U.S. patent number 3,731,735 [Application Number 05/126,174] was granted by the patent office on 1973-05-08 for selective orificing steam condenser.
This patent grant is currently assigned to Ecodyne Corporation. Invention is credited to Kenneth B. Ris.
United States Patent |
3,731,735 |
Ris |
May 8, 1973 |
SELECTIVE ORIFICING STEAM CONDENSER
Abstract
An air cooled steam condenser having plate means or a series of
plates mounted within the steam intake header compartment. The
plate means in effect form a series of interconnected subchambers,
each of which communicates with a row of cooling tubes in which
steam is condensed by a stream of cooling air flowing over, around
and past the tubes. The rows of tubes extend transversely of the
direction of airflow and the rows extend perpendicular to the
direction of airflow at spaced intervals. An opening is formed in
each plate through which steam flows between sub-chambers. The
openings are smaller in area in successive plates in the header
through which the steam flows so that only that amount of steam
that can be condensed effectively within the tubes in any row,
enters such row, having regard to the tube length and the
temperature difference at the particular row which determines the
cooling effect of the airflow over the successive rows of
tubes.
Inventors: |
Ris; Kenneth B. (Massillon,
OH) |
Assignee: |
Ecodyne Corporation (Chicago,
IL)
|
Family
ID: |
22423388 |
Appl.
No.: |
05/126,174 |
Filed: |
March 19, 1971 |
Current U.S.
Class: |
165/110; 165/146;
165/174; 165/DIG.222 |
Current CPC
Class: |
F28B
1/06 (20130101); F28B 11/00 (20130101); F28F
27/02 (20130101); Y10S 165/222 (20130101) |
Current International
Class: |
F28B
1/00 (20060101); F28B 1/06 (20060101); F28f
013/00 (); F28b 001/06 () |
Field of
Search: |
;165/174,111,146,110,147 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
1,291,617 |
|
Mar 1962 |
|
FR |
|
908,806 |
|
Oct 1962 |
|
GB |
|
Primary Examiner: Davis, Jr.; Albert W.
Claims
I claim:
1. In a steam condenser of a type in which a plurality of tubes are
arranged in a plurality of generally parallel rows, extending
between and communicating with a steam inlet header and a
condensate outlet header; and in which the rows of tubes extend
transversely of and at spaced intervals perpendicular to the
direction of airflow of cooling air that passes over and around the
rows of tubes to condense steam flowing through the tubes from the
inlet to the outlet header; the steam inlet header having a chamber
and inlet means for said chamber; partition means mounted within
said chamber dividing the chamber into a series of metered steam
zones each communicating with at least one row of tubes; said
partition means including a plurality of partition plates which
divide said chamber into a plurality of sub-chambers which form
said series of metered zones; said partition plates having openings
formed therein in facing relationship to said inlet means; said
openings in successive plates being successively smaller and
concentric with one another so as to distribute inlet steam in said
chamber in successively smaller amounts to each successive zone
corresponding to the reduced cooling effect of the airflow of
cooling air passing successively over the spaced rows of tubes to
which steam is distributed from successive zones.
2. The construction defined in claim 1 in which the inlet header
includes a tubesheet and a plug sheet; in which the plates are
mounted on and extend between said tubesheet and plug sheet; and in
which each plate is mounted between a pair of adjacent tube rows.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to heat exchangers and in particular to air
cooled steam condensers. More particularly the invention relates to
orificing means mounted within the condenser header whereby the
amounts of steam entering various rows of condensing tubes are
metered or reduced proportionally to the reduced cooling effect of
the cooling air due to increased cooling air temperature resulting
from heat extracted from tubes previously cooled, so that only that
amount of steam that can be cooled efficiently is supplied to the
tubes of a particular row.
2. Description of the Prior Art
Air cooled steam condensers usually include a plurality of
condenser tubes arranged in rows one behind the other in the
direction of airflow of the cooling air. Steam enters the condenser
inlet header which communicates with the inlet ends of the tubes
and then flows through the tubes wherein it is condensed. Fan blow
cooling air across the tubes in an airflow direction generally
perpendicular to the rows of tubes. The steam is condensed by the
cooling air to form condensate as it travels through the tubes, and
the condensate is collected at the outlet ends of the tubes in any
suitable manner. Condensation should take place throughout the
length of the tubes for most efficient condenser operation.
Problems have arisen in the construction and operation of air
cooled steam condensers as described in U.S. Pat. No. 3,073,575
relating to inefficient steam feed distribution to the cooling
tubes, temperature differential changes due to changing weather
conditions, etc. The various solutions to such problems suggested
in said U.S. Pat. No. 3,073,575, however, are complicated in
structure and expensive in execution.
