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Low temperature NO adsorption over Pd-based catalysts for cold start application : 냉시동 적용을 위한 Pd 기반 촉매의 저온 NO흡장 능력

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dc.contributor.advisor김도희-
dc.contributor.author유영석-
dc.date.accessioned2018-11-12T00:58:02Z-
dc.date.available2018-11-12T00:58:02Z-
dc.date.issued2018-08-
dc.identifier.other000000152095-
dc.identifier.urihttps://hdl.handle.net/10371/143177-
dc.description학위논문 (박사)-- 서울대학교 대학원 : 공과대학 화학생물공학부, 2018. 8. 김도희.-
dc.description.abstractThe abatement of NOx arising from automobiles becomes an important societal problem due to detrimental effect on human health and environment. Therefore, global regulations on NOx emission have been continuously issued and reinforced. To fulfill the legislations, various NOx reduction technologies such as three-way catalysis (TWC), selective catalytic reduction (SCR), and NOx storage reduction (NSR) systems have been successfully developed and applied. Among them, SCR and NSR have been adapted to address NOx

emission in diesel engines. However, both systems require high temperature (above 200 °C) to acquire proper NOx reduction efficiency. Recently, in order to control the NOx emission during cold start, low temperature NO adsorption materials, namely, cold start catalysts (CSC) or passive NOx adsorbers (PNA) having the ability of storing NOx at low temperature and releasing them at high temperature where SCR and NSR properly operate draw significant attention.

To have proper function as the low temperature NO adsorption catalyst, it must have not only catalytic ability (such as high NO storage capacity and proper NOx desorption temperature) but also durability under diesel exhaust conditions. In this work, various materials such as PGM(active metal), metal-oxide and zeolite(support) were investigated to identify the possibility for the low temperature NO adsorption catalyst. Especially, to evaluate the potential for the practical application of catalyst, exhaust gas conditions (such as

hydrothermal aging and sulfur aging) causing catalytic deactivation were applied.

At first, hydrothermally aged Pd/CeO2 was employed for NO adsorption at low temperature (80 – 160 °C). For comparison, Pt or Pt-Pd supported on CeO2 or Al2O3 catalysts were also evaluated. Analysis of the hydrothermally aged catalysts clearly demonstrate that Pt and/or Pd on CeO2 is more resistant to sintering than that on Al2O3 support. NO adsorption/desorption results indicate that CeO2-based catalysts have superior NO adsorption ability than Al2O3-based catalysts. In addition, PGM/CeO2 catalysts exhibit the desirable desorption temperature for cold start application. DRIFT spectra of adsorbed NOx species on Pd/CeO2 during NO adsorption/desorption demonstrate that NOx desorption peaks at 250, 300, and 450 °C derive from weakly bound nitrite, nitro-nitrito species, and nitrate species, respectively. Based on the activity test and characterization, it can be mentioned that Pd in Pd/CeO2 plays an important role in generating additional NO adsorption site arising from the interaction between Pd and CeO2 and helping the oxidation from adsorbed nitrite to nitrate. Therefore, Pd/CeO2 can be a good candidate as low temperature NO adsorption catalyst for cold start application.

Next, to investigate the effect of sulfur aging (SA) and regeneration (DeSOx) on the changes in NO adsorption ability and physicochemical properties of catalysts, both treatments were applied to Pd/CeO2 and Pd/Ce0.58Zr0.42O2 (Pd/Ce58) catalysts. SA treatment on both catalysts leads to the negligible NO

adsorption ability since it gives rise to form thermodynamically more stable Ce(SO4)2 than adsorbed NOx species. Structural and textural analysis after regeneration treatment exhibits that Pd/Ce58 maintains the crystalline size with similar pore size distribution, while Pd/CeO2 does not. In addition, the former

sample recovers its own Pd distribution after regeneration, although the latter does not. However, the fact that both regenerated catalysts do not restore the NO adsorption ability to the level of HTA ones indicates that either textural property or Pd dispersion cannot account for the deterioration of NO adsorption ability after sulfur aging and regeneration. Instead, H2-TPR analysis on both samples indicates that the intimate interaction between Pd and ceria is disappear after regeneration, as proved by the absence of the simultaneous reduction of CeO2 and PdO below 20 °C. Hence, it can be concluded that the sulfur aging and the subsequent regeneration has negative effect on the interaction between PdO and CeO2, resulting in the irreversible degradation in the NO adsorption ability at low temperature. This result implies that the application of Pd/Ce based catalyst to practical condition is difficult.

