U.S. patent number 3,814,177 [Application Number 05/223,880] was granted by the patent office on 1974-06-04 for steam condensers.
This patent grant is currently assigned to GKN Birwelco Limited. Invention is credited to Peter John Harris, Barry Stanford Holmes, John Lee Ryder.
United States Patent |
3,814,177 |
Harris , et al. |
June 4, 1974 |
**Please see images for:
( Certificate of Correction ) ** |
STEAM CONDENSERS
Abstract
A direct sub-atmospheric steam condenser having horizontal
condenser tubes arranged in pairs of banks of tubes. The banks in
each pair are inclined to each other and converge upwardly, and the
steam inlet header for each bank is connected to a steam manifold
which is arranged below the tops of the banks of tubes.
Inventors: |
Harris; Peter John (Birmingham,
EN), Holmes; Barry Stanford (Birmingham,
EN), Ryder; John Lee (Birmingham, EN) |
Assignee: |
GKN Birwelco Limited
(Birmingham, EN)
|
Family
ID: |
9777825 |
Appl.
No.: |
05/223,880 |
Filed: |
February 7, 1972 |
Foreign Application Priority Data
|
|
|
|
|
Feb 11, 1971 [GB] |
|
|
4472/71 |
|
Current U.S.
Class: |
165/110; 165/114;
165/122; 165/900 |
Current CPC
Class: |
F28B
1/06 (20130101); F28B 9/10 (20130101); Y10S
165/90 (20130101) |
Current International
Class: |
F28B
1/00 (20060101); F28B 9/00 (20060101); F28B
9/10 (20060101); F28B 1/06 (20060101); F28b
001/00 (); F28b 009/08 () |
Field of
Search: |
;165/110,111,122,128,124,126,71 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
900,407 |
|
Jul 1962 |
|
GB |
|
904,959 |
|
Sep 1962 |
|
GB |
|
903,397 |
|
Aug 1962 |
|
GB |
|
Primary Examiner: Antonakas; Manuel A.
Attorney, Agent or Firm: Merriam, Marshall, Shapiro &
Klose
Claims
What we claim then is:
1. A steam powered plant comprising a steam turbine; an air cooled,
sub-atmospheric, steam condenser comprising a plurality of pairs of
banks of tubes, the banks of each pair converging upwardly, each
bank comprising two horizontally spaced apart, aligned headers and
a plurality of straight substantially horizontal tubes connected
between the headers, steam inlet chambers and condensate outlet
chambers formed by the headers, flow directing means for directing
the steam to flow through at least two tubes in series between a
steam inlet chamber and a condensate outlet chamber, a steam
manifold below said banks and connected to the outlet of said steam
turbine, elongated feed pipes extending upwardly from the manifold
to the steam inlet chambers, suction means connected to said
condensate outlet chambers, fan means arranged below the banks and
operable to cause a flow of air to the banks and operable to cause
a flow of air upwardly over the banks, means to collect condensate
from said condensate outlet chambers and a steam generator to
receive said condensate and to generate steam and to feed the same
to the steam turbine.
2. An air-cooled, sub-atmospheric, steam condenser comprising a
plurality of pairs of banks of tubes, the banks of each pair
converging upwardly and each bank comprising two horizontally
spaced apart, aligned headers and a plurality of straight
substantially horizontal tubes connected between the headers, steam
inlet chambers and condensate outlet chambers formed by the
headers, flow directing means for directing steam to flow through
at least two tubes in series between a steam inlet chamber and a
condensate outlet chamber, said flowing directing means comprising
a divider in one header of each of at least some of the banks and
serving to divide said header into a steam inlet chamber and a
condensate outlet chamber, the tubes in each bank containing a
divided header and connected to the condensate outlet chamber of
said divided header being above the tubes of the bank connected to
the steam inlet chamber of said divided header, a steam manifold
below said banks, elongated feed pipes extending upwardly from the
manifold to the steam inlet chambers, suction pipes connected to
said condensate outlet chambers, and fan means arranged below the
banks and operable to cause a flow of air upwardly over the
banks.
3. A steam condenser according to claim 3, wherein, in each bank
having a divided header, there is a greater number of tubes
connected to the steam inlet chamber than to the condensate outlet
chamber.
