BACKGROUND OF THE INVENTION
1. FIELD OF THE INVENTION
[0001] The present invention relates to an improved method of cleaning a nuclear steam generator
or other tube bundle heat exchanger by removing the buildup of sedimentation or "sludge"
which accumulates in the bottom of a heat exchanger vessel through utilization of
a repetitive shock wave induced in the sludge and in flushing fluid. The shock wave
serves to effectively and safely loosen the products of corrosion and other elements
which settle at the bottom of the heat exchanger or steam generator and thereby facilitates
their easy removal through flushing and vacuuming the vessel.
2. DESCRIPTION OF THE PRIOR ART
[0002] One of the major components in a power generating facility such as a nuclear power
plant is the steam generator or heat exchanger portion of the facility. Large scale
heat exchanger systems are essentially comprised of a primary system which contains
a large number of individual tubes which have fluid circulating through them and a
secondary system which consists of a second fluid surrounding said tubes contained
within a housing which enwraps both systems. Heat is transferred from the fluid running
through these heat exchanger tubes to the fluid in the secondary system which is itself
eventually turned to steam. The steam, in turn, generates power.
[0003] These heat exchangers or steam generators have experienced many problems due to the
buildup of products of corrosion, oxidation, sedimentation and comparable chemical
reactions within the heat exchanger. The problem of magnetite buildup at the junctions
of the primary heat exchanger tubes and the support plates for those tubes, and further
magnetite buildup within the crevices between the tubes and their support plates was
extensively treated in United States Patent No. 4,320,528. That patent addressed the
use of ultrasonic methods to facilitate the removal of the magnetite from those junctions.
The present inventors are the same as the inventors in Patent No. 4,320,528.
[0004] At the bottom of the heat exchanger is a tube sheet. This is a thick metal plate
which acts as the support base for numerous heat exchanger tubes. In addition to the
problems of magnetite buildup at the junctions and inside the crevices of the primary
heat exchanger tubes and their support plates, a second problem has also troubled
steam generators for many years. There is a buildup of sedimentation or "sludge" which
accumulates in the bottom of heat exchanger vessels. This sludge includes copper oxide,
magnetite and other oxidation or corrosion products which have not adhered to the
tubing or other surfaces and therefore accumulate at the bottom. The sludge pile rests
on top of the tube sheet and on top of the higher elevation support plates and may
form a thick layer. The sludge further accumulates in the crevices between the tube
sheet and the primary heat exchanger tubes which are embedded in the tube sheet for
support and also accumulates on the tube support plates. The problem of removing the
sludge which enters the deep crevices in the tube sheet was addressed in presently
pending patent application Serial No. 06/370,826 filed on 4/22/82. Patent application
06/370,826 solves the problem of removing sludge from the deep crevices through use
of specialized ultrasonic waves which are directed in a certain way to produce the
desired result.
[0005] In addition to the above two prior art references, the following prior art patents
address the problem of cleaning a nuclear steam generator or else keeping it clean
before it becomes dirty through the use of ultrasonics:
1. Patent Number 2,664,274 issued to Worn et al.
2. Patent Number 2,987,086 issued to Branson.
3. Patent Number 3,033,710 issued to Hightower et al.
4. Patent Number 3,240,063 issued to Sasaki
et al.
5. Patent Number 3,295,596 issued to Ostrofsky et al.
6. Patent Number 3,433,669 issued to Kouril.
7. Patent Number 3,428,811 issued to Harriman et al.
8. Patent Number 3,447,965 isued to Teumac et al.
9. Patent Number 3,854,996 issued to Frost et al.
10. Patent Number 4,120,699 issued to Kennedy et al.
11. Patent Number 4,167,424 issued to Jubenville et al.
[0006] All of the above-referenced patents have been extensively discussed in both United
States Patent 4,320,528 or else in presently pending Patent Application Serial Number
06/370,826 filed on 4/22/82. The following two prior art publications have also been
discussed in these references:
1. Chemical cleaning of BWR and Steam Water System at:
Dresden Nuc. Pw. Station, Obrecht et al., pp. 1-18, (10/26/60) 21st Ann. Conf. of
Eng.
2. Special Tech. Pub. 42 (1962) ASTM Role of Cavitation in Sonic Energy Cleaning,
by Bulat.
3. R&D Status Report Nuclear Power Division, which appeared on pages 52 through 54
of the April 1981 issue of the EPRI Journal. The Article was by John J. Taylor.
