How can high-throughput testing enable the transition to a circular economy?

Over the last decades, the chemical industry has been challenged with the target to reduce the fossil resource dependency, mitigate climate change and resolve pollution. Waste recycling can contribute to all of these pillars and, as a result, these challenges have initiated the search for means to recycle waste streams, preferably at the source of production before harming ecosystems in order to transit to a circular economy.

In this Catalysis Insider, we want to highlight two trending topics, which are important enablers to reach a circular economy:  chemo-catalytic CO2 valorization and plastic recycling. Both their respective chemical process & R&D challenges can benefit from high-throughput testing.

Chemo-catalytic CO2 valorization: adsorptive separation followed by valorization

 

Source : Chem. Rev. 2017, 117, 14, 9804-9838

Excessive CO2 emission is estimated to contribute 57% of global greenhouse effect. Separating CO2 from relevant sources such as flue gas, natural gas, and syngas may reduce emissions directly or indirectly by increasing the energy efficiency. Compared with amine absorption, adsorptive separation offers merits such as low energy cost, no corrosion, and many other advantages. The need to get sufficiently pure CO2 for further valorization demands research and development on new adsorbents, which involves a lot of material testing. Therefore Avantium has identified this field as an area for the development and commercialization of high-throughput R&D solutions which accelerate adsorbent performance testing activities.

The separation is followed by chemo-catalytic CO2 conversion processes. This is an active option to reduce greenhouse gas emissions and actually utilize CO2 as a feedstock to produce fuels and valuable chemicals.

In the various CO2-to-chemcials routes, new catalytic materials have to be identified and developed with the optimal selectivity and activity in achieving the desired value-added products (e.g. olefins and aromatics).

The early discovery phase of such new catalytic materials offers a great opportunity to apply high-throughput testing methodologies. One of the key advantages of high-throughput testing in the early discovery phase is that it enables to develop a kinetic model that gives a better understanding of mechanisms of reactions. Applying multi parallel fixed bed reactors (up to 64 reactors in parallel) enable the possibility to vary multiple parameters in one single experiment. This approach will significantly reduce the time in the search of an optimal catalytic material.

 

Plastic recycling

Plastics recycling, as it exists today, is mainly based on mechanical recycling and is not yet optimal. As below graph shows, few plastics get recycled—only about 9% in the US and 15% in Europe.

Plastics Recycling in the USA

Sources: https://cen.acs.org/environment/recycling/Plastic-problem-chemical-recycling-solution/97/i39 &  US Environmental Protection Agency.

Chemical recycling could be a way around some of the shortcomings of mechanical recycling. Chemical processes are more tolerant of contamination, and they yield polymers that are identical to the originals, eliminating down-cycling. Thus chemical recycling could play a key part in dealing with the current plastic waste problem. In chemical recycling processes, plastic waste is purified and chemically separated into new, pure chemical building blocks. These, in turn, can be used to manufacture new plastics. When it comes to processing more complex plastics, chemical recycling is the only option.  This offers new opportunities for the development of innovative technologies that promote recycling of plastics. This includes research and development on new materials and additives that facilitate recycling processes, as well as several chemical recycling processes to create value out of the plastic waste.

There are two main routes in the chemical plastic recycling domain and the choice usually depends on the purity of the feed plastic stream: decomposition and de-polymerization (see below table)

 

Method Characteristics feedstock Typical applications
Decomposition typically olefin feedstock
  • Liquefaction
  • Pyrolysis
  • Oxidative cleavage
  • Co-blending liquefied wast plastic with crude oil in existing refining and upgrading operations
De-polymerization

typically polyester feedstock

  • Solvonolysis (like glycolysis)

 

Summary

We observe that many of our customers are working in the above mentioned two areas to find and optimize new materials and processes. In several cases Avantium has supported customers with the appropriate high-throughput testing solutions, applying both batch and flow reactors, in order to accelerate their R&D in the field of adsorbents and catalysts, with either fixed-bed or batch solutions.

Please contact us if you would like to know more about our solutions in the areas of CO2 valorization and chemical plastic recycling.

Flowrence® products specifications

Reactor Section

Easy and quick reactor exchange system. Possibility to use quartz reactors at high pressure.

