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Ardizzi et al. 81procedure described in (7), and having an Al/P atomic ratio equal to 0.74. Catalytictests in the gas phase have been performed in a tubular flow glass reactor. Thefollowing reaction conditions were used: (a) with the H-mordenite and AlF 3catalysts, catechol/methanol 1/10 molar ratio, residence time 0.6 s for the total feedflow, including N 2 as the carrier gas (0.1 l/min). (b) with the AlPO 4 catalyst,catechol/methanol 1/3.4 molar ratio, residence time 7.5 s.100Conversion, selectivity, %selectivity to Guaiacol806040Catechol conversion20Selectivity to Methylcatechol + Veratrol0220 230 240 250 260 270 280Temperature, °CFigure 3. Catechol conversion, selectivity to guaiacol and to methylcatechol +veratrol as functions <strong>of</strong> temperature. Catalyst Al/P/O. Feed: catechol and methanol(1/3.4 molar feed ratio).References1. P. Marion, R. Jacquot, S. Ratton and M. Guisnet, Zeolites for CleanerTechnologies, M. Guisnet and J.-P. Gilson, Eds., ICP, London, p. 281. 20022. P. Métivier, Fine Chemicals through Heterogeneous <strong>Catalysis</strong>, R.A. Sheldonand H. van Bekkum, Eds., Wiley-VCH, p. 161 and 173. 20013. M. Marczewski, J.-P. Bodibo, G. Perot and M. Guisnet, J. Mol. Catal., 50, 211(1989).4. S. Balsamà, P. Beltrame, P.L. Beltrame, P. Carniti, L. Forni and G. Zuretti,Appl. Catal., 13, 161 (1984).5. R.F. Parton, J.M. Jacobs, D.R. Huybrechts and P.A. Jacobs, Stud. Surf. Sci.Catal., 46, 163 (1989).6. F.M. Bautista, J.M. Campelo, A. Garcia, D. Luna, J.M. Marinas and A.A.Romero, Appl. Catal., 96, 175 (1993).7. F. Cavani, T. Monti, P. Panseri, B. Castelli and V. Messori, WO Pat. 74,485, toBorregaard Italia (2001).
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Catalysis ofOrganic Reactions
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14. Catalyst Manufacture: Laborator
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62. Catalysis of Organic Reactions,
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108. Metal Oxides: Chemistry and Ap
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CRC PressTaylor & Francis Group6000
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xiii14. The Transformation of Light
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xviien Catalisis y Petroquimica (UN
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xix56. Transition Metal Removal fro
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xxiiiChronology of Organic Reaction
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To Zsuzsanna and Tim
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Jones et al. 31. On the Use of Immo
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Jones et al. 5three-phase tests in
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Jones et al. 7In the HKR of rac-epi
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Jones et al. 9term performance char
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Jones et al. 115. A. S. Gruber, D.
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Moses et al. 132. Supported Re Cata
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Moses et al. 15perrhenate, followed
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Moses et al. 17SnCOSnMe 4≡SiOReO
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Moses et al. 19(AlOSi) of the cube.
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Moses et al. 212.510 3 k obs / s -1
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Wang et al. 233. Catalytic Hydrogen
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Wang et al. 25The rate expressions
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Wang et al. 27Schiff’s base forma
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Wang et al. 29AcknowledgementsWe gr
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Page 61 and 62: 34Halophosphite LigandsThe ligands,
Page 63 and 64: 36Halophosphite LigandsTable 2 Temp
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Page 72 and 73: Gőbölös et al. 456. Highly Selec
Page 74 and 75: Gőbölös et al. 47was practically
Page 76 and 77: Gőbölös et al. 49noteworthy that
Page 78 and 79: Gőbölös et al. 51Figure 2 NMR sp
Page 80: Gőbölös et al. 53internal TMS in
Page 83 and 84: 56Hydrotalcite-like Catalysts[A n-
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Page 95 and 96: 68Synthesis of MIBKwe examined the
Page 97 and 98: 70Synthesis of MIBK1412Conversion (
Page 99 and 100: 72Synthesis of MIBK4,4’-dimethyl
Page 101 and 102: 74Synthesis of MIBKobtained for MIB
Page 104 and 105: Ardizzi et al. 7710. The Control of
Page 106 and 107: Ardizzi et al. 79type acidity at th
Page 110 and 111: Ardizzi et al. 8311. The Environmen
Page 112 and 113: Ardizzi et al. 85the selectivity to
Page 114: Ardizzi et al. 87Experimental Secti
Page 118 and 119: Hu et al. 9112. Biphasic Catalytic
Page 120 and 121: Hu et al. 93Results and DiscussionM
Page 122 and 123: Hu et al. 95ionic liquid is used in
Page 124 and 125: Hu et al. 97Figure 4. Schematic flo
Page 126 and 127: Singh and Chuang 9913. Reaction Pat
Page 128 and 129: Singh and Chuang 101for O 2 , 40 fo
Page 130 and 131: Singh and Chuang 103537373650Temp (
Page 132 and 133: Singh and Chuang 1050.064m/e = 32 (
Page 134 and 135: Singh and Chuang 107In summary, hyd
Page 136 and 137: Bacchini et al . 10914. The Transfo
Page 138 and 139: Bacchini et al . 1111 summarizes th
Page 140 and 141: Bacchini et al . 113these samples h
Page 142 and 143: Bacchini et al . 115around 1. The d
Page 144 and 145: Bacchini et al . 117Experimental Se