[0007] The buildup of sludge on the tube sheet and upper tube support plates degrades the
heat transfer process from the fluid in the primary system to the fluid in the secondary
system, and may also restrict secondary fluid flow as well as producing a stagnant
zone which enhances corrosion of the tubes, tube sheet and support plates. As addressed
in Patent Application 06/370,826, the sludge which enters crevices within the tube
sheet creates further problems and serves to damage the heat exchanger tubes. As a
result, it is very important to clean the heat exchanger or steam generator to effectively
remove the sludge from the surface of the tube sheet. All of the prior art discussed
above employs the use of ultrasonics. While the methods discussed in the prior art,
especially those in Patent No. 4,320,528 and application 06/370,826, are very effective
and valuable, the requirement of using ultrasonics has several significant disadvantages.
First, in order to generate the ultrasonic waves, expensive transducers must be used.
This requires considerable effort and expense to bring the ultrasonic transducers
to the site of the steam generator and then putting them in their proper place at
the location of the steam generator. Second, in order to achieve an effective level
of ultrasonic waves, it is often necessary to cut away a portion of the steam generator
wall and put the face of the transducer at the location of the cut away portion. Many
owners of the power plant which incorporates a steam generator are very reluctant
to have a portion of the wall cut away and then later welded back in place after the
steam generator has been cleaned.
[0008] A third problem which arises with prior art aplications is the use of corrosive chemicals
to assist in the cleaning operation. While the chemicals serve to clean and remove
the sludge, they also serve to eat away at the various components of the steam generator.
Therefore, it is desirable to find a method of cleaning which does not require the
use of corrosive chemicals. One method known in the prior art is called water lancing.
This is in effect the use of a jet of water which is shot into the sludge pile for
the purpose of loosening the sludge. There are some problems with this water lancing
process. The loosening process is not very effective because it is difficult to penetrate
to the interior of the tube bundle and in addition there may be a problem of using
the jet of water to impinge against the heat exchanger tubes at that location. The
jet of water might cause sludge particles to reflect onto and then off the heat exchanger
tubes, thereby possibly resulting in damage to these tubes.
[0009] Therefore, although the use of ultrasonics combined with chemicals and the of
a jet of water are all known in the prior art for cleaning and removing sludge at
the bottom of a heat exchanger or steam generator, none of these methods can be employed
without the significant problems discussed above. At present, there has been no prior
art method for effectively removing the sludge through a very quick, inexpensive method
which does not require the use of chemicals or the cutting away of a portion of the
steam generator.
SUMMARY OF THE PRESENT INVENTION
[0010] The present invention relates to an improved method of cleaning a nuclear steam generator
or other tube bundle heat exchanger by removing the buildup of sedimentation or "sludge"
which accumulates in the bottom or on top of higher elevation support plates of a
heat exchanger vessel through utilization of a repetitive shock wave induced in the
sludge. The shock wave serves to effectively and safely loosen the products of corrosion
and other elements which settle at the bottom of the heat exchanger or steam generator
and thereby facilitates their easy removal through flushing and vacuuming the vessel.
[0011] It has been discovered, according to the present invention, that if a source of high
energy is used to generate a shock wave or pressure pulse which is directed into the
sludge pile, either directly or else into a level of water above the sludge pile,
the shock wave will impinge upon the sludge, agitate it and loosen it, and will thus
permit the sludge to remain in suspension from which it can be removed by a subsequent
water flushing and vacuuming operation.
[0012] It has also been discovered, according to the present invention, that the use of
a shock wave to loosen the sludge permits the operation to be effectively achieved
without the use of corrosive chemicals which might damage the components of the steam
generator.
[0013] It has also been discovered, according to the present invention, that the use of
a pressure pulse or shock wave can also be used in conjunction with chemical solvents,
if desired, to remove heavily encrusted materials such as magnetite from various locations
within the steam generator.
[0014] It is therefore an object of the present invention to provide a method for quickly
and efficiently loosening the products of oxidation and corrosion which settle on
top of the tube support plate at the bottom of a steam generator as well as on the
tube support plates at higher elevations.
[0015] It is another object of the present invention to provide a method for providing such
pressure or shock waves which can be utilized with existing steam generator or tube
bundle heat exchanger facilities and which will not require the cutting away of steam
generator walls to fit the pressure source into the vessel wall.
[0016] It is another object of the present invention to provide a method of cleaning the
sludge pile which can be used without corrosive chemicals but which also can be used
in conjunction with corrosive chemicals if desired.
[0017] It is a further object of the present invention to provide a method for cleaning
the steam generator which can use either a gaseous source, a liquid source or an electrical
source of generating the pressure pulse which is used to agitate and loosen the sludge
and keep it in suspension.
[0018] Further novel features and other objects of the present invention will become apparent
from the following detailed description, discussion and the appended claims taken
in conjunction with the drawings.
DRAWING SUMMARY
[0019] Referring particularly to the drawings for the purpose of illustration only and not
limitation, there is illustrated:
FIG. 1 is a side-sectional view of a typical heat exchanger or steam generator which
contains a tube bundle through which the primary fluid is circulated.