1 block of 4 reactors

HT = High Temperature max. 800°C nominal, limited to 925°C (<0.5°C reactor to reactor deviation)

4 blocks of 4 reactors

HT  or MT = Medium Temperature max. 525°C (<0.5°C block-to-block deviation)

16 reactors with iRTC

individual Reactor Temperature Control
max. 550°C (<0.5°C reactor-to-reactor)

4 reactors with iRTC

individual Reactor Temperature Control
max. 550°C (<0.5°C reactor-to-reactor)

Temperature Ranges (°C)

100 – 800°C
up 925°C (Option)

50 – 525°C
100 – 800°C
up 925°C (Option)

50 – 550°C

50 – 550°C

Reactor Types

L= Length
OD= Outer Diameter
ID= Inner Diameter
SS= Stainless Steel (< 550⁰C)
Qz= Quartz (< 925⁰C)

L 300 mm 561 mm
OD 3 mm 6 mm
ID SS 2 / 2.6 mm 2 / 3 / 4 / 5 mm
ID Qz 2 mm 2 / 4 mm
300 mm 561 mm 561 mm
3 mm 3 mm 6 mm
2 / 2.6 mm 2 / 2.6 mm 2 / 3 / 4 / 5 mm
2 mm 2 mm 2 / 4 mm
561 mm
3 mm
2 / 2.6 mm
2 mm
561 mm
3 mm
2 / 2.6 mm
2 mm

Maximum Catalyst Bed Length

(isothermal zone tolerance ± 1°C)
Note: isothermal length is dependent on the temperature range

300 / 3 HT 561 / 6 HT
>120 mm @ 450°C >200 mm @ 500°C
>90 mm @ 800°C >150 mm @ 800°C
>140 mm @ 925°C
300 / 3 HT 561 / 3 MT 561 / 6 HT
>120 mm @ 450°C >310 mm @ 450°C >200 mm @ 500°C
>90 mm @ 800°C >150 mm @ 800°C
>140 mm @ 925°C
561 / 3 MT iRTC
250°C ±0.5°C 41cm (4reactors)
350°C±0.5°C 38cm (4reactors)
550°C±0.5°C 28cm (4reactors)
3 reactors at 550°C, 1 reactor 350°C:
550°C=27cm 350°C=41cm ±0.5°C
561 / 3 MT iRTC
250°C ±0.5°C 41cm (4reactors)
350°C±0.5°C 38cm (4reactors)
550°C±0.5°C 28cm (4reactors)
3 reactors at 550°C, 1 reactor 350°C:
550°C=27cm 350°C=41cm ±0.5°C

Catalyst Volume (mL)

(isothermal zone)

0.2 - 0.6 mL 0.4 - 2.0 mL
0.2 - 0.6 mL 0.4 - 1.0 mL 0.4 - 2.0 mL
0.4 - 1.0 mL
0.4 - 1.0 mL

Pressure Ranges (barg)

2 – 80 barg
0.5 – 180 barg (option)

2 – 100 barg
0.5 – 180 barg

2 – 80 barg
0.5 – 180 barg

2 – 20 barg
2 – 50 barg (option)

Reactor Pressure Control

Advanced control RSD ±0.1 barg at reference conditions (gas phase only and 20 barg). For trickle flow Advanced control RSD ±0.5barg.

Standard (±0.5 barg)
Advanced (±0.1 barg) (option)

Standard (±0.5 barg)
Advanced (±0.1 barg) (option)

Advanced (±0.1 barg)

Advanced (±0.1 barg)

Gas Feed Lines

(#Gas Feeds)

Up to 6 + Diluent gas

He, Ar, N2, H2, CH4, CO2, C2H4, C2H6, O2/Inert (≤5%), CO, Other gases

Up to 7 + Diluent gas

He, Ar, N2, H2, CH4, CO2, C2H4, C2H6, O2/Inert (≤5%), CO, Other gases

Up to 7 + Diluent gas

He, Ar, N2, H2, CH4, CO2, C2H4, C2H6, O2/Inert (≤5%), CO, Other gases

Up to 6 + Diluent gas

He, Ar, N2, H2, CH4, CO2, C2H4, C2H6, O2/Inert (≤5%), CO, Other gases

Online Analysis

Full integration GC, MS , GC/MS with data visualisation (option)

Full integration GC, MS , GC/MS with data visualisation

Full integration GC, MS , GC/MS with data visualisation

Full integration GC, MS , GC/MS with data visualisation

Liquid Feed

 Split feeding 8 + 8 reators (option)

Pump-Coriolis dosing system
(ambient, cooled)

Pump-Coriolis dosing system
(ambient, cooled, heated 80°C)

Pump-Coriolis dosing system
(ambient, cooled, heated 80°C)

