U.S. patent number 3,894,834 [Application Number 05/407,386] was granted by the patent office on 1975-07-15 for ignition and flame stabilization system for coal-air furnace.
This patent grant is currently assigned to Airco, Inc.. Invention is credited to James W. Estes.
United States Patent |
3,894,834 |
Estes |
July 15, 1975 |
Ignition and flame stabilization system for coal-air furnace
Abstract
A steam generating furnace with multiple coal-air burners has a
corresponding number of supplemental oxygen-fuel burners, each
mounted centrally of a coal-air burner respectively, for directing
an oxy-fuel flame into a combustible mixture of powdered coal and
air; the oxy-fuel burners are controlled to operate at a standby
low-head setting during normal coal-air combustion, and are
automatically controlled by flame sensing means during transitory
coal-air flame deficiency and instability to operate at maximum
heat for maintaining continuous furnace combustion. A manual
over-ride switch operates the oxy-fuel burners at maximum heat such
as for furnace starting, etc.
Inventors: |
Estes; James W. (Piscataway,
NJ) |
Assignee: |
Airco, Inc. (Montvale,
NJ)
|
Family
ID: |
23611832 |
Appl.
No.: |
05/407,386 |
Filed: |
October 17, 1973 |
Current U.S.
Class: |
431/174; 110/185;
110/192; 110/261; 431/12; 431/8; 431/284 |
Current CPC
Class: |
F23N
1/02 (20130101); F23C 1/12 (20130101); F23N
2241/10 (20200101); F23N 2239/02 (20200101); Y02E
20/34 (20130101); F23N 2237/08 (20200101); F23N
5/20 (20130101); F23N 2229/00 (20200101); F23N
2227/36 (20200101); F23N 2237/02 (20200101) |
Current International
Class: |
F23C
1/12 (20060101); F23C 1/00 (20060101); F23N
1/02 (20060101); F23N 5/20 (20060101); F23c
001/10 (); F23c 001/12 () |
Field of
Search: |
;431/8,12,42,60,74,75,174,284 ;110/22A,22R |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
323,578 |
|
Jan 1930 |
|
GB |
|
819,133 |
|
Aug 1959 |
|
GB |
|
Primary Examiner: Myhre; Charles J.
Assistant Examiner: Anderson; William C.
Attorney, Agent or Firm: Rae; David L. Mathews; H. Hume
Bopp; Edmund W.
Claims
I claim:
1. Apparatus for maintaining flames in excess of a predetermined
length in a furnace comprising, fuel-air burner means for
projecting a fuel-air flame in an annular converging pattern from a
furnace wall; oxy-fuel burner means disposed substantially
centrally within said fuel-air burner means for projecting oxy-fuel
flames into said converging fuel-air flames thereby augmenting the
length and stability of said fuel-air flames; radiation responsive
detection means, disposed along a side wall of said furnace
adjacent to said wall from which said fuel-air and oxy-fuel flames
are projected, for producing first and second signals upon said
fuel-air flame failing to exceed and exceeding a predetermined
length; main O.sub.2 and fuel valve means; auxiliary O.sub.2 and
fuel valve means; means responsive to said first signal for closing
said auxiliary O.sub.2 and fuel valve means and for opening said
main O.sub.2 and fuel valve means to project a hot, intense
oxy-fuel flame into said fuel-air flame thereby increasing the
length of said fuel-air flame to at least said predetermined
length; and means responsive to said second signal for closing said
main O.sub.2 and fuel valve means and opening said auxiliary
O.sub.2 and fuel valve means to maintain a low intensity, standby
oxy-fuel flame as long as said fuel-air flame length exceeds said
predetermined length.
2. Apparatus as defined in claim 1 further comprising manually
operable switch means connected to said means responsive to said
second signal such that upon operation of said switch means, said
second signal is overridden thereby supplying fuel and oxygen to
said oxy-fuel burner to enable projection of said hot, intense
oxy-fuel flame notwithstanding an indication by said radiation
responsive detection means that said fuel-air flame exceeds said
predetermined length.
