Skip navigation

DSpace

機構典藏 DSpace 系統致力於保存各式數位資料(如:文字、圖片、PDF)並使其易於取用。

點此認識 DSpace
DSpace logo
English
中文
  • 瀏覽論文
    • 校院系所
    • 出版年
    • 作者
    • 標題
    • 關鍵字
    • 指導教授
  • 搜尋 TDR
  • 授權 Q&A
    • 我的頁面
    • 接受 E-mail 通知
    • 編輯個人資料
  1. NTU Theses and Dissertations Repository
  2. 工學院
  3. 化學工程學系
請用此 Handle URI 來引用此文件: http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/61349
完整後設資料紀錄
DC 欄位值語言
dc.contributor.advisor劉懷勝(Hwai-Shen Liu)
dc.contributor.authorPei-Sheng Tangen
dc.contributor.author唐沛陞zh_TW
dc.date.accessioned2021-06-16T13:01:26Z-
dc.date.available2015-08-22
dc.date.copyright2013-08-22
dc.date.issued2013
dc.date.submitted2013-08-07
dc.identifier.citationAdam, J.,Lindblad, N.,Hendricks, C., (1968) The collision, coalescence, and disruption of water droplets. Journal of Applied Physics. 39 (11) 5173-5180.
Ashgriz, N.,Givi, P., (1989) Coalescence efficiencies of fuel droplets in binary collisions. International Communications in Heat and Mass Transfer. 16 (1) 11-20.
Ashgriz, N.,Poo, J., (1990) Coalescence and separation in binary collisions of liquid drops. Journal of Fluid Mechanics. 221 (1) 183-204.
Bruining, W.,Joosten, G.,Beenackers, A.,Hofman, H., (1986) Enhancement of gas-liquid mass transfer by a dispersed second liquid phae. Chem. Eng. Sci. 41 (7) 1873-1877.
Burns, J. R.,Jamil, J. N.,Ramshaw, C., (2000) Process intensification: operating characteristics of rotating packed beds - determination of liquid hold-up for a high-voidage structured packing. Chem. Eng. Sci. 55 (13) 2401-2415.
Burns, J. R.,Ramshaw, C., (1996) Process intensification: Visual study of liquid maldistribution in rotating packed beds. Chem. Eng. Sci. 51 (8) 1347-1352.
Cents, A.,Brilman, D.,Versteeg, G., (2001) Gas absorption in an agitated gas-liquid-liquid system. Chem. Eng. Sci. 56 (3) 1075-1083.
Chandra, A.,Goswami, P.,Rao, D., (2005) Characteristics of flow in a rotating packed bed (HIGEE) with split packing. Ind. Eng. Chem. Res. 44 (11) 4051-4060.
Chang, C. C.,Chiu, C. Y.,Chang, C. Y.,Chang, C. F.,Chen, Y. H.,Ji, D. R.,Yu, Y. H.,Chiang, P. C., (2009) Combined photolysis and catalytic ozonation of dimethyl phthalate in a high-gravity rotating packed bed. J. Hazard. Mater. 161 (1) 287-293.
Chang, C. F.,Lee, S. C., (2012) Adsorption behavior of pesticide methomyl on activated carbon in a high gravity rotating packed bed reactor. Water Res. 46 (9) 2869-2880.
Chen, J.,Li, Y.,Wang, Y.,Yun, J.,Cao, D., (2004) Preparation and characterization of zinc sulfide nanoparticles under high-gravity environment. Materials research bulletin. 39 (2) 185-194.
Chen, J.,Shao, L.,Zhang, C.,Chen, J.,Chu, G., (2003) Preparation of TiO 2 nanoparticles by a rotating packed bed reactor. Journal of materials science letters. 22 (6) 437-439.
Chen, J. F.,Gao, H.,Zou, H. K.,Chu, G. W.,Zhang, L.,Shao, L.,Xiang, Y.,Wu, Y. X., (2010) Cationic Polymerization in Rotating Packed Bed Reactor: Experimental and Modeling. AIChE J. 56 (4) 1053-1062.
Chen, J. F.,Wang, Y. H.,Guo, F.,Wang, X. M.,Zheng, C., (2000) Synthesis of nanoparticles with novel technology: high-gravity reactive precipitation. Ind. Eng. Chem. Res. 39 (4) 948-954.
Chen, J. F.,Zhou, M. Y.,Shao, L.,Wang, Y. Y.,Yun, J.,Chew, N. Y. K.,Chan, H. K., (2004) Feasibility of preparing nanodrugs by high-gravity reactive precipitation. Int. J. Pharm. 269 (1) 267-274.