FIG. 2 is a cross-sectional view of the heat exchanger or steam generator, taken along
line 2-2 of FIG. 1.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0020] With reference to the drawings of the invention in detail and more particularly to
FIG. 1, there is shown at 10 a heat exchanger or steam generator. The external shell
or envelope 12 of said steam generator 10 is a pressure vessel. In this external shell
12 are a large number of heat exchanger tubes 32. At the base of the heat exchanger
tubes 32 is the support tube sheet 20.
[0021] At the base of the steam generator 10 is a primary entrance nozzle 24 which leads
to the entrance chamber 25 located directly below the tube sheet 20. On the opposite
side of the heat exchanger 10 is the exit chamber 27 and the primary exit nozzle 26.
The exit chamber 27 is also located directly below the tube sheet 20. The entrance
chamber 25 and the exit chamber 27 are separated by a metal wall 22.
[0022] Initially, a secondary fluid 4 enters the heat exchanger or steam generator 10 through
secondary entrance inlets 42 and 40 located in the external shell 12. The secondary
fluid 4 fills the steam generator 10 and surrounds the heat exchanger tubes 32.
[0023] In normal operation, the primary fluid 2 comes from a heat source such as a nuclear
reactor and enters said steam generator 10 through the primary entrance nozzle 24.
The fluid enters into the entrance chamber 25 and is forced through the heat exchanger
tubes 32 and up through the steam generator or heat exchanger 10. The heat exchanger
10 illustrated in FIG. 1 is of the U-bend type, where the primary heat exchanger tubes
32 run most of the length of the steam generator or heat exchanger 10 and are bent
at the top to form a U-shaped configuration. Upon reaching the uppermost portion of
the primary heat exchangers tubes 32, the primary fluid 2 starts back down the opposite
side of the primary heat exchanger tubes 32, goes into the exit chamber 27 and exits
the heat exchanger 10 through primary outlet nozzle 26.
[0024] Heat which is carried by the primary fluid 2 is transferred to the secondary fluid
4 while the primary fluid 2 is circulating through heat exchanger tubes 32. Sufficient
heat is transferred to the secondary fluid 4 so that the primary fluid 2 leaving the
exit nozzle 26 is at a substantially lower temperature than it was when it entered
the heat exchanger through entrance nozzle 24. The secondary fluid 4 absorbs heat
carried by the primary fluid 2 and said secondary fluid 4 becomes steam 8 during the
heat absorption process. Said steam 8 passes through separators 30 which remove excess
moisture from said steam 8, and then exits through steam outlet 11 at the top of the
heat exchanger or steam generator 10. The high pressure steam 8 can then be used to
drive a turbine.
[0025] The primary fluid 2 can be water. A gas such as helium or another liquid sodium can
also be used for the primary fluid. The secondary fluid is usually water.
[0026] During the process described above, a large amount of moisture and heat is generated
within the steam generator 10. This leads to corrosion of various portions of the
steam generator 10. Some of the corrosion remains on the metal, especially at the
juncture of the primary heat exchanger tubes 32 and their support plates 16. This
problem was addressed by the present inventors in their United States Patent No. 4,320,528.
Much of the corrosion and other chemical reactions do not remain on the metal but
instead settle at the bottom of the steam generator 10 and on the top of the upper
support plates 16. There is created a buildup of sedimentation or "sludge" which accumulates
at the bottom of the heat exchanger vessel and on the support plates. This sludge,
shown as 60 in FIGS. 1 and 2 includes copper oxide, magnetite, and other oxidation
or corrosion products which have not adhered to the tubing or other surfaces and therefore
accumulate at the bottom.
[0027] Reference to FIG. 1 shows the sludge pile 60 which rests on the tube sheet 20 and
surrounds the exposed lower portion of the primary heat exchanger tubes 32. The prese
nce of sludge 60 not only affects the rate of flow of the secondary fluid 4, but also
degrades the heat transfer process from the fluid in the primary system to the fluid
in the secondary system. As the sludge layer deepens, the lowermost portion of the
vessel becomes only marginally useful as a heat exchanger.
[0028] The use of ultrasonics to remove most of the sludge 60 was addressed by the present
inventors in their Patent No. 4,320,528. In that patent, transducers are placed around
the circumference of the metal wrapper 18 at the level of the sludge pile 60 and the
heat exchanger 10 is filled with an appropriate chemical solvent which covers the
sludge pile. The transducers are then activated and the combined effect of chemical
solvent and transverse sonic energy serves to agitate, loosen, and dissolve the sludge
pile. Ultrasonic cleaning is most effective when used in conjunction with a chemical
solvent. Steam generator owners are reluctant to introduce chemical solvents into
their generators. In addition, the use of a lot of transducers can be both expensive
and cumbersome to install.
