FIELD OF INVENTIONThis invention relates generally to systems and methods for analyzing the reliability and need for replacement of components, and more specifically, to a forecasting tool for a utility network, such as a pipeline network.[0001]
BACKGROUND OF THE INVENTIONAs used herein, a pipe includes a cylindrical structure or tube that fluids, such as water, oil, or gas, can flow through. Further, also as used herein, a pipeline typically may include a plurality of discrete sections of pipe arranged in series so that the fluid may flow through the pipeline, through each section in turn, for instance, from one end of the pipeline to the other. In addition, as used herein, a pipe system may include a plurality of sections of pipe arranged as needed or desired to perform the intended function of the system. As used herein, a section of, for example, bell and spigot pipe, may be the length from one bell to the next, or may be a greater or lesser predetermined length of pipe.[0002]
Pipes may be comprised of, for example, concrete, ductile iron, and/or steel, which may deteriorate due to corrosion, leaching, cracking, and other processes. For example, pipes in industrial cooling water processes and municipal water systems installed over the past 20 to 50 years are aging and the degradation of these pipes may be related to inadequate design, manufacturing defects, improper installation, or simply the pipes approaching the end of their useful life. Such degradation may lead to pipeline or system failures, which may result in costly unplanned outages or down times.[0003]
In the past, management techniques for pipelines were typically minimal. In general, pipelines were typically not maintenanced regarding their structural integrity until a failure occurred, at which time either the failed section, or the entire pipeline, would be replaced. Pipelines may have been inspected at planned outages, at which time obvious problems were typically repaired. However, systematic methods of managing pipe, pipelines, or pipe systems were typically not used to anticipate failures and attempt to conduct preventative maintenance or replace the pipe before failure occurs. However, the previous approach of fixing the pipe when it breaks may not be acceptable such as in cases in which a burst pipe may result in damage to property or injury to people, or where loss of the process fluid would have deleterious environmental consequences. Thus, although methods for inspecting pipe for deterioration exist in the art, a pipeline reliability management system and method is needed for such pipelines to increase their reliability and availability for use, and to effectively manage and minimize maintenance, repair, and replacement costs over the long term.[0004]
As discussed above, a variety of types of pipe typically exist in the municipal, industrial, and commercial industries, including a concrete pipe which may be precast (e.g., centrifugally cast) such as in bell and spigot construction, or may be cast in place. The pipe is often reinforced with embedded reinforcement steel or rebar, which is typically not significantly stressed when the pipe is not pressurized, or may obtain its structural strength (i.e., ability to withstand internal pressure, from prestressed or post tensioned wires or tendons). Such wires or tendons may be circumfrentially installed or helically wound around the pipe, and may be covered with mortar or another coating or material to protect the wire or tendon from corrosion or other environmental degradation. As examples, pipe may comply with American Water Works Association (AWWA) standard 303 or 304.[0005]
For instance, referring to FIG. 1, the pipe may be prestressed concrete cylinder pipe (e.g., PCCP)[0006]100, which may consist of acylindrical concrete core105 helically wound withsteel wire111, and coated withmortar114. Thesteel wire111 may be highly stressed in tension when wound around theouter surface112 of thecore105. For design and pipeline reliability management purposes, theprestressed wire111 is typically considered to withhold the entire pressure (e.g., hydrostatic pressure) of the contents of the pipe or fluid (e.g., water106). In other words, thewire111 holds the hoop stress ofpipe100. Due to the high prestressed tension in thewire111, the concrete of thecore105 typically remains in compression, thereby minimizing the early development of cracking in the concrete (of core105) since cracks are more likely to develop when concrete is loaded in tension.
The[0007]mortar114 generally protects thesteel wire111 from corrosion by excluding moisture, and/or oxygen, or by maintaining a high pH. However, since thewire111 may be so highly stressed, if thewire111 slightly deteriorates, thewire111 may break. Experience in the industry has revealed thatsuch wire111 breaks occur with PCCP, due to, for example, damage to themortar114 during installation of thepipe100,defective wire111, hydrogen embrittlement ofwire111, inadequate cleanliness of theouter surface112 ofconcrete core105 when thewire111 is installed, corrosion ofwire111, and other causes, which sometimes cannot be accurately identified. When a wire break occurs, thewire111 may slightly slip near the break, but friction between thewire111 andouter surface112 ofconcrete core105, typically prevents thewire111 from loosening over the entire section ofpipe100. Moreover, even if a certain number of wires were found to be broken, the compression from the adjacent non-broken wires was found to extend over the area of the broken wires. In most applications, one or even several wire breaks may occur without failure of the pipeline; however, ifenough wires111 break, the pipeline may fail.
In the past, despite the presence of the[0008]can107, for PCCP design and pipeline reliability management purposes, theprestressed wire111 was typically considered to withhold the entire pressure (e.g., hydrostatic pressure and surge) of the contents of the pipe (e.g., water106). In other words, can107 was not considered to take any circumferential load or hoop stress. As described above, due to the high tension in thewire111, the concrete of thecore105 typically was assumed to remain in compression. However, this model often resulted in overly conservative and expensive pipe management practices, which resulted in, for example, the replacing of pipe that could have remained in service for some time.
Various methods have been developed to inspect the various types of pipe in service throughout the world. For instance, the degree of physical degradation or deterioration of the pipeline may be determined by inspection. However, effective and economical inspection may require considerable ingenuity, since the load-bearing component, (e.g., prestressing wire[0009]107) may be located underneath other layers, and the pipeline (e.g., pipe100) may be buried under the ground. Still, PCCP, as an example, may be inspected in several ways. These ways include, as examples, eddy current inspection, ultrasonic inspection, visual inspection, sounding, and acoustic monitoring.
Eddy current inspection, such as remote field eddy current/transformer coupling (RFEC/TC) testing, provides estimations of broken[0010]prestressed wires111 in PCCP (e.g., pipe100) and identifies sections of PCCP with no degradedprestressing wires111. For PCCP with distress, RFEC/TC provides an estimated number of wire breaks and the location of the breaks along the axial length of PCCP.
Ultrasonics or Ultrasonic Testing (UT) is another method of inspection, which has applications beyond PCCP. In fact, UT thickness and defect examination of metallic piping has been used since at least the late 1960s for construction and monitoring of piping systems. For instance, UT is used as a volumetric examination for certain critical welds at nuclear power plants. Power plants (fossil and nuclear) also use UT for erosion/corrosion inspection of high energy process piping lines.[0011]
Visual inspection is another option, when access permits, to determine the level of pipeline degradation. Referring once again to FIG. 1, the[0012]inside102 and/or outside122 ofpipe100 may be visually inspected, and visual inspection may be either direct or remote (e.g., via a camera inserted withinpipe100 to view inside surface102). Corrosion, spawling, cracking and deflection provide visual indications that piping is in distress.
Sounding is another method of inspecting pipe, which involves tapping on the pipe and listening for the resulting sound. In the recent past, engineers attempted to analyze a pipe for areas of delamination by simplistic manual methods, such as by walking through a pipe and tapping on the inside of the pipe in an effort to hear tone changes which were often indicative of hollow areas within the pipe wall. The engineers often determined that the hollow areas in the pipe wall were areas of concrete failure. When access permits, such sound (impact echo) can be used to determine the level of degradation in pipes.[0013]
Sounding may be performed manually (e.g., with a hammer and the human ear) or may also be performed with sophisticated equipment that may provide a consistent impact, record the resulting sound, and display or analyze the frequency response of the sound, rate of attenuation, or other characteristics. However, in order for UT, visual inspection, or sounding to be effective, it may be necessary to uncover the pipe. Even if access to the[0014]inside102 of the pipe is possible, theprestressing wires111 are typically located far from the inside surface of the pipe, and distress may not show up on surface concrete until failure is imminent. As can be appreciated, uncovering buried pipelines for periodic inspection of the outside122 may also be cost prohibitive.
