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

Claim 2

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the exposed surfaces of the tube support plate and the flow holes within the tube support plate so that the tube support plate and flow holes are clean; e. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 3

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjaent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of the heat exchanger; b. filling said heat exchanger wiTh a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 ;pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the tube support plate just below the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 4

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjaent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of the heat exchanger; b. filling said heat exchanger wiTh a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 ;pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the tube support plate just below the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 5

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plats contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side; and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level between the upper and lower surface of the tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level within the thickness of the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 6

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plats contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side; and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level between the upper and lower surface of the tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level within the thickness of the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 7

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just above the support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. varying the level of liquid from above to just below the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 8

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just above the support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. varying the level of liquid from above to just below the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 9

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through whch objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at leat one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source presure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. varying the level of liquid from just below to just above the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 10

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through whch objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at leat one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source presure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. varying the level of liquid from just below to just above the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 11

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level below the lowermost tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. filling the heat exchanger with additional liquid at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is above the uppermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 12

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level below the lowermost tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. filling the heat exchanger with additional liquid at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is above the uppermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 13

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level above the uppermost tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave sources; d. removing liquid from the heat exchanger at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is below the lowermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 14

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level above the uppermost tube support plate to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave sources; d. removing liquid from the heat exchanger at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is below the lowermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 15

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the area of the components of the heat exchanger to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned; e. changing the water level to a level just below the next area of the components of the heat exchanger to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each area of the components of the heat exchanger to be cleaned until all of said areas have been cleaned.

Claim 16

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the area of the components of the heat exchanger to be cleaned; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned; e. changing the water level to a level just below the next area of the components of the heat exchanger to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each area of the components of the heat exchanger to be cleaned until all of said areas have been cleaned.

Claim 17

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling the entire heat exchanger with a liquid; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; and d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned.

Claim 18

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one air-gun type pressure pulse shock wave source and placing the at least one air-gun type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling the entire heat exchanger with a liquid; c. activating said at least one air-gun type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one air-gun type pressure pulse shock wave source; and d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned.

Claim 19

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube suppoort plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the exposed surfaces of the tube support plate and the flow holes within the tube support plate so that the tube support plate and flow holes are clean; e. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 20

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube suppoort plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the exposed surfaces of the tube support plate and the flow holes within the tube support plate so that the tube support plate and flow holes are clean; e. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 21

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the tube support plate just below the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 22

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the tube support plate just below the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 23

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level between the upper and lower surface of the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level within the thickness of the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 24

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level between the upper and lower surface of the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes within the the level of the liquid so that the tube support plate and flow holes are clean; e. changing the water level to a level within the thickness of the next tube support plate to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 25

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said head exchanger; b. filling said heat exchanger with a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. varying the level of liquid from just above to just below the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 26

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said head exchanger; b. filling said heat exchanger with a liquid to a level just above the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. varying the level of liquid from just above to just below the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just above the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 27

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. varying the level of liquid from just below the just above the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 28

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. varying the level of liquid from just below the just above the tube support plate and flow holes to be cleaned and then back and forth in this manner at a speed of between 0.001 and 10 inches per minute while the shock waves are being generated; e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of the tube support plate and the flow holes located adjacent the surface of the liquid so that the tube support plate and flow holes are clean; f. changing the water level to a level just below the next tube support plate to be cleaned and continuing the generation of shock waves and variation of the level of the liquid relative to the support plate until the next support plate and flow holes therein are cleaned; and g. continuing in this fashion at the level of each successive tube support plate and flow holes to be cleaned until all of said tube support plates and flow holes have been cleaned.

Claim 29

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level below the lowermost tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. filling the heat exchanger with additional liquid at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is above the uppermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between appoximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 30

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level below the lowermost tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. filling the heat exchanger with additional liquid at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is above the uppermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between appoximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 31

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level above the uppermost tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. removing liquid from the heat exchanger at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is below the lowermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 32

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, the process of removing the deposits from the tube support plates and the flow holes while the heat exchanger tubes and support plates remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level above the uppermost tube support plate to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. removing liquid from the heat exchanger at a rate between approximately 0.001 and 10 inches per minute while the shock wave sources are being generated until the level of liquid is below the lowermost tube support plate to be cleaned; and e. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from the surfaces of all of the tube support plates and the flow holes within each tube support plate so that all of the tube support plates and flow holes are clean.

