Much thermal generation is near the sea/ocean since a lot of population is there as well. Once through cooling is no problem there, only a diffusor pipe system has to be built to mitigate local thermal pollution issues.

Anyways, for inland locations, dry cooling is a proven option available at a small increment in levelised cost. Historically little value was placed on water conservation, so most plants are wet cooled. Adding a tax on freshwater cooling (bigger in arid areas) is one solution.

However, a more productive option is to use CHP thermal desalination and water treatment plant, using the nuclear plant's turbine heat rejection. This both creates a lot of new freshwater supply (from eg sewage water, brakish water, salt water if a sea/ocean is nearby) while reducing cooling water use (because the CHP can be seen as increased efficiency). If no water supply is nearby (could be the case in arid areas where freshwater supply is most dire), other CHP uses can be devised, such as paper and pulp heat input, other chemical processes etc. etc. that can also greatly reduce cooling water use.

This is one problem that is easily solved, and that can actually reduce fuel use and imports even more in the process by reducing natural gas and oil that would otherwise be needed if CHP was not available. This all does require the right policy. So now that you're reading along, Barack... :)

Is it possible (reasonable) to go back and retrofit some existing power plants for dry cooling? It seems like both the Southwest and Southeast could use the additional water, if it were available.

Is it possible (reasonable) to go back and retrofit some existing power plants for dry cooling?

Retrofitting is possible, however the plants electrical output would suffer. Thermodynamics of heat engines, of which steam turbines, diesel engines, and gas turbines are examples, state that the output is directly proportional to the heat flux times the difference between the input temperature and output temperature. For water it is difficult go higher than about 350º C on the hot end because of corrosion, high pressure and other engineering problems. On the low side we can go down to about 50º C if we can use cold sea water for cooling. For PWRs, (Pressurized Water Reactor) this limits us to about 34% efficiency. With a dry heat exchanger it would be difficult to get the low end temperature lower that about 110º C which would lower system efficiency to maybe 30%.

One large advantage of the LFTR and gas turbine is it can operate at between 650º- to 900º C on the hot end. With an air cooled heat exchanger on the low end running at 110º C we have an efficiency of over 50%, and lower cost.

The Lower Mississippi River has no foreseeable heat sink issues. The volume of water is incredibly vast.

Just the shipping channel at New Orleans is 900' wide and 100' deep moving at several knots at the summer minimum. Add the water underneath the shipping channel and to the sides.

Alan

I was pretty sure 'frombigeasy' was refering to your hometown and not some techy organization that feels big things come easy (you do paint bright pictures with a broad brush). Always good to see someone give good information about a place they know well, thanks. :)

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