Another method of inspection is acoustic monitoring, which was invented by Douglas Buchanan of the U.S. Bureau of Reclamation in the 1990's for use on the Central Arizona Project. Acoustic monitoring involves installing listening devices on or within the pipeline, and monitoring the devices for the sounds generated by the degradation of the pipe. As an example, hydrophones may be installed in[0015]water106 carried by PCCP (pipe100), which may be monitored by one or more computers or processors, which may be programmed to recognize the sound made by breakingprestressing wires111. The location of the breaks along thepipe100 may be determined by comparing the arrival times of the sound at hydrophones on either side of the break. Hydrophones may be installed through taps in the pipe wall (e.g., through core105) or in a string located withinpipe100.
SUMMARY OF THE INVENTIONThe present invention provides, inter alia, a system and method for facilitating the forecasting of pipeline and pipe system reliability to effectively manage maintenance, repair, and replacement costs over the long term. The system and method may be employed in the design, installation, testing, and operational phases of new pipelines, for instance, to maximize service life.[0016]
In specific embodiments, the present invention provides a method of facilitating the determination of whether to take pipe management action such as repairing or replacing pipe. The method generally includes (in any order) the steps of: acquiring a first parameter (e.g., a design parameter for the pipe, such as the diameter); inspecting the pipe a first time; acquiring a second parameter (e.g., an evaluation of the structural integrity of the pipe); and acquiring a third parameter (e.g., a pressure within the pipe, which may be the maximum pressure anticipated in future service). The method generally also includes the step of: using at least a relation (e.g., a graph) of the evaluation of the structural integrity of the pipe and the pressure within the pipe, facilitating a determination of whether or not to take pipe management action. When the pipe management action should be taken may also be determined.[0017]
The method may also include the steps of: waiting until the next time to inspect; inspecting the pipe a second time; and acquiring a fourth parameter (e.g., another evaluation of the structural integrity of the pipe taken at a later time). The degradation rate of the pipe may be calculated, (e.g., from the difference in the structural integrity of the pipe from the first time the pipe was inspected to the second time it was inspected). In the alternative, the degradation rate may be assumed, (e.g., from prior experience). Whether assumed or calculated for the particular pipe or section of pipe, the degradation rate may be used, for instance, to calculate when the pipe should be, for example, repaired or replaced.[0018]
In an exemplary embodiment, the pipe may be prestressed concrete cylinder pipe, and the second parameter may include a quantity of broken wires. The inspecting may utilize, as examples, eddy current inspection, ultrasonic inspection, visual inspection, or sounding (or a combination thereof). The pipe management action may involve, as examples, repairing, replacing, or monitoring the pipe.[0019]
The relation or graph may be either physically-viewable or embedded within a computer or computer program (e.g., in a computer implemented method), and may have a plurality of zones of risk (e.g., high and low risk). As an example, in the case of PCCP, the graph or relation may include the anticipated maximum pressure within the pipe versus the number of failed prestressing wires discovered during inspection. The method may further be tested over time to verify that it works.[0020]
In another embodiment, the present invention further provides a system for facilitating a determination of whether to take pipe management action. The system generally includes a relation of pressure versus a quantification of the degradation of the structural integrity of the pipe. Similar to as described above for the method, the relation may be either a physically-viewable graph or embedded within a computer, such as an algorithm, data, or a combination thereof. The relation may have a zone of higher risk and a zone of lower risk, and may also have a zone of medium risk.[0021]
The pipe for which the system is used may have a concrete core, and may be prestressed concrete cylinder pipe. Thus, the quantification of the degradation of the structural integrity of the pipe may include a quantity of broken wires. The quantity of broken wires may be, for example, an actual number of contiguous broken wires, a length of pipe wherein all wires are broken, or an equivalent length of pipe where in actuality not all contiguous wires are broken. Further, the pressure that is used may be maximum anticipated pressure (e.g., within the pipe). The relation (e.g., a graph) may further include the anticipated pressure for the ultimate strength of the cylinder, the anticipated rupture pressure of the pipe, or even the pressure anticipated to cause the concrete core to crack. The relation may even further include an action pressure, which may be less than the anticipated rupture pressure of the pipe, but greater than the pressure anticipated to cause the concrete core to crack.[0022]
The present invention even further provides a method of facilitating the management of a pipeline. In this embodiment, the pipeline may include a plurality of sections of prestressed concrete cylinder pipe. The method may include in any order the steps of storing design data (e.g., one or more dimensions, external loading, etc.) for each of the sections, inspecting a plurality of the sections (e.g., evaluating the quantity of failed wires within the sections), and estimating the maximum pressure that is likely to exist within the sections in future service. The method may also include using the design data, the quantity of failed wires, and the maximum pressure to designate a classification for the condition of the sections of pipe, and implementing pipe management action based on these classifications.[0023]
The inspecting may be repeated at different times, and changes in the quantity of failed wires may be tracked over time. In addition, there may be two, three, or more classifications, and each classification may have a corresponding action. Furthermore, the method may include the steps of calculating the rate of wire failures for the sections, and predicting when the sections will enter another classification.[0024]
The pipe management action that is taken (e.g., corresponding to a classification) may be, for instance, doing nothing to the section (at least until the next inspection), monitoring the section, repairing the section, or replacing one or more sections. In some embodiments, sections may be repaired individually until the pipeline deteriorates to the point that it is advantageous to replace the entire pipeline.[0025]
The method further may include the step of analyzing one of the sections for lack of prestress pressure over the section's entire circumference, but over a limited length of the section. The sections may also be analyzed for lack of prestress pressure over just a portion of the section's circumference, and over a limited length of the section. The sections may even further be analyzed for lack of prestress pressure over a first limited length of the section, and over a second limited length of the section, where there is a segment of pipe with intact prestressed wire located between the first limited length and the second limited length. The segment may be, for example, more than 3-inches long, but less than 25-inches long, and an effective length of failed wires may be used, which may be calculated as a function of the two limited lengths of failed wires and the length of the segment in between.[0026]
The method further may include the steps of analyzing the rupture pressure of the sections, and designating a classification based on whether the maximum pressure exceeds the rupture pressure. Whether the maximum pressure exceeds the rupture pressure of the section by more than a predetermined non-zero amount, may also be determined. In addition, crack onset pressure may be analyzed, and whether the maximum pressure exceeds the crack onset pressure may be determined. Even further, an action pressure may be determined, which may be less than the rupture pressure of the section, but may be greater than the crack onset pressure. Thus, the step of designating a classification may include determining whether the maximum pressure is greater than or less than the action pressure of the section. The designating a classification may also include determining whether the maximum pressure is less than the rupture pressure of the cylinder or can.[0027]
The present invention still further provides a computer implemented system for facilitating a determination of whether to take pipe management action. The system generally uses a processor that is configured to acquire or input one or more design parameters (e.g. the diameter of the pipe), input one or more inspection parameters (e.g. information indicating the degradation of the structural integrity of the pipe, such as a quantity of broken wires in PCCP, that may be determined via eddy current inspection), and input the pressure within the pipe (e.g. the maximum pressure anticipated in future service). The system generally uses at least a relation of these parameters (e.g. the number of broken wires v. pressure) to output information to facilitate determining whether or not to take pipe management action (e.g. to recommend whether or not to repair, replace, or monitor the pipe). In some embodiments, information indicating the degradation of the structural integrity of the pipe may also be determined again at a later time, and the change in the structural integrity may be used to calculate the degradation rate of the pipe. Further, when to take pipe management action may also be output, (e.g. using the degradation rate of the pipe).[0028]
BRIEF DESCRIPTION OF THE DRAWINGSThe present invention is illustrated by way of example and not limitation in the accompanying figures, in which like reference numbers indicate similar elements, and in which:[0029]
FIG. 1 is an orthographic projection of a section view of prestressed concrete cylinder pipe, showing typical layers in the wall of such pipe;[0030]
