U.S. patent number 3,633,665 [Application Number 05/036,036] was granted by the patent office on 1972-01-11 for heat exchanger using thermal convection tubes.
Invention is credited to David M. France, Michael Petrick.
United States Patent |
3,633,665 |
France , et al. |
January 11, 1972 |
HEAT EXCHANGER USING THERMAL CONVECTION TUBES
Abstract
A heat exchanger is constructed with the hotter fluid in a lower
region and the cooler fluid in an upper region. A single wall
separates the two regions. Vertically mounted thermal convection
tubes extending from the hotter fluid to the cooler fluid through
the wall act to transfer heat between the fluids. The thermal
convection tubes contain a working fluid and provide for
substantially isothermal heat transfer, the latent heat of
vaporization of the working fluid being the primary mechanism
responsible for this heat transfer.
Inventors: |
France; David M. (Lombard,
IL), Petrick; Michael (Joliet, IL) |
Assignee: |
|
Family
ID: |
21886237 |
Appl.
No.: |
05/036,036 |
Filed: |
May 11, 1970 |
Current U.S.
Class: |
165/104.21;
122/33; 122/32; 165/104.14; 376/367; 376/402 |
Current CPC
Class: |
F28D
15/025 (20130101); F28D 15/0275 (20130101) |
Current International
Class: |
F28D
15/02 (20060101); F28d 015/00 () |
Field of
Search: |
;165/105,106
;122/367A,32,33 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
The embodiments of the invention in which an exclusive property or
privilege is claimed are defined as follows:
1. A heat exchanger system for use in generating steam with heat
from a sodium fluid which has been heated in a nuclear reactor,
including in combination, a first chamber coupled to the reactor
for receiving said sodium fluid therefrom, said first chamber
having a top wall, a second chamber positioned above said first
chamber with said top wall of said first chamber forming the bottom
wall of said second chamber, said top and bottom wall forming a
separation wall between said top and bottom chambers, said second
chamber further containing water, a plurality of sealed hollow
members each having an upper portion and a lower portion, each of
said sealed hollow members being placed in a substantially vertical
position and extending through said separation wall with said lower
portion in said first chamber and said upper portion in said second
chamber, said sealed hollow members being mechanically secured to
said separation wall at the middle portion of said sealed hollow
members, each of said sealed hollow members being in the form of a
first tube having sides and closed bottom and top ends, with said
lower portion thereof being substantially filled with liquid
mercury, a second tube having open top and bottom ends and
centrally located with reference to said sides of said first tube,
said bottom end of said second tube being spaced away from said
bottom end of said first tube, said top end of said second tube
being positioned below the surface of said liquid mercury in said
lower portion of said sealed hollow member, said heated sodium
acting to heat said liquid mercury to form a mercury gas, said
mercury gas rising to said upper portion and transferring heat to
said water while in said upper portion to generate steam in said
second chamber, said gas condensing to liquid mercury after said
heat transfer and returning to said lower portion, said second tube
acting as a downcomer to promote circulation of said liquid mercury
in said lower portion.
Description
CONTRACTUAL ORIGIN OF THE INVENTION
The invention described herein was made in the course of, or under,
a contract with the UNITED STATES ATOMIC ENERGY COMMISSION.
BACKGROUND OF THE INVENTION
To date, the development of heat exchangers for use in liquid metal
breeder reactors has been predominantly in the area of conventional
type shell and tube heat exchangers. In order to isolate the water
from the primary sodium which circulates through the reactor and
which is radioactive, a secondary sodium loop is employed. This
requires two heat exchangers, one to transfer heat from the primary
sodium to the secondary sodium and one to transfer heat from the
secondary sodium to the water. However, the water is still adjacent
liquid sodium and hazards of a sodium-water reaction resulting from
a leak are present. Another problem is in the welds used in the
construction of the shell and tube heat exchangers. The welded
regions are subject to considerable stress and are the source of
many failures.
Heat pipes are known to have the ability to transfer relatively
large quantities of heat at small thermal gradients. However, heat
pipes have had relatively short lifetimes compared to the
requirements for nuclear reactor application. The interaction of
the working fluid with the heat pipe walls creates a residue of
material which has been found to accumulate at the boiler section
of the heat pipe. The residue acts to obstruct the return flow of
the working fluid through the wick passages of the heat pipe.
It is therefore an object of this invention to provide a heat
exchanger wherein sodium-water contact does not occur subsequent to
a single tube rupture.
Another object of this invention is to provide a heat exchanger
wherein exchanger elements are not rigidly fastened at each end,
thus substantially reducing stress problems.
Another object of this invention is to provide a single heat
exchanger in place of the primary and intermediate heat exchangers
used in liquid-metal nuclear reactors.
Another object of this invention is to provide a heat exchanger
wherein boiling and superheating take place in separate
chambers.
Another object of this invention is to provide a heat exchanger
having a lifetime compatible with nuclear reactor requirements by
employing wickless heat pipes, "thermal convection tubes."
SUMMARY OF THE INVENTION
In practicing this invention a heat exchanger is provided having
two regions with one region positioned above the other and
separated therefrom by a separation wall. The lower region contains
a first fluid which may be, for example, liquid sodium. The second
region contains a second cooler fluid which may be, for example,
water. A sealed hollow tubular member extends from the lower region
through the separation wall to the upper region, with its
longitudinal axis substantially vertical. The lower portion of the
hollow tube which is within the lower region is substantially full
of a third fluid in its liquid state. The third fluid may be, for
example, mercury. In operation, heat from the sodium would be
transferred to the mercury which boils. The mercury vapor rises to
the upper portion of the tube which is within the upper chamber.
