U.S. patent number 3,716,045 [Application Number 05/031,928] was granted by the patent office on 1973-02-13 for heat exchanger.
This patent grant is currently assigned to Siegener Aktiengesellschaft. Invention is credited to Frohmut Vollhardt.
United States Patent |
3,716,045 |
Vollhardt |
February 13, 1973 |
HEAT EXCHANGER
Abstract
A heat exchanger for cooling hot inert gases in a metal bath
while producing steam in two serially arranged chambers each
containing a metal bath and heat exchanging surfaces, the
arrangement being such that the gases are introduced into the
respective metal bath from above and the withdrawal of the gases
from said chambers is effected above the level of the metal bath
while the heat absorbing medium flows through the chambers in
counter-current flow to the gases, and the exchanger surfaces are
so designed that the metal bath temperature in the serially first
chamber is the highest.
Inventors: |
Vollhardt; Frohmut
(Siegen-Burbach, DT) |
Assignee: |
Siegener Aktiengesellschaft
(Geisweid, DT)
|
Family
ID: |
5733174 |
Appl.
No.: |
05/031,928 |
Filed: |
April 27, 1970 |
Foreign Application Priority Data
|
|
|
|
|
May 3, 1969 [DT] |
|
|
P 19 22 647.2 |
|
Current U.S.
Class: |
126/350.1;
122/31.2; 165/104.29; 165/111; 165/144; 165/104.19; 165/140 |
Current CPC
Class: |
F28C
3/06 (20130101); F28D 15/00 (20130101); F22B
1/06 (20130101) |
Current International
Class: |
F22B
1/00 (20060101); F22B 1/06 (20060101); F28C
3/00 (20060101); F28C 3/06 (20060101); F28D
15/00 (20060101); F24h 001/20 () |
Field of
Search: |
;165/1,104,111,140,145
;122/28,31 ;126/36A |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
What I claim is:
1. A heat exchanger which guarantees a sufficient heat transfer for
cooling hot inert gases passing through tubing in a standing liquid
metal bath while producing steam, which includes: container means
having at least first chamber means wherein temperature is higher
and separate second chamber means, a standing liquid metal bath
received and contained in each of said first and second chamber
means, first conduit means leading into said first chamber means
near the bottom thereof for conveying hot gases into the standing
liquid metal bath in said first chamber means, second conduit means
extending from above into and through the lower portion of said
first chamber means for conveying saturated steam into and
discharging superheated steam from said second conduit means,
immersion pipe means leading from the upper portion of said first
chamber means to said second chamber means near the bottom thereof
for conveying hot gas above the standing liquid metal bath in said
first chamber means into the standing liquid metal both in said
second chamber means, evaporator pipe feeding and discharge lines
extending in part through the standing liquid metal bath in said
second chamber means, and discharge conduit means communicating
with the upper portion of said second chamber means for withdrawing
therefrom inert gas cooled relative to the metal bath in said first
and in said second chamber means while avoiding any circulating
metal bath and avoiding any Mammut-pumping effect and bubbling in
any column through the liquid metal bath.
2. A heat exchanger according to claim 1, which includes equalizing
means communicating with a bottom portion in said first chamber
means and a bottom portion in said second chamber means for
equalizing the level of the metal baths in said first and second
chamber means respectively.
3. A heat exchanger according to claim 2, in which said equalizing
means includes conduit means interconnecting said first and second
chamber means and check valve means interposed in said last
mentioned conduit means.
4. A heat exchanger according to claim 1, which includes tank means
common to and containing said first and second chamber means, and
partition means separating said first and second chamber means from
each other.
5. A heat exchanger according to claim 1, which includes another
metal bath, third chamber means following said second chamber means
for receiving the further metal bath having a lower melting point
than the metal baths to be received in said first and second
chamber means.
Description
The present invention relates to a heat exchanger for cooling hot
inert gases in a metal bath while producing steam in two serially
arranged chambers respectively receiving a metal bath with heat
exchanger surfaces (preheater, evaporator, superheater). It is
known to employ liquid metal as intermediate carrier between a
heating medium and a working medium, for instance water or steam.