4. An air-cooled, sub-atmospheric, steam condenser comprising a
plurality of pairs of banks of tubes including primary and
secondary banks of tubes, the banks of each pair converging
upwardly and each bank comprising two horizontally spaced apart,
aligned headers and a plurality of straight substantially
horizontal tubes connected between the headers, steam inlet
chambers and condensate outlet chambers formed by the headers, a
steam manifold below said banks, elongated feed pipes extending
upwardly from the steam manifold to the steam inlet chambers,
suction pipes connected to said condensate outlet chambers, fan
means arranged below the banks and operable to cause a flow of air
upwardly over the banks and interconnecting manifolds connecting
each secondary bank to a plurality of primary banks whereby steam
flows first through tubes of a primary bank and then flows through
tubes of a secondary bank.
Description
This invention relates to steam condensers of the type in which
steam at sub-atmospheric pressure is passed through tubes having
extended external surfaces over which pass cooling air. This type
of condenser is known and will hereinafter be referred to as a
"direct, sub-atmospheric, steam condenser."
Known condensers of this type which are arranged to occupy a
minimum plot area, have the tubes arranged with their centre lines
in generally vertical planes and grouped in pairs of banks. The
tubes in each bank of a pair are parallel and inclined to the tubes
in the other bank of the pair so that the tubes in the respective
banks converge upwardly and at their upper ends are connected to a
steam manifold common to the banks of the pair. A condenser will
normally include a number of pairs of banks, such a pair being
known as an A-frame, all or some of which are fed from the same
steam manifold.
This known type of direct, sub-atmospheric steam condenser has been
commercially successful and has been used where the plot area to be
occupied by the condenser is limited. However, such condensers
suffer from the following disadvantages:
1. The use of longer finned tubes of larger diameter than those at
present in use and which would result in simpler and cheaper design
of the steam distribution manifold system is not practicable since
their use would increase the overall height of the unit. Such
height increase would lead to a considerable increase in cost of
the support structure for the steam manifolds and banks of tubes.
Such additional cost would reduce or nullify any benefit brought
about by the use of such longer tubes of larger diameter.
2. Since the economic limit of tube length for the above reason is
less than 20 ft. or thereabouts and since it is normal when using
force draft to use fans as large as possible (up to diameters of 20
ft. or thereabouts) it is not economically possible with this
arrangement to achieve a design which ensures that each tube of the
condenser is served by air from more than one fan whilst using fans
of optimum size. This means that, if a fan has to be shut down for
any reason, the whole of a tube bank will become inoperative.
3. Since it is not regarded as good design practice to allow the
condensate to fall back into the entering steam it is necessary to
connect the manifold distribution system to headers at the upper
ends of the tubes. This leads to long manifolds and to an expensive
support structure for the manifolds due both to the large diameter
of the manifolds and to their positions at or near to the highest
point of the condenser.
4. Since the size and shape of a pair of tube banks forming an
A-frame unit is such as to preclude the possibility of shop
assembling such a unit for easy road or rail transport expensive
field assembly is required. Also since the steam distribution
manifolds are mounted on the tops of the tube banks the manifolds
cannot be placed in position until the tube banks are in
position.
5. Each bank of tubes normally consists of a number of tube rows
and during winter operation there is danger of freezing of the
condensate in the tubes due to the fact that the condensate is
mainly formed in the lower rows of tubes which are exposed to the
cooler part of the air flow over the tubes.
It is an object of the invention to provide a direct,
sub-atmospheric steam condenser in which the first four of the
above disadvantages are avoided and in which, if desired, simple
means may be provided for overcoming the fifth disadvantage.
According to the invention we provide a steam condenser having
horizontal steam condenser tubes through which steam is passed at
sub-atmospheric pressure while cooling air passes over the external
surfaces of said tubes; comprising at least one pair of banks of
tubes, the banks in each pair being mutually inclined and
converging upwardly; a steam inlet header connected to one end of
each bank and a further header connected to the other end of each
bank; suction means connected to said headers; drain means arranged
to drain condensate from at least one of said headers for each bank
of tubes; and a steam manifold connected to said steam inlet
headers, the manifold being arranged below the tops of the
banks.
When we say that the tubes are substantially horizontal, we mean
that the tubes make an angle of no more than 5.degree. with the
horizontal. A slight slope of this nature may be desirable to
assist the condensate to flow out of the tubes into the condensate
headers.
A condenser embodying the invention has the following advantages as
compared with the known type of steam condenser referred to
above:
1. The use of larger diameter and hence longer tubes is quite
practicable and this enables shorter and more compact steam
distribution manifolds to be used. Thus the larger the diameter of
a tube in a condenser of this type the longer it can be and the
less manifolding will be required due to the reduced number of
tubes. Also since the manifolds are mounted at a level below the
tops of tube banks (if desired below the banks) this reduces the
length of the steam manifolds which lead up from a turbine mounted
at a lower level than the condenser and whose exhaust is fed to the
condenser.
