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完整後設資料紀錄
DC 欄位 | 值 | 語言 |
---|---|---|
dc.contributor.advisor | 蔣本基 | |
dc.contributor.author | Hsiao-Wen Chu | en |
dc.contributor.author | 朱孝文 | zh_TW |
dc.date.accessioned | 2021-06-13T00:05:01Z | - |
dc.date.available | 2010-07-30 | |
dc.date.copyright | 2007-07-30 | |
dc.date.issued | 2007 | |
dc.date.submitted | 2007-07-30 | |
dc.identifier.citation | Asavapist, S.; Fowler, G.; Cheeseman, C.; Solution chemistry during
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Park, Ah-Hyung Alissa, Fan Liang-Shih. Carbon dioxide mineral sequestration: Chemical and Physical Activation of Aqueous Mineral Carbonation and pH Swing Process. Department of chemical engineering, 2005. Park, Ah-Hyung Alissa, Fan Liang-Shih. CO2 mineral sequestration: physically activated dissolution of serpentine and pH swing process; Chemical Engineering Science, 59, 5242-5247. 2004. Park, A.-H.A., R. Jadhav, and L.-S. Fan., CO2 mineral sequestration: chemically enhanced aqueous carbonation of serpentine; Canadian journal of chemical engineering. 2003. 81 (3): 885 -890. Park, A.-H.A., R. Jadhav, and L.-S. Fan., CO2 mineral sequestration in a highpressure,high temperature three-phase fluidised bed reactor; 20th annual international Pittsburgh coal conference, Pittsburgh, PA, USA. 2003 Penner, L.R., W.K. O'Connor, D.C. Dahlin, S.J. Gerdemann, and G.E. Rush., Mineral carbonation: Energy costs of pretreatment options and insights gained from flow loop reaction studies; 3rd annual conference on carbon sequestration, Alexandria, VA, USA. 2004 Sorochkin, M. A.; Shchrov, A. F.; Safonov, I. A.; Study of the possibility of using carbon dioxide for accelerating the hardening of products made from Portland cement, J. Appl. Chem. 48, 1975. Schulze, R.K., M.A. Hill, R.D. Field, P.A. Papin, R.J. Hanrahan, and D.D. Byler., Characterization of carbonated serpentine using XPS and TEM; Energy Conversion and Management, 2004. 45 (20): 3169-3179. Walton, J.; Bin-Shafique, S.; Smith, R.; Gutierrez, N.; Tarquin, A.; Role of carbonation in transient leaching of cementitious waste forms, Environ, Sci. Technol. 31, 2345, 1997. Wendt, C.H., D.P. Butt, K.S. Lackner, R. Vaidya, and H.-J. Ziock., Thermodynamic calculations for acid decomposition of serpentine and olivine in MgCl2 melts III; Los Alamos National Laboratory, LA-UR-98-5633, Los Alamos, NM, USA. 1998 Wendt, C.H., D.P. Butt, K.S. Lackner, and H.-J. Ziock., Thermodynamic calculations for acid decomposition of serpentine and olivine in MgCl2 melts I; Los Alamos National Laboratory, LA-UR-98-4528, Los Alamos, NM, USA. 1998 Wu, J.C.S., J.-D. Sheen, S.-Y. Chen, and Y.-C. Fan., Feasibility of CO2 fixation via artificial rock weathering; Industrial and engineering chemistry research. 2001, 40 (18):3902-3905 Zhang, Q., K. Sugiyama, and F. Saito., Enhancement of acid extraction of magnesium and silicon from serpentine by mechanochemical treatment;Hydrometallurgy. 1996, 45: 323-331. Zevenhoven, R. and S. Teir., Long-term storage of CO2 as magnesium carbonate in Finland; 3rd annual conference on carbon capture and sequestration, Alexandria, VA, USA. 2004 徐啟龍,「以礦物碳酸化法封存CO2」, 碩士論文,國立台灣大學環境工程研究所,台北,2006. | |
