U.S. patent number 3,612,172 [Application Number 04/859,829] was granted by the patent office on 1971-10-12 for air-cooled condenser.
This patent grant is currently assigned to Borsig Gesellschaft mit beschrankter Haftung. Invention is credited to Dietrich Dohnt.
United States Patent |
3,612,172 |
Dohnt |
October 12, 1971 |
AIR-COOLED CONDENSER
Abstract
An air-cooled condenser in which pipes extending between an
upper header and a lower header are divided into upper and lower
axial sections by the upper ends of condensate tubes which lead
downwardly to a condensate chamber. Steam is supplied through the
headers to opposite ends of the pipes and condensate from the upper
section of each pipe draining down the respective tube to the
condensate chamber which condensate from the lower section of each
pipe drains into the lower header. A fan causes cooling air to pass
over the pipes which, for efficient heat transfer, may be
finned.
Inventors: |
Dohnt; Dietrich (Berlin,
DT) |
Assignee: |
Borsig Gesellschaft mit
beschrankter Haftung (Berlin, DT)
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Family
ID: |
5702865 |
Appl.
No.: |
04/859,829 |
Filed: |
September 22, 1969 |
Foreign Application Priority Data
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Sep 25, 1968 [DT] |
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P 17 76 130.7 |
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Current U.S.
Class: |
165/111;
165/DIG.197; 62/289; 165/114; 62/290; 165/174 |
Current CPC
Class: |
F28B
1/06 (20130101); F28B 9/005 (20130101); Y10S
165/197 (20130101); F28B 2001/065 (20130101) |
Current International
Class: |
F28B
9/00 (20060101); F28B 1/00 (20060101); F28B
1/06 (20060101); F28f 013/04 () |
Field of
Search: |
;165/111,174,175,110
;159/28 ;202/185,185B ;62/289,290,DIG.16 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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255,445 |
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0000 |
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DT |
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908,429 |
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0000 |
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GB |
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Primary Examiner: Matteson; Frederick L.
Assistant Examiner: Streule; Theophil W.
Claims
What is claimed is:
1. A condenser having an upper header means and a lower header
means, conduit means connected to said header means for supplying
steam thereto, pipe bundle means connected to and extending between
said header means, and fan means operable for causing cooling
airflow through said pipe bundle means, a condensate discharge tube
extending into each pipe of said pipe bundle means from the lower
end of the respective pipe, the upper end of each discharge tube
engaging the inside of the respective pipe and dividing the pipe
into upper and lower axial sections whereby steam to be condensed
flows in countercurrent direction simultaneously from said header
means into both ends of said pipes, condensate chamber means
connected to the lower ends of said tubes to receive from said
tubes the condensate from the upper sections of said pipes, the
condensate from the lower sections of said pipes drawing from said
pipes into said lower header means, and means for withdrawing
condensate from said condensate chamber means and from said lower
header means.
2. A condenser according to claim 1 in which said steam flows
axially in said header means and the length of said pipe sections
varies in increasing direction in conformity with the length of
travel of the steam prior to entry into pipes along said header
means to the end of the respective section.
3. A condenser according to claim 1 in which said steam flows
axially in said header means and the length of said pipe sections
varies in decreasing direction in conformity with the length of
travel of the steam prior to entry into pipes along said header
means to the end of the respective section.
4. A condenser according to claim 1 in which steam is supplied to
about the middle of the length of said lower header means for flow
outwardly therein toward the ends and flows from the ends thereof
to the ends of said upper header means and then toward the middle
of the length of said upper header means, the length of the said
sections of said pipes into which steam flows progressively
increasing in the direction of steam flow prior to entry into pipes
through said header means.
5. A condenser according to claim 1 in which each said tube has
aperture means therein immediately below the region of engagement
of the upper end of the tube with the respective pipe whereby inert
air from both collectively withdrawn axial sections of each pipe
passes into the respective condensate discharge tube and downwardly
therethrough to said condensate chamber means.
