Renewable power and/or water generator

1 . A power and/or water generator, comprising:

an absorption heat transformer (AHT) containing a binary liquid-vapour mixture and including:

a low pressure (LP) evaporator, and

a vapour absorption binary (VAB) reactor;

the AHT configured to extract thermal energy from an external heat source and function as a heat pump creating a temperature gradient used to drive an Organic Rankine Cycle (ORC) that employs a high pressure (HP) vapour expansion drive mechanism for generation of power;

the VAB reactor including:

an absorption section, and

a distillation section;

with an absorber heat exchanger (H/E) located inside the absorption section to draw heat from the absorption section;

the distillation section provided by a rotating centrifugal unit for increasing a volatile component concentration of the binary liquid-vapour mixture in a distillate outlet liquid to be used both in:

(a) the LP evaporator, and

(b) a working vapour supply assembly for the vapour expansion drive mechanism;

the LP evaporator arranged

for heat extraction from the external heat source,

to receive distillate outlet liquid from the distillation section for conversion to LP evaporator vapour, and

to supply the LP evaporator vapour through a first return line from the LP evaporator to the absorption section;

in which a heat carrier fluid medium is connected through a branch to the LP evaporator with a fluid medium chilling flow path on a first side of the LP evaporator that is isolated from and in thermal communication with a second side of the LP evaporator and a low pressure supply line for distillate outlet liquid from the distillation section connected to the second side of the LP evaporator for evaporation of the distillate outlet liquid and thermal energy extraction from the fluid medium in the fluid medium chilling flow path;

the absorption section generating heat in a vapour absorption process inside the absorption section;

the working vapour supply assembly incorporating the absorber H/E and arranged to use heat from the absorber H/E inside the absorption section for conversion of distillate outlet liquid from the distillation section to heated high pressure (HP) working vapour;

the HP working vapour supplied to the vapour expansion drive mechanism which is coupled to a generator; and

LP exhaust vapour from the expansion drive mechanism connected through a second return line to the absorption section of the VAB reactor.

2 . The generator as claimed in claim 1 wherein the absorption section and the distillation section are provided as parts of an integral component in the rotating centrifugal unit with the absorption section provided adjacent a periphery of the rotating centrifugal unit and the absorber H/E provided as a conduit that runs along the absorber section.

3 . The generator as claimed in claim 2 wherein the conduit of the absorber H/E is a coil that runs around the distillation section within the absorber section.

4 . The generator as claimed in claim 2 wherein the rotating centrifugal unit provides a rotating drive for an integrated pump that displaces the distillate outlet liquid, and the pump is a pitot-type pump with multiple pitot pipes provided as a multi-stage cascade arrangement.

5 . The generator as claimed in claim 1 wherein the working vapour supply assembly comprises a high pressure (HP) supply line for distillate outlet liquid from the distillation section that is pumped through the absorber H/E to provide the HP working vapour supply to the vapour expansion drive mechanism.

6 . The generator as claimed in claim 5 further comprising an HP working vapour supply line extending from the absorber H/E to the vapour expansion drive mechanism includes a by-pass return with a condenser heat exchanger (H/E) and a connection into the second return line to the absorber section of the VAB reactor, and for the by-pass return to include a pressure reducing valve.

7 . The generator as claimed in claim 1 wherein the working vapour supply assembly comprises:

a supply line for a heat carrier fluid that is pumped through the absorber H/E where it is heated and delivered as heated absorber output heat carrier fluid to a first side of an HP evaporator for passage through a flow path that is isolated from and in thermal communication with a second side of the HP evaporator, and

a high pressure supply line for distillate outlet liquid from the distillation section connected to a second side of the HP evaporator for thermal energy extraction from the heat carrier fluid in the flow path and evaporation of the distillate outlet liquid on the second side of the HP evaporator,

wherein the HP working vapour is generated in the HP evaporator to provide HP vapour supply to the vapour expansion drive mechanism.

8 . The generator as claimed in claim 7 wherein the absorber output heat carrier fluid flow path includes a by-pass away from the HP evaporator to provide a decrease in hot mass flow through the HP evaporator.

