Apparatus and methods of cooling a hot fluid stream

• US 4,270,358 A
• Filed: 05/25/1979
• Issued: 06/02/1981
• Est. Priority Date: 05/25/1979
• Status: Expired due to Term

• Current Assignee: Organization - World Intellectual Property
• Original Assignee: Chicago Bridge & Iron Company (Mcdermott International Incorporated)
• Inventors: Lai, Ban-Yen, Husain, Matloob, Schmitt, Richard L.
• Primary Examiner(s): DAVIS JR, ALBERT
• Application Number:
  US06/042,364
• Time in Patent Office: 739 Days
• Field of Search: 165/DIG. 1, 165/107, 165/45, 165/104 S, 165/110, 165/111, 60/693, 62/506, 62/115
• US Class Current: 60/693
• CPC Class Codes: F01K 9/003 condenser cooling circuits
• CPC Class Codes: Y10S 165/90 Cooling towers

Abstract

A hot fluid stream is cooled by contacting it, in indirect heat exchange, with a base cooling fluid so long as the base cooling fluid accepts heat rejected from the hot fluid stream and adequately cools the same. When the cooling capacity of the base cooling fluid is inadequate supplemental cooling is provided contemporaneously and indirectly by contacting the hot fluid stream with a secondary cooling liquid which is cold thereby heating the secondary cooling liquid. The heated secondary cooling liquid is delivered to a hot reservoir for storage. The hot secondary cooling liquid is later removed from the hot reservoir, cooled and delivered to a cold reservoir for storage. The cold secondary cooling liquid is removed when needed from the cold reservoir and again delivered into indirect heat exchange with the hot fluid stream when the base cooling fluid provides inadequate cooling for the hot fluid stream.

The base cooling fluid can be a refrigerant such as ammonia and the secondary cooling liquid can be water. The hot fluid stream can be steam condensed in a condenser of an electric power generating plant.

Claims

1. Apparatus comprising:

a first heat exchanger sized to cool and/or condense a hot fluid stream passed into contact therewith by rejection of heat to a first cooling fluid up to an average predetermined temperature and flow of the first cooling fluid, with said heat exchanger having inadequate cooling capacity during peak cooling conditions,

means to pass the hot fluid stream through the first heat exchanger in indirect heat exchange with the first cooling fluid,

a second heat exchanger for cooling the hot fluid stream when heat rejection therefrom to the first cooling fluid alone provides inadequate cooling of the hot fluid stream in the first heat exchanger,

the second heat exchanger being arranged to be in a series or parallel position with respect to the first heat exchanger,

means to pass the hot fluid stream through the second heat exchanger,

a hot reservoir for a secondary cooling liquid when hot,

a cold reservoir for the secondary cooling liquid when cold,

the capacities of the hot and cold reservoirs being adequate to hold the entire volume of secondary cooling liquid for the peak cooling conditions,

a conduit from the cold reservoir to the second heat exchanger for supplying cold secondary cooling liquid in indirect heat exchange to the hot fluid stream passed through the second heat exchanger,

a conduit for withdrawing hot secondary cooling liquid from the second heat exchanger and delivering it to the hot reservoir,

a conduit communicating with the hot reservoir and a cooler for delivering hot secondary cooling liquid from the hot reservoir to the cooler to be cooled, and

a conduit communicating with the cooler and the cold reservoir for delivering cold secondary cooling liquid from the cooler to the cold reservoir.

2. Apparatus according to claim 1 in which the first cooling fluid is a refrigerant gas, air or water.

3. Apparatus according to claim 1 including a closed loop containing the first coolng fluid, and means for cooling the first cooling fluid after it is heated by passage through the first heat exchanger.

4. Apparatus according to claim 3 in which the means for cooling the first cooling fluid after it is heated comprises a cooling tower in which heat is rejected to water, air or both.

5. Apparatus according to claim 1 in which the first and second heat exchangers are located in the steam condensor of a steam powered turbine.

6. Apparatus according to claim 5 including a closed loop containing the first cooling fluid, and a cooling tower for cooling the first coolng fluid after it is heated by passage through the first heat exchanger, said cooling tower functioning by rejecting heat to the air.

7. Apparatus according to claim 1 in which the cooling liquid fed to the second heat exchanger is water.

8. Apparatus according to claim 7 in which the cold reservoir and the hot reservoir are enclosed.

9. Apparatus according to claim 8 in which the cold reservoir and the hot reservoir are in the same enclosed tank.

10. Apparatus according to claim 1 in which the cooler, in which the hot secondary cooling liquid is cooled, rejects heat at least in part to air.