For generating steam, it is known to carry out the transfer of the
heat content of a hot inert gas, for instance a gas for cooling a
nuclear reactor, to a liquid metal in two serially arranged
chambers respectively receiving a metal bath with heat exchanger
surfaces, such as preheater, evaporator and superheater. In this
connection, for securing a good heat transfer between the media,
the metal is circulated in the individual chambers while employing
the Mammut pump principle (secondary air lifting means). The said
Mammut pump principle is based on the following physical behavior.
Compressed air or compressed gas is in a riser mixed with the
liquid to be conveyed and thereby reduces the specific weight of
the liquid so that the latter will rise in view of the effect
exerted by the outer atmospheric pressure acting upon the level of
the liquid. The employment of the Mammut pump principle will with
metal baths always result in a circulation and conveying of the
liquid metal (see German Auslegeschrift No. 1,201,856).
It is an object of the present invention to provide a heat
exchanger of the above mentioned type which will have a simplified
construction and an improved degree of efficiency and which during
the discharge of the cooled gases from the heat exchanger will not
carry off metal particles.
This object and other objects and advantages of the invention will
appear more clearly from the following specification in connection
with the accompanying drawing diagrammatically illustrating a
section through a heat exchanger according to the invention.
The heat exchanger according to the present invention is
characterized primarily in that the gases are introduced into the
metal bath of the individual chambers from above while the
withdrawal of the gas above the level of the metal bath is effected
in each chamber and while the heat absorbing medium passes in
counter flow to the gases through the chambers, the heat exchanger
surfaces being so designed that the temperature of the metal bath
of the first chamber adjacent the gas is the highest
temperature.
The present invention differs in its operation from heretofore
known heat exchangers with liquid metal as exchanging medium in
that according to the invention the liquid metal is not circulated
and the heat transfer is not effected by a heat transport.
According to the present invention, the liquid metal is at rest and
the heat transfer is effected by heat conduction within the liquid
metal. In this way, all means for transporting the liquid metal,
including the insulation of such transporting means, will become
superfluous.
In contrast to the possibility at the gas side to provide a heat
exchanger ahead of the metal bath, the heat exchanger according to
the invention yields the advantage that, for instance when
employing fission gas as heat releasing medium, the usually
extensive soiling of the heat exchanger will be avoided. When
introducing such gas into a liquid metal bath, soiling particles
will float on the surface of the metal bath without affecting the
heat exchange in the interior of the bath.
According to a further development of the invention, the chambers
are interconnected through a connecting line with a control valve.
The metal which at a temperature of the metal bath of from
500.degree. to 700.degree. C is carried away from the bath in the
first chamber passes through immersion pipes into the metal bath of
the second chamber. An equalization of the quantity of metal in
both chambers may be effected by means of the above mentioned
connecting line and the control valve. For the transport of the
liquid metal in the connecting line, advantage may be taken of the
difference in the level of the baths in both chambers.
Preferably, the two chambers are arranged in a common tank which is
separated by a partition into which the end of the immersion pipes
is inserted. The chamber which receives the superheater pipes may
be insulated by a special insulating lining.
The two chambers may be followed by a third chamber containing a
metal of a lower melting point than that of the metal in the two
preceding chambers. A preheating of the feed water may be effected
in the metal bath with the lower melting temperature.
FIG. 1 is a diagrammatic view showing features in accordance with
the present invention.
FIG. 2 is a diagrammatic view showing a modified embodiment of the
present invention.
Referring now to FIG. 1 of the drawings in detail, the heat
exchanger illustrated therein comprises a horizontally arranged
boiler 1 one end portion of which is provided with an inner
insulating layer 2. This insulating layer 2 together with a
partition 3 defines the chamber I. A feeding pipe 4 extends into
the chamber I for the hot gas which at a temperature of
approximately from 800.degree. to 900.degree.C flows in the
direction of the arrow A. This hot gas represents the heat
releasing medium. As will be seen from the drawing, the lower end
4a of the pipe 4 extends into the vicinity of the bottom 5 or the
lining thereof while the lower section of the pipe 4 is surrounded
by superheater pipes 6. These pipes 6 as well as the said pipe
section are so arranged that when the level of the metal bath 8 has
the height customary for the operation of the heat exchanger, the
said parts are located below the level of the bath. The superheater
pipes 6 are through headers 9, 10 in communication with
corresponding feeding and withdrawing pipes 11, 12 for the
saturated steam and the superheated steam respectively.
