U.S. patent number 3,630,276 [Application Number 05/010,161] was granted by the patent office on 1971-12-28 for shell-side liquid metal boiler.
Invention is credited to Jerry P. Davis, Gerald M. Kikin, N/A, T. O. Administrator of the National Aeronautics and Space Paine, Maurice L. Peelgren, Wayne M. Phillips.
United States Patent |
3,630,276 |
Paine , et al. |
December 28, 1971 |
SHELL-SIDE LIQUID METAL BOILER
Abstract
A shell-side liquid metal boiler including a tube and shell heat
exchanger particularly suited for use in effecting a heat exchange
between continuously flowing primary and secondary fluids within a
two-loop Rankine cycle power system, characterized by a plurality
of tubular conduits through which there is delivered a heated
primary fluid, and a boiler shell circumscribing the conduits
defining a boiler chamber within which shell-side boiling of the
secondary fluid is achieved, a feature of the invention being the
provision of a plurality of mutually spaced, angularly related
baffle plates mounted within the boiler and defining a tortuous
path having both crossflow and spiral-flow path components, whereby
the secondary fluid is permitted to circulate about the surfaces of
the tubular conduits for achieving a heat exchange through
shell-side boiling of the liquid metal within the boiler
chamber.
Inventors: |
Paine; T. O. Administrator of the
National Aeronautics and Space (N/A), N/A (Pasadena,
CA), Kikin; Gerald M. (Pasadena, CA), Peelgren; Maurice
L. (Altadena, CA), Phillips; Wayne M. (La Crescenta,
CA), Davis; Jerry P. |
Family
ID: |
21744229 |
Appl.
No.: |
05/010,161 |
Filed: |
February 10, 1970 |
Current U.S.
Class: |
165/158; 376/906;
122/32; 165/133; 165/155; 165/161; 165/174; 165/DIG.409 |
Current CPC
Class: |
F22B
1/023 (20130101); F28F 9/22 (20130101); F22B
3/02 (20130101); Y10S 165/409 (20130101); Y10S
376/906 (20130101) |
Current International
Class: |
F28F
9/22 (20060101); F22B 3/00 (20060101); F22B
1/00 (20060101); F22B 1/02 (20060101); F22B
3/02 (20060101); F28f 009/22 (); F22 () |
Field of
Search: |
;122/32 ;176/92
;165/159,160,161,158,174,133,155 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Davis, Jr.; Albert W.
Claims
What is claimed is:
1. A shell-side metal boiler comprising:
A. a sealed shell defining therewithin a first chamber of a
substantially cylindrical configuration;
B. a plurality of tubular conduits mounted in said first chamber in
parallelism with the longitudinal axis thereof for delivering a
heated primary fluid therethrough;
C. means defining a secondary fluid delivery port within one end
portion of said shell for introducing a secondary fluid into said
first chamber;
D. means defining a secondary fluid discharge port within the
opposite end portion of said shell for discharging the secondary
fluid from the first chamber;
E. means including a plurality of angularly related and
longitudinally spaced baffle plates transversely seated in said
first chamber defining a helical path extending between said end
portions of said shell for conducting the secondary fluid through
said first chamber from said secondary fluid delivery port to said
secondary fluid discharge port;
F. means defining within said opposite end portion of said shell an
entry plenum chamber communicating with the conduits for delivering
said primary fluid to said conduits;
G. means defining an exit plenum chamber within said one end
portion of said shell communicating with the conduits for receiving
said primary fluid from said conduits;
H. a substantially sealed jacket of a cylindrical configuration
spaced from the external surface of said shell and concentrically
related thereto defining therebetween a second chamber
concentrically related to said first chamber;
I. means defining within said sealed jacket, adjacent said one end
portion of said shell, a primary fluid delivery port for delivering
primary fluid to said second chamber; and
J. means defining within said opposite end portion of the shell a
primary fluid discharge port extending between said second chamber
and said entry plenum chamber, whereby the primary fluid delivered
to said second chamber is discharged into said entry plenum
chamber.
Description
ORIGIN OF INVENTION
The invention described herein was made in the performance of work
under a NASA contract and is subject to the provisions of Section
305 of the National Aeronautics and Space Act of 1958, Public Law
85-568 (72 stat. 435; 42 USC 2457).
BACKGROUND OF THE INVENTION
1. Field of the Invention
The field of the invention relates to liquid metal boilers and more
particularly to boilers employed in heating liquid metals for use
in generating electrical power within Rankine cycle systems.
