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公开(公告)号:DE1557018A1
公开(公告)日:1970-03-12
申请号:DEB0086601
申请日:1966-04-09
Applicant: BASF AG
Inventor: RICHARD SINN DR , GUENTER HERRMANN DR , OTTO NAGEL DR , HUBERTUS SCHEURING DIPL-ING , PAUL HORNBERGER DR
IPC: B01F3/04 , B01F3/08 , B01F5/02 , B01F13/10 , B01J10/00 , C02F3/12 , C07C29/50 , C07C45/33 , B01F
Abstract: 1,173,812. Circulation mixers. BADISCHE ANILIN-& SODA-FABRIK A.G. 7 April, 1967 [9 April, 1966], No. 16065/67. Heading B1C. [Also in Division C2] In a process and apparatus for mixing gas and liquid into a liquid medium, the gas and liquid (which has a velocity of 5-100 m/sec) are injected through nozzles into an openended chamber the mean inlet diameter of which is twice to twenty times the mean diameter of the liquid nozzle, and the length of of which is three to thirty times the diameter of the equivalent cylindrical tube (if the chamber is not of circular cross-section). As shown the chamber is a tube 3; liquid and gas are injected by coaxial nozzles 1, 2; and mixture is discharged at 10. Part of the liquid is externally recirculated by a pump 9, and there may be a tube 7 through which internal circulation in either direction may take place on the air lift principle with the assistance of guide baffles (not depicted). The chamber may be a conical frustum, or (see Fig. 2, not shown) annular (3) in conjunction with radial nozzles (1, 2) in star formation. The process may be applied to the oxidation of hydrocarbons especially cyclohexane.
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公开(公告)号:DE1545234A1
公开(公告)日:1969-06-26
申请号:DE1545234
申请日:1965-09-01
Applicant: BASF AG
Inventor: DIETER STOCKBURGER DR DIPL-ING , RICHARD SINN DR , LUDWIG RAICHLE DIPL-ING , KARL BUSCHMANN DR , WOLF-DIETER STEGE DIPL-ING
Abstract: 1,149,950. Coking; recovering hydrocarbon quench oils. BADISCHE ANILIN- & SODAFABRIK A.G. 31 Aug., 1966 [1 Sept., 1965], No. 38818/66. Heading C5E. Hydrocarbons and chlorinated hydrocarbons containing carbon black, e.g. obtained by washing hot gases, are recovered and particulate coke is produced from the carbon black by atomizing the hydrocarbons containing the carbon black and contacting the atomized material with a stream of hot gas to evaporate the hydrocarbons without cracking them. Hydrocarbons boiling in the range 140 to 350 C., e.g. propylbenzene, xylenes, naphthalene, and chloronaphthalene are mentioned and the hot gas stream should be free of oxygen, halogens and halohydrocarbons, examples being superheated steam, superheated hydrocarbon vapour, nitrogen, flue gas and cracked gas, and the maximum temperature is 800 C. A binder, e.g. resins, asphalt or bitumen, may be added to the mixture to be treated. The coke particles are separated from the gas/vapour stream and the hydrocarbons are recovered therefrom by conventional methods. Concurrent or counter-current contacting of the gas with the hydrocarbon may be employed, and in one embodiment (see Fig. 3, not shown), coking &c. is completed in a fluidized bed. The gas may be recycled after recovering the hydrocarbons therefrom. An example is described.
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公开(公告)号:DE1498572A1
公开(公告)日:1969-02-20
申请号:DE1498572
申请日:1963-03-16
Applicant: BASF AG
Inventor: RICHARD SINN DR , HERMANN KIENITZ DR , FRITZ ELLER DIPL-ING
IPC: B01L9/02
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