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''The technology is based on an Integrated Cascading Catalytic Pyrolysis (ICCP) process, being able to produce aromatics including benzene, toluene, and xylene (BTX) as well as light olefins from low grade biomass and plastics waste. This technology utilises catalytic cracking in a two-step process at temperatures between 450- 850 °C. In the first step the feedstock material is vaporised via thermal cracking. The pyrolysis vapours are then directly passed into a second reactor in which they are converted into aromatics by utilising a zeolite catalyst which can be continuously regenerated. Finally, the products are separated from the gas via condensation. An ex situ approach of catalytic conversion has several advantages such as the protection of the catalyst from deactivation/degradation expanding its lifetime, a greater variety of feedstock, and a precise adjustment of process conditions (e.g. temperature, catalyst design, and Weight Hourly Space Velocity (WHSV) in each step for improved yields. In current pilot plant with 10 kg h-1 feed capacity for either waste plastics or biomass, final design details are established, which will be include in the running engineering activities for the commercial plant.'' | ''The technology is based on an Integrated Cascading Catalytic Pyrolysis (ICCP) process, being able to produce aromatics including benzene, toluene, and xylene (BTX) as well as light olefins from low grade biomass and plastics waste. This technology utilises catalytic cracking in a two-step process at temperatures between 450- 850 °C. In the first step the feedstock material is vaporised via thermal cracking. The pyrolysis vapours are then directly passed into a second reactor in which they are converted into aromatics by utilising a zeolite catalyst which can be continuously regenerated. Finally, the products are separated from the gas via condensation. An ex situ approach of catalytic conversion has several advantages such as the protection of the catalyst from deactivation/degradation expanding its lifetime, a greater variety of feedstock, and a precise adjustment of process conditions (e.g. temperature, catalyst design, and Weight Hourly Space Velocity (WHSV) in each step for improved yields. In current pilot plant with 10 kg h-1 feed capacity for either waste plastics or biomass, final design details are established, which will be include in the running engineering activities for the commercial plant.'' | ||
=== Bio Base === | === Bio Base Europe Pilot Plant === | ||
{{Infobox provider-chromatography}} | {{Infobox provider-chromatography|Company=Bio Base Europe Pilot Plant|Country=Belgium|Webpage=https://www.bbeu.org/what-we-offer/technologies/product-recovery-and-purification/|Technology name=Chromatography|TRL=4-6|Other=Preparative chromatography unit (GRACE) – BENCH scale, adsorption chromatography for ATEX environment,|Capacity=pre-pilot scale: Glass for 8l; | ||
pilot scale: Acrylic for 38l, max. 5 bar; | |||
pilot scale: Glass for 80l}} | |||
Bio Base provides scale up of chromatography processes from lab-scale up to 4000 L scale. There is mainly a very broad knowledge of anion exchange, cation exchange and activated carbon processes, since (economically) those are most realistic to scale-up. | Bio Base provides scale up of chromatography processes from lab-scale up to 4000 L scale. There is mainly a very broad knowledge of anion exchange, cation exchange and activated carbon processes, since (economically) those are most realistic to scale-up. | ||