Bioprocessing
Accelerate your biologic drug development with Praesto®
chromatography resins.

Accelerate your biologic drug development with Praesto®
chromatography resins.
As a global leader in resin technology, we develop and manufacture small beads that are used in the most regulated industries in the world to separate, remove or recover very specific elements and compounds.
Learn MoreWith 40 years of manufacturing expertise and 30 years of regulatory experience, we supply leading separation, purification and extraction technologies to support chromatography and biocatalysis applications in healthcare and life sciences.
Learn moreWe are a world leader in resin-based separation, purification and extraction technology, that provides sustainable solutions for our environment, businesses and healthcare.
Learn Morepoliacrilic macroporos, Rășină chelatica tip amidoximă
Echipele noastre de asistență tehnică și service mereu pregătite fac un pas suplimentar pentru a fi resursa ta cea mai de U00EEncredere. Suntem aici pentru tine.
Structura polimerica | Poliacrilic reticulat cu divinilbenzen | |
Aspect | Perle sferice | |
Grupari functionale | Amidoxima | |
Forma ionica | forma FB | |
capacitatea cuprului (min.) | 40 g/L | |
reținerea umidității | 52 - 60 % ( forma FB ) | |
Distribuția granulometrică | 300 - 1200 µm | |
< 300 µm (max.) | 1 % | |
coeficient de uniformitate (max.) | 1.7 | |
Dilatare reversibilă, FB → Cl- (max.) | 10 % | |
densitate specifică | 1.19 | |
Greutate de transport (aprox.) | 740 - 790 g/L (46.2 - 49.4 lb/ft³) |
A 20 BV downflow rinse is required before the vessel is put into service. This rinse can be done onsite or offsite pre-installation. Once the resin is put into service, backwashing is not permitted as this will lead to shortened bed life. This is a uniform grade resin with beads of similar size and will not require backwashing for classification / stratification before use. If it is determined, before startup, that air bubbles or particulate matter are trapped within the bed, then backwashing can be done. In that case, the resin bed should be expanded by 50-70% for 10-15 minutes. Please note that bed expansion increases with higher flow rate and lower water temperature. Avoid loss of resin through the top of the vessel by over expansion of the bed.
The pressure drop across a bed of ion exchange resin depends on the particle size distribution, bed depth, and voids volume of the exchange material, as well as on the flow rate and viscosity of the influent solution. Factors affecting any of these parameters— such as the presence of particulate matter filtered out by the bed, abnormal compressibility of the resin, or the incomplete classification of the bed—will have an adverse effect, and result in an increased head loss. Depending on the quality of the influent water, the application and the design of the plant, service flow rates may vary from 10 to 40 BV/h.
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