Introduction
[0001] Due to the increasing need of cooling / heating fluids in a more efficient way and
using less space, and so reducing the resources used, it appears the necessity of
designing more efficient and compact heat exchangers that obtains a better energy
efficiency in the heat exchange.
[0002] In most of applications where heat exchangers are used to cool - heat a fluid usually
is also present the necessity of heat - cool another fluid for any other requirement,
if this heating function is done using the same exchanger that is used to cool the
other fluid the efficiency of the whole process will be increased notably (regeneration).
[0003] Next pages describe the basis of a rotating - regenerative heat exchanger that is
able to do in an efficient way the functions described in previous paragraph.
[0004] The use of this device is also possible in the cooling of blades in the hot gas path
areas, showing a clear application as cooler of materials located in hot gas areas,
increasing this way the useful life of this components, as well as their substitution
by others of lower heat resistant characteristics reducing costs.
[0005] Also, taking in account its rotative concept and the amount of energy that in the
way of pressure and kinetic energy the fluids to cool - heat usually have, with an
adequate blade design a turbine type device can be obtained simultaneously extracting
power from both fluids.
Description and working concept
[0006] First of all fluids to heat - cool have to be conducted to the heat exchanger using
concentrical conduction, being the cooling fluid in the inner pipe and the fluid to
cool down in the exterior one. Both fluids can circulate in the same direction or
in opposite directions, being more effective the second one to also increase the heat
exchange across the concentrical pipes.
[0007] Using the concentrical pipes both fluids are conducted to the hollow rotating blades
that are the heat exchange pieces, both fluids get across the blades without mixing,
because there is a sealing system between both fluids, and at the exit of the blades
the fluids are conducted using the concentrical scheme to the areas where they are
required.
[0008] Concentrical conduction are only required at the inlet and outlet of the heat exchanger,
being any other disposition possible before or after the exchanger.
[0009] All the heat exchanger is shown in schematics in figure 1.
[0010] Refrigeration takes place in the hollow blades as follows. In the inner hollow part
of the blades there is a liquid that is able to have a phase change to gas between
the temperatures of the cooling and cooled fluids (i.e. at cooling fluid temperature
the inner fluid of the blades is liquid and at the cooled fluid temperature is gas).
[0011] When the inner fluid circulates in the external area of the blades that is in contact
with the hot external fluid this was will make the phase change of the inner liquid
to gas. Being the heat exchange with phase change of the inner fluid the heat exchange
efficiency is highly increased.
[0012] The fluid inside the blades gasified in the external area of the blade is rotating
as well as the blade, and as long as the fluid located in the inner area of the blade
is still liquid it will push down the gas to the inner part of the blade (this happens
due to the rotation force on the liquid part of the fluid that is more dense that
the gas phase and it is pushed to the external area of the blade), in this area the
gas will be liquefied again because of the temperature of the external fluid circulating
into the inner pipe that will be heated by the heat exchange phase of the inner blade
fluid.
[0013] This working cycle is continuos , providing the centre of rotation of the blades
is coincident with the centre of both concentrical conductions.
[0014] Figure 2 shows an scheme of the described process.
[0015] External and internal walls of the blades will be designed in a way that increases
as much as possible the HTC, using ribs, turbulators, or whaterever improved design.
[0016] The rotation of the blades can be achieved using an external motor or, in order to
get a better efficiency, using the energy available in the fluids to cool - heat designing
the blades in an adequate mode. It can be seen a scheme of design of the blades powered
by fluids in figure 3.
[0017] The transition of the fluids from the static zone (concentrical pipes) to the rotating
one (blades) will be designed using adequate sealing systems depending on the fluids
(i.e. labyrinth seals, gas seals, mechanical seals..).
[0018] As it has been commented previously the same device is also useful to cool down the
material of the blades located in the hot fluid path, because as long as in the inner
hollow are is all the time circulating a mixture of the inner gas liquid fluid, the
temperature of this mixing is always lower than the one of the fluid located in the
external area of the blade, so the blade material temperature is sensibly reduced.
[0019] To use the device in whatever of its applications is not required to use any other
device or external cooling fluid, this reduces the cost of auxiliary pumping cooling
device (cooling towers) for the external cooling fluid.
