Method and apparatus for evaporating organic working media
The present invention provides a device which comprises: a heat exchanger ( 1 ) for transferring heat of a heat-supplying medium to a working medium which differs from said heat-supplying medium, a first supply device designed to provide a flow of the heat-supplying medium at a first temperature from a heat source to the heat exchanger, and a second supply device which is designed to deliver the heat-supplying medium after it has passed through the heat exchanger, and/or a further medium at a second temperature lower than the first temperature, to the flow of the heat-supplying medium at the first temperature.
1. Organic Rankine Cycle apparatus, comprising:
a heat exchanger for transferring heat of a heat-supplying medium to an organic working medium which differs from the heat-supplying medium;
a first supply device adapted to supply a flow of the heat-supplying medium having a first temperature from a heat source to the heat exchanger;
a second supply device adapted to supply at least partially the heat-supplying medium, after the heat-supplying medium has passed through the heat exchanger, and/or a further medium, each of the heat-supplying medium and the further medium having a second temperature that is lower than the first temperature, to the flow of the heat-supplying medium having the first temperature such that the temperature of the heat-supplying medium at the heat exchanger lies below a decomposition temperature of the organic working medium; and
a device adapted to heat or cool the heat-supplying medium, after the heat-supplying medium has passed through the heat exchanger, and/or the further medium to the second temperature before the heat-supplying medium, after passing through the heat exchanger, and/or the further medium is supplied to the flow of the heat-supplying medium supplied from the heat source to the heat exchanger.
2. The Organic Rankine Cycle apparatus according to claim 1 , wherein the first supply device comprises a vacuum device and/or the second supply device comprises a fan and/or a vacuum device.
3. The Organic Rankine Cycle apparatus according to claim 2 , wherein the second supply device is adapted to supply the heat-supplying medium, after passing through the heat exchanger, and/or the further medium to the flow of the heat-supplying medium having the first temperature such that the heat-supplying medium, after passing through the heat exchanger, and/or the further medium is supplied to same distributed over a circumference of the flow.
4. The Organic Rankine Cycle apparatus according to claim 1 , wherein the second supply device is adapted to supply the heat-supplying medium, after passing through the heat exchanger, and/or the further medium to the flow of the heat-supplying medium having the first temperature such that the heat-supplying medium, after passing through the heat exchanger, and/or the further medium is supplied to same distributed over a circumference of the flow.
5. The Organic Rankine Cycle apparatus according to claim 4 , wherein the first supply device comprises a first conduit for conducting the heat-supplying medium having the first temperature, and the second supply device comprises a second conduit for conducting the heat-supplying medium, after passing through the heat exchanger, and/or for conducting the further medium, and wherein the apparatus comprises a mixing piece or a mixing section, which is designed for a fluidic connection of the heat-supplying medium having the first temperature in the first conduit and the heat-supplying medium, after passing through the heat exchanger, and/or the further medium in the second conduit.
6. The Organic Rankine Cycle apparatus according to claim 5 , wherein the mixing piece or mixing section comprises a part of the first conduit with holes formed therein in a shell of same, and a part of the second conduit surrounding the part of the first conduit.
7. The Organic Rankine Cycle apparatus according to claim 1 , which further comprises an expansion machine, a generator, and a device for supplying the working medium evaporated in the heat exchanger to the expansion machine.
8. The Organic Rankine Cycle apparatus according to claim 1 , further comprising an expansion machine and a generator and a condenser, wherein the latter is adapted to condense the working medium, after passing through the expansion machine, from a vaporous state into a liquid state.
9. Steam power plant comprising the apparatus according to claim 1 .
10. The Organic Rankine Cycle apparatus according to claim 1 , wherein a heat-transfer surface of the heat exchanger for transferring heat of the heat-supplying medium to the organic working medium is formed large enough to accommodate for an increased mass flow through the heat exchanger, due to at least partially supplying the heat-supplying medium, after passing through the heat exchanger, and/or supplying the further medium, without increased back pressure of the heat-supplying medium.
11. Apparatus, comprising:
a heat exchanger for transferring heat of a heat-supplying medium to an organic working medium that differs from the heat-supplying medium;
a first supply device adapted to supply a flow of the heat-supplying medium having a first temperature from a heat source to the heat exchanger;
a second supply device adapted to supply a further medium having a second temperature that is lower than the first temperature to the flow of the heat-supplying medium having the first temperature such that the temperature of the heat-supplying medium at the heat exchanger lies below a decomposition temperature of the organic working medium, and
wherein the heat-supplying medium is or contains flue gas.
12. Method for evaporating an organic working medium in an Organic Rankine Cycle thermal power plant, comprising the steps of:
supplying the organic working medium in a liquid state to a heat exchanger,
supplying a heat-supplying medium having a first temperature, the heat-supplying medium differing from the organic working medium, from a heat source to the heat exchanger,
recirculating at least a portion of the heat-supplying medium, after the heat-supplying medium has passed through the heat exchanger, having a second temperature that is lower than the first temperature, and/or supplying a further medium having the second temperature which is lower than the first temperature into the flow of the heat-supplying medium supplied from the heat source to the heat exchanger such that the temperature of the heat-supplying medium at the heat exchanger lies below a decomposition temperature of the organic working medium, and
cooling or heating the heat-supplying medium, after the heat-supplying medium has passed through the heat exchanger, and/or the further medium to the second temperature before the heat-supplying medium, after being passed through the heat exchanger, and/or the further medium is supplied to the flow of the heat-supplying medium supplied from the heat source to the heat exchanger.
13. The method according to claim 12 , wherein the step of recirculating the at least a portion of the heat-supplying medium, after passing through the heat exchanger, and/or of supplying the further medium is accomplished by means of a fan and/or a vacuum device.
14. The method according to claim 13 , wherein the at least a portion of the heat-supplying medium, after passing through the evaporator, and/or the further medium is mixed with the flow of the heat-supplying medium having the first temperature and supplied from the heat source to the heat exchanger in a manner distributed over a circumference of the flow.
15. The method according to claim 12 , wherein the at least a portion of the heat-supplying medium, after passing through the heat exchanger, and/or the further medium is mixed with the flow of the heat-supplying medium having the first temperature and supplied from the heat source to the heat exchanger in a manner distributed over a circumference of this flow.
16. The method according to claim 12 , wherein the heat-supplying medium is or includes flue gas.
17. The method according to claim 12 , further comprising:
supplying the organic working medium evaporated in the heat exchanger to an expansion machine for expanding the evaporated organic working medium;
supplying the expanded, evaporated organic working medium to a condenser for liquefying the expanded, evaporated organic working medium; and
supplying the liquefied organic working medium to the evaporator.
18. The method according to claim 12 , wherein 10 to 60% of the heat-supplying medium, after passing through the heat exchanger, are recirculated.
19. Method for evaporating an organic working medium in an Organic Rankine Cycle thermal power plant, comprising the steps of:
supplying the organic working medium in a liquid state to a heat exchanger;
supplying a heat-supplying medium having a first temperature, the heat-supplying medium differing from the organic working medium, from a heat source to the heat exchanger,
supplying a further medium having a second temperature that is lower than the first temperature to the flow of the heat-supplying medium supplied from the heat source to the heat exchanger such that the temperature of the heat-supplying medium at the heat exchanger lies below a decomposition temperature of the organic working medium, and
wherein the heat-supplying medium is or contains flue gas.