dc.identifier.uri | http://tdr.lib.ntu.edu.tw/jspui/handle/123456789/28316 | - |
dc.description.abstract | 以鹼性固體廢棄物碳酸化法封存二氧化碳對於減少二氧化碳排放至大氣中是為可行的方法。三種以鈣成份為主的鹼性固體廢棄物即高細度水淬爐石,飛灰爐石,高強牌高爐水泥被選為二氧化碳封存的材料。這三種材料的優點是便宜,離二氧化碳排放源較近且有較好的反應性。三種材料皆在濕式(泥漿)的條件下與二氧化碳進行碳酸化反應,並探討其反應機制。
操作因子有反應時間、泥漿的液固比、反應溫度、二氧化碳分壓和溶液的初始pH值,改變這些因子來探討其對轉換率的影響。結果顯示高強牌高爐水泥在反應時間達到12小時,溫度控制在160 oC,二氧化碳壓力控制在700psig,且粒徑小於44μm時有最大的轉換率約86%。最主要影響轉換率的因子為反應時間(5分鐘到12小時)與反應溫度(40到160 oC),而此反應動力可用表面覆蓋模式來描述。 另外一種碳酸化方式叫做pH震盪,藉由此方法來提高碳酸化的轉換率。在這系統中,控制pH值來分出三種產物即碳酸鈣、高二氧化矽含量固體和金屬混合物固體。pH 震盪的優點在於其消耗較少的能源並且產生的產物碳酸鈣具有經濟價值可用來補償封存二氧化碳所消耗的成本。最後,應用LCA方法來計算整個實驗過程中二化碳的淨排放量,結果顯示,高強牌高爐水泥和pH震盪程序的二氧化碳淨排放量為-0.028和-0.05 kg/kg (負號代表封存),表示其為可行的二氧化碳減量技術。 | zh_TW |
dc.description.abstract | CO2 sequestration by carbonation of alkaline solid wastes is a potential technology to reduce carbon dioxide emissions to the atmosphere. In this study, three kinds of alkaline Ca-rich solid wastes, i.e., ultra-fine slag; fly ash slag; blended hydraulic cement slag, are selected as possible materials for CO2 sequestration. These materials were carbonated in aqueous condition (slurry) and operated under various conditions of reaction time, liquid to solid ratio, temperature, CO2 partial pressure and initial pH to determine their influence on the carbonation conversion.
The results indicate that the blended hydraulic cement slag has the highest carbonation conversion about 86% in 12 hr at 700 psig and 160 oC. The major factors effecting the conversion are reaction time (5 min to 12 hr) and temperature (40 oC to 160 oC), furthermore, the reaction kinetics can be expressed by surface coverage model. Another route of carbonation, so called pH swing process, was also employed to enhance the conversion of ultra-fine slag. By controlling the pH in this process, three solid products, i.e., CaCO3, SiO2¬-rich solids and metal mixture solids were formed. The advantages of pH swing process include lower energy consumption and the high purity product of CaCO3 which could reduce the operation and maintenance cost of this sequestration technology. Finally, LCA method was applied to compute the net CO2 emission which indicates that both the blended hydraulic cement slag and pH swing process exhibit a negative sign of CO2 emission, i.e., -0.028 and -0.05 kg/kg, respectively, therefore, they are feasible techniques to reduce CO2. | en |
dc.description.provenance | Made available in DSpace on 2021-06-13T00:05:01Z (GMT). No. of bitstreams: 1 ntu-96-R94541126-1.pdf: 3078999 bytes, checksum: 8f37c8f72804a7a74f6ec8a1d7d0d3fd (MD5) Previous issue date: 2007 | en |
dc.description.tableofcontents | Contents