Chen, Y. H.,Huang, Y. H.,Lin, R. H.,Shang, N. C., (2010) A continuous-flow biodiesel production process using a rotating packed bed. Bioresour. Technol. 101 (2) 668-673.
Chen, Y. H.,Huang, Y. H.,Lin, R. H.,Shang, N. C.,Chang, C. Y.,Chang, C. C.,Chiang, P. C.,Hu, C. Y., (2011) Biodiesel production in a rotating packed bed using K/gamma-Al2O3 solid catalyst. J. Taiwan Inst. Chem. Eng. 42 (6) 937-944.
Chen, Y. S., (2011) Correlations of Mass Transfer Coefficients in a Rotating Packed Bed. Ind. Eng. Chem. Res.
Chen, Y. S.,Hsu, Y. C.,Lin, C. C.,Tai, C. Y. D.,Liu, H. S., (2008) Volatile organic compounds absorption in a cross-flow rotating packed bed. Environ. Sci. Technol. 42 (7) 2631-2636.
Chen, Y. S.,Lin, C. C.,Liu, H. S., (2005) Mass transfer in a rotating packed bed with various radii of the bed. Ind. Eng. Chem. Res. 44 (20) 7868-7875.
Chen, Y. S.,Lin, C. C.,Liu, H. S., (2005) Mass transfer in a rotating packed bed with viscous newtonian and non-Newtonian fluids. Ind. Eng. Chem. Res. 44 (4) 1043-1051.
Chen, Y. S.,Lin, F. Y.,Lin, C. C.,Tai, C. Y. D.,Liu, H. S., (2006) Packing characteristics for mass transfer in a rotating packed bed. Ind. Eng. Chem. Res. 45 (20) 6846-6853.
Chen, Y. S.,Liu, H. S., (2002) Absorption of VOCs in a rotating packed bed. Ind. Eng. Chem. Res. 41 (6) 1583-1588.
Chen, Y. S.,Liu, H. S.,Lin, C. C.,Liu, W. T., (2004) Micromixing in a rotating packed bed. Journal of Chemical Engineering of Japan. 37 (9) 1122-1128.
Chen, Y. S.,Tai, C. Y. D.,Chang, M. H.,Liu, H. S., (2006) Characteristics of micromixing in a rotating packed bed. J. Chin. Inst. Chem. Eng. 37 (1) 63-69.
Chiang, C. Y.,Chen, Y. S.,Liang, M. S.,Lin, F. Y.,Tai, C. Y. D.,Liu, H. S., (2009) Absorption of ethanol into water and glycerol/water solution in a rotating packed bed. J. Taiwan Inst. Chem. Eng. 40 (4) 418-423.
Chiang, C. Y.,Liu, Y. Y.,Chen, Y. S.,Liu, H. S., (2012) Absorption of Hydrophobic Volatile Organic Compounds by a Rotating Packed Bed. Ind. Eng. Chem. Res. 51 (27) 9441-9445.
Chu, G. W.,Gao, X.,Luo, Y.,Zou, H. K.,Shao, L.,Chen, J. F., (2013) Distillation studies in a two-stage counter-current rotating packed bed. Separation and Purification Technology. 102 62-66.
Dagaonkar, M.,Heeres, H.,Beenackers, A.,Pangarkar, V., (2003) The application of fine TiO2 particles for enhanced gas absorption. Chem. Eng. J. 92 (1-3) 151-159.
Das, A.,Bhowal, A.,Datta, S., (2008) Continuous biosorption in rotating packed-bed contactor. Ind. Eng. Chem. Res. 47 (12) 4230-4235.
Das, T.,Bandopadhyay, A.,Parthasarathy, R.,Kumar, R., (1985) Gas--liquid interfacial area in stirred vessels: The effect of an immiscible liquid phase. Chem. Eng. Sci. 40 (2) 209-214.
Demmink, J.,Mehra, A.,Beenackers, A., (1998) Gas absorption in the presence of particles showing interfacial affinity:: case of fine sulfur precipitates. Chem. Eng. Sci. 53 (16) 2885-2902.
Dumont, E.,Andres, Y., (2012) Styrene absorption in water/silicone oil mixtures. Chem. Eng. J. 200 81-90.
Dumont, E.,Andres, Y.,Le Cloirec, P., (2006) Mass transfer coefficients of styrene and oxygen into silicone oil emulsions in a bubble reactor. Chem. Eng. Sci. 61 (17) 5612-5619.
