U.S. patent number 3,692,096 [Application Number 05/133,318] was granted by the patent office on 1972-09-19 for boiler plant including two rotary regenerative air preheaters.
This patent grant is currently assigned to Swenska Rotor Maskiner Aktiebolag. Invention is credited to Bo Johnsson, Birger Pettersson.
United States Patent |
3,692,096 |
Pettersson , et al. |
September 19, 1972 |
**Please see images for:
( Certificate of Correction ) ** |
BOILER PLANT INCLUDING TWO ROTARY REGENERATIVE AIR PREHEATERS
Abstract
In a boiler plant including two rotary regenerative air
preheaters connected in parallel in conduits branched off from main
air and gas ducts are provided flow distributing damper means
controllable such as to keep the discharge temperatures of the gas
flows from the preheater at the same value.
Inventors: |
Pettersson; Birger (Alta,
SW), Johnsson; Bo (Kungsbacka, SW) |
Assignee: |
Swenska Rotor Maskiner
Aktiebolag (Nacka, SW)
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Family
ID: |
10099106 |
Appl.
No.: |
05/133,318 |
Filed: |
April 12, 1971 |
Foreign Application Priority Data
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Apr 14, 1970 [GB] |
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17,666/70 |
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Current U.S.
Class: |
165/7; 110/190;
122/DIG.1; 165/101; 110/308; 122/1A; 165/296 |
Current CPC
Class: |
F28D
19/04 (20130101); F23L 15/02 (20130101); F24F
2203/104 (20130101); Y02E 20/34 (20130101); Y10S
122/01 (20130101); F24F 2203/1072 (20130101); F24F
2203/1084 (20130101); Y02E 20/348 (20130101) |
Current International
Class: |
F23L
15/00 (20060101); F23L 15/02 (20060101); F28D
19/04 (20060101); F28D 19/00 (20060101); F28d
019/00 () |
Field of
Search: |
;165/7,4,10,101,34
;122/DIG.1,1A ;110/56 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
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717,782 |
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Nov 1954 |
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GB |
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592,483 |
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May 1925 |
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FR |
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209,356 |
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Jun 1960 |
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DT |
|
Primary Examiner: Davis, Jr.; Albert W.
Claims
What we claim is:
1. A boiler plant including two rotary regenerative air preheaters
connected in parallel in conduits branched off from a main air duct
and a main gas duct, characterized by adjustable damper means
positioned in the main gas duct upstream of the preheaters for
controlling the distribution of gas flow between the two
preheaters.
2. A boiler plant as defined in claim 1 in which temperature
sensing means are provided in the gas outlet conduit of each
preheater and the damper means is adapted to be actuated by an
adjusting device controlled by said temperature sensing means in
such manner as to keep the temperatures in the gas outlet conduits
at the same value.
3. A boiler plant as defined in any of the preceding claims in
which each preheater is associated with means for by-passing at
least part of the air flow passing through the air branch
conduit.
4. A boiler plant as defined in claim 3 in which the by-pass means
include adjustable dampers interconnected in such manner as to
change the rate of air flow through the preheaters to the same
degree in both preheaters.
5. A boiler plant as defined in claim 4 in which an adjusting
device for the dampers is controlled by means responsive to the
mean temperature of the gas leaving the preheaters whereby to keep
said temperature at a desired level.
Description
This invention relates to boiler plants which include two rotary
regenerative air preheaters connected in parallel in conduits
branched off from main air and gas ducts.
Even though the two preheaters are of identical general
construction they almost never have the same characteristics. For
instance, they may present different resistances to flow and
different tendencies to accumulate soot and ash. Further, the flow
patterns in the ducts and branch conduits may also be different.
All these differences result in different heat transfer conditions
so that the temperature drop of the gases is not the same in the
two preheaters.
Of course it is desireable to utilize the heat contents of the
gases to the greatest possible extent. However, for certain reasons
the gas temperature at the outlet from the preheater must not lie
below a predetermined minimum value which may be different for
different plants. On the other hand, the discharge temperature of
the gas must not be much higher than this minimum temperature but
lie at or closely above said temperature. It is evident that if the
discharge temperatures of the gas flows from the two preheaters are
different the heat contents of the gas flow of the higher
temperature will not be sufficiently utilized.
