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Author:Hameed B. Mahood , A.O. Sharif ...
Data Source:[J].Energy(IF 3.651), 2014, Vol.67, pp.538-547Elsevier
Abstract:Abstract(#br)An experimental and analytical investigation for the temperature distribution prediction of a three-phase bubble-type direct-contact condenser conducted, using a short Perspex column with 4 cm internal diameter and 70 cm height as a direct contact condenser. Vap...
Author:Hameed B. Mahood , A. N. Campbell ...
Data Source:[J].Heat and Mass Transfer(IF 0.84), 2018, Vol.54 (6), pp.1697-1705Springer
Abstract:Abstract(#br)Energy usage is increasing around the world due to the continued development of technology, and population growth. Solar energy is a promising low-grade energy resource that can be harvested and utilised in different applications, such solar heater systems, whic...
Author:Hameed B. Mahood , Ali Sh. Baqir ...
Data Source:[J].Heat and Mass Transfer(IF 0.84), 2019, Vol.55 (9), pp.2593-2603Springer
Abstract:Abstract(#br)The evaporation of a single n-pentane drop in another warm flowing liquid (water) medium has been studied experimentally. A Perspex column with an internal diameter of 10 cm and height of 150 cm was used throughout the experiments. N-pentane liquid at its satura...
Author:Hameed B. Mahood , Rex B. Thorpe ...
Data Source:[J].Applied Thermal Engineering(IF 2.127), 2015, Vol.87, pp.161-174Elsevier
Abstract:Abstract(#br)The transient characteristics of a three-phase direct contact condenser have been investigated experimentally, utilising a short Perspex column with 48 cm active height and 4 cm internal diameter, and theoretically. Two immiscible fluids, namely pentane vapour w...
Author:Hameed B. Mahood , A.N. Campbell ...
Data Source:[J].Applied Thermal Engineering(IF 2.127), 2016, Vol.95, pp.106-114Elsevier
Abstract:Abstract(#br)The transient temperature distribution and volumetric heat transfer coefficient during the inception of flooding in a three-phase bubble type direct contact condenser have been experimentally investigated. The flooding mechanism and the factors affecting the ons...
Author:Hameed B. Mahood , Alasdair N. Campbell ...
Data Source:[J].Chemical Engineering Science(IF 2.386), 2015, Vol.131, pp.76-83Elsevier
Abstract:Abstract(#br)A semi-analytical model for the drag coefficient of a swarm of two-phase bubbles, condensing in direct contact with an immiscible sub-cooled liquid, has been developed. The analysis used a cellular model configuration, assuming potential (but not inviscid) flow ...
Author:Hameed B. Mahood , Alasdair N. Campbell ...
Data Source:[J].Energy Conversion and Management(IF 2.775), 2015, Vol.106, pp.101-109Elsevier
Abstract:Abstract(#br)Low-grade energy cycles for power generation require efficient heat transfer equipment. Using a three-phase direct contact heat exchanger instead of a surface type exchanger, such as a shell and tube heat exchanger, potentially makes the process more efficient a...
Author:Hameed B. Mahood , Alasdair.N. Campbell ...
Data Source:[J].International Communications in Heat and Mass Transfer(IF 2.208), 2015, Vol.66, pp.180-188Elsevier
Abstract:Abstract(#br)The volumetric heat transfer coefficient of a three-phase direct contact heat transfer condenser has been investigated analytically and experimentally. The experiments were carried out utilising a column of 70 cm in total height and 4 cm inner diameter. The acti...
Author:Hameed B. Mahood , Alasdair N. Campbell
Data Source:[J].Applied Thermal Engineering(IF 2.127), 2016, Vol.103, pp.47-55Elsevier
Abstract:Abstract(#br)The average volumetric heat transfer coefficient in a spray column liquid–liquid–vapour direct contact evaporator has been experimentally investigated. The experiments were carried out utilising a cylindrical Perspex tube of diameter 10 cm and height and 150 cm....
Author:Hameed B. Mahood , Mudher S. Hameed
Data Source:[J].Energy Conversion and Management(IF 2.775), 2016, Vol.126, pp.342-351Elsevier
Abstract:Abstract(#br)Energy recovery from low-grade energy resources requires an efficient thermal conversion system to be economically viable. The use of a liquid-liquid-vapour direct contact heat exchanger in such processes could be suitable due to their high thermal efficiency an...

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