FIG. 2 is a block diagram illustrating a system in accordance with the present invention;[0031]
FIG. 3 is a flow chart illustrating the steps of one exemplary embodiment of a method in accordance with the present invention;[0032]
FIG. 4 is a graph of pressure versus number of wires broken, illustrating various aspects of an exemplary embodiment of the present invention;[0033]
FIG. 5 is another flow chart illustrating the steps of another exemplary embodiment of a method in accordance with the present invention; and[0034]
FIG. 6 is another flow chart illustrating the steps of a further exemplary embodiment of a method in accordance with the present invention.[0035]
DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTSThe present invention includes systems and methods for analyzing the reliability and replacement of components, and more specifically, to a forecasting and reliability management tool for a utility network, such as a pipeline network or pipe system. As such, while the system and methods shall be described in relation to a pipeline or pipe system, one skilled in the art will appreciate that much of the functionality is applicable to other components, utilities, networks and/or the like. For example, at least certain aspects of the present system and method may be applied to any portion of roads, canals, sewer systems, power lines, railroad tracks, buildings, circuits, fences, walls or any other system with components that may fail or degrade. The present invention may also be applicable to heat exchanger tube inspections and monitoring pipelines for erosion or corrosion.[0036]
In this regard, the present invention may be described herein in terms of functional block components and various processing steps. It should be appreciated that such functional blocks may be realized by any number of hardware, firmware, and/or software components configured to perform the specified functions. For example, the present invention may employ various integrated circuit components, such as memory elements, digital signal processing elements, look-up tables, databases, and the like, which may carry out a variety of functions under the control of one or more microprocessors or other control devices. Such general techniques and components that are known to those skilled in the art are not described in detail herein.[0037]
It should further be understood that the exemplary process illustrated may include more or less steps or may be performed in the context of a larger processing scheme. Furthermore, the various flowcharts presented in the drawing figures are not to be construed as limiting the order in which the individual process steps may be performed.[0038]
As a general overview, the present invention provides a system and method for managing or facilitating the management of pipe, pipeline, or pipe system reliability, for example, to increase the reliability of a pipeline and availability for use, and to effectively manage actions that may be taken such as maintenance, repair, and replacement, and their costs (e.g., over a longer term). Embodiments include a system and method that may be employed in the design, installation, testing, and operational phases of new or existing pipelines or pipe systems, for instance, to maximize service life or minimize life cycle costs. Many embodiments are computer-implemented, and comprise, inter alia, a method of forecasting, managing or determining whether or when to take pipe management action such as to repair or replace prestressed concrete cylinder pipe (e.g., PCCP). Various embodiments include steps such as inspecting the pipe and storing or inputting various parameters, such as design parameters, inspection parameters, and environmental parameters. Inspection may involve, for instance, eddy current inspection, ultrasonic inspection, visual inspection, sounding, or some combination of these. Embodiments may also include acquiring or inputting the maximum pressure (e.g., expected within the pipe) and determining whether or not to repair or replace the pipe, and in some embodiments, whether or not to monitor the pipe.[0039]
In general, various embodiments may use a relation or graph of pressure versus a quantification of the structural integrity or degradation of the structural integrity of the pipe, wherein the degradation of the structural integrity of the pipe may include, for instance, the number of broken prestressing wires in PCCP or the degree of wall thinning in other pipes. As would be apparent to a person skilled in the art, the structural integrity of the pipe and the degradation of the structural integrity of the pipe are usually related. For instance, the structural integrity of the pipe may be the number of wires that are intact, while the degradation in the structural integrity may be the number of wires that are broken. Thus, as the terms are used herein, a relation or graph that involves the structural integrity of the pipe also generally includes the degradation of the structural integrity of the pipe, and vice versa.[0040]
The relation or graph may have zones of high, medium, and low risk and may show the pressure for the ultimate strength of the cylinder (in the case of PCCP). The method may also include designating a zone of risk or classification for the condition of the pipe, and implementing pipe management action based on the classification. The pipe may be analyzed for lack of prestress pressure over various portions of the pipe's circumference and length. The method may also include analyzing the rupture pressure of the pipe, the crack onset pressure, or the rupture pressure of the cylinder (of PCCP) alone, each of which may be compared to the maximum pressure anticipated within the pipe. The method may further include the steps of testing the method over time to verify that it works or repeating the inspection at different times, and tracking changes in the quantity of failed wires. The action may involve doing nothing (at least until the next inspection), monitoring the pipe, repairing the pipe, or replacing the pipe.[0041]
More particularly, embodiments of the present invention may provide a system and method of facilitating the determination of whether to take pipe management action such as repairing or replacing pipe. The system or method may be used for pipeline or pipe system reliability management, which may include manual mapping, automation and/or analysis facilitated through a computer or processor.[0042]
With respect to system components, FIG. 2 is a block diagram illustrating an exemplary system in accordance with the present invention. More particularly, FIG. 2 illustrates in an exemplary embodiment, a computer implemented[0043]system200 for facilitating a determination of whether to take pipe management action, for instance, determining the next action for the management of a pipeline. Thesystem200 generally uses a computer orprocessor230 that is configured to receive or input various parameters (e.g.first parameter201,second parameter202, etc.). Seven inputs or parameters are shown (first parameter201 through seventh parameter207); however, fewer or more parameters could be used as would be apparent to a person of ordinary skill in the art. Parameters201-207 may include one or more design parameters (e.g. the diameter of pipe100), one or more inspection parameters (e.g. information indicating the degradation of the structural integrity of the pipe, such as a quantity of broken wires in PCCP, that may be determined, for instance, via eddy current inspection), and the pressure within pipe100 (e.g. the maximum pressure anticipated in future service).Processor230 is generally configured to receive these inputs, which are described in more detail below.
In the exemplary embodiment shown,[0044]processor230 is configured to analyze the input parameters (e.g., some or all of parameters201-207) and output recommendedaction260, which may include a mapping function and/or a recommended action ranging from, for instance, doing nothing to repairing or replacing pipe100 (e.g., pipe management action as described herein). To determine the recommendedaction260,processor230 may use a relation of at least some of parameters201-207 (e.g. the degradation of the structural integrity ofpipe100 or the number ofbroken wires111 v. pressure). This relation (described in more detail with reference to FIG. 4 below) may be used to determine and output viarecommended action260, information configured to facilitate determining whether or not to take pipe management action, or which pipe management action to take.
Still referring to FIG. 2, in some embodiments of the present invention, information indicating the degradation of the structural integrity of[0045]pipe100 may be determined again at a later time, andprocessor230 may be configured to use the change in the structural integrity to calculate the degradation rate ofpipe100. Further,processor230 may be configured so thatrecommended action260 includes when to take pipe management action, which may be calculated (e.g. by processor230), as an example, using the degradation rate ofpipe100. Output (e.g. recommended action260) may be tabular or graphic, andprocessor230 may be programmed to provide numerical data or graphic information. In addition, as would be apparent to a person of skill in the art, althoughsystem200 shows aprocessor230, some or all of the functions or analysis performed byprocessor230 could also be performed manually.
systems (such as[0046]system200 illustrated in FIG. 2) utilizing a computer, the system may include a host server or other computing systems, including, as examples: a processor for processing digital data; a memory coupled to the processor for storing digital data; an input digitizer coupled to the processor for inputting digital data; an application program stored in the memory and accessible by the processor for directing processing of digital data by the processor; a display coupled to the processor and memory for displaying information derived from digital data processed by the processor; and a plurality of databases, which may include input data, historical data, specification data and/or like data that could be used in association with the present invention. As those skilled in the art will appreciate, user computer will typically include an operating system (e.g., Windows NT, 95/98/2000, Linux, Solaris, etc.) as well as various conventional support software and drivers typically associated with computers.