9 . The generator as claimed in claim 1 wherein the fluid medium chilling flow path of the LP evaporator is connected to an air-chilling heat exchanger (H/E) for extraction of atmospheric water from air.

10 . The generator as claimed in claim 9 wherein the heat carrier fluid medium is a high density liquid heat carrier in the form of environmental water that provides the external heat source.

11 . The generator as claimed in claim 1 wherein the absorption section is provided as an absorber unit separate from and in fluid communication with the rotating centrifugal unit, the absorber H/E is a conduit that runs within the absorber unit and for:

a hot outlet from a heated periphery of the rotating centrifugal unit to be connected and pumped into the absorber unit; and

an outlet from the absorber unit to be connected to the rotating centrifugal unit, a cold outlet from a low temperature centre of the rotating centrifugal unit to be connected to:

(a) an LP evaporator pump which feeds the LP evaporator, and

(b) an HP absorber turbine pump which feeds the absorber H/E in the absorber unit,

an outlet from the LP evaporator to be connected to the absorber unit, and

an outlet from the absorber H/E to be connected to the vapour expansion drive mechanism.

12 . The generator as claimed in claim 11 further comprising a booster pump is provided between the hot outlet from the rotating centrifugal unit and the absorber unit.

13 . The generator as claimed in claim 12 wherein the rotating centrifugal unit includes a hydraulic powered rotating packed bed and rotor with hydraulic turbine blades driven by radial inflow from the first pump via the absorber unit.

14 . The generator as claimed in claim 13 wherein heated, low volatile component concentration binary liquid is pumped out of the rotating centrifugal unit by the hydraulic turbine blades to feed the absorber unit via the first pump and for the booster pump.

15 . The generator as claimed in claim 14 wherein pressure added by the booster pump serves to sub-cool the low volatile component concentration binary liquid providing higher volatile component concentration binary liquid after vapor absorption in the absorber unit.

16 . The generator as claimed in claim 1 wherein the distillate outlet liquid from the rotating centrifugal unit is supplied through an LP evaporator pump to the LP evaporator and through an HP absorber turbine pump to the absorber H/E in the absorber unit.

17 . A power and/or water generator, comprising:

an absorption heat transformer (AHT) containing a binary liquid-vapour mixture and including:

a low pressure (LP) evaporator, and

a vapour absorption binary (VAB) reactor;

the AHT configured to extract thermal energy from an external heat source and function as a heat pump creating a temperature gradient used to drive an Organic Rankine Cycle (ORC) that employs a high pressure (HP) vapour expansion drive mechanism for generation of power;

the VAB reactor including:

n absorption section, and

a distillation section;

with an absorber heat exchanger (H/E) located inside the absorption section to draw heat from the absorption section;

the distillation section provided by a rotating centrifugal unit for increasing a volatile component concentration of the binary liquid-vapour mixture in a distillate outlet liquid to be used both in:

(a) the LP evaporator, and

(b) a working vapour supply assembly for the vapour expansion drive mechanism;

the LP evaporator arranged

for heat extraction from the external heat source,

to receive distillate outlet liquid from the distillation section for conversion to LP evaporator vapour, and

to supply the LP evaporator vapour through a first return line from the LP evaporator to the absorption section;

in which ambient air provides the external heat source and is directed over a first side of the LP evaporator that is isolated from and in thermal communication with a second side of the LP evaporator with a low pressure supply line for distillate outlet liquid from the distillation section connected to the second side of the LP evaporator for evaporation of the distillate outlet liquid and thermal energy extraction from the ambient air providing an air-chilling heat exchanger (H/E) for extraction of atmospheric water from the ambient air;

the absorption section generating heat in a vapour absorption process inside the absorption section;

the working vapour supply assembly incorporating the absorber H/E and arranged to use heat from the absorber H/E inside the absorption section for conversion of distillate outlet liquid from the distillation section to heated high pressure (HP) working vapour;

the HP working vapour supplied to the vapour expansion drive mechanism which is coupled to a generator; and

LP exhaust vapour from the expansion drive mechanism connected through a second return line to the absorption section of the VAB reactor.