The convective heat transfer coefficient and pressure drop in ceramic
foam structures are measured. Cordierite foams with 10, 20, 30 und 50
pores per inch (PPI) at empty tube velocities (of air) at 0.5 to 14 m/
s are investigated. The convective heat transfer between fluid and sub
strate is described well within this velocity range by means of the as
sumption Nu = c . Re(m) . Pr1/3. The experimental method developed to
obtain the values of c and m is described. The data thus gained are di
scussed in view of an application of ceramic foams as catalyst support
s and are compared with data of conventional parallel channel monolith
s mentioned in the literature.