Natural gas liquid fractionation plant waste heat conversion to power using dual turbines organic Rankine cycle
Certain aspects of a natural gas liquid fractionation plant waste heat conversion to power using dual turbines Organic Rankine Cycle can be implemented as a first heating fluid circuit thermally coupled to first multiple heat sources of a natural gas liquid (NGL) fractionation plant, a second heating fluid circuit thermally coupled to second multiple heat sources of the NGL fractionation plant, and two power generation systems, each including an organic Rankine cycle (ORC). A control system actuates a first set of control valves to selectively thermally couple the first heating fluid circuit to at least a portion of the first multiple heat sources of the NGL fractionation plant, and to actuate a second set of control valves to selectively thermally couple the second heating fluid circuit to at least a portion of the second multiple heat sources of the NGL fractionation plant.
1. A system, comprising:
a first heating fluid circuit thermally coupled to a first plurality of heat sources of a natural gas liquid (NGL) fractionation plant, the first plurality of heat sources comprising:
a first portion of first sub-units of the NGL fractionation plant that comprises an ethane system,
a second plurality of first sub-units of the NGL fractionation plant that comprises a propane system,
a third portion of first sub-units of the NGL fractionation plant that comprises a butane system,
a fourth portion of first sub-units of the NGL fractionation plant that comprises a natural gasoline system, and
a fifth portion of first sub-units of the NGL fractionation plant that comprises a solvent regeneration system;
a second heating fluid circuit thermally coupled to a second plurality of heat sources of the NGL fractionation plant, the second plurality of heat sources comprising:
a first portion of second sub-units of the NGL fractionation plant that comprises the ethane system,
a second plurality of second sub-units of the NGL fractionation plant that comprises the propane system,
a third portion of second sub-units of the NGL fractionation plant that comprises the butane system,
a fourth portion of second sub-units of the NGL fractionation plant that comprises a pentane system, and
a fifth portion of second sub-units of the NGL fractionation plant that comprises the natural gasoline system;
a first power generation system that comprises a first organic Rankine cycle (ORC), the first ORC comprising (i) a first portion of a working fluid that is thermally coupled to the first heating fluid circuit in an evaporator of the first ORC to heat the first portion of the working fluid, and (ii) a first expander configured to generate electrical power from the heated first portion of the working fluid;
a second power generation system that comprises a second organic Rankine cycle (ORC), the second ORC comprising (i) a second portion of the working fluid that is thermally coupled to the first and second heating fluid circuits in an evaporator of the second ORC to heat the second portion of the working fluid, and (ii) a second expander configured to generate electrical power from the heated second portion of the working fluid; and
a flow control system that comprises a first set of control valves to selectively thermally couple a heating fluid of the first heating fluid circuit to at least a portion of the first plurality of heat sources of the NGL fractionation plant, the control system further comprising a second set of control valves to selectively thermally couple a heating fluid of the second heating fluid circuit to at least a portion of the second plurality of heat sources of the NGL fractionation plant.
2. The system of claim 1 , further comprising a heating fluid tank that is fluidly coupled to the evaporators of the first and second ORCs.
3. The system of claim 1 , wherein the system further comprises conduits containing the working fluid and the working fluid comprises isobutane.
4. The system of claim 3 , the first and second fluid heating circuits further comprise pipes containing water or oil.
5. The system of claim 4 , further comprising:
a condenser fluidly coupled to the first and second expanders and to a condenser fluid source to cool the working fluid;
a first pump to circulate the first portion of the working fluid through the first ORC; and
a second pump to circulate the second portion of the working fluid through the second ORC.
6. The system of claim 1 , wherein the first and second fluid heating circuits further comprise pipes containing water or oil.
7. The system of claim 1 , further comprising:
a condenser fluidly coupled to the first and second expanders and to a condenser fluid source to cool the working fluid;
a first pump to circulate the first portion of the working fluid through the first ORC; and
a second pump to circulate the second portion of the working fluid through the second ORC.