Similarly, the software elements of the present invention may be implemented with a spreadsheet or computer program such as Excel or Dbase. In addition, a programming or scripting language may be used such as C, C++, Java, COBOL, assembler, PERL, extensible markup language (XML), with the various algorithms being implemented with any combination of data structures, objects, processes, routines or other programming elements. Further, it should be noted that the present invention may employ any number of conventional techniques for data transmission, signaling, data processing, network control, and the like. Still further, the invention could be used to detect or prevent security issues with a client-side scripting language, such as JavaScript, VBScript or the like. The users may interact with the system via any input device such as a keyboard, mouse, kiosk, personal digital assistant, handheld computer (e.g., Palm Pilot®), cellular phone and/or the like. Similarly, the invention could be used in conjunction with any type of personal computer, network computer, workstation, minicomputer, mainframe, or the like running any operating system such as any version of Windows, Windows NT, Windows2000, Windows 98, Windows 95, MacOS, OS/2, BeOS, Linux, UNIX, Solaris, ArcSoft (GIS) or the like.[0047]
The database may be any type of database, such as relational, hierarchical, object-oriented, and/or the like. Common database products that may be used to implement the databases include DB[0048]2 by IBM (White Plains, N.Y.), any of the database products available from Oracle Corporation (Redwood Shores, Calif.), Microsoft Access by Microsoft Corporation (Redmond, Wash.), or any other database product. The database may be organized in any suitable manner, including as data tables or lookup tables. Association of certain data may be accomplished through any data association technique known and practiced in the art. For example, the association may be accomplished either manually or automatically. Automatic association techniques may include, for example, a database search, a database merge, GREP, AGREP, SQL, and/or the like. The association step may be accomplished by a database merge function, for example, using a “key field” in each of the manufacturer and retailer data tables. A key field partitions the database according to the high-level class of objects defined by the key field. For example, a certain class may be designated as a key field in both the first data table and the second data table, and the two data tables may then be merged on the basis of the class data in the key field. In this embodiment, the data corresponding to the key field in each of the merged data tables is preferably the same. However, data tables having similar, though not identical, data in the key fields may also be merged by using AGREP, for example.
Turning now to exemplary methods, FIGS. 3, 5, and[0049]6 are flow charts illustrating various steps of various embodiments of the present invention. Embodiments of methods in accordance with the present invention may contain, inter alia, steps from one or more of these drawing figures. In general, FIG. 3, illustrates input steps, pipe management action, and the decisions regarding which pipe management action to take. In comparison, FIG. 5 illustrates input steps, calculations, and the decisions made based on those calculations. In further comparison, FIG. 6 illustrates input steps, analyses, and various other intermediate steps such as tracking changes.
Specifically, FIG. 3 illustrates an exemplary embodiment of a method in accordance with the present invention, which depicts, inter alia, a method of pipeline reliability management, for example, a method of determining or facilitating the determination of whether or when to take pipe management action such as repairing or replacing pipe. The pipe may be, for example, PCCP, although the present system and[0050]method300 would generally work for other types of pipe, conduit, and ductwork, as well, which may be made of, as examples, concrete, welded steel, screwed steel, riveted steel, ductile iron, cast iron, plastic, copper, stainless steel, or aluminum bronze.Method300 may include steps that are computer-implemented, (e.g., viaprocessor230 illustrated in FIG. 2) although some steps (e.g., replacing the pipe (step324)) generally must be performed manually or by mechanical means and/or other means. Such external steps may not be part of embodiments of the present invention involving only the computer system. In addition, a computer simulation of pipeline systems and replacement of pipes may be part of the system and method.
[0051]Method300 generally includes the steps of acquiring or inputting design parameters (step305), inspecting the pipe (step302), and acquiring or inputting inspection parameters (step308). Although shown and described in the plural, in some embodiments only one design parameter or inspection parameter may be acquired or input. In other embodiments, multiple design parameters and inspection parameters may be acquired or input. Design parameters (e.g., as input in step305) may include dimensions of the pipe, such as diameter, configuration, hydraulic performance, design loading, degraded pipe performance and/or the like. Other input data may include the diameter, thickness, and material strength ofcan107, the diameter, thickness, and material strength ofcore105, the wire size (e.g., diameter), spacing, tensile strength, and prestress tension ofwire111, the maximum operating pressure and anticipated transient pressure, the process fluid temperature and chemistry, and the pipe dead load (e.g., soil cover) and live load (e.g., road or railroad loading), and information related to the degradation rate of particular systems.
The inspection parameters (input in step[0052]308) may include an evaluation of the structural integrity of the pipe, which, in the case of PCCP, may be the length or quantity of continuous or adjacent wire (e.g.,wire111 shown in FIG. 1) breaks within the section of pipe being analyzed. As used herein, a quantity of failed or broken wires may mean the actual number of wires broken or another value that is convertible to the actual number of wires broken, such as the length of pipe having adjacent broken wires. Further, a quantity of broken wires may include an effective value (e.g. an effective length as described in more detail below) where not all wires in a continuous portion of pipe have failed or are broken.
The inspection from which the inspection parameters (of step[0053]308) are derived may involve eddy current inspection, ultrasonic inspection, visual inspection, sounding, acoustic monitoring, or other methods, which may be known in the art. FIG. 3 also shows the step of acquiring or inputtinginternal pressure311, which may be either a design parameter or an inspection parameter depending on various factors including whether the design pressure is still the best information available. The maximum future pressure within the pipe may be estimated considering design data, field conditions, and planned use. However, the internal pressure (of step311) could be based only on design data or historical measured pressure, for instance, the maximum pressure measured to date in service similar to that anticipated. The steps of acquiring or inputting design parameters (step305), and acquiring or inputting inspection parameters (step308) may include acquiring or inputting one or more environmental parameters or conditions specific to the site. These may include the amount of moisture or pH of the soil, etc.
Program inputs or parameters (e.g.,[0054]201-207 in FIG. 2) may originate from a piping design review (e.g., forstep305 in FIG. 3) and inspection (e.g.,step302 in FIG. 3), and the system (e.g.,200) or method (e.g.,300) may result in various outputs (e.g., recommended action260). The piping design review (e.g., forstep305 in FIG. 3) may involve gathering various design data, which may already exist within drawings, specifications, and other documentation typically kept for pipelines. An understanding of the design, installation and construction of the pipeline may be helpful as a baseline for a pipeline reliability management determination. A typical review may consider the pipeline and control systems (including cathodic protection, if any), interconnected/adjacent systems, the fluid or gases conveyed by the pipeline, and the pipelines environmental conditions. One area that may be reviewed is the configuration of the pipeline. The original design, manufacture and installation drawings/specifications and field observations may be used to establish the materials of construction, diameter, and unit length for each spool or section of the pipeline. Where applicable, this data may be entered into the computer or processor (e.g.,230 in FIG. 2) and may be verified. Another area that may be reviewed is the hydraulic performance of the pipeline. The hydraulic performance characteristics (i.e., operating pressures, temperatures as a result normal/abnormal design conditions) of the pipeline may be reviewed, verified, and where applicable, entered into the computer (e.g.,processor230 in FIG. 2) for each corresponding pipe spool (i.e., section of pipe or unit length).