3. A furnace combustion system as specified in claim 1 wherein the
oxygen-fuel burner means is of the rocket type for projecting
oxygen-fuel flames into the fuel-air mixture at different rates of
heat output.
Description
BACKGROUND OF THE INVENTION
Central station steam generating boilers wherein multiple burners
are arranged in banks or tiers to project a mixture of air and
solid fuel such as powdered coal, into the furnace combustion
chamber have long been in common use. In furnaces of this type, the
powdered coal and pressurized air are blown into the combustion
chamber as a combustible mixture and ignited; the resulting
coal-air flames extend a material distance into the chamber, the
walls of which unlike those of a kiln, are kept comparatively cool
by heat transfer to water tubes lining the chamber. Thus, the
chamber does not tend to "run hot" for ensuring reignition or
stable combustion in case of momentary flame dieout or
instability.
Accordingly, transient conditions such as brief clogging of the
coal feeder, pulverizer discontinuity, decrease of blower air, etc.
that reduce or briefly cut off the coal or air supply tend to cause
flame instability and possible flame-out, which in turn can result
in shut-down of the furnace with loss of steam generating capacity,
production time, etc. Restarting the furnace after flame-out and
shut-down is complicated by several factors including the need for
first cleaning the combustion chamber of all gases, combustion
products and unburned mixtures before reignition. This not only
consumes valuable production time but also results in objectionable
stack emissions tending to foul the plant pollution control
equipment.
Although various flame sensing and ignition schemes have been
proposed for improving furnace performance and safety, such as high
voltage electrodes for igniting a coal-air mixture, stand-by pilot
burners interlocked with the main burners, flame-out detectors that
signal for furnace shut-down, etc. such proposals have not been
altogether satisfactory. In general, they either fail to provide
for reignition at flame-out, or fail to provide sufficient heat for
continuous furnace operation under severe transient conditions that
ordinarily cause flame instability or flame-out. In some plants,
the old established practice of restarting the furnace with an
oil-soaked rag torch is still in use because of complexities and
possible explosion hazards in prior art automatic ignition
systems.
In brief, prior art furnace combustion control systems as presently
understood do not solve economically and efficiently the main
problem of furnace down-time due to flame instability, nor the
related problem of stack emissions incident to furnace ignition and
reignition. The present invention is therefore concerned with an
improved furnace ignition and flame stabilization system that
overcomes the problems described above.
SUMMARY OF THE INVENTION
In accordance with the invention, the main coal-air burners of a
central station steam generating furnace for example, are each
equipped with a supplemental rocket type oxygen-fuel burner that is
adapted to project on demand intense "oxy-fuel" flames into a
coal-air mixture to ignite the mixture as it is projected into the
furnace combustion chamber. Thus, the oxy-fuel flame serves a dual
purpose, i.e., (1) to ignite the combustible mixture for fast,
clean furnace starting, and (2) to stabilize on demand the coal-air
flames should brief fluctuations or interruptions in the coal or
air supplies occur during furnace operation. For performing the
latter function, the oxy-fuel burners are initially set for standby
operation at economical low-heat for normal furnace operation. In
the event of flame instability, i.e., potential flame-out, as
evidenced by material pulling back or shortening of the coal-air
flames, such as due to feeder clogging, etc., narrow-angle flame
detectors or radiation sensors automatically cause the oxy-fuel
burners to fire at high-heat, thereby projecting intense, high
velocity, oxy-fuel flames into the weakening coal-air flames. Thus,
the required high temperature for maintaining furnace heat and for
igniting any unburned coal-air mixture is provided; accordingly,
the furnace resumes normal operation without interruption and the
oxy-fuel burners automatically resume economical standby operation
when the transient condition has cleared.