The second chamber II which is separated from the chamber I by a
wall or partition 3 does not require a lining and comprises the
immersion pipes 13, 14 which through a common immersion line 15 are
in communication with each other. The pipe 15 ends in the wall 3 so
that the gas which is above the metal bath 8 can pass through
conduit 15 to the immersion pipes 13, 14. The lower end 13a, 14a of
the pipes 13, 14 is again located slightly above the bottom 15 of
the chamber II while the lower section of the pipes 13, 14 is
surrounded by evaporator pipes 16. The lower ends 13a, 14a of the
pipes 13, 14 and the pipe 16 are so arranged that these parts will
during the operation of the heat exchanger be located below the
level 17 of the metal bath 18 in chamber II.
A discharge connection 19 for the inert gas which with regard to
the metal in chambers I and II has been cooled to 330.degree. to
400.degree.C extends into the chamber II.
The connection 19 may be followed by a conduit with a feed water
preheater, and there may furthermore be provided in this conduit a
blower or compressor which produces the necessary pressure for the
gas which is pressed through the heat source in which the inert gas
is heated again to a temperature of from 800.degree. to
900.degree.C and is also pressed through the metal baths 8, 18 of
the heat exchanger.
The headers 20, 21 of the evaporator pipe 16 communicate with the
feeding and discharge lines 22, 23 respectively. The two chambers I
and II are in communication by means of a connecting line 24
adjacent the bottoms 5, 15 of the two chambers. This connecting
line 24 has interposed therein a control valve 25. When the levels
of the baths 7, 17 differ from each other by .DELTA. h, a
corresponding pressure difference is obtained as a result of which
liquid metal can be passed from chamber II into chamber I. As a
result thereof, the quantity of metal carried away by the gas in
the direction of the arrows B and flowing into the chamber II, can
again be compensated for.
If desired, the illustrated heat exchanger with, for instance, a
bath of lead or a bath of a lead compound may be followed by
another heat exchanger the metal of which may have a lower melting
temperature than lead, for instance, tin.
As inert gas for operating the heat exchanger, preferably fission
or synthesis gas or helium may be employed which are heated
directly or indirectly in a nuclear reactor or fission furnace.
With the embodiment according to FIG. 2, a container or vessel
consists of three chambers III, IV, and V, whereby the chamber III
is partially filled with a lead bath 30 and both chambers IV and V
are partially filled each with a lead bath 31 and 32. A supply
tubing 33 projects into the chamber III; the tubing lower end dips
into the lead bath 30 in which on the other hand the overheating
tube means 34 is provided. After the supplied gas has bubbled
through the bath by way of the supply tubing 33, the same reaches
the chamber IV in the direction of arrow 35 in the dip conduit 36
of which the lower end emanates in the bath 31. The gas bubbles
again through this bath and reaches the dip conduit 37 of the
chamber V where the lower end of the dip tubing 37 dips into the
bath 32. In the bath 32 there lie the tube means 38 which form the
exchange surfaces and by way of which the heat-receiving medium for
instance water, respectively water vapor is supplied. The tube
means 38 proceed into the exchanger tubes 39 of chamber IV. From
these tubes the saturated vapor, respectively hot steam is
withdrawn at 40.
Between the last chamber V and the first chamber III there is a
connection conduit 41 provided in which a valve 42 is arranged and
by way of which an equalization of the metal parts drawn therewith
is created so that these parts collect in the chamber V.
It is, of course, to be understood that the present invention is,
by no means, limited to the particular showing in the drawing but
also comprises any modifications within the scope of the appended
claims.
* * * * *