EP0265549B1 - Method of pressure pulse cleaning a tube bundle heat exchanger - Google Patents

Method of pressure pulse cleaning a tube bundle heat exchanger Download PDF

Info

Publication number
EP0265549B1
EP0265549B1 EP86115100A EP86115100A EP0265549B1 EP 0265549 B1 EP0265549 B1 EP 0265549B1 EP 86115100 A EP86115100 A EP 86115100A EP 86115100 A EP86115100 A EP 86115100A EP 0265549 B1 EP0265549 B1 EP 0265549B1
Authority
EP
European Patent Office
Prior art keywords
heat exchanger
sludge
shock wave
tube
pressure pulse
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP86115100A
Other languages
German (de)
French (fr)
Other versions
EP0265549A1 (en
Inventor
Terry D. Sharton
George B. Taylor
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Anco Engineers Inc
Original Assignee
Anco Engineers Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to US06/742,134 priority Critical patent/US4655846A/en
Application filed by Anco Engineers Inc filed Critical Anco Engineers Inc
Priority to DE8686115100T priority patent/DE3679674D1/en
Priority to AT86115100T priority patent/ATE64189T1/en
Priority to ES86115100T priority patent/ES2022803B3/en
Priority to EP86115100A priority patent/EP0265549B1/en
Publication of EP0265549A1 publication Critical patent/EP0265549A1/en
Application granted granted Critical
Publication of EP0265549B1 publication Critical patent/EP0265549B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G7/00Cleaning by vibration or pressure waves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G7/00Cleaning by vibration or pressure waves
    • F28G7/005Cleaning by vibration or pressure waves by explosions or detonations; by pressure waves generated by combustion processes

Definitions

  • 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.
  • 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.
  • a tube sheet 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.
  • a second problem has also troubled steam generators for many years.
  • 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.
  • a third problem which arises with prior art adjations 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.
  • a method of removing the products of corrosion, oxidation, sedimentation and comparable chemical reactions collectively known. as sludge which settle in a tube bundle heat exchanger the tube bundle heat exchanger including a tube bundle heat exchanger wall, a multiplicity of heat exchanger tubes and preferably a series of tube support plates arranged transverse to and sequentially space along the longitudinal axis of the multiplicity of heat exchanger tubes and forming junctions therewith, the tube bundle heat exchanger further including 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 above the tube sheet and preferably along the height of the tube bundle heat exchanger, the method of removing the pile of sludge which settles on the tube sheet or on the tube support plates and the junctions between the heat exchanger tubes
  • 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.
  • 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.
  • 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.
  • the present invention provides 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.
  • the present invention provides further 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.
  • the present invention provides 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.
  • 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.
  • 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.
  • a primary entrance nozzle 24 which leads to the entrance chamber 25 located directly below the tube sheet 20.
  • the exit chamber 27 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.
  • a secondary fluid 4 enters the heat exchanger or steam generator 10 through secondary entrance inlet 42 located in the external shell 12.
  • the secondary fluid 4 fills the steam generator 10 and surrounds the heat exchanger tubes 32.
  • 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.
  • 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.
  • 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.
  • 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.
  • 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 presence 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.
  • 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 operation.
  • 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 introduce 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.
  • 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.
  • 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.
  • 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, manways, 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.
  • 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.
  • the Pressure Pulse Shock Wave Source 80 can be fit directly into a hand hole 14.
  • 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 in the present invention it is possible to utilize 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.
  • 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.
  • 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.
  • 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 possible.
  • the liquid such as water 4 can be placed into the steam generator 10 through other 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 pile 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.
  • 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.
  • 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.
  • 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.
  • the steam generator 10 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.
  • the time over which the pressure pulses are provided can range from approximately 1 hour to approximately 24 hours.
  • 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.
  • the present invention has been described as being used only with water which acts as a cap over the sludge pile 60.
  • 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.
  • the present invention can be used with cleaning solvents and chemicals in conjunction with or else without the water.
  • 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.
  • 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 1/100 th 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
  • 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.
  • the flushing water may be directed or channeled to the upper support plates to intensify the transport of the sludge from those areas.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Cleaning In General (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Heat Treatment Of Articles (AREA)

Abstract

The present invention relates to an improved method of cleaning a tube bundle heat exchanger by removing the buildup of sedimentation or "sludge" which accumulates in the bottom or at other elevations of a heat exchanger vessel through utilization of a repetitive shock wave induced in the water layer above 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.

