請用此 Handle URI 來引用此文件:
http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/71217完整後設資料紀錄
| DC 欄位 | 值 | 語言 |
|---|---|---|
| dc.contributor.advisor | 蔣本基 | |
| dc.contributor.author | Tzu-Hao Huang | en |
| dc.contributor.author | 黃子郝 | zh_TW |
| dc.date.accessioned | 2021-06-17T04:59:10Z | - |
| dc.date.available | 2019-08-01 | |
| dc.date.copyright | 2018-08-01 | |
| dc.date.issued | 2018 | |
| dc.date.submitted | 2018-07-26 | |
| dc.identifier.citation | 林益生,「環氧成型模料對構裝後晶片可靠度的影響」,工程科技與教育學刊,7:4 2010.10[民99.10] 頁532-545
Byeon, S.-H., et al. (2012). 'Removal of ammonia and particulate matter using a modified turbulent wet scrubbing system.' Separation and Purification Technology 98: 221-229. Chen, Yu-Shao & Lin, Chia-Chang & Liu, Hwai-Shen. (2005). “Mass Transfer in a Rotating Packed Bed with Viscous Newtonian and Non-Newtonian Fluids.” Industrial & Engineering Chemistry Research - IND ENG CHEM RES. 44. 10.1021/ie0499409. Clyde V. Owen, JR., et al. (2007). “Identification of Estrogenic Compounds Emitted from the Combustion of Computer Printed Circuit Boards in Electronic Waste.” Environ. Sci. Technol 41: 8506–8511. Curran, M. A. (2013). 'Life Cycle Assessment: a review of the methodology and its application to sustainability.' Current Opinion in Chemical Engineering 2(3): 273-277. C. Zheng, K. Guo, Y. Feng, C. Yang, and N. C. Gardner. (2000) “Pressure drop of centripetal gas flow through rotating beds,” Industrial and Engineering Chemistry Research, vol. 39,no. 3, pp. 829–834. Englert, N. (2004). 'Fine particles and human health--a review of epidemiological studies.' Toxicol Lett 149(1-3): 235-242. Fen Guo, Chong Zheng, Kai Guo, Yuanding Feng, Nelson C. Gardner. (1997). “Hydrodynamics and mass transfer in cross-flow rotating packed bed.” Chemical Engineering Science, Volume 52, Issues 21–22, pp. 3853-3859. Feng, S., et al. (2016). 'The health effects of ambient PM2.5 and potential mechanisms.' Ecotoxicol Environ Saf 128: 67-74. Fu, J., Qi, G., Liu, Y., Tian, J., Guo, Q., Dong, M., (2015b). “Research on removal of fine particles by cross-flow rotating packed bed.” Chem. Industry Eng. Prog. 34, 680-694 Gao, X.-Y., et al. (2016). 'Numerical simulation for mass transfer characteristics of CO 2 capture in a rotating packed bed.' Chemical Engineering and Processing: Process Intensification 109: 68-79. Gao, Z., et al. (2015). 'Droplet characteristics and behaviors in a high-speed disperser.' Chemical Engineering Science 126: 329-340. Guo, T.-Y., et al. (2017). 'Three-Dimensional Simulation on Liquid Flow in a Rotating Packed Bed Reactor.' Industrial & Engineering Chemistry Research 56(28): 8169-8179. Hakobyan, N.A. (2015). “Introduction to Basics of Submicron Aerosol Particles Filtration Theory via Ultrafine Fiber Media.” Armenian Journal of Physics, 8 (3). pp. 140-151. H. T. Kim, C. H. Jung, S. N. Oh, and K. W. Lee. (2001). “Particle Removal Efficiency of Gravitational Wet Scrubber Considering Diffusion, Interception, and Impaction.” Environmental Engineering ScienceVol. 18, No. 2. Hu, X.-P., Tian, D.-L., Deng, X.-H., (2009). Experimental research on removing of micron scale dust by high gravity rotating packed bed (in Chinese). Mod. Chem. Ind. 29, 69-74. Hutzinger, O, et al. (1985). “Formation of Polychiorinated Dibenzofurans and Dioxins during Combustion, Electrical Equipment Fires and PCB Incineration.” Environmental Health Perspectives Vol. 60, pp. 3-9. Islam, S., et al. (2016). 