[0029] It is therefore the primary desire of the present invention to create a method of
removing the sludge 60 which does not require the use of ultrasonics and their associated
transducers and which will work with only water as the solvent. The general idea of
the present invention is to use an "air gun" device to clean and remove the corrosion
deposits from a nuclear power plant steam generator or other tube bundle heat exchanger.
The concept is to induce a repetitive shock wave within a fluid layer on top of sludge
60 to thereby provide agitation which will loosen the sludge 60 and thereby permit
it to be easily removed through a subsequent flushing oeration.
[0030] Typically, the sludge pile 60 consists of a layer which can be a fraction of an inch
to several feet thick of loose iron and copper metals and oxides of granular structure
which is comparable to loose sand. One application of the present invention is to
use an air gun consisting of a high pressure air source which for example can be 2000
psi, modulated by a sharp rise-time value at a repetition of 1 Hertz to repeatedly
intorduce shock waves and pressure fluctuations in the fluid layer above and in the
sludge pile 70. The repetitive shock waves will loosen the sludge 60 and move it across
the base of the steam generator 10, where it may be removed by a subsequent flushing
and vacuuming operation. In the preferred embodiment, the sludge pile is covered with
a level of water or other fluid 4, for example to a height of approximately twelve
inches above the sludge pile 60. The shock wave is then introduced into the water
or other fluid 4 which then transmits the shock wave to the sludge pile 60. An ultrasonic
wave which was used in prior art applications is a wave of high frequency whose primary
purpose was to induce cavitation. The high frequency ultrasonic waves have short wavelengths,
low amplitudes and therefore low energy. In contrast, the concept of the present invention
is to use a pressure pulse shock wave which is generated from a very intense and powerful
compact source and is enhanced by frequent repetitions. The shock wave which is thereby
produced is of lower frequency but of much higher energy which therefore can create
a larger wavelength and a correspondingly larger movement on objects which it impacts.
The pressure pulse spherical shock wave therefore moves across either the water above
the sludge pile or else across the sludge pile in a discontinuous fashion, to thereby
loosen up the sludge.
[0031] Having thus described the concept of the present invention, one embodiment to produce
the above result is illustrated in FIGS. 1 and 2. In most embodiments, the outer shell
12 of the steam generator has a series of small holes which are known as "hand holes"
located near its lower portion and near the support tube sheet. These holes can be
anywhere from approximately 1 to 6 inches in diameter. Also, manway s,
drain and vent lines can be used if available. One such hole is shown at 14 in FIG.
1. It will be appreciated that a conventional steam generator may contain any multiplicity
of such holes which are located around the circumference of outer shell 12 or else
can be lcoated in several vertical rows along the outer shell. While only one such
hole 14 is shown in FIG. 1, it will be appreciated that any multiplicity of such holes
14 can be located around the circumference of the steam generator 10, in one or more
vertical rows.
[0032] A Pressure Pulse Shock Wave Source 80 is located outside of the steam generator 10
and in alignment with a corresponding one of said hand holes 14. In some embodiments,
the Pressure Pulse Shock Wave Source 80 can be fit directly into a hand hole 14. In
other embodiments, as shown in FIG. 1, an Interface Means 70 joins the Pressure Pulse
Shock Wave Source 80 to the hand hole 14. While only one Pressure Pulse Shock Wave
Source 80 and associated Interface Means 70 is shown in FIG. 1, it will be appreciated
that the scope of the present invention encompasses the utilization of any multiplicity
of Pressure Pulse Shock Wave Sources 80 with or without associated Interface Means
70 located either adjacent one another in associated adjacent hand holes 14 or else
in spaced locations around the circumference of the outer shell 12 either all in the
same vertical row or else in various vertical rows. Alternatively, the Pressure Pulse
Shock Wave source 80 can be located inside the steam generator 10 and can be placed
in any position inside the steam generator 10, utilizing hand holes, manways, drain
lines, and vent lines. In some cases it may be desirable to locate the sources in
lanes or spaces interior to the tube bundle which are accessible from the shell penetrations.
Also, more than one source 80 can be used inside and adjacent the heat exchanger 10.
Also, sources may be located at higher elevations with the fluid layer level raised
appropriately to immerse them.
[0033] The preferred method of the present invention is as follows. A multiplicity of Pressure
Pulse Shock Wave Source 80 is placed around the circumference of the shell 12, with
one Pressure Pulse Shock Wave Source 80 placed into an associated one hand hole 14.
