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研究生: Muhammad Fiji Firdaus
Muhammad Fiji Firdaus
論文名稱: Acid-Functionalized Carbon for Xylan Depolymerization to Xylose
Acid-Functionalized Carbon for Xylan Depolymerization to Xylose
指導教授: 林昇佃
Shawn D. Lin
鍾博文
Po-Wen Chung
口試委員: 李明哲
Ming-Jer Lee
孫一明
Yi-Ming Sun
學位類別: 碩士
Master
系所名稱: 工程學院 - 化學工程系
Department of Chemical Engineering
論文出版年: 2018
畢業學年度: 106
語文別: 英文
論文頁數: 80
中文關鍵詞: depolymerizationacid catalysismesoporous carbonxylanadsorption-enhanced hydrolysis
外文關鍵詞: depolymerization, acid catalysis, mesoporous carbon, xylan, adsorption-enhanced hydrolysis
相關次數: 點閱:273下載:3
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Depolymerization of lignocellulosic biomass into carbohydrates remains a challenge for selective production of biofuels or biochemicals. During the dilute acid pretreatment to remove lignin, some hemicellulose also removed. Thus, hemicellulose is not efficiently utilized for biochemical productions. Solid catalysis with strong protonic acid sites is an approach to produce carbohydrates with easy separation from liquid products. Here, we report the hydrolysis of commercially available xylans (birchwood, corncob, and beechwood) into xylose at moderate to high yields (up to 95%) at mild conditions, using acid-functionalized non-porous carbon and mesoporous carbon nanoparticles (MCN). The hydrolysis of birchwood xylan, comprising of 69% of xylan at 150oC for 4 hours over functionalized non-porous carbon and MCN catalysts results in a xylose yield of 32-57% and 43-61%, respectively. The better hydrolysis performance of MCNs than non-porous carbon can be attributed to its higher adsorption capacity.

In order to understand the correlation between xylan properties and hydrolysis performance, comparative hydrolysis studies were performed using various commercially available xylans such as birchwood, corncob, and beechwood xylan over functionalized non-porous carbon and MCN catalysts. Corncob xylan, comprised of 75% xylan having low molecular weight, is soluble in water. Birchwood xylan, comprising of 69% xylan having an average of 184 xylose repeating units is only partially soluble in water. Hydrolysis of corncob xylan over non-porous carbon at 150oC for 4 hours gave a high xylose yield up to 90%. To further determinate which xylan properties contributed to the hydrolysis, beechwood xylan (comprised of 68% xylan), and a water-soluble xylan with almost the same xylose repeating units as birchwood xylan was examined. The hydrolysis of beechwood xylan over non-porous carbon catalysts gave comparable performance as the corncob xylan hydrolysis with a xylose yield of 55-84%. The results indicate that xylan solubility gives major contribution for xylan hydrolysis.

Recommendation Form i Qualification Form ii Abstract iii Acknowledgements iv Contents v List of Figures vii List of Tables viii Chapter 1 Introduction 1 1.1 Research Background 1 1.2 Related Research Trends 3 1.3 Research Purpose 5 1.4 Thesis Structure 6 Chapter 2 Literature Review 7 2.1 Lignocellulose Biomass Structure 7 2.1.1 Cellulose 7 2.1.2 Hemicellulose 9 2.1.3 Lignin 9 2.2 The Concept of Biorefinery 10 2.3 Hydrolysis of Lignocellulosic Biomass into Monomeric Sugars 11 2.3.1 Acid-Catalyzed Hydrolysis Kinetics and Mechanism 12 2.3.2 Homogenous Catalysts for Hydrolysis of Cellulose and Hemicellulose 14 2.3.3 Heterogeneous Catalysts for Hydrolysis of Cellulose and Hemicellulose 16 2.4 Further Utilization of Monomers into Furans and Derivatives 18 2.5 Carbon Materials as Catalyst for Hydrolysis Reaction 19 Chapter 3 Experimental Protocol 21 3.1 Materials and Chemicals 21 3.2 Material Preparation 21 3.2.1 Pretreatment of Raw carbon 21 3.2.2 Sulfonated non-porous carbon 21 3.2.3 Hydrothermal-treated non-porous carbon 23 3.2.4 Nitric acid-treated non-porous carbon 23 3.2.5 Mesoporous Carbon Nanoparticles (MCN) 23 3.2.6 Sulfonated Mesoporous Carbon Nanoparticles (HSO3-MCN) 24 3.2.7 Hydrothermal-treated MCNs (HT-HSO3-MCN) 24 3.2.8 Nitric acid-treated MCN (COOH-MCN) 25 3.3 Characterization Methods 25 3.3.1 Acid Site Determination of Materials 25 3.3.2 Characterization of Materials 26 3.3.3 Composition Determination of Xylan 26 3.3.4 Size Exclusion Chromatography/Gel Permeation Chromatography 27 3.4 Adsorption Capacity of Mesoporous Carbon Nanoparticle (MCN) 27 3.4.1 Adsorption of Xylose and Xylobiose on MCN 27 3.4.2 Corncob Xylan Adsorption on MCN 27 3.4 Hydrolysis of Xylan 28 3.5 Leaching Test of Xylan 29 3.6 Product Analysis Using HPLC 29 Chapter 4 Results and Discussion 31 4.1 Characterization of Materials 31 4.1.1 Determination of Acid Site 31 4.1.2 Thermogravimetric Analysis (TGA) 33 4.1.3 X-Ray Diffraction (XRD) 35 4.1.4 Fourier-Transform Infrared Spectroscopy (FTIR) 36 4.2 Reactant Characterization 37 4.2.1 Size-Exclusion Chromatography/Gel Permeation Chromatography 37 4.2.2 Thermogravimetric Analysis (TGA) of Xylan 38 4.2.3 Composition Analysis of Xylan 39 4.2.4 Xylose and Xyolobiose Adsorption Test 40 4.2.5 Corncob Xylan Adsorption on MCN 42 4.3 Hydrolysis Reaction Result 43 4.3.1 Overview of Hydrolysis Reaction 43 4.3.2 Birchwood Xylan Hydrolysis 45 4.3.3 Effect of Catalyst Loading of non-porous carbon on Birchwood Xylan Hydrolysis 49 4.3.4 Effect of Reaction Time on Birchwood Xylan Hydrolysis 52 4.3.5 Effect of Xylan Source for Xylan Hydrolysis 53 4.3.6 Effect of Reaction Time on Corncob Xylan Hydrolysis 57 Chapter 5 Conclusions 61 5.1 Conclusions 61 5.2 Future Works 61 References 63 Appendix 68

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