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PARALLEL POISONING IN BIDISPERSE STRUCTURED CATALYST. https://doi.org/10.1021/acs.energyfuels.7b03064, https://doi.org/10.1021/bk-1996-0634.ch004, https://doi.org/10.1016/B978-0-12-818713-5.00009-5, https://doi.org/10.1016/j.energy.2019.116030, https://doi.org/10.1016/j.cherd.2019.04.042, https://doi.org/10.1007/978-3-662-56444-8_22-1, https://doi.org/10.1007/978-3-319-67798-9_11, https://doi.org/10.1016/j.fuproc.2017.09.003, https://doi.org/10.1016/j.ces.2017.05.023, https://doi.org/10.1016/j.micromeso.2017.02.067, https://doi.org/10.1016/j.compchemeng.2016.11.033, https://doi.org/10.1016/j.apenergy.2015.12.093, https://doi.org/10.1007/s00449-016-1635-4, https://doi.org/10.1016/j.apcatb.2016.03.071, https://doi.org/10.1134/S0023158416050116, https://doi.org/10.1002/9781119248491.ch3, https://doi.org/10.1016/j.ces.2015.12.004, https://doi.org/10.1016/j.apcatb.2015.05.017, https://doi.org/10.1016/j.ces.2015.04.024, https://doi.org/10.1016/j.egypro.2015.07.514, https://doi.org/10.1016/j.cej.2015.01.067, https://doi.org/10.1016/j.carbpol.2014.11.056, https://doi.org/10.1016/j.apm.2013.04.021, https://doi.org/10.1016/j.compchemeng.2010.12.001, https://doi.org/10.1016/j.ces.2011.02.016, https://doi.org/10.1016/j.energy.2010.10.034, https://doi.org/10.1007/s10295-007-0217-5, https://doi.org/10.1016/j.memsci.2005.04.017, https://doi.org/10.1016/S0168-1656(01)00235-8, https://doi.org/10.1016/S0016-2361(00)00037-5, https://doi.org/10.1002/1097-0290(20000920)69:6<639::AID-BIT8>3.0.CO;2-V, https://doi.org/10.1016/S0016-2361(99)00274-4, https://doi.org/10.1016/S0082-0784(00)80631-1, https://doi.org/10.1002/j.2050-0416.1998.tb00970.x, https://doi.org/10.1080/0738-859891224239, https://doi.org/10.1007/978-1-4757-0516-4_43, https://doi.org/10.1016/0376-7388(94)00156-S, https://doi.org/10.1016/0009-2509(93)80039-S, https://doi.org/10.1080/00986449108911545, https://doi.org/10.1080/00986449108910858, https://doi.org/10.1016/0360-1285(90)90025-X, https://doi.org/10.1016/S0167-2991(08)60232-3, https://doi.org/10.1080/00986448408911140, https://doi.org/10.1016/0009-2509(84)80118-9, https://doi.org/10.1016/S0167-2991(08)65215-5, https://doi.org/10.1016/0360-1285(78)90008-4, https://doi.org/10.1016/0009-2509(77)80028-6, https://doi.org/10.1016/0021-9991(69)90006-0. Department of Chemical Engineering and Biotechnology https://doi.org/10.1021/acs.energyfuels.7b03064, https://doi.org/10.1021/bk-1996-0634.ch004, https://doi.org/10.1016/B978-0-12-818713-5.00009-5, https://doi.org/10.1016/j.energy.2019.116030, https://doi.org/10.1016/j.cherd.2019.04.042, https://doi.org/10.1007/978-3-662-56444-8_22-1, https://doi.org/10.1007/978-3-319-67798-9_11, https://doi.org/10.1016/j.fuproc.2017.09.003, https://doi.org/10.1016/j.ces.2017.05.023, https://doi.org/10.1016/j.micromeso.2017.02.067, https://doi.org/10.1016/j.compchemeng.2016.11.033, https://doi.org/10.1016/j.apenergy.2015.12.093, https://doi.org/10.1007/s00449-016-1635-4, https://doi.org/10.1016/j.apcatb.2016.03.071, https://doi.org/10.1134/S0023158416050116, https://doi.org/10.1002/9781119248491.ch3, https://doi.org/10.1016/j.ces.2015.12.004, https://doi.org/10.1016/j.apcatb.2015.05.017, https://doi.org/10.1016/j.ces.2015.04.024, https://doi.org/10.1016/j.egypro.2015.07.514, https://doi.org/10.1016/j.cej.2015.01.067, https://doi.org/10.1016/j.carbpol.2014.11.056, https://doi.org/10.1016/j.apm.2013.04.021, https://doi.org/10.1016/j.compchemeng.2010.12.001, https://doi.org/10.1016/j.ces.2011.02.016, https://doi.org/10.1016/j.energy.2010.10.034, https://doi.org/10.1007/s10295-007-0217-5, https://doi.org/10.1016/j.memsci.2005.04.017, https://doi.org/10.1016/S0168-1656(01)00235-8, https://doi.org/10.1016/S0016-2361(00)00037-5, https://doi.org/10.1002/1097-0290(20000920)69:6<639::AID-BIT8>3.0.CO;2-V, https://doi.org/10.1016/S0016-2361(99)00274-4, https://doi.org/10.1016/S0082-0784(00)80631-1, https://doi.org/10.1002/j.2050-0416.1998.tb00970.x, https://doi.org/10.1080/0738-859891224239, https://doi.org/10.1007/978-1-4757-0516-4_43, https://doi.org/10.1016/0376-7388(94)00156-S, https://doi.org/10.1016/0009-2509(93)80039-S, https://doi.org/10.1080/00986449108911545, https://doi.org/10.1080/00986449108910858, https://doi.org/10.1016/0360-1285(90)90025-X, https://doi.org/10.1016/S0167-2991(08)60232-3, https://doi.org/10.1080/00986448408911140, https://doi.org/10.1016/0009-2509(84)80118-9, https://doi.org/10.1016/S0167-2991(08)65215-5, https://doi.org/10.1016/0360-1285(78)90008-4, https://doi.org/10.1016/0009-2509(77)80028-6, https://doi.org/10.1016/0021-9991(69)90006-0. 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