Dumont, E.,Darracq, G.,Couvert, A.,Couriol, C.,Amrane, A.,Thomas, D.,Andres, Y.,Le Cloirec, P., (2010) Determination of partition coefficients of three volatile organic compounds (dimethylsulphide, dimethyldisulphide and toluene) in water/silicone oil mixtures. Chem. Eng. J. 162 (3) 927-934.
Dumont, E.,Delmas, H., (2003) Mass transfer enhancement of gas absorption in oil-in-water systems: a review. Chem. Eng. Process. 42 (6) 419-438.
Gudena, K.,Rangaiah, G. P.,Lakshminarayanan, S., (2012) Optimal Design of a Rotating Packed Bed for VOC Stripping from Contaminated Groundwater. Ind. Eng. Chem. Res. 51 (2) 835-847.
Guo, F.,Zheng, C.,Guo, K.,Feng, Y. D.,Gardner, N. C., (1997) Hydrodynamics and mass transfer in crossflow rotating packed bed. Chem. Eng. Sci. 52 (21-22) 3853-3859.
Guo, K.,Guo, F.,Feng, Y.,Chen, J.,Zheng, C.,Gardner, N. C., (2000) Synchronous visual and RTD study on liquid flow in rotating packed-bed contactor. Chem. Eng. Sci. 55 (9) 1699-1706.
Jiang, Y.,Umemura, A.,Law, C., (1992) An experimental investigation on the collision behaviour of hydrocarbon droplets. Journal of Fluid Mechanics. 234 (-1) 171-190.
Jiao, W. Z.,Liu, Y. Z.,Qi, G. S., (2010) Gas Pressure Drop and Mass Transfer Characteristics in a Cross-flow Rotating Packed Bed with Porous Plate Packing. Ind. Eng. Chem. Res. 49 (8) 3732-3740.
Jiao, W. Z.,Liu, Y. Z.,Qi, G. S., (2012) Micromixing Efficiency of Viscous Media in Novel Impinging Stream-Rotating Packed Bed Reactor. Ind. Eng. Chem. Res. 51 (20) 7113-7118.
Kelleher, T.,James, R., (1996) Distillation studies in a high-gravity contactor. Ind. Eng. Chem. Res. 35 (12) 4646-4655.
Keyvani, M., (1989) OPERATING CHARACTERISTICS OF ROTATING BEDS. Chem. Eng. Prog. 85 (9) 48-52.
Ku, Y.,Ji, Y. S.,Chen, H. W., (2008) Ozonation of o-cresol in aqueous solutions using a rotating packed-bed reactor. Water Environ. Res. 80 (1) 41-46.
Kumar, M. P.,Rao, D. P., (1990) STUDIES ON A HIGH-GRAVITY GAS-LIQUID CONTACTOR. Ind. Eng. Chem. Res. 29 (5) 917-920.
Lalanne, F.,Malhautier, L.,Roux, J. C.,Fanlo, J. L., (2008) Absorption of a mixture of volatile organic compounds (VOCs) in aqueous solutions of soluble cutting oil. Bioresour. Technol. 99 (6) 1699-1707.
Lashkarbolooki, M.,Vaferi, B.,Mowla, D., (2012) Using Artificial Neural Network to Predict the Pressure Drop in a Rotating Packed Bed. Sep. Sci. Technol. 47 (16) 2450-2459.
Lekhal, A.,Chaudhari, R.,Wilhelm, A.,Delmas, H., (1997) Gas-liquid mass transfer in gas-liquid-liquid dispersions. Chem. Eng. Sci. 52 (21-22) 4069-4077.
Li, Y.,Ji, J.,Yu, Y.,Xu, Z.,Li, X., (2010) Hydrodynamic Behavior in a Rotating Zigzag Bed. Chinese Journal of Chemical Engineering. 18 (1) 34-38.
Li, Y. M.,Ji, J. B.,Xu, Z. C.,Wang, G. Q.,Li, X. H.,Liu, X. J., (2013) Pressure Drop Model on Rotating Zigzag Bed as a New High-Gravity Technology. Ind. Eng. Chem. Res. 52 (12) 4638-4649.
Lin, C. C.,Chao, C. Y.,Liu, M. Y.,Lee, Y. L., (2009) Feasibility of ozone absorption by H2O2 solution in rotating packed beds. J. Hazard. Mater. 167 (1-3) 1014-1020.
Lin, C. C.,Chen, B. C., (2010) Carbon Dioxide Absorption in a Cross-Flow Rotating Packed Bed. Chemical Engineering Research and Design. 89 (9) 1722-1729.
