Air source heat pump system and method of use for industrial steam generation
A system for generating steam for industrial heat. The system may include a plurality of heat pump cycles in thermal communication with each other and in thermal communication with a steam generation cycle. The plurality of heat pump cycles may include first and second heat pump cycles. The first heat pump circulates a first a working fluid and includes a first heat exchanger. The second heat pump cycle circulates a second working fluid and includes a second heat exchanger. The first heat exchanger transfers heat from the first to the second working fluid. The second heat exchanger transfers heat to a third working fluid in the steam generation cycle.
1. A method for generating steam, said method comprising:
(a) providing two or more heat pump cycles comprising a bottom heat pump cycle and a top heat pump cycle coupled via at least one intermediate heat exchanger;
(b) circulating a first working fluid in said bottom heat pump cycle to absorb heat from an ambient air source;
(c) using a first centrifugal compressor stage in said bottom heat pump cycle and a second centrifugal compressor stage in said bottom heat pump cycle in series to increase a pressure of said first working fluid;
(d) circulating a second working fluid in said at least one intermediate heat exchanger to transfer said heat from said first working fluid to said second working fluid;
(e) circulating said first working fluid in a first economizer, thereby
splitting said first working fluid into a first primary fluid stream and a first secondary fluid stream;
expanding said first secondary fluid stream of said first working fluid to a lower pressure via a first expansion valve in said bottom heat pump cycle, and absorbing heat in said first secondary fluid stream of said first working fluid; and
rejecting heat from said first primary fluid stream of said first working fluid to said first secondary fluid stream of said first working fluid;
(f) cooling said second working fluid in a first location and heating said second working fluid in a second location by rejecting heat from said first location and absorbing heat in said second location in said top heat pump cycle;
(g) using a first centrifugal compressor stage in said top heat pump cycle and a second centrifugal compressor stage in said top heat pump cycle in series to increase a pressure of said second working fluid and to compress said second working fluid;
(h) circulating said second working fluid in said top heat pump cycle to transfer said heat from said second working fluid to a feed stream comprising water, thereby generating said steam at a target steam saturation temperature of at least 120 degrees Celsius, wherein said transfer of said heat from said second working fluid to said feed stream occurs in a steam generator, and wherein a pressure of said feed stream in said steam generator is greater than or equal to a pressure of said steam at said target steam saturation temperature; and
(i) circulating said second working fluid in a second economizer, thereby
splitting said second working fluid into a second primary fluid stream and a second secondary fluid stream;
expanding said second secondary fluid stream of said second working fluid to a lower pressure via a first expansion valve in said top heat pump cycle, and absorbing heat in said second secondary fluid stream of said second working fluid;
rejecting heat from said second primary fluid stream of said second working fluid to said second secondary fluid stream of said second working fluid; and
directing said second secondary fluid stream of said second working fluid to an inlet of said second centrifugal compressor stage in said top heat pump cycle.
2. The method of claim 1 , wherein step (e) further comprises directing said first secondary fluid stream of said first working fluid to an inlet of said second compressor stage in said bottom heat pump cycle.
3. The method of claim 1 , wherein a coefficient of performance (COP) of said two or more heat pump cycles is greater than two.
4. The method of claim 1 , wherein an efficiency of at least one of said first centrifugal compressor stage in said bottom heat pump cycle or said first centrifugal compressor stage in said top heat pump cycle is greater than or equal to 80%.
5. The method of claim 1 , wherein a specific speed (N S ) versus a specific diameter (D S ) of at least one of said first centrifugal compressor stage in said bottom heat pump cycle, said second centrifugal compressor stage in said bottom heat pump cycle, said first centrifugal compressor stage in said top heat pump cycle, or said second centrifugal compressor stage in said top heat pump cycle results in an efficiency greater than or equal to 80%.
6. The method of claim 1 , wherein said target steam saturation temperature of said steam is between 120 degrees Celsius and 150 degrees Celsius.
7. The method of claim 1 , wherein said target steam saturation temperature of said steam is greater than or equal to 150 degrees Celsius.
8. The method of claim 1 , wherein a temperature of said ambient air source is 20 degrees Celsius.
9. The method of claim 1 , wherein a temperature difference or lift between said ambient air source and said steam is 100 degrees Celsius to 150 degrees Celsius.
10. The method of claim 1 , wherein (c) increases a temperature of said first working fluid by at least 30 degrees Celsius.
11. The method of claim 1 , wherein (g) increases a temperature of said second working fluid by at least 30 degrees Celsius.
12. The method of claim 1 , wherein compressing said second working fluid using said second centrifugal compressor stage in said top heat pump cycle increases a temperature of said second working fluid by at least 40 degrees Celsius.
13. The method of claim 1 , wherein (i) at least one of said first centrifugal compressor stage in said bottom heat pump cycle or said first centrifugal compressor stage in said top heat pump cycle, and (ii) at least one of said second centrifugal compressor stage in said bottom heat pump cycle or said second centrifugal compressor stage in said top heat pump cycle, have a same workload.
14. The method of claim 1 , wherein a pressure ratio of at least one of said first centrifugal compressor stage in said bottom heat pump cycle or said first centrifugal compressor stage in said top heat pump cycle is at least 20% less than a pressure ratio of at least one of said second centrifugal compressor stage in said bottom heat pump cycle or said second centrifugal compressor stage in said top heat pump cycle.
15. The method of claim 1 , wherein an inlet volumetric flow rate of at least one of said first centrifugal compressor stage in said bottom heat pump cycle or said first centrifugal compressor stage in said top heat pump cycle is at most 110% more than an inlet volumetric flow rate of at least one of said second centrifugal compressor stage in said bottom heat pump cycle or said second centrifugal compressor stage in said top heat pump cycle.
16. The method of claim 1 , wherein an isentropic efficiency of at least one of said first centrifugal compressor stage in said bottom heat pump cycle or said first centrifugal compressor stage in said top heat pump cycle is substantially same as an isentropic efficiency of at least one of said second centrifugal compressor stage in said bottom heat pump cycle or said second centrifugal compressor stage in said top heat pump cycle.
17. The method of claim 1 , further comprising:
expanding said first working fluid to a lower pressure using a second expansion valve in said bottom heat pump cycle.
18. The method of claim 1 , further comprising:
expanding said second working fluid to a lower pressure using a second expansion valve in said top heat pump cycle.
19. The method of claim 1 , further comprising:
compressing said steam using a steam compressor.
20. The method of claim 1 , further comprising:
heating said first working fluid by rejecting and using heat from another location in said bottom heat pump cycle.
21. The method of claim 1 , wherein at least one of said first working fluid or said second working fluid comprises a fluorocarbon, a hydrofluoroolefin, a hydrofluoroether, a hydrocarbon, carbon dioxide, ammonia, or water.
22. The method of claim 21 , wherein at least one of said first working fluid or said second working fluid comprises said hydrofluoroolefin or said hydrofluoroether.