CFD simulation of helical coil heat exchanger with Different coil pitch to heating heavy fuel oil

Safaa A. Saleh, Z. K. Kadhim, K. Khalaf
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Abstract

In current work, CFD simulation of "shell and helical coil heat exchanger" has been done using ANSYS FLUENT package 19.2.  Numerical study involved design of helical tube with different curvature ratio (di/Dc) 0.166, 0.153, and 0.142 and different coil pitch (30, 50, 75, and 100) mm has been chosen to study the effect of curvature ratio and coil pitch. In shell side cold fluid (oil) "flow rate" is varying from (0.06 - 0.1) kg/s and hot fluid (air) velocity ranges are from (20 to 48) m/s in helical tube with inlet temperature (200, 225, 250) °C. It has been found out that increasing "oil mass flow rate" from (0.06-0.1) kg/s cause decreasing "oil outlet temperature" about 3% and increasing "heat transfer rate", with percentage 37%. From numerical results the curvature ratio 0.142 gives higher heat transfer rate and oil outlet temperature while higher Dean number and Nusselt number in coil with curvature ratio 0.166. Also, results show increases of coil pitch led to increasing in overall heat transfer coefficient and Nusselt number of the shell side. while, heat transfer, oil outlet temperature effectiveness and pressure drop, decreases along the coil with increasing coil pitch.
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不同盘管间距螺旋盘管热交换器加热重油的 CFD 仿真
在目前的工作中,利用ANSYS FLUENT软件包19.2对“壳式螺旋盘管换热器”进行了CFD模拟。选取曲率比(di/Dc)为0.166、0.153和0.142、线圈间距(30、50、75和100)mm的螺旋管进行了数值研究,研究了曲率比和线圈间距的影响。壳体侧冷液(油)“流量”变化范围为(0.06 - 0.1)kg/s,热流体(空气)速度范围为(20至48)m/s,螺旋管入口温度为(200,225,250)°C。结果表明,在(0.06 ~ 0.1)kg/s范围内增加“油质量流量”,可使“油出口温度”降低约3%,“换热率”提高约37%。计算结果表明,曲率比为0.142时,线圈的换热率和出油温度较高,曲率比为0.166时,线圈的迪安数和努塞尔数较高。盘管间距的增大导致壳侧总换热系数和努塞尔数的增大。而随着盘管间距的增大,沿盘管方向的换热系数、油出口温度有效性和压力降均减小。
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