Lin, C. C.,Chen, B. C.,Chen, Y. S.,Hsu, S. K., (2008) Feasibility of a cross-flow rotating packed bed in removing carbon dioxide from gaseous streams. Separation and Purification Technology. 62 (3) 507-512.
Lin, C. C.,Chen, Y. S.,Liu, H. S., (2000) Prediction of liquid holdup in countercurrent-flow rotating packed bed. Chemical Engineering Research and Design. 78 (3) 397-403.
Lin, C. C.,Chen, Y. S.,Liu, H. S., (2004) Adsorption of dodecane from water in a rotating packed bed. J. Chin. Inst. Chem. Eng. 35 (5) 531.
Lin, C. C.,Chiang, Y. J., (2012) Feasibility of using a rotating packed bed in preparing coupled ZnO/SnO2 photocatalysts. J. Ind. Eng. Chem. 18 (4) 1233-1236.
Lin, C. C.,Chien, K. S., (2008) Mass-transfer performance of rotating packed beds equipped with blade packings in VOCs absorption into water. Separation and Purification Technology. 63 (1) 138-144.
Lin, C. C.,Ho, T. J.,Liu, W. T., (2002) Distillation in a rotating packed bed. Journal of chemical engineering of Japan. 35 (12) 1298-1304.
Lin, C. C.,Jian, G. S., (2007) Characteristics of a rotating packed bed equipped with blade packings. Separation and Purification Technology. 54 (1) 51-60.
Lin, C. C.,Liu, H. S., (2000) Adsorption in a centrifugal field: Basic dye adsorption by activated carbon. Ind. Eng. Chem. Res. 39 (1) 161-167.
Lin, C. C.,Liu, W. T., (2003) Ozone oxidation in a rotating packed bed. J. Chem. Technol. Biotechnol. 78 (2-3) 138-141.
Lin, C. C.,Liu, W. T., (2007) Mass transfer characteristics of a high-voltage rotating packed bed. J. Ind. Eng. Chem. 13 (1) 71-78.
Lin, C. C.,Liu, W. T.,Tan, C. S., (2003) Removal of carbon dioxide by absorption in a rotating packed bed. Ind. Eng. Chem. Res. 42 (11) 2381-2386.
Lin, C. C.,Su, Y. R., (2008) Performance of rotating packed beds in removing ozone from gaseous streams. Separation and Purification Technology. 61 (Compendex) 311-316.
Lin, C. C.,Su, Y. R., (2008) Performance of rotating packed beds in removing ozone from gaseous streams. Separation and Purification Technology. 61 (3) 311-316.
Lin, C. C.,Wei, T. Y.,Hsu, S. K.,Liu, W. T., (2006) Performance of a pilot-scale cross-flow rotating packed bed in removing VOCs from waste gas streams. Separation and Purification Technology. 52 (2) 274-279.
Lin, C. C.,Wei, T. Y.,Liu, W. T.,Shen, K. P., (2004) Removal of VOCs from gaseous streams in a high-voidage rotating packed bed. Journal of chemical engineering of Japan. 37 (12) 1471-1477.
Littel, R.,Versteeg, G.,Van Swaaij, W., (1994) Physical absorption of CO2 and propene into toluene/water emulsions. Aiche J. 40 (10) 1629-1638.
Liu, H. S.,Lin, C. C.,Wu, S. C.,Hsu, H. W., (1996) Characteristics of a rotating packed bed. Ind. Eng. Chem. Res. 35 (10) 3590-3596.
Luo, Y.,Chu, G. W.,Zou, H. K.,Xiang, Y.,Shao, L.,Chen, J. F., (2012) Characteristics of a two-stage counter-current rotating packed bed for continuous distillation. Chem. Eng. Process. 52 55-62.
Mondal, A.,Pramanik, A.,Bhowal, A.,Datta, S., (2012) Distillation studies in rotating packed bed with split packing. Chem. Eng. Res. Des. 90 (4) 453-457.
Munjal, S.,Dudukovic, M. P.,Ramachandran, P., (1989) Mass-transfer in rotating packed beds--II. Experimental results and comparison with theory and gravity flow. Chem. Eng. Sci. 44 (10) 2257-2268.
Nagy, E., (1995) Three-phase mass transfer: one-dimensional heterogeneous model. Chem. Eng. Sci. 50 (5) 827-836.
Nascimento, J. V. S.,Ravagnani, T. M. K.,Pereira, J., (2009) EXPERIMENTAL STUDY OF A ROTATING PACKED BED DISTILLATION COLUMN. Braz. J. Chem. Eng. 26 (1) 219-226.