A further area that may be reviewed (e.g., for[0055]step305 in FIG. 3) is design loading. Live and dead loads on the pipeline may be documented, which may include soil cover, roads and railroads, seismic conditions (e.g., earthquake loads), etc. An even further area that may be reviewed is the performance of pipe that has undergone degradation. A design review/study may be performed to determine how the piping system will perform under design loading with varying degrees of degradation. Specifically, an understanding of the failure progression for the pipe may be needed. As an example, prestressed concrete cylinder pipe (PCCP) may be analyzed to determine the amount of loss of prestressing wires (e.g.,111 in FIG. 1), concrete core (105) cracking, or loss of steel cylinder (can107) thickness that can be withstood for a given system design and pressure. Similar engineering reviews for ductile iron or steel pipe may model wall thickness reductions in terms of area, minimum wall thicknesses, and corrosion allowances. Results of such a review may be expressed in numerical terms (e.g. number ofbroken wires111, minimum wall thickness, minimum design, corrosion allowance per year, etc.) which in computer implemented embodiments may be entered into the computer (e.g.,processor230 in FIG. 2) for each spool or section.
The second type of data or program inputs to the system and method of pipeline reliability management are the result of inspection (e.g., inspection parameters of[0056]step308 shown in FIG. 3). Various methods have been developed to inspect (e.g., step302) the various types of pipe to evaluate the integrity or extent of physical degradation of the pipeline. Some of these methods are described above, including, as examples, eddy current, ultrasonic, visual inspection, sounding, and acoustic monitoring. The application to different pipelines may be selected based on access, materials of construction, and cost. In embodiments where a computer or processor (e.g.,processor230 in FIG. 2) is used, results of the above inspections may be input into the computer or processor. As an example, in addition to applications of the above inspection techniques with PCCP, UT could also be used for reliability evaluation of metallic piping systems. In the exemplary embodiment of use with PCCP, wire break numbers and locations may be entered into the computer or processor (e.g., processor230) for each spool or section of pipe. RFEC techniques may also be used to measure wall thinning in metallic pipe, such as 12-inch ductile iron fire protection piping. These values/degradation parameters could also be input to the computer or processor (e.g., processor230) for reliability evaluation of ductile iron piping systems.
Still referring to FIG. 3, in the exemplary embodiment illustrated, after the data input steps (input parameters of[0057]steps305,308, and311), the data may be analyzed (as described below) (e.g., byprocessor230 shown in FIG. 2), and the output may include one or more recommended options regarding corrective action, or action to manage the pipe or pipeline. The output may include, for example, whether to replace (step314), repair (step317), or monitor (step319) the pipe. The output may involve, for instance, each section or spool of pipe (e.g., each bell and spigot section), or larger sections of pipe, up to the entire pipeline. Although these three options are shown inmethod300, embodiments of the present invention may have fewer, more, or different options for pipe management action.
Taking a closer look at the pipe management actions illustrated in FIG. 3,[0058]method300 illustrates and may include the steps of replacing the pipe (step324), repairing the pipe (step327) or monitoring the pipe (step329).Method300 illustrates and may also include the steps of determining when to inspect the pipe (e.g.,100) next (steps332 and339), and either monitoring the pipe (step329) or simply waiting until it is time to inspect the pipe again (step335). Replacing the pipe (step324) may involve replacing with the same kind or a different kind of pipe (e.g., replacing PCCP with steel pipe or cast-in-place).
Determining when to inspect next (step[0059]332), may involve making a determination of how quickly the pipe is deteriorating, (e.g., a degradation rate). The degradation rate may be determined from the difference in condition of the pipe between at least two successive inspections performed at different times. For instance, methods of extrapolation may be used, which may be commonly known. The degradation rate may be used not only to determine when to inspect the pipe next, but may also be used to estimate or forecast when the pipe will need to be or should be repaired or replaced. This estimate may be used to determine when funding, manpower, or equipment will be needed, or otherwise to plan the work. In the alternative, a degradation rate may be assumed rather than determined for a particular pipe, and when the pipe will need to be or should be repaired or replaced may be determined from the assumed degradation rate and the results of one inspection.
Repairing the pipe (step[0060]327) may involve installing post tensioned tendons around theoutside surface122 ofpipe100, installing a steel liner within theinside surface102 ofpipe100, or other methods of repairing pipe, including those known in the art. Post tensioned tendons may comprise wire rope, which may be installed within a polymer sleeve to protect the wire rope from corrosion. The sleeve may further contain a corrosion inhibiting material or grease. However, a possible disadvantage of this repair method includes the need to excavate all the way around the pipe (e.g., pipe100), which may need to be done for each tendon at a time below spring-line, in order to install post tensioned tendons. Once excavated, the tendon may be wrapped once around the pipe, and then tensioned (e.g., to replace the lost prestress). The excavation may require hand excavation to avoid damaging the pipe, and may be labor intensive and expensive. However, it may be possible to do it while the pipeline is in service, and it may be considerably less expensive than replacing the entire pipeline.
In contrast, repairing pipe (step[0061]327 of FIG. 3) by installing a steel liner may involve taking the pipe out of service for an extended period of time to install the liner, and may involve extensive field welding and grouting between the liner andinterior102 ofpipe100. In addition, a liner ultimately results in a reduction of the inside diameter of the pipe, which may reduce capacity or increase the pumping energy required for a given flow. Further, a protective coating, such as coal tar epoxy or cement mortar, may need to be applied and maintained on the steel liner to protect it from corrosion.
Whether a pipe is repaired or replaced may depend on how may spools or sections of pipe are in a seriously distressed condition, the importance of the pipeline, whether funding is available now, the time value of money, and other factors. It may be less expensive to replace a pipeline than to repair the entire pipeline; however, if areas of distress can be consistently identified prior to failure, considering the time value of money, it may be less expensive to repair a portion of a pipeline each year for an extended period of time than to incur the up-front cost of replacing the entire pipeline. Monitoring the pipe (step[0062]329) may involve installing and using an acoustic monitoring system (e.g., as described above) or inspecting the pipe frequently.
The analysis of the present invention (e.g., of method[0063]300) may involve using agraph400 or relation of pressure versus a quantification of the structural integrity or the degradation of the structural integrity of the pipe, an example of which is illustrated in FIG. 4, and is described in more detail below. Althoughgraph400 is depicted in FIG. 4 as being physically viewable, as would be apparent to one skilled in the art, a relation may be used in the present invention that is, for instance, embedded within a computer program and may not be readily viewable. Thus, the zones or curves (such as shown in graph400) may be defined by equations, look-up tables, or the like. Further, as used herein, a relation may be embedded within a computer program and may not be readily viewable, or may be a physically viewable graph such asgraph400. For the sake of explanation herein, aviewable graph400 is described. However, the characteristics described forgraph400 may apply to a relation in various embodiments of the present invention.
The relation or graph (e.g.,[0064]400) may have at least zones of high risk (e.g.,1aand1b) and low risk (e.g.,4 and5). Further, the relation or graph (e.g.,400) may include additional zones of intermediate or medium risk (e.g.,2a,2b,3a, and3b). Thus, the various zones may have higher risk or lower risk, e.g. relative to each other. For instance, ongraph400, the higher the number of the zone, the lower the risk. The boundaries of these zones (e.g. the curves shown on graph400), among other factors in the analysis, may be refined over time based, for example, on failures in service and destructive or non-destructive testing (e.g., of pipe that is designated for replacement). Thus, the determinations of whether to replace (step314), repair (step317), or monitor (step319) the pipe may include the step of testing the method over time to refine the accuracy of the method.
Referring generally to FIGS.[0065]1-5, once the necessary information is obtained or input into a computer or processor (e.g.,processor230 in FIG. 2), the data may be analyzed in accordance with various aspects of the present invention. One step may be to analyze or calculate the rupture pressure of the pipe (step551). In the example of PCCP, the analysis of rupture pressure may involve considering a loss of prestress (wire111 failure) extending over a significant part of thepipe100. To do so, thecore105 may be modeled as a long cylindrical shell subjected to the effective external pressure of prestressing, and the anticipated maximum pressure (e.g., of step311) within the pipe. In the case of a liquid fluid, such aswater106, the maximum pressure within the pipe (internal pressure) may include hydrostatic pressure, but may also include local dynamic effects such as surge or potential water hammer.
