STUDY ON PARAMETERS IN COUNTER CURRENT DOUBLE PIPE HEAT EXCHANGER APPLYING CIRCULAR TURBULATOR

S. Sudiono, R. Sundari, Rini Anggraini
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Abstract

Many industries dealing with manufacturing and HVAC (heating, ventilation, and air cooling) are rely heavily on thermodynamics principles with respect to heat and mass transfer. The objective of this study is to do optimization to yield optimum heat transfer rate and minimized pressure drop with regard to number of circular turbulator (CT) and water debit on Nusselt number (Nu) in counter current double pipe heat exchanger. This work has applied the classical rule of thermal science dealing with Nusselt number in relation to convection and conduction of heat transfer rate due to temperature effect. The result shows the highest Nu found to be 835.3 at 5 CT and water debit of 9 L/min. The addition of CT number gives effect on fluid current due to vortex generation. This study also investigates the effect of CT number on friction coefficient that the friction coefficient of a heat exchanger in the absence of CT is lower than that in the presence of CT. For any CT number, the friction coefficient is reduced with increasing water debit. The study has also found that the thermal performance ratio has achieved higher values for heat exchanger in the absence of CT.
应用圆形紊流器的逆流双管换热器参数研究
许多涉及制造业和暖通空调(采暖、通风和空气冷却)的行业在很大程度上依赖于关于传热和传质的热力学原理。本研究的目的是对逆流双管换热器中圆形紊流器(CT)的数量和努塞尔数(Nu)的水量进行优化,以获得最优的换热率和最小的压降。这项工作应用了热科学的经典规则,处理与温度效应引起的对流和导热率有关的努塞尔数。结果表明,5 CT时最高Nu为835.3,用水量为9l /min。CT数的增加会对涡流产生的流体电流产生影响。本研究还考察了连续油管数对摩擦系数的影响,发现无连续油管时换热器的摩擦系数低于有连续油管时的摩擦系数。对于任意CT数,摩擦系数随水的增加而减小。研究还发现,在没有CT的情况下,换热器的热工性能比达到了更高的值。
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