Heat transfer with single- and dual-gas distribution in a pressurised bubble column

被引:2
作者
Bae, Keon [1 ]
Kim, Jun Young [1 ,2 ]
Go, Kang Seok [3 ,4 ]
Nho, Nam Sun [3 ,4 ]
Kim, Dongjae [5 ]
Bae, Jong Wook [1 ]
Lee, Dong Hyun [1 ]
机构
[1] Sungkyunkwan Univ SKKU, Sch Chem Engn, 2066 Seobu Ro, Suwon 16419, Gyeonggi Do, South Korea
[2] Sungkyunkwan Univ SKKU, Inst Convergent Chem Engn & Technol, Suwon 16419, Gyeonggi Do, South Korea
[3] Ctr Convergent Chem Proc, 141 Gajeong Ro, Daejeon 34114, South Korea
[4] Korea Inst Energy Res, Climate Change Res Div, 152 Gajeong Ro, Daejeon 34129, South Korea
[5] Seoul Natl Univ, Sch Chem & Biol Engn, Seoul 08826, South Korea
关键词
Pressurised bubble column; Dual distribution; Microbubbles; Kinetic energy; Low surface tension liquid; MASS-TRANSFER; SCALE-UP; HOLDUP; HYDRODYNAMICS;
D O I
10.1016/j.ces.2022.118264
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effects of the heat transfer coefficient variance on microbubble formation in a pressurised bubble column and its variance in the dual gas distribution were investigated. The tests were performed with a cylindrical column with an inner diameter of 0.097 m and a height of 1.8 m with air-kerosene media. The heat transfer coefficient was measured using various distributors with different numbers of orifices, and its size was fixed. For an opening fraction of 0.223 %, the heat-transfer coefficient increased with increasing superficial gas velocity (Ug) under all pressure conditions in the tested range. The amount of microbubble generation increased with an increase in pressure and Ug when the opening fraction decreased. To analyse the effect of the kinetic energy rate at the orifice on the number of microbubbles, the gas holdup was measured according to the increase in Ug and system pressure. When the total kinetic energy rate was equal to or higher than 1 J/s, the gas holdup rapidly increased owing to microbubble generation. To increase the heat transfer coefficient in the presence of microbubbles, a dual gas distribution was applied by inserting a single nozzle with different orifice hole diameters (1.7, 2.0, 2.5, and 3.46 mm). In this system, the heat transfer coefficient increased by approximately 25 % compared with the dispersion in a single distributor.
引用
收藏
页数:11
相关论文
共 32 条
[1]   Bubble/micro-bubble regime transition in a pressurized bubble column of a low surface tension liquid system [J].
Bae, Keon ;
Kim, Jun Young ;
Go, Kang Seok ;
Nho, Nam Sun ;
Kim, Dongjae ;
Bae, Jong Wook ;
Lee, Dong Hyun .
CHEMICAL ENGINEERING SCIENCE, 2022, 249
[2]   Effect of distributor type on microbubble dispersion in a pressurized bubble column [J].
Bae, Keon ;
Kim, Jun Young ;
Go, Kang Seok ;
Nho, Nam Sun ;
Kim, DongJae ;
Bae, Jong Wook ;
Lee, DongHyun .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2021, 174 :188-198
[3]   Bubble characteristics in pressurized bubble column associated with micro-bubble dispersion [J].
Bae, Keon ;
Go, Gang Seok ;
Noh, Nam Seon ;
Lim, Young-Il ;
Bae, JongWook ;
Lee, Dong Hyun .
CHEMICAL ENGINEERING JOURNAL, 2020, 386
[4]   HEAT-TRANSFER IN 3-PHASE FLUIDIZED-BEDS [J].
BAKER, CGJ ;
ARMSTRONG, ER ;
BERGOUGNOU, MA .
POWDER TECHNOLOGY, 1978, 21 (02) :195-204
[5]   Hydrodynamics of air-kerosene bubble column under elevated pressure in homogeneous flow regime [J].
Bay Van Tran ;
Ngo, Son Ich ;
Lim, Young-Il ;
Bae, Keon ;
Lee, Dong Hyun ;
Go, Kang-Seok ;
Nam-Sun Nho .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2021, 33 :190-202
[6]   Experimental investigation on the influence of ethanol on bubble column hydrodynamics [J].
Besagni, Giorgio ;
Inzoli, Fabio ;
De Guido, Giorgia ;
Pellegrini, Laura Annamaria .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2016, 112 :1-15
[7]   Dynamic characteristics of heat transfer coefficient in pressurized bubble columns with viscous liquid medium [J].
Cho, YJ ;
Woo, KJ ;
Kang, Y ;
Kim, SD .
CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2002, 41 (08) :699-706
[9]   ON THE MECHANISM OF HEAT-TRANSFER IN BUBBLE COLUMN REACTORS [J].
DECKWER, WD .
CHEMICAL ENGINEERING SCIENCE, 1980, 35 (06) :1341-1346
[10]   HYDRODYNAMIC PROPERTIES OF THE FISCHER-TROPSCH SLURRY PROCESS [J].
DECKWER, WD ;
LOUISI, Y ;
ZAIDI, A ;
RALEK, M .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (04) :699-708