Abstract: A transfer device for passing material between two different fluid environments which uses a multi-passageway rotor member rotatable about a vertical axis and interposed between upper and lower ported members. Each passageway (or chamber) passes through the rotor and has a major axis parallel to the vertical axis of the rotor. Rotation of the rotor brings each passageway successively into fluid communication with the upper ported member whereby the passageway is filled with material, then to at least one position where the passageway is not aligned with either ported member, and finally to a position where the passageway is aligned with the lower ported member and the material is transferred to the second environment. The rotation may be continuous or incremental, and the fluid environments are maintained in isolation from each other. Methods of transferring solids, and a solids transfer system in a steam hydrolysis and drying plant are also disclosed.

Abstract: A transfer device for passing material between two different fluid environments which uses a multi-passageway rotor member rotatable about a vertical axis and interposed between upper and lower ported members. Each passageway (or chamber) passes through the rotor and has a major axis parallel to the vertical axis of the rotor. Rotation of the rotor brings each passageway successively into fluid communication with the upper ported member whereby the passageway is filled with material, then to at least one position where the passageway is not aligned with either ported member, and finally to a position where the passageway is aligned with the lower ported member and the material is transferred to the second environment. The rotation may be continuous or incremental, and the fluid environments are maintained in isolation from each other. Methods of transferring solids, and a solids transfer system in a steam hydrolysis and drying plant are also disclosed.

Abstract: An energy efficient process for hydrolyzing lignocellulosic materials which comprises using a primary system by providing a start-up energy input to operating saturated steam conditions and thereafter operating the primary system with substantially constant energy input, the condition of the hydrolyzing saturated steam being controlled by water injection and/or steam bleeding from the primary system. The dwell time of the solids stream in the primary sustem is controlled by controlling its passage with flashing off of steam into a secondary system where drying occurs together with some small measure of hydrolysis in a lower pressure superheated steam environment, there being an energy input into the secondary system using steam bled from the primary system. The output solids material stream is preferably capable of being self polymerized into a formed shape eg a board.