BEGIN:VCALENDAR
PRODID:Veranstaltungen IKFT
VERSION:2.0
X-WR-CALNAME:Veranstaltungen IKFT
NAME:Veranstaltungen IKFT
REFRESH-INTERVAL;VALUE=DURATION:PT12H
X-PUBLISHED-TTL:PT12H
BEGIN:VTIMEZONE
TZID:Europe/Berlin
TZURL:http://tzurl.org/zoneinfo-outlook/Europe/Berlin
X-LIC-LOCATION:Europe/Berlin
BEGIN:DAYLIGHT
TZOFFSETFROM:+0100
TZOFFSETTO:+0200
TZNAME:CEST
DTSTART:19700329T020000
RRULE:FREQ=YEARLY;BYMONTH=3;BYDAY=-1SU
END:DAYLIGHT
BEGIN:STANDARD
TZOFFSETFROM:+0200
TZOFFSETTO:+0100
TZNAME:CET
DTSTART:19701025T030000
RRULE:FREQ=YEARLY;BYMONTH=10;BYDAY=-1SU
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END:VTIMEZONE
BEGIN:VEVENT
UID: 62282
DTSTAMP:20260706T094754Z
SUMMARY:Bridging Thermo- and Electrocatalysis: Understanding Hydrogen Reactivity
through Thermodynamics
X-ALT-DESC;FMTTYPE=text/html:Bridging Thermo- and
Electrocatalysis: Understanding Hydrogen Reactivity through
Thermodynamics
Seminar Room 202, Building
727
DESCRIPTION: Bridging Thermo- and Electrocatalysis: Understanding
Hydrogen Reactivity through Thermodynamics\n\nSeminar Room 202, Building
727\n\n
DTSTART;TZID=Europe/Berlin:20260715T140000
DTEND;TZID=Europe/Berlin:20260715T150000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61887
DTSTAMP:20260706T094754Z
SUMMARY:Hydrothermal Liquefaction of Black Liquor – Depolymerization of Lignin
in near-critical water under the influence of salts
X-ALT-DESC;FMTTYPE=text/html:Hydrothermal
Liquefaction of Black Liquor – Depolymerization of Lignin in
near-critical water under the influence of salts
Seminar Room 202,
Building 727
DESCRIPTION: Hydrothermal Liquefaction of Black Liquor –
Depolymerization of Lignin in near-critical water under the influence of
salts\nSeminar Room 202, Building 727\n\n
DTSTART;TZID=Europe/Berlin:20260720T130000
DTEND;TZID=Europe/Berlin:20260720T133000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 62283
DTSTAMP:20260706T094754Z
SUMMARY:Coupling of micro mixer for precipitation and thickener for ripening for
the scalable production of optimized catalysts
X-ALT-DESC;FMTTYPE=text/html:Coupling of micro mixer
for precipitation and thickener for ripening for the scalable production
of optimized catalysts
Seminar Room 202, Building
727
DESCRIPTION: Coupling of micro mixer for precipitation and thickener for
ripening for the scalable production of optimized catalysts\n\nSeminar
Room 202, Building 727\n\n
DTSTART;TZID=Europe/Berlin:20260720T133000
DTEND;TZID=Europe/Berlin:20260720T140000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61209
DTSTAMP:20260706T094754Z
SUMMARY:Development of a two-step continuous process for reductive catalytic
fractionation of lignocellulosic biomass into aromatic compounds.
X-ALT-DESC;FMTTYPE=text/html:Development of a
two-step continuous process for reductive catalytic fractionation of
lignocellulosic biomass into aromatic compounds.
IKFT Seminar Room
202, Building 727
Abstract:
A two-step RCF
process is used. In the first step, lignin is dissolved by solvation in
a flow reactor as well as in batch mode, thereby separating lignin from
carbohydrates. In the second step, the lignin solution obtained in the
first step is catalytically reduced in a batch reactor to gain data for
the design of a continuous fixed-bed reactor. In the second step, the
formic acid produced by the decomposition of hemicellulose and solvent
is used as the hydrogen source.
DESCRIPTION: Development of a two-step continuous process for reductive
catalytic fractionation of lignocellulosic biomass into aromatic
compounds.\nIKFT Seminar Room 202, Building
727\n\nAbstract:
\n\nA two-step RCF process is used. In the
first step, lignin is dissolved by solvation in a flow reactor as well
as in batch mode, thereby separating lignin from carbohydrates. In the
second step, the lignin solution obtained in the first step is
catalytically reduced in a batch reactor to gain data for the design of
a continuous fixed-bed reactor. In the second step, the formic acid
produced by the decomposition of hemicellulose and solvent is used as
the hydrogen source.
