Ammonia catalyst testing is a perfect fit for the 4-reactors Flowrence XD and the 16-reactors Flowrence XR. Inherently safe with small-scale reactors and small volume holdup, with the smallest footprint in the industry. Advantages in ammonia containment with no customized ammonia storage required. Proven online GC analytics and stable liquid pumping with immediate evaporation at the inlet of the of the reactors. Easy to combine synthesis and reforming in one system!

“These new Flowrence systems strengthen our high-throughput facilities for heterogeneous catalysis and make sure that our researchers keep having access to state of the art technology. We have an excellent experience with Avantium’s equipment and technical support and look forward to developing new catalysts by making use of these systems.”

Jorge Gascon, Director & Full Professor, KAUST Catalysis Center

Conditions: 1 bar, 350-500 °C, NH3 flow: 1.4-8.0 mL min-1, GHSV = 5500-32000 mL gcat-1h-1NH3 conv. = 1-78 %;  TOS = 12 h (above), 100 h (below)

• 2NH3 à N2 + 3H2
• Ammonia employed as a promising green hydrogen carrier by reversible synthesis/decomposition.
• Key challenge is maintaining catalyst performance over time at high NH3 conversion and low temperature
• This research employed Hastelloy equipped Flowrence® XD with 4 parallel reactors to assess catalytic performance for various Ru-based catalysts.

Kim, Nguyen, Mahmood, Yavuz, , Chemical Engineering Journal 463, (2023), p.142474

2 Flowrence® XD high throughput catalyst testing systems with 4-reactors installed at the Catalysis Hub of ETH Zürich configured for CO2 and Methane valorization. The Flowrence® XD systems are embedded in a glovebox, allowing to test moisture and oxygen-sensitive catalysts and recover spent catalysts after reaction without air exposure for subsequent surface characterization. This feature vastly increases the catalyst testing options.

CO-to-Aromatics

Conditions: 20 bar, 300 °C, H2/CO = 1 V/V, GHSV = 4,500-40,000 h−1TOS = 6-9 h, CO conv. = 15–20 %

• Investigated syngas-to-aromatics over stacked bed
• Fe-K-based FT catalyst upstream of H-ZSM-5 olefin-to-aromatics catalyst
• Understanding of single pass-through syngas-to-aromatics systems established
• All catalysts tested in parallel with different bed heights and GHSVs

J.L. Weber et al., Catal Today, 2021, 369, 175–183.

CO2-to-Methanol

Conditions: 4.2 mg Cu per reactor, 40 bar(g), 600 mL min−1 gCu−1, H2/CO2/He = 67.5/22.5/10 vol%.

• Effect of Cu particle size (4-20 nm) on CO2 hydrogenation investigated.
• Fully automated pretreatment and performance testing.
• 5 catalyst formulations tested in parallel between 200-260 °C for over 100 h at 40 bar.
• Small particles (< 13 nm) had low activity, but high MeOH selectivity
• Catalytic performance and selectivity results in line with Density Functional Theory (DFT)

L. Barberis et al., Nanoscale, 2022, 14, 13551–13560.

CO2-to-Olefin and MeOH

• Investigated the effect of steam addition (0-7 %) during MOF pyrolysis during Fe and In MOF-based catalyst synthesis.
• 4 catalysts tested in parallel
• Performance in high pressure CO2 hydrogenation to olefins and MeOH investigated at 350 °C and 50 bar
• Accurate conversions and selectivities determined towards CO, hydrocarbons (C1-C5+), MeOH and DME
• Fe-based MOFs exhibited improved selectivity towards higher olefins (above)
• In-based MOFs exhibited improved selectivity towards MeOH (below)

I. S. Khan et al., ACS Catal, 2023, 13, 1804–1811.

Dry Reforming of Methane

Reaction conditions:

(a) 1 bar, 800 °C, GHSV = 30,000 mL/(gcat h)
(b) 14 bar, 800 °C, GHSV = 12,000 mL/(gcat h)