謝誌 I Abstract II 中文摘要 IV Contents V List of Figures IX List of Tables XIII Chapter 1 Introduction 1-1 1-1 Research Background 1-1 1-2 Objectives 1-5 Chapter 2 Literatures Review 2-1 2-1 Selection of alkaline solid wastes 2-1 2-1-1 Selection of suitable element 2-1 2-1-2 Selection of suitable alkaline solid wastes 2-1 2-2 Principles of carbonation reaction 2-3 2-2-1 Thermodynamics of carbonation 2-3 2-2-2 Kinetics 2-6 2-2-2-1 Dry carbonation 2-6 2-2-2-2 Aqueous carbonation 2-8 2-3 Carbonation process routes 2-9 2-3-1 Pre-treatment 2-9 2-3-2 Direct carbonation 2-12 2-3-3 Indirect carbonation 2-17 2-3-4 Comparison of process routes 2-22 2-4 Life Cycle Assessment 2-27 Chapter 3 Materials and Methods 3-1 3-1 Research flowchart 3-1 3-2 Materials 3-2 3-2-1 Source of agents 3-2 3-2-2 Procedure of preparing alkaline solid wastes 3-3 3-3 Physico-chemical analyses 3-6 3-3-1 Density Analysis 3-6 3-3-2 Particle Size Distribution Analysis 3-6 3-3-3 Specific Surface Area and Pore Size Distribution Analysis 3-7 3-3-4 Scanning Electron Microscope (SEM) 3-8 3-3-5 X-Ray Diffractometry (XRD) 3-8 3-3-6 Composition Analysis 3-9 3-4 Carbonation Experiment 3-10 3-4-1 Direct Aqueous Carbonation unit process 3-10 3-4-2 pH swing process (Indirect Carbonation) 3-14 3-5 Life Cycle Assessment 3-16 Chapter 4 Results and Discussion 4-1 4-1 Physical characteristics and composition of Alkaline solid waste 4-1 4-1-1 Particle size, Density, Specific area and Pore Distribution 4-1 4-1-2 Composition analysis 4-4 4-1-3 SEM analysis 4-5 4-2 Direct Aqueous Carbonation 4-8 4-2-1 Preliminary experiment 4-8 4-2-2 Factors affecting carbonation reaction 4-11 4-2-2-1 Effects of reaction time 4-11 4-2-2-2 Effects of liquid to solid ratio 4-13 4-2-2-3 Effects of reaction temperature and reaction pressure 4-15 4-2-2-4 Effects of initial pH 4-19 4-2-3 Product analyses 4-22 4-2-3-1 SEM analysis for carbonated solid wastes 4-22 4-2-3-2 XRD analysis for fresh and carbonated solid wastes 4-24 4-2-4 Predictive model and the optimized operating conditions for CO2 sequestration 4-26 4-2-4-1 Predicative Model for CO2 Sequestration 4-26 4-2-4-2 Determination of the Optimum Operating Conditions 4-32 4-3 pH Swing process (Indirect Aqueous Carbonation) 4-34 4-3-1 Leaching test of calcium 4-34 4-3-2 Analyses of products and by-products 4-35 4-3-3 Conversion comparison 4-42 4-4 CO2 Budget Estimation 4-43 4-4-1 The CO2 emission in the process of transportation 4-43 4-4-2 The CO2 emission due to energy consumption 4-44 4-4-3 The CO2 emission due to chemicals process 4-45 4-4-4 The CO2 sequestration in carbonation process 4-45 4-4-5 Using amounts assessment in laboratory scale 4-48 Chapter 5 Conclusions and Recommendations 5-1 5-1 Conclusions 5-1 5-2 Recommendations 5-2 References Appendix | |
dc.language.iso | en | |
dc.title | 以鹼性固體廢棄物碳酸化法封存二氧化碳 | zh_TW |
dc.title | CO2 sequestration by carbonation of alkaline solid waste | en |
dc.type | Thesis | |
dc.date.schoolyear | 95-2 | |
dc.description.degree | 碩士 | |
dc.contributor.oralexamcommittee | 張怡怡,顧洋,林財富,曾迪華 | |
dc.subject.keyword | 鹼性固體廢棄物,二氧化碳封存,pH震盪,生命週期評估, | zh_TW |
dc.subject.keyword | Alkaline solid waste,CO2 sequestration,pH swing,LCA, | en |
dc.relation.page | 136 | |
dc.rights.note | 有償授權 | |
dc.date.accepted | 2007-07-30 | |
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 |
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