Population balance models predict purge performance by tracking granule size distribution, reducing reliance on large purge bins.
Integrated catalyst transport passage eliminates hopper cones and expansion joints to reduce inventory and simplify removal.
Segmenting the reaction into dispersed droplets maintains effective heat exchange below 240°C, preventing fouling and eliminating de-volatilization steps.
A valveless piston pump transfers catalyst slurry vertically to prevent attrition and reduce oil residue in polymer products.
Discontinuous thermal runaway reducing agent addition prevents hot spots in fluidized bed reactors while maintaining catalyst activity.
Intermediary pressure chambers separate hydrogen from polymer particles, reducing agglomeration risks and enabling independent reactor operation.
A multi-bed catalytic converter merges separate shell-and-tube units into one structure, reducing tube sheets and welds while maintaining inter-bed cooling.
Curved inner surfaces eliminate stagnant zones and prevent resin accumulation, allowing continuous reactor operation without shutdowns.
Series cyclones remove agglomerates from a double cone reactor, enabling high gas velocities and stable operation.