the Process of Preheating the Combustion Air.

(148) The combustion air drawn from the environment is pushed by the fan 92 and passes into the cooler 43, where it acquires energy and increases in temperature from Th1 to Th3, thus facilitating the combustion process.

(149) D12_Recovery of Energy with a Reduction in the Temperature of the Combustion Fumes.

(150) Given that the function envisaged for the heat machine is also to provide energy-heat to be destined to auxiliary uses (space heating and/or production of domestic hot water, etc.), before the hot fumes are discharged into the atmosphere (through the conduit 102), they are first made to pass through the superheater 96 (where their temperature is reduced from Th7 to Th6) and then all their residual energy is recovered by reducing their temperature as much as possible (it also being possible to recover further energy through their possible condensation). To achieve this purpose, use is made of a specific hydraulic circuit, where the following mode of conveyance is adopted: the incoming thermal fluid (normally water) from the auxiliary uses 103 passes into the pipe 103′ and, pushed by the circulation pump 104, passes into the pipe 104′, reaches the recuperator 101 at the low temperature Tf and then, on passing through it, thanks to the reduction in the temperature of the fumes S from Th6 to Th2, acquires energy-heat and heats up to the higher temperature Tg, so as to be made available, via the pipe 101′, for the auxiliary uses 130, and for the intended purpose.

(151) E. Detailed Description of the Heat Machine 121 Operating According to the Most Complete Functional Configuration, Represented in FIG. 12.

(152) Compared to the Joule-Ericsson cycles on their own and the sole “drive unit”, the novelty introduced with this configuration regards the realization of a “combined” operating cycle, where the thermal fluid is a mixture of air and water (transformed into superheated vapour); this ensures the lubrication of the cylinder (where the pistons slide) and enables a higher unit power to be obtained and a considerable improvement in the overall efficiency.

(153) With reference to FIG. 12, in the position where the pistons are located, the following main steps of the cycle can be identified:

(154) E1_Setting into Motion the Heat Machine 121.

(155) Noting first of all that all control and regulating devices are powered via a specific auxiliary electric line (not represented), the start-up of the heat machine 121 takes place in the following manner: the primary shaft 17 (visible in FIG. 2b) and the whole transmission system that moves the six pistons 7a,7b,7c,9a,9b,9c are set in rotation via the starter motor, thus creating the preliminary condition for start-up of the cycle; the condensate water pump 94 is activated; the water pump 99 is electrically powered up; the fan 92 is activated; the burner 40 is activated by acting on the regulation valve 91 (which controls the injection of fuel F) and the combustion process is started; when the circulating thermal fluid has reached the predetermined minimum operating condition, the drive unit 1 will be capable of producing the work necessary in order to be able to run autonomously.
E2_Start of the Cycle, Starting from the Step of Suctioning the Cooled Thermal Fluid.

(156) The thermal fluid, exiting from the cooler 43 (at temperature T1), passes into the pipe 43′, passes through the condensate trap 93 (where the water in the thermal fluid is condensed and separated from the air), passes into the pipe 93′ at temperature T1′, passes through the suctioning opening 15′″ and, following the movement of the two pistons 9c-7c away from each other, is suctioned into the chamber 13′″.

(157) E3_Step of Compression and Recovery of the Suctioned Thermal Fluid.

(158) Following the movement of the two pistons 7c-9a towards each other, the previously suctioned air is compressed in the chamber 14′ (up to the limit, which is normally preset with a minimum ratio of 1:4 and a maximum ratio of 1:20), undergoes an increase in temperature from T1′ to T2, passes through the discharge opening 16′″, the pipe 44′ and the check valve 44a and ends up in the compensation tank 44, where it remains available for immediate use.

(159) E4_Step of Preheating the Compressed Thermal Fluid.

(160) With the intermittency determined by the rotation of the pistons and the resulting opening/closing of the inlet openings 15,15″, the air flows out from the tank 44, passes through the pipe 44″ and the check valve 44b, travels through the pipe 44′, and passes into the regenerator 42 (where it undergoes an increase in temperature from T2 to T2′).

(161) E5_Step of Vaporizing/Superheating the Condensate Water.

(162) Pushed by the high pressure pump 94, the condensate water previously extracted from the air by the trap 93, flows through the pipes 93″ and 94′ at temperature T1“, passes through the evaporator 95, where it is heated/vaporized (changing in state from a liquid to a vapour, with an increase in temperature from T1” to Ta), travels through the pipe 95″, passes through the superheater 96 (where it acquires further energy and undergoes an increase in temperature from Ta to Tb).

(163) E6_Step of Injection of the Superheated Vapour in the Air Conduit.

(164) The air, exiting from the regenerator 42, travels through the pipe 42′, passes through the check valve 42a and passes into the pipe 42′ where, via the injector 97, the superheated vapour conveyed in the pipe 96′ is introduced. As a result of the mixing of the air with the superheated vapour, the thermal fluid undergoes an increase in energy and its temperature increases from T2′ to T2″, enabling the recovery of useful energy, which is schematically represented in the area Q96 in FIG. 10.

(165) E7_Step of Superheating the Circulating Thermal Fluid.