Referring still to FIG. 1, other external pressures such as soil loading or groundwater pressure may also be considered where applicable and ascertainable. Pipe weight and fluid weight may also be considered. These loads may produce bending in the pipe wall, but may not have a significant effect on the[0066]can107 after cracking of thecore105. In some cases, thrust effect of external loading may be considered, although they may be small relative to internal pressure. In more sophisticated embodiments of the present invention, in addition to the foregoing effects, the effects of microcracking and cracking of theconcrete core105, and yielding and strain (work) hardening of the steel cylinder or can107 may also be considered.
To perform the analysis or decide what pipe management action to take or recommend, the loss of prestress over the pipe's entire circumference may be simulated by removing the prestressing pressure around the entire circumference over a limited length of[0067]pipe100. Using the loss of pre-stress and the maximum pressure within the pipe, the maximum circumferential stresses in the concrete core may be calculated. The maximum stress may be compared with the allowable stress for the degraded pipe (i.e., thepipe100 with broken wires111). For instance, the ultimate strength of the degraded composite structure (e.g., concrete core and steel cylinder or can107, with no wires111) may be determined. Allowable stresses may be set lower to provide a design or safety margin. In this way, risk of failure can be measured by how close actual stresses compare to allowable or ultimate stresses. Generally, all other things being equal, the closer actual stresses are to the ultimate stress, the higher the risk.
If the maximum circumferential stress in the[0068]core105 exceeds the cracking strength, then it may be assumed that the core105 cracks aroundpipe100, resulting in softening (generally a significant reduction in strength in the circumferential direction) ofcore105 around the entire circumference. However, since in this scenario can107 is still intact andwire111 is still intact nearby, theconcrete core105 can still resist the internal pressure, for example, by longitudinal strips of the core105 loaded (as beams) in bending. (The analysis of these strips is performed instep546 shown on FIG. 5 and described below.) Thus, in the case of PCCP, the steel cylinder or can107 may increase the strength of thecore105. The tensile strength of thecan107 can be considered in the circumferential direction; however, the tensile strength of thecan107 may also increase the strength of the longitudinal strips of the core105 loaded as beams in bending.
A loss of prestress may also exist over just a portion of the circumference of the[0069]pipe100. As an example, such a localized loss of prestress may be modeled as being absent within an 11.25 degree angle. In this scenario, bending moments may develop along the termination points of prestressing, which may lead to cracking. The strength of thecore105 beyond the prestress-loss zone will prevent cracking if the length of such a zone is small, as may be analyzed and revealed by a finite element analysis. In addition, the analysis of the loss of prestress may be effected by whether the loss is at the end of a section ofpipe100, or somewhere in the middle.
Embodiments of the present invention may analyze the case in which there are multiple prestress loss zones or areas near each other, with a segment of intact[0070]prestressed wire111 in between. If the segment of intactprestressed wire111 in between is large enough (e.g., greater than 25 inches), then the two areas of prestress loss may be analyzed independently from each other. In such a case, the worst case scenario is the larger of the two lengths of prestressed loss, and there may be no reason to consider the shorter section. On the other extreme, if the segment of intactprestressed wire111 in between is small enough (e.g., less than 3 inches), then the lengths of the two sections of prestress loss may be added together into one effective length. In addition, there may be an intermediate length of the segment of intactprestressed wire111 between the two sections of prestress loss wherein an effective length of prestress loss may be given by a formula such as:
effective length =L2(0.6064−0.02424B)+L1(1.0754−0.00303B)
where L1 and L2 are lengths of the two area of prestress loss, L1>L2, and B is the length of the area of intact[0071]prestressed wire111 in between the two areas of prestress loss.
As would be apparent to a person skilled in the art, the constants in the above equations, and the range of B for which the equations apply, may vary depending on the size and design of the pipe.[0072]
Returning to FIG. 4, in various embodiments of the present invention, different designs and sizes of pipe may be evaluated for rupture and cracking. For each pipe design, the length of the prestress loss and the magnitude of the internal pressure may be varied to calculate, for example, the maximum stress in the[0073]core105. The relationship between prestress loss length and internal pressure may then be determined. The length of prestress loss, which may be readily convertible to the number ofwire111 breaks (and vice versa), may be plotted as a function of pressure that causes cracking or rupture. In one exemplary embodiment, separate relations or plots may be prepared and considered for prestress loss at the end of the pipe, and prestress loss in the middle of the pipe.
An example of a plot of pressure versus wires broken (graph or plot[0074]400) is shown in FIG. 4, which illustrates a relation that may be computer implemented. Four curves (407,410,415, and420) are shown ongraph400. In the embodiment illustrated,curve410 indicates rupture,curve420 indicates cracking onset, andcurve415 is located betweencurve410 andcurve420, dividing the zone in between into repair priority zones, described in more detail below.Graph400 also showspressure412, which may be essentially the rupture pressure of the steel cylinder or can107 without the benefit of anyprestressing wire111 orconcrete core105 strength. The right hand portion ofpressure412 is in common with the right hand portion ofcurve410 wherein a large number ofwires111 are broken. Thus, the condition ofwire111 may not be relevant for pipe operated at maximum anticipated pressures significantly belowpressure412, sincecan107 may adequately withstand the pressure.
Referring further to FIG. 4, an exemplary embodiment of the present invention is a system or method of facilitating the management of a pipeline, such as determining whether or when to repair or replace pipe (e.g., PCCP) that involves using a relation or graph such as[0075]graph400 of pressure versus a quantification of the degradation of the structural integrity of the pipe (e.g.,100). As mentioned above, the relation orgraph400 has repair priority zones of high risk (e.g.,1aand1b) and low risk (e.g.,4 and5), plus additional zones of intermediate or medium risk (e.g.,2a,2b,3a, and3b). (However, other zones could be considered high, medium, or low risk, or higher or lower, e.g. relative to each other.) The quantification of the degradation of the structural integrity of the pipe may include, for example, determining the quantity of broken wires (111 shown in FIG. 1), and the pressure may be, for example, the maximum pressure anticipated in thepipe100. In the exemplary embodiment shown, the relation orgraph400 further shows thepressure412 for the ultimate strength of the cylinder or can107. This may be the pressure at which thecan107 will rupture absent any prestressing force (e.g., from wire111).
Still referring to FIG. 4, and occasionally to FIG. 1, the repair priorities or repair priority zones in the exemplary embodiment shown in FIG. 4 are as follows:[0076]Priority1ais generally located where the expected maximum pressure exceeds by more than a predetermined amount, the rupture pressure of thecomposite pipe100 given the number (or effective number) ofwire111 breaks that were found. Thus,priority1ais generally located where the maximum pressure exceedscurve407 for the quantity of wire breaks found during inspection. The predetermined amount may be, as examples, 10 percent of the rupture pressure (depicted by curve410).Priority1ais the highest priority or zone of highest risk shown ongraph400.
[0077]Priority1bis generally located where the expected maximum pressure exceeds, by less than the predetermined amount, the rupture pressure of thepipe100 given the number (or effective number) ofwire111 breaks that were found. In other words,priority1bis generally located betweencurves410 and407.
[0078]Priority2ais generally located where the expected maximum pressure exceeds the pressure that causes theconcrete core105 to crack (depicted by curve420), by more than the amount delineated bycurve415, but is generally below the rupture pressure of the pipe100 (the rupture pressure depicted by curve410) given the number (or effective number) ofwire111 breaks that were found.Priority2ais generally located betweencurves415 and410, and above (can107 rupture) pressure412 (of the composite pipe100).