6. A condenser according to claim 1 in which said pipe bundle means
comprise pipe sections longer in differing pipes displaced from
each other in the direction of airflow through the bundle means,
the upper sections of said pipes varying in length in the direction
of said airflow.
7. A condenser according to claim 1 in which each of said tubes
comprises a first upper portion which at its upper end engages a
respective pipe and a second lower portion extending into said
condensate chamber means, said respective portions being in
slidable telescopic engagement and thereby compensating for
differential thermal expansion of individual pipes in the
condenser.
8. A condenser according to claim 1 in which said pipes
individually are finned for each bundle means.
9. A condenser according to claim 1 in which said lower header
interconnected also to bypass means is in the form of two laterally
spaced lower headers, said pipes converging in the upward direction
from said lower headers, said fan discharging air upwardly into the
space confined between said pipes and flowing laterally over and
between said pipes.
10. A condenser according to claim 6 in which said upper
respectively sections of said pipes individually increase in length
progressively in the direction of airflow through said pipe bundle
means.
Description
The present invention relates to a condenser which is cooled by an
automatically moved airflow, and in which there are provided at
least two rows of substantially parallel condenser pipes spaced
from each other and located one behind the other when looking in
the direction of flow of the cooling air. More specifically, the
present invention concerns an air-cooled condenser of the
above-mentioned type in which the rows of condenser pipes are in
parallel arrangement connected to steam-distributing chambers
common thereto and are in communication with condensate collecting
chambers. The round or profiled condenser pipes, which are in most
instances of the same design, are, as a rule, equipped with fins.
On the outside, the condenser pipes are acted upon by a cool
airflow which is drawn from the atmosphere and is automatically put
into motion by a fan.
Generally, condensers are so operated that the stream to be
condensed flows from the top into or about the pipes, and the
condensate flows in the direction of the steam downwardly into the
condensate collector.
Air-cooled condenser installations of the above-mentioned type,
especially such for depositing turbine exhaust steam with finned
pipe bundles which at the upper end are connected to a common
steam-distributing pipe system so that the steam and the condensate
in each pipe can flow in one direction only, namely, from the top
downwardly, and with cooling air temperatures below the freezing
point cause considerable disturbances in the operation for instance
in the vacuum installation. With turbine exhaust steam, for
instance, the condensation temperature is generally at 60.degree.
C. and in most instances even lower which means that the
temperature distance between the water steam condensate and the
freezing point thereof is relatively small. The condensate flows
along the inner pipe wall downwardly to the mouth of the pipe into
the condensate chamber. In view of the very unfavorable heat
passage conditions between the condensate and the cooling air in
the lower portion of the pipes, also air under certain conditions
of operation, a steam condensation no longer occurs, with low outer
air temperatures also a low temperature of the pipe wall occurs. On
the other hand, with low outer air temperatures also the
temperature distance between exhaust steam and cooling air is
relatively great. This brings about that the condensation is
completed at a greater distance from the lower pipe mouth than for
instance at the point for which the installation was designed,
whereas the condensate with a forming temperature of for instance
60.degree. C. has to overcome this relatively long path along the
cold inner pipe wall, which means that the condensate has a long
staying time in the unfavorable cooling zone. In the lower pipe
section, the condensate conveys its heat up to solidifying to the
cold pipe wall.
It is a well-known fact that the icing danger is greatest in the
first pipe row when looking in the direction of flow of the cooling
air, because here the temperature drop between steam and cooling
air is greater than in the pipe rows therebehind. This means that
the condensate stays particularly long in the first pipe row in the
unfavorable cooling zone. Similar remarks also apply to the partial
load operation for instance of a condensation turbine. The
condensation of the exhaust steam may in this instance be completed
soon after the steam enters the upper pipe mouth because the
excessive cooling surface will under partial load operation have
such an effect that the major portion of the lower section of the
cooling surface is not contacted by the excess steam. Also in this
connection, the condensate has to pass over a larger under cool
surface. A control of the quantity of cooling air or the turning
off of cooling surfaces may at less low outer air temperatures
result in a slight improvement, however, at surrounding
temperatures approximately from -5.degree. C. on, the less
mentioned step is not effective against formation of ice in the
pipes. Noncontrollable wind influences increase the icing danger in
winter considerably.
