Search engine for discovering works of Art, research articles, and books related to Art and Culture
ShareThis
Javascript must be enabled to continue!

Stress Classification Lines for Non-Standard Y-Tee Design in Piping System

View through CrossRef
All processes fluids in the oil and gas industry are generally transferred from one point to another via complex piping networks. The process temperature and the pressure of the fluids may vary between -21 °C to 816 °C and from atmospheric, 1.013 barg to 431 barg, respectively. Under these conditions, the entire piping networks are exposed to thermal expansion and contraction resulting in mechanical bending, potentially causing mechanical failures. The most common pipe fitting used in piping networks to divide the fluid flow into two different directions would be a standard equal tee which was designed in accordance with ASME B16.9. The equal tee, however, has distinctive flexibility characteristics compared to the pipe, which is well defined in ASME B31.3. These flexibility characteristics generate a stress intensification factor (SIF) through bending moment equations for beam-type element analysis for standard equal tee components. However, due to the limitation of SIF and flexibility characteristics for the non-standard pipe fittings, the stress evaluation could not be done using beam-type element analysis. When using finite element method (FEM) analysis, generally equivalent stresses (Von Mises or Tresca) or principal stresses would be evaluated depending on the stress categorization as explained in ASME codes and standards. In this paper, a stress evaluation method for non-standard Y-tee was developed and demonstrated against ASME VIII Div. 2 Part 5 requirement. The developed SCLs line for the non-standard Y-tee fittings provides the guides for stress assessment against design stress allowable. An optimum design for non-standard Y-tee is proposed at 45° and 60° crotch radii which resulted in lower stress value at SCL lines, hence improving the structural integrity.
Title: Stress Classification Lines for Non-Standard Y-Tee Design in Piping System
Description:
All processes fluids in the oil and gas industry are generally transferred from one point to another via complex piping networks.
The process temperature and the pressure of the fluids may vary between -21 °C to 816 °C and from atmospheric, 1.
013 barg to 431 barg, respectively.
Under these conditions, the entire piping networks are exposed to thermal expansion and contraction resulting in mechanical bending, potentially causing mechanical failures.
The most common pipe fitting used in piping networks to divide the fluid flow into two different directions would be a standard equal tee which was designed in accordance with ASME B16.
9.
The equal tee, however, has distinctive flexibility characteristics compared to the pipe, which is well defined in ASME B31.
3.
These flexibility characteristics generate a stress intensification factor (SIF) through bending moment equations for beam-type element analysis for standard equal tee components.
However, due to the limitation of SIF and flexibility characteristics for the non-standard pipe fittings, the stress evaluation could not be done using beam-type element analysis.
When using finite element method (FEM) analysis, generally equivalent stresses (Von Mises or Tresca) or principal stresses would be evaluated depending on the stress categorization as explained in ASME codes and standards.
In this paper, a stress evaluation method for non-standard Y-tee was developed and demonstrated against ASME VIII Div.
2 Part 5 requirement.
The developed SCLs line for the non-standard Y-tee fittings provides the guides for stress assessment against design stress allowable.
An optimum design for non-standard Y-tee is proposed at 45° and 60° crotch radii which resulted in lower stress value at SCL lines, hence improving the structural integrity.

Related Results

Ensuring the Reliability of Offshore Gas Compression Systems
Ensuring the Reliability of Offshore Gas Compression Systems
Summary Selection of offshore gas equipment is based on intended application, efficiency, reliability, and compatibility with platform structural requirements. Th...
Modeling Refractory Stiffness for Piping Flexibility Analysis
Modeling Refractory Stiffness for Piping Flexibility Analysis
Abstract Refractory is commonly used in pipes for cold wall design. Generally, to analyze refractory lined piping, a piping stress analysis is done using commerciall...
Numerical Simulation of Gas–Liquid–Solid Three-Phase Erosion in a Gas Storage Tank Tee
Numerical Simulation of Gas–Liquid–Solid Three-Phase Erosion in a Gas Storage Tank Tee
The objective is to address the issue of gas-carrying particles generated by erosion wear problems in the transportation process of gas storage reservoir pipelines. In accordance w...
Design
Design
Conventional definitions of design rarely capture its reach into our everyday lives. The Design Council, for example, estimates that more than 2.5 million people use design-related...
Dual-mode Integrity Measurement System Based on Virtualized TEE
Dual-mode Integrity Measurement System Based on Virtualized TEE
Abstract The Trusted Execution Environment (TEE) is mainly used to protect sensitive information and ensure information security. TEE has been used in the system str...
Improving LNG Plant Piping: Or How LNG Plants Are Improving Piping
Improving LNG Plant Piping: Or How LNG Plants Are Improving Piping
Abstract An LNG plant is essentially a variety of static and rotating mechanical equipment interconnected by piping. LNG plants contain a significant amount of pipin...
Tide induced piping risk assessed by transient groundwater flow
Tide induced piping risk assessed by transient groundwater flow
Dutch dike and levee design codes provide a solid framework for the design of dikes and levees. One of the failure modes that have to be considered by these codes is ‘pip...

Back to Top