No air cooled steam condenser constructions of which I am aware
have eliminated the problems of uneven steam distribution by
efficiently metering or distributing the steam within the condenser
inlet header by simple partition means using simple finned
condenser tubes in all rows of the condenser having the same
structure and characteristics as to diameter, length and cooling
fin surface.
SUMMARY OF THE INVENTION
Objectives of the invention include providing selective orificing
for steam condensers which meters the amounts of steam flowing to
and through the cooling tubes in tube rows of the condenser,
proportional to the condensing ability of the tubes in any
particular tube row; providing selective orificing for steam
condensers having condenser tubes all of which are the same in
length, passage cross section, number of fins, and total heat
exchange surface area; providing selective orificing for steam
condensers in which plates having openings of varying sizes are
mounted within the condenser inlet header for selective
distribution of steam; providing selective orificing for steam
condensers permitting existing condenser designs to be converted
easily and inexpensively to establish predetermined metered
distribution of steam to the several rows of cooling tubes in the
condenser; and providing selective orificing for steam condensers
which eliminate difficulties heretofore encountered, achieve the
stated objectives simply and effectively, and solve problems and
satisfy existing needs.
These objectives and advantages are obtained by the selective
orificing construction for steam condensers, the general nature of
which may be stated as including in a steam condenser for
condensing steam in a plurality of tubes arranged in a plurality of
generally parallel rows, extending between and communicating with a
steam inlet header and a condensate outlet header; the rows of
tubes extending transversely of and at spaced intervals
perpendicular to the direction of airflow of cooling air that
passes over and around the rows of tubes to condense steam flowing
through the tubes from the inlet header; the steam inlet header
having a chamber and inlet means for said chamber; partition means
mounted within the chamber dividing the chamber into a series of
metered steam zones each communicating with at least one row of
tubes; said partition means being constructed to distribute inlet
steam in the chamber in successively smaller amounts to each
successive zone corresponding to the reduced cooling effect of the
airflow of cooling air passing successively over the spaced rows of
tubes to which steam is distributed from successive zones; means
preferably including a plurality of partition plates dividing the
chamber into a plurality of sub-chambers forming said successive
zones and communicating respectively with successive rows of tubes;
an opening formed in each plate for supplying steam from one
sub-chamber zone to the adjacent sub-chamber zone; and the openings
in successive plates between adjacent sub-chamber zones being
successively smaller.
In the alternative the partition means may include a partition
plate located in the inlet header angularly with respect to the
tubesheet at the inlet ends of the rows of tubes; and said angular
plate defining in said header a passage and a series of
successively smaller tube inlet zones communicating respectively
with successive rows of tubes.
BRIEF DESCRIPTION OF THE DRAWINGS
Preferred embodiments of the invention -- illustrative of the best
modes in which applicant has contemplated applying the principles
-- are set forth in the following description and shown in the
drawings and are particularly and distinctly pointed out and set
forth in the appended claims.
FIG. 1 is a perspective view, with portions broken away, showing an
air cooled steam condenser equipped with the improved selective
orificing plate construction;
FIG. 2 is a diagrammatical side elevation of the steam condenser
shown in FIG. 1;
FIG. 3 is an enlarged fragmentary top plan view, with portions
broken away and in section, looking in the direction of arrows
3--3, FIG. 2 and showing one condenser section;
FIG. 4 is a sectional view taken on line 4--4, FIG. 3;
FIG. 5 is an enlarged sectional view taken on line 5--5, FIG.
3;
FIG. 6 is a further enlarged fragmentary sectional view taken of
line 6--6, FIG. 5;
FIG. 7 is a fragmentary top plan view, with portions broken away
and in section, showing a modified steam condenser construction
having a cylindrical steam drum or header equipped with improved
selective orificing plate means;
FIG. 8 is a sectional view taken on line 8--8, FIG. 7;
FIG. 9 is an enlarged fragmentary sectional view taken on line
9--9, FIG. 7; and
FIG. 10 is a view similar to FIG. 9 showing a modified form of
construction .
Similar numerals refer to similar parts throughout the
drawings.
DESCRIPTION OF PREFERRED EMBODIMENTS
First Embodiment
A typical air cooled heat exchanger is indicated at 1, (FIG. 1 and
2) and includes two steam condenser sections 2 and 3 supported on
frame members 4 and having side and end panels 5 mounted on the
frame members 4. Fans 6 mounted on pedestals 7 beneath condenser
sections 2 and 3 blow cooling air (indicated by arrows A, FIG. 2)
upward through sections 2 and 3.
A steam supply manifold 8 communicates with a source of steam, such
as the exhaust of a steam turbine, to be condensed, and pipes 9
form steam inlets for the individual sections 2 and 3 from manifold
8. Condensate outlet lines 11 are connected to the opposite ends of
sections 2 and 3 and deliver condensate into a main condensate line
12.