Where applicable depending on the type of Pressure Pulse Shock Wave Source 80 used,
an Interface Means 70 connects the Pressure Pulse Shock Wave Source 80 into the hand
hole 14. The sludge pile 60 is covered with a liquid medium such as water 4, to a
depth of approximately twelve inches above the sludge pile. It will be appreciated
that other water levels, both greater than or less than twelve inches are certainly
within the spirit and scope of the present invention. The liquid such as water 4 can
be placed into the steam generator 10 through othr hand holes, manways and penetrations
in the shell 12. The Pressure Pulse Shock Wave Sources 80 are then activated to emit
a very intense and powerful shock wave 72 which is transmitted directly into the liquid
4 above the sludge pil 60. The shock wave which for example can be a spherical shock
wave is transmitted from the liquid 4 to the sludge pile 60 and serves to impinge
upon the sludge pile 60, agitate it, and loosen the encrusted sludge 60.
[0034] In the preferred embodiment, one or a multiplicity of Pressure Pulse Shock Wave Sources
80 emit a high pressure shock wave at a pressure ranging from 50 to 5000 pounds per
square inch (psi). The Pressure Pulse Shock Wave Sources 80 contain a valve which
can be rapidly and repeatedly opened and closed to provide the pressure pulses. By
way of example, the valve can be opened and closed approximately once each second.
On a scale of pressure versus time, it is preferable to create a shock wave which
produces a pressure level range of approximately 1/100th to 100 Bars of Pressure at
1 Meter. A desirable pressure scale is illustrated in Figure A 17 of the technical
paper OTC 4255, "Marine Seismic Energy Sources Acoustic Performance Comparison" by
Roy C. Johnston, ARCO Oil & Gas Co., and Byron Cain, Geophysical Service
Inc. It will now be appreciated why in the preferred embodiment the sludge pile should
be covered with a layer of water or other liquid. Due to the intense pressure created,
it is necessary to have the liquid layer over the sludge to act like a cap to help
absorb the strength of the shock. The wavelengths of the shock waves produced can
range from approximately 0 Hertz to 1000 Hertz. The effect, therefore, is to tear
a hole in the water, then into the sludge, impinge upon the sludge, agitate it and
loosen it, and then allow it to remain in suspension from which it can be removed.
While the pressure source is in action to keep the sludge in suspension, the steam
generator 10 is continuously flushed with water to remove the sludge. Manways, hand
holes or other penetrations in the shell 12 are used to provide inlets and exits for
this flushing. The flushing water is filtered outside the heat exchanger to remove
the sludge particles. The sludge particles are removed from the flushing water outside
the steam generator using filters, settling tanks, separator or a combination thereof.
Depending upon the extent of the sludge and the amount and intensity of the desired
applied pressure pulse, the time over which the pressure pulses are provided can range
from approximately 1 hour to approximately 24 hours.
[0035] Another advantage of using the pressure pulse technique is that the spherical shock
wave emitted can reflect off various surfaces of the heat exchanger tubes 32 to thereby
clean the tubes from the rear as well as from the direct frontal impact of the shockwave.
This facilitates the use of fewer Pressure Pulse Shock Wave Sources 80. While any
type of air pressure generating source is within the spirit and scope of the present
invention, it is preferred that the source emit a non-oxidizing gas such as nitrogen.
In this way, oxygen will not be placed inside the steam generator 10. This is important
because the oxygen will lead to corrosion of the steam generator components which
is exactly the problem the present invention is addressing.
[0036] So far the present invention has been described with the use of an air source. It
is also within the spirit and scope of the present invention to provide a Pressure
Pulse Shock Wave Source from a water source or an electrical spark source. An air
source, a water source and an electrical source are all usable with the present invention
provided the source creates a shock wave or pressure pulse which travels radially
outward from the source, thereby giving everything in its path a kick. The repetitions
can be approximately once each second with the frequencies and pressures previously
set forth.
[0037] So far, the present invention has been described as being used only with water which
acts as a cap over the sludge pile 60. As previously mentioned, one advantage of the
present invention is that it can be used without corrosive chemicals which might damage
the components of the steam generator 10. However, the present invention can be used
with cleaning solvents and chemicals in conjunction with or else without the water.
When used in conjunction with chemicals, the use of the repetitive shock wave or pressure
pulse induced in the cleaning solvent, water or chemical, provides agitation to loosen
and transport the corrosion deposit and to bring fresh solvent to the corrosion/solvent
interface. The technique, therefore, can be used to remove heavily encrusted deposits
such as magnetite from the junctions of the heat exchanger tubes 32 and their associated
tube support plates 16. The pressure pulse or shock wave moves into and laterally
of the junction between the tube support sheet and the heat exchanger tubes, to thereby
remove used solvent and allow fresh chemical solvent to arrive at the junction to
eat away at the encrusted magnetite.
