Literature is reviewed relating to the treatment of phytomass in an ap
paratus identified as a ''flow-through reactor'' (FTR), i.e. one in wh
ich a solid phase (such as phytomass) is held immobile within the reac
tor while a fluid phase is caused to flow, usually at a steady rare, t
hrough the reactor. Fluid flow through nit FTR may be characterized in
terms of average residence time (RT), residence time distribution (RT
D), and in other ways. Differences between results obtained from an FT
R versus a batch reactor (BR), i.e. one in which the reactive fluid al
ways remains contained with ill the reactor; are pointed out. Many sig
nificant results have arisen from laboratory FTR experiments in wood c
hemistry and pulp and paper technology.