Different heat exchanger installations may have a different number
of condenser sections 2 and 3 assembled together. The operation and
function of condenser sections each having the improved selective
orificing means incorporated therein are similar. Therefore only
one condenser section 2 (FIGS. 3-6) is described in detail.
Condenser section 2 includes a plurality of cooling tubes 13
preferably having helical fins 14 extending outward therefrom.
Tubes 13 are mounted within a frame having side channels 10, an
inlet header 15 and an outlet header 16.
Tubes 13 are mounted parallel to each other within the frame in a
plurality of rows 17, 18, 19 and 20 spaced one above the other
(FIGS. 4, 5 and 6) arranged in that order along the direction of
flow indicated by the arrow A. Tubes 13 in a particular row may be
spaced intermediate the tubes in the adjacent rows, above and
below, as shown in FIG. 5. Likewise, tubes 13 are assembled within
the frame so as to have a slight incline from inlet header 15 to
outlet header 16 so that condensate flows or drains into header
16.
Inlet header 15 may have a welded construction as shown in U.S.
Pat. No. 3,582,599 (Ser. No. 748,311) of Melvin G. Yohn. Such
construction may include a generally rectangular cross section
formed by top and bottom walls 21 and 22, tubesheet 23, plug sheet
24, and end walls 25. The inlet ends of tubes 13 are connected in a
usual manner by expending or welding in tubesheet 23; and holes 27
in plug sheet 24 aligned with tubes 13 permit access into header 15
and tubes 13 for expending or welding tubes 13 into the header and
for cleaning and for removing any obstructions that may form in
tubes 13.
A flanged coupling connected to header bottom wall 22 forms a steam
inlet opening 30 for header 15. Coupling 29 has a flange 31 for
connection with steam inlet pipe coupling 32 of pipe 9 by bolts
32a.
Condensate outlet header 16 may be constructed similar to header 15
having aligned holes 33 and 34 formed in tubesheet 35 and plug
sheet 36 for expanding or welding the outlet ends of tubes 13 in
holes 33 and for removable plugs 37 for access holes 34. Outlet
opening 38 in bottom wall 39 of header 16 is connected by flanged
coupling 40 with coupling 41 on condensate outlet line 11.
In accordance with the invention a plurality of partition plates
42, 43 and 44 are mounted within header 15 extending between
tubesheet 23 and plug sheet 24 and attached by welds 45. The plates
42, 43 and 44 are parallel to each other and to bottom wall 22, and
are mounted between tube rows 17 and 18, 18 and 19, and 19 and 20,
respectively. Thus sub-chambers 46, 47, 48 and 49 are formed within
header 15. Openings 50, 51 and 52 are formed in plates 42 and 43
and 44, respectively, with opening 50 being larger in area than
opening 51, and opening 51 being larger in area than opening 52.
The openings 50, 51 and 52 are shown as being circular. However,
they may have any desired shape to obtain the required area and may
be square, rectangular or elliptical.
Steam flow, indicated by arrow B (FIG. 6), enters header 15 through
distribution pipe 9 and inlet opening 30. The amount of steam that
passes through sub-chambers 46-49 and subsequently rows 17-20 of
tubes 13, respectively, becomes decreasingly smaller due to the
decreasing size of openings 50-52.
Therefore, a larger amount of steam B.sub.1 enters the tubes in row
17 for condensation therein than the reduced amount of steam
B.sub.2 entering tube row 18, and likewise the further reduced
amounts of steam B.sub.3 and B.sub.4 entering tube rows 19 and 20.
This continual reduction in amounts of steam entering succeeding
tube rows of similar tubes spaced along the direction of flow A of
the cooling air, is a characteristic of the concept of the
invention. This compensates for the continual increase in
temperature of the air and the decreasing mean effective
temperature difference as the air passes from row 17 over the
subsequent rows 18-20 picking up heat from the previously cooled
rows of tubes.
The areas of openings 50-52 are determined in designing any
particular installation by taking into consideration factors
including the average pressure and temperature of the steam
entering header 15, the velocity and average temperature of cooling
air flowing at A past the tubes 13, and the total finned heat
exchange cooling surface of tubes 13. Ideally, the areas of
openings 50-52 will be such that the amounts of steam B.sub.1
-B.sub.4 entering the respective rows 17, 18, 19 and 20 of tubes 13
will be completely condensed as steam flow in any tube 13 reaches
the outlet header 16.