Ng, C. M.,Chen, P. C.,Manickam, S., (2012) Green High-Gravitational Synthesis of Silver Nanoparticles Using a Rotating Packed Bed Reactor (RPBR). Ind. Eng. Chem. Res. 51 (15) 5375-5381.
Qian, J.,Law, C., (1997) Regimes of coalescence and separation in droplet collision. Journal of Fluid Mechanics. 331 (-1) 59-80.
Qian, Z.,Xu, L. B.,Li, Z. H.,Li, H.,Guo, K., (2010) Selective Absorption of H2S from a Gas Mixture with CO2 by Aqueous N-Methyldiethanolamine in a Rotating Packed Bed. Ind. Eng. Chem. Res.
Quarderer, G. J.,Trent, D. L.,Stewart, E. J.,Tirtowidjojo,Mehta, J.,Tirtowidjojo, A. Method for synthesis of hypohalous acid. 2000.
Ramshaw, C., (1983) HIGEE DISTILLATION - AN EXAMPLE OF PROCESS INTENSIFICATION. Chem. Eng.-London. (389) 13-14.
Ramshaw, C.,Mallinson, R. H., Mass transfer process. Google Patents: 1981.
Rao, D. P.,Bhowal, A.,Goswami, P. S., (2004) Process intensification in rotating packed beds (HIGEE): An appraisal. Ind. Eng. Chem. Res. 43 (4) 1150-1162.
Sawistowski, H., (1957) Flooding velocities in packed columns operating at reduced pressures. Chem. Eng. Sci. 6 (3) 138-140.
Shao, L.,Yu, Y.,Bian, S.,Chen, J.,Li, X., (2005) Synthesis of nanosized Y-type TiOPc by a high gravity method. Journal of materials science. 40 (16) 4373-4374.
Shen, S. H.,Ma, Y. G.,Liu, W. L.,Lu, S. M.,Zhu, C. Y., (2010) Mass Transfer Enhancement of Propane Absorption into Dodecane-Water Emulsions. Chinese Journal of Chemical Engineering. 18 (2) 217-222.
Singh, S. P.,Wilson, J. H.,Counce, R. M.,Villiersfisher, J. F.,Jennings, H. L.,Lucero, A. J.,Reed, G. D.,Ashworth, R. A.,Elliott, M. G., (1992) REMOVAL OF VOLATILE ORGANIC-COMPOUNDS FROM GROUNDWATER USING A ROTARY AIR STRIPPER. Ind. Eng. Chem. Res. 31 (2) 574-580.
Sung, W. D.,Chen, Y. S., (2012) Characteristics of a rotating packed bed equipped with blade packings and baffles. Separation and Purification Technology. 93 52-58.
Tai, C. Y.,Chia-Te Tai,Chang, M. H.,Liu, H. S., (2007) Synthesis of magnesium hydroxide and oxide nanoparticles using a spinning disk reactor. Ind. Eng. Chem. Res. 46 (17) 5536-5541.
Tai, C. Y.,Tai, C.,Liu, H., (2006) Synthesis of submicron barium carbonate using a high-gravity technique. Chem. Eng. Sci. 61 (22) 7479-7486.
Tai, C. Y.,Wang, Y. H.,Liu, H. S., (2008) A green process for preparing silver nanoparticles using spinning disk reactor. Aiche J. 54 (2) 445-452.
Tan, C.-S.,Lee, P.-L., (2008) Supercritical CO2 desorption of activated carbon loaded with 2,2,3,3-tetrafluoro-1-propanol in a rotating packed bed. Environmental Science and Technology. 42 (Compendex) 2150-2154.
Tan, C. S.,Chen, J. E., (2006) Absorption of carbon dioxide with piperazine and its mixtures in a rotating packed bed. Separation and purification technology. 49 (2) 174-180.
Tan, C. S.,Lee, P. L., (2008) Supercritical CO2 desorption of activated carbon loaded with 2,2,3,3-tetrafluoro-1-propanol in a rotating packed bed. Environ. Sci. Technol. 42 (6) 2150-2154.
Tung, H. H.,Mah, R. S. H., (1985) Modeling liquid mass transfer in higee separation process. Chemical Engineering Communications. 39 (1) 147-153.
Vanede, C. J.,Vanhouten, R.,Beenackers, A., (1995) ENHANCEMENT OF GAS TO WATER MASS-TRANSFER RATES BY A DISPERSED ORGANIC-PHASE. Chem. Eng. Sci. 50 (18) 2911-2922.