Page 146 and 147: Tanielyan et al. 11915. Transition
Page 148 and 149: Tanielyan et al. 121We wish to repo
Page 150 and 151: Tanielyan et al. 123Fig 1a shows th
Page 152 and 153: Tanielyan et al. 125TEMPO concentra
Page 154 and 155: Tanielyan et al. 127complete conver
Page 156 and 157: Tanielyan et al. 129ConclusionsIt h
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Liu, Cant and Smith 13116. The Conv
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Liu, Cant and Smith 133calculated f
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Liu, Cant and Smith 135Table 3. App
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Liu, Cant and Smith 137noting that
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Liu, Cant and Smith 139an exact fit
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Tanielyan et al. 14117. Bromine-Fre
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Tanielyan et al. 143TEMPO catalyst,
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mmol),Tanielyan et al. 145catalyst.
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Miller and Chuang 14718. In situ In
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Miller and Chuang 1492(a)2359217516
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Miller and Chuang 151(a)33802973292
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III. Symposium on Catalytic Hydroge
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156 Raney® Metastable PrecursorsIn
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158 Raney® Metastable Precursorsfe
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160 Raney® Metastable Precursorssl
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162 Raney® Metastable Precursorsfu
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164 Raney® Metastable Precursorsva
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Gelder, Jackson and Lok 16720. Comp
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Gelder, Jackson and Lok 169hydrogen
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Gelder, Jackson and Lok 171more rap
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Gelder, Jackson and Lok 173and that
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Gelder, Jackson and Lok 175measured
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Nikoshvili et al . 17721. Selective
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Nikoshvili et al . 179Experimental
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Nikoshvili et al . 181gasometrical
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Nikoshvili et al . 183causes the se
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Nikoshvili et al . 185determined th
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Salmi et al. 18722. Modeling and Op
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Salmi et al. 189andn−1( ) ( 1)) 1
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Salmi et al. 191dci= Niap− NGLiaG
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Salmi et al. 193of adsorption and t
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Salmi et al. 195Notationaa pa GLAcd
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Ostgard et al . 19723. The Effects
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Ostgard et al . 199not the ionic sa
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Ostgard et al . 201-2-0,9 -0,7 -0,5
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Ostgard et al . 2032,22Figure 8 NiM
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Ostgard et al . 205Max Act., mol/(m
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Ostgard et al . 207Flat Adsorbtion
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Ostgard et al . 209product mixture.
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Ostgard et al . 2116. M. Makkee, A.
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214 Cavitating Ultrasound Hydrogena
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228 Hydrogenation of Pynitrilesuch
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230 Hydrogenation of Pynitrile%Sele
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232 Hydrogenation of Pynitrile%Sele
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234 Hydrogenation of Pynitrile10. A
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236Deactivation of Catalyst in Suga
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238Deactivation of Catalyst in Suga
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Jackson and Spence 24127. Selectivi
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Jackson and Spence 243been related
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Jackson and Spence 245Acknowledgeme
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248Homogeneous Hydrogenationthe pre
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250Homogeneous Hydrogenationmetal s
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252Homogeneous Hydrogenation2. R. R
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254 Amination of Isobutanolnotewort
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256 Amination of Isobutanoland (iBu
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259IV. Symposium on Novel Methods i
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262Find the Best Catalystquantitati
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264Find the Best CatalystSTARTcreat
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266Find the Best CatalystNHNPNO NNC
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268Find the Best CatalystFigure 4.