The action pressure or[0079]curve415 may be generally located, as an example, halfway between the onset ofcore105 cracking (curve420) and rupture pressure (curve410). However, the action pressure orcurve415 may be located higher or lower for various applications, as may be determined by experience. For instance, if experience shows that pipe sections just belowcurve415 often fail in service, then it may be advisable to lowercurve415 so that such pipe sections are classified in a higher repair priority and are then repaired or replaced before they fail. On the other hand, if pipe sections designated for replacement are hydrostatically tested to failure, and it is found that they consistently fail far abovecurve415, then it may be advisable to raisecurve415 such that sections of pipe are classified in a lower repair priority to avoid the unnecessary expense of repairing or replacing sections of pipe that are fit for service. In addition, although only onecurve415 is shown, additional action pressures or curves defining additional priority zones or classifications may be utilized, as would be apparent to a person of skill in the art.
Continuing to refer to FIG. 4, in the exemplary embodiment illustrated,[0080]priority2bis generally located where the expected maximum pressure exceeds the pressure that causes the concrete core (e.g.,core105 shown in FIG. 1) to crack, by less than the amount delineated bycurve415, and is further less than the rupture pressure of thepipe100 given the number (or effective number) ofwire111 breaks that were found.Priority2bis located betweencurves420 and415, and abovepressure412.
[0081]Priority3ais generally located where the expected maximum pressure exceeds the pressure that causes theconcrete core105 to crack, by more than the amount delineated bycurve415, but the expected maximum pressure is less than the rupture pressure of thepipe100 given the number (or effective number) ofwire111 breaks that were found.Priority3ais generally located betweencurves415 and410, and belowpressure412.
[0082]Priority3bis generally located where the expected maximum pressure exceeds the pressure that causes theconcrete core105 to crack, by less than the amount delineated bycurve415, and is therefore significantly less than the rupture pressure of thepipe100 given the number (or effective number) ofwire111 breaks that were found. Thus,priority3bis generally located betweencurves420 and415, and belowpressure412.
[0083]Priority4 is generally located where the expected maximum pressure is less than the pressure that causes theconcrete core105 to crack (and is therefore much less than the rupture pressure of the pipe) given the number (or effective number) ofwire111 breaks that were found.Priority4 is generally located to the left of, or below,curve420, and is abovepressure412.Priority4 is the zone in which PCCP is typically designed to operate.
[0084]Priority5 is generally located where the expected maximum pressure is less than the pressure that causes theconcrete core105 to crack (and is therefore much less than the rupture pressure of the pipe) given the number (or effective number) ofwire111 breaks that were found.Priority5 is generally located to the left of or belowcurve420, and is belowpressure412.Priority5 is the lowest risk zone shown ongraph400.
Generally, the lower the number of the priority zone described above, the greater the risk or urgency that pronounced action be taken in the management of the[0085]pipe100 such as repairing (step327 in FIG. 3) or replacing (step324 in FIG. 3) thepipe100.Zones2aand2bare considered to be a higher priority thanzones3aand3bbecauseadditional wire111 breakage will theoretically not lead topipe100 failure inzones3aand3bsince the anticipated maximum internal pressure is less than the pressure required to rupture thecan107 absent anyprestressed wires111. Although cracking ofcore105 may allowwater106 to leak intocan107, it has been found that corrosion of the embedded steel cylinder or can107 may be a very slow process, even if theconcrete core105 is cracked. However, embodiments of the present invention may take into consideration deterioration ofcan107 such as via corrosion. This may be particularly important where the pipe is operated for a long time below (can107 rupture) pressure412 (e.g. inzones3aor3b).
Returning once again to FIG. 2, the analysis or program outputs or recommended
[0086]action260 may include tracking the condition of the pipe. In embodiments where a computer or
processor230 is used, the computer or
processor230 may store design, configuration, and repair history for the pipeline, which may be input (at least at one time) as parameters (e.g.,
201-
207, for example, via
step305 shown in FIG. 3). This may include design information (e.g., step
305) and as-built conditions for the piping system, and may be useful in outage and emergency situations where rapid and accurate feedback may be essential. The computer (processor
230) may also predict trends such as considering the element of time-related degradation rate. As an example, the computer or
processor230 may calculate the time interval that may be used to predict when a degraded pipe spool or section will enter the next zone of risk, classification, or repair priority, using the following algorithm:
where:[0087]
WB=number of wire breaks[0088]
xWBT=wire break threshold, i.e., the number of wire breaks it takes to enter repair category X. (from engineering review of prestress concrete cylinder structural performance data, and pipe management risk assessment).[0089]
GWB=governing wire break, i.e., the number of wire breaks used to determine repair priority X. (from engineering review of remote field eddy current data).[0090]
The computer or[0091]processor230 may also output repair prioritization, operating methods, design, maintenance and repair alternatives, or some combination of these.
Referring primarily to FIG. 5, a further exemplary embodiment of the present invention is a[0092]method500 of managing or facilitating the management of pipe (e.g., pipe having a plurality of sections of PCCP).Method500 may include, for example, the steps of inspecting the pipe (step302), acquiring or inputting design parameters (step305) acquiring or inputting inspection parameters (step308), and acquiring or inputting the internal pressure (step311), which may be an estimated maximum pressure that is likely to exist in future service as described above. All or part of the step of acquiring or inputting design parameters (step305) may be performed before the inspection of the pipe (step302), and once the design parameters are acquired or input (step305), it may not be necessary to repeat this step when additional inspections (step302) are performed in the future.Method500 may also include the step of calculating the crack onset pressure (e.g., of core105), for instance, absent any prestress (in wire111). This step is also described above.
In the example of[0093]Method500, a determination may then be made whether the internal pressure (input in step311) exceeds the crack onset pressure (calculated in step541) (step543). If not, then the risk of pipe failure is fairly low (zones3a,3b, or5 shown in FIG. 4), and in the exemplary embodiment depicted in FIG. 5, no further action is taken other than to determine when to inspect the pipe again (step332), and to wait until it is time to perform the next inspection (step335). However, as would be apparent to a skilled artisan, in other embodiments, other action may be taken, which may include further analysis and classification intozones3a,3b, or5 shown in FIG. 4.
If the internal pressure exceeds the crack onset pressure (as determined in step[0094]543), then FIG. 5 shows the steps of calculating the maximum load of the longitudinal strips of the core105 (step546) (the analysis of the strips was described in more detail above). If the internal pressure exceeds the crack onset pressure (as determined in step543), then in the case of PCCP, the maximum load of thecan107 is also calculated (step548) (generally pressure412 shown in FIG. 4). The maximum load of the longitudinal strips of the core105 (calculated in step546), and the maximum load of the can107 (calculated in step548) may be used to calculate the rupture pressure of the pipe (step551), as described above. The rupture pressure of the pipe (calculated in step551) may, for instance, be a point oncurve410 illustrated in FIG. 4 for the corresponding number of broken wires (e.g., input in step308).
