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公开(公告)号:US3639659A
公开(公告)日:1972-02-01
申请号:US3639659D
申请日:1969-03-28
Applicant: BASF AG
Inventor: NIESWANDT WERNER , LINGE HERMANN , PIRZER HANS , HOERAUF WERNER , HETZ HERBERT
CPC classification number: C08G69/46
Abstract: PROCESS FOR THE CONTINUOUS EXTRACTION OF LOW MOLECULAR WEIGHT CONSTITUENTS FROM GRANULAR POLYAMIDES IN AN EXTRACTION ZONE IN WHOSE UPPER PART THE EXTRACTANT IS RECYCLED.
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公开(公告)号:US3905946A
公开(公告)日:1975-09-16
申请号:US39224473
申请日:1973-08-28
Applicant: BASF AG
Inventor: NIESWANDT WERNER , HOERAUF WERNER , GUENTHER ERNST , KISSEL ERNST , NEUMANN ECKART , VALENTIN GUENTER
IPC: C08G69/00 , B01D11/02 , C07D201/12 , C08G69/46
CPC classification number: C08G69/46
Abstract: Continuous extraction of polylactam granules for the removal of monomers and/or oligomers therefrom by means of hot water flowing countercurrently in an extraction zone, which extraction zone is divided into subzones by at least one heating zone and the water is accelerated, at certain time intervals, cocurrently and countercurrently to the flow of granules.
Abstract translation: 连续提取多内酰胺颗粒以通过在提取区域中逆流流动的热水从其中除去单体和/或低聚物,该提取区通过至少一个加热区被分成次区域,并以特定的时间间隔加速水 与流动的流动并流逆流。
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公开(公告)号:AU525107B2
公开(公告)日:1982-10-21
申请号:AU3845878
申请日:1978-07-28
Applicant: BASF AG
Inventor: HOERAUF WERNER , VALENTIN GUENTER , KEGEL ROBERT , KUHN KELMUT
IPC: B29B9/00 , B29B7/00 , B29B9/06 , B29C47/00 , B29C47/78 , B29C48/30 , B29C48/76 , B29C48/92 , B29F3/03
Abstract: A process for removing volatile constituents which are evolved from plastic melts when extruding the latter and are drawn off together with the surrounding air. The volatile constituents are drawn off immediately as they are evolved by the plastic melt and the air containing such volatile constituents is heated immediately after entering the suction orifice, and an apparatus for carrying out this process.
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公开(公告)号:CA1076743A
公开(公告)日:1980-04-29
申请号:CA266548
申请日:1976-11-25
Applicant: BASF AG
Inventor: MATTHIES PAUL , KUNDE JOACHIM , HOERAUF WERNER
Abstract: O.Z. 31,765 An improved process for the continuous polymerization of .epsilon.-capro-lactam in the presence of water as initiator in a vertical downward-flow tubular reactor, in which the .epsilon.-caprolactam is partially polymerized at elevated temperature in a first, mechanically agitated reaction zone and is further polymerized in further reaction zones to the desired degree of polymerization. Poly-.epsilon.-caprolactam is discharged in the form of a melt. The polymerization is carried out at a gauge pressure of from 0.2 to 0.9 bar, constant in all reaction zones. The temperature in the first reaction zone is from 260 to 295.degree.C whilst obeying the condition t ? 265 + 43 p .degree.C, wherep is the numerical value of the gauge pressure in bars.
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公开(公告)号:CA1012679A
公开(公告)日:1977-06-21
申请号:CA179854
申请日:1973-08-28
Applicant: BASF AG
Inventor: NIESWANDT WERNER , HOERAUF WERNER , GUENTHER ERNST , KISSEL ERNST , NEUMANN ECKART , VALENTIN GUENTHER
IPC: C08G69/00 , B01D11/02 , C07D201/12 , C08G69/46
Abstract: Continuous extraction of polylactam granules for the removal of monomers and/or oligomers therefrom by means of hot water flowing countercurrently in an extraction zone, which extraction zone is divided into subzones by at least one heating zone and the water is accelerated, at certain time intervals, cocurrently and countercurrently to the flow of granules.
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公开(公告)号:CA754235A
公开(公告)日:1967-03-07
申请号:CA754235D
Applicant: BASF AG
Inventor: ILLING GERHARD , LINGE HERMANN , HOERAUF WERNER
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公开(公告)号:CA1187852A
公开(公告)日:1985-05-28
申请号:CA406727
申请日:1982-07-06
Applicant: BASF AG
Inventor: BELDE HORST , LANGENFELDER HANS , HOERAUF WERNER
Abstract: Aqueous suspensions of finely divided titanium dioxide are produced in the presence of dispersants by a process in which titanium dioxide powder and caprolactam are kneaded together in the dry state at from 15 to 40.degree.C, the resulting mixture is kneaded with the addition of water, the paste thus obtained is suspended in water, the suspension is then allowed to sediment, and the resulting suspension containing finely divided titanium dioxide is decanted.
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公开(公告)号:CA1066030A
公开(公告)日:1979-11-13
申请号:CA218338
申请日:1975-01-21
Applicant: BASF AG
Inventor: HOERAUF WERNER , GUENTHER ERNST , KISSEL ERNST , VALENTIN GUENTER , DIETRICH ERNST
Abstract: An extraction tube for the continuous removal of low molecular weight components of polylactam granules by means of hot water by the countercurrent principle of operation, the water being fed upwardly and the granules downwardly, the tube being provided with inlets and outlets for the granules and the water and exhibiting baffles within the tube, wherein there is provided, within the tube, a heat exchanger which (a) divides the tube into two sections bearing a ratio to each other of from 50:50 to 85:15 by volume, the smaller section being at the top of the tube, (b) exhibits ducts for the granules over the entire cross-section of the tube and (c) has upper inlet surfaces leading into each duct on the upper side of said heat exchanger facing the stream of granules, said inlet surfaces being inclined to taper inwardly toward the vertical ducts at an angle .beta. to the horizontal, this angle being equal to or greater than the angle of repose of the granules but less than 90.degree., further similar heat exchangers being provided beneath said heat exchanger if desired.
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公开(公告)号:FR1347623A
公开(公告)日:1963-12-27
申请号:FR925419
申请日:1963-02-20
Applicant: BASF AG
Inventor: ILLING GERHARD , LINGE HERMANN , HOERAUF WERNER
IPC: C08G69/14 , C08K5/3412
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公开(公告)号:CA1150445A
公开(公告)日:1983-07-19
申请号:CA350012
申请日:1980-04-16
Applicant: BASF AG
Inventor: ROTZOLL RUDI-HEINZ , MATTHIES PAUL , VALENTIN GUENTER , HOERAUF WERNER
Abstract: The present invention is directed to a process for the continuous preparation of polycaprolactam which comprises: passing .epsilon.-caprolactam in the presence of water as an initiator downwardly through a vertical tubular reactor, wherein the .epsilon.-caprolactam is partially polymerized at a temperature of from 245 to 260.degree.C in a mixing zone equipped with a mechanical stirrer, which zone has a diameter which is 30 to 80% greater than that of the balance of the tube, circulating the polymerizing caprolactam melt through a heat exchange zone located at a distance from the stirrer which is 0.3 to 1.5 times the diameter of the narrower part of the tube, in the lower part of the mechanically mixed reaction zone, passing the melt through additional heat exchange zones at a temperature of from 240 to 290.degree.C, wherein the desired degree of polymerization is reached, and thereafter discharging poly-.epsilon.-caprolactam as a melt from the tubular reactor.
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