Impact of the fluid flow conditions on the formation rate of carbon dioxide hydrates in a semi-batch stirred tank reactor

被引:28
作者
Douieb, S. [1 ,2 ]
Fradette, L. [1 ]
Bertrand, F. [1 ]
Haut, B. [2 ]
机构
[1] Ecole Polytech, Dept Chem Engn, URPEI, Stn CV, Montreal, PQ H3C 3A7, Canada
[2] Univ Libre Bruxelles, TIPs, B-1050 Brussels, Belgium
基金
加拿大自然科学与工程研究理事会;
关键词
hydrates; mixing; crystal growth (industrial crystallization); mathematical modeling; heat transfer; GAS HYDRATE; MAXBLEND(R) IMPELLER; CLATHRATE HYDRATE; HEAT-TRANSFER; MASS-TRANSFER; NATURAL-GAS; MIXING TIME; CO2; METHANE; SEPARATION;
D O I
10.1002/aic.14952
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
CO2 hydrate formation experiments are performed in a 20L semi-batch stirred tank reactor using three different impellers (a down-pumping pitched blade turbine, a Maxblend, and a Dispersimax) at various rotational speeds to examine the impact of the flow conditions on the CO2 hydrate formation rate. An original mathematical model of the CO2 hydrate formation process that assigns a resistance to each of its constitutive steps is established. For each experimental condition, the formation rate is measured and the rate-limiting step is determined on the basis of the respective values of the resistances. The efficiencies of the three considered impellers are compared and, for each impeller, the influence of the rotational speed on the rate-limiting step is discussed. For instance, it is shown that a formation rate limitation due to heat transfer can occur at the relatively small scale used to perform our experiments. (c) 2015 American Institute of Chemical Engineers
引用
收藏
页码:4387 / 4401
页数:15
相关论文
共 63 条
[1]   Separation of CO2 from flue gas:: A review [J].
Aaron, D ;
Tsouris, C .
SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (1-3) :321-348
[2]  
[Anonymous], 2007, TRANSPORT PHENOMENA
[3]  
[Anonymous], 2016, CARBON DIOXIDE CAPTU
[4]   Effect of low off-bottom impeller clearance on the minimum agitation speed for complete suspension of solids in stirred tanks [J].
Armenante, PM ;
Nagamine, EU .
CHEMICAL ENGINEERING SCIENCE, 1998, 53 (09) :1757-1775
[5]   A review of the hydrate based gas separation (HBGS) process for carbon dioxide pre-combustion capture [J].
Babu, Ponnivalavan ;
Linga, Praveen ;
Kumar, Rajnish ;
Englezos, Peter .
ENERGY, 2015, 85 :261-279
[6]  
Beenackers AACM, 2001, CHEM ENG SCI, V48, P3109
[7]   Reaction Rate Constant of CO2 Hydrate Formation and Verification of Old Premises Pertaining to Hydrate Growth Kinetics [J].
Bergeron, Sebastien ;
Servio, Phillip .
AICHE JOURNAL, 2008, 54 (11) :2964-2970
[8]   CO2 and CH4 mole fraction measurements during hydrate growth in a semi-batch stirred tank reactor and its significance to kinetic modeling [J].
Bergeron, Sebastien ;
Servio, Phillip .
FLUID PHASE EQUILIBRIA, 2009, 276 (02) :150-155
[9]   Air entrainment in baffled stirred tanks [J].
Bhattacharya, S. ;
Hebert, D. ;
Kresta, S. M. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2007, 85 (A5) :654-664
[10]   Formation and decomposition of gas hydrates [J].
Bishnoi, PR ;
Natarajan, V .
FLUID PHASE EQUILIBRIA, 1996, 117 (1-2) :168-177