Pump-Coriolis dosing system
(ambient, cooled, heated 80°C)

Liquid Distribution

Microfluidic Distribution
(4-channel glass-chip)

Microfluidics Distribution
(4x4-channel glass-chip)
(16-channel glass-chip)
Active Liquid Distribution (option)
(with automatic isolation valves)

Active Liquid Distribution
(with automatic isolation valves)

Microfluidic Distribution
(4-channel glass-chip)

Liquid Sampling

(G/L Separation)

Parallel liquid sampling (4 x 20ml vials) with sequential on-line gas phase sampling (option)

Automated liquid sampling (4 rows x 16 vials x 8ml) with sequential on-line gas phase sampling (option)

Automated liquid sampling (4 rows x 16 vials x 8ml) with sequential on-line gas phase sampling (option)

Parallel liquid sampling (4 x 20ml vials) with sequential on-line gas phase sampling (option)

Reactors Effluent Handling

(Off-line Analysis Connection)

Full heated circuit up to 180°C with sequential on-line full gas phase sampling (option)

Full heated circuit up to 200°C with sequential on-line full gas phase sampling

Full heated circuit up to 200°C with sequential on-line full gas phase sampling

Full heated circuit up to 200°C with sequential on-line full gas phase sampling

Offline Analysis

Integrated Workflow: SimDist, total S/N, liquid density, balance, label printer, barcode (option)

Integrated Workflow: SimDist, total S/N, liquid density, balance, label printer, barcode

Integrated Workflow: SimDist, total S/N, liquid density, balance, label printer, barcode

Integrated Workflow: SimDist, total S/N, liquid density, balance, label printer, barcode

Waste Handling

Ambient temperature
Heated wax trapping (option)

Ambient temperature / Cooled containers / Heated compartment (wax trapping, heavies)

Ambient temperature / Cooled containers / Heated compartment (wax trapping, heavies)

Ambient temperature / Cooled containers / Heated compartment (wax trapping, heavies)

Safety

Gas sensors and control box (CO, LEL, VOC)

Gas sensors and control box (CO, LEL, VOC)

Gas sensors and control box (CO, LEL, VOC)

Gas sensors and control box (CO, LEL, VOC)

Flowrence® Software

Flowrence® recipe builder, control & database builder

Flowrence® recipe builder, control & database builder

Flowrence® recipe builder, control & database builder

Flowrence® recipe builder, control & database builder

Microfluidics modular gas distribution

Unrivalled accuracy in gas distribution with patented glass-chips for 4 and 16 reactors, with a guaranteed flow distribution of 0.5% RSD. Quick exchange of glass-chips for different operating conditions. Flexibility to cover a wide range of applications.

TinyPressure glass-chip holder with integrated pressure measurement

Compact modular design for gas and liquid distribution. No high-temperature pressure sensors required. Quick exchange of the microfluidic glass-chips, without the need for time-consuming leak testing.

Tube-in-tube reactor technology with effluent dilution

Unique tube-in-tube design with easy and rapid exchange of the reactor tubes (within minutes!). No need for any connections. Use of inert diluent gas (outside of reactor) to maintain the pressure prevents dead volumes and back flow. Possibility to use quartz reactors at high pressure applications.

Automated liquid sampling system

Programmable, fully automated liquid product sampling robot for 24/7 hands-off operation. Robot equipped with a compact manifold aiming at depressurizing the effluent immediately after each reactor to atmospheric pressure. Eliminates the use of high pressure valves.

Reactor Pressure Control (RPC)

The most accurate and stable pressure regulator for a 16-parallel reactors with just ±0.1bar RSD. The RPC uses microfluidics technology to regulate the pressure of each reactor, maintaining equal distribution of the inlet flow over the 16 reactors.

Auto-calibrating liquid feed distribution, measurement, and control

Distribution of difficult feedstocks e.g., VGO, HVGO, DAO. Liquid distribution 0.2% RSD, making it the most accurate liquid distribution device on the market. Option to selectively isolate each reactor.

Single-Pellet-String-Reactors (SPSR)

No dead-zones, no bed packing & distribution effects. The catalyst packing is straightforward and does not require special procedures. A single string of catalyst particles is loaded in the reactors avoiding maldistribution, eliminating channeling and incomplete wetting.

EasyLoad®

Unique reactor closing system with no connections. Rapid reactor replacement minimizing delays, improving uptime and reliability. Stable evaporation by liquid injection into reactor.

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+31 (0)20 586 8080

Zekeringstraat 29
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The Netherlands

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