Description

    BACKGROUND OF THE INVENTION 1. FIELD OF THE INVENTION
  • 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
  • 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.
  • 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.
  • 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.
  • 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 Teumacet 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.
  • 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.
  • 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.
  • 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.
  • Therefore, although the use of ultrasonics combined with chemicals and the use 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
  • According to one aspect of the invention, there is provided a method of removing the products of corrosion, oxidation, sedimentation and comparable chemical reactions collectively known. as sludge which settle in a tube bundle heat exchanger, the tube bundle heat exchanger including a tube bundle heat exchanger wall, a multiplicity of heat exchanger tubes and preferably a series of tube support plates arranged transverse to and sequentially space along the longitudinal axis of the multiplicity of heat exchanger tubes and forming junctions therewith, the tube bundle heat exchanger further including 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 above the tube sheet and preferably along the height of the tube bundle heat exchanger, the method of removing the pile of sludge which settles on the tube sheet or on the tube support plates and the junctions between the heat exchanger tubes and the tube support plates, being characterized by:
    • 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 or 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 the tube bundle heat exchanger with a liquid to a level at or above the tube sheet or the 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 the liquid and from the liquid into the pile of sludge or into the 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 1/100 th 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; and
    • f. after removing the sludge from the heat exchanger draining the liquid from the heat exchanger and removing the at least one air-gun type pressure pulse shock wave source.
  • 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.
  • 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.
  • 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.
  • 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.
  • 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.
  • Additionally, the present invention provides 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.
  • The present invention provides further 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.
  • Finally, the present invention provides 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.
  • DRAWING SUMMARY
  • 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
  • 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.
  • 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.
  • Initially, a secondary fluid 4 enters the heat exchanger or steam generator 10 through secondary entrance inlet 42 located in the external shell 12. The secondary fluid 4 fills the steam generator 10 and surrounds the heat exchanger tubes 32.
  • 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.
  • 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.
  • 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.
  • 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.
  • 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 presence 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.
  • 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.
  • 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 operation.
  • 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 introduce 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.
  • 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, manways, 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.
  • 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 in the present invention it is possible to utilize 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.
  • 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 possible. The liquid such as water 4 can be placed into the steam generator 10 through other 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 pile 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.
  • 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 1/100 th 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.
  • 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 possible, 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.
  • So far the present invention has been described with the use of an air source. It is also possible 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.
  • 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.
  • 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 1/100 th 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.
  • 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.

Claims (3)

1. A method of removing the products of corrosion, oxidation, sedimentation and comparable chemical reactions collectively known as sludge which settle in a tube bundle heat exchanger, the tube bundle heat exchanger including a tube bundle heat exchanger wall, a multiplicity of heat exchanger tubes and preferably a series of tube support plates arranged transverse to and sequentially spaced along the longitudinal axis of the multiplicity of heat exchanger tubes and forming junctions therewith, the tube bundle heat exchanger further including 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 above the tube sheet and preferably along the height of the tube bundle heat exchanger, the method of removing the pile of sludge which settles on the tube sheet or on the tube support plates and the junctions between the heat exchanger tubes and the tube support plates, being characterized by:
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 or 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 sheet or 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 or 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 1/100 th 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; and
f. after removing the sludge from the heat exchanger draining the liquid from the heat exchanger and removing said at least one air-gun type pressure pulse shock wave source.
2. A method as claimed in Claim 1, wherein, instead of an air-gun, a pressurized gas-type pressure pulse shock wave source is used.
3. A method according to Claim 2 applied on tube support plates, wherein said tube bundle heat exchanger is filled with liquid and the level of liquid is selectively varied.
EP86115100A 1983-04-19 1986-10-30 Method of pressure pulse cleaning a tube bundle heat exchanger Expired - Lifetime EP0265549B1 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
US06/742,134 US4655846A (en) 1983-04-19 1985-06-06 Method of pressure pulse cleaning a tube bundle heat exchanger
DE8686115100T DE3679674D1 (en) 1986-10-30 1986-10-30 PRESSURE-PULSE CLEANING PROCESS FOR A TUBE BUNDLE HEAT EXCHANGER.
AT86115100T ATE64189T1 (en) 1986-10-30 1986-10-30 PRESSURE PULSATING CLEANING PROCESS FOR A TUBE BUNDLE HEAT EXCHANGER.
ES86115100T ES2022803B3 (en) 1986-10-30 1986-10-30 CLEANING METHOD BY IMPULSE PRESSURE OF A TUBULAR BEAM HEAT EXCHANGER.
EP86115100A EP0265549B1 (en) 1986-10-30 1986-10-30 Method of pressure pulse cleaning a tube bundle heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP86115100A EP0265549B1 (en) 1986-10-30 1986-10-30 Method of pressure pulse cleaning a tube bundle heat exchanger