2. Since it is practicable to use tubes of 30 ft. or more in length
it is quite feasible to arrange for each tube to be fed by air from
two or more fans whilst still using optimum fan sizes. This means
that at least 50 percent of each tube bank can still be operated
whilst any one fan is out of action.
3. Since the manifolds are mounted at a level beneath the tops of
the tube banks this enables a more economical support structure to
be used, and also enables the manifolds to be erected prior to the
erection of the tube banks.
4. Since the tubes are horizontal it is also quite feasible to
arrange pairs of banks into A-frames whose base width is of the
order of 12-14 ft. and which can be completely shop assembled and
transported by road or rail ready for directly mounting on to a
simple support structure. This reduces erection time and the
complexity and the cost of the support structure. This is possible,
if, e.g., the capacity of an electric generating station including
the condenser is between 6 and 30 Megawatts whereas for larger
stations it may be necessary to assemble the tubes into the headers
on site.
The steam manifolding may be arranged in the lower half of the
condenser above the bottoms of the banks. Alternatively, the steam
manifolding may be arranged below the banks with upwardly extending
connections between the manifolds and the headers.
The cooling air may be caused to flow over the tubes either by
forced or natural draught. If forced draught is used then there is
provided, beneath the banks, a plurality of fans rotatable about
vertical axes. If natural draught is used, there is provided a
tower with peripherally extending means between the lower end of
the tower and the ground so that said lower end is spaced above the
ground. Air thus flows into the base of the tower between the
bottom of the tower and the ground and then upwardly through the
banks of tubes.
Various pass arrangements are possible with a condenser embodying
the invention. In a first, or partial co-current, pass arrangement
steam passes first along the tubes of a lower part of each bank and
then flows back along an upper part of the bank. In this
arrangement, the inlet header may be divided by a pass plate or
other means. Since the final stages of the condensation take place
in the second pass, i.e., in the upper part of each bank, the
danger of freezing is reduced since these upper parts of the banks
are heated by the warmer air passing through the condenser.
This partial co-current arrangement constitutes a major advantage
over a single pass arrangement particularly when using the
condenser in very cold climatic conditions. As compared with known
condensers of the type specified cheaper control systems are
possible for maintaining the desired vacuum in the condenser and
savings in the power required to drive the fans (where provided)
may be achieved during operation at low temperatures. During the
final stages of condensation, air which is unavoidably drawn into
the system at the turbine represents an appreciable volume of the
gas flowing through the condenser and the known phenomenon of
"vapour blanketing" takes place in which an insulating layer of
non-condensable gas flows adjacent to the tube wall thus reducing
the rate of condensation. A substantial temperature difference may
build up across this insulating layer so that the tube wall may
fall to freezing temperatures whilst the bulk steam temperature of
the gas flowing in the tube is in excess of the freezing point. For
this reason it is a considerable advantage not to allow very cold
air in contact with the outside of the tube whilst condensing under
these conditions.
Prevention of tube blockage due to frozen condensate may be
prevented by simple control schemes with this pass design and in
moderate climatic conditions only fan switching may be
required.
Alternatively, the steam may make a single pass through each bank
and then proceed through a secondary bank at another part of the
condenser. Thus there will be a number of primary banks through
which the steam first flows and a number of secondary banks fed
from the primary banks. Normally a number of primary banks will
feed a single secondary bank.
If desired, each header may be formed as a rolled box section each
having secured thereto two rows of tubes. The tubes are externally
fillet welded to the headers. If it is desired to make each bank of
three or more rows of tubes then each header may be formed of a
plurality of box sections, two in the case of three rows of tubes,
one header supporting the third row of tubes. Connections will be
provided between the parts of the same header which are constituted
by different rolled sections.
Alternatively fabricated box sections may be used with plugs
opposite each tube or removable cover plates for tube fixing,
inspection and maintenance.
One of the problems encountered in direct steam condensers is
corrosion of the tubes. If the tubes of the normal external
diameter used, e.g. 1 - 11/2, have their walls thickened to resist
corrosion then the flow area for the steam is reduced below a
desirable value.
An advantage is gained if tubes which have an increased wall
thickness and external diameter are used so that the tubes still
provide sufficient flow area for the steam and sufficient wall
thickness to resist corrosion. We prefer to use tubes having an
external diameter of between 11/2 and 3 inches.
The extended surface of the tubes will normally be provided by
fins. These fins may be secured to the tube in any of the known
methods for example by first grooving the tube and then inserting
an edge of a helically wound strip of material into the groove and
closing the groove to grip the strip.