According to the invention there is provided an adjustable damper
means for controlling the distribution of the main flow of one of
the fluids between the two preheaters. Such damper means makes it
possible to keep the discharge temperatures of the gas flows from
the preheaters at the same value under all operating conditions
irrespective of differences in the characteristics of the
preheaters, flow patterns etc. The magnitude of this value may be
controlled in any suitable manner.
If the damper means is provided in the air system the control of
the temperature level may be accomplished by by-passing a
controllable portion of the total air flow. However, preferrably
the damper means is provided in the gas system while each preheater
is associated with means for by-passing at least part of the air
flow passing through its air branch conduit.
The invention will now be described more in detail with reference
to the accompanying drawing which diagrammatically illustrates an
embodiment of a preheater section of a boiler plant according to
the invention.
The preheater section shown in the drawing includes two air
preheaters 10 of the well-known Ljungstrom type and of identical
design each comprising a rotatable matrix and stationary air and
gas conduit connections.
Flue gases from the boiler are supplied to the preheater section
through a main supply duct 12 which divides into two branch
conduits 14, one for each preheater 10. After having passed through
the preheaters 10 the gases are discharged through conduits 16
which merge into a main discharge duct 18.
Air is supplied through two supply ducts 20, one for each preheater
10, and is discharged through discharge ducts 22. For each
preheater there is provided a by-pass conduit 24 interconnecting
the air supply and discharge ducts 20 and 22. At the branch point
on each supply duct 20 is provided a damper 26 by means of which
the air quantity by-passed through the by-pass conduit 24 can be
controlled.
In the gas supply duct 12 is provided a damper 28 by means of which
the distribution of the main gas flow between the two preheaters
can be controlled. The damper 28 is actuated by an adjusting device
30 governed by temperature sensing devices 32 located in the gas
discharge conduits 16. The signals from the sensing devices 32
bring the adjusting device 30 to move the damper 28 to a position
in which the ratio between the gas quantities passing through the
branch conduits 14 is such that the gas temperature is the same in
both discharge conduits 16.
At a point in the gas discharge duct 18 where the two gas flows
from the discharge conduits 16 can be regarded as thoroughly
intermingled there is located a further temperature sensing device
34 which controls an adjusting device 36 connected to the two
dampers 26 by means of links 38. The adjusting device 36 is adapted
to maintain the gas temperature in the duct 18 at or closely above
a predetermined minimum value by throttling the by-pass conduits 24
at increasing temperature in the duct 18 and thereby increasing the
air quantity passing through the preheaters and by increasing the
by-passed air quantity when the temperature in the duct 18 tends to
decrease.
From the foregoing description it is apparent that the gas damper
28 serves to maintain the same temperature in both gas discharge
conduits 16 and that the air dampers 26 serve to maintain the
temperature in the gas discharge duct 18 at a predetermined
constant value. However, on account of the inertia of the whole
system certain temperature oscillations are inevitable. If the
temperatures in the two gas discharge conduits 16 become different
the gas damper 28 is actuated to change the relative magnitudes of
the two gas flows accordingly. Such temperature oscillations need
not necessarily affect the temperature sensed by the sensing device
34 because the mean temperature may remain constant. On the other
hand, if the temperature is the same in both gas discharge conduits
16 but increases or decreases the air dampers 26 are actuated while
the gas damper 28 is not actuated. Finally, if the temperatures in
the conduits 16 changes differently and in such a manner that the
mean temperature also changes all dampers 26, 28 are actuated.
It is evident that the temperature sensing device 34 may be
replaced by temperature sensing devices in the gas discharge
conduits 16 connected to a simple computer device or the like the
output signal of the computer being indicative of the mean
temperature.
The air may be supplied to the air ducts 20 by separate fans or the
ducts 20 may form branches of a larger duct containing a single
fan. The fans may be of variable capacity. The air discharge ducts
20 may lead to different parts of the boiler furnace or they may
merge into a single larger duct leading to the air distributing
means of the boiler.
The temperature sensing devices and the adjusting devices may be of
conventional suitable types and the control system as a whole may
be designed according to known principles.
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