公开(公告)号：AU2333777A

公开(公告)日：1978-09-21

申请号：AU2333777

申请日：1977-03-17

Applicant: BASF AG

Inventor： PLATZ ROLF ,  FUCHS WERNER ,  RIEBER NORBERT ,  SAMEL ULF-RAINER ,  JUNG JOHANN ,  WUERZER BRUNO

IPC: A01N43/54 ,  A01N43/836 ,  A01N43/90 ,  A01N47/16 ,  A01N55/10 ,  A01P21/00 ,  C07D229/00 ,  C07D487/04 ,  C07D487/08 ,  C07D519/00 ,  A01N5/00

Abstract: New and valuable polycyclic compounds which contain nitrogen-containing rings and have a strong action on plants, agents for influencing plant growth containing these compounds, and a method of influencing plant growth with these compounds.

公开(公告)号：CA1003850A

公开(公告)日：1977-01-18

申请号：CA150721

申请日：1972-08-30

Applicant: BRESSEL ULRICH ,  FUCHS WERNER ,  PLATZ ROLF ,  BASF AG

Inventor： BRESSEL ULRICH ,  FUCHS WERNER ,  PLATZ ROLF ,  BADISCHE ANILIN-SODA FABRIK AK

IPC: C07C5/48 ,  C07B31/00 ,  C07B35/04 ,  C07C1/00 ,  C07C5/44 ,  C07C5/56 ,  C07C11/00 ,  C07C15/44 ,  C07C67/00 ,  C07C69/54

Abstract: Dehydrogenation of isobutyronitrile, ethylbenzene or methyl isobutyrate with iodine and oxygen into methacrylonitrile, styrene or methyl methacrylate at 400 DEG to 800 DEG C is carried out in a reaction chamber in which there are arranged, in the direction of flow of the bulk of the reactants introduced through a nozzle, coaxially from inside to outside first a mixing zone and then a circulation tube.

公开(公告)号：CA947639A

公开(公告)日：1974-05-21

申请号：CA82192

申请日：1970-05-07

Applicant: BASF AG

Inventor： PLATZ ROLF ,  FUCHS WERNER ,  NAGEL OTTO

IPC: B01F3/04 ,  B01F3/08 ,  B01F5/02 ,  C02F3/12 ,  C02F3/22 ,  C12M1/08

Abstract: 1303163 Aerating liquids BADISCHE ANILIN- & SODA-FABRIK AG 7 May 1970 [8 May 1969] 22051/70 Heading B1C Liquid is aerated by means of an ejector which dips into the liquid. The ejector has a central tube 3 through which liquid flows, e.g. from a pump, and induces a flow of air through a surrounding tube 4. The air and liquid pass through a mixing tube 5 completely immersed in the liquid, inducing through the tube 5 the circulation of the liquid in the container. The liquid may be a lake or river, or be in a container 1 as shown. The process may be used to speed up fermentations, or to aerate sewage. The liquid flows through the tube 3 at between 5 and 100 m/sec., the diameter of the mixing tube 5 is 2-20 times the diameter of the tube 3, and the length of the mixing tube 5 is 2-30 times the diameter of the mixing tube.

公开(公告)号：CA887106A

公开(公告)日：1971-11-30

申请号：CA887106D

Applicant: BASF AG

Inventor： MERGER FRANZ ,  FUCHS WERNER

公开(公告)号：CA713588A

公开(公告)日：1965-07-13

申请号：CA713588D

Applicant: BASF AG

Inventor： KROEPER HUGO ,  FUCHS WERNER ,  PLATZ ROLF

公开(公告)号：GB951518A

公开(公告)日：1964-03-04

申请号：GB563462

申请日：1962-02-14

Applicant: BASF AG

Inventor： PLATZ ROLF ,  FUCHS WERNER

IPC: C10G51/02 ,  C10K3/00 ,  C10K3/02

Abstract: A process for producing high calorific value fuel gas comprises cracking liquid hydrocarbons with oxygen by the submerged-flame process and passing the product at an elevated temperature over a catalyst containing at least one element or compound of a Group VI or VIII metal. The gaseous product from the submerged flame process may be cooled before and after passing over the catalyst, and at normal or increased pressures, e.g. 8 atmospheres gauge. The temperature of the catalyst may be from 60 DEG to 400 DEG C. The catalyst may be supported on a carrier and may be a fixed or fluidized bed, and is exemplified by oxides and/or sulphides of chromium, molybdenum, tungsten, iron group metals such as nickel or cobalt, or platinum metals such as palladium. Mixtures of the oxides and/or sulphides of Group VI metals with Group VIII metals may also be used. Suitable carriers are aluminium oxide, aluminiferrous clays, alumina cements, pumice, or silica gel, and may be of 2-50 mm. grain size for the fixed bed, and 0.01 to 10 mm. for the fluidized bed. Specification 827,438 is referred to.

公开(公告)号：FR1285772A

公开(公告)日：1962-02-23

申请号：FR857894

申请日：1961-04-06

Applicant: BASF AG

Inventor： FUCHS WERNER

IPC: C10K1/10 ,  C10K1/16