BACKGROUND
[0001] The disclosure relates to industrial equipment. More particularly, the disclosure
relates to the detonative cleaning of industrial equipment.
[0002] Surface fouling is a major problem in industrial equipment. Such equipment includes
furnaces (coal, oil, waste, etc.), boilers, gasifiers, reactors, heat exchangers,
and the like. Typically the equipment involves a vessel containing internal heat transfer
surfaces that are subjected to fouling by accumulating particulate such as soot, ash,
and minerals, more integrated buildup such as slag and/or fouling, and the like. Such
particulate build-up may progressively interfere with plant operation, reducing efficiency
and throughput and potentially causing damage. Cleaning of the equipment is therefore
highly desirable and is attended by a number of relevant considerations. Often direct
access to the fouled surfaces is difficult. Additionally, to maintain revenue it is
desirable to minimize downtime associated with cleaning. A variety of technologies
have been proposed.
[0003] An exemplary detonative cleaning apparatus includes a conduit into which fuel and
oxidizer are introduces and then ignited. The ignition causes a shock wave to be discharged
from the conduit to impact the surfaces to be cleaned. By way of example,
U.S. patent application publication 20050199743, the disclosure of which is incorporated herein by reference in its entirety as if
set forth at length, discloses a detonative cleaning apparatus control system and
has a specific illustration relative to a segmented conduit assembly. Alternative
apparatus are of the retractable lance-type. Such systems are often identified as
"soot blowers" after the key application for the technology.
SUMMARY
[0004] One aspect of the disclosure involves an apparatus for cleaning one or more surfaces
within a vessel having a vessel wall separating a vessel exterior from a vessel interior
and having a wall aperture. The apparatus has at least one elongate conduit having
an upstream first end and a downstream second end and positioned to direct a shockwave
from the second end into the vessel interior. A source of fuel and oxidizer is coupled
to the conduit to deliver the fuel and oxidizer to the conduit An initiator is positioned
to initiate a reaction of the fuel and oxidizer to produce the shockwave. At least
one sensor coupled to the conduit to detect motion characteristic of a detonation.
A control system coupled to the initiator, the source, and the sensor for receiving
input from the sensor and controlling operation of the initiator and source responsive
to said input.
[0005] The details of one or more embodiments of are set forth in the accompanying drawings
and the description below. Other features and advantages will be apparent from the
description and drawings, and from the claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0006]
FIG. 1 is a view of an industrial furnace associated with several soot blowers positioned
to clean a level of the furnace.
FIG. 2 is a side view of one of the blowers of FIG. 1.
FIG. 3 is a schematic view of a control system for multiple cleaning apparatus.
[0007] Like reference numbers and designations in the various drawings indicate like elements.
DETAILED DESCRIPTION
[0008] FIG. 1 shows a furnace 20 having an exemplary three associated soot blowers 22. In
the illustrated embodiment, the furnace vessel is formed as a right parallelepiped
and the soot blowers are all associated with a single common wall 24 of the vessel
and are positioned at like height along the wall. Other configurations are possible
(e.g., a single soot blower, one or more soot blowers on each of multiple levels,
and the like).
[0009] Each soot blower 22 includes an elongate combustion conduit 26 extending from an
upstream (e.g., distal/inlet) end 28 away from the furnace wall 24 to a downstream
(e.g., proximal/outlet) end 30 closely associated with the wall 24. Optionally, however,
the end 30 may be well within the furnace. In operation of each soot blower, combustion
of a fuel/oxidizer mixture within the conduit 26 is initiated proximate the upstream
end (e.g., within an upstreammost 10% of a conduit length) to produce a detonation
wave. The detonation wave is expelled from the downstream end as a shockwave along
with associated combustion gases for cleaning surfaces within the interior volume
of the furnace.