In the next step shown in the exemplary embodiment illustrated in FIG. 5, the action pressure between the crack onset pressure (calculated in step[0095]541) and the rupture pressure (calculated in step551) is calculated (step556). The action pressure between the crack onset pressure and the rupture pressure may be, for instance, the same or analogous tocurve415 shown in FIG. 4 and described above. Once the action pressure is calculated (step556), a determination is made whether the internal pressure (input in step311) exceeds the action pressure (step563). If so, then in the exemplary embodiment depicted in FIG. 5, action is taken (step570), e.g. pipe management action. This action (of step570) may involve, inter alia, repairing, replacing, or monitoring the pipe, for instance, as described in more detail elsewhere herein. Pipe management action in this and other embodiments, may also (or in the alternative) include other activities such as making operational changes to reduce the pressure or flow rate in the pipe, adding devices or procedures to relieve or reduce surge or water hammer, constructing a back-up pipeline to be used if the original pipeline fails, stockpiling materials or equipment or arranging for properly skilled labor to be available in the event repair or replacement is needed, or initiating action to reduce the harm or damage that would be caused by a failure. Pipe management action may even further (or in the alternative) include doing nothing (as used herein, “doing nothing” may include undertaking no new pipe management action for the section of pipe, e.g. until the next time to inspect the pipe, but would generally not preclude initiating action that would have been taken anyway, such as using or cleaning the pipe), monitoring the pipe differently, inspecting the pipe sooner, initiating any of the above identified pipe management actions sooner, or other action that may be identified by a person of skill in the art.
In the exemplary embodiment depicted in FIG. 5, if the internal pressure (input in step[0096]311) is less than the action pressure (compared in step563), then the risk of pipe failure may be fairly low (zones2bor3bshown in FIG. 4), and no further action may be needed, other than to determine when to inspect the pipe again (step332) and to wait until it is time to perform the next inspection (step335). As would be apparent to a person of skill in the art, other embodiments of the present invention may involve other calculations and comparisons, for example, to differentiate between the various zones depicted in FIG. 4.
FIG. 6 illustrates, as a further exemplary embodiment, a[0097]method600 of managing or facilitating the management of pipe or a pipeline, (e.g., PCCP). The present invention (e.g., Method600) may be applied, for instance, to each section or spool of pipe (e.g., each bell and spigot section), or for larger sections of pipe, up to the entire pipeline.Method600 may include the step of storing design data (step605) for the pipe (e.g.,pipe100 shown in FIG. 1). The design data (of step605) may include dimensions of thepipe100, external loading on thepipe100 and other design data described herein, for instance, with reference to step305 of FIGS. 3 and 5. As an example,method600 may involve a computer or processor (e.g.,processor230 shown in FIG. 2) which may store e.g., 100 design drawings, and data for 150 degraded PCCP spools or sections and 100 repaired PCCP spools or sections, or what is needed for storage for the particular application.
Still referring to FIG. 6,[0098]method600 may also include the step of inspecting the pipe (step302), which may be as described above, and may include an evaluation of the quantity of broken or failed wires (e.g.,wires111 shown in FIG. 1, for instance, within a predetermined length of pipe (e.g., pipe100). The predetermined length may be, for example, one spool or section of bell and spigot pipe. However, shorter or longer predetermined lengths may be used, for instance, as would be conducive to inspection, repair, or other pipe management action.Method600 may further include the step of estimating pressure (step611) which may be the maximum pressure that will, or is expected to (e.g. is likely to), exist withinpipe100 in future service. The pressure (of step611) may be the same or similar to the pressure ofstep311 described above with reference to step305 of FIGS. 3 and 5.
[0099]Method600 may also include a step of facilitating a determination or designating a classification (step660 (e.g., for the condition of the pipe). This step may involve using the design data for the pipe (e.g., stored in step605), the quantity of failed wires (e.g., from step302), and the maximum pressure (e.g., from step611). The inspecting step (step302) may be repeated at different times (e.g., along with other steps as shown in FIG. 6), andmethod600 may include the step of tracking the condition of thepipe100, such as tracking changes (step640), for example, in the quantity of failedwires111 over time. For instance, tracking changes (step640) ofmethod600 may include calculating the rate ofwire111 failures, and predicting whenpipe100 will enter the next lower classification (designated in step660) or zone (e.g., of risk as shown in FIG. 4 and described above with reference thereto).
[0100]Method600 generally also includes the step of taking, initiating or implementing pipe management action (step670) which may be based on the classification (e.g., of step660) or zone (as shown in FIG. 4). Each classification (e.g., of step660) may have a corresponding action (taken in step670), which may be, as examples, doing nothing, monitoring the pipe, repairing the pipe, or replacing the pipe.Method600 may involve two classifications, three classifications, or more (e.g., eight classifications corresponding to the eight zones shown in FIG. 4). As an example, if there are three classifications, the action corresponding to the first classification may be doing nothing, at least until the next inspection; the action corresponding to the second classification may be monitoring the pipe; and the action corresponding to the third classification may be repairing or replacing the pipe.
The parameters or criteria upon which the classification is determined (e.g., in step[0101]660) may involve crack onset pressure (e.g., as described above, for instance, with reference tosteps541 and543 in FIG. 5), rupture pressure (e.g., as described above, for instance, with reference tosteps551 in FIG. 5), the maximum load of the can (e.g., as described above, for instance, with reference tosteps548 in FIG. 5), or an intermediate action pressure (e.g., as described above with reference tosteps556 and563 in FIG. 5), or other measurable or calculable parameters or criteria, including those described herein.
Still referring to FIG. 6,[0102]method600 may further include the step of analyzing thepipe100 for lack of prestress pressure (step650). This analysis (of step650) may be over the pipe's entire circumference and over a limited length ofpipe100, or it may be over just a portion of the pipe's circumference, and over a limited length of pipe. In addition, this analysis (of step650) may include analyzing thepipe100 for lack of prestress pressure over two limited lengths of pipe with a segment of intactprestressed wire111 located between the first limited length and the second limited length. The segment with intactprestressed wire111 may be, for instance, more than 3-inches long, and less than 25-inches long, and may involve using the formula described above. These analyses may be as described in more detail above.
Still referring to FIG. 6,[0103]method600 may include the step of analyzing the rupture pressure (step610), e.g., of thepipe100 shown in FIG. 1. Thus, the step of designating a classification (step660) may include determining whether the maximum pressure (e.g., estimated in step611) exceeds the rupture pressure of the pipe (e.g.,curve410 shown in FIG. 4). Further, the step of designating a classification (step660) may include determining whether the maximum pressure exceeds, by more than a predetermined amount, the rupture pressure of the pipe (e.g., exceedscurve407 shown on FIG. 4).
[0104]Method600 may even further include the step of analyzing the crack onset pressure (step620) (e.g., ofpipe100 shown in FIG. 1). The step of designating a classification (step660) may include determining whether the maximum pressure (e.g., estimated in step611) is less than the rupture pressure (e.g., analyzed in step610) of the pipe (e.g.,pipe100 shown in FIG. 1), and the maximum pressure exceeds the crack onset pressure (e.g., analyzed in step620). Further, the step of designating a classification (step660) may include determining whether the maximum pressure (e.g., estimated in step611) is closer to the rupture pressure (e.g., analyzed in step610) of the pipe (e.g.,pipe100 shown in FIG. 1), than to the crack onset pressure (e.g., analyzed in step620), or vice versa. Even further still, the step of designating a classification (step660) may include determining whether the maximum pressure (e.g., estimated in step611) is less than the crack onset pressure (e.g., analyzed in step620). Still further,method600 may include the step of analyzing the rupture pressure of the can107 (step612), for instance, without anyprestressing wire111. Thus, the step of designating a classification (step660) may include determining whether the maximum pressure (e.g., estimated in step611) is less than the rupture pressure of the cylinder or can (e.g.,pressure412 shown in FIG. 4). In other embodiments, the step of designating a classification (step660) may involve, inter alia, identifying any of the repair priority zones or zones of risk shown in FIG. 4, described herein, or known in the art.
Other variations and modifications of the present invention will be apparent to those of ordinary skill in the art, and it is the intent of the appended claims that such variations and modifications be covered. The particular values and configurations discussed above can be varied, are cited to illustrate particular embodiments of the present invention, and are not intended to limit the scope of the invention. It is contemplated that the use of the present invention can involve components having different characteristics as long as the elements of at least one of the claims below, or the equivalents thereof, are included.[0105]