Alternatively, a helically wound strip of L-section may be secured
to the external surface of the tube.
Embodiments of the invention will now be described in detail by way
of example with reference to the accompanying drawings, in
which:
FIG. 1 is a side view of a bank of tubes in a condenser embodying
the invention;
FIGS. 2 and 3 are views in the directions of the arrows X and Y in
FIG. 1 of the return and inlet headers respectively of the bank of
FIG. 1;
FIGS. 4, 5 and 6 are plan, side and end views respectively of a
condenser embodying the invention;
FIG. 7 is a plan view of a condenser having a different arrangement
of banks of condenser tubes;
FIGS. 8 to 11 are detail views of the ends of banks of tubes
employed in the arrangement of FIG. 7;
FIG. 12 is a vertical sectional view taken on line 12--12 in FIG.
13 of a natural draught cooling tower having a steam condenser
according to the invention;
FIG. 13 is a plan view of the steam condenser mounted in the
cooling tower of FIG. 12; and
FIG. 14 is a schematic view of a steam operated plant.
Referring now to the drawings, a direct, subatmospheric steam
condenser embodying the invention comprises a rectangular frame 10
which is supported above either the ground, or the roof of a
building such as a turbine house, by means of a plurality of
upright columns 11. Mounted on the top of rectangular frame 10 are
a number of pairs 13 of banks 14 of tubes 15. Each bank is similar
and comprises three rows of finned tubes (FIGS. 2 and 3) which are
arranged with their centre lines generally horizontal, the rows
being inclined to the vertical. The tubes preferably have an
outside diameter of between 11/2 and 3 inches for the reasons set
forth above. At each end, each tube is secured to a header 16 or 17
by conventional tube sheet practice. The two banks 14 of a pair
converge upwardly as shown in FIG. 5 and the tubes lie parallel to
two opposite sides 18 of the rectangular framework 10.
Substantially the whole area of the framework is covered with
longitudinally extending rows of pairs 13 of banks of tubes
arranged in four lateral rows 19, 20, 21 and 22.
Two steam manifolds 23 are provided each extending parallel to one
of the other sides 24 of the framework and arranged below, but
aligned with the gap between, the rows of each outer pair of rows
19, 20 and 21, 22. The manifolds are fed from their one ends 25 and
each has outlets or feed pipes 26 (see FIGS. 1 and 3) extending
upwardly to the headers 16 at those ends of the banks adjacent the
manifold. The outlets connect to nozzles in the headers which feed
the steam from the manifold into headers.
Suspended below the framework are a number of fans 27 with driving
motors 28 and which are rotatable about vertical axes and serve to
entrain air and pass it upwardly over the tubes of the banks. It
will be seen from FIGS. 4 and 5 that two fans such as 27a supply
air to each bank of each pair 13 so taht if one fan should fail or
be turned off the other fan still impels air over the tubes of the
banks 13.
Various pass arrangements may be provided. Assuming that, as shown
in FIGS. 1 to 3, the first arrangement described above is used, the
steam passes first along the tubes in a major part of each bank
from the header 16 to the header 17 and then back from the header
17 to the header 16 along the tubes in an upper part of the bank.
The inlet headers 16 which are connected to the steam manifolds 23
are divided by pass plates 29 so that the steam is directed into
the tubes in the lower major part of each header. Condensate drain
means 30 and 31 are respectively provided in each return header 17
and in the part 32 of each inlet header 16 separated from the main
part thereof by the pass plate 29. The drain means 30 communicate
with condensate headers 33 shown in FIGS. 1, 2, 4, 5 and 6 and the
drain means 31 with condensate headers 34 shown in FIGS. 1, 3, 5
and 6. The parts 32 of the inlet headers 16 are connected to vent
manifolds 35 connected to a vacuum source to remove the
non-condensable gases.
Referring now to FIGS. 7 to 11, there is shown a construction of
steam condenser employing pairs of banks of condenser tubes which
are somewhat similar to the banks of tubes previously described,
and corresponding parts will be designated by the similar
references. However, the connections to the headers of the banks of
tubes and the flow paths for the steam are somewhat different.
Referring to FIG. 7, it will be seen that the steam condenser
comprises the lateral rows of banks of tubes 19, 20, 21 and 22, and
also includes 16 longitudinal rows of pairs of banks of tubes. The
pairs of banks of tubes in each longitudinal row are spaced axially
from each other to provide the four lateral rows 19 to 22 and the
two steam manifolds 23 extend between rows 19 and 20 and 21 and 22
in similar manner as described with reference to FIG. 4.