2. Description of the Prior Art
Energy conversion systems are notoriously old. However, where
electrical energy is obtained through a thermal energy conversion
system it has been found that about 50 percent to 80 percent of the
available heat must be radiated or rejected. Liquid metal radiators
provide radiation and rejection of energy at high temperatures of
operation. Liquid metal boilers are deemed to be particularly
useful in Rankine cycle systems and are suited for use with nuclear
reactors. However, liquid metal boilers heretofore available have
not totally satisfied existing needs.
The prior art includes liquid metal boilers wherein a plurality of
parallel tubes serve as conduits for conducting liquid metals along
parallel paths through a heat transfer zone of a heat exchanger so
that heat is transferred to the liquid metal as the metal flows
through the tubes for thereby converting the liquid metal to its
vapor state. Such boilers inherently lack the capability of
providing a 100 percent pure vapor, free from surged and splashed
liquid and liquid spray.
In employing metal boilers of the prior art variety, wherein the
metal is heated as it is delivered through parallel tubes for
conduits, total vaporization of metals is quite difficult to
achieve, as such requires that the liquid remain in contact with
the walls of the heated conduits. This, of course, requires the
liquid to be delivered in streams of a tubular configuration having
a vapor core. As a practical matter such delivery cannot be
achieved. Furthermore, where the metal is confined as a mixture of
vapor and liquid "slugging" invariably occurs, since the vapor
tends to force "slugs" of liquid through the conduits.
Another difficulty often encountered in employing parallel conduits
for delivering liquid metals through a heat transfer zone of a heat
exchanger is system instability which arises as a result of the
fact that different rates of vaporization simultaneously occurs
within the several conduits.
Therefore, even though nuclear reactors constitute ideal sources of
energy for Rankine cycle systems there exists a need for a
practical boiler to boil liquid metals with a high degree of
efficiency and predictability. This is particularly true where such
systems are employed aboard space craft for use in space flight
operations of an extended duration.
OBJECTS AND SUMMARY OF THE INVENTION
It is therefore an object of the instant invention to provide an
improved liquid metal boiler which employs a tube and shell heat
exchanger having a high degree of operational stability.
Another object is to provide an improved metal boiler particularly
suited for use in imposing a change of phase on liquid alkali
metals for achieving metal vapors through shell-side boiling.
Another object is to provide an improved liquid metal boiler which
is adapted to impose a change of phase on alkali metals with a high
degree of predictability.
Another object is to provide an improved liquid metal boiler which
is adapted to achieve shell-side boiling of potassium.
Another object is to provide an improved liquid metal boiler for
converting cooled liquid potassium to a heated vapor by achieving a
heat exchange between liquid lithium and the potassium as the
potassium is caused to circulate about tubular conduits employed in
delivering heated lithium through the boiler.
Another object is to provide an improved shell-side liquid metal
boiler adapted to conduct a heated primary fluid through a
plurality of spaced, tubular conduits, and to deliver a secondary
fluid along a tortuous path having both crossflow and spiral-flow
path components extending about the conduits so that a change of
phase is imposed on the secondary fluid as it progresses through
the boiler.
Another object is to provide an improved liquid metal boiler for
converting liquid alkali metal to heated vapor by achieving a heat
exchange between liquid metals through conduction, as the alkali
metal is caused to circulate about tubular conduits employed in
delivering a heated fluid therethrough, whereby a heat exchange
through conduction is achieved.
Another object is to provide within a liquid metal shell-side
boiler a plurality of substantially parallel baffle plates for
directing liquid potassium along a tortuous path having both
crossflow and spiral-flow path components circumscribing a heat
delivery system including a bundle of substantially parallel,
spaced tubular conduits through which heated liquid lithium is
delivered in order that the lithium be permitted to give up
relatively large quantities of heat to the potassium for achieving
a heat exchange therebetween, whereby the potassium is caused to
undergo a change of phase from a liquid to a vapor having a high
exit quality extending into vapor superheat.
These and other objects and advantages of the instant invention are
achieved by providing a liquid metal boiler having a shell of a
tubular configuration circumscribing a plurality of axially
extended, lithium conducting conduits and baffle plates arranged
within the shell in a manner such that circulation of liquid
potassium about the conduits is achieved to effect shell-side
boiling of the potassium as it is caused to progress along a
tortuous path, having both spiral and crossflow path components
extending between the adjacent surfaces of the conduits and the
boiler shell.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a diagrammatic view of the system embodying the
shell-side liquid metal boiler of the instant invention.
