For a pseudofluid consisting of a particle assembly, particle stress is tra
nsmitted through mutual contact between particles. When the particles are d
ensely agglomerated, contacts are usually of long duration and frictional,
and this part of the stress is the frictional stress. When the particles ar
e sparsely spaced, on the other hand, contacts are temporary and collisiona
l, and this part of the stress consists of kinetic and collisional stresses
. In many cases the particle contact lies between these two extremes in a g
as-solid fluidized bed, and all of these three parts of the stress-kinetic,
collisional, and frictional stresses-play important roles in particle-phas
e transport. However, the existing kinetic theory for granular flow (KTGF)
only involves the kinetic and collisional parts of transport. In this paper
, a frictional particle pressure was introduced for correction of KTGF in t
he case of highly dense flow, and the solid shear stress was corrected to b
e consistent with Einstein's effective viscosity equation for dilute suspen
sions. This modified KTGF model may account for the stress over the entire
range between two extremes of a densely packed state and a sparsely spaced
state. As verification in the dense gas-solid flow, the time-averaged total
pressure drop and the particle pressure predicted by this modified KTGF mo
del were found to be in agreement with the measurements in a cylindrical fl
uidized bed. The inflection point on the particle pressure curve, implying
competition among the three transport mechanisms, was also predicted. Moreo
ver, instantaneous formation of slugs starting from a homogeneous inflow co
ndition was reproduced through simulation and the quantitative comparison o
f the slug velocity with empirical correlation was approving. For dilute ga
s-solid flow in a circulating fluidized-bed riser, the model predictions ag
ree with the time-averaged solid viscosity in order of magnitude. Further m
odeling may require a better understanding of the drag force and turbulence
.