\n\n
\n
DTSTART;TZID=Europe/Berlin:20260721T100000
DTEND;TZID=Europe/Berlin:20260721T103000
LOCATION:IKFT Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61210
DTSTAMP:20260706T094754Z
SUMMARY:Techno-economic assessment of by-products from carbon capture and
utilization processes
X-ALT-DESC;FMTTYPE=text/html:Techno-economic
assessment of by-products from carbon capture and utilization
processes
IKFT Seminar Room 202, Building 727
DESCRIPTION: Techno-economic assessment of by-products from carbon
capture and utilization processes\nIKFT Seminar Room 202, Building
727\n\n
DTSTART;TZID=Europe/Berlin:20260727T130000
DTEND;TZID=Europe/Berlin:20260727T133000
LOCATION:IKFT Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61885
DTSTAMP:20260706T094754Z
SUMMARY:Designing Sustainable Electrocatalysis: Cost- and Carbon-Informed
Decisions; CO₂ Reduction and HCH Case Studies
X-ALT-DESC;FMTTYPE=text/html:Designing Sustainable
Electrocatalysis: Cost- and Carbon-Informed Decisions; CO₂
Reduction and HCH Case Studies
Seminar Room 202, Building
727
DESCRIPTION: Designing Sustainable Electrocatalysis: Cost- and
Carbon-Informed Decisions; CO₂ Reduction and HCH Case Studies\nSeminar
Room 202, Building 727\n\n
DTSTART;TZID=Europe/Berlin:20260831T130000
DTEND;TZID=Europe/Berlin:20260831T133000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 62284
DTSTAMP:20260706T094754Z
SUMMARY:1D Modeling of a Co-current Upflow Fixed-Bed Reactor for the
Dehydrogenation of Perhydro-benzyltoluene to Evaluate Calculation
Methods for the Liquid Holdup
X-ALT-DESC;FMTTYPE=text/html:1D Modeling of a
Co-current Upflow Fixed-Bed Reactor for the Dehydrogenation of
Perhydro-benzyltoluene to Evaluate Calculation Methods for the Liquid
Holdup
Seminar Room 202, Building 727
A 1D reactor
model for the dehydrogenation of perhydro benzyltoluene in a fixed-bed
reactor is developed. The model predicts concentration profiles, phase
fractions as well as an axial temperature profile and is validated with
experimental data from a laboratory reactor. The work was conducted in
the framework of a Master's thesis at the Institute for a
sustainable Hydrogen Economy (IHE) of FZJ.
DESCRIPTION: 1D Modeling of a Co-current Upflow Fixed-Bed Reactor for
the Dehydrogenation of Perhydro-benzyltoluene to Evaluate Calculation
Methods for the Liquid Holdup\nSeminar Room 202, Building
727\n\nA 1D reactor model for the dehydrogenation of perhydro
benzyltoluene in a fixed-bed reactor is developed. The model predicts
concentration profiles, phase fractions as well as an axial temperature
profile and is validated with experimental data from a laboratory
reactor. The work was conducted in the framework of a Master's thesis at
the Institute for a sustainable Hydrogen Economy (IHE) of
FZJ.
\n\n
\n\n
\n
DTSTART;TZID=Europe/Berlin:20260914T130000
DTEND;TZID=Europe/Berlin:20260914T133000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61704
DTSTAMP:20260706T094754Z
SUMMARY:In Situ XAS/FEXRAV and 2D XRF Study of IrOx/ZrOx Catalysts for PEM Water
Electrolysis
X-ALT-DESC;FMTTYPE=text/html:In Situ XAS/FEXRAV and
2D XRF Study of IrOx/ZrOx Catalysts for PEM Water
Electrolysis
Seminar Room 202, Building 727
Abstract:
Bridging the gap between local active-site structure and catalyst-layer
architecture is essential for the rational design of catalytic systems.
Using IrOx/ZrOx anodes for PEM water electrolysis as a case study, this
presentation shows how in situ XAS/FEXRAV and 2D XRF can be combined to
connect structural evolution, spatial heterogeneity, and performance
under realistic conditions.
DESCRIPTION: In Situ XAS/FEXRAV and 2D XRF Study of IrOx/ZrOx Catalysts
for PEM Water Electrolysis\nSeminar Room 202, Building
727\n\nAbstract: Bridging the gap between local active-site structure
and catalyst-layer architecture is essential for the rational design of
catalytic systems. Using IrOx/ZrOx anodes for PEM water electrolysis as
a case study, this presentation shows how in situ XAS/FEXRAV and 2D XRF
can be combined to connect structural evolution, spatial heterogeneity,
and performance under realistic conditions.
\n
DTSTART;TZID=Europe/Berlin:20260914T133000
DTEND;TZID=Europe/Berlin:20260914T140000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
BEGIN:VEVENT
UID: 61886
DTSTAMP:20260706T094754Z
SUMMARY:Scale-up of Co-Precipitation in Mixing Nozzles for the production of
high quality catalyst precursors
X-ALT-DESC;FMTTYPE=text/html:Scale-up of
Co-Precipitation in Mixing Nozzles for the production of high quality
catalyst precursors
Seminar Room 202, Building
727
DESCRIPTION: Scale-up of Co-Precipitation in Mixing Nozzles for the
production of high quality catalyst precursors\nSeminar Room 202,
Building 727\n\n
DTSTART;TZID=Europe/Berlin:20260928T130000
DTEND;TZID=Europe/Berlin:20260928T133000
LOCATION:Seminar Room 202, Building 727
END:VEVENT
END:VCALENDAR