FIG. 2 is a flow diagram depicting the path of flow for primary and
secondary fluids as the fluids are caused to flow along adjacent
paths through the boiler illustrated in FIG. 1.
FIG. 3 is a cross-sectional elevation of the boiler shown in FIG.
1, illustrating the relationship established between the conduits
utilized in conducting a primary fluid through the boiler and the
baffle plates employed in delivering a secondary fluid along a
tortuous path having both crossflow and spiral-flow path components
and extending about the conduits.
FIG. 4 is a cross-sectional view taken generally along line 4--4 of
FIG. 3.
FIG. 5 is a cross-sectional elevation of a modified form of the
boiler shown in FIG. 1.
DESCRIPTION OF THE PREFERRED EMBODIMENT
Turning to FIG. 1, therein is illustrated a shell-side liquid metal
boiler 10 operatively disposed within Rankine cycle power system.
As shown, the system includes a primary loop 12 and a secondary
loop 14. The primary loop is adapted to deliver heated liquid
lithium to the boiler 10 for purposes of achieving a transfer of
heat while the secondary loop 14 is adapted to deliver liquified
potassium, which absorbs heat from the lithium of the primary loop,
and to conduct heat from the boiler 10 as a discharge of vaporized
potassium occurs.
Since Rankine cycle power systems are known, and lithium-potassium
boiler systems have heretofore been employed in such systems, a
detailed description thereof is omitted in the interest of brevity.
However, it is to be understood that the primary loop 12 is a
substantially closed-loop which includes a heat generator 16 of a
suitable configuration, such as a nuclear reactor, adapted to
elevate the temperature of a primary fluid, such as liquid lithium,
to a working temperature of approximately 2,100.degree. F., while
the secondary loop 14 is a substantially closed-loop which is
utilized to deliver a cooled secondary fluid, such as potassium, to
the boiler 10 for purposes of achieving a heat exchange between the
metals, whereupon the secondary fluid is converted to a vapor and
delivered from the boiler 10 at an exit temperature of
approximately 1,900.degree. F.
At the output side of the heat generator 16 there is provided a
pump 18 which serves to impel the primary fluid through the loop.
The pump 18 is of a suitable design which, as a practical matter,
may be a centrifugal unit driven by a variable speed DC motor, not
shown. At the output side of the pump 18, between the pump and the
boiler 10, there is a flowmeter 20 which, where desired, is
employed in detecting and controlling the rates of flow for liquid
lithium flowing through the loop 12.
As depicted, the secondary loop 14 includes therein a turbine 22
directly connected with the output of the boiler 10 so that it is
driven by the secondary fluid as the fluid is circulated within the
loop. In practice, the turbine 22 is employed in driving an
electrical energy generating device, such as, for example, a
three-phase, 200 cycle induction generator.
At the hydraulic output side of the turbine 22, there is connected
a condenser 24 which is employed in extracting heat from the
secondary fluid, as it egresses from the turbine 22, to impose a
phase change for reverting the secondary fluid to its liquid phase
in order that flow control be enhanced. From the condenser the
cooled secondary fluid is delivered to a suitable pump 26 which
serves to impart to the secondary fluid a given flow rate. At the
output side of the pump 26, between the pump and the boiler 10,
there is a preheater 28 which serves to elevate the temperature of
the secondary fluid to preselected values prior to its being
delivered to the boiler 10. As a practical matter, the loop 14 also
includes a flow meter 30 adapted to be employed in controlling the
flow of a secondary fluid through the secondary loop as it is
delivered from the pump to the boiler 10.
As best illustrated in FIG. 2, the primary fluid is delivered
through the boiler 10 along substantially parallel paths,
designated by parallel arrows 32, while the secondary fluid is
delivered along a tortuous path including both crossflow and
spiral-flow path components, as indicated by the arrows 34. By
employing both spiral-flow and crossflow path components, an
efficient heat transfer is achieved within the boiler as the
primary fluid is caused to give up its heat to the secondary fluid
so that a high exit vapor heat is achieved as the secondary fluid
is discharged from the boiler 10.