Ice formation in the lower pipe mouth brings about an increase in
pressure in the condenser and considerably reduces the vacuum.
Ice plugs which may form may even burst the pipes with the result
that air will break in. Under certain circumstances, it may then be
necessary to disassemble the installation.
Condensers have become known in which the exhaust steam line is so
arranged that the steam can enter the mouth of the finned pipes
only from below, and in which the condensate flows downwardly in
countercurrent flow to the upwardly flowing steam, into the
condensate collecting chambers. This arrangement of the exhaust
steam line, which is also known as dephlegmatoric circuit, prevents
the undercooling of the condensate by the fact that the upwardly
flowing warm steam keeps warm the condensate which flows in
opposite direction. However, this circuit can be employed only
under certain conditions of operation, but wherever it can be
employed, it will safely prevent ice formation in the pipes. This
dephlegmatoric circuit, however, as already indicated, can be
employed only under certain conditions when the proper function of
the condenser installation is to be assured. In this connection, it
has to be taken into consideration that the speed of the steam when
flowing into the lower mouth of the pipes is not very high. Too
high steam velocities bring about an accumulation of the downwardly
flowing condensate in the mouths of the pipes. Variations in the
pressure in the condenser and shockwise flowing off of the liquid
and thereby an irregular operation for instance of a vacuum
installation will result. Admissible inflow speeds require a
relatively small specific volume of the steam to be condensed or a
correspondingly high inlet cross section of all mouths of the
pipes. Vacuum steam, especially turbine exhaust steam, however, has
a relatively large specific steam volume so that the inlet cross
section of all mouths or exits of the pipes must be very great in
order to make possible a corresponding inlet speed of the steam
during full load operation. Large inflow cross sections, however,
require short pipes and a constant cooling surface. It is a
well-known fact that devices and therefore air-cooled condensers
with relatively short pipes have the drawback that for instance a
considerable number of chambers, long pipelines and a plurality of
fans increase the cost of the installation and make the same
uneconomical.
On the other hand, the construction of a condenser with such short
pipes is frequently not possible at all because with such short
pipes an economic relationship with regard to the diameter of the
fans cannot be realized. It is for this reason that the
dephlegmatoric operation is frequently not possible at all.
There have also become known condenser installations with nozzles
which are inserted into the pipe bottom of the steam distributing
chamber or directly into the pipes. These nozzles, when looking in
the direction of the cooling airflow have their cross-sectional
passage for the steam decreasing successively so that a better
distribution of the steam over the individual rows of pipes will be
obtained and the pressure drop in the rear rows of pipes will be
increased. For certain definite conditions of operation, it is
possible by such an arrangement to bring about that in the rows of
pipes which are first acted upon or passed through by the cooling
air, the condensation of the steam is completed only shortly in
front of those areas where the pipes lead into the condensate
collecting chamber so that an undercooling of the condensate will
be avoided. However, with such air-cooled condenser equipped with
nozzles, it is not possible to adapt the arrangement to the
respective conditions of operation in such a way that in particular
at low-cooling temperatures and low steam loads, the icing danger
will be eliminated, because in view of the excessive cooling
surface, the condensation of the steam is completed far away from
the lower mouth of the pipes. Furthermore, the nozzles bring about
a considerable pressure loss at the steam side and thus create a
poor vacuum. Furthermore, an air-cooled condenser installation has
become known in which the condenser chambers provided at the lower
end of the pipe bundle are in the direction of flow of the cooling
air subdivided into individual subchambers. These finned pipe
bundles, in which the steam flows from the top downwardly while
condensing, have associated therewith dephlegmator bundles which on
the air side are parallel to each other and on the steam side are
arranged one behind the other. These subchambers are individually
and adjustably connected to the air suction devices. Such an
arrangement is supposed to bring about that the underpressure in
the succeeding subchambers decreases in the direction of the
airflow whereby the steam distribution is, in conformity with the
pipe rows, connected to the individual subchambers in conformity
with the respective available temperature drop between steam and
cooling air. The condensation is supposed in this way to be
completed in all pipe rows at a slight distance from where the pipe
ends lead into the pertaining subchambers. Such an arrangement has
the drawback that the exhaust steam condenses first from the top in
downward direction and only subsequently the residual steam passes
into the dephlegmator. It will be evident therefrom that with
partial load operation, for instance, a condenser turbine, and at
low cooling temperatures, an excessive cooling surface is obtained
in the condenser portion which with regard to the steam side is
located in front. This cooling surface completes the condensation
of the exhaust steam not at a short distance from where the pipe
ends lead into the lower chambers but at a considerable distance
therefrom . The controllable air suction device will definitely not
remedy the situation because with said air suction devices it is
possible only to maintain the condensation in the individual pipe
rows approximately equal. Under no circumstances is it possible by
means of the air suction device to displace the condensation
downwardly which has been completed at a considerable distance from
the lower pipe mouth. Consequently, also with the condenser
equipped with these devices, the desired effect cannot be realized.
