Experimental Investigation of an Intensified Heat Transfer Adsorption Bed (IHTAB) Reactor Prototype

被引:21
|
作者
Grabowska, Karolina [1 ]
Zylka, Anna [1 ]
Kulakowska, Anna [1 ]
Skrobek, Dorian [1 ]
Krzywanski, Jaroslaw [1 ]
Sosnowski, Marcin [1 ]
Ciesielska, Katarzyna [1 ]
Nowak, Wojciech [2 ]
机构
[1] Jan Dlugosz Univ Czestochowa, Fac Sci & Technol, Armii Krajowej 13-15, PL-42200 Czestochowa, Poland
[2] AGH Univ Sci & Technol, Fac Energy & Fuels, Mickiewicza 30 St, PL-30059 Krakow, Poland
关键词
silica gel; porous media; adsorption bed; fluidized bed; low-pressure sorption; heat transfer; FLUIDIZED-BEDS; SILICA-GEL; ADSORBENT; CHILLER; PERFORMANCE; CONFIGURATION; CONSTRUCTION; TEMPERATURE; IMPROVEMENT; SIMULATION;
D O I
10.3390/ma14133520
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The first experience in the operation of intensified heat transfer adsorption bed reactor designed for low-pressure adsorption processes is presented in this paper. This work aims to assess the possibility of fluidizing the porous media bed induced by the pressure difference between the evaporator and the adsorption reactor. The conducted experimental research allowed indicating the type of silica gel recommended to use in fluidized beds of adsorption chiller. The fixed bed of silica gel was observed for the lower pressure differences, while fluidization appeared in the case of the pressure difference between the evaporator and the adsorption chamber higher than 1000 Pa. The most significant differences in the adsorption process between the fixed bed and the fluidized bed are revealed in the changes of sorbent temperatures. The silica gel bed was fluidized with water vapor generated in the evaporator.
引用
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页数:13
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