In order to achieve the flows indicated by the arrows 32 and 34,
the boiler 10 also includes a tubular shell 36 sealed at opposite
ends by a pair of spaced end plates 38 and 40. Consequently, within
the shell there is established a substantially sealed boiler
chamber 42, FIG. 3. The boiler chamber thus established is provided
with a primary fluid delivery port 44, which serves to introduce to
the chamber heated, liquid lithium, and a primary fluid discharge
port 46, which serves to discharge the lithium from the boiler
chamber 42, once a heat exchange has been achieved between the
primary and secondary fluids.
Adjacent to the delivery port 44 there is an entry plenum chamber
48 defined by a transverse plate 50 spaced inwardly from the plate
38. The plate 50 is provided with a plurality of openings 52
disposed at equidistances throughout the plate and extends
therethrough for accommodating passage of the primary fluid so that
the chamber 48 functions as an input manifold.
Adjacent to the discharge port 46 there is provided an exit plenum
chamber 54 defined by a transverse plate 56 spaced from the end
plate 40. This includes a plurality of openings 58 arranged in
coaxial alignment with the openings 52 of the plate 50 so that the
chamber 54 is caused to serve as a discharge manifold.
Between the plates 50 and 56 there is extended a plurality of
tubular conduits 60 disposed in substantial parallelism with the
opposite ends of each being inserted in the coaxial openings 52 and
58 of the plates 50 and 56, respectively, so that the entry plenum
chamber 48 is caused to communicate with the exit plenum chamber 54
through the conduits 60. It will therefore be appreciated that a
flow of primary fluid is, in operation, established between the
entry and exit plenum chambers as it is introduced through the port
44. Within the plenum chamber 48 there is arranged a plate 62
including therein a myriad of relatively small openings 64 defining
parallel fluid passages which tend to reduce turbulence within the
flow of the primary fluid, prior to its delivery to the tubular
conduits 60 in order that turbulence within the flow be reduced
prior to the delivery of the primary fluid through the tubular
conduits 60.
In communication with the chamber 42, between the plates 50 and 56,
there is a secondary fluid delivery port 66 and a secondary fluid
discharge port 68 by which the secondary fluid is delivered to and
extracted from the boiler chamber 42 of the boiler 10. It is
important here to note that the secondary fluid is confined by the
shell 36 as it progresses through the boiler chamber 42, and that
the primary fluid is confined by the tubular conduits 60 axially
extended through the chamber 42. By employing this arrangement,
shell-side boiling for the secondary fluid is achieved whereby
system stability is greatly enhanced.
As it is desirable to achieve efficient heat transfer, in order
that a high exit vapor quality predictably be achieved, there is
provided a plurality of baffle plates 70 which impose direction
control on the flow of the secondary fluid as the secondary fluid
flows through the boiler chamber 42. Each of the baffle plates 70
is of a generally disk-shaped configuration having a portion
severed along a predetermined chord so that the periphery of each
of the plates defines a truncated circle. As a practical matter,
the manner in which the peripheral portion of the baffle plate is
removed is a manner of convenience and the extent thereof is
dictated by the flow rate to be imposed on the system. In any
event, it is to be understood that the truncated portions of the
plates 70 and the internal surface of the shell 36 establish a
plurality of passageways 72 accommodating a desired flow rate for
the secondary fluid as it flows through the chamber 42.
The plates 70 are so arranged within the shell 36 that the
passageways 72 are angularly displaced by 120.degree. for thereby
defining a tortuous path helically extended through the boiler
chamber 42, including both crossflow and spiral-flow path
components. Hence, as the secondary fluid is introduced through the
delivery port 66 it is conducted about the conduits 60 along a
helical path of progression extending from the secondary fluid
delivery port 66 to the secondary fluid discharge port 68.
Consequently, the fluid is caused to be delivered into engagement
with the external surfaces of the tubular conduits 60 for thereby
achieving a heat exchange between the primary and the secondary
fluids as they progress in substantially opposite directions
through the boiler chamber 42.
In practice, each of the tubes 60 further is provided with a
plurality of minute nucleation cavities 74 formed along the surface
of the tubes in order to initiate nucleate boiling of the secondary
fluid as it progresses through the boiler chamber 42 and
experiences shell-side boiling.
Of course the material employed in fabricating the boiler 10 is
dictated by the types of primary and secondary fluids utilized and
the operative temperatures encountered during the operation of the
system. In practice, where the boiler 10 is to be employed in a
lithium-potassium system, the components and piping are of a
material such as niobium wrapped with layers of zirconium and
tantalum. Therefore, the technique employed in joining the various
components is a matter of convenience dictated by the particular
metals being employed.
