SpinChem® RBR S3

1. Material
2. Stainless Steel (SS316L, EN2348)
3. Height
4. 30 mm
5. Diameter
6. 70 mm
7. Porosity
8. 104 µm
9. Volume
10. 69 mL
11. Shaft Length
12. 41 cm
13. Shaft Diameter
14. 10 mm
15. Vessel Volume Range
16. 300-2000 mL
17. Weight
18. 148 g (397 g including shaft)
19. Rotational Direction
20. Counterclockwise
21. Rotational Speed
22. 200-800 rpm (maximum 500 rpm continuously when shaft guide is used!)

Shaft for S3

Filter kit for S3

Assembly tool for S3

Activated carbon decolorization, fast and without filtration, Automatic processes for efficient production, Biocatalysis engineering: the big picture, Decolourization more efficient in rotating bed reactor than fixed bed reactor, Rotating bed reactor faster than stirred tank reactor for a mass transfer limited reaction, High-viscosity applications made faster, Viscous solutions decolourized using a rotating bed reactor and a stirred tank reactor, Design of a green chemoenzymatic cascade for scalable synthesis of bio-based styrene alternatives, Efficient biocatalysis with immobilized enzymes or encapsulated whole cell microorganism by using the SpinChem reactor system, Efficient synthesis of chiral lactones by encapsulated cells in a rotating bed reactor, L-Asparaginase production in rotating bed reactor from Rhizopus microsporus IBBL-2 using immobilized Ca-alginate beads, Lipase catalyzed regioselective lactamization as a key step in the synthesis of N-Boc (2R)-1,4-oxazepane-2-carboxylic acid, Mass transfer revolutionized, How to find the optimal rotational speed when using a rotating bed reactor, Recent advances in whole cell biocatalysis techniques bridging from investigative to industrial scale, Role of biocatalysis in sustainable chemistry, Simple scale-up using flexible reactors, SpinChem RBR S3 and S3+ Assembly Guide, SpinChem RBR Tips ‘n’ Tricks, Lipase-catalyzed hydrolysis in 750 L using a rotating bed reactor, Epoxidation of Tall Oil Fatty Acids and Tall Oil Fatty Acids Methyl Esters Using the SpinChem Rotating Bed Reactor, Determination of kinetics and equilibria of heterogeneously catalyzed gas-phase reactions in gradientless autoclave reactors by using the total pressure method: Methanol synthesis