Vinke, H.,Hamersma, P.,Fortuin, J., (1993) Enhancement of the gas-absorption rate in agitated slurry reactors by gas-adsorbing particles adhering to gas bubbles. Chem. Eng. Sci. 48 (12) 2197-2210.
Wang, C.,Lin, C.,Hung, W.,Huang, W.,Law, C., (2004) On the burning characteristics of collision-generated water/hexadecane droplets. Combustion science and technology. 176 (1) 71-93.
Wang, D. G.,Guo, F.,Chen, J. F.,Liu, H.,Zhang, Z. T., (2006) Preparation of nano aluminium trihydroxide by high gravity reactive precipitation. Chem. Eng. J. 121 (2-3) 109-114.
Wang, G.,Xu, Z.,Yu, Y.,Ji, J., (2008) Performance of a rotating zigzag bed--A new HIGEE. Chemical Engineering and Processing: Process Intensification. 47 (12) 2131-2139.
Whelpdale, D.,List, R., (1971) The coalescence process in raindrop growth. Journal of Geophysical Research. 76 (12) 2836-2856.
Xiao, Q. G.,Tao, X.,Chen, J. F., (2007) Silica nanotubes based on needle-like calcium carbonate: fabrication and immobilization for glucose oxidase. Ind. Eng. Chem. Res. 46 (2) 459-463.
Yang, H. J.,Chu, G. W.,Zhang, J. W.,Shen, Z. G.,Chen, J. F., (2005) Micromixing efficiency in a rotating packed bed: Experiments and simulation. Ind. Eng. Chem. Res. 44 (20) 7730-7737.
Yang, K.,Chu, G. W.,Shao, L.,Luo, Y.,Chen, J. F., (2009) Micromixing efficiency of rotating packed bed with premixed liquid distributor. Chem. Eng. J. 153 (1-3) 222-226.
Yang, K.,Chu, G. W.,Zou, H. K.,Sun, B. C.,Shao, L.,Chen, J. F., (2011) Determination of the effective interfacial area in rotating packed bed. Chem. Eng. J. 168 (3) 1377-1382.
Yang, S. T.,Lo, Y. M.,Min, D. B., (1996) Xanthan gum fermentation by Xanthomonas campestris immobilized in a novel centrifugal fibrous-bed bioreactor. Biotechnol. Prog. 12 (5) 630-637.
Yang, W. J.,Wang, Y. D.,Chen, J. F.,Fei, W. Y., (2010) Computational fluid dynamic simulation of fluid flow in a rotating packed bed. Chem. Eng. J. 156 (3) 582-587.
Zhang, G. D.,Cai, W. F.,Xu, C. J.,Zhou, M., (2006) A general enhancement factor model of the physical absorption of gases in multiphase systems. Chem. Eng. Sci. 61 (2) 558-568.
Zhang, L. L.,Wang, J. X.,Xiang, Y.,Zeng, X. F.,Chen, J. F., (2011) Absorption of Carbon Dioxide with Ionic Liquid in a Rotating Packed Bed Contactor: Mass Transfer Study. Ind. Eng. Chem. Res. 50 (11) 6957-6964.
Zhao, H.,Wang, J. X.,Zhang, H. X.,Shen, Z. G.,Yun, J.,Chen, J. F., (2009) Facile Preparation of Danazol Nanoparticles by High-Gravity Anti-solvent Precipitation (HGAP) Method. Chinese Journal of Chemical Engineering. 17 (2) 318-323.
許宜群 (2004) 錯流式旋轉填充床之特性研究, 國立台灣大學化學工程學碩士論文.
劉奕瑩 (2008) 旋轉填充床之疏水性有機揮發物質的質傳研究, 國立台灣大學化學工程學碩士論文.
蔡詞伊 (2011) 以矽油加水在旋轉填充床吸收甲苯之研究, 國立台灣大學化學工程學碩士論文.
王鈺傑 (2012) 旋轉填充床內部之溫度分佈, 國立台灣大學化學工程學碩士論文.