8. The system of claim 1 , wherein the first portion of first sub-units of the NGL fractionation plant comprises at least one ethane system heat source, comprising:
a first ethane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ethane dryer.
9. The system of claim 1 , wherein the second portion of first sub-units of the NGL fractionation plant comprises at least three propane system heat sources, comprising:
a first propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane dehydrator;
a second propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane vapor recovery compressor stream;
a third propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane main compressor stream.
10. The system of claim 1 , wherein the third portion of first sub-units of the NGL fractionation plant comprises at least two butane system heat sources, comprising:
a first butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a butane dehydrator; and
a second butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a debutanizer bottoms.
11. The system of claim 1 , wherein the fourth portion of first sub-units of the NGL fractionation plant comprises at least two natural gasoline system heat sources, comprising:
a first natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a natural gasoline decolorizer overhead stream; and
a second natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a Reid vapor pressure control column overhead stream.
12. The system of claim 1 , wherein the fifth portion of first sub-units of the NGL fractionation plant comprises at least two solvent regeneration system heat sources, comprising:
a first solvent regeneration system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ADIP regeneration section overhead stream; and
a second solvent regeneration system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ADIP regeneration section bottoms.
13. The system of claim 1 , wherein the first portion of second sub-units of the NGL fractionation plant comprises at least one ethane system heat source, comprising:
a first ethane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a deethanizer refrigeration compressor.
14. The system of claim 1 , wherein the second portion of second sub-units of the NGL fractionation plant comprises at least two propane system heat sources, comprising:
a first propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a depropanizer overhead stream;
a second propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane refrigeration compressor stream.
15. The system of claim 1 , wherein the third portion of second sub-units of the NGL fractionation plant comprises at least two butane system heat sources, comprising:
a first butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a debutanizer overhead stream; and
a second butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a butane refrigeration compressor stream.
16. The system of claim 1 , wherein the fourth portion of second sub-units of the NGL fractionation plant comprises at least one pentane system heat source, comprising:
a first pentane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a depentanizer overhead stream.
17. The system of claim 1 , wherein the fifth portion of second sub-units of the NGL fractionation plant comprises at least one natural gasoline system heat source, comprising:
a first natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a natural gasoline decolorizing section pre-flash drum overhead stream.
18. A method of recovering heat energy generated by a natural gas liquid (NGL) fractionation plant, the method comprising:
circulating a first heating fluid through a first heating fluid circuit thermally coupled to a first plurality of heat sources of a natural gas liquid (NGL) fractionation plant, the first plurality of heat sources comprising:
a first portion of first sub-units of the NGL fractionation plant that comprises an ethane system,
a second plurality of first sub-units of the NGL fractionation plant that comprises a propane system,
a third portion of first sub-units of the NGL fractionation plant that comprises a butane system,
a fourth portion of first sub-units of the NGL fractionation plant that comprises a natural gasoline system, and
a fifth portion of first sub-units of the NGL fractionation plant that comprises a solvent regeneration system;
circulating a second heating fluid through a second heating fluid circuit thermally coupled to a second plurality of heat sources of the NGL fractionation plant, the second plurality of heat sources comprising:
a first portion of second sub-units of the NGL fractionation plant that comprises the ethane system,
a second plurality of second sub-units of the NGL fractionation plant that comprises the propane system,
a third portion of second sub-units of the NGL fractionation plant that comprises the butane system,
a fourth portion of second sub-units of the NGL fractionation plant that comprises a pentane system, and
a fifth portion of second sub-units of the NGL fractionation plant that comprises the natural gasoline system;
generating electrical power through a first power generation system that comprises a first organic Rankine cycle (ORC), the first ORC comprising (i) a first portion of a working fluid that is thermally coupled to the first heating fluid circuit in an evaporator of the first ORC to heat the first portion of the working fluid, and (ii) a first expander configured to generate electrical power from the heated first portion of the working fluid;
generating electrical power through a second power generation system that comprises a second organic Rankine cycle (ORC), the second ORC comprising (i) a second portion of the working fluid that is thermally coupled to the first and second heating fluid circuits in an evaporator of the second ORC to heat the second portion of the working fluid, and (ii) a second expander configured to generate electrical power from the heated second portion of the working fluid;
actuating, with a flow control system, a first set of control valves to selectively thermally couple a heating fluid of the first heating fluid circuit to at least a portion of the first plurality of heat sources of the NGL fractionation plant; and
actuating, with the flow control system, a second set of control valves to selectively thermally couple a heating fluid of the second heating fluid circuit to at least a portion of the second plurality of heat sources of the NGL fractionation plant.
