scholarly journals Reliability modeling for a two-phase degradation system with a change point based on a Wiener process

2020 ◽  
Vol 193 ◽  
pp. 106601 ◽  
Author(s):  
Hongda Gao ◽  
Lirong Cui ◽  
Qinglai Dong
Keyword(s):  
Wiener Process ◽  
Change Point ◽  
Two Phase ◽  
Reliability Modeling

Bayesian analysis of two-phase degradation data based on change-point Wiener process

2018 ◽  
Vol 170 ◽  
pp. 244-256 ◽  
Author(s):  
Pingping Wang ◽  
Yincai Tang ◽  
Suk Joo Bae ◽  
Yong He
Keyword(s):  
Bayesian Analysis ◽  
Wiener Process ◽  
Change Point ◽  
Two Phase ◽  
Degradation Data

Two-Phase Degradation Process Model With Abrupt Jump at Change Point Governed by Wiener Process

2017 ◽  
Vol 66 (4) ◽  
pp. 1345-1360 ◽  
Author(s):  
Dejing Kong ◽  
Narayanaswamy Balakrishnan ◽  
Lirong Cui
Keyword(s):  
Wiener Process ◽  
Change Point ◽  
Process Model ◽  
Degradation Process ◽  
Two Phase ◽  
Abrupt Jump

Reliability modeling for intermittent working system based on Wiener process

2021 ◽  
pp. 107599
Author(s):  
Haizhen Zhu ◽  
Xueqi Wang ◽  
Mingqing Xiao ◽  
Zhao Yang ◽  
Xilang Tang ◽  
...  
Keyword(s):  
Wiener Process ◽  
Reliability Modeling

Using Change Point Analysis for Image Processing of Developing Adiabatic Two-Phase Flow After Expansion Valve

2007 ◽  
Author(s):  
Chad D. Bowers ◽  
Predrag S. Hrnjak
Keyword(s):  
Change Point ◽  
High Speed ◽  
Separation Distance ◽  
Change Point Analysis ◽  
Working Fluid ◽  
High Speed Camera ◽  
Two Phase ◽  
Flow Parameters ◽  
Point Analysis ◽  
Expansion Valve

This paper presents a method of analyzing images obtained from a high speed camera in a study of developing two-phase refrigerant flow after an expansion valve, using a technique known as Change Point Analysis. Specifically, a method for automating the determination of separation distance and the location of the liquid/vapor interface in stratified type flows is outlined. The experiments were conducted in transparent PVC tubes, with inner diameters of 8.7mm and 15.3mm. A working fluid of oil free R134a was used. Dynamic flow parameters of inlet quality and mass flux were varied from 5–35% and 15–40g/s, respectively. Flow visualization was achieved through the use of a high speed camera.

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