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研究生:蘇崇毅
研究生(外文):Chung- Yi Su
論文名稱:蜂巢狀波洛斯凱特觸媒用於合成氣燃燒反應之研究
論文名稱(外文):Study on the Activities of Honeycomb-supported Perovskite Catalysts for Syngas combustion
指導教授:翁鴻山翁鴻山引用關係
指導教授(外文):Hung-Shan Weng
學位類別:碩士
校院名稱:國立成功大學
系所名稱:化學工程學系碩博士班
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:2007
畢業學年度:95
語文別:中文
論文頁數:123
中文關鍵詞:Mars-Van Krevelen model甲烷燃燒Perovskite觸媒蜂巢狀觸媒
外文關鍵詞:Methane combustionMars-Van Krevelen modelMonolith catalystsPerovskite-type catalyst
相關次數:
  • 被引用被引用:8
  • 點閱點閱:231
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  • 收藏至我的研究室書目清單書目收藏:0
本研究是以研製高效能奈米級波洛斯凱特型(Perovskite-type)觸媒,用於合成氣燃燒為目標。採用檸檬酸溶膠凝膠法製備LaCoO3,用於甲烷燃燒反應;並以多種金屬部份取代La與Co對觸媒進行改質,期能提高其催化活性。在篩選出活性較佳的改質觸媒後,進行觸媒穩定性測試及動力學實驗,並求出甲烷燃燒反應之速率表示式。研究中,也藉由觸媒表面性質之鑑定(BET、XRD、SEM及TEM等),以瞭解觸媒之表面性質與觸媒活性間之關聯性。最後將篩選出活性最佳的波洛斯凱特型觸煤,披覆在蜂巢狀金屬和陶瓷載體上(事先以溶膠凝膠披覆一層γ-Al2O3)上,製成蜂巢狀擔體觸媒。
觸媒篩選的結果,發現活性最佳的觸媒是La0.7Ce0.3Co0.6Mn0.4O3,它可在約275℃讓甲烷起燃,CO的點燃溫度約在100℃,H2的點燃溫度約在125℃,合成氣各成份氣體在此觸媒的反應性為:CO>H2>CH4。製備觸媒時最適煅燒溫度是700℃。穩定性測試顯示,該觸媒在高溫或低溫皆具有良好的穩定性。觸媒的活性不會因為生成物的產生及積碳而造成觸媒活性衰退。由混合氣體之反應測試,發現CH4的轉化率會因CO或H2的存在而略為下降。也發現低濃度的硫化氫會使La0.7Ce0.3Co0.6Mn0.4O3此種觸媒產生毒化,且是不可逆的反應。將波洛斯凱特型觸媒(La0.7Ce 0.3Co0.6Mn0.4O3)擔載在蜂巢狀陶瓷上,披覆重量約為陶瓷擔體的2.6 %,厚度約為10 μm,製得之蜂巢狀陶瓷擔體觸媒在約400℃可將甲烷起燃。
利用微分型反應器,以La0.7Ce 0.3Co0.6Mn0.4O3觸媒進行甲烷氧化反應,評估動力模式之適用性。結果發現當氧氣過量時,Mars-Van Krevelen模式適合描述甲烷之氧化反應,根據該模式可推導出甲烷氧化反應之速率表示式:
r=(KRCCH4KOCO2)/(2KRCCH4+KOCCO2)
KR = 4.46×105 exp (-72.3/RT);Ea = 72.3 KJ/mol
KO = 3.80×105 exp (-79.1/RT);Ea = 79.1 KJ/mol
The main objective of this research is to prepare high efficiency perovskite-type catalysts for syngas combustion. With the aim of improving catalyst activity, we prepared lanthanum cobaltite LaCoO3 powders via the so called “citric-acid sol-gel method “, and investigated the influence of substituting of several kinds of metals in LaCoO3 perovskite on the activity towards the catalytic combustion of methane. After finding the best one for methane combustion, a kinetic study for finding an appropriate rate expression and stability test were carried out. In order to understand the correlation between physical properties and activities, catalysts were characterized by BET, XRD, SEM, and TEM. Finally, the best perovskite catalyst was washcoated on the cordierite and metallic honeycomb monoliths and their performances were compared.
