[1] WAND G Q,XU Z C,YU Y L,et al. Performance of a rotating zigzag bed-A new HIGEE[J]. Chemical Engineering and Processing,2008,47(12):2131-2139.
[2] WANG G Q,XU O G.,XU Z C,et al. New HIGEE-rotating zigzag bed and its mass transfer performance[J]. Industrial and Engineering Chemistry Research,2008,47(22):8840-8846.
[3] WANG G Q,XU Z C,JI J B. Progress on higee distillation-introduction to a new device and its industrial applications[J]. Chemical Engineering Research and Design,2011,89(8):1434-1442.
[4] LI Y M,JI J B,XU Z C,WANG G Q,et al. Pressure drop model on rotating zigzag bed as a new high-gravity technology[J]. Industrial and Engineering Chemistry Research,2013,52(12):4638-4649.
[5] LI Y M,LU Y S,WANG G Q,et al. Liquid entrainment and flooding in a rotating zigzag bed[J]. Industrial and Engineering Chemistry Research,2015,54(9):2554-2563.
[6] LI Y M,WANG H J,JI J B,et al. Gas velocity investigations in a HIGEE of rotating zigzag bed[C]//AIChE Annual Meeting,Conference Proceedings,2011,
[7] SUN Y L,ZHANG Y,ZHANG L H,et al. Structure optimization of a rotating zigzag bed via computational fluid dynamics simulation[J]. Industrial and Engineering Chemistry Research,2014,53(35):13764-13772.
[8] LI Y M,LI X H,WANG Y,et al. Distillation in a counter flow concentric-ring rotating bed[J]. Industrial and Engineering Chemistry Research,2014,53(12):4821-4837.
[9] 焦纬洲,刘有智,祈贵生,等. 超重力旋转填料床的有效比表面积[J]. 化学反应工程与工艺,2007,23(4):296-301. JIAO W Z,LIU Y Z,QI G S,et al. Effective interfacial area of high gravity rotating packed bed[J]. Chemical Reaction Engineering and Technology,2007,23(4):296-301.
[10] 陈海辉,简弃非,邓先和. 化学吸收法测定旋转填料床有效相界面积[J]. 华南理工大学学报,1999,27(7):33-37. CHEN H H,JIAN Q F,DENG X H. The measurement of effective gas-liquid interfacial area of rotating bed by chemical absorption method[J]. Journal of South China University of Technology,1999,27(7):33-37.
[11] 姚远,郭锴,肖占敏,等. 旋转填料床内有效传质比表面积的测定与验证试验研究[J]. 现代化工,2013,33(6):130-133. YAO Y,GUO K,XIAO Z M,et al. Measurement and verification of gas-liquid interfacial area in rotating packed beds [J]. Modern Chemical Industry,2013,33(6):130-133.
[12] MUNJAL S,DUDUKOVIC M P,RAMACHANDRAN P. Mass-transfer in rotating packed beds. Ⅱ. Experimental results and comparison with theory and gravity flow [J].Chemical Engineering Science,1989,44(10):2257-2268.
[13] ZHENG X H,CHU G W,KONG D J,et al. Mass transfer intensification in a rotating packed bed with surface-modified nickel foam packing[J]. Chemical Engineering Journal,2016,285(2):236-242
[14] RAJAN S,KUMAR M,ANSARI M J,et al. Limiting gas liquid flows and mass transfer in a novel rotating packed bed [J]. Industrial and Engineering Chemistry Research,2011,50(2):986-997.
[15] GUO K,ZHANG Z Z,LUO H J,et al. An innovative approach of the effective mass transfer area in the rotating packed bed [J]. Industrial and Engineering Chemistry Research,2014,53(10):4052-4058.
[16] LUO Y,CHU G W,ZOU H K,et al. Mass transfer studies in a rotating packed bed with novel rotors:chemisorption of CO2[J]. Industrial and Engineering Chemistry Research,2012,51(26):9164-9172.
[17] LUO Y,CHU G W,SANG L,et al. A two-stage blade-packing rotating packed bed for intensification of continuous distillation[J]. Chinese Journal of Chemical Engineering,2016,24(1):109-115.
[18] TSAI C Y,CHEN Y S. Effective interfacial area and liquid-side mass transfer coefficients in a rotating bed equipped with baffles[J]. Separation and Purification Technology,2015,144(4):139-145.
[19] LIU Y Z,ZHANG F F,GU D,et al. Gas-phase mass transfer characteristics in a counter airflow shear rotating packed bed[J]. Canadian Journal of Chemical Engineering,2016,94(4):771-778.
[20] CHU G W,LUO Y,XING Z Y,et al. Mass-transfer studies in a novel multiliquid-inlet rotating packed bed[J]. Industrial and Engineering Chemistry Research,2014,53(48):18580-18584.
[21] CHU G W,SANG L,DU X K,et al. Studies of CO2 absorption and effective interfacial area in a two-stage rotating packed bed with nickel foam packing [J]. Chemical Engineering and Processing: Process Intensification,2015,90(4):34-40.
[22] DANCKWERTS P V. Gas liquid reactions[M]. Mitchell Litt,New York: Mcgraw-Hill,1970:221.
[23] 汪大翚,贾缨,杜有根,等. 化学法测定旋流塔板气液相界面积的研究[J]. 化学工程,1985(2):30-35. WANG D H,JIA Y,DU Y G. The research method determination of vortex plate gas-liquid boundary area of research [J]. Chemical Engineering,1985(2):30-35.
[24] POHORECHI R. Mass transfer with chemical reaction during gas absorption on a sieve plate[J]. Chemical Engineering Science,1979,31(8): 637-644.
[25] LUO Y,CHU G W,ZOU H K,et al. Gas-liquid effective interfacial area in a rotating packed bed[J]. Industrial and Engineering Chemistry Research,2012,51(50):16320-16325.
[26] YANG K,CHU,G W,ZOU H K,et al. Determination of the effective interfacial area in rotating packed bed[J]. Chem. Eng.,2011,168(3):1377-1382. |