Publications (2)

Publication Number Publication Date
EP0265549A1 EP0265549A1 (en) 1988-05-04
EP0265549B1 true EP0265549B1 (en) 1991-06-05

Family

ID=8195547

Family Applications (1)

Application Number Title Priority Date Filing Date
EP86115100A Expired - Lifetime EP0265549B1 (en) 1983-04-19 1986-10-30 Method of pressure pulse cleaning a tube bundle heat exchanger

Country Status (4)

Country Link
EP (1) EP0265549B1 (en)
AT (1) ATE64189T1 (en)
DE (1) DE3679674D1 (en)
ES (1) ES2022803B3 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102012104744A1 (en) 2012-06-01 2013-12-05 Karl Karner Device for removing clogging deposit in fluid-carrying lines, has electrical conduction line that is insulated during operation of high-voltage conductors so as to ignite at open end by high voltage arc discharge and trigger shock wave

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5002079A (en) * 1988-12-15 1991-03-26 Westinghouse Electric Corp. Pressure pulse method and system for removing debris from nuclear fuel assemblies
US5092355A (en) * 1988-12-15 1992-03-03 Westinghouse Electric Corp. Pressure pulse method for removing debris from nuclear fuel assemblies
US7093649B2 (en) 2004-02-10 2006-08-22 Peter Dawson Flat heat exchanger plate and bulk material heat exchanger using the same
GB0916887D0 (en) 2009-09-28 2009-11-11 Wellmack Resources Ltd Improved blockage apparatus and method
US10502510B2 (en) 2016-02-09 2019-12-10 Babcock Power Services, Inc. Cleaning tubesheets of heat exchangers
CN107457230B (en) * 2017-09-05 2019-10-25 马鞍山久特新材料科技有限公司 A kind of solar pipe automatic flushing device
CN112974444B (en) * 2018-07-26 2022-09-23 德州鲁斯泰铝业有限公司 Use method of air explosion cleaning equipment for columnar garbage can

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2351163A (en) * 1943-01-21 1944-06-13 Diamond Power Speciality Boiler cleaner
GB686842A (en) * 1950-01-25 1953-02-04 Airnesco Products Ltd Fluid pressure actuated blast gun primarily for cleaning purposes
BE666832A (en) * 1964-07-13
US3457108A (en) * 1964-08-03 1969-07-22 Dow Chemical Co Method of removing adherent materials
US4276856A (en) * 1978-12-28 1981-07-07 Westinghouse Electric Corp. Steam generator sludge lancing method
DE2948201C2 (en) * 1979-11-30 1985-09-26 Degussa Ag, 6000 Frankfurt Apparatus and method for periodically cleaning heat exchanger tubes from solid deposits and the use of this apparatus
US4320528A (en) * 1980-01-23 1982-03-16 Anco Engineers, Inc. Ultrasonic cleaner
US4492113A (en) * 1982-12-10 1985-01-08 Philip Weatherholt Method and apparatus for cleaning and testing heat exchangers
US4461651A (en) * 1983-02-08 1984-07-24 Foster Wheeler Limited Sonic cleaning device and method
US4632705A (en) * 1984-03-20 1986-12-30 Westinghouse Electric Corp. Process for the accelerated cleaning of the restricted areas of the secondary side of a steam generator
US4774975A (en) * 1984-09-17 1988-10-04 Westinghouse Electric Corp. Method and apparatus for providing oscillating contaminant-removal stream
FR2573179B1 (en) * 1984-11-13 1987-02-13 Framatome Sa SLUDGE REMOVAL DEVICE FOR CLEANING INSTALLATION OF THE TUBULAR PLATE OF A STEAM GENERATOR AND INSTALLATION COMPRISING SUCH A DEVICE