Experimental results reveal that the best perovskite for methane combustion is La0.7Ce0.3Co0.6Mn0.4O3 catalysts, and the light-off temperature for CH4, CO, and H2 are 275℃, 100℃, and 125℃, respectively. Therefore, the activities of this catalyst for the components of syngas is in the order of CO>H2>CH4. The optimal calcination temperature for this catalyst is 700℃. And the stability test shows that this catalyst has a good durability no matter at high or low temperatures. The catalyst would not be deactivated by the production of the products and coke deposition in the reaction. Addition of H2 and CO to the feed slightly inhibited the activity of catalyst for methane combustion. In addition, this catalysts are poison-sensitive to low concentration of H2S in the feed. When the cordierite and metallic monolith were coated with perovskite catalyst (La0.7Ce0.3Co0.6Mn0.4O3), the loading percentages of active species, based on monolithic support, was about 2.6 %, and the thickness was about 10 μm. The light-off temperature of methane combustion over both honeycomb monoliths coated with perovskite catalysts is 400℃.
The oxidation kinetics of methane over La0.7Ce0.3Co0.6Mn0.4O3 catalyst was carried out in a differential reactor. The results show that the Mars–Van Krevelen model could satisfactorily fit the experimental kinetic data when excess oxygen was utilized. The rate expression of methane combustion derived from this model is as follows:
r=(KRCCH4KOCO2)/(2KRCCH4+KOCCO2)
KR = 4.46×105 exp (-72.3/RT);Ea = 72.3 KJ/mol
KO = 3.80×105 exp (-79.1/RT);Ea = 79.1 KJ/mol
中文摘要 I
ABSTRACT III
目錄 V
圖目錄 IX
表目錄 XII
第一章 序論 1
1-1 前言 1
1-2 研究動機與目的 4
第二章 文獻回顧 6
2-1 觸媒燃燒基本原理 6
2-2-1 貴金屬觸媒 9
2-2-2 金屬氧化物觸媒 11
2-2-3 Perovskite觸媒 12
2-3 蜂巢狀觸媒 20
2-3-1蜂巢狀陶瓷載體 (Ceramic monolith) 21
2-3-2 蜂巢狀金屬載體(Metallic monolith) 22
2-3-4 蜂巢狀觸媒用於甲烷燃燒 26
第三章 觸媒之製備與實驗步驟 29
3.1 藥品與材料 29
3.2儀器設備 30
3-3 PEROVSKITE金屬氧化物觸媒粉末之製備 32
3-4蜂巢狀PEROVSKITE觸媒製備 34
3-4-1蜂巢狀陶瓷載體 34
3-4-2蜂巢狀金屬載體 37
3-5 觸煤物理性質分析 40
第四章 觸媒物性鑑定 42
4-1 熱重分析(TGA)與熱差分析(DTA) 42
4-2 BET等溫物理吸附分析 44
4-3 XRD繞射分析 53
4-4 SEM與EDAX分析 65
第五章 觸媒反應性能測試 74
5-1實驗設備與裝置 74
5-2 觸媒活性測試 79
5-2-1甲烷轉化之空白實驗 79
5-2-2 不同A’金屬部份取代La對La-Co系列觸媒活性的影響 79
5-2-3 Ce部份取代La對La-Co系列觸媒活性的效應 80
5-2-4 不同B’金屬取代Co對觸媒(La0.7Ce 0.3Co0.4B’0.6O3)活性影響 80
5-2-5 Mn部份取代Co對觸媒(La0.7Ce 0.3Co1-yMnyO3)活性的效應 81
5-2-6 煅燒溫度對觸媒(La0.7Ce 0.3Co0.6Mn0.4O3)活性的影響 82
5-2-7混合氣體之燃燒反應測試 82
5-2-8 La0.7Ce0.3Co0.6Mn0.4O3觸媒之穩定性測試 83
5-2-9 La0.7Ce0.3Co0.6Mn0.4O3觸媒之抗硫毒化測試 84
5-2-11 蜂巢狀觸媒之甲烷燃燒反應測試 85
5-2-12蜂巢狀觸媒長度對甲烷轉化率的影響 86
第六章 甲烷燃燒之動力學實驗 98
6-1實驗方法 98
6-2 動力學模式的選擇 99
6-3觸媒動力學實驗 103
6-3-1外質傳阻力測試 103
6-3-3 動力學適用性評估 105
6-3-4動力學模式參數之求取 111
6-3-5 模式預測值與實驗值之比較 112
第七章 總結 117
7-1結論 117
7-2 未來研究方向與建議 118
參考文獻 119
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