A principal object of the invention therefore is an improved
ignition and combustion control system for solid fuel and air
furnaces as described above, wherein the main burner flames upon
detected instability are automatically supplemented for sustained
heat generation by high velocity, high-heat oxygen-fuel flames.
Another object of the invention is an improved system of the
character described above, wherein oxy-fuel burners at
corresponding main burners are automatically operated, either at
economical standby heat or at maximum heat settings, according to
sensed stability or instability respectively, of the main furnace
flames.
A related object of the invention is an improved furnace starting
control system wherein a rocket type oxy-fuel burner is integrally
related to a main coal-air burner and projects on demand intense
oxy-fuel flames into the combustible mixture from the main burner
for quickly and safely starting the furnace and for stabilizing
furnace combustion with minimal stack emission and pollution.
Other objects, features and advantages will appear from the
following description with reference to the accompanying
drawings.
BRIEF DESCRIPTION OF DRAWINGS
FIG. 1 is a partial plan view in section of the combustion chamber
of a steam generating furnace showing one row of multiple coal-air
burners with supplemental oxy-fuel burners according to the
invention;
FIG. 2 is an enlarged sectional view of a combined coal-air and
oxy-fuel burner unit of FIG. 1;
FIG. 3 is a generally schematic illustration of the oxygen and
natural gas distribution and control systems for the oxy-fuel
burners of FIGS. 1 and 2, and
FIG. 4 is a diagram of network circuitry illustrating the valve
controls for the oxy-fuel distribution system of FIG. 3.
DESCRIPTION OF PREFERRED EMBODIMENT
As generally shown in FIG. 1, a furnace 10 has an array of burners
12 that are mounted in the front wall 14 of the furnace for
projecting fuel-air flames 16 into the combustion chamber 30. The
burners in the present instance are arranged in two tiers or banks
of four burners each (the lower tier not showing), and are of known
type using a combustible mixture of solid fuel and air. Details of
the fuel-air supply to the main burners are not required for an
understanding of this invention, and are not shown in FIG. 1. Where
the main fuel is coal, it is pulverized and conveyed as a powder to
the respective burners where it is ejected, mixed with air at
normal blower pressure and blown into the furnace. The resulting
combustible coal-air mixture upon ignition maintains the furnace
flames. Although a "coal-air" mixture is referred to herein for
brevity, it will be understood that any suitable solid fuel such as
lignite, solid waste, etc. may also be used in practising the
invention.
For greatly facilitating the furnace "light off" or ignition
process, and for stabilizing as required the main furnace flames,
the coal-air burners have incorporated therein means for injecting
on demand a very hot, high velocity flame into the center of the
coal-air mixture. To this end, the main cylinder-like coal-air
burners 12 are open at the firing ends 18 respectively, for
ejecting the coal-air mixture into the furnace, and each main
burner has a rocket type oxy-fuel burner 20 mounted within and
concentrically of the longitudinal axis thereof. The oxy-fuel
rocket burners 20 are each supplied with commercially pure oxygen
and a fuel gas such as natural gas, by mains 22 and 24
respectively, and the mains in turn feed branch lines 22' and 24'
leading to the individual burners. The oxygen and gas connections
to the rocket burners are controlled and regulated by means
hereinafter described for operating these burners at an economical
standby low-heat setting when the coal-air combustion flames are
normal and stable. For furnace starting, and in case of flame
instability during furnace operation, the rocket burners on demand
are quickly brought up to a maximum high heat output.