[0010] Each soot blower may be associated with a fuel/oxidizer source 32. Such source or
one or more components thereof may be shared amongst the various soot blowers. An
exemplary source includes a liquified or compressed gaseous fuel cylinder 34 and an
oxygen cylinder 36 in respective containment structures 38 and 40. In the exemplary
embodiment, the oxidizer is a first oxidizer such as essentially pure oxygen. A second
oxidizer may be in the form of shop air delivered from a central air source 42. In
the exemplary embodiment, air is stored in an air accumulator 44. Fuel, expanded from
that in the cylinder 34 is generally stored in a fuel accumulator 46. Each exemplary
source 32 is coupled to the associated conduit 26 by appropriate plumbing below. Similarly,
each soot blower includes a spark box 50 for initiating combustion of the fuel oxidizer
mixture and which, along with the source 32, is controlled by a control and monitoring
system (discussed below).
[0011] FIG. 2 shows further details of an exemplary soot blower 22. The exemplary detonation
conduit 26 is formed with a main body portion formed by a series of doubly flanged
conduit sections or segments 60 arrayed from upstream to downstream and a downstream
nozzle conduit section or segment 62 having a downstream portion 64 extending through
an aperture 66 in the wall and ending in the downstream end or outlet 30 exposed to
the furnace interior 68. The term nozzle is used broadly and does not require the
presence of any aerodynamic contraction, expansion, or combination thereof. Exemplary
conduit segment material is metallic (e.g., stainless steel). The outlet 30 may be
located further within the furnace if appropriate support and cooling are provided.
FIG. 2 further shows furnace interior tube bundles 70, the exterior surfaces of which
are subject to fouling.
[0012] An overall length L between ends 28 and 30 may be 1-15 m, more narrowly, 5-15 m.
A fizel/oxidizer charge may be introduced to the detonation conduit interior in a
variety of ways. There may be one or more distinct fuel/oxidizer mixtures. Such mixture(s)
may be premixed external to the detonation conduit, or may be mixed at or subsequent
to introduction to the conduit. FIG. 2 shows conduit configured for distinct introduction
of two distinct fuel/oxidizer combinations: a predetonator combination; and a main
combination. In the exemplary embodiment, at an upstream first location, one or more
predetonator fuel injection conduits 90 are coupled to one or more ports 92 in the
conduit to define fuel injection ports. Similarly, one or more predetonator oxidizer
conduits 94 may be coupled to oxidizer inlet ports 96. A purge gas conduit 98 may
be similarly connected to a purge gas port 100 yet further upstream., An igniter/initiator
106 (e.g., a spark plug) may be located near the upstream end of the combustion conduit.
[0013] In the exemplary embodiment, a main fuel is carried by a number of main fuel conduits
112 and a main oxidizer is carried by one or more main oxidizer conduits 110. In exemplary
embodiments, the fuels are hydrocarbons. In particular exemplary embodiments, both
fuels are the same, drawn from a single fuel source but mixed with distinct oxidizers:
essentially pure oxygen for the predetonator mixture; and air for the main mixture.
Exemplary fuels useful in such a situation are propane, MAPP gas, or mixtures thereof.
Other fuels are possible, including ethylene and liquid fuels (e.g., diesel, kerosene,
and jet aviation fuels). The oxidizers can include mixtures such as air/oxygen mixtures
of appropriate ratios to achieve desired main and/or predetonator charge chemistries.
Further, monopropellant fuels having molecularly combined fuel and oxidizer components
may be options.
[0014] In operation, at the beginning of a use cycle, the combustion conduit is initially
empty except for the presence of air (or other purge gas). The predetonator fuel and
oxidizer are then introduced through the associated ports to fill an upstream section
(e.g., just beyond the main fuel/oxidizer ports). The predetonator fuel and oxidizer
flows may then be shut off. An exemplary volume filled the predetonator fuel and oxidizer
is 1-40%, more narrowly 1-20%, of the combustion conduit volume. The main fuel and
oxidizer are then introduced, to substantially fill some fraction (e.g., 20-100%)
of the remaining volume of the combustor conduit. The main fuel and oxidizer flows
are then shut off. The prior introduction of predetonator fuel and oxidizer past the
main fuel/oxidizer ports largely eliminates the risk of the formation of an air or
other non-combustible slug between the predetonator and main charges. Such a slug
could prevent migration of the combustion front between the two charges.
[0015] With the charges introduced, the spark box is triggered to provide a spark discharge
of the initiator igniting the predetonator charge. The predetonator charge being selected
for very fast combustion chemistry, the initial deflagration quickly transitions to
a detonation within the segment 84 and producing a detonation wave. Once such a detonation
wave occurs, it is effective to pass through the main charge which might, otherwise,
have sufficiently slow chemistry to not detonate within the conduit of its own accord.
