Fundamental basis and implementation of shell and tube heat exchanger project design: condenser and evaporator study


DALKILIÇ A. S. , AÇIKGÖZ Ö. , TAPAN Ş., WONGWISES S.

HEAT AND MASS TRANSFER, cilt.52, ss.2863-2878, 2016 (SCI İndekslerine Giren Dergi)

  • Cilt numarası: 52 Konu: 12
  • Basım Tarihi: 2016
  • Doi Numarası: 10.1007/s00231-016-1790-9
  • Dergi Adı: HEAT AND MASS TRANSFER
  • Sayfa Sayısı: ss.2863-2878

Özet

A shell and tube heat exchanger is used as a condenser and an evaporator in this theoretical study. Parametric performance analyses for various actual refrigerants were performed using well-known correlations in open sources. Condensation and evaporation were occurred in the shell side while the water was flowing in the tube side of heat exchanger. Heat transfer rate from tube side was kept constant for condenser and evaporator design. Condensing temperatures were varied from 35 to 60 A degrees C whereas evaporating temperatures were ranging from -15 to 10 A degrees C for the refrigerants of R12, R22, R134a, R32, R507A, R404A, R502, R407C, R152A, R410A and R1234ZE. Variation of convective heat transfer coefficients of refrigerants, total heat transfer coefficients with Reynolds numbers and saturation temperatures were given as validation process considering not only fouling resistance and omission of it but also staggered (triangular) and line (square) arrangements. The minimum tube lengths and necessary pumping powers were calculated and given as case studies for the investigated refrigerants considering validation criteria. It was understood that refrigerant type, fouling resistance and arrangement type are one of the crucial issues regarding the determination of heat exchanger's size and energy consumption. Consequently, R32 and R152a were found to require the shortest tube length and lowest pumping power in the condenser, whereas R507 and R407C have the same advantages in the evaporator. Their heat transfer coefficients were also determined larger than others as expectedly.