(166) The mixed thermal fluid travels through the pipe 97′, passes through the heater 41 (adjacent to the combustion chamber 40A, provided with the multi-fuel burner 40), where it receives heat-energy and increases in temperature from T2″ to T3.

(167) E8_Step of Expanding the Superheated Thermal Fluid and Producing Useful Work.

(168) When the pistons 7a-7b, by rotating in the annular cylinder in the direction of motion indicated by the arrows, open the inlet openings 15-15″, the superheated thermal fluid flowing through the pipes 41′-41″-41′″ is introduced into the expansion chambers 13′ and 13″, where it is expanded (decreasing in temperature from T3 to T4) and, by making the pistons rotate, produces useful work.

(169) E9_Step of Expulsion and of Recovering Energy from the Exhausted Thermal Fluid.

(170) Following the movement of the pistons 7a-9b and 7b-9c towards each other, the chambers 14′ and 14″ diminish in volume, the exhausted thermal fluid (already expanded in the previous cycle) is expelled from the drive unit 1, passes through the two discharge openings 16′-16″, flows through the pipes 45′-45″-45′″, passes through the regenerator 42 (where it surrenders part of the energy-heat still possessed and undergoes a first decrease in temperature from T4 to T4′), then passes into the pipe 42″, passes through the evaporator 95, where it again surrenders part of the energy-heat possessed and undergoes a second decrease in temperature from T4′ to T4″, enabling the recovery of useful energy, which is schematically represented in the area Q95 in FIG. 10.

(171) E10_Conclusion of the Cycle with Further Cooling of the Exhausted Thermal Fluid.

(172) The thermal fluid passes into the pipe 95′ and reaches the cooler 43, from where the cycle can continue and repeat itself in a continuous mode.

(173) E11_Optimized Cooling of the Drive Unit 1, with Recovery of Energy.

(174) The water cooled in the recuperator 98 (at temperature Tc) is constantly maintained in circulation by the pump 99, flows through the pipes 98′-99′, passes through a specific interspace 2R formed in the drive unit 1, (where, by performing a cooling action, it undergoes an increase in temperature from Tc to Td), travels through the pipe 2′, passes through the recuperator 100 (where it acquires heat-energy, increasing in temperature from Td to Te), travels through the pipe 100′ and, finally, arrives at the recuperator 98, where its path ends. The interspace 2R constitutes a cooling unit for the drive unit 1. The pipes 2′, 98′, 99′ and 100′ constitute cooling pipes. The interspace 2R (or cooling unit) of the first recuperator 98, the second recuperator 100, the cooling pump 99 and the cooling pipes together constitute a cooling circuit of the heat machine.

(175) E12_Recovery of Energy with the Optimization of the Process of Preheating the Combustion Air.

(176) The combustion air drawn from the environment at temperature Th1 is pushed by the fan 92 and passes into the cooler 43 (where it acquires energy and increases in temperature to Th3), passes into the recuperator 98 (where it acquires further energy and increases in temperature to Th5).

(177) The preheated air is mixed in the burner 40 with the fuel conveyed through the regulation valve 91 and is introduced into the combustion chamber 40A, where the gas, mixed at a high temperature, can undergo optimal combustion, thus reducing harmful emissions.
E13_Recovery of Energy with a Reduction in the Temperature of the Combustion Fumes.

(178) The hot fumes produced by combustion at temperature Th7 are first cooled to temperature Th6 (passing through the superheater 96), then further cooled to temperature Th4 (passing through the recuperator 100) and then, given that the function envisaged for the heat machine is also to provide energy-heat to be destined to auxiliary uses (space heating and/or production of domestic hot water, etc.), before the hot fumes are discharged into the atmosphere (through the conduit 102), all their residual energy is recovered by reducing their temperature as much as possible (it also being possible to recover further energy through their possible condensation). To achieve this purpose, use is made of a specific hydraulic circuit, where the following mode of conveyance is adopted: the incoming thermal fluid (normally water) from the auxiliary uses 103 passes into the pipe 103′ and, pushed by the circulation pump 104, passes into the pipe 104′, reaches the recuperator 101 at the low temperature Tf and then, on passing through it, thanks to the reduction in the temperature of the fumes from Th4 to Th2, it acquires energy-heat and heats up to the higher temperature Tg, so as to be made available, via the pipe 101′, for the auxiliary uses 130, and for the intended purpose.

(179) The pipes 101′, 103′ and 104′ constitute auxiliary pipes. The auxiliary recuperator 101, the auxiliary pump 104 and the auxiliary pipes together constitute a cooling circuit of the heat machine 121.

(180) The invention thus conceived is susceptible of numerous modifications and variants, all falling within the scope of the inventive concept, and the components mentioned may be replaced by other technically equivalent elements.

(181) The invention achieves important advantages. First of all, the invention enables at least some of the drawbacks of the prior art to be overcome.

(182) Furthermore, the heat machine and the associated method according to the present invention are capable of using a variety of heat sources and of generating mechanical energy (work), as they can be employed in any place and for any use, but preferably for the production of electrical energy.

(183) Furthermore, the heat machine according to the present invention is characterized by a high thermodynamic efficiency and an excellent weight-power ratio.

(184) In addition, the heat machine according to the present invention is characterized by a simple, easy to produce structure.

(185) Furthermore, the heat machine according to the present invention is characterized by a reduced production cost.