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80052040105
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H-1031 Budapest, Zahony u.7., Hungary
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ThalesNano Nanotechnology Inc., Graphisoft Park, H-1031 Budapest, Zahony u.7., Hungary. http://www.ThalesNano.com.
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Graphisoft Park
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6
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31544463062
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Continuous-flow high pressure hydrogenation reactor for optimization and high-throughput synthesis
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Jones, R. V.; Godorhazy, L.; Varga, N.; Szalay, D.; Urge, L.; Darvas, F. J. Comb. Chem. 2006, 8, 110-116. doi:10.1021/cc050107o (Pubitemid 43166089)
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Journal of Combinatorial Chemistry
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Jones, R.V.1
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Urge, L.5
Darvas, F.6
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7
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A novel method for high-throughput reduction of compounds through automated sequential injection into a continuous-flow microfluidic reactor
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DOI 10.1002/qsar.200540006
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Jones, R.; Gödörházy, L.; Szalay, D.; Gerencsér, J.; Dormán, G.; Ürge, L.; Darvas, F. QSAR Comb. Sci. 2005, 24, 722-727. doi:10.1002/qsar.200540006 (Pubitemid 41191994)
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Jones, R.1
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Darvas, F.7
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8
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Knudsen, K.R.1
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Oakley Road, Chinnor, Oxfordshire, OX39 4TW, UK
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Aitken Scientific Ltd, Sanderum House, Oakley Road, Chinnor, Oxfordshire, OX39 4TW, UK, http://www.aitken-sci.com.
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Sanderum House
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10
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38849197788
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Clapham, B.; Wilson, N. S.; Michmerhuizen, M. J.; Blanchard, D. P.; Dingle, D. M.; Nemcek, T. A.; Pan, J. Y.; Sauer, D. R. J. Comb. Chem.2008, 10, 88-93. doi:10.1021/cc700178a
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Nemcek, T.A.6
Pan, J.Y.7
Sauer, D.R.8
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Irfan, M.; Petricci, E.; Glasnov, T. N.; Taddei, M.; Kappe, C. O. Eur. J. Org. Chem. 2009, 1327-1334. doi:10.1002/ejoc.200801131
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Irfan, M.1
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Kappe, C.O.5
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12
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21444450169
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The use of a continuous flow-reactor employing a mixed hydrogen-liquid flow stream for the efficient reduction of imines to amines
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DOI 10.1039/b504854k
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Saaby, S.; Knudsen, K. R.; Ladlow, M.; Ley, S. V. Chem. Commun. 2005, 2909-2911. doi:10.1039/b504854k (Pubitemid 40917033)
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Chemical Communications
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Saaby, S.1
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77955972853
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Cserényi, S.; Szollosi, G.; Szori, K.; Fülöp, F.; Bartók, M. Catal. Commun. 2010, 12, 14-19. doi:10.1016/j.catcom.2010.08. 008
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Cserényi, S.1
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Bartók, M.5
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14
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80052076668
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Kappe reported a 92% yield of ethyl piperidine-3-carboxylate from ethyl pyridine-3-carboxylate, using the H-Cube®, with substrate concentration 0.05 M in AcOH, Pt/C, at 100 bar, H2 controlled mode setting, at 100 °C, and 0.5 mL/min flow rate. We were unable to reproduce those conditions due to stabilization issues. By changing the solvent to 0.5 M AcOH in EtOH, we achieved 100% conversion in the full mode (0.05 M substrate, 10% Pt/C, 100 °C, 0.5 mL/min). Repeating our modified conditions at 100 bar in the H2 controlled mode reduced the conversion to 78%
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Kappe reported a 92% yield of ethyl piperidine-3-carboxylate from ethyl pyridine-3-carboxylate, using the H-Cube®, with substrate concentration 0.05 M in AcOH, Pt/C, at 100 bar, H2 controlled mode setting, at 100 °C, and 0.5 mL/min flow rate. We were unable to reproduce those conditions due to stabilization issues. By changing the solvent to 0.5 M AcOH in EtOH, we achieved 100% conversion in the full mode (0.05 M substrate, 10% Pt/C, 100 °C, 0.5 mL/min). Repeating our modified conditions at 100 bar in the H2 controlled mode reduced the conversion to 78%.
