Abstract The process for separating the solid particles in the column is based on the intermittent supply of pressurized suspension to the apparatus which pressure supplies the energy required for feeding the suspension near one end into the column, the squeezing of the suspension liquid out of the suspension under withdrawal of the suspension liquid from the column near that same end of the column, the compaction of the solid particles, the transport of the compacted bed of particles towards the opposite end of the column and the washing of the compacted bed with wash liquid, the bed is mechanically disintegrated, the product of this disintegration is removed in suspended form while maintaining a wash front separating the non washed and washed parts in the compacted bed.
A process comprising separating solid particles from a liquid suspension and/or purification or leaching of solid particles in a column based on the pulsating movement of a compacted bed in this column to which a liquid suspension, under withdrawal of liquid phase, by supplying pulsewise at one end of the column and disintegrating the washed compacted bed removing the product of this disintegration at the opposite end of the column, moving the washfront in the compacted bed between two outermost limits in the compacted bed, supplying the energy for the compacting and filtering of the suspension, the transport of the compacted bed to the scraper and the washing by the feeding pump 13, while operating the wash column at pressures P 2 and P 3 determined by permeability and length of the compacted bed, the feed rate of the suspension, the fraction of suspended solids in the feed, the wall friction and the pressure of the scraper against the bed.
Claim 2
Dependent Claim
160 words
A process comprising separating solid particles from a liquid suspension and/or purification or leaching of solid particles in a column based on the pulsating movement of a compacted bed in this column to which a liquid suspension, under withdrawal of liquid phase, by supplying pulsewise at one end of the column and disintegrating the washed compacted bed removing the product of this disintegration at the opposite end of the column, moving the washfront in the compacted bed between two outermost limits in the compacted bed, supplying the energy for the compacting and filtering of the suspension, the transport of the compacted bed to the scraper and the washing by the feeding pump 13, while operating the wash column at pressures P 2 and P 3 determined by permeability and length of the compacted bed, the feed rate of the suspension, the fraction of suspended solids in the feed, the wall friction and the pressure of the scraper against the bed.
Claim 3
Dependent Claim
23 words
A process according to claim 1 characterized in that a total cycle of the feeding and washing amounts between 0.1 and 40 seconds.