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公开(公告)号:BR112014015258A8
公开(公告)日:2017-07-04
申请号:BR112014015258
申请日:2012-12-17
Applicant: BASF SE
Inventor: BERNHARD SCHMIED , FRANK BRAUN , GREGOR HAVERKEMPER , JAN HOLOCH , KLAUS HAHN , LIBOR SEDA , PASCAL HESSE , PATRICK SPIES , RAINER OSTERMANN , UWE - JOHANNES LEHNEN
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公开(公告)号:MY145366A
公开(公告)日:2012-01-31
申请号:MYPI20085049
申请日:2008-12-12
Applicant: BASF SE
Inventor: THILO KREBS , JAN HOLOCH , BERNHARD SCHMIED
IPC: C08F2/18
Abstract: PROCESS FOR PRODUCTION OF EXPANDABLE STYRENE POLYMERS 5 A PROCESS FOR PRODUCTION OF EXPANDABLE STYRENE POLYMERS WITH NARROW BEAD-SIZE DISTRIBUTION WITH HIGH SPECIFIC REACTOR YIELD VIA POLYMERIZATION OF THE MONOMERS IN AQUEOUS SUSPENSION IN A STIRRED TANK IN THE PRESENCE OF A VOLATILE BLOWING AGENT, WHERE THE STYRENE-CONTAINING ORGANIC PHASE IS ADDED SIMULTANEOUSLY WITH THE AQUEOUS PHASE TO THE STIRRED TANK OVER A PERIOD OF FROM 5 10 TO 60 MINUTES.
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3.
公开(公告)号:BR112014015248A2
公开(公告)日:2017-06-13
申请号:BR112014015248
申请日:2012-12-17
Applicant: BASF SE
Inventor: BERNHARD SCMIED , FRANKBRAUN , GREGOR HAVERKEMPER , JAN HOLOCH , KLAUS HAHN , LIBOR SEDA , PASCAL HESSE , PATRICK SPIES , RAINER OSTERMANN , UWE-JOHANNES LEHNEN
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4.
公开(公告)号:BR112014015248A8
公开(公告)日:2017-07-04
申请号:BR112014015248
申请日:2012-12-17
Applicant: BASF SE
Inventor: BERNHARD SCMIED , FRANKBRAUN , GREGOR HAVERKEMPER , JAN HOLOCH , KLAUS HAHN , LIBOR SEDA , PASCAL HESSE , PATRICK SPIES , RAINER OSTERMANN , UWE-JOHANNES LEHNEN
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公开(公告)号:BR112014015258A2
公开(公告)日:2017-06-13
申请号:BR112014015258
申请日:2012-12-17
Applicant: BASF SE
Inventor: BERNHARD SCHMIED , FRANK BRAUN , GREGOR HAVERKEMPER , JAN HOLOCH , KLAUS HAHN , LIBOR SEDA , PASCAL HESSE , PATRICK SPIES , RAINER OSTERMANN , UWE - JOHANNES LEHNEN
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公开(公告)号:MY147779A
公开(公告)日:2013-01-31
申请号:MYPI20083693
申请日:2007-03-15
Applicant: BASF SE
Inventor: PAULUS SCHMAUS , MICHAEL HEEGER , JOACHIM RUCH , JAN HOLOCH , CHRISTIAN RASCH
IPC: B29C44/34
Abstract: THE INVENTION RELATES TO A PROCESS AND AN APPARATUS FOR PELLETIZING POLYMER MELTS COMPRISING BLOWING AGENT IN A PELLETIZING CHAMBER (1) THROUGH WHICH A LIQUID FLOWS, ITS PRESSURE BEING ABOVE THE AMBIENT PRESSURE. IN A FIRST STEP, THE POLYMER MELT IS INJECTED INTO THE PELLETIZING CHAMBER (1), IN A SECOND STEP THE POLYMER MELT IS CUT VIA A CUTTING APPARATUS INTO INDIVIDUAL PELLETS AND, IN A THIRD STEP, THE PELLETS PRODUCED IN THE PELLETIZING PROCESS ARE DISCHARGED WITH THE LIQUID FROM THE PELLETIZING CHAMBER (1) AND ARE THEN ISOLATED FROM THE LIQUID. THIS PROCESS ALSO COMPRISES AT LEAST ONE OF THE FOLLOWING STEPS: (A) COMMINUTION OF AGGLOMERATES OR OF PELLETS WHICH EXCEED A PRESCRIBED MAXIMUM SIZE, IN A COMMINUTING MACHINE (23) DOWNSTREAM OF THE PELLETIZING CHAMBER (1) OR IN A COMMINUTING UNIT DOWNSTREAM OF THE CUTTING APPARATUS, (B) DEPRESSURIZATION OF THE LIQUID IN A DEPRESSURIZING MACHINE (14),(C) DEPRESSURIZATION OF THE LIQUID IN A THROTTLE APPARATUS (28), WHERE THERE IS, UPSTREAM OF THE THROTTLE APPARATUS (28), A PRESSURE-EQUALIZING CONTAINER (33), (D) ISOLATION OF THE PELLETS FROM THE LIQUID, WITHOUT ANY PRIOR DEPRESSURIZATION OF THE LIQUID WITH THE PELLETS WHICH IT COMPRISES.
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