Abstract: The liquid content of sugar cane bagasse is reduced by a low pressure process having a substantially longer duration than the duration of prior art high pressure liquid removal processes. For this purpose the liquid containing bagasse, as it emerges from a diffuser, is exposed to a relatively slowly increasing yet low pressure as compared to prior art high pressures, whereby the bagasse travels with a substantially constant speed sequentially through a dewatering zone, wherein a further compaction takes place, a preliminary squeeze-out zone and a final squeeze-out zone. During the preliminary squeeze-out the pressure above an open surface area or section without a sieve or screen is about 0.2 kg/cm.sup.2. During the final squeeze-out the pressure (p) is about p/0.6D>0.003, wherein D is the diameter, in mm, of a squeeze-out roller. The pressing duration t in seconds is also related to the squeeze-out roller diameter D such that D:t is smaller than a constant value K.

Abstract: The liquid content of sugar cane bagasse is reduced by a low pressure process having a substantially longer duration than the duration of prior art high pressure liquid removal processes. For this purpose the liquid containing bagasse, as it emerges from a diffuser, is exposed to a relatively slowly increasing yet low pressure as compared to prior art high pressures, whereby the bagasse travels with a substantially constant speed sequentially through a dewatering zone, wherein a further compaction takes place, a preliminary squeeze-out zone and a final squeeze-out zone. During the preliminary squeeze-out the pressure above an open surface area or section without a sieve or screen is about 0.2 kg/cm.sup.2. During the final squeeze-out the pressure (p) is about p/0.6D>0.003, wherein D is the diameter, in mm, of a squeeze-out roller. The pressing duration t in seconds is also related to the squeeze-out roller diameter D such that D:t is smaller than a constant value K 16.