11. Apparatus according to claim 1 in which the cooler has means to reject heat from the hot secondary cooling liquid to the first cooling fluid when it is cold.

12. Apparatus according to claim 3 in which the first cooling fluid is a gas, the closed loop is part of a refrigeration cycle, and the first cooling fluid enters the first heat exchanger as a liquid and leaves as a vapor.

13. Apparatus comprising:

a steam condensor of a steam turbine containing a first heat exchanger and a second heat exchanger,

the first heat exchanger being sized to condense spent steam in the condensor by passage of a first cooling fluid through the heat exchanger up to an average predetermined temperature and flow of the first cooling fluid, with said heat exchanger having inadequate cooling capacity during peak cooling conditions,

a second heat exchanger in the condensor for condensing steam when heat rejection therefrom to the first cooling fluid alone provides inadequate cooling in the first heat exchanger,

a hot reservoir for a secondary cooling liquid when hot,

a cold reservoir for the secondary cooling liquid when cold,

the capacities of the hot and cold reservoirs being adequate to hold the entire volume of secondary cooling liquid for the peak cooling conditions,

a conduit from the cold reservoir to the second heat exchanger for withdrawing cold secondary cooling liquid from the cold reservoir and supplying it to the second heat exchanger in indirect heat exchange in the steam condensor,

a conduit for withdrawing hot secondary cooling liquid from the second heat exchanger and delivering it to the hot reservoir,

a conduit communicating with the hot reservoir and a cooler for delivering hot secondary cooling liquid from the hot reservoir to the cooler to be cooled, and

a conduit communicating with the cooler and the cold reservoir for delivering cold secondary cooling liquid from the cooler to the cold reservoir.

14. Apparatus according to claim 13 in which the cooler includes at least a portion which is air cooled.

15. Apparatus according to claim 13 in which the cooler includes at least a portion which is cooled by the first cooling fluid.

16. A method of cooling a hot fluid stream which comprises:

contacting a hot fluid stream in indirect heat exchange with a base cooling fluid so long as the base cooling fluid accepts heat rejected from the hot fluid stream and adequately cools the same,

supplementing the cooling of the hot fluid stream when the base cooling fluid provides inadequate cooling thereof, by contemporaneously also indirectly contacting the hot fluid stream with a secondary cooling liquid which is cold thereby heating the secondary cooling liquid,

delivering the hot secondary cooling liquid to a hot reservoir for storage with said hot reservoir having a capacity adequate to hold the entire volume of secondary cooling liquid,

removing the hot secondary cooling liquid from the hot reservoir, cooling it and delivering the cold secondary cooling liquid to a cold reservoir for storage with said cold reservoir having a capacity adequate to hold the entire volume of secondary cooling liquid, and

withdrawing cold secondary cooling liquid from the cold reservoir and again delivering it into indirect heat exchange with the hot fluid stream when the base cooling fluid provides inadequate cooling.

17. A method according to claim 16 in which the hot fluid stream is waste steam from a steam driven turbine.

18. A method according to claim 16 in which the base cooling fluid is heated by absorption of heat from the hot fluid stream, the hot base cooling fluid is cooled by passing it through a cooling tower and then is returned to again accept heat rejected by the hot fluid stream.

19. A method according to claim 18 in which the base cooling fluid is in a closed loop refrigeration cycle, and is a gas.

20. A method according to claim 19 in which the base cooling fluid is converted from a liquid to a vapor by heat rejected to it from the hot fluid stream, and the vapor is condensed to a liquid in passing through the cooling tower.

21. A method according to claim 18 in which the hot fluid stream is cooled in the cooling tower by indirect heat rejection to air.

22. A method according to claim 21 in which the temperature of the air, the size of the cooling tower and the rate of air flow through the cooling tower provide a limit as to the cooling of the hot fluid stream which can be effected by the base cooling fluid on hot days so that when such cooling is inadequate, supplemental cooling by means of the secondary cooling liquid is activated.

23. A method according to claim 22 in which the hot secondary cooling liquid removed from the hot reservoir is indirectly cooled at least partially by air.

24. A method according to claim 22 in which the hot secondary cooling liquid removed from the hot reservoir is indirectly cooled at least partially by base cooling fluid following cooling of the base cooling fluid in the cooling tower.

25. A method according to claim 23 or 24 in which the hot secondary cooling liquid is cooled primarily during evening hours and the cold secondary cooling liquid is used during daylight hours to cool the hot fluid stream.

26. A method according to claim 25 in which the hot fluid stream is waste steam from a steam driven turbine.

27. A method according to claim 26 in which the steam driven turbine is used to generate electric power and the steam is condensed to water in a steam condensor.