The wave passes longitudinally downstream and emerges from the downstream end 30 as
a shockwave within the furnace interior, impinging upon the surfaces to be cleaned
and thermally and mechanically shocking to typically at least loosen the contamination.
The wave will be followed by the expulsion of pressurized combustion products from
the detonation conduit, the expelled products emerging as a jet from the downstream
end 30 and further completing the cleaning process (e.g., removing the loosened material).
After or overlapping such venting of combustion products, a purge gas (e.g., air from
the same source providing the main oxidizer and/or nitrogen) is introduced through
the purge port 100 to drive the final combustion products out and leave the detonation
conduit filled with purge gas ready to repeat the cycle (either immediately or at
a subsequent regular interval or at a subsequent irregular interval (which may be
manually or automatically determined by the control and monitoring system)). Optionally,
a baseline flow of the purge gas may be maintained between charge/discharge cycles
so as to prevent gas and particulate from the furnace interior from infiltrating upstream
and to assist in cooling of the detonation conduit.
[0016] The apparatus may be used in a wide variety of applications. By way of example, just
within a typical coal-fired furnace, the apparatus may be applied to: the pendants
or secondary superheaters, the convective pass (primary superheaters and the economizer
bundles); air preheaters; selective catalyst removers (SCR) scrubbers; the baghouse
or electrostatic precipitator; economizer hoppers; ash or other heat/accumulations
whether on heat transfer surfaces or elsewhere, and the like. Similar possibilities
exist within other applications including oil-fired furnaces, black liquor recovery
boilers, biomass boilers, waste reclamation burners (trash burners), and the like.
[0017] A variety of systems may be provided for monitoring and/or controlling operation
of the detonative cleaning apparatus. The implementation of any particular control
and monitoring system may be influenced by the physical environment including the
nature and configuration of the vessel and its surfaces and the arrangement of the
combustion conduit(s). FIG. 3 schematically shows one of a number of levels of a vessel
200. At this level, a number of combustion conduits 202A-D are positioned. In the
exemplary embodiment, downstream outlets of the conduits are positioned in the interior
of the vessel and upstream ends are external to the vessel. Although shown straight,
the conduits may have non-straight configurations to discharge shockwaves in desired
locations with desired directions. Each conduit is closely associated with an interface
module 204A-D which may provide local control of various operational parameters (e.g.,
including fuel and oxidizer introduction, purge and cooling gas introduction, initiation,
and the like). Further details of an exemplary interface module are discussed below.
The given vessel level may also include sensors 206, 207, and 208. However, the sensors
need not be level-specific. Similarly, the conduits could be other than level-specific
and other than oriented to discharge in parallel planes. The sensors may be conduit-specific
(e.g., close to the outlet of a specific associated conduit or to the furnace surface
cleaned by such conduit) or may be more generally located. The sensors may detect
one or more of thermal conditions, pressures, flows, chemical conditions, and/or visual
conditions. Exemplary sensor operation is discussed in further detail below.
[0018] For signal communication, the modules and sensors are coupled via communication lines
209 to a hub (e.g., ethernet) 210. In the exemplary embodiment, the sensors are coupled
to the hub via the modules (e.g., coupled to the modules by communication or signal
lines). For physical input (e.g., fuel, oxidizer, purge gas, coolant, power, and the
like), the modules are coupled to a central supply unit 212 via fluid and power lines
213. The hub and supply unit may be level-specific, common, or some combination. The
hub is coupled for signal communication (e.g., via network lines 215 such as a fiber
optic line, Ethernet line, or the like) to a control and monitoring system 214 of
the facility (e.g., a general purpose computer running control/monitoring software)
which may be specific to the vessel or central to a group of vessels at a site (e.g.,
a given facility). The supply unit may similarly be coupled to the system 214 via
the hub 210 or may exist independently. The system 214 is in communication with a
remote control and monitoring system 216. The system 216 may be in secure communication
with a number of systems 214 at a number of different sites. In such a situation,
however, the system 216 may be colocated with one or more of those systems 214 and
off-site of the others. The exemplary communication between the system 216 and systems
214. is via a wide area network 217 such as the internet. Alternative public and private
networks or other communication systems may be used. The supply unit 212 may, itself,
be fed from a remotely located tank farm 218 (e.g., a central tank farm of the facility)
via lines 219 for supply of non-air gases and other fluids and from appropriate shop
air and power sources (not shown) which may also be central sources of the facility).