The boiler 10 has been employed with a 30-kw. Rankine cycle system
such as that shown in FIG. 1. In such a system, the heat generator
16 serves to elevate the temperature of the primary fluid, or
lithium, sufficiently for heating the secondary fluid, or
potassium, to a superheated vapor state for driving a
turbogenerator. As a practical matter, the temperatures to which
the lithium operatively is heated by the generator 16 approximates
2,100.degree. F., while the working temperature of the secondary
fluid, as it exits the boiler 10, is approximately 1,900.degree. F.
When employing the boiler 10 with a Rankine cycle system it has
been found possible to achieve approximately 100 percent boiler
exit vapor quality and heat transfer rates of greater than 3,000
B.t.u/hr.-ft..sup.2 -.degree. F. at flow rates of 4-8
lb./sec.-ft.sup.2.
In instances where it is found desirable to accelerate the heating
of the secondary fluid by applying heat to the external walls of
the shell 36, a modified boiler 75 may be employed. As illustrated
in FIG. 5, the shell 36, of the boiler 75 is circumscribed by a
secondary jacket 76 which serves to define a cylindrical chamber 78
surrounding the external surfaces of the shell 36 while an
additional primary fluid injection port 80 is provided at a
location such that the primary fluid is caused to progress along
the external surfaces of the shell 36, prior to being delivered
through the delivery port 44 into the plenum chamber 48.
OPERATION
The operation of the described embodiment of the subject invention
is believed to be clearly apparent and is briefly summarized at
this point. With the boiler 10 coupled within a Rankine cycle
system, of the type illustrated in FIG. 1, the heat generator 16 is
activated for elevating the temperature of the primary fluid as it
exits the boiler 10. The heater 16, in effect, serves as a means
for replenishing the heat given up or lost to the secondary fluid
as the fluids are circulated through the boiler 10. Upon exiting
the heat generator 16, the heated primary fluid is impelled by the
pump 18 on a return flow to the conduits 60 within boiler chamber
42. As a practical matter, the pump 18 delivers the lithium through
the flow meter 20 and is adjustable for imposing selected flow
rates upon the system. As the lithium is delivered through the flow
meter 20 it is caused to be delivered to the entry plenum chamber
48, and thence to the tubular conduits 60, via the plate 62, which
serves to inhibit turbulence as the direction of flow for the fluid
is altered. As the lithium progresses through the conduits 60, heat
is extracted therefrom and conducted by the walls of the conduits
thus tending to cool or reduce the temperature of the lithium. In
order that the lithium be returned for reheating within the
generator 16, it is delivered from the conduits 60 into the exit
plenum chamber 54 and thence through the port 46 for recycling.
Simultaneously, with the circulation of the primary fluid, the
secondary fluid, or liquid potassium, is delivered as a liquid at
approximately 600.degree. F. from the preheater 28, through the
secondary fluid delivery port 66 and into the boiler chamber 42 in
a manner such that it is caused to contact the external surfaces of
the tubular conduits 60. As the secondary fluid is brought into
contact with the external surfaces of the conduits, it is heated,
by extracting heat from the walls of the conduits 60. As sufficient
quantities of heat are extracted from the conduits a phase change
is imposed upon the secondary fluid for thus causing the liquid to
be converted to a vapor as it progresses along the tortuous path
defined by the passageways 72. As the passageways 72 are angularly
related, the path followed by the secondary fluid includes both
crossflow and spiral-flow path components which cause the fluid to
pass across the surfaces of the tubular conduits 60 at right angles
thereto, as well as to experience helical progression. As the
secondary fluid progresses through the chamber 42, the nucleate
cavities 74 initiate nucleate boiling of the fluid, so that at exit
the temperature of the thus vaporized potassium is approximately
1,900.degree. F. From the boiler 10 the fluid is delivered as a
vapor to the turbine and ultimately returned to the preheater
through the condenser 24 and pump 28.
Where a secondary jacket 76 is employed in delivering heat
externally through the wall of the shell 36, the primary fluid also
is delivered through the conduit 80 and caused to circulate about
the shell 36 as it progresses towards the delivery port 44.
Consequently, the temperature of the secondary fluid is elevated by
heat delivered through the walls of the conduits 60, as well as by
heat delivered through the wall of the shell 36.
Although the invention has been herein shown and described in what
is conceived to be the most practical and preferred embodiment, it
is recognized that departures may be made therefrom within the
scope of the invention, which is not to be be limited to the
illustrative details disclosed.
* * * * *