'Review on life cycle inventory: methods, examples and applications.' Journal of Cleaner Production 136: 266-278. ISO 14040. (2006). Environmental Management- Life Cycle Assessment- principles and Framework. International Organization for Standardization (ISO),Geneva. J.R. Burns, C. Ramshaw. (1996). “Process intensification: Visual study of liquid maldistribution in rotating packed beds.” Chemical Engineering Science, Volume 51, Issue 8, pp. 1347-1352, J.R. Burns, J.N. Jamil, C. Ramshaw. (2000). “Process intensification: operating characteristics of rotating packed beds — determination of liquid hold-up for a high-voidage structured packing.” Chemical Engineering Science, Volume 55, Issue 13, pp. 2401-2415. Lamb, H., (1993). Hydrodynamics, sixth ed. Cambridge University Press. Levchik, S. V. and E. D. Weil (2004). 'Thermal decomposition, combustion and flame-retardancy of epoxy resins-a review of the recent literature.' Polymer International 53(12): 1901-1929. Li, W., et al. (2017). 'Modelling of dust removal in rotating packed bed using artificial neural networks (ANN).' Applied Thermal Engineering 112: 208-213. Li, Y., et al. (2015). 'Visual study of liquid flow in a rotor-stator reactor.' Chemical Engineering Science 134: 521-530. Li, Z.-Y., et al. (2017). 'Study on the removal of fine particles by using water in a rotating packed bed.' The Canadian Journal of Chemical Engineering 95(6): 1063-1068. Liu, Y., et al. (2017). '3D numerical simulation of a rotating packed bed with structured stainless steel wire mesh packing.' Chemical Engineering Science 170: 365-377. Llerena-Chavez, H. and F. Larachi (2009). 'Analysis of flow in rotating packed beds via CFD simulations—Dry pressure drop and gas flow maldistribution.' Chemical Engineering Science 64(9): 2113-2126. Mohebbi, A., et al. (2003). 'Simulation of an orifice scrubber performance based on Eulerian/Lagrangian method.' Journal of Hazardous Materials 100(1-3): 13-25. Ouyang, Y., et al. (2018). 'Computational fluid dynamics modeling of viscous liquid flow characteristics and end effect in rotating packed bed.' Chemical Engineering and Processing: Process Intensification 123: 185-194. Pak, S. I. and K. S. Chang (2006). 'Performance estimation of a Venturi scrubber using a computational model for capturing dust particles with liquid spray.' J Hazard Mater 138(3): 560-573. Pan, S.-Y., et al. (2017). 'Development of high-gravity technology for removing particulate and gaseous pollutant emissions: Principles and applications.' Journal of Cleaner Production 149: 540-556. Pitch, J. (1964).” Impaction of aerosol particles in the neighborhood of a circular hole.” Collect. Czech. Chem. Commun. 29, 2223-2227 Qian, G.-H., et al. (2004). 'Soot removal from diesel engine exhaust using a rotating fluidized bed filter.' Advances in Environmental Research 8(3-4): 387-395. R.A. Pulley. (1997). “Modelling the performance of venturi scrubbers.”Chemical Engineering Journal, Volume 67, Issue 1. pp. 9-18. Rebitzer, G., et al. (2004). 'Life cycle assessment part 1: framework, goal and scope definition, inventory analysis, and applications.' Environ Int 30(5): 701-720. Sang, L., et al. (2017). 'Modeling and experimental studies of mass transfer in the cavity zone of a rotating packed bed.' Chemical Engineering Science 170: 355-364. Sang, L., et al. (2017). 'Liquid flow pattern transition, droplet diameter and size distribution in the cavity zone of a rotating packed bed: A visual study.' Chemical Engineering Science 158: 429-438. Shi, X., et al. (2013). 'CFD analysis of liquid phase flow in a rotating packed bed reactor.' Chemical Engineering Journal 228: 1040-1049. Song, Y., Chen, J., Fu, J., Chen, J., (2003). Research on particle removal efficiency of the rotating packed bed (in Chinese). Chem. Industry Eng. Prog. 22, 499-502 Tardif, François & Danel, Adrien & Raccurt, Olivier. (2005). Understanding of wet and alternative particle removal processes in microelectronics: theoretical capabilities and limitations. WHO (2006). “Global air-quality guidelines for particulate matter, ozone, nitrogen dioxide and sulfur dioxide.” Lancet, 2005.368(9544):p.5. Xie, P., et al. (2017). 