Referring to FIG. 2, each coal-air burner 12 comprises essentially
a plurality of spaced concentric cylinders and shells including a
cylinder 11 within the rocket burner 20 is centrally mounted on
supporting spiders 19 or the like, a larger concentrically spaced
cylinder 13, and outer positioned shells 15 and 17. An annular
cooling space 46 is formed between the cylinder 11 and rocket
burner 20, and the shell 15 forms with the cylinder 13 an annular
passage 35 through which powdered coal is fed to the furnace from a
circumferential extension passage 15'. The extension 15' is
connected to conventional coal conveyor and pulverizing means, not
shown. The outer shell 17 forms with the shell 15 an annular
passage 37 for blower air that is forced into the extension passage
at 17'. The coal and air passages 35 and 37 converge somewhat at
the burner annular exhaust 18 so that the surrounding blower air
stream 37' is directed at an angle into the coal particles 35' for
good mixing and for projecting the resulting mixture into the
furnace. At exhaust, the coal particles carried by the low pressure
blower air surround the rocket exhaust in an annular stream and
therefore are drawn into the low pressure center by the high
velocity rocket flames; thus maximum contact is made between the
coal particles and hot oxy-fuel flames. Normally, the axially
positioned rocket burner 20 has simply standby function, i.e.,
low-heat anchor flames originating within the burner, keep the
burner in readiness for maximum heat output on demand.
The co-axial arrangement of the main and rocket burner shown in the
preferred embodiment can be modified for offset or tangential
rocket firing into the coal-air mixture, the main requirement being
that the oxy-fuel flames be brought into good heating contact with
the coal-air mixture.
In the furnace arrangement of FIG. 1 which shows only the upper
tier of coal-air burners, all the burners are represented as
normally projecting the coal-air flames 16 into the combustion
chamber 30 for a distance such as d.sub.1 which would correspond to
normal coal-air combustion for the current boiler load of the
furnace. Heat is transferred from the flames to watersteam pipes 32
that line the walls of the chamber. Suitable insulating material 44
separates the pipes from the walls. Thus, the combustion chamber
tends to run "cool" due to the large amounts of heat absorbed by
the water tubes for steam generation; combustion of the coal-air
mixture therefore can be properly maintained only by continuously
supplying coal and air at the required rate. When this rate is
significantly decreased, as where the flames withdraw to a distance
such as d.sub.2 for example, the rate of heat transfer from the
flames becomes excessive, i.e., the flames tend to cool and become
unstable. During such instability, flame-out may occur, ordinarily
requiring shut-down of the furnace as described above.
For avoiding shut-down under such conditions, the unstable or
short-flame condition is detected by small-angle flame radiation
sensors or the like, 34 and 36 which are sensitive to the visible
flame and produce a signal for quickly bringing the rocket burners
20 up to maximum heat. At this setting, the long, centrally
projected oxy-fuel flames re-establish proper combustion conditions
at the powdered coal exhasut conduit 35. The flame detectors 34 and
36 which can conveniently be mounted in the sidewall inspection
doors 40 and 42 opposite the upper and lower burner tiers
respectively, have narrow-angle sensing as indicated at angle a for
the upper tier detector 34. The detector at each level is
positioned so that normally the full combustion flames from the
corresponding tier burners are positively sensed in the range
beyond distance d.sub.2 to keep the rocket burner control at the
standby low-heat setting; retraction of the coal-air flames to the
unstable limit represented, for example, by distance d.sub.2 is
negatively sensed to actuate controls for firing the rocket burner
at maximum high heat. Optimum positioning of the flame detectors
depends on the furnace characteristics; that is, it may be
preferable to focus the detector on the outer edges of the normal
coal-air flames 30 so that any shortening of the flames produces a
demand signal for maximum rocket heat.
The so-called "rocket" oxygen-fuel burner used in the invention is
preferably of the type disclosed in U.S. Pat. Nos. 3,092,166 and
3,135,626 which are assigned to the same assignee as the present
invention. This type burner has characteristics such as large
turn-down ratio for example, whereby high temperature, oxy-fuel
flames can be supplied over a minimum-to-maximum heat range within
a short time. This feature is especially advantageous in practicing
the invention, both for clean, fast furnace starting and for
supplementing the coal-air flames as needed.
