-
公开(公告)号:WO0216019A9
公开(公告)日:2004-05-13
申请号:PCT/EP0109683
申请日:2001-08-22
Applicant: BASELL POLIOLEFINE SPA , BIDELL WOLFGANG , LUTZ GERALD , LANGHAUSER FRANZ , SCHERER GUENTER , MECKELNBURG DIRK , OELZE JUERGEN , GERBIG HANS-JUERGEN , HUEHNERBEIN JUERGEN
Inventor: BIDELL WOLFGANG , LUTZ GERALD , LANGHAUSER FRANZ , SCHERER GUENTER , MECKELNBURG DIRK , OELZE JUERGEN , GERBIG HANS-JUERGEN , HUEHNERBEIN JUERGEN
IPC: B01J8/00 , B01J8/24 , C08F2/34 , C08F10/06 , C08F110/06 , C08F210/06 , G01F23/288
CPC classification number: B01J8/1809 , B01J8/001 , B01J2208/0061 , C08F10/06 , C08F110/06 , C08F210/06 , G01F23/2885 , C08F2/34 , C08F2500/12 , C08F2500/24 , C08F210/16
Abstract: The invention relates to a method for measuring the level of a medium in a reactor during continuously operated polymerisation processes, whereby the limiting surface of each phase in the reactor is measured with the aid of an ionising radiation. Said method is characterised in that at least one measuring unit, consisting of a radiation source that emits ionising radiation and a corresponding detector, is brought up to the limiting surface in the reactor and is fixed in a flexible manner in the vicinity. To measure the level of the medium, the limiting surface of the phase is determined by measuring the radioactive backscatter of said phase.
Abstract translation: 一种用于在连续操作的聚合反应器中的液位测量的过程中,各相的边界在反应器中测得的电离辐射的帮助下,其特征在于,其包含发射致电离辐射的辐射源,至少一个测量单元和在反应器中带来了相应的检测器在相界面和 固定有柔性的,该反应器的液位测量以这样一种方式,它确定由放射性反向散射测量的手段相界面进行。
-
公开(公告)号:TR200402352T4
公开(公告)日:2004-12-21
申请号:TR200402352
申请日:2001-05-23
Applicant: BASELL POLIOLEFINE SPA
Inventor: DAHN ULRICH , BIDELL WOLFGANG , ZIMMERMANN HANS-JUERGEN , HINGMANN ROLAND , ROESCH JOACHIM , SCHWEIER GUENTHER , OELZE JUERGEN
IPC: C08J5/00 , C08F2/00 , C08F4/642 , C08F10/06 , C08F110/06 , C08F210/06 , C08F297/08 , C08L53/00 , D01F6/30
Abstract: The invention relates to highly flowable propylene block copolymers that comprise 50 to 80 wt.-% of a propylene homopolymer and 10 to 70 wt.-% of a propylene copolymer having 5 to 50 wt.-% of a C 2 -C 8 alk-1-ene polymerized into it that is different from propylene, and that are obtainable from the gaseous phase by a two-step polymerization by means of a Ziegler-Natta catalyst system. In a first polymerization step, the propylene is polymerized at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of the reaction mixture of 0.3 to 5 hours in the presence of at least 2.0% by volume, based on the total volume, of hydrogen. The propylene homopolymer obtained in said first polymerization step is transferred together with the Ziegler-Natta catalyst system into an intermediate container, expanded for 0.01 to 5 minutes to less than 5 bar and maintained at a temperature of 10 to 80° C. The pressure in the intermediate container is then increased by 5 to 60 bar by introducing under pressure a gaseous mixture, and the propylene homopolymer is then transferred to a second polymerization step together with the Ziegler-Natta catalyst system. In said second polymerization step, a mixture from propylene and a C 2 -C 8 alk-1-ene is polymerized into the propylene homopolymer at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of 0.5 to 5 hours. The weight ratio between the monomers reacted in the first and those reacted in the second polymerization step are adjusted to be in the range of from 4:1 to 1:1.
