THE TRANSITION BETWEEN TRICKLE FLOW AND PULSE FLOW IN A COCURRENT GAS-LIQUID TRICKLE-BED REACTOR AT ELEVATED PRESSURES

被引:57
作者
WAMMES, WJA [1 ]
MECHIELSEN, SJ [1 ]
WESTERTERP, KR [1 ]
机构
[1] TWENTE UNIV TECHNOL,DEPT CHEM ENGN,CHEM REACT ENGN LABS,POB 217,7500 AE ENSCHEDE,NETHERLANDS
关键词
D O I
10.1016/0009-2509(90)80060-R
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of reactor pressure in the range of 0.2-2.0 MPa on the transition between the trickle-flow and the pulse-flow regime has been investigated for the non-foaming water-nitrogen and aqueous 40% ethyleneglycol-nitrogen systems. Most models and flow charts which are all based on atmospheric experiments were able to describe the transition experiments performed at 0.2 MPa reasonably well. However, this is not so at elevated pressures. For both gas-liquid systems it is found that at a constant superficial gas velocity and higher reactor pressures the transition of trickle flow to pulse flow occurs at a relative higher liquid throughput. In the pressure range of 2.5-7.0 MPa the pulse-flow regime could not be obtained for throughputs up to 1.7 cm/s superficial liquid velocity. An explanation for this effect is given based on the dynamic liquid hold-up and pressure drop data determined at the flow regime transition. Finally an empirical equation is proposed, relating the parameters governing the flow regime transition and describing the hydrodynamic conditions at the transition between trickle flow and pulse flow. © 1990.
引用
收藏
页码:3149 / 3158
页数:10
相关论文
共 24 条
[1]  
[Anonymous], 1954, OIL GAS J, DOI DOI 10.2118/323-G
[2]   TRANSITION TO PULSING FLOW, HOLDUP AND PRESSURE-DROP IN PACKED-COLUMNS WITH CO-CURRENT GAS-LIQUID DOWNFLOW [J].
BLOK, JR ;
VARKEVISSER, J ;
DRINKENBURG, AAH .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (05) :687-699
[3]   SOME LIQUID HOLDUP EXPERIMENTAL-DATA IN TRICKLE-BED REACTORS FOR FOAMING AND NONFOAMING HYDROCARBONS [J].
CHARPENTIER, JC ;
FAVIER, M .
AICHE JOURNAL, 1975, 21 (06) :1213-1218
[4]   COCURRENT DOWNFLOW OF AIR AND WATER IN A TWO-DIMENSIONAL PACKED-COLUMN [J].
CHRISTENSEN, G ;
MCGOVERN, SJ ;
SUNDARESAN, S .
AICHE JOURNAL, 1986, 32 (10) :1677-1689
[5]   INTERFACIAL AREA AND BOUNDARY OF HYDRODYNAMIC FLOW REGION IN PACKED-COLUMN WITH COCURRENT DOWNWARD FLOW [J].
FUKUSHIMA, S ;
KUSAKA, K .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1977, 10 (06) :461-467
[6]   HYDRODYNAMICS AND SOLID-LIQUID CONTACTING EFFECTIVENESS IN TRICKLE-BED REACTORS [J].
GIANETTO, A ;
BALDI, G ;
SPECCHIA, V ;
SICARDI, S .
AICHE JOURNAL, 1978, 24 (06) :1087-1104
[7]   TRICKLE-BED REACTORS - A REVIEW [J].
HERSKOWITZ, M ;
SMITH, JM .
AICHE JOURNAL, 1983, 29 (01) :1-18
[8]   THE HYSTERETIC BEHAVIOR OF PRESSURE-DROP AND LIQUID HOLDUP IN TRICKLE BEDS [J].
LEVEC, J ;
GROSSER, K ;
CARBONELL, RG .
AICHE JOURNAL, 1988, 34 (06) :1027-1030
[10]  
Perry R., 1984, PERRYS CHEM ENG HDB, Vsixth