The system 214 may communicate with several central systems. For example, the system
216 may be a central system of a facility owner/operator communicating with systems
214 at various facilities of that owner/operator. A central system 223 may be a central
system of a service vendor communicating with systems 214 of various facilities of
various owners/operators either directly or via the systems 216. Based ultimately
upon data provided by the sensors 206 and 208, the systems 214 may inform the system
223 that service or routine maintenance is necessary or otherwise appropriate (the
decision being made at any of the systems 214, 216, or 223).
[0019] In the exemplary embodiment, an emergency control panel 220 is in close proximity
to the system 214. The exemplary emergency control panel includes one or more status
lights and one or more switches (e.g., red/green status lights and emergency kill
switches for each conduit plus a master kill switch for all conduits). These are coupled
by lines 222 extending to the individual interface modules. In the event of a control
system failure which might prevent control (namely safing) of the conduits via the
system 214 and hub 210, the kill switches may be tripped by a technician to safe the
conduits (e.g., shut the fuel and oxidizer valves, disable the ignition, and the like,
to safely shut down and/or disable the associated conduits). The interface modules
themselves may be set up in a failsafe mode whereby a break in the associated line(s)
215 or 222 causes a module to transition to a safe mode.
[0020] The sensors 206 and/or 207 may also represent motion sensors used to sense conduit
motion responsive to the combustive event. In particular, the sensors may be used
to verify detonation, generally, and the magnitude/sufficiency of the detonation,
in particular. An exemplary motion sensor is an accelerometer. An exemplary accelerometer
is a piezoelectric sensor such as a ceramic shear accelerometer. Another exemplary
sensor is a vibration sensor. An exemplary vibration sensor is a mercury-free mechanical
vibration switch. Another exemplary sensor is a strain gauge. Such sensors do not
need direct exposure to the conduit interior or vessel interior (although the microphone
in particular may also be amenable to interior exposure for more direct measurement).
Such sensors may be mounted on the conduit exterior without an associated aperture
to the conduit interior. This can save complexity, sensor robustness, etc. Advantageous
sensor positioning may be outside the vessel to limit sensor exposure to severe environments.
[0021] Exemplary sensor coupling is a series coupling of the sensors (or back end signal
processing circuit) for a plurality (e.g., all) of the conduits. The series circuit
may be normally closed. In the event of a detonation on any conduit, the sensor will
toggle and the circuit will open. The signal processing circuit may be configured
to hold the open circuit open long enough (e.g., greater than a second) for the controller
to read. At this point, if a particular conduit was commanded to fire and the circuit
doesn't open, the controller knows which conduit failed to detonate. After a pre-defined
number of failures of a given conduit to successfully fire, the control system may
alert the operator and takes that particular conduit offline (e.g., while allowing
for continued operation of the remaining conduits).
[0022] Another option for the sensors 206 and/or 207 is a pressure switch (as distinguished
from a continuous pressure sensor). The switch threshold may be selected in view of
its positioning to correspond to a desired threshold for the pressure associated with
detonation. Triggering of the switch would thus indicate a successful detonation,
while a failure to trigger would indicate an unsucccessful or sub-threshold event.
An exemplary positioning is in an upstream half of a length of the conduit.
[0024] One or more embodiments have been described. Nevertheless, it will be understood
that various modifications may be made. For example, the invention may be adapted
for use with a variety of industrial equipment and with variety of soot blower technologies.
For example, the principles may be adapted to various existing or yet-developed detonative
cleaning apparatus, including fixed and extensible/retractable units. Aspects of the
existing equipment and technologies may influence aspects of any particular implementation.
Accordingly, other embodiments are within the scope of the following claims.
