Study on secondary side flow of steam generator with coupled heat transfer from primary to secondary side

被引:43
作者
Cong, Tenglong [1 ]
Tian, Wenxi [1 ]
Qiu, Suizheng [1 ]
Su, Guanghui [1 ]
机构
[1] Xi An Jiao Tong Univ, State Key Lab Multiphase Flow Power Engn, Sch Nucl Sci & Technol, Xian 710049, Peoples R China
关键词
Steam generator; Porous media; Flow-induced vibration; Fouling; Separator load; THERMAL-HYDRAULIC CHARACTERISTICS; 3-DIMENSIONAL NUMERICAL-SIMULATION; MACROSCOPIC TURBULENCE MODEL; WET COOLING-TOWERS; POROUS-MEDIA; 2-PHASE FLOW; BOILING FLOW; EXCHANGERS; FLUID; CONDENSERS;
D O I
10.1016/j.applthermaleng.2013.08.024
中图分类号
O414.1 [热力学];
学科分类号
摘要
Thermohydraulics characteristics in the secondary side of AP1000 steam generator (SG) are simulated based on the porous media models. The drift flux two-phase flow model coupled with a simplified flow boiling model is utilized. The heat transfer from primary side fluid to secondary side fluid is calculated three-dimensionally during iterations. The resistances caused by downcomer, tube bundle, support plates and primary separators are considered. Three-dimensional distributions of velocity, temperature, pressure, enthalpy, density, void fraction and flow vapor quality are obtained from the calculation by using the CFD code ANSYS FLUENT. Flow-induced vibration (FIV) damage is analyzed based on the cross flow velocity over the U-bend region of the outmost U-tube. The most severe FIV damages occur at the angles of -0.544 rad on the cold side and 0.353 rad on the hot side with maximum cross flow energies of 1145.2 J/m(3) and 658.9 J/m(3), respectively. Fouling is expected to deposit at the bottom of tube bundle since the velocity there is close to zero. The flow vapor qualities of mixture flowing into separators vary from each other significantly, with the maximum and minimum flow vapor quality in separators of 0.659 and 0.073, which is a severe challenge to the capacity design of separators. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:519 / 530
页数:12
相关论文
共 58 条
[1]  
A. Inc, 2009, ANSYS CFX MULT 12 0
[2]  
[Anonymous], 1974, HEAT EXCHANGER DESIG
[3]  
[Anonymous], ICHMT DIGIT LIB ONLI
[4]   A general two-equation macroscopic turbulence model for incompressible flow in porous media [J].
Antohe, BV ;
Lage, JL .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1997, 40 (13) :3013-3024
[5]  
Antunes J., 1985, T 8 INT C STRUCT MEC, VF1-F2, P229
[6]   OVERVIEW OF NUMERICAL-METHODS FOR PREDICTING FLOW-INDUCED VIBRATION [J].
AXISA, F ;
ANTUNES, J ;
VILLARD, B .
JOURNAL OF PRESSURE VESSEL TECHNOLOGY-TRANSACTIONS OF THE ASME, 1988, 110 (01) :6-14
[7]  
Bergles A.E., 1964, J HEAT TRANSF, V86, P365, DOI DOI 10.1115/1.3688697
[8]   A macroscopic turbulence model for flow in porous media suited for channel, pipe and rod bundle flows [J].
Chandesris, M. ;
Serre, G. ;
Sagaut, P. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2006, 49 (15-16) :2739-2750
[9]   Flow-induced vibration of nuclear steam generator U-tubes in two-phase flow [J].
Chu, In-Cheol ;
Chung, Heung June ;
Lee, Seungtae .
NUCLEAR ENGINEERING AND DESIGN, 2011, 241 (05) :1508-1515
[10]  
DeLemos MJS, 2012, TURBULENCE IN POROUS MEDIA: MODELING AND APPLICATIONS, 2ND EDITION, P1