The burner has inherent stability which is achieved by permanent
anchor flames; this ensures reliable and stable flame output
notwithstanding wide variations of fuel supply within a
comparatively brief time. The rocket burner flame is projected at
velocities up to the speed of sound, and at very high temperatures.
By valve adjustments of the oxygen and fuel gas lines, the burner
flame length can be varied as required from about 1 foot to as much
as 10 feet, and the heat output can be varied from about 20,000
Btu/hr. to approximately 10 million Btu/hr. for a comparatively
small size burner; also valve adjustment serves to control the
flame temperature and its oxidizing effect by varying the
oxygen-fuel ratio. Thus, the ratio control can be varied if
desired, to provide excess amounts of oxygen in situations such as
temporary reduction of furnace blower air where additional oxygen
is required.
At the low-heat standby setting, the rocket burner 20 can be
economically operated at about 50 scf/hr. natural gas (NG) and 75
scf/hr. oxygen (O.sub.2); at the high firing rate (which is
ordinarily used only for starting and during transient flame
instability) the burner can utilize approximately 1000 scf/hr. NG
and 1500 scf/hr. O.sub.2 for achieving very high heat outputs.
Although the rocket burner is described herein as using NG fuel, it
can where preferred use a suitable liquid fuel, or a combination of
liquid and gas fuels such as described in U.S. Pat. No. 3,092,166
above.
As shown in FIG. 2, the O.sub.2 and NG are fed through the branch
supply lines 22' and 24' respectively, to a housing 21 at the
breech end of the rocket barrel 20'. The barrel has a water jacket
through which cooling water is circulated from supply line 23 to a
drain line 23'. The rocket barrel near its firing end has a
partition member 25 with passages for the NG and O.sub.2
respectively. The NG supply line 24' connects with a tube 28 that
extends centrally of the rocket barrel to a stream divider 31, from
which the NG flows in separate tubes 33 through the partition 25 as
jets to the rocket exhaust. The O.sub.2 supply line 22' connects
with the annular chamber 26 in the barrel, from which O.sub.2 flows
through multiple passages 26' in the partition 25 to mix with the
surrounding NG jets at the rocket exhaust 38.
Separate electrical starting means for each rocket burner comprises
a high voltage ignition transformer 27, FIG. 2, that is connected
by lead 27' and insulated conductor 29 to an electrode 29', the
latter forming a spark gap at the burner exhaust with the rocket
barrel functioning as return conductor. When ignition is turned on,
a 120 volt primary winding (not shown) is energized to induce in
the transformer secondary 6000 volts for high voltage sparking. The
transformer circuitry, which can be energized at ignition through a
standard relay (as indicated in FIG. 4) from a 120 volt supply
outlet, is well-known and therefore not shown.
The gas distribution system shown in FIG. 3 comprises
valve-controlled by-pass lines 22B and 24B that are connected in
shunt with corresponding valve controlled sections of the O.sub.2
and NG conduit mains 22 and 24 respectively, for supplying the
rocket burners 20 when at the standby or low-heat "idle" settings.
The by-pass lines remain open during both "idle" and maximum heat
settings. In particular, the NG by-pass line 24B comprises a
flow-rate meter 50 in series with a manually operated valve 52 that
is pre-set for minimum gas flow, and an on-off solenoid valve 54,
the coil 56 of which is controlled by the circuitry of FIG. 4.
SImilarly, the O.sub.2 by-pass line 22B has a flow-rate meter 58,
manual flow-adjustment valve 60 and an on-off solenoid valve 62
with an operating coil 64 also controlled by the FIG. 4
circuitry.
The main NG supply conduit 24 has in series a main shut-off valve
66, and in the shunted section thereof, a flow controller 68 of the
plate orifice type, a manual valve 70 that is preset according to
orifice flow, and an on-off solenoid valve 72 with operating coil
74. The flow controller is connected across the orifice plate to a
flow meter 76 and at the high pressure side to a pressure gauge 78.