Application fields
[0020] The design in its heat exchanger version is applicable to whatever industrial field
requiring an efficient heat exchange. Clear immediate application examples can be
found in gas or steam turbines for the cooling of different stages, secondary airflow
preconditioning or preheating of heavy fuels. In petrochemical or industrial plants
to heat or cool several process fluids. In terrestrial vehicles, ships or planes to
cool down engines and heating the air-conditioned for passengers. In air conditioning
systems to reduce their size and achieve better efficiencies, ...
[0021] The design in its material cooling version it can be applied immediately in all type
of turbo machinery that deals with hot fluids to refrigerate turbo machinery components
located in the hot fluid path.
Figure description
[0022] Figures shown are only schemes not showing any dimension as long as these values
will change depending on the application. The only point for showing this figure is
to help on the description and location of the main components of the system.
[0023] Figure 4 shows cooling and cooling fluids circulating in the same direction to simplify
the figure, not existing in the design any obstacle to make both fluids to circulate
in different directions as we have told before.
[0024] Surfaces have also been represented without any HTC increasing device to ease the
drawings.
[0025] In side view of figure 5 external cases has been turn transparent to facilitate the
view of internal components.
[0026] Relationship between L1, L2, L3, D1, D2 & D3 will be fixed depending on the fluids
to use, the flow to cool, the materials to use,... The number of cooling stages (discs)
of blades will be also fixed taking in account the specific application.
[0027] Some of the major required data to dimension the system are next ones (and of course
there can be others that can also play a role in the design):
- Mass flows of the cooling and cooled fluids.
- Adaptation capacity of the fluid from the normal piping on the system to the required
concentrical disposition of the exchanger.
- Rotating speed of the blade and number of blades per stage.
- Pressure of the fluids in the system.
- Temperature reduction (on increase) that will be achieved using the exchanger.
[0028] Figure 6 shows a front view showing inlet of both fluids to the device.
[0029] Figure 7 shows the blades transparent to allow the viewing of the concentrical disposition
of the concentrical conducts.
1. Heat exchanger - cooler regenerative with intermediate fluid and phase change, where
the intermediate fluid is used to do the heat exchange between the hot and cold sides
improving the exchange efficiency because the intermediate fluids is subjected to
phase change during the exchange periods as it is described in the description annexed
to this patent claim.
2. Equipment according to claims 1 to be used in whatever the industry as heat exchanger
as well as in turbo machinery or rotating machinery as coolant for materials of the
machinery itself.
3. Equipment according to previous claims, not depending on its dimensions, shape, finishing,
number of blades, number of stages of blades, combined use with other devices or being
part of those ones, materials for manufacturing the device, sealing systems to be
used between rotating and static parts.
Amended claims under Art. 19.1 PCT
1. Heat exchanger - cooler regenerative with intermediate fluid and phase change, where
the intermediate fluid is used to do the heat exchange between the hot and cold sides
improving the exchange efficiency because the intermediate fluids is subjected to
phase change during the exchange periods as it is described in the description annexed
to this patent claim. The heat exchange is being done continuously between the intermediate
interchange fluid and the hot fluid cooling the last one, and betweent the intermediate
interchange fluid and the cold one heating this one. The hot and cold fluids circulate
through concentrical conducts in the heat exchanger being the cold fluid in the inner
area and the hot one in the external area. The intermediate cooling fluid is gasified
when is in the area of the hot fluid and get condensed back when is in the cold fluid
area. Due to the rotational movements of the hollow blades where the intermediate
fluid is located, the liquid part of the fluid that is located in the inner area is
pushed to the external area of the blade due to the rotational forces (because the
density of the liquid is bigger than the one of the gasified part) making this way
the gasified part to be sent back to the inner part of the blade. This process is
repetitive being always condensation and vaporisation in the inner and outer areas
of the hollow blades.
2. Equipment according to claims 1 to be used in whatever the industry as heat exchanger
as well as in turbo machinery or rotating machinery as coolant for materials of the
machinery itself. Beyond its function as heat exchanger described in first claim the
proposed system is also useful as internal cooling of components located in hot fluid
areas. As long as the intermediate fluid is continuously changing from liquid to gas
and from this back to liquid, this fluid is able to get a lot of hot from the hot
areas that is going to be released in the cold one when condensation takes place.
In this way the temperature inside the hollow blade is going to be more or less constant
and of course lower that the one in the hot area getting this way an effective cooling
of the blade material.
3. Equipment according to previous claims, not depending on its dimensions, shape, finishing,
number of blades, number of stages of blades, combined use with other devices or being
part of those ones, materials for manufacturing the device, sealing systems to be
used between rotating and static parts.