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    Method of crystallizing nitro products
    193.
    发明授权
    Method of crystallizing nitro products 失效

    公开(公告)号：US2874196A

    公开(公告)日：1959-02-17

    申请号：US47759154

    申请日：1954-12-24

    Applicant: BOFORS AB

    Inventor： TORVALD NORELL KARL

    IPC: C07C201/16

    CPC classification number: C07C201/16 ,  C07C205/06 ,  C07C205/12

    Abstract: Mononuclear aromatic nitro-compounds are crystallized from nitric acid of 55 to 68 per cent concentration in a quantity insufficient for a complete dissolution of the nitro-compounds during any part of the crystallization. The crude product of a nitration process may be mixed with the nitric acid in a small mixing vessel, where incipient crystallization occurs, and allowed to run into a larger vessel where the mixture is maintained at a lower temperature, crystals being separated by filtration or centrifuging. The mixture of nitro-compound and nitric acid may also be passed continuously through a series of three vessels at progressively decreasing temperatures, the final slurry being continuously taken to a filter or centrifuge; the mother liquor may then be cooled to a still lower temperature to obtain further crystals, which are returned to the mixing stage as such, or in solution in the nitric acid added thereto. In examples crude products are treated to obtain (1 to 5) 2,4,6-trinitroluene, (6) a dinitrochlorobenzene product (2,4- and 2,6-dinitrochlorobenzenes), and (7) m-dinitrobenzene.ALSO:A method of crystallizing mononuclear aromatic nitro-compounds, particularly di- and tri-nitro compounds, from nitric acid, is characterized in that acid of 55 to 68 per cent. concentration is used and in a quantity that is insufficient for a complete dissolution of the nitro-compounds during any part of the crystallization. Crude product of a nitration process may be mixed with the nitric acid in asmall mixing vessel, where incipient crystallization occurs, and allowed to run continuously into a larger crystallization vessel where the mixture is maintained at a lower temperature, and the crystals are separated by filtration or centrifuging. The mixture of nitro-compound and nitric acid may also be passed continuously through a series of three vessels at progressively decreasing temperatures, the final slurry being continuously taken to a filter or centrifuge; the mother liquor may then be cooled to a still lower temperature to obtain further crystals, which are returned to the mixing stage as such or in solution in the nitric acid added thereto. In examples (1 to 5) 2, 4, 6-trinitrotoluene is obtained from crude product, (6) a dinitrochlorobenzene product (2, 4- and 2, 6- dinitrochlorobenzenes) is obtained from crude material, and (7) m-dinitrobenzene is obtained from crude material. In the examples secondary products of lower solidification points are obtained on regeneration of the nitric acid solutions.

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