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    4.
    发明专利
    未知

    公开(公告)号：DE1253701B

    公开(公告)日：1967-11-09

    申请号：DEB0085824

    申请日：1966-02-16

    Applicant: BASF AG

    Inventor： WEITZ DR HANS-MARTIN ,  HAUSDOERFER DIPL-ING DR BERTHO ,  KOOPMANN DR JUERGEN

    IPC: B01J10/00 ,  C07C17/02

    Abstract: 1,168,695. Mixing apparatus. BADISCHE ANILIN-& SODA-FABRIK A.G. 15 Feb., 1967 [16 Feb., 1966], No. 7234/67. Heading B1C. [Also in Division C2] An apparatus for mixing gases, e.g. bromine and butadiene, in such a way as to produce turbulent flow (the Reynold number being above 2300), comprises a loop-shaped reactor 4 into which the gases are continuously introduced via nozzles 3 and 7 at such a velocity that the impulse transmitted to the gas causes it to circulate. The gases may be produced by evaporating liquids stored in tanks 1 and 5. Any liquid condensing in the bottom of the reactor may be recirculated via pump 9, condenser 10 and nozzle 8; discharge is effected through tank 11.

    10.
    发明专利
    未知

    公开(公告)号：DE1902461A1

    公开(公告)日：1970-07-23

    申请号：DE1902461

    申请日：1969-01-18

    Applicant: BASF AG

    Inventor： WEITZ DR HANS-MARTIN ,  FUERST DR ERNST

    IPC: B01D11/04 ,  C07C7/10 ,  C10G21/20

    Abstract: 1286891 Extraction to separate aromatic hydrocarbons BADISCHE ANILIN- & SODAFABRIK AG 16 Jan 1970 [18 Jan 1969] 2220/70 Heading C5E Aromatic compounds are recovered from hydrocarbon feeds by extraction with a solvent containing (a) an N-alkylpyrrolidone together with (b) one or more compounds of the Formula I where Y is an alkylene or alkenylene group containing 2 or 3 carbon atoms or an o-phenylene group which can be partially hydrogenated, Z is an oxygen atom or two hydrogen atoms, and where R is an alkylene group of 2 to 12 carbon atoms. The solvent can contain 1-10 wt. per cent water and component (a) can be N-methylpyrrolidone and component (b) is suitably the N-hydroxyethyl derivative of pyrrolidone, maleimide, succinimide, glutarimide, phthalimide or of the imide of tetrahydrophthalic acid. Benzene, toluene, xylene, ethylbenzene, styrene and naphthalene can be separated from feeds such as straight-run gasolines, cracked gasolines, pyrolysis gasolines, low-temperature coking gasolines, reformed gasolines, diesel oils, gas oils and lubricating oils by batchwise or countercurrent liquid-liquid solvent extraction, countercurrent washing of vapours or extractive distillation. Fig. 1 illustrates a solvent extraction in which the feed enters the bottom of the column 1 and the extraction solvent is fed to the top of the column to produce a raffinate P and an extract phase which is removed from the bottom of the column. The extract is distilled at 3 to produce a stream of light hydrocarbons which is condensed at 4 and recycled to the bottom of the column 1, the extracting solvent which is removed from the bottom of the column 3 and recycled to the extraction, and an aromatic vapour stream which is washed at 5 with some of the condensed aromatic product. Fig. 2 (not shown) illustrates the separation of aromatics by countercurrent washing; the feed is vapourized at 7 and washed by a countercurrent of the liquid extraction solvent which is passed into the top of the column 6. The non-aromatic vapour P is condensed and part of the condensate is used to wash the non-aromatic vapour and recycled to the column 6. The extract containing the aromatics is distilled at 8 to provide a light hydrocarbon stream which is recycled to the washing column 6, recovered solvent which is recycled and an aromatic stream which is washed. In an example pure benzene is separated from a mixture of 50 parts by volume nheptane, 40 parts benzene and 10 parts cyclohexene by batchwise solvent extraction with a mixture of equal volumes of N-methylpyrrolidone and N-hydroxyethyl succinimide.

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