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15
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80052075620
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Eschelbach, J. W. manuscript in progress
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Eschelbach, J. W. manuscript in progress.
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16
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80052071742
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Personal communication with Richard V. Jones of ThalesNano
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Personal communication with Richard V. Jones of ThalesNano.
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18
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67650099411
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doi:10.1016/j.apcata.2009.06.003
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van Herk, D.; Castaño, P.; Quaglia, M.; Kreutzer, M. T.; Makkee, M.; Moulijn, J. A. Appl. Catal., A 2009, 365, 110-121. doi:10.1016/j.apcata. 2009.06.003
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Van Herk, D.1
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Makkee, M.5
Moulijn, J.A.6
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19
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27744595150
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van Herk, D.; Kreutzer, M. T.; Makkee, M.; Moulijn, J. A. Catal. Today 2005, 106, 227-232. doi:10.1016/j.cattod.2005.07.180
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67651174615
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van Herk, D.; Castaño, P.; Makkee, M.; Moulijn, J. A.; Kreutzer, M. T. Appl. Catal., A 2009, 365, 199-206. doi:10.1016/j.apcata.2009.06.010
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Van Herk, D.1
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Moulijn, J.A.4
Kreutzer, M.T.5
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21
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80052050334
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The AutoH3 system was washed by replacing the solvent reservoirs (at both the Gilson and the Knauer pump) with wash solvent, then injecting 1.9 mL wash solvent through each CatCart Changer™ port position (quartz CatCart® cartridges), sequentially, and collecting 10 mL of wash solvent per injection
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The AutoH3 system was washed by replacing the solvent reservoirs (at both the Gilson and the Knauer pump) with wash solvent, then injecting 1.9 mL wash solvent through each CatCart Changer™ port position (quartz CatCart® cartridges), sequentially, and collecting 10 mL of wash solvent per injection.
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22
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80052075244
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The SAH3 system was washed by replacing the solvent reservoir with wash solvent and installing a 30 mm quartz CatCart® in the holder. Wash solvent was pumped at a rate of 1.0 mL/min for 10-40 min per solvent, with the system set to the full H2 mode at 30 °C
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The SAH3 system was washed by replacing the solvent reservoir with wash solvent and installing a 30 mm quartz CatCart® in the holder. Wash solvent was pumped at a rate of 1.0 mL/min for 10-40 min per solvent, with the system set to the full H2 mode at 30 °C.
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23
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80052065448
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Back-flushing was performed by plumbing directly from the Knauer pump to the outlet pressure sensor with flow direction reversed and disconnecting the remaining plumbing. The sensor was flushed with MeOH (15 mL 3 mL/min) 10% HNO3 (100 mL 2 mL/min) water (100 mL 2 mL/min) and DMF (10 mL by syringe)
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Back-flushing was performed by plumbing directly from the Knauer pump to the outlet pressure sensor, with flow direction reversed, and disconnecting the remaining plumbing. The sensor was flushed with MeOH (15 mL, 3 mL/min), 10% HNO3 (100 mL, 2 mL/min), water (100 mL, 2 mL/min), and DMF (10 mL by syringe).
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24
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58449122729
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Glasnov, T. N.; Findenig, S.; Kappe, C. O. Chem.-Eur. J. 2009, 15, 1001-1010. doi:10.1002/chem.200802200
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Chem.-Eur. J.
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Glasnov, T.N.1
Findenig, S.2
Kappe, C.O.3
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25
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Auer, E.; Freund, A.; Pietsch, J.; Tacke, T. Appl. Catal., A 1998, 173, 259-271. doi:10.1016/S0926-860X(98)00184-7
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Auer, E.1
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