SImilarly, the main O.sub.2 supply conduit 22 has a main shut-off
valve 80, orifice-plate flow controller 82 with flow meter 84 and
pressure gauge 86, manually preset valve 88 and solenoid valve 90
with operating coil 92. The solenoid coils 74 and 92 are controlled
from FIG. 4 as indicated. For each main supply conduit, the
corresponding by-pass is in shunt with the section having the flow
controller, preset valve and solenoid valve. Accordingly, it will
be seen from FIG. 3 that the rocket burners in each tier of main
burners (the upper tier only being shown) can be supplied when in
use with O.sub.2 and NG either through the by-pass connections 22B
and 24B solely, at the standby rates set in the respective
by-passes (the shunted sections of the main conduits being closed),
or through the main conduits for the maximum rates set at the
respective flow controllers 82 and 68 when the main solenoid valves
90 and 72 are open.
ROCKET BURNER OPERATION
In FIG. 4, which shows a circuit network 100 for controlling the
starting sequence of the rocket burners and subsequent settings for
standby and maximum firing, a main power controlling switch S is
arranged to connect the network line terminals 102 and 104 with a
source of voltage E. A power-on indicating lamp 106 is connected
across the line and has in parallel therewith a branch circuit
including in series, a rocket ignition switch 108, a normally
closed emergency stop switch 110 and a relay coil 112 that
gang-operates through connections 114, a pair of switches 116 and
118 for "on-off" and "off-on" conditions, respectively. As shown,
the coil 112 is de-energized so that the switch 116 is closed to
light the "off" ignition signal lamp 120.
To start, the power switch S and the ignition switch 108 are
closed, thereby energizing coil 112 for opening the off signal
switch 116 and closing switch 118 which lights "idle" signal lamp
122 and locks in the ignition circuit from terminal 104 through
"stop" switch 110. According to preferred rocket starting sequence,
the fuel gas is first turned on and spark-ignited at the rocket
exhaust, and after a brief delay O.sub.2 is turned on. Immediately
upon closing of the ignition switch 108 (subsequently through the
holding circuit switch 118) the coil 56 of the NG by-pass solenoid
valve 54 is energized to open the by-pass line for supplying NG at
the idle rate to the respective rocket burners 20, FIG. 3. During
starting, the main NG and O.sub.2 valves 72 and 90 remain closed as
the line switch 134 is open.
The spark igniter coil 130 (in shunt through a normally closed time
delay switch 126 with idle relay coil 112) is also energized as the
ignition switch 108 is closed, through the time delay switch 126.
The energization of coil 130 causes through circuitry hereinafter
referred to, energization of the high voltage ignition transformer
27, FIG. 2. Ignition sparking at 6000 volts is thereby produced at
the rocket starting electrode 29' for igniting the NG fuel as soon
as it is turned on.
With an idle NG flame at the rocket exhaust and the ignition
transformer still energized for ensuring ignition, the rocket is in
readiness for flow of O.sub.2 to the rocket exhaust. A time-delay
relay coil 132 is energized through the locked-in ignition switch
118 to actuate the timing means 136 which after a five-second delay
closes the line switch 134 for energizing the coil 64 of the
O.sub.2 by-pass valve 62. The rocket burner is now operating
normally at "idle" with permanently established oxy-fuel flames,
and will continue to operate at this setting in the absence of
further control. The high voltage sparking referred to above
continues for ten seconds and is then automatically shut off at the
switch 126 by timer 128. The time delay relay coil 124 that started
operation of the timer is in parallel with idle coil 112 and was
energized therewith.
