The present invention relates to a method of producing lignin with reduced amount of guaiacoland etylguaiacol in order to reduce the content of odorous substances by subjecting the ligninto a heating processing order to remove guaiacol.

In order to enable dehydration of a slurry of expanded particles with a simple structure, a dehydration device includes: a transporting tube configured to transport a liquid mixture of expanded particles, the transporting tube having a curved part in which the transporting tube is curved, and a mesh member provided to the curved part of the transporting tube. The mesh member is configured to separate the expanded particles and a liquid component in the liquid mixture from each other.

A DAF skimmings separation system 10 that processes SPN/DAF skimmings 11 received from a meat processing facility to separate water and SPN-content solids includes a heating chamber coupled to a processor chamber having one or more pressurized discharge nozzles that expels DAF skimmings onto a spatter plate to cause SPN animal components within the DAF skimmings to break into smaller pieces denaturing the molecular structure and allowing the entrapped moisture to be evaporated within a heated airstream in the processing chamber, for separating nutritionally valuable SPN while reducing moisture content. A method of processing DAF skimmings to yield dryer SPN with reduced moisture content is disclosed.

The invention is based on a star-shaped rotation dryer (1) for segmenting a fluidizing chamber 4) into process compartments (11), whereby the star-shaped rotation dryer (1) is pivot mounted and features dividing wall (9) or similar for the conveyance of solid particles along a conveyance path, whereby a flow-receiving base (10) is detachably mounted below the star-shaped rotation dryer (1); the invention further relates to a method of spray-coating solid particles for the purpose of agglomeration, coating, layering, spray granulation or pelletization, whereby the retention time spectrum of the solid particles inside the fluid-bed apparatus (2) has a margin of at least 1:3 (alternatively tRTD903 tRTD10).

Herein is disclosed a spin flash dryer further comprising a waste outlet arranged in a chamber bottom of the spin flash dryer for removal of a residual organic waste material from a spin flash dryer during spin flash operation and a method of operating a such spin flash dryer to remove residual organic waste material from said spin flash dryer during operation.

A gas-particle processing method comprising: introducing gas into a chamber through a gas inlet; flowing the gas through the chamber from the gas inlet to the gas outlet at a first controlled mass flowrate; introducing at least one particle stream into the chamber through one or more particle inlets of the chamber at a second controlled mass flowrate; flowing each particle stream through a respective processing region in the chamber; and controlling the first and/or second mass flowrates, such that the gas-particle mixture porosity in a substantial portion of each processing region is 0.900-0.995.

Herein is disclosed a spin flash dryer further comprising a waste outlet arranged in a chamber bottom of the spin flash dryer for removal of a residual organic waste material from a spin flash dryer during spin flash operation and a method of operating a such spin flash dryer to remove residual organic waste material from said spin flash dryer during operation.