In FIG. 7, the reference B and A designate respectively sections of
primary and secondary banks of tubes. The banks of tubes in the
section B constitute the primary banks fed with steam from the
manifolds 23 and the banks of tubes in Sections A constitute the
secondary banks which are fed with uncondensed steam from the
primary banks. The corresponding parts in the construction of the
bank of tubes in sections A and B to the members described with
reference to FIGS. 1 to 6 will be designated with the letter A or B
accordingly.
Referring now to FIGS. 8 and 9, there are shown end views of a bank
of tubes as employed in a section B. The staem inlet header is
shown in FIG. 9 and is designated by reference 16 B and is supplied
with steam from steam manifold 23 through outlets or feed pipes
26B. However, steam inlet header 16B does not have a pass plate or
drain means as in the previously described construction.
Turning now to FIG. 8, this shows the header 17B at the other end
of the bank of tubes and this has drain means 30B which
communicates with condensate header 33B. Also header 17B has a
steam outlet 38 by which uncondensed steam from the primary bank
(Section B) may pass to the secondary bank (Section A) by way of an
interconnecting manifold 39.
Referring now to FIGS. 10 and 11, there are shown the headers at
each end of a bank of tubes as used in a Section A. The steam inlet
header 16A is supplied with uncondensed steam from the primary bank
by way of inter-connecting manifold 39 and outlets or feed pipes
26A. The uncondensed steam from Section B passes down the secondary
bank comprised by Section A and is condensed therein and passes to
header 17A (FIG. 11) at the other end of the bank of tubes.
Condensate drains off by way of drain means 30A and condensate
header 33A. A vent manifold 35A is connected to the header 17A and
serves to place the steam under sub-atmospheric pressure throughout
the condenser.
Returning now to FIG. 7, the flow path for the steam sas it passes
from the two steam manifolds 25 is indicated by the arrows in the
figure from which it will be apparent that the steam passes
initially through the pairs of primary banks in the Sections B
where it undergoes a partial condensation, and then passes to the
pairs of secondary banks in Section A where the condensation is
completed. The arrangement may be provided with fan units similar
to the fan units 27 to provide forced draught cooling, or the
arrangement may be mounted in a natural draught cooling tower.
Referring now to FIGS. 12 and 13, there is shown a steam condenser
according to the invention mounted in a natural draught cooling
tower. The structure of the cooling tower is indicated generally by
reference numeral 40 and the steam condenser indicated generally by
reference numeral 41 is mounted above the ground in the lower
portion of the tower. The supporting framework 10 of the condenser
is supported by struts 11 and the steam condenser 41 is indicated
only schematically but comprises pairs of banks of tubes 13. The
construction and arrangement of the steam condenser may be as
described with reference to FIGS. 1 to 6 though of course without
the provision of the fan units 27 to provide the forced draught, or
the arrangement described with reference to FIGS. 7 to 11 may be
employed.
Referring to FIG. 14, there is shown schematically a steam powered
plant comprising a steam generator 42 which supplies steam under
pressure to a steam turbine 43. Exhaust steam is fed from the
turbine to a steam condenser 44 which then recycles condensed steam
to the steam generator. The steam condenser shown in FIG. 14 may
comprise a forced draught steam condenser installation. as shown in
FIGS. 1 to 6 or FIGS. 7 to 11, or may comprise a natural draught
tower and steam condenser installation as shown in FIGS. 12 and
13.
It will be seen from the foregoing description that the condenser
can be made of comparatively small height since the tubes are
horizontal and the steam manifolds are arranged below the banks as
shown. Thus the heights of the banks between horizontal planes
containing the lines 36 and 37 in FIG. 5 is of the order of 12 to
14 ft. as compared with the corresponding height of approximately
25 ft. above a similar frame which is required by the known type of
condenser referred to above.
In condensers embodying the invention a multiplicity of small
A-frames will normally be employed where one large A-frame may have
been used in previously known designs. A windshield may not be
required in a condenser embodying the invention because only the
outermost banks are seriously affected by wind. In previous designs
a very much larger portion of the condenser could be subjected to
the effect of wind. Various modifications may be made to the
invention Thus instead of having three rows of tubes in each bank
there may be two rows. The headers may be formed of rolled box
sections. If there are only two rows of tubes per bank then one box
section will serve both rows of tubes which may be externally
welded by fillet welds to a wall of the header. If three rows of
tubes are used, there will have to be two box sections which
together form each header, the box sections being inter-connected
by steam pipes. The pass arrangement may be as described above with
primary and secondary banks.
* * * * *