Extended Data Fig. 2: Influence of pressure and temperature on performance and viscosity.
From: Assessment of transport phenomena in catalyst effectiveness for chemical polyolefin recycling
a,b, Variation of product distribution with pressure (a) and temperature (b) for hydrogenolysis of HDPE200. Corresponding results for PP340 are available in Supplementary Fig. 4. c, Three-phase CFD simulations of viscosity distribution (top) and Reynolds number (bottom) at the mid x-y plane of the stirrer at different temperatures. Values in Supplementary Table 7. Reaction and simulated conditions: dp = 0.0-0.2 mm (0.2 mm for simulations), stirrer = impeller, stirring rate = 750 r.p.m.