[0038] Therefore, in summary, the present invention involves a method of removing the pile
of sludge which set on the tube sheet comprising, placing a Pressure
Pulse Shock Wave Source into one or more of the multiplicity of hand holes, manways,
drain lines and vents filling the steam generator with a liquid to a level above said
pile of sludge, activating the Pressure Pulse Shock Wave Sources to generate a series
of repetitive shock waves approximately once every second into the liquid and from
the liquid into the pile of sludge, containing the generation of repetitive shock
waves which are generated with pressure between approximately 50 pounds per square
inch and 5000 pounds per square inch which produce a range of frequencies between
0 Hertz and 1000 Hertz to create shock waves which produce a pressure level of approximately
1/100th to 100 Bars of Pressure at 1 Meter, continuing the shock wave impact for approximately
1 to 24 hours whereby the impact of the spherical shock waves serves to agitate and
loosen the sludge and permits the sludge to remain in suspension, and flushing the
steam generator with a liquid and vacuuming the steam generator to remove the liquid
and carry the loosened sludge with it.
[0039] The above description of the present invention has concentrated on removing sludge
from the bottom tube support sheet. The application of the above-described present
invention can also be used to remove sludge which has accumulated on top of the tube
support plates 16. The same process is used but the liquid level is raised to several
inches above the level of sludge to be removed. The Pressure Pulse Shock Wave Source
may be correspondingly raised to strengthen the shock wave at the upper levels, but
this may not be required. Similarly, the flushing water may be directed or channeled
to the upper support plates to intensify the transport of the sludge from those areas.
[0040] Of course, the present invention is not intended to be restricted to any particular
form or arrangement, or any specific embodiment disclosed herein, or any specific
use, since the same may be modified in various particulars or relations without departing
from the spirit or scope of the claimed invention herein above shown and described
of which the method shown is intended only for illustration and for disclosure of
an operative embodiment and not to show all of the various forms of modification in
which the invention might be embodied.
[0041] The invention has been described in considerable detail in order to comply with the
patent laws by providing a full public disclosure of at least one of its forms. However,
such detailed description is not intended in any way to limit the broad features of
principles of the invention, or the scope of patent monopoly to be granted.
1. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the bottom of a tube
bundle heat exchanger, the tube bundle heat exchanger characterized by a tube bundle
heat exchanger wall and a thick metal plate known as a tube sheet near the lower portion
of the tube bundle heat exchanger wall's interior surface, the tube sheet serving
to support the lower ends of a multiplicity of heat exchanger tubes within the tube
bundle heat exchanger, the tube bundle heat exchanger wall further comprising a multiplicity
of small holes known as hand holes, manways, drain lines and vents, located around
its circumference and above the tube sheet, the method of removing the pile of sludge
which settles on the tube sheet comprising:
a. locating at least one air-gun type pressure pulse shock wave source outside the
tube bundle heat exchanger so as to be able to introduce pressure pulse shock waves
through one or more of the multiplicity of hand holes, manways, drain lines and vents;
b. filling said tube bundle heat exchanger with a liquid to a level above said pile
of sludge;
c. activating the at least one air-gun type pressure pulse shock wave source to generate
a repetitive series of explosive, transient shock waves into said liquid and from
said liquid into said pile of sludge such that the explosive transient shock waves
and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter;
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid; and
f. draining the liquid from the heat exchanger and removing said at least one air-gun
type pressure pulse shock wave source.
2. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the bottom of a tube
bundle heat exchanger, the tube bundle heat exchanger characterized by a tube bundle
heat exchanger wall and a thick metal plate known as a tube sheet near the lower portion
of the tube bundle heat exchanger wall's interior surface, the tube sheet serving
to support the lower ends of a multiplicity of heat exchanger tubes within the tube
bundle heat exchanger, the tube bundle heat exchanger wall further comprising a multiplicity
of small holes known as hand holes, manways, drain line and vents, located around
its circumference and above the tube sheet, the method of removing the pile of sludge
which settles on the tube sheet comprising:
a. introducing at least one air-gun type pressure pulse shock wave source through
one or more of the multiplicity of hand holes, manways, drain lines and vents such
that the at least one air-gun type pressure pulse shock wave source is located inside
the tube bundle heat exchanger;
b. filling said tube bundle heat exchanger with a liquid to a level above said pile
of sludge;
c. activating the at least one air-gun type pressure pulse shock wave source to generate
a repetitive series of explosive, transient shock waves into said liquid and from
said liquid into said pile of sludge such that the explosive, transient shock waves
and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter;
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid; and
f. draining the liquid from the heat exchanger and removing said at least one air-gun
type pressure pulse shock wave source.
3. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the tube support plates
of a tube bundle heat exchanger, the tube bundle heat exchanger characterized by a
tube bundle heat exchanger wall and a series of tube support plates arranged transverse
to and sequentially spaced along the longitudinal axis of a multiplicity of heat exchanger
tubes and forming junctions therewith, the tube bundle heat exchanger further character
ized by a thick metal plate known as a tube sheet near the lower portion of the heat
exchanger wall, the tube sheet serving to support the lower ends of the heat exchanger
tubes, the tube bundle heat exchanger wall further comprising a multiplicity of small
holes known as hand holes, manways, drain lines and vents, located around its circumference
and along the height of the tube bundle heat exchanger, the method of removing the
pile of sludge which settles on the tube support plates and the junctions between
the heat exchanger tubes and the tube support plates, comprising:
a. locating at least one air-gun type pressure pulse shock wave source outside the
tube bundle heat exchanger so as to be able to introduce pressure pulse waves through
one or more of the multiplicity of hand holes, manways, drain lines and vents;
b. filling said tube bundle heat exchanger with a liquid to a level at or above said
tube support plate to be cleaned;
c. activating the at least one air-gun type pressure pulse shock wave source to generate
a repetitive series of explosive, transient shock waves into said liquid and from
said liquid into said pile of sludge and into the junctions between the tube support
plate and the heat exchanger tubes such that the explosive transient shock waves and
resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter; and
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically activate and move the sludge in the liquid.
4. A method of removing the products of corrosion, oxidation, sedimentation and comaprable
chemical reactions collectively known as sludge which settle on the tube support plates
of a tube bundle heat exchanger, the tube bundle heat exchanger characterized by a
tube bundle heat exchanger wall and a series of tube support plates arranged transverse
to and sequentially spaced along the longitudinal axis of a multiplicity of heat exchanger
tubes and forming junctions therewith, the tube bundle heat exchanger further characterized
by a thick metal plate known as a tube sheet near the lower portion of the heat exchanger
wall, the tube sheet serving to support the lower ends of the heat exchanger tubes,
the tube bundle heat exchanger wall further comprising a multiplicity of small holes
known as hand holes, manways, drain lines and vents, located around its circumference
and along the height of the tube bundle heat exchanger, the method of removing the
pile of sludge which settles on the tube support plates and the junctions between
the heat exchanger tubes and the tube support plates, comprising:
a. introducing at least one air-gun type pressure pulse shock wave source through
one or more of the multiplicity of hand holes, manways, drain lines and vents such
that the at least one air-gun type pressure pulse shock wave source is located inside
the tube bundle heat exchanger;
b. filling said tube bundle heat exchanger with a liquid to a level at or above said
tube support plate to be cleaned;
c. activating the at least one air-gun type pressure pulse shock wave source to generate
a repetitive series of explosive, transient shock waves into said liquid and from
said liquid into said pile of sludge and into the junctions between the tube support
plate and the heat exchanger tubes such that the explosive, transient shock waves
and resultant liquid motion serve to agitate and
loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter; and
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid.
5. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the bottom of a tube
bundle heat exchanger, the tube bundle heat exchanger characterized by a tube bundle
heat exchanger wall and a thick metal plate known as a tube sheet near the lower portion
of the tube bundle heat exchanger wall's interior surface, the tube sheet serving
to support the lower ends of a multiplicity of heat exchanger tubes within the tube
bundle heat exchanger, the tube bundle heat exchanger wall further comprising a multiplicity
of small holes known as hand holes, manways, drain lines and vents, located around
its circumference and above the tube sheet, the method of removing the pile of sludge
which settles on the tube sheet comprising:
a. locating at least one pressurized gas-type pressure pulse shock wave source outside
the tube bundle heat exchanger so as to be able to introduce pressure pulse shock
waves through one or more of the multiplicity of hand holes, manways, drain lines
and vents;
b. filling said tube bundle heat exchanger with a liquid to a level above said pile
of sludge;
c. activating the at least one pressurized gas-type pressure pulse shock wave source
to generate a repetitive series of explosive transient shock waves into said liquid
and from said liquid into said pile of sludge such that the explosive transient shock
waves and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter;
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid; and
f. draining the liquid from the heat exchanger and removing said at least one pressurized
gas-type pressure pulse shock wave source.
6. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the bottom of a tube
bundle heat exchanger, the tube bundle heat exchanger characterized by a tube bundle
heat exchanger wall and a thick metal plate known as a tube sheet near the lower portion
of the tube bundle heat exchanger wall's interior surface, the tube sheet serving
to support the lower ends of a multiplicity of heat exchanger tubes within the tube
bundle heat exchanger, the tube bundle heat exchanger wall further comprising a multiplicity
of small holes known as hand holes, manways, drain lines and vents, located around
its circumference and above the tube sheet, the method of removing the pile of sludge
which settles on the tube sheet comprising:
a. introducing at least one pressurized gas-type press
ure pulse shock wave source through one or more of the multiplicity of hand holes,
manways, drain lines and vents such that the at least one pressurized gastype pressure
pulse shock wave source is located inside the tube bundle heat exchanger;
b. filling said tube bundle heat exchanger with a liquid to a level above said pile
of sludge;
c. activating the at least one pressurized gas- type pressure pulse shock wave source
to generate a repetitive series of explosive, transient shock waves into said liquid
and from said liquid into said pile of sludge such that the explosive, transient shock
waves and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter;
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid; and
f. draining the liquid from the heat exchanger and removing said at least one pressurized
gas-type pressure pulse shock wave source.
7. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the tube support plates
of a tube bundle heat exchanger, the tube bundle heat exchanger characterized by a
tube bundle heat exchanger wall and a series of tube support plates arranged transverse
to and sequentially spaced along the longitudinal axis of a multiplicity of heat exchanger
tubes and forming junctions therewith, the tube bundle heat exchanger further characterized
by a thick metal plate known as a tube sheet near the lower portion of the heat exchanger
wall, the tube sheet serving to support the lower ends of the heat exchanger tubes,
the tube bundle heat exchanger wall further comprising a multiplicity of small holes
known as hand holes, manways, drain lines and vents, located around its circumference
and along the height of the tube bundle heat exchanger, the method of removing the
pile of sludge which settles on the tube support plates and the junctions between
the heat exchanger tubes and the tube support plates, comprising:
a. locating at least one pressurized gas-type pressure pulse shock wave source outside
the tube bundle heat exchanger so as to be able to introduce pressure pulse shock
waves through one or more of the multiplicity of hand holes, manways, drain lines
and vents;
b. filling said tube bundle heat exchanger with a liquid to a level at or above said
tube support plate to be cleaned;
c. activating the at least one pressurized gas-type pressure pulse shock wave source
to generate a repetitive series of explosive transient shock waves into said liquid
and from said liquid into said pile of sludge and into the junctions between the tube
support plate and the heat exchanger tubes such that the explosive, transient shock
waves and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter; and
e. continuing the shock wave impact for approximately 1 to 24 hours
whereby the impact of the repetitive, explosive, transient shock waves and resultant
liquid motion serves to mechanically agitate and move the sludge in the liquid.
8. The invention as defined in Claim 7 wherein said tube bundle heat exchanger is
filled with liquid and the level of liquid is selectively varied.
9. A method of removing the products of corrosion, oxidation, sedimentation and comparable
chemical reactions collectively known as sludge which settle on the tube support plates
of a tube bundle heat exchanger, the tube bundle heat exchanger characterized by a
tube heat exchanger wall and a series of tube support plates arranged transverse to
and sequentially spaced along the longitudinal axis of a multiplicity of heat exchanger
tubes and forming junctions therewith, the tube bundle heat exchanger further characterized
by a thick metal plate known as a tube sheet near the lower portion of the heat exchanger
wall, the tube sheet serving to support the lower ends of the heat exchanger tubes,
the tube bundle heat exchanger wall further comprising a multiplicity of small holes
known as hand holes, manway, drain lines and vents, located around its circumference
and along the height of the tube bundle heat exchanger, the method of removing the
pile of sludge which settles on the tube support plates and the junctions between
the heat exchanger tubes and the tube support plates, comprising:
a. introducing at least one pressurized gas-type pressure pulse shock wave source
through one or more of the multiplicity of hand holes, manways, drain lines and vents
such that the at least one pressurized gas-type pressure pulse shock wave source is
located inside the tube bundle heat exchanger;
b. filling said tube bundle heat exchanger with a liquid to a level at or above said
tube support plate to be cleaned;
c. activating the at least one pressurized gas-type pressure pulse shock wave source
to generate a repetitive series of explosive transient shock waves into said liquid
and from said liquid into said pile of sludge and into the junctions between the tube
support plate and the heat exchanger tubes such that the explosive, transient shock
waves and resultant liquid motion serve to agitate and loosen the sludge;
d. continuing the generation of repetitive, explosive, transient shock waves which
are generated with pressure between approximately 50 pounds per square inch and 5000
pounds per square inch which result in energy predominantly in the frequency range
between 1 Hertz and 1000 Hertz for each pulse to create transient shock waves which
produce a pressure level of approximately 1/100th to 100 Bars in the liquid of Pressure
at 1 meter; and
e. continuing the shock wave impact for approximately 1 to 24 hours whereby the impact
of the repetitive, explosive, transient shock waves and resultant liquid motion serves
to mechanically agitate and move the sludge in the liquid.
10. The invention as defined in Claim 9 wherein said tube bundle heat exchanger is
filled with liquid and the level of liquid is selectively varied.