Heat transfer to medium and highly viscous non-Newtonian fluids in the fin-and -tube heat exchanger under the conditions of Re<2
270 was studied. The correlation of heat transfer was also presented. The modified Wilsons method was used for processing the experimental data. In order to lessen the effect of flow maldistribution on the experimental results
a measurement method was put forward to study the flow distribution in the heat exchanger by determining the temperatures of fluids.
Controlled synthesis of Bi2MoO6/MoO3 composite fibers via in-situ hydrothermal method and their high-efficiency photocatalytic hydrogen production performance
Exothermic characteristics of energy carrier for calcium looping thermo-chemical energy storage
Identification of gas-liquid two-phase flow patterns in a riser based on recursive characteristics and CNN
A hybrid modeling and optimization strategy for sequential simulated moving bed
Advantages and risks of swirling cooling granulation towers