Pressure reactor with a capacity of (300 ml) with magnetic stirrer, heating jacket and temperature controller. In the project, it is used in the high-temperature and high-pressure PET ammonolysis to ethylene glycol and functional derivatives of terephthalic acid, as well as catalytically assisted PET decomposition processes. More information available on https://www.parrinst.com/products/non-stirred-pressure-vessels/series-4760/
Total project cost: 1 496 905.00 PLN
Device purchase cost: 37 447.39 PLN
The chromatograph was originally equipped with a single TCD detector. During the project, it was additionally equipped with an FID detector and a methanizer with a noiseless air compressor. In the project, it is used to determine the purity of products separated from post-reaction mixtures. More information available on https://www.srigc.com/home/product_detail/model-310-gas-chromatograph
Total project cost: 1 496 905.00 PLN
Device purchase cost: 32 604.84 PLN
The mill can be used for soft and medium-hard materials grinding prior the pulverization. In the project, the pulverizer is used for r-PET grinding and powderingin order to improve the possibility of its further processing in a pressure reactor. More information available on https://www.retsch.pl/pl/produkty/mlynki-laboratory/mlynki-tnace/sm-100/
Total project cost: 1 496 905.00 PLN
Device purchase cost: 39 154.00 PLN
Heat press with the pneumatic pressure, equipped with a display, oil compressor, power cables and compressor fastening. The minimum operating temperature is 220°C, the minimum pressing force is 300 g/cm2. The press has working plates with dimensions of 40 x 50 cm. In the project, it is used to produce polymer substrates. More information available on https://viscar.pl/prasy-termotransferowe-do-nadrukow-stahls/571-secabo-tpd-7-pneumatic.html
Total project cost: 1 496 905.00 PLN
Device purchase cost: 11 633.30 PLN
The device is one of the effects of the project, which is also a research and demonstration installation. The target capacity of the demonstration plant will be 5 L/h. The reactor will operate in a continuous mode and will be coordinated with the pre-evaporation module used to remove water generated during the synthesis of 1,3-dioxolane derivatives. In the project, it is used in catalyst research and optimization of the process of continuous production of 1,3-dioxolane derivatives. More information: the reactor is under construction. We soon will inform you about the effects of the work.
Total project cost: 1 496 905.00 PLN
Device purchase cost: 42 361.79 PLN