Influence of intermittent flow sub-patterns on erosion-corrosion in horizontal pipe

被引:60
作者
Thaker, Jignesh [1 ]
Banerjee, Jyotirmay [1 ]
机构
[1] SVNIT, Dept Mech Engn, Surat 395007, Gujarat, India
关键词
Intermittent flow; Flow visualization; Flow characteristics; Erosion-corrosion regime map; 2-PHASE SLUG FLOW; STATISTICAL PARAMETERS; PRESSURE-DROP; VOID FRACTION; LIQUID SLUGS; MODEL; DISTRIBUTIONS; TRANSITION; PREDICTION; INITIATION;
D O I
10.1016/j.petrol.2016.05.006
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Thinning of pipe wall due to erosion and corrosion has resulted in many catastrophic failures and huge economic losses in petroleum refineries (Wood et al., 2013) and nuclear power stations (Ahmed, 2012). The intermittent structure of two-phase flow through pipe (intermittent flow regime) is an important factor responsible for such erosion and corrosion. The present research is an effort to develop a regime map showing possible erosion and corrosion phenomena due to intermittent flows in pipe. In this direction, flow visualization experiments are carried out for three distinct sub-regimes of intermittent flow namely, plug flow with or without bubble rim, less aerated slug flow and highly aerated slug flow. Images captured at a rate of 1600 frames per second at 288 diameter downstream of inlet are utilised for analysing the dynamics of intermittent flow structure in terms of expansion, contraction, breaking, coalescence, collapse, and collision of bubbles. Quantitative measurements of intermittent flow characteristics (including plug/slug frequency, plug/slug velocity and length of liquid plug/slug) and their influence on erosion-corrosion phenomena in the pipe are reported in detail. Based on these qualitative and quantitative analysis, a regime map for prediction of erosion-corrosion phenomena in pipes is established as a function of inlet flow conditions for both the phases. Transition boundaries for four distinct erosion-corrosion phenomena: shear stress induced erosion, cavitation erosion, liquid impact induced erosion and flow accelerated corrosion are represented in the map and eight distinct regimes of erosion corrosion are illustrated. The regime map is represented in terms of non-dimensional superficial Reynolds numbers of both the phases to account for pipe diameter, flow rate and fluid viscosity. This erosion corrosion regime map developed in this research will immensely aid to the effective design of piping systems and optimization of operating conditions for safer operation of petroleum refineries and nuclear power stations. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:298 / 320
页数:23
相关论文
共 70 条
[1]   Liquid slug holdup in horizontal and slightly inclined two-phase slug flow [J].
Abdul-Majeed, GH .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2000, 27 (1-2) :27-32
[2]   Experimental investigation of flow accelerated corrosion under two-phase flow conditions [J].
Ahmed, Wael H. ;
Bello, Mufatiu M. ;
El Nakla, Meamer ;
Al Sarkhi, Abdelsalam ;
Badr, Hassan M. .
NUCLEAR ENGINEERING AND DESIGN, 2014, 267 :34-43
[3]   Prediction of slug liquid holdup in high viscosity liquid and gas twophase flow in horizontal pipes [J].
Al-Safran, Eissa ;
Kora, Ceyda ;
Sarica, Cem .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2015, 133 :566-575
[4]   Prediction of Slug Liquid Holdup in Horizontal Pipes [J].
Al-Safran, Eissa .
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME, 2009, 131 (02) :0230011-0230018
[5]  
Alssayh M., 2013, P 1 EUR C STRUCT DYN
[6]   DRIFT VELOCITY OF ELONGATED BUBBLES IN INCLINED PIPES [J].
ALVES, IN ;
SHOHAM, O ;
TAITEL, Y .
CHEMICAL ENGINEERING SCIENCE, 1993, 48 (17) :3063-3070
[7]   AN INVESTIGATION OF VOID FRACTION IN LIQUID SLUGS FOR HORIZONTAL AND INCLINED GAS-LIQUID PIPE-FLOW [J].
ANDREUSSI, P ;
BENDIKSEN, K .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (06) :937-946
[8]   EFFECT OF LIQUID VISCOSITY ON THE STRATIFIED SLUG TRANSITION IN HORIZONTAL PIPE-FLOW [J].
ANDRITSOS, N ;
WILLIAMS, L ;
HANRATTY, TJ .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (06) :877-892
[9]  
[Anonymous], 2013, JRC SCI POLICY REPOR
[10]  
[Anonymous], 1999, 2 INT C CFD MIN PROC