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    • 9. 发明专利
    • Process to control hydraulic wash column, comprises feeding mother liquor, conducting liquor to filter tube, feeding control liquor to wash column, purifying liquor, transporting crystal bed, removing crystal and determining flow rate
    • DE102005018702A1
    • 2006-10-26
    • DE102005018702
    • 2005-04-21
    • BASF AG
    • HEILEK JOERGMUELLER-ENGEL KLAUS JOACHIMHAMMON ULRICHWALTER THOMAS
    • B01D9/00C07B63/00C07C57/07
    • Process for controlling a hydraulic wash column having a cylindrical shell (1) which delimits the column and within which filter tubes (2) in the vicinity of the second end of column and at least one filter (3) in the filter tube wall, comprises: feeding of mother liquor (7) into first end of column; conducting mother liquor into filter tube; feeding control liquor (9) into wash column (12); purifying the mother liquor and control liquor flow; transporting the crystal bed (10); continuous removing; melting; passing the melt through the crystal bed; and determining flow rates. Process for controlling a hydraulic wash column comprises: continuous feeding of a stream of a suspension comprises a substance to be purified suspended in a mother liquor (7) into the first end of the column with a pressure P2, which is greater than P1; conducting the mother liquor through the filters into the filter tube interior and out of the column through the filter tubes; feeding the control liquor (9) into the wash column (12) at the first end of the column and/or between this end and the start of the filter; purifying the mother liquor and control liquor flow in the column from the crystal bed of the substance, where the crystal bed (10) is having a buildup front faces the first end of the column and at which the crystals are added continuously to the crystal bed; transporting the crystal bed by the force resulting from the hydraulic flow pressure drop of the mother liquor and the control liquor flow in the column, where the filters into the wash zone disposed between the filters and the second end of the wash column; continuous removing of the crystals at the opposite end of the crystal bed to the buildup front; melting the removed crystals; passing the melt through the crystal bed as a wash liquid stream coming from the second end of the column against the transport direction of the crystals; and determining the flow rates of the control liquor and/or suspension conducted into the wash column by utilizing at least one pressure difference delta P s k, which exists in the column between at least one point in the zone projecting from the buildup front up to the end of the crystal bed (preferably in the concentration zone, projecting up to the start of the wash zone, of the crystal bed), where the hydraulic wash column has a cylindrical shell (1), which delimits and within which one or more filter tubes (2) extend through the column parallel to the cylinder axis and have, in the vicinity of the second end of the column, at least one filter (3) in the filter tube wall, which forms the sole direct connection between the filter tube interior under the pressure P1 and the interior of the column.