A further drawback consists in that expensive and sensitive control
devices are necessary for the air withdrawal.
It is, therefore, an object of the present invention to provide an
air-cooled condenser which will overcome the above mentioned
drawbacks.
It is another object of this invention to provide an air-cooled
condenser, in which the condensation of the steam is effected in
two spaced sections with clear flow relationship in the pipes in
flow directions which are opposite to each other. The length of the
pipe up to the condensate discharging means in the upper subsection
of the finned pipe bundle is relatively short so that also the
undercooling distance at very low cooling temperatures will be
reduced to a minimum.
These and other objects and advantages of the invention will appear
more clearly from the following specification in connection with
the accompanying drawings, in which:
FIG. 1 diagrammatically illustrates a condenser.
FIG. 2 represents a section taken along the line II--II of FIG.
1.
FIG. 3 represents a cross section through a condenser element on a
larger scale than that of FIG. 1.
The condenser according to the present invention is characterized
primarily in that the steam-distributing chambers and pipelines at
the upper end of the finned pipe bundle, and the steam distributor
and condensate collecting chambers combined at the lower end are so
connected to the bypass lines that the steam flows through the
finned pipes in countercurrent direction while the finned pipes
spaced at a certain distance from the upper and lower mouths of the
pipes are subdivided transverse to the pipe axis into pipe sections
by means of condensate withdrawing means which are connected to the
central pipes which latter lead into the condensate collecting
chamber. In this way, the condensation of the steam is effected in
two separate subsections with clear flow conditions in the pipes in
countercurrent flow direction. The pipe length up to the condensate
withdrawing line in the upper partial section of the finned pipe
bundle is relatively short so that also the undercooling distance
will be reduced to a minimum at low-cooling air temperatures. The
condensate is detached from the upper pipe section before it is
undercooled and might ice. This detachment from the inner pipe wall
is effected by the condensate withdrawal means, and the detached
condensate passes through the central pipes countercurrent to the
upwardly flowing warm steam in the dephlegmator part, and is here
held warm by the steam, which is extremely advantageous.
A further advantage by subdividing the finned pipe in a direction
transverse to the pipe axis in two separate subsections and by the
bilateral steam action consists in that the steam has available a
pipe section which is large (approximately twice as large) as is
available with the heretofore known condenser designs. As a result
thereof, the loss in pressure of the steam when flowing into the
mouth of the pipes is reduced and thereby an economic vacuum is
realized. Particularly during the summer season, the heretofore
known condensers have a poor vacuum because they lack the
above-mentioned advantage.
It is further advantageous at reduced quantity of steam, to keep
only the dephlegmator part in operation which is particularly
suitable in this connection inasmuch as it prevents the freezing of
the condensate. Also when in this instance, i.e. at a low steam
quantity, still some steam should come in from above, the path
through the pipe bundle part which is operated as a condenser is
shorter than is the case with heretofore known designs requiring
the entire or full-pipe length.
