id	author	title	date	pages	extension	mime	words	sentence	flesch	summary	cache	txt
fumecheng-66	Vukić, Mića V.; Vučković, Goran; Živković, Predrag; Stevanović, Žarko; Tomić, Mladen	3D NUMERICAL SIMULATIONS OF THE THERMAL PROCESSES IN THE SHELL AND TUBE HEAT EXCHANGER	2014	12	.pdf	application/pdf	3611	144	54	Determination of the extra source terms of the distributed resistance and volume heat transfer coefficients has been made by linearization technique of the special source terms. 4 Variation of heating fluid temperature along the STHE’s axis Fig. 4 shows the comparison between the experimental and the numerical values of the heating fluid temperature by using the local volume overall heat transfer coefficient in the shell axis for the case of three segmental baffle Np = 3, with baffle cut of BC = 22%, with leakage flow between the baffle and the shell, for the heating fluid flow rate of Vt = 3m 3 /h and initial temperature of t1t = 60°C. Fig.	cache/fumecheng-66.pdf	txt/fumecheng-66.txt