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Systems, Types, and Components

The risk assessment framework described here is very robust. It can be used for any pipeline material, service (product transported), component, etc. It can also be used for non-pipeline systems and components including subsurface storage caverns. Yes, even geologic formations used for subsurface storage of fluids can be efficiently risk-assessed by methodologies outlined here. For some applications, there will be nuances in segmentation and handling of certain phenomena. However, changes in the risk assessment platform are not needed.

Following are discussions and lessons learned when applying the risk assessment framework to various pipeline types, materials, component types, system types, products, geographic locations (including offshore). The focus here is on pipelines and pipeline-like systems–anything involving transport (and transport-related activities) of fluidized products (gas, liquids, slurries, etc) through continuous conduits.

System

The word ‘system’ has many uses here. It is used in context such as safety system, control system, management system, procedure system, training system, to indicate a collection of parts or sub-systems. While no set definition exists, a pipeline system normally refers to a large collection of pipeline segments and related stations/facilities.

Pipeline Types

Pipeline systems are often categorized into types such as transmission, distribution, gathering, offshore, and others, as discussed in . All types are appropriately assessed using the same methodology.

Pipe, pipeline, component, facility

As used here, a pipeline segment can be any length of pipe, not necessarily a ‘joint’ length. A component is a part of a pipeline that is other than a pipe segment and can be a flange, valve, fitting, tank, pump, compressor, separator, filter, regulator, or any of many other portions of a typical pipeline. A pipeline is a collection of pipe segments and components. A facility is similarly a collection of segments and components but usually with more variety than simply pipe. A system is one or more pipelines and associated facilities. See also the discussion of segmentation for purposes of assessing risk.

Risk concepts covered here are meant to apply to any segment of pipe, component, entire pipeline, facility, or system. While pipe is often used to illustrate a concept, the concept also applies to any other component.

As a convenience, the terms component and segment will be used most often in these discussions.

The basic risk concepts also apply to all component material types. While steel is often the focus of discussion, risks associated with all other materials of construction such as plastic, cast iron, concrete, and others, can be efficiently assessed using these same methods.

Owner/Operator references are used interchangeably here, both referring to the decision-makers who control choices in pipeline design, operations, and maintenance.

As previously noted, there are admittedly, some nuances when assessing risk of certain components. For instance, consider threaded and other mechanical connections.

Mechanical Connections

When a threaded, flanged, or other mechanical connection leaks, the leak is often classified as ‘material failure’ or some similar but incorrect classification. We say incorrect because material failure is not a failure mechanism but rather the result of some failure mechanism. ‘Material failure’ explains nothing until the failure mechanism is identified.

Any mechanical connection such as a threaded connection, is efficiently modeled as susceptible to degradation similar to corrosion or cracking. In the case of threaded connections, the threads and gasket or sealant, if present, form the containment envelope. That envelope relies on friction as part of its sealing ability and is susceptible to ‘degradation’ from, for example, vibrations which reduce the needed friction.

Just as corrosion is modeled as metal loss–the containment envelope is degrading–the threaded connection can be modeled in an analogous way. Just as with corrosion or cracking, mpy measures the loss of sealing ability and ‘effective’ wall thickness (across interlocked threads) as the surrogate for that sealing ability. Loss of this theoretical wall thickness as stand-in for sealing ability occurs from sources similar to cracking: fatigue cycling from thermal or mechanical origins, vibrations from rotating equipment, wind, wave action, etc.

Published inBeginners CornerDeeper DiveDoing it RightRisk Modeling