'Characteristics of liquid flow in a rotating packed bed for CO 2 capture: A CFD analysis.' Chemical Engineering Science 172: 216-229. Xu, C & Jiao, Weizhou & Liu, Y & Guo, L & Yuan, Z & Zhang, Q. (2014). “Effects of Airflow Field on Droplets Diameter inside the Corrugated Packing of a Rotating Packed Bed.” China Petroleum Processing and Petrochemical Technology. 16. 38-46. Yan, Z.-y., et al. (2012). 'Hydrodynamics in a Rotating Packed Bed. I. A Novel Experimental Method.' Industrial & Engineering Chemistry Research 51(31): 10472-10481. Yan, Z.-y., et al. (2014). 'Dynamics of droplets and mass transfer in a rotating packed bed.' AIChE Journal 60(7): 2705-2723. Yan, Z.-y., et al. (2012). 'Hydrodynamics in a Rotating Packed Bed. II. A Mathematical Model.' Industrial & Engineering Chemistry Research 51(31): 10482-10491. Yang, W., et al. (2010). 'Computational fluid dynamic simulation of fluid flow in a rotating packed bed.' Chemical Engineering Journal 156(3): 582-587. Yang, Y., et al. (2015). 'A noninvasive X-ray technique for determination of liquid holdup in a rotating packed bed.' Chemical Engineering Science 138: 244-255. Zou, H.-K., et al. (2017). 'Study on the Removal of Fine Particles from Gas Steam Using Water in a Rotating Packed Bed Combined with a Charged Device.' Energy & Fuels 31(2): 1764-1770. | |
| dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/71217 | - |
| dc.description.abstract | 本研究與優勝奈米有限公司進行合作,利用超重力旋轉床進行IC碳化製程中產生之懸浮微粒減量去除效益評估。IC碳化過程中產生大量人體有害之懸浮微粒,超重力旋轉填充床可產生大量小液滴及液膜,可增加對液滴與懸浮微粒之碰撞機率,提升對懸浮微粒之捕捉去除效率。本研究目標包含不同操作條件下對於總懸浮微粒去除效率的影響:研究不同轉速、液體流量與進口濃度對於效率的影響,同時透過反應曲面方法,找出可達之最高效率操作條件,並透過半理論公式進行去除機制分析,同時將實驗結果進行擬合,進行效率預估,最後利用生命週期評估分析整個程序對環境之衝擊。研究結果發現提高轉速和液體流量皆會對去除效率有很大的提升,提高入口濃度亦可提高效率,但在高轉速與高液體流量下影響並不明顯。利用反應曲面法將轉速與流量進行操作最佳化,在實驗設備極限中所能達到之最高效率為99.5%,對應之條件為1740 rpm、1448 ml/min。透過半理論公式進行超重力旋轉填充床之去除機制進行了解,發現填充物與液滴皆對懸浮微粒有顯著的去除效果,低轉速時以填充物去除為主,反之高轉速液滴的去除才較為重要。透過實驗數據進行數據擬合同時也得到良好的相關性進行效率預測。最後透過生命週期評估進行環境衝擊量化,發現利用超重力旋轉填充床進行懸微粒去除可有效降低環境之衝擊,最低之環境衝擊僅有未經處理的0.29倍,證明超重力旋轉填充床不只可達到良好的去除效率,同時也可降低環境衝擊,可視為環境有益之空氣污染處理技術。 | zh_TW |
| dc.description.abstract | This research was in cooperation with the Uwin Nanotech. Co., Ltd. The rotating packed bed (RPB) was used to enhance particle reduction from the integrated circuit (IC) carbonized process. The IC carbonized process may produce harmful particle. The RPB could create plenty of droplet and liquid film, which could enhance collision probability to obtain high particle removal efficiency. Objectives of this research include investigating the effect of operating conditions on particle removal efficiency. The operating parameters were rotating speed, liquid flow rate and particle concentration. Meanwhile the highest achievable efficiency was studied by the response surface methodology (RSM). The semi-theoretical model was used to analyze the removal mechanism inside RPB, and an empirical model was developed to predict the removal efficiency. Finally, life cycle assessment (LCA) was applied to evaluate the environment impact of RPB. Results showed that increasing in rotating speed, liquid flow rate and particle concentration could increase particle removal efficiency, but for high rotating speed and liquid flow rate, the effect of particle concentration was insignificant. By RSM method, the highest achievable efficiency within equipment limitation was determined at 99.5%, 1740 rpm rotating speed and 1448 ml/min flow rate. From semi-theoretical model, both packing zone and cavity zone was both important in the particle removal process. In lower rotating speed, the packing zone was dominated, as for high rotating speed the cavity zone became dominate. The empirical model showed good agreement between the predicted data and the experimental data, which could be used for efficiency prediction. Final, from LCA, the result showed that by using RPB for particle reduction, the minimum impact was only 0.29 times of a conventional process without RPB. Results from this study indicated that RPB could not only achieving r high removal efficiency, but also be an environment benefit air pollution control technology. | en |