Claim 33

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the area of the components of the heat exchanger to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned; e. changing the water level to a level just below the next area of the components of the heat exchanger to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each area of the components of the heat exchanger to be cleaned until all of said areas have been cleaned.

Claim 34

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplicity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling said heat exchanger with a liquid to a level just below the area of the components of the heat exchanger to be cleaned; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which reach an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned; e. changing the water level to a level just below the next area of the components of the heat exchanger to be cleaned and continuing the generation of shock waves until the next support plate and flow holes therein are cleaned; and f. continuing in this fashion at the level of each area of the components of the heat exchanger to be cleaned until all of said areas have been cleaned.

Claim 35

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplcity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling the entire heat exchanger with a liquid; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; and d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned.

Claim 36

In the art of removing corrosive deposits from locations within a heat exchanger in which the heat exchanger is characterized by an enclosed tank containing a plurality of heat exchanger tubes which are closely packed together and a plurality of support plates arranged transverse to and sequentially spaced along the longitudinal axis of the heat exchanger tubes and forming junctions therewith, where the support plates contain a multiplicity of transverse holes extending through their entire thickness and where crevices exist between the outer surface of the heat exchanger tubes and the support plates at the site of the junctions and wherein these crevices and the holes in the support plates act as flow holes to permit liquid which is placed in the enclosed tank to rise to a multiplcity of levels within the tank, the heat exchanger also containing an outer shell and a tube support sheet at the lower extremity of the tank to provide a base support for the multiplicity of heat exchanger tubes, the outer shell containing a multiplicity of openings known as hand holes adjacent the tube support sheet and another multiplicity of openings known as manways and additional hand holes located at various locations on the shell through which objects may be inserted into the heat exchanger, and further containing a metal wrapper inside the tank which envelopes the plurality of heat exchanger tubes and support plates and which is set above the tube support sheet to thereby provide a space between the metal wrapper and tube support sheet, wherein the region defined between the outer shell and all of the outer surfaces of all of the heat exchanger tubes is known as the secondary side, and wherein products of corrosion, oxidation and sedimentation tend to build up and form deposits on said tube support plates and further within the flow holes to thereby occlude one or more flow holes, on heat exchanger tubes, on the metal wrapper, on the internal wall of the external shell, and on other heat exchanger components, the process of removing the deposits from all of the heat exchanger components while the heat exchanger tubes, tube support plates and all other components remain in their operative position inside the heat exchanger, comprising the steps of: a. selecting at least one pressurized gas-type pressure pulse shock wave source and placing the at least one pressurized gas-type pressure pulse shock wave source into the secondary side of said heat exchanger; b. filling the entire heat exchanger with a liquid; c. activating said at least one pressurized gas-type pressure pulse shock wave source to generate a series of repetitive shock waves which are generated with a source pressure between approximately 100 pounds per square inch and 5000 pounds per square inch which result in an energy pulse in the frequency range between approximately 1 Hertz and 1000 Hertz for each pulse to create a pulse amplitude between approximately 1 and 200 pounds per square inch at a distance of approximately one foot from the at least one pressurized gas-type pressure pulse shock wave source; and d. continuously generating said shock waves for a period between approximately one hour to approximately twenty-four hours until the deposits have been loosened and removed from said area of the components of the heat exchanger to be cleaned.

Claim 37

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 comprising the further step of circulating a liquid through the heat exchanger to flush and vacuum deposits from the heat exchanger and filtering the liquid to remove the deposits before the liquid is returned to the heat exchanger.

Claim 38

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 wherein cleaning chemicals are added to the liquid to increase cleaning effectiveness.

Claim 39

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 wherein said liquid is water.

Claim 40

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 wherein the type of heat exchanger being cleaned is a U-bend type heat exchanger.

Claim 41

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 wherein the type of heat exchanger being cleaned is a once through type heat exchanger.

Claim 42

The invention as defined in claims 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, or 18 wherein said heat exchanger is a nuclear reactor core barrel.