A comparative study between the effect of swirl flow and axial flow on the rate of diffusion controlled corrosion in a double tube heat exchanger

被引:6
作者
Mustafa, S. [1 ]
Abdel-Aziz, M. H. [1 ,2 ]
Sedahmed, G. H. [1 ]
El-Gayar, D. A. [1 ]
机构
[1] Alexandria Univ, Fac Engn, Chem Engn Dept, Alexandria, Egypt
[2] King Abdulaziz Univ, Chem & Mat Engn Dept, Rabigh, Saudi Arabia
关键词
Swirl flow; drag-reducing polymer; annular ducts; corrosion inhibition; corrosion allowance; MASS-TRANSFER; TURBULENT-FLOW; DRAG REDUCTION; TRANSFER ENHANCEMENT; MOMENTUM-TRANSFER; DECAYING FLOW; PIPE; ADDITIVES; BEHAVIOR; REACTOR;
D O I
10.1080/08916152.2021.1996485
中图分类号
O414.1 [热力学];
学科分类号
摘要
The rate of diffusion-controlled corrosion of an annulus under swirl flow was studied by measuring the limiting current of the cathodic reduction of potassium ferricyanide depolarizer in the presence and absence of polyox WSR-301 drag-reducing polymer. It was found that the rate of diffusion-controlled corrosion of the inner cylinder of the annulus increases with increasing swirl flow solution velocity and decreases with increasing the active height of the cylinder. The data in the absence of polymer (blank solution) under swirl flow were fitted by a dimensionless equation. The importance of this equation in predicting the rate of diffusion-controlled corrosion and the corrosion allowance during the design of the swirl flow equipment was highlighted. For a given set of conditions, the rate of accelerated swirl flow corrosion was much higher than that of axial flow. Drag reducing polymer was found to inhibit the rate of diffusion-controlled corrosion by a maximum of 23%, if other benefits of the polymer are considered such as the decrease in the shear stress and the associated decrease in the erosion-corrosion tendency besides the decrease in pressure drop and pumping power requirement it may be concluded that the use of drag-reducing polymers in industry is worthwhile.
引用
收藏
页码:964 / 978
页数:15
相关论文
共 52 条
[1]   Liquid-solid mass and heat transfer behavior of a concentric tube airlift reactor [J].
Abdel-Aziz, M. H. ;
Nirdosh, I. ;
Sedahmed, G. H. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2013, 58 (1-2) :735-739
[2]   Study of the rate of liquid-solid mass transfer controlled processes in helical tubes under turbulent flow conditions [J].
Abdel-Aziz, M. H. ;
Mansour, I. A. S. ;
Sedahmed, G. H. .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2010, 49 (07) :643-648
[3]  
ALTAWEEL AM, 1978, CHEM ENG J BIOCH ENG, V15, P81, DOI 10.1016/0300-9467(78)85001-1
[4]   EXPERIMENTAL COMPARISON OF ELECTROCHEMICAL AND DOT-PAINT METHODS FOR THE STUDY OF DECAYING SWIRLING FLOW [J].
AOUABED, H ;
LEGENTILHOMME, P ;
NOUAR, C ;
LEGRAND, J .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1994, 24 (07) :619-625
[5]   Review on the applications and developments of drag reducing polymer in turbulent pipe flow [J].
Asidin, M. A. ;
Suali, E. ;
Jusnukin, T. ;
Lahin, F. A. .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2019, 27 (08) :1921-1932
[6]   DENSITIES, VISCOSITIES, AND DIFFUSIVITIES IN AQUEOUS SODIUM-HYDROXIDE POTASSIUM FERRICYANIDE AND FERROCYANIDE SOLUTIONS [J].
BOURNE, JR ;
DELLAVA, P ;
DOSSENBACH, O ;
POST, T .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1985, 30 (02) :160-163
[7]   MECHANISMS OF HEAT-TRANSFER ENHANCEMENT AND SLOW DECAY OF SWIRL IN TUBES USING TANGENTIAL INJECTION [J].
CHANG, F ;
DHIR, VK .
INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 1995, 16 (02) :78-87
[8]   Fluid dynamics and heat transfer investigations of swirling decaying flow in an annular pipe Part 1: Review, problem description, verification and validation [J].
Chen, Baiman ;
Ho, Kelvin ;
Abakr, Yousif Abdalla ;
Chan, Andrew .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2016, 97 :1029-1043
[9]   MASS AND MOMENTUM-TRANSFER AT THE ROTATING SURFACE OF A CONTINUOUS ANNULAR ELECTROCHEMICAL REACTOR [J].
COEURET, F ;
LEGRAND, J .
ELECTROCHIMICA ACTA, 1983, 28 (05) :611-617
[10]   MASS-TRANSFER IN THE ENTRANCE REGION FOR AXIAL AND SWIRLING ANNULAR-FLOW [J].
DESA, MS ;
SHEMILT, LW ;
SOEGIARTO, IV .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1991, 69 (01) :294-299