| dc.description.provenance | Made available in DSpace on 2021-06-17T04:59:10Z (GMT). No. of bitstreams: 1 ntu-107-R05541105-1.pdf: 5169368 bytes, checksum: bfd0dc1e6aa3bf27254e1adeeb1c6c4b (MD5) Previous issue date: 2018 | en |
| dc.description.tableofcontents | 誌謝 ii
中文摘要 iii Abstract iv Contents vi List of Figures ix List of Table xiii Orel Defense Comments xiv Chapter 1. Introduction 1-1 1.1 Background 1-1 1.2 Objectives 1-4 Chapter 2. Literature Review 2-1 2.1 PM removal mechanism 2-1 2.1.1 Inertial impaction. 2-1 2.1.2: Interception 2-3 2.1.3: Brownian diffusion 2-4 2.2 Performance of PM removed by RPB 2-6 2.3 Liquid flow pattern and velocity 2-11 2.3.1 Liquid flow pattern 2-11 2.3.2 Droplet characteristic 2-14 2.3.4 Liquid velocity 2-18 2.4 Gas flow pattern and velocity 2-20 Chapter 3. Materials and Methods 3-1 3.1 Research framework 3-1 3.2 Experiment setup 3-2 3.3 Materials 3-4 3.4 Equipment 3-5 3.5 Experiment methods 3-10 3.5.1: Pre-treatment and post-treatment of filter paper. 3-10 3.5.2 Experimental parameters 3-11 3.5.3 The determination of highest achievable removal efficiency. 3-12 3.5.4 Life cycle assessment (LCA) 3-16 Chapter 4. Results and Discussion 4-1 4.1 Performance of fine particle removal by RPB. 4-1 4.1.1: Fine particles generation 4-2 4.1.2: Removal efficiency of fine particle by RPB 4-9 4.1.3: Effect of inlet particle concentration on removal efficiency 4-15 4.1.4 Summary 4-18 4.2 Determination of maximum achievable removal efficiency by RPB. 4-19 4.2.1 The creation of response surface 4-20 4.2.2 The maximum achievable efficiency of RPB. 4-25 4.2.3 The effect of inlet gas flow rate on removal efficiency 4-29 4.2.4 The effect of surfactant concentration on removal efficiency. 4-31 4.2.5 Summary 4-33 4.3 Modeling fine particle removal by RPB. 4-34 4.3.1: Semi-theoretical model 4-35 4.3.2: Empirical model 4-45 4.3.3 Summary 4-48 4.4 Environmental impacts of particle removal by RPB. 4-49 4.4.1 Goal and scope 4-50 4.4.2 Life cycle assessment 4-55 4.4.3 Summary 4-61 Chapter 5. Conclusions and Recommendations 5-1 5.1 Conclusions 5-1 5.2 Recommendations 5-2 Appendix a Reference b | |
| dc.language.iso | en | |
| dc.subject | 細懸浮微粒 | zh_TW |
| dc.subject | 電子廢棄物焚燒 | zh_TW |
| dc.subject | 超重力旋轉填充床 | zh_TW |
| dc.subject | 空氣污染減量 | zh_TW |
| dc.subject | 生命週期評估 | zh_TW |
| dc.subject | life cycle assessment (LCA) | en |
| dc.subject | E-waste combustion | en |
| dc.subject | rotating packed bed (RPB) | en |
| dc.subject | air pollution reduction | en |
| dc.subject | Fine particle | en |
| dc.title | 利用超重力旋轉填充床於電子廢棄物焚化處理排氣中細懸浮微粒去除效益評估 | zh_TW |
| dc.title | Performance Evaluation of Fine Particle Removal from Air Emissions of the E-waste Combustion Process via a Rotating Packed Bed | en |
| dc.type | Thesis | |
| dc.date.schoolyear | 106-2 | |
| dc.description.degree | 碩士 | |
| dc.contributor.oralexamcommittee | 曾迪華,顧洋,張怡怡,陳奕宏 | |
| dc.subject.keyword | 細懸浮微粒,電子廢棄物焚燒,超重力旋轉填充床,空氣污染減量,生命週期評估, | zh_TW |
| dc.subject.keyword | Fine particle,E-waste combustion,rotating packed bed (RPB),air pollution reduction,life cycle assessment (LCA), | en |
| dc.relation.page | 117 | |
| dc.identifier.doi | 10.6342/NTU201801966 | |
| dc.rights.note | 有償授權 | |
| dc.date.accepted | 2018-07-26 | |
| dc.contributor.author-college | 工學院 | zh_TW |
| dc.contributor.author-dept | 環境工程學研究所 | zh_TW |
| 顯示於系所單位: | 環境工程學研究所 | |
文件中的檔案:
| 檔案 | 大小 | 格式 | |
|---|---|---|---|
| ntu-107-1.pdf 未授權公開取用 | 5.05 MB | Adobe PDF |
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。
