跳到主要內容

臺灣博碩士論文加值系統

(216.73.216.17) 您好!臺灣時間:2025/09/03 05:05
字體大小: 字級放大   字級縮小   預設字形  
回查詢結果 :::

詳目顯示

: 
twitterline
研究生:邱明豐
論文名稱:酯化/部份氧化雙功能觸媒之特性分析
論文名稱(外文):Characterization of Esterification/Partial Oxidation Bifunctional Catalysts
指導教授:張仁瑞
指導教授(外文):Jen-Ray Chang
學位類別:碩士
校院名稱:國立中正大學
系所名稱:化學工程研究所
學門:工程學門
學類:化學工程學類
論文種類:學術論文
論文出版年:2001
畢業學年度:89
語文別:中文
論文頁數:91
中文關鍵詞:乙酸乙酯雙功能觸媒
外文關鍵詞:ethyl acetatebifunctional catalyst
相關次數:
  • 被引用被引用:2
  • 點閱點閱:277
  • 評分評分:
  • 下載下載:20
  • 收藏至我的研究室書目清單書目收藏:1
酯化/部份氧化雙功能Pd / SDB( styrene-divinyl benzene copolymer)觸媒可將含水酒精催化反應生成乙酸乙酯,部份氧化反應會造成鈀金屬的聚集,酯化反應從自發性乙酸解離再藉由質子催化產生,並且酸觸媒的加入有利於酯化反應的產生,反應後並沒有直接証據証明氧化反應發生是由於吸收氧氣形成Pd —O。此外,伴隨著Pd的濾取,我們發現會因此而增加鈀金屬的聚集,Pd-Pd配位數會從原來的3.0增加到7.9,且觸媒上鈀的含量從1.0 wt%減少到0.55 wt%,然而酸性觸媒如Amberlyst 15的加入,可改善此種情形,但仍無法達到我們的要求,因此我們發展出雙功能Pd / Zeolite觸媒。為了了解觸媒結構對催化性質的影響,我們應用了EXAFS (Extended X — Ray Absorption Fine Structure )對觸媒進行特性分析。為了往後的商業應用,我們對觸媒進行了長期老化及再生實驗,並且應用TGA (Thermal Gravity Analysis )及TPO(Temperature Programmed Oxidation)來尋找最佳的再生溫度,在進行了三個多月的長期老化實驗後,我們發現乙醇的轉化率仍可維持在58 %,而乙酸乙酯的選擇率仍可維持大約在90 %,這顯示觸媒在長時間的反應後仍可維持非常好的穩定性及活性,且再生後觸媒其活性才約略的下降而已。
Catalyzed by styrene-divinyl benzene copolymer (SDB)-supported Pd (Pd/SDB) catalysts, ethyl acetate can be formed from water-containing ethanol via concomitant partial oxidation and esterification reaction. The partial oxidation reaction is carried out over palladium clusters on the catalysts. The esterification reaction is catalyzed by protons formed from the spontaneous dissociation of acetic acid and can be enhanced by addition solid acid catalysts. After the reaction, there is no evidence of palladium oxide formation suggesting that the oxidation reaction takes place via the adsorbed oxygen. In addition, concomitantly with Pd leaching, increase of average Pd cluster size was observed. Pd-Pd coordination number increases from 3.0 to 7.9 and the Pd content decreases from 1.0 to 0.55 wt%. Addition of solid acid catalysts such as Amberlyst 15, slightly reduces leaching and growth of Pd clusters but the yield pattern of the solid-acid-promoted Pd/SDB catalyst system were still not satisfied. Therefore, zeolite supported metal catalysts with bifunctional catalytic properties were developed. In order to understand the relationship between structure and catalytic properties, EXAFS (Extended X — Ray Absorption Fine structure) spectroscopy was used to characterize the catalysts. For considering the utilization of the catalysts in commercial plant, aging tests were performed and then followed with regeneration experiments. TGA (Thermal Gravity Analysis ) and TPO ( Temperature Programmed Oxidation ) were used to investigate optimal regeneration temperature. The testing results indicated the catalysts present very good stability maintenance and the activity is only slightly loss after regeneration; after four months run the ethanol conversion still keep 58 % , and ethyl acetate selectivity also keep about 90 %.
第一章 緒論............................................1
1.1 乙酸乙酯簡介.......................................1
1.2 乙酸乙酯製程簡介...................................2
1.3 各製程比較.........................................5
1.4 研究目的...........................................6
第二章 觸媒、催化反應、特性分析.......................14
2.1 觸媒選擇..........................................14
2.2 藥品及氣體........................................15
2.3 反應設備..........................................15
2.4 觸媒床填充........................................16
2.5 實驗步驟及產物分析................................16
2.6 觸媒特性分析......................................18
第三章 實驗結果與討論.................................34
3.1 前言..............................................34
3.2 Pd / SDB之EXAFS特性分析...........................38
3.3 Pd — X / Zeolite與Pd / SDB +Amberlyst 15比較.....41
3.4 Pd / Zeolite之EXAFS特性分析.......................45
3.5 Pd — X / Zeolite 長期老化實驗....................48
3.6 觸媒再生..........................................51
第四章 總結與未來展望.................................86
1. 李秉傑、邱宏明、王亦凱,非均勻系催化原理與運用。
2. 鐘東霖,碩士論文, ”乙醇製造乙酸乙酯製程觸媒性能之改善”,民國八十六年。