• CO2 + CH4 > 2CO + 2H2
• Investigate the effect of catalyst promotion of Ni-based DRM catalysts
• DRM performance studied between 550-800 °C.
  • Accurate analytics (e.g., H2/COx ratio) essential for mechanistic insights.
• Catalyst stability and deactivation measured at 800 °C at both 1 bar (250 h) and 14 bar (40 h)
  • High temperature studies enabled by Flowrence® compatibility with quartz reactors
  • High pressure study with quartz enabled by Flowrence® tube-in-tube reactor design

X. Yao et al., Appl Catal B, 2023, 328, 122479.V. K. Velisoju et al., Journal of CO2 Utilization, 2023, 75, 102573.

Reaction conditions:(a) 1 bar, 800 °C, GHSV = 30,000 mL/(gcat h)(b) 14 bar, 800 °C, GHSV = 12,000 mL/(gcat h)

• CO2 + CH4 à 2CO + 2H2
• Investigate the effect of catalyst promotion of Ni-based DRM catalysts
• DRM performance studied between 550-800 °C.
  • Accurate analytics (e.g., H2/COx ratio) essential for mechanistic insights.
• Catalyst stability and deactivation measured at 800 °C at both 1 bar (250 h) and 14 bar (40 h)
  • High temperature studies enabled by Flowrence® compatibility with quartz reactors
  • High pressure study with quartz enabled by Flowrence® tube-in-tube reactor design

X. Yao et al., Appl Catal B, 2023, 328, 122479.V. K. Velisoju et al., Journal of CO2 Utilization, 2023, 75, 102573.

CO2-to-Olefin and MeOH

Reaction conditions: 1 bar, 800 °C, and GHSV = 16,100 mL/(gcat h)

• CO2 + CH4 à 2CO + 2H2
• Investigated the effect of Zn-doping on ZrO2-supported Ni-based catalyst performance in DRM between 550-800 °C
• Stability measured at 800 °C for over 100 h to study catalyst deactivation
• Accurate analytics to determine H2/COx ratio vital to obtain mechanistic insights (DRM vs. reverse water-gas shift)
• High temperature performance and stability study enabled by Flowrence® compatibility with quartz reactors

V. K. Velisoju et al., Journal of CO2 Utilization, 2023, 75, 102573.

Flowrence® XD 4-parallel reactor system provided to Christian-Albrechts University of Kiel is highly flexible, self-contained fixed-bed catalyst testing unit which excels at producing valuable data promptly leveraging high-throughput chemical technology. This technology offers you step-change improvements in the effectiveness of R&D efforts to generate your valuable results and facilitates the reproduction and comparison of catalyst performance over multiple runs. Researchers can test the process performance of a variety of catalysts with peace of mind that their results are accurate, reliable and reproducible.

Fischer-Tropsch

• Influence of Na and S on CoMn-based FT catalysts investigated
• 8 catalyst systems tested in parallel
• Assessed performance at different T (240-280 °C) and P (3-10 bar). Conditions: Flowrence® XR,a Activity and selectivity at 240–280 °C, 10 bar, and H2/CO = 2, and b activity and selectivity at 240 °C, 3–10 bar, and H2/CO = 2.
• Assessed evolution of stability and selectivity evolution (70+ h). Conditions: Flowrence® XR, 3 bar, 220 °C, H2/CO = 2 V/V, conversion < 10 %

J. Xie et al., Nat Commun, 2019, 10, 167.

The examples provided in this article clearly show that the Avantium Flowrence high-throughput 16-parallel reactors system produces consistent high data quality (repeatability, reproducibility, and scalability) for hydroprocessing applications.This high quality can only be achieved with the highest accuracy and precision in gas and liquid distribution with patented microfluidic glass chips, excellent pressure control, and the most accurate and narrowest mass balance. Also, the reactor design allows for a long, accurate, and precise isothermal zone where we ensure a plug flow regime. Typical issues related to bed packing and distribution effects are avoided with Avantium’s SPSR catalyst loading approach. This article also show examples of the scalability of this technology, comparing results with bench-scale and pilot-scale reactors.