高天冀 (1998) 液滴碰撞行為分析和液滴產生器研發設計, 國立成功大學機械工程學碩士論文
洪偉恭 (2001) 撞擊液滴於高溫下之燃燒現象觀察與研究, 國立台灣大學機械工程學碩士論文
傅新淵 (2002) 多組份二元液滴碰撞與燃燒之研究, 國立台灣大學機械工程學碩士論文
黃偉智 (2002) 雙組份撞擊液滴在高溫環境下之燃燒現象觀察, 國立台灣大學機械工程學碩士論文
黃偉豪 (2004) 雙組份柴油撞擊液滴之碰撞現象觀察, 國立台灣大學機械工程學碩士論文
dc.identifier.urihttp://tdr.lib.ntu.edu.tw/jspui/handle/123456789/61349-
dc.description.abstract本研究為錯流式旋轉填充床內同時吸收甲苯與異丙醇的質傳程序,甲苯為疏水性揮發有機物,而異丙醇為親水性揮發有機物,分別使用水、矽油以及矽油加水混合物作為吸收劑進行吸收程序。單獨用水時,異丙醇最高吸收分率可達到0.99,而甲苯最高吸收分率只有0.1,顯示對於親水性揮發有機物水是一個適當的吸收劑;單獨使用矽油時,甲苯最佳吸收分率為0.78,而異丙醇只有0.33,明顯可看出矽油適合作為疏水性揮發有機物的吸收劑。
接著,使用矽油加水混合物吸收甲苯與異丙醇實驗,其結果顯示,甲苯與異丙醇皆可達到0.9以上的吸收分率。為了探討矽油加水混合物對於甲苯與異丙醇的吸收是正向或負向幫助,透過E factor(enhancement factor)的計算進行分析。甲苯的E值在矽油流量為0.1L/min時,隨水流量增加而上升到最大值為2.5,當矽油流量越大,能提昇的E值幅度就越小,而異丙醇的E值在水流量為0.01 L/min與0.03L/min時皆小於1,隨著水量的增加回逐漸上升到1左右。以上的結果主要來自碰撞包覆效應與總液體流量效應兩個因素所影響,碰撞包覆效應會使得矽油包覆在水的外面,造成矽油與氣體接觸面積增加,但讓水與氣體接觸面積減少,因此有利於甲苯的吸收,卻不利於吸收異丙醇;總液體流量效應可藉由水使得黏度高的矽油均勻分布於床體中,使得甲苯與矽油接觸面積大幅提升,使得甲苯的質傳效果變好。
zh_TW
dc.description.abstractThis work presented a mass transfer process of absorbing toluene and isopropanol in a cross-flow rotating packed bed (RPB) at the same time. Toluene is a hydrophobic volatile organic compound (VOC) while isopropanol is a hydrophilic VOC. Water, silicone oil, as well as the mixture of silicone oil and water were used as absorbents for these absorption processes. When using water as the only absorbent, the best absorption fraction of isopropanol was 0.99, but it was only 0.1 for toluene. It obviously indicated that water is a suitable absorbent for hydrophilic VOCs. When silicone oil was the absorbent alone, the best absorption fraction for toluene was 0.78, and 0.33 for isopropanol. It suggested that silicone oil is a appropriate absorbent for hydrophobic VOCs.
Then, we implemented the absorption processes of toluene and isopropanol by the mixture of silicone oil and water. Both absorption fractions for these two compounds could reach more than 0.9. We calculated the enhancement factor (E) to evaluate the impacts on absorptions of toluene and isopropanol by this mixed absorbent. As the silicone oil flow rate was 0.1, the E value of toluene rose significantly to 2.5 with increasing water flow rate. Higher the silicone oil flow rate resulted in less enhancements. However, the E value of isopropanol was less than 1 when the water flow rate were 0.01 and 0.03 L/min, and it would gradually increase to about 1 with the increase of water flow rate. The “insertive merging effect” and the total liquid flow rate effect could be used to explain the results above. The insertive merging effect means that the water droplet inserted into silicone oil droplet. This effect increased the effective gas-liquid contact area of oil but hindered that of water. Thus it was favorable for absorption of toluene but not for isopropanol. The total liquid flow rate effect means that water lead silicone oil of high viscosity to distribute better inside the RPB, and it causes higher gas-liquid contact area between toluene and silicone oil. Therefore, it could enhance mass transfer for hydrophobic VOCs.