A further important advantage of the present invention over
heretofore known structures consists in that not only the steam
side is separated but also the condenser side. Due to the fact that
a portion of the condensate is separated by the central pipes from
the condensate flowing off from the dephlegmator part, an
accumulation of condensate in the lower pipe mouth, i.e. at the
steam inlet of the dephlegmator is avoided for all practical
purposes.
With the present design, no control elements and shutoff devices
are necessary which at temperatures below the freezing point are
necessary with the heretofore known designs in order to prevent
freezing.
A further development of the present invention consists in that the
pipe sections, measured from the condensate withdrawal means to the
respective pipe mouth in the lower as well as in the upper pipe
sections prior to flowing into the pipe mouth are so designed that
they become greater in steps. In view of this stepwise greater
configuration, it will be assured that where the steam enters the
finned pipe bundles, the shortest pipe length and thereby the
smallest cooling surface is available to the incoming steam. The
finned pipe bundles which are located farthest from the steam entry
have, when viewing in the flow direction of the steam, the larger
cooling surface. At full-load and relatively large inflow speed of
the steam, the actuation on the steam side in the individual finned
pipe bundles is distributed better due to the fact that between the
inflowing steam and the finned pipe bundles remote therefrom, with
the increasing cooling surfaces, an ever greater pressure drop will
form. This brings about that the nonuniform flow conditions of the
steam in the distributing chambers or pipelines and the different
pressure losses in the pipe mouths are equalized with regard to
each other.
With small quantities of steam, however, the steam is condensed
only in the lower dephlegmator part. As a result thereof, it will
be realized that a residue steam quantity will penetrate the
connecting pipes and pass into the condenser operated pipe bundle
part whereby the safety of operation will be increased.
If the inflow velocity of the steam, contrary to the just described
instance, is relatively small, it will be understood that a
stepping of the cooling surface also in the inverse direction may
be effected in conformity with the present invention so that the
fin pipe mouths which are the first when looking in the steam
direction are actuated open to the same extent by the said
operation as are the finned pipe mouths located therebehind.
According to a further feature of the invention, the bores are
arranged slightly below the condensate withdrawal means in the
central pipes so that from the lower condensate collecting chamber,
the inert air is withdrawn from the upper subsection of the pipe
through the pipe mouth of the central pipes in the condensate
withdrawing means, as well as from the lower subsection of the
pipes through the bores, and the withdrawn inert air then passes
through the central pipe. In view of this arrangement of the bores,
the dephlegmator chamber or cooling surface is better taken
advantage of so that the condensate withdrawing means will be kept
warm at this area.
It is known that the condensation in the first row of pipes when
viewing in the cooling airflow direction is completed at a larger
distance from the lower pipe mouth than is the case with the pipe
rows therebehind. According to a further development of the
invention, the pipe sections measured from the condensate
withdrawing means to the pipe mouth in the upper steam distributing
chamber when seen in the flow direction of the cooling air is in
each pipe row designed longer. By shortening the front pipe rows of
the part operated as condenser, the condensate withdrawing means
are closer to the end of the condensation, and the path of the
condensate along the cold pipe inner wall is reduced and is earlier
introduced into the central pipes in the warm dephlegmator part. In
the last row of pipes when viewing the arrangement in the airflow
direction, the cooling surface in the part operated as a condenser
is so large that the steam does not penetrate the central pipes of
the dephlegmator part but is already condensed. As a result
thereof, optimum design of the installation will be assured.
In order to be able to equalize different temperature expansions of
the individual pipes, the central pipe is, in conformity with the
present invention, built up of two parts. The lower part with a
larger diameter is connected to the combined steam distributor and
condensate collecting chamber and overlaps the upper portion of the
central pipe.
Referring now to the drawings in detail, the condenser illustrated
in FIGS. 1 and 2 comprises a plurality of roof-shaped condenser
elements which are formed of at least one or, as illustrated, of
three rows of substantially parallel finned pipe bundles 1 which
are spaced from each other or are arranged one behind the other
when viewing in the flow direction d of the cooling air. Steam from
below is conveyed to the finned pipe bundles 1 through the lower
combined steam producing and condensate collecting chamber 5.
