Tray and point efficiencies from a 0.6 metre diameter distillation columnLOCKETT, M. J; AHMED, I. S.Chemical engineering research and design. 1983, Vol 61, Num 2, pp 110-118Article

Impact of manifold design on heat exchanger efficiencyHARRIS, D. K; WARREN, D. G; GOLDSCHMIDT, V. W et al.Journal of heat transfer. 1997, Vol 119, Num 2, pp 357-362, issn 0022-1481Article

Effect of unbalanced passes on performance of split-flow exchangersVAIDYA, N. Y; SUBRAMANIAN, V.Journal of heat transfer. 1992, Vol 114, Num 2, pp 512-515, issn 0022-1481Article

Predict the number of transfer units for cooling towersKAMAL ADHAM KHODAPARAST.Chemical engineering progress. 1992, Vol 88, Num 4, pp 67-68, issn 0360-7275Article

Thermodynamic optimization of irreversible power cycles with constant external reservoir temperaturesSWANSON, L. W.Journal of engineering for gas turbines and power. 1991, Vol 113, Num 4, pp 505-510, issn 0742-4795Article

Measurements of thermal performance of cryocooler regenerators using an improved single-blow methodCHEN, P.-H; CHANG, Z.-C.International journal of heat and mass transfer. 1997, Vol 40, Num 10, pp 2341-2349, issn 0017-9310Article

Neue Näherungsgleichung zur einheitlichen Berechnung von Wärmeübertragern = New approximate equation for uniform heat exchanger designSPANG, B; ROETZEL, W.Heat and mass transfer. 1995, Vol 30, Num 6, pp 417-422, issn 0947-7411Article

Thermoeconomic considerations in the design and rating of two-phase heat exchangersZUBAIR, S. M.Energy (Oxford). 1998, Vol 23, Num 12, pp 1057-1063, issn 0360-5442Article

Simple new formulae for efficiency and mean temperature difference in heat exchangersMARTIN, H.Chemical engineering & technology. 1990, Vol 13, Num 4, pp 237-241, issn 0930-7516, 5 p.Article

DESIGN OF TRANSFER-LIMITED CATALYTIC INCINERATORSRETALLICK WB.1981; CHEM. ENG. (N.Y.); ISSN 0009-2460; USA; DA. 1981; VOL. 88; NO 1; PP. 123-125; BIBL. 2 REF.Article

DIAGRAMA DE TEMPERATURI SI UNITATEA DE TRANSFER IN SCHIMBUL DE CALDURA = DIAGRAMME DES TEMPERATURES ET UNITE DE TRANSFERT DANS LE TRANSFERT DE CHALEURPECULEA M.1979; REV. CHIM.; ROM; DA. 1979; VOL. 30; NO 2; PP. 159-164; ABS. ENG; BIBL. 11 REF.Article

On the optimum heat exchanger sizing for heat recoverySÖYLEMEZ, M. S.Energy conversion and management. 2000, Vol 41, Num 13, pp 1419-1427, issn 0196-8904Article

An improved model for the single-blow measurement including the non-adiabatic side wall effectCHEN, P.-H; CHANG, Z.-C.International communications in heat and mass transfer. 1996, Vol 23, Num 1, pp 55-68, issn 0735-1933Article

Determining the number of gas-phase and liquid-phase transfer units from point efficiencies in distillationCHEN, G. X; CHUANG, K. T.Industrial & engineering chemistry research. 1994, Vol 33, Num 4, pp 907-913, issn 0888-5885Article

Characterising PCM thermal storage systems using the effectiveness-NTU approachBELUSKO, M; HALAWA, E; BRUNO, F et al.International journal of heat and mass transfer. 2012, Vol 55, Num 13-14, pp 3359-3365, issn 0017-9310, 7 p.Article

Entropy generation on a crossflow heat exchanger including three gas streams with different arrangements and the effect of longitudinal wall conductionYUAN, Ping; KOU, Hong-Sen.Numerical heat transfer. Part A, Applications. 2003, Vol 43, Num 6, pp 619-638, issn 1040-7782, 20 p.Article

Entropy generation on a three-gas crossflow heat exchanger with longitudinal wall conductionPING YUAN; KOU, Hong-Sen.International communications in heat and mass transfer. 2001, Vol 28, Num 6, pp 803-813, issn 0735-1933Article

The comparison of longitudinal wall conduction effect on the crossflow heat exchangers including three fluid streams with different arrangementsPING YUAN; KOU, Hong-Sen.Applied thermal engineering. 2001, Vol 21, Num 18, pp 1891-1907, issn 1359-4311Article

Countercurrent heat exchangers with both fluids subjected to external heatingAMEEL, T. A; HEWAVITHARANA, L.Heat transfer engineering. 1999, Vol 20, Num 3, pp 37-44, issn 0145-7632Article

The effect of longitudinal wall conduction on the crossflow heat exchanger with nonuniform inlet temperaturesKOU, H.-S; PING YUAN.Heat transfer engineering. 1998, Vol 19, Num 2, pp 54-63, issn 0145-7632Article

Performance degradation due to longitudinal heat conduction in very high NTU counterflow heat exchangersPRADEEP NARAYANAN, S; VENKATARATHNAM, G.Cryogenics (Guildford). 1998, Vol 38, Num 9, pp 927-930, issn 0011-2275Article

Global analysis of refrigerative adsorption cycles with thermal regeneration (non-uniform temperature)PONS, M.International journal of refrigeration. 1997, Vol 20, Num 6, pp 411-420, issn 0140-7007Article

On the analysis of conter-flow cooling towersOSTERLE, F.International journal of heat and mass transfer. 1991, Vol 34, Num 4-5, pp 1313-1316, issn 0017-9310Article

Relating transfer units and theoretical stagesVATCHA, S. R.Chemical engineering (New York, NY). 1987, Vol 94, Num 16, pp 101-103, issn 0009-2460Article

ANALYTICAL METHOD FOR CALCULATION OF NUMBER OF TRANSFER UNITSSHARMA SK; GHOSH B.1979; J. INST. ENGRS (INDIA), CHEM. ENGNG DIV.; IND; DA. 1979; VOL. 59; NO 3; PP. 72-74; BIBL. 17 REF.Article