en
dc.description.provenanceMade available in DSpace on 2021-06-16T13:01:26Z (GMT). No. of bitstreams: 1
ntu-102-R00524067-1.pdf: 4435601 bytes, checksum: 2dcd600c4da50845981e95704a806770 (MD5)
Previous issue date: 2013
en
dc.description.tableofcontents摘要 I
Abstract II
目錄 IV
表目錄 VII
圖目錄 XII
第一章 緒論 1
1-1 序言 1
1-2 研究方向 2
第二章 文獻回顧 3
2-1 旋轉填充床 (Rotating packed bed, RPB) 3
2-1.1旋轉填充床之構造與床體設計 4
2-1.2 壓降 10
2-1.3 旋轉填充床之液體流態、液體滯留量、液體滯留時間 14
2-1.4 旋轉填充床之有效質傳界面積 18
2-1.5 液膜質傳係數 20
2-1.6 氣膜質傳係數 23
2-1.7 旋轉填充床之微觀混合 26
2-1.8 錯流式旋轉填充床之回顧 29
2-1.9 旋轉填充床之應用與發展 33
2-2 揮發性有機物質處理方法 43
2-3旋轉填充床中液滴的碰撞 47
2-3.1相同液滴之碰撞行為 47
2-3.2 具有表面張力差異之雙液滴碰撞 49
第三章 實驗與分析方法 54
3-1 實驗裝置 54
3-2實驗藥品與分析儀器 56
3-3 實驗方法 58
3-3.1 實驗流程 58
3-3.2平衡常數實驗方法 60
3-4總括氣膜體積質傳係數(overall volumetric mass transfer coefficient)分析 62
3-4.1雙膜理論(two-film theory) 62
3-4.2 錯流式旋轉填充床之氣膜質傳係數分析 65
第四章 結果與討論 70
4-1 以吸收分率評估質傳效果 70
4-1.1 以水為吸收劑吸收甲苯與異丙醇氣體 71
4-1.2 以矽油為吸收劑吸收甲苯與異丙醇氣體 71
4-1.3 矽油加水混合作為吸收劑吸收甲苯與異丙醇氣體 72
4-1.3-1 水與油碰撞包覆效應以及總液體流量對吸收分率之影響 74
4-2 矽油加水與單獨水或矽油之吸收效果比較,E factor 84
4-2.1-1 水的流量(Lw)對於E factor的影響 84
4-2.1-2矽油的流量(Lo)對於E factor的影響 86
4-2.2 轉速對於E factor之影響 98
4-3 總液體流量效應與碰撞包覆效應對於矽油加水吸收程序的影響 104
4-3.1 觀察總液體流量對於吸收效果之影響 104
4-3.2 觀察碰撞包覆效應對於吸收效果之影響 110
4-4 以質傳係數評估質傳的效果 113
4-4.1 平衡常數的估算 113
4-4.2矽油加水對於質傳係數(KGa)的影響 116
第五章 結論 122
參考文獻 125
符號說明 134
dc.language.isozh-TW
dc.subject旋轉填充床zh_TW
dc.subject吸收zh_TW
dc.subject質傳zh_TW
dc.subject疏水性揮發有機物zh_TW
dc.subject親水性揮發有機物zh_TW
dc.subjectMass transferen
dc.subjectHydrophilic VOCsen
dc.subjectHydrophobic VOCsen
dc.subjectAbsorptionen
dc.subjectRotating packed bed (RPB)en
dc.title在旋轉填充床內吸收親疏水性有機揮發物之研究zh_TW
dc.titleAbsorption of hydrophilic and hydrophobic volatile organic compounds in a rotating packed beden
dc.typeThesis
dc.date.schoolyear101-2
dc.description.degree碩士
dc.contributor.oralexamcommittee林佳璋(Chia-Chang Lin),陳昱劭(Yu-Shao Chen),江佳穎(Chia-Ying Chiang)
dc.subject.keyword旋轉填充床,吸收,質傳,疏水性揮發有機物,親水性揮發有機物,zh_TW
dc.subject.keywordRotating packed bed (RPB),Absorption,Mass transfer,Hydrophilic VOCs,Hydrophobic VOCs,en
dc.relation.page138
dc.rights.note有償授權
dc.date.accepted2013-08-07
dc.contributor.author-college工學院zh_TW
dc.contributor.author-dept化學工程學研究所zh_TW
顯示於系所單位:化學工程學系

文件中的檔案:
檔案 大小格式 
ntu-102-1.pdf
  未授權公開取用
4.33 MBAdobe PDF
顯示文件簡單紀錄


系統中的文件,除了特別指名其著作權條款之外,均受到著作權保護,並且保留所有的權利。

社群連結
聯絡資訊
10617臺北市大安區羅斯福路四段1號
No.1 Sec.4, Roosevelt Rd., Taipei, Taiwan, R.O.C. 106
Tel: (02)33662353
Email: ntuetds@ntu.edu.tw
意見箱
相關連結
館藏目錄
國內圖書館整合查詢 MetaCat
臺大學術典藏 NTU Scholars
臺大圖書館數位典藏館
本站聲明
© NTU Library All Rights Reserved