1. An apparatus for cleaning one or more surfaces within a vessel (200) having a vessel
wall (24) separating a vessel exterior from a vessel interior (68) and having a wall
aperture (66), the apparatus comprising:
at least one elongate conduit (26; 202) having an upstream first end and a downstream
second end and positioned to direct a shockwave from the second end into the vessel
interior (68); and
a source of fuel and oxidizer (32) coupled to the conduit (26) to deliver the fuel
and oxidizer to the conduit (26);
an initiator (106) positioned to initiate a reaction of the fuel and oxidizer to produce
the shockwave;
at least one sensor (206 ...) coupled to the conduit (202) to detect motion indicative
of a detonation; and
a control system coupled to the initiator (106), the source (32), and the sensor (206)
for receiving input from the sensor (206 ...) and controlling operation of the initiator
(106) and source (32) responsive to said input.
2. The apparatus of claim 1 wherein:
the sensor (206 ...) is a piezoelectric sensor.
3. The apparatus of claim 1 wherein:
the sensor (206 ...) is a contact accelerometer.
4. The apparatus of claim 1 wherein:
the sensor (206 ...) is a contact vibration sensor.
5. The apparatus of claim 1 wherein:
the sensor (207) is in contact with an exterior of the conduit (202) without an associated
aperture to the interior of the conduit (202).
6. The apparatus of any preceding claim wherein:
there are a plurality of such conduits (202) and such initiators (106), each of the
conduits (202) associated with an associated one or more of the initiators (106);
and
the sensors (206 ...) are series coupled to the control system.
7. The apparatus of claim 6 wherein:
the control system is programmed to generate maintenance or service requests responsive
to the input.
8. The apparatus of claim 6 or 7 wherein:
the control system is programmed to determine detonation failures of the conduits
individually.
9. The apparatus of claim 8 wherein:
the control system is programmed to individually adjust operational parameters of
the conduits responsive to the determined failures.
10. The apparatus of any preceding claim wherein:
the control system communicates with a remote monitoring system (214).
11. The apparatus of any preceding claim wherein:
the control system is programmed to determine a detonation success or failure status.
12. The apparatus of any preceding claim wherein:
the control system is programmed with a plurality of different cleaning processes
and to execute the processes responsive to corresponding sensed conditions.
13. A method for cleaning a surface within a vessel (200), the method comprising:
introducing fuel and oxidizer to at least one elongate conduit (202) having an upstream
first end and a downstream second end and positioned to direct a shockwave from the
second end into the vessel interior;
initiating a reaction of the fuel and oxidizer;
detecting a motion of the conduit (202);
responsive to the detecting, determining a characteristic of the reaction; and
responsive to the determined characteristic, adjusting at least one parameter of the
introducing and initiating so as to provide feedback control of the characteristic.
14. The method of claim 13 wherein:
the detecting comprises detecting an acceleration.
15. The method of claim 13 wherein:
the detecting comprises detecting a vibration parameter.
16. The method of claim 13 wherein:
the determining comprises determining a sufficiency of a detonation.
17. The method of any of claims 13 to 16 further comprising:
responsive to the determined characteristic, generating an automated maintenance or
service request.
18. An apparatus for cleaning one or more surfaces within a vessel (200) having a vessel
wall (24) separating a vessel exterior from a vessel interior (68) and having a wall
aperture (66), the apparatus comprising:
at least one elongate conduit (202) having an upstream first end and a downstream
second end and positioned to direct a shockwave from the second end into the vessel
interior; and
a source (32) of fuel and oxidizer coupled to the conduit (202) to deliver the fuel
and oxidizer to the conduit;
an initiator (106) positioned to initiate a reaction of the fuel and oxidizer to produce
the shockwave;
a pressure switch (206 ...) coupled to the conduit (202) to be exposed to pressure
associated with the reaction; and
a control system coupled to the initiator (106), the source (32), and the pressure
switch for receiving input from the pressure switch (206 ...) and controlling operation
of the initiator and source responsive to said input.
19. The apparatus of claim 18 wherein the pressure switch (206 ...) is a binary switch,
with an open condition associated with pressure below a threshold and a closed condition
associated with pressure above the threshold.
20. The apparatus of claim 18 or 19 wherein the pressure switch (207) is along an upstream
half of a length of the conduit (202).