A comparison between the packed and coated finned tube for adsorption system using aluminium fumarate: Numerical study

被引:19
作者
Albaik, Ibrahim [1 ]
Al-Dadah, Raya [1 ]
Mahmoud, Saad [1 ]
Almesfer, Mohammed K. [2 ]
Ismail, Mohamed A. [2 ,3 ]
机构
[1] Univ Birmingham, Dept Mech Engn, Birmingham B15 2TT, W Midlands, England
[2] King Khalid Univ, Dept Chem Engn, Coll Engn, Abha 61411, Saudi Arabia
[3] Natl Ctr Res, Inst Engn Res & Mat Technol, Khartoum 2424, Sudan
基金
英国工程与自然科学研究理事会;
关键词
Specific cooling power; Specific water daily production; Adsorption system; Segregated solution approach; Aluminium Fumarate; HEAT-EXCHANGER; ADSORBENT BED; CONTACT RESISTANCE; MASS-TRANSFER; PERFORMANCE; PARAMETERS; DESIGN; COATINGS; TRANSFORMATION; BEHAVIOR;
D O I
10.1016/j.tsep.2021.100859
中图分类号
O414.1 [热力学];
学科分类号
摘要
A transient numerical model has been developed using the segregated solution approach to study the performance of packed and coated finned tubes in adsorber beds for desalination and cooling applications. Published isotherms and kinetics of the Aluminium Fumarate in granular packed and powder-coated forms are used in the model to investigate the adsorber bed design. The fin configurations (fin spacing and fin height) were investigated at different operating conditions to obtain the optimum geometrical design for the packed and coated adsorber beds in terms of the specific daily water production (SDWP) and the specific cooling power (SCP). A comprehensive comparison of the SDWP and SCP was carried out at different fin height and coated thickness. The results showed that the maximum SCP and SDWP for the packed bed are 300 W/kg and 12.5 L/day/kg, while they are 825 W/kg and 34.2 L/day/kg respectively for the coated bed. The optimum design of the heat exchanger was found using the coated finned tube with an adsorbent material thickness of 0.3 mm.
引用
收藏
页数:14
相关论文
共 51 条
[1]   Non-equilibrium numerical modelling of finned tube heat exchanger for adsorption desalination/cooling system using segregated solution approach [J].
Albaik, Ibrahim ;
Al-Dadah, Raya ;
Mahmoud, Saad ;
Solmaz, Ismail .
APPLIED THERMAL ENGINEERING, 2021, 183
[2]   Characterization of transport limitations in SAPO-34 adsorbent coatings for adsorption heat pumps [J].
Ammann, Jens ;
Michel, Bruno ;
Ruch, Patrick W. .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2019, 129 :18-27
[3]  
[Anonymous], 1928, Z PHYS CHEM, P132
[4]   Synthesis of SAPO-34/graphite composites for low temperature heat adsorption pumps [J].
Bonaccorsi, L. ;
Calabrese, L. ;
Proverbio, E. ;
Frazzica, A. ;
Freni, A. ;
Restuccia, G. ;
Piperopoulos, E. ;
Milone, C. .
JOURNAL OF ENERGY CHEMISTRY, 2013, 22 (02) :245-250
[5]   The effect of fin design parameters on the heat transfer enhancement in the adsorbent bed of a thermal wave cycle [J].
Caglar, Ahmet .
APPLIED THERMAL ENGINEERING, 2016, 104 :386-393
[6]   Effect of process parameters on behaviour of zeolite coatings obtained by hydrothermal direct synthesis on aluminium support [J].
Calabrese, L. ;
Bonaccorsi, L. ;
Di Pietro, D. ;
Proverbio, E. .
CERAMICS INTERNATIONAL, 2014, 40 (08) :12837-12845
[8]   Recent Developments in Coating Technologies for Adsorption Heat Pumps: A Review [J].
Capri, Angela ;
Frazzica, Andrea ;
Calabrese, Luigi .
COATINGS, 2020, 10 (09)
[9]   Water vapor adsorption kinetics on small and full scale zeolite coated adsorbers; A comparison [J].
Dawoud, Belal .
APPLIED THERMAL ENGINEERING, 2013, 50 (02) :1645-1651
[10]   Effects of porosity on heat and mass transfer in a granular adsorbent bed [J].
Demir, Hasan ;
Mobedi, Moghtada ;
Ulku, Semra .
INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2009, 36 (04) :372-377