The main objective of this work was to determine the effects of pyroly
sis heating rate on intrinsic O-2 reactivity of coal chars. Relationsh
ips of intrinsic reactivity to other pyrolysis conditions and char phy
sical and chemical structure were also investigated, and empirical cor
relations were obtained. Two different entrained flow reactors (a flat
flame methane/air burner and a drop tube reactor) were used to prepar
e chars under a variety of different pyrolysis conditions at maximum p
article temperatures and heating rates of 840-1627 K and 10(4) to 2 x
10(5) Ws, respectively. Intrinsic reactivities of a lignite and two bi
tuminous coal chars decrease with increasing preparation heating rate.
Maximum particle temperature and heating rate are difficult preparati
on parameters to separate and were closely coupled in this work, as in
most entrained flow coal research. Indeed, much of the work described
in the literature defining the effects of pyrolysis heating rate on c
oal char reactivity has utilized vast residence time differences, comp
aring data from fixed bed (residence time of similar to 1 h) and entra
ined flow reactors (residence time of similar to 100 ms). It is conclu
ded from this work that observations made on the basis of such experim
entation are a function more of residence time and reactor variations
(packed or fixed bed, as opposed to entrained flow) than particle heat
ing rate. This work also provides evidence that intrinsic reactions of
O-2 With coal char (for the three coals observed in this study) are n
ot significantly influenced by large differences in char meso- or micr
opore surface area obtained by varying pyrolysis conditions.