Through the conveying lines 3 and steam lines 2, also steam from
above is conveyed to the finned pipe bundles 1. The pipe bundles
are thus passed through by the steam in opposite direction.
However, it is also obvious that, if desired, the exhaust steam
conduits may be connected to the finned pipe bundles in such a way
that a portion of the steam is condensed first in the upper pipe
sections and the residual steam is condensed in the lower pipe
sections. The supply of steam may also be effected (in a
nonillustrated manner) from a gable side (FIG. 1) through only one
bypass line 3 in such a way that the steam acts upon the upper and
lower pipe sections parallel or in series and passes therethrough
in opposite direction in conformity with the invention. The pipes
are, by a condensate withdrawing means 14, subdivided on the inside
transverse to the pipe axis into an upper section 12a and a lower
section 12b. The steam fed from above through the steam
distributing chambers 4 will condense in the upper pipe section
12a, and the condensate will flow through the condensate
withdrawing lines 14 and central pipes 15 into the condensate
collecting chambers 8.
The steam which flows from the combined steam distributor and
condensate collecting chambers 5 upwardly will condense in the
lower pipe sections 12b, and the condensate will flow back into the
above-mentioned condensate collecting chambers 5. The condensate is
withdrawn from the condensate collecting chambers 5 and 8 through
the pipes 9 and condensate lines 10, respectively, in the direction
of the arrow b. The inert air from the lower pipe sections 12b is,
through bores 13, located shortly below the condensate withdrawing
lines 14 in the central pipes 15, withdrawn together with the inert
air from the upper pipe sections 12a through the central pipes 15,
the condensate collecting chambers 8, and pipes 6 into the air
lines 7 in the direction indicated by the arrow c. FIG. 1 further
shows the bulkheads 11 of the air condensator which is supported by
four supports 17 illustrated at the lower end.
FIG. 1 furthermore illustrates that the pipe sections, measured
from the condensate withdrawing line 14 to the respective mouth of
the pipes increase by steps or continuously not only in the upper
but also in the lower pipe sections 12a and 12b when viewed in the
flow direction "a" of the steam. The pipe sections measured from
the condensate withdrawing means 14 to the respective pipe mouth
not only in the upper but also in the lower pipe sections 12a and
12b when viewed in the flow direction "a" of the steam may be
designed stepwise smaller (not illustrated).
FIG. 2 shows that the roof-shaped finned pipe bundles 1 have a
cross section forming the sides of an approximately equilateral
triangle the basis of which is formed by an axial fan 18. The
fin-equipped pipe bundles may also be so arranged that in the
direction of the pipe axis they are perpendicular with regard to
the horizontally arranged fan axis (not illustrated). Above the
axial fan 18 there is provided a transmission 19 and a motor 20. As
indicated by the arrows d, the cooling air is, by at least one
axial fan 18, conveyed from the bottom in upward direction or in
reverse direction (not illustrated) and passes by the outside of
the smooth or fin-equipped bundle 1.
FIG. 3 shows the subdivision of the upper pipe sections 12a which,
when viewed in cooling airflow direction d are longer in each pipe
row. The condensate withdrawing means 14 is thus arranged closer to
the condensation end in the upper pipe section 12a, because the
latter is displaced as is well known in downward direction when
viewing the flow direction of the cooling air. Thus, the path of
the condensate along the cold inner wall of the pipe section 12a is
reduced in those pipe rows which, when viewing the direction of
flow of the cooling air, are located in front. The central pipe 15
comprises two parts. The lower part 16 with a larger diameter is
connected to the combined steam distributor and condensate
collecting chamber 5, and the upper part of the central pipe 15,
which has a smaller diameter, is covered up by said lower part 16
in such a way that therebetween a labyrinthlike sealing effect is
obtained. This subdivision of the central pipe compensates for the
temperature expansions of the individual pipes.
It is, of course, to be understood that the present invention is,
by no means, limited to the particular showing in the drawings but
also comprises any modifications within the scope of the appended
claims.
* * * * *