3. 蘇世芳,碩士論文, ”以雙功能觸媒從乙醇製造乙酸乙酯”,民國八十七年。
4. 曾褔勝,碩士論文,”脂肪酯類製程之開發”,民國八十九年。
5. 劉繼中,碩士論文, ”媒裂汽油及柴油中含硫化合物之反應研究”,民國八十五年。
6. 同步輻射研究中心簡介,1992
7. 陳建德,同步幅射光源之應用,1996
8. Gurule, R. A., "Ethyl Acetate-United States", Chemical Economics Handbook, SRI International, 1988.
9. Chemical Marketing Reporter, 1998, avg(''98.1~''98.12)
10. Tishchenko, W., J. Russ. Phys. Chem. Soc., 38, 1906, p.398.
11. Dr. A. Wacker A.G., German Patents 579,566, 1932.
12. Dr. A. Wacker A.G., German Patents 733,884, 1943.
13. I. G. Farben A.G., German Patent 766027, 1942.
14. Keyes, D. B., Ind. Eng. Chem., 24, 1932, p.1096.
15. Inoue, K.; Iwasaki, M.; Matsui, K., U.S. Patent 5,241,106, 1993.
16. Larkins, T. H., U.S. Patent 4,886,905, 1989.
17. Larkins, T. H.; Tennant, B. A., U.S. Patent 4,471,136, 1984.
18. Lin, T. B.; Chung, D.-L.; and Chang, J.-R. “Ethyl Acetate Production from Water-Containing Ethanol Catalyzed by Supported Pd Catalysts: Advantages and Disadvantages of Hydrophobic Supports”, Ind. & Eng. Chem. Res., 1999, Revised.
19.Froment, G. F.; Bischoff, K. B. “Chemical Reactor Analysis and Design”; John Wiley And Sons: New York, 1988; pp198-218.
20.Gates, B. C. “Catalytic Chemistry”, John Wiley & Sons, Inc. p. 285, 1991.
21.Kwantes, A. and Gautier, P. A. U.S. Patnet, 4,191,843., 1980.
22. Jones , A. ; Mcnicol , B. , 1986 ,”Temperature — Programmed Reduction for Solid Materials Characterization” , marcel Dekker Inc. , p.70
23. Teo. B. — K ; Lee. P. A. J. Am. Chem. Suc. , 1979 , 101 , 11 , 2819.
24. Lin, T.-B.; Chung, K. T.; Tsai, K.-Y.; Chang, J.-R. “Process for Ethyl Acetate Production”,U.S. Patent 1998, 5,770,761.
25. van Zon, J. B. A. D. Extended X-ray Absorption Fine Sturcture Spectroscopy Design of a Spectrometer and Application to Rhodium Supported on Alumina Catalysts. Ph.D. Dissertation, Eindboven University of Technology, The Netherlands, 1988; p18
26. Kampers, F. W. H. EXAFS in Catalysis: Instrumentation and Application; Ph.D. Dissertation, Eindhoven University of Technology, The Netherlands, 1988; pp 32-39
27. Varrkamp, M. XDAP User’s Guide. XAFS Services International: The Netherlands, 1996.
28. Vaarkamp, M.; Miller, J. T.; Modica, F. S.; Lane, G. S.; Koningsberger, D. C. Sulfur Poisoning of a Pt/BaK-LTL Catalyst: A Catalystic and Structural Study Using Hydrogen Chemisorption and X-ray Absorption Spectrospcopy. J. Catal. 1992,138,675.
29. Chang, J. R.; Chang, S. L.; Lin, T. B. Alumina-Supported Pt Catalysts for Aromtics Reduction: A Structural Investigation of Sulfur-Poisoning Catalyst Deactivation . J. Catal. 1997,169,668.
30. Chang, J. R.; Jan, C. A.; Lin, T. B. Aromatics Reduction over Supported Platinum Catalysts.2. Improvement in Sulfur Resistance by Addition of Palladium to Supported Platinum Catalysts. 1995,34,4284.
31. Biloen, P,; Helle, J. N.; Verbeek, H.; Dautzenberg, F. M.; Sachtler, W. M. H. The Role of Rhenium and Sulfur in Platinum-Based Hydrocarbon-Conversion Catalysts. J. Catal. 1980, 63.112.
32. Dossi, C,; Tsang, C. M.; Satchtler, W. M. H. Reforming-Type Catalysts with Zeolite-Supported PtRe. Energy Fuels 1989, 3,468.
33. Gallezot, P. The State and Catalytic Properties of Platinum and Palladium in Faujasite-type Zeolites. Catal. Rev. Sci. Eng. 1979, 20(1),121.
34. Gallezot, P.; Bergeret, G. Catalyst Deactivation ; Peterson, E. E., Bell, A. T., Eds.; Dekker: New York, 1987; p 263.
35. Lee, J. F. ; Zheng, F. S. ; Chang, J. R. Structural Investigation of Solid — Acid — Promoted Pd / SDB Catalysts for Ethyl Acetate Production from Ethanol. J. Phys. Chem.B , 2001 , 105(17) , 3400-3404
36. Fung, S. C. Regenerating a Reforming Catalyst. CHEMTECH 1994, Jan, 40.
QRCODE
 
 
 
 
 
                                                                                                                                                                                                                                                                                                                                                                                                               
第一頁 上一頁 下一頁 最後一頁 top