To obtain the hydrothermal stability and sulfur resistance, zeolite-based catalyst was employed. Fresh Pd/SSZ-13 did not possess good NO adsorption capacity irrespective of the preparation methods such as incipient wetness impregnation, wet impregnation, ion-exchange, and solid state ion exchange. However, after hydrothermal aging (HTA) treatment, Pd/SSZ-13 could obtain enhanced NO adsorption ability at low temperature, which will be suitable for the application of cold start catalyst. H2-TPR and XAFS results clearly indicate that PdO mainly existed over the fresh sample, while HTA treated sample contained ionic Pd species, demonstrating the redistribution of PdO into highly dispersed ionic Pd species within the SSZ-13 structure arising from HTA treatment. DRIFT results display the formation of two nitrosyl complexes adsorbed on Pd2+ ions, which are directly related to two desorption peaks of NOx at 250 and 400 °C. All combined results provide the unambiguous evidence about the generation of Pd ions in SSZ-13 zeolite induced by HTA

treatment, which play as the active sites for NO adsorption at low temperature.
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dc.description.tableofcontentsContents

Abstract.......................................................................................................................i

List of Tables............................................................................................................... viii

List of Figures ............................................................................................................. ix

Chapter 1. Introduction .............................................................................................. 1

1.1. Diesel vehicle exhaust and exhaust gas purification system....................................1

1.2. Cold start catalyst for low temperature NO adsorption ......................................... 4

1.3. Objectives............................................................................................................ 7

Chapter 2. Low temperature NO adsorption ability over hydrothermally aged

PGM/metal-oxide catalysts for cold start application ................................................... 9

2.1. Introduction ........................................................................................................ 9

2.2. Experimental....................................................................................................... 12

2.2.1. Catalysts preparation........................................................................................ 12

2.2.2. Catalyst characterizations .................................................................................12

2.2.3. Activity measurement for the adsorption/desorption of NO................................14

2.3. Result & discussion...............................................................................................16

2.3.1. Structural properties and CO-chemisorption..................................................... 16

2.3.2. Low temperature NO adsorption ...................................................................... 21

2.3.2.1. Adsorption/desorption of NO on various catalysts ......................................... 21

2.3.2.2. Effect of adsorption time on the adsorption/desorption of NO on

Pd/CeO2 ................................................................................................................... 30

2.3.2.3. Effect of gas mixture on the adsorption/desorption of NO on

Pd/CeO2 ................................................................................................................... 33

2.3.3. DRIFT results during the adsorption/desorption of NO on Pd/CeO2 36

Chapter 3. Effect of sulfur poisoning and regeneration on NO adsorption ability

over Pd/Ce-based catalysts......................................................................................... 44

3.1. Introduction ....................................................................................................... 44

3.2. Experimental....................................................................................................... 46

3.2.1. Catalysts preparation........................................................................................ 46

3.2.2. Catalysts characterizations................................................................................. 47

3.2.2. NO adsorption/desorption activity..................................................................... 49

3.3. Result & discussion............................................................................................... 50

3.3.1. Low temperature NO adsorption/desorption activity of Pd/CeO2 and

Pd/Ce58...................................................................................................................... 50

3.3.2. Characterization of Pd/CeO2 and Pd/Ce58 with various treatments................... 58

3.3.2.1. XPS and FTIR analysis..................................................................................... 58

3.3.2.2. XRD and BET................................................................................................. 62

3.3.2.3. CO-chemisorption and H2-TPR ..................................................................... 67

Chapter 4. Activation of Pd/SSZ-13 by hydrothermal aging treatment for low

temperature NO adsorption........................................................................................ 73

4.1. Introduction ....................................................................................................... 73

4.2. Experimental....................................................................................................... 76

4.2.1. Catalysts preparation........................................................................................ 76

4.2.2. Catalysts characterizations................................................................................ 77

4.2.3. NO adsorption activity ..................................................................................... 80

4.3. Results................................................................................................................ 82

4.3.1. Low temperature NO adsorption over various Pd/SSZ-13 catalysts ................... 82

4.3.2. XRD and NMR ................................................................................................ 89

4.3.3. H2-TPR and XPS ............................................................................................. 94

4.3.4. XAFS and STEM............................................................................................... 99

4.3.5. DRIFT result during NO adsorption/desorption of HTA Pd(2)/SSZ-13

................................................................................................................................ 106

4.3.6. CO-DRIFT results for fresh and HTA samples................................................... 109

4.3.7. Sulfur aging effect on NO adsorption ability over HTA Pd/SSZ-13.....................111

4.4. Discussion..........................................................................................................114

4.4.1. The change in Pd species during HTA treatment..............................................114

4.4.2. The effect of Pd ion exchange methods on the physicochemical state of

Pd/SSZ-13.................................................................................................................116

4.4.3. The limit of Pd ion exchange in SSZ-13 by HTA treatment................................118

4.4.4. The effect of hydrothermal treatment on Pd/SSZ-13 ...................................... 121

Summary and Conclusions....................................................................................... 124

Bibliography ........................................................................................................... 127

국 문 초 록 ............................................................................................................... 136
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dc.language.isoen-
dc.publisher서울대학교 대학원-
dc.subject.ddc660.6-
dc.titleLow temperature NO adsorption over Pd-based catalysts for cold start application-
dc.title.alternative냉시동 적용을 위한 Pd 기반 촉매의 저온 NO흡장 능력-
dc.typeThesis-
dc.description.degreeDoctor-
dc.contributor.affiliation공과대학 화학생물공학부-
dc.date.awarded2018-08-
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