Benchmarking Diesel Hydrotreating Loading Schemes

This article describes the results from ULSD testing where four experimental conditions were used to evaluate the catalysts during each run, in addition to the initial lining-out step after the sulphiding of the catalysts. The following section presents a summary of the main results obtained during the evaluation test for comparing catalyst performance with the three levels of LCO: 15%, 30%, and 45%.

Hydrotreating of Vegetal Oil

This article shows the results obtained in a Flowrence XP processing Vegetable Oil. Takeaways. No plugging was observed in any of small-scale reactors during the 23-d test with various VO blends and 6-d of running 100% VO. Quantifying theamount of water in the gas effluent using an online GC is a feasible method for closing the mass balance. The accuracy of the mass balance and yields obtained during the test are similar to conventional hydroprocessing catalyst testing.

Download article > 2023 – HP Reliable naphtha reforming catalyst testing

This article presents the new test designed developed by Avantium in collaboration with Axens and UOP. This innovative test design is enabled by the Flowrence XP and the independent control per reactor for kinetic studies and process design.

Download article > PTQ Catalysis 2021 – Refinery’s performance confirms Reforming catalyst testing

This article provides a comparison of the test results obtained in a Flowrence XR and the commercial naphtha reforming unit.

Fully automated with preprogrammed recipes for naphtha reforming catalyst testing and integrated GC with built-in constant octane testing (iso-RON), multi-coking testing (iso-Coking, patent pending), and isothermal testing. Powered by our extensive experience in naphtha reforming catalyst testing for refineries. This systems comes prepared to test Isomerization and Aromatics catalysts with feed drying, moisture level measurement, and dedicated liquid cleaning circuit.

This 16-reactors system can be used to test catalysts from:

• Naphtha Reforming
• Isomerization
• Transalkylation
• Disproportionation
• Metathesis
• Dealkylation
• Other Aromatics

Reaction conditions: 150-300 °C, Propene conversion < 10 %

• Influence of zeolite framework (MFI, MTW, TON), crystallite size, and pore diameter, on propene oligomerization rate.
• Catalysts’ performance compared in parallel between 150-300 °C with clear crystallite size effects observed at high temperatures.
• Stable catalyst screening

N. Hijazi and J. Gascon, React Chem Eng, 2023, DOI:10.1039/D3RE00285C

Avantium performed multiple tests in a dedicated Flowrence® XR high-throughput system with 16-parallel-reactors to validate its performance for the evaluation of commercial Selective Acetylene Hydrogenation catalysts, under industrial conditions, and facilitating the discrimination of catalysts with similar performance by providing accurate, repeatable and reproducible Operating Window results.

Avantium’s Flowrence® XR parallel fixed bed reactor platform has been validated by Axens.

• Full Maintenance & Support Contracts
• Remote Support
• Chemical Application Support
• Analytical Application Support
• Retrofit Existing Systems

• Hardware: calibration of temperature controllers, pressure controllers, flow controllers (testing of alarm matrix)
• Software: full back up, performance tuning of databases, software upgrade

• Complete training package during the factory acceptance and site acceptance testing
• Refresher training to  all operators

Accelerated exploration of heterogeneous CO₂ hydrogenation catalysts by Bayesian-optimized high-throughput and automated experimentation

Chem Catalysis, Volume 4, Issue 2, 100888

High-Throughput Experimentation, Theoretical Modeling, and Human Intuition: Lessons Learned in Metal–Organic-Framework-Supported Catalyst Design

ACS Cent. Sci. 2023, 9, 2, 266–276

Process-constrained batch Bayesian approaches for yield optimization in multi-reactor systems

Computers & Chemical Engineering 189:108779

High-throughput screening and literature data-driven machine learning-assisted investigation of multi-component La₂O₃-based catalysts for the oxidative coupling of methane

Catal. Sci. Technol., 2022,12, 2766-2774