19. The method of claim 18 , further comprising circulating the first and second heating fluids to a heating fluid tank from the evaporators of the first and second ORCs.
20. The method of claim 19 , wherein the working fluid comprises isobutane.
21. The method of claim 20 , wherein each of the first and second heating fluids comprises water or oil.
22. The method of claim 21 , further comprising:
a condenser fluidly coupled to the first and second expanders and to a condenser fluid source to cool the working fluid;
a first pump to circulate the first portion of the working fluid through the first ORC; and
a second pump to circulate the second portion of the working fluid through the second ORC.
23. The method of claim 18 , wherein the working fluid comprises isobutane.
24. The method of claim 18 , wherein each of the first and second heating fluids comprises water or oil.
25. The method of claim 18 , further comprising:
a condenser fluidly coupled to the first and second expanders and to a condenser fluid source to cool the working fluid;
a first pump to circulate the first portion of the working fluid through the first ORC; and
a second pump to circulate the second portion of the working fluid through the second ORC.
26. The method of claim 18 , wherein the first portion of first sub-units of the NGL fractionation plant comprises at least one ethane system heat source, comprising:
a first ethane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ethane dryer.
27. The method of claim 18 , wherein the second portion of first sub-units of the NGL fractionation plant comprises at least three propane system heat sources, comprising:
a first propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane dehydrator;
a second propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane vapor recovery compressor stream;
a third propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane main compressor stream.
28. The method of claim 18 , wherein the third portion of first sub-units of the NGL fractionation plant comprises at least two butane system heat sources, comprising:
a first butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a butane dehydrator; and
a second butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a debutanizer bottoms.
29. The method of claim 18 , wherein the fourth portion of first sub-units of the NGL fractionation plant comprises at least two natural gasoline system heat sources, comprising:
a first natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a natural gasoline decolorizer overhead stream; and
a second natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a Reid vapor pressure control column overhead stream.
30. The method of claim 18 , wherein the fifth portion of first sub-units of the NGL fractionation plant comprises at least two solvent regeneration system heat sources, comprising:
a first solvent regeneration system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ADIP regeneration section overhead stream; and
a second solvent regeneration system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of an ADIP regeneration section bottoms.
31. The method of claim 18 , wherein the first portion of second sub-units of the NGL fractionation plant comprises at least one ethane system heat source, comprising:
a first ethane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a deethanizer refrigeration compressor.
32. The method of claim 18 , wherein the second portion of second sub-units of the NGL fractionation plant comprises at least two propane system heat sources, comprising:
a first propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a depropanizer overhead stream;
a second propane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a propane refrigeration compressor stream.
33. The method of claim 18 , wherein the third portion of second sub-units of the NGL fractionation plant comprises at least two butane system heat sources, comprising:
a first butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a debutanizer overhead stream; and
a second butane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a butane refrigeration compressor stream.
34. The method of claim 18 , wherein the fourth portion of second sub-units of the NGL fractionation plant comprises at least one pentane system heat source, comprising:
a first pentane system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a depentanizer overhead stream.
35. The method of claim 18 , wherein the fifth portion of second sub-units of the NGL fractionation plant comprises at least one natural gasoline system heat source, comprising:
a first natural gasoline system heat source that comprises a heat exchanger that is thermally coupled to an outlet stream of a natural gasoline decolorizing section pre-flash drum overhead stream.