The rocket system is set to operate automatically at maximum rate
upon demand by momentary closing of the run switch 138 (the idle
switch 140 being closed) to energize the relay coil 142 that closes
through a connection 143 the automatic control switch 144. The idle
switch 145 for signal light 122 is concurrently opened through
relay connection 147. Closing of the automatic control switch 144
establishes a holding circuit for the relay coil 142 and also puts
control potential on the open terminals of the parallel-connected
manual and flame detector switches 146 and 148 respectively. Either
switch when closed jointly energizes the parallel-connected
solenoid coils 74 and 92 of the main NG and O.sub.2 valves 72 and
90 respectively, for maximum high-heat firing of the rocket
burners.
Referring briefly to FIG. 1, the upper and lower tier flame
detectors 34 and 36 can be connected to the associated control
circuitry so that flame instability signals from either burner tier
can turn on for high firing all the rocket burners of both tiers,
thereby quickly injecting very large amounts of heat into the
combustion chamber for supplementing all the coal-air flames; or
simply the rocket burners of the affected tier can be fired,
assuming that each tier has its separate coal conveyor and
pulverizer feed system. For operating the flame detector relay
switch 148 in proper sense, FIG. 4, the relay 150 is controlled in
obvious manner through amplifier or intermediate relay means 149 so
that the relay 150 is energized when the signal from the detector
is "negative". That is, when the millivolt output of the detector
drops below a set point (as where the visible flame recedes from
the detector angle a), a sensitive relay is tripped which in turn
causes energization of the flame relay coil 150. The flame
detectors 34 and 36 are calibrated for proper sensitivity to
radiation from the visible flame. This gives more reliable flame
temperature indication than would be obtained by ultra-violet or
infra-red detectors.
As shown, the manual switch 146 can override as desired, the flame
detector switch 148 thereby providing on demand high rocket burner
heat for furnace starting, or for optionally supplementing the main
coal-air flames, such as in marginal situations involving possible
inadequate coal and air supplies. A "run" signal lamp 152 connected
across the relay coils of the main valves indicates when the rocket
burners are firing at maximum rates. The high firing rate is
continued while the abnormal transient conditions such as coal
pulverizer discontinuity, etc. continue. When the coal-air flames
have returned to normal length to indicate stable combustion
conditions, the extended visible flame is detected and the
resulting positive signal causes opening of the flame detector
switch 148 and closing of the main NG and O.sub.2 valves 72 and 90.
The burners automatically return to standby firing as the NG and
O.sub.2 by-pass valves 54 and 62 have remained open during the
high-rate firing. In case of failure of oxygen and fuel gas
pressures or water cooling failure, the rocket burner is
automatically shut down by conventional safety controls.
Where maximum firing of the rockets is no longer desirable, as
where the coal-air feed is sufficiently restored and shut down is
not indicated, the manually controlled idle switch 140 can be
opened to de-energize relay 142 and open the line power switch 144,
thereby overriding the detector switch 148 and causing closing of
main valves 72 and 90 and return of the burners to idle. Manual
high-fire control can be advantageously had through the override
switch 146 for boiler load changes when irregular combustion may
occur. Rocket firing immediately corrects this condition with
practically no formation of smoke or soot during the load change;
also at start, the maximum-heat firing of the oxy-fuel rockets not
only establishes normal combustion of the coal-air flames in less
time, but also avoids stack emissions of the black smoke and soot
ordinarily observed at starting.
Multiple tiers of coal-air burners can as mentioned above, be
supplemented by oxy-fuel rocket burners according, for example, to
the furnace feed arrangements, i.e., where each tier has its own
coal pulverizer and conveyor system, the flame detector for a
specific tier may have its control limited to that tier. In such
case, the control circuitry of FIG. 4 would be substantially
duplicated for each tier.
Accordingly, it is seen that the manual and automatic combustion
controls of the invention encompass in combination the entire range
of operating conditions encountered in central stations boiler
operations.
Having set forth the invention in which is considered to be the
best embodiment thereof, it will be understood that changes may be
made in the system and apparatus as above set forth without
departing from the spirit of the invention or exceeding the scope
thereof as defined in the following claims.
* * * * *