Second Embodiment
A modified selective orificing steam condenser construction
indicated at 53 is shown in FIGS. 7-9 having a cylindrical steam
manifold or header 54 provided with a header inlet section 55
communicating with the inlet tubesheet 63 of the condenser. Header
54 is mounted in a cradle support structure 56, and header section
55 may be formed by plates 57, 58, 60 and 61 secured by welds 59 to
header 54.
Header section 55 is provided with a flange 62 which is connected
in a suitable manner with tubesheet 63, as shown in FIG. 9. The
connection may be sealed by a gasket 64.
Rows of tubes 65-68 each having a plurality of tubes 69, have their
inlet ends connected to tubesheet 63 and communicate with header
inlet section 55. Tubes 69 otherwise are arranged like tubes 13 in
condenser 1 and cooling air flows past tubes 69 as indicated at
C.
A partition plate 70 is mounted within the header inlet section 55
of the header compartment of header 54, preferably by welding the
plate 70 at 71 to header inlet section plates 60, 57 and 58 (FIG.
9). Plate 70 extends outwardly downwardly at an angle away from
tubesheet 63, and the lower or free edge 70a of plate 70 is spaced
above plate 61 of header section 55 to form a passage 73
communicating between the header compartment and header sub-chamber
72 located between partition plate 70 and the inlet ends of tubes
69.
The angular arrangement of partition plate 70 with respect to
tubesheet 63 forms a series of zones in sub-chamber 72 of
decreasing size from bottom to top (FIG. 9) opposite the inlet ends
of the rows 65, 66, 67 and 68 of tubes 69. This series of zones of
decreasing size meters the amounts of steam flowing into tube rows
65-68 in decreasing amounts, as indicated at D-1, D-2, D-3 and D-4,
and distributed from the main steam flow indicated at D entering
the sub-chamber 72 from the inlet header 54.
Partition plate 70 thus forms partition means defining in the
header 54 and header section 55 a passage 73 and a series of
successively smaller tube inlet zones communicating respectively
with the successive rows of tubes 65-68.
The amounts of steam entering the various rows can be changed by
changing the angle of projection of plate 70, thereby changing the
capacity of sub-chamber 72. The flow C of cooling air is in a
direction across the rows 65-68 of tubes 69 such that row 65, which
receives the greatest amount of steam, is cooled by the coolest
air. If for some reason the direction of airflow C is from top to
bottom in FIG. 9, plate 70 would project upwardly outwardly with
respect to tubesheet 63 from plate 61.
Third Embodiment
The construction shown in FIG. 10 is similar to that shown in FIG.
9 excepting that the partition plate 74 may be curved, as shown,
rather than a flat plate 70 as illustrated in FIG. 9. The curved
shape may be designed so that the respective series of zones of
decreasing size in sub-chamber 75 will have the required size or
volume to obtain the steam distribution pattern to be achieved in
the design of the sub-chamber 75.
IN GENERAL
In each of the embodiments of the invention illustrated in the
drawings and described above, partition means is provided within
the inlet header to distribute the incoming steam in decreasing
amounts of successive rows of cooling tubes so that the row of
tubes first cooled by the coolest airflow receives the greatest
amount of steam and subsequent tube rows along the path of airflow
receive proportionally decreasing amounts of steam. Any individual
row of tubes therefore receives only that amount of steam that can
be condensed throughout its length, eliminating premature or
insufficient condensation within the tubes, while using tubes all
identically the same in the construction of the condenser.
Accordingly, the selective orificing steam condenser construction
provides for progressively reducing the amount of steam passing
through header zones so as to correspond to the location of the
rows of tubes in the path of flow of cooling air; enables condenser
tubes having the same length, the same passage cross section, the
same number of fins and the same total heat exchange surface to be
used in fabricating the condenser; enables many designs of steam
condensers to be easily and inexpensively converted to include the
improved selective orificing construction; enables maximum
efficiency to be achieved in the operation of the condenser;
prevents premature condensation which may result in frozen
conditions during cold weather; and provides such a construction
which is effective, safe, inexpensive, and efficient in assembly,
operation and use, and which achieves all the enumerated
objectives, provides for eliminating difficulties encountered with
prior devices, and solves problems and obtains new results in the
art.
In the foregoing description, certain terms have been used for
brevity, clearness and understanding but no unnecessary limitations
are to be implied therefrom beyond the requirements of the prior
art, because such terms are used for descriptive purposes and are
intended to be broadly construed.
Moreover, the description and illustration of the invention is by
way of example, and the scope of the invention is not limited to
the exact details of the construction shown or described.
Having now described the features, discoveries and principles of
the invention, the manner in which the improved selective orificing
steam condenser is constructed, assembled and operated, the
characteristics of the new construction, and the advantageous, new
and useful results obtained; the new and useful structures,
devices, elements, arrangements, parts, and combinations are set
forth in the appended claims.
* * * * *