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270Find the Best Catalyst14. For a
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272 Acidic Ionic LiquidsThe effect
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274 Acidic Ionic Liquidssites for H
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276 Acidic Ionic Liquids102.2 ppm 9
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278 Acidic Ionic LiquidsClClClClClC
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280 Acidic Ionic Liquids9. E. J. An
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282 Chemoselective Hydrogenationthe
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284 Chemoselective HydrogenationThe
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286 Chemoselective HydrogenationCNN
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288 Chemoselective Hydrogenation11.
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290 Hydrogenolysis over Structured
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Pugin et al. 29334. Twinphos: A New
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Pugin et al. 295ferrocene binding m
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Pugin et al. 297complexes with one
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Pugin et al. 2993: 50.1 (J pp =50 H
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Pugin et al. 301temperature, then t
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Margitfalvi et al. 30335. Catalyst
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Margitfalvi et al. 305Based on the
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Margitfalvi et al. 307Table 1. Vari
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Margitfalvi et al. 309Combination o
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Margitfalvi et al. 311Figure 1. Map
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Margitfalvi et al. 313Acknowledgeme
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Auten, Crump, Singh and Chandler 31
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Falling et al. 32737. Development o
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Falling et al. 329With these proces
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Falling et al. 331salt, TOP18 has v
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Falling et al. 333The catalyst syst
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Falling et al. 335Normal operation
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Bianchi, Borzatta, Poluzzi and Vacc
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Griffin, Johnston, Prétôt and van
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356Synthesis of PseudoiononesOOO- H
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358Synthesis of PseudoiononesMgO Pe
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360Synthesis of Pseudoionones0.5 wt
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362Synthesis of PseudoiononesTable
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364Synthesis of Pseudoiononesstrong
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366 MIBK Synthesis via CDproduce me
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368 MIBK Synthesis via CDExperiment
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370 MIBK Synthesis via CDreboiler p
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372 MIBK Synthesis via CDIn MIBK, t
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374 MIBK Synthesis via CDConclusion
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Sanders et al. 37742. Producing Pol
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Sanders et al. 379For the purposes
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Sanders et al. 381corresponding alc
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Sanders et al. 383polyurethane foam
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Zoeller and Barnette 38543. Carbony
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Zoeller and Barnette 387The first s
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Zoeller and Barnette 389Material ac
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Zoeller and Barnette 391above 120°
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Zoeller and Barnette 393tributyl am
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Hallett, Pollet, Eckert and Liotta
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Kiss, Rothenberg and Dimian 40545.
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Kiss, Rothenberg and Dimian 407C 10
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Kiss, Rothenberg and Dimian 409Tabl
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Kiss, Rothenberg and Dimian 411X (m
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Kiss, Rothenberg and Dimian 413Prep
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Snåre et al. 41546. Continuous Deo
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Snåre et al. 417The production of
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Snåre et al. 419was 15 μm and the
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Snåre et al. 421to 13% of conversi
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Snåre et al. 423Ethyl stearate con
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Snåre et al. 425increase in the fo
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428Glycerol Hydrogenolysisfundament
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430Glycerol Hydrogenolysisreaction
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432Glycerol Hydrogenolysisexpense o
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434Glycerol Hydrogenolysis[GO], M1.
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436Glycerol HydrogenolysisReference
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438Sustainable Process Technologyth
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440Sustainable Process Technologyco
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442Sustainable Process Technologywi
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444Sustainable Process TechnologyTh
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Lee, Shi, Subramaniam and Busch 447
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VII. Symposium on Other Topics in C
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...456Chiral BisphospholanesToday,
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458Chiral BisphospholanesFirst, the
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460Chiral BisphospholanesInterestin
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Augustine, Tanielyan, Marin and Alv
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Knifton and Sanderson 46952. Select
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Knifton and Sanderson 4711414141413
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Knifton and Sanderson 4733. O. C. A
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476 Palladium LeachingResults and D
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478 Palladium Leachingtemperatures
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Arunajatesan, Cruz, Möbus and Chen
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488Profiling of Catalytic Performan
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494 Transition Metal Removalmetal r
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496 Transition Metal RemovalDeloxan
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498 Transition Metal Removalreduced
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Durán Pachón and Rothenberg 50157
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Durán Pachón and Rothenberg 503th
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Durán Pachón and Rothenberg 505Ac
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508Author IndexDíez Verónica K. 4
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510Author IndexPhillips Gerald W. 3
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Catalysis of Organic Reactions 513K
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Catalysis of Organic Reactions 515c
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Catalysis of Organic Reactions 517h
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Catalysis of Organic Reactions 519p
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