Heat is transferred from the mercury vapor to the water, heating
and boiling the water while simultaneously condensing the mercury.
The condensed mercury falls by gravity to the lower portion of the
hollow tube where it is again heated by the sodium. Vapor from the
boiling water may be transferred to a second chamber and
superheated in a similar manner.
BRIEF DESCRIPTION OF THE DRAWINGS
The invention is illustrated in the drawings, of which:
FIG. 1 is a cross-sectional view of the heat exchanger elements of
this invention.
FIG. 2 is a cross-sectional view of a heat exchanger having
separate boiling and superheating chambers.
FIGS. 3 and 4 are cross-sectional views of another embodiment of
heat exchangers having separate boiling and superheating
chambers.
FIG. 5 is a schematic showing the heat transfer path of prior art
shell and tube heat exchangers.
FIG. 6 is a schematic showing the heat transfer path in the heat
exchanger of this invention.
DETAILED DESCRIPTION OF THE INVENTION
FIG. 1 is a schematic representation of a cross section of the
cylindrical thermal convection tube of this invention. Heat from a
primary fluid 14, which may be, for example, sodium, is transferred
to the working fluid 19 inside of the tube 10, causing the working
fluid 19 to boil. The vapor 19A rises into the condenser section 11
of tube 10 where heat is removed to a secondary fluid 16, for
example, water, thus condensing the working fluid 19. Gravitational
forces cause the condensed working fluid 19B to return to the
heater section 13 of tube 10. A downcomer 20 is used to promote the
natural circulation of the working fluid and thus increase the
efficiency of the system. A wall 17 separates the primary fluid 14
from the secondary fluid 16. Wall 17 can be made as thick as is
required by strength and shielding considerations without
significantly affecting the heat transfer through the thermal
convection tube 10.
The axial temperature of the working fluid 19 in the thermal
convection tube 10 varies only a few degrees from the saturation
temperature at the liquid-vapor interface. This tube, like a heat
pipe, represents a method of sustaining large heat fluxes over
significant distances at nearly isothermal conditions. However, in
the case of the thermal convection tube, the absence of a wick
material permits the heat flux per unit area to be greatly
increased over the normal heat pipe by allowing for boiling of the
working fluid without decreasing tube lifetime.
FIG. 2 illustrates a thermal convection tube steam generator which
may, for example, use sodium as the primary fluid and water as the
secondary fluid. However, the invention is not restricted to use of
these two fluids. The primary fluid enters through inlet 21,
circulates past tube 38 in chamber 22, tube 34 in chamber 23 and
tube 31 in chamber 24. The fluid exits through outlet 25. As the
primary fluid moves past each of the tubes, heat is transferred to
the working fluid within the tube. In the upper portion of the
steam generator, a secondary fluid such as water in the liquid
state enters through inlet 28 into section 29. Heat from the
working fluid within tube 31 is transferred to the water in section
29, causing the water to boil. The vapors are carried into section
33 where heat from tube 34 acts to superheat the vapor. The vapor
is then transferred to section 37 where additional superheating
takes place by the transfer of heat from thermal tube 38. The
superheated vapor exits through outlet 39. Separation of the stages
allows the water to be boiled most efficiently in the nucleate
boiling region in the boiler stage and then superheated in separate
stages.
FIGS. 3 and 4 show a steam generator in which the tubes and stages
are concentrically arranged. The primary fluid enters through
inlets 42 and 43 in the lower portion of the generator and flows
past thermal tubes 59 and 55 in sections 45 and 46. The primary
fluid then flows into the center chamber 47, circulates past tubes
51 and is removed through outlet 49. Water enters through an inlet
(not shown) into the upper chamber 52, where heat from tubes 51
causes the water to boil, generating steam. The steam flows
radially to the inlet to chamber 53 where it is heated by heat
transferred from tubes 55. The superheated steam flows radially
into chamber 58, where it is superheated to higher temperatures by
heat transferred from tubes 59. The superheated steam exhausts
through outlets 61 and 62.
Referring to FIG. 5, there is shown the heat path from the primary
sodium 65 to water 66 in the prior art single-pass shell and tube
steam generation system. The path is through the secondary sodium
68 and through tube walls 69 and 71.
Referring to FIG. 6, there are shown two paths of heat transfer
from primary sodium 73 to the water 74 in the thermal convection
system. One path is through the working fluid 76, which may be, for
example, mercury, plus two tube walls 78 and 79. This heat path is
the same as the heat path in the shell and tube system with the
secondary sodium replaced by the working fluid 76. The second path
is from the primary sodium 73 through the separation wall 80 (17 in
FIG. 1). The thickness of the separation wall 80 may be very large
without significantly reducing the performance of the thermal
convection tube; most of the heat transfer occurs through the
thermal convection tube. The working fluid 76 takes the place of
the secondary sodium of the conventional system and thus an
intermediate heat exchanger is not required. Further, the water is
not immediately adjacent the sodium, so that the problems
associated with sodium-water leaks are not present.
* * * * *