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102012104744A1 (en) 2012-06-01 2013-12-05 Karl Karner Device for removing clogging deposit in fluid-carrying lines, has electrical conduction line that is insulated during operation of high-voltage conductors so as to ignite at open end by high voltage arc discharge and trigger shock wave

Also Published As

Publication number Publication date
ATE64189T1 (en) 1991-06-15
ES2022803B3 (en) 1991-12-16
DE3679674D1 (en) 1991-07-11
EP0265549A1 (en) 1988-05-04

Similar Documents

Publication Publication Date Title
US4655846A (en) Method of pressure pulse cleaning a tube bundle heat exchanger
US4699665A (en) Method of pressure pulse cleaning heat exchanger tubes, upper tube support plates and other areas in a nuclear steam generator and other tube bundle heat exchangers
US4645542A (en) Method of pressure pulse cleaning the interior of heat exchanger tubes located within a pressure vessel such as a tube bundle heat exchanger, boiler, condenser or the like
US4320528A (en) Ultrasonic cleaner
US6572709B1 (en) Ultrasonic cleaning method
US4756770A (en) Water slap steam generator cleaning method
US4773357A (en) Water cannon apparatus and method for cleaning a tube bundle heat exchanger, boiler, condenser, or the like
US5764717A (en) Chemical cleaning method for the removal of scale sludge and other deposits from nuclear steam generators
CA2378932C (en) An ultrasonic cleaning method
US6290778B1 (en) Method and apparatus for sonic cleaning of heat exchangers
EP0265549B1 (en) Method of pressure pulse cleaning a tube bundle heat exchanger
JP3293928B2 (en) Ultrasonic cleaning method and apparatus
US4276856A (en) Steam generator sludge lancing method
US4972805A (en) Method and apparatus for removing foreign matter from heat exchanger tubesheets
JPS58127003A (en) Method and apparatus for removing sludge deposited onto pipe support plate of steam generator
US5092280A (en) Pressure pulse cleaning apparatus
EP0339288B1 (en) Improved pressure pulse cleaning method
JPH0217390A (en) Method of separating and removing sludge and foreign matter from inside of heat exchanger
EP0458533B1 (en) Chemical cleaning method for steam generators utilizing pressure pulsing
US5092355A (en) Pressure pulse method for removing debris from nuclear fuel assemblies
US20060018419A1 (en) Heat exchange system for a cavitation chamber
US4071376A (en) Ultrasonic cleaning with floating transducers
US5002079A (en) Pressure pulse method and system for removing debris from nuclear fuel assemblies
GB1323317A (en) Method and apparatus for generating a shock wave beneath the surface of a body of water
JPS63116099A (en) Pressure-pulse cleaning method of bundle type heat exchanger

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE

17P Request for examination filed

Effective date: 19880926

17Q First examination report despatched

Effective date: 19900220

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRE;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.SCRIBED TIME-LIMIT

Effective date: 19910605

Ref country code: LI

Effective date: 19910605

Ref country code: CH

Effective date: 19910605

Ref country code: AT

Effective date: 19910605

Ref country code: SE

Effective date: 19910605

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 19910605

Ref country code: NL

Effective date: 19910605

REF Corresponds to:

Ref document number: 64189

Country of ref document: AT

Date of ref document: 19910615

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3679674

Country of ref document: DE

Date of ref document: 19910711

ET Fr: translation filed
REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19911031

NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19970917

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19971007

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 19971021

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19971030

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19971105

Year of fee payment: 12

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19981030

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19981031

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19981031

BERE Be: lapsed

Owner name: ANCO ENGINEERS INC.

Effective date: 19981031

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19981030

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990630

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 19990803

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 19991113