-
公开(公告)号:AT271080T
公开(公告)日:2004-07-15
申请号:AT01936391
申请日:2001-05-23
Applicant: BASELL POLIOLEFINE SPA
Inventor: DAHN ULRICH , BIDELL WOLFGANG , ZIMMERMANN HANS-JUERGEN , HINGMANN ROLAND , ROESCH JOACHIM , SCHWEIER GUENTHER , OELZE JUERGEN
IPC: C08J5/00 , C08F2/00 , C08F4/642 , C08F10/06 , C08F110/06 , C08F210/06 , C08F297/08 , C08L53/00 , D01F6/30
Abstract: The invention relates to highly flowable propylene block copolymers that comprise 50 to 80 wt.-% of a propylene homopolymer and 10 to 70 wt.-% of a propylene copolymer having 5 to 50 wt.-% of a C 2 -C 8 alk-1-ene polymerized into it that is different from propylene, and that are obtainable from the gaseous phase by a two-step polymerization by means of a Ziegler-Natta catalyst system. In a first polymerization step, the propylene is polymerized at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of the reaction mixture of 0.3 to 5 hours in the presence of at least 2.0% by volume, based on the total volume, of hydrogen. The propylene homopolymer obtained in said first polymerization step is transferred together with the Ziegler-Natta catalyst system into an intermediate container, expanded for 0.01 to 5 minutes to less than 5 bar and maintained at a temperature of 10 to 80° C. The pressure in the intermediate container is then increased by 5 to 60 bar by introducing under pressure a gaseous mixture, and the propylene homopolymer is then transferred to a second polymerization step together with the Ziegler-Natta catalyst system. In said second polymerization step, a mixture from propylene and a C 2 -C 8 alk-1-ene is polymerized into the propylene homopolymer at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of 0.5 to 5 hours. The weight ratio between the monomers reacted in the first and those reacted in the second polymerization step are adjusted to be in the range of from 4:1 to 1:1.
-
公开(公告)号:AT266855T
公开(公告)日:2004-05-15
申请号:AT01976133
申请日:2001-08-22
Applicant: BASELL POLIOLEFINE SPA
Inventor: BIDELL WOLFGANG , LUTZ GERALD , LANGHAUSER FRANZ , SCHERER GUENTER , MECKELNBURG DIRK , OELZE JUERGEN , GERBIG HANS-JUERGEN , HUEHNERBEIN JUERGEN
IPC: B01J8/00 , B01J8/24 , C08F2/34 , C08F10/06 , C08F110/06 , C08F210/06 , G01F23/288
Abstract: In a method of measuring the fill level of a reactor in continuously operated polymerization processes using measurement of the respective phase interface in the reactor by means of ionizing radiation, at least one measuring unit comprising a radiation source which emits ionizing radiation and a corresponding detector is brought to the phase interface in the reactor and flexibly installed there, with the fill level of the reactor being measured by determining the phase interface by means of the radioactive backscattering measurement.
-
公开(公告)号:BR0114800A
公开(公告)日:2003-12-23
申请号:BR0114800
申请日:2001-08-22
Applicant: BASELL POLIOLEFINE SPA
Inventor: BIDELL WOLFGANG , LUTZ GERALD , LANGHAUSER FRANZ , SCHERER GUENTER , MECKELNBURG DIRK , OELZE JUERGEN , GERBIG HANS-JUERGEN , HUEHNERBEIN JUERGEN
IPC: B01J8/00 , B01J8/24 , C08F2/34 , C08F10/06 , C08F110/06 , C08F210/06 , G01F23/288
Abstract: In a method of measuring the fill level of a reactor in continuously operated polymerization processes using measurement of the respective phase interface in the reactor by means of ionizing radiation, at least one measuring unit comprising a radiation source which emits ionizing radiation and a corresponding detector is brought to the phase interface in the reactor and flexibly installed there, with the fill level of the reactor being measured by determining the phase interface by means of the radioactive backscattering measurement.
-
公开(公告)号:BR0111340A
公开(公告)日:2003-06-17
申请号:BR0111340
申请日:2001-05-23
Applicant: BASELL POLIOLEFINE SPA
Inventor: DAHN ULRICH , BIDELL WOLFGANG , ZIMMERMANN HANS-JUERGEN , HINGMANN ROLAND , ROESCH JOACHIM , SCHWEIER GUENTHER , OELZE JUERGEN
IPC: C08J5/00 , C08F2/00 , C08F4/642 , C08F10/06 , C08F110/06 , C08F210/06 , C08F297/08 , C08L53/00 , D01F6/30
Abstract: The invention relates to highly flowable propylene block copolymers that comprise 50 to 80 wt.-% of a propylene homopolymer and 10 to 70 wt.-% of a propylene copolymer having 5 to 50 wt.-% of a C 2 -C 8 alk-1-ene polymerized into it that is different from propylene, and that are obtainable from the gaseous phase by a two-step polymerization by means of a Ziegler-Natta catalyst system. In a first polymerization step, the propylene is polymerized at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of the reaction mixture of 0.3 to 5 hours in the presence of at least 2.0% by volume, based on the total volume, of hydrogen. The propylene homopolymer obtained in said first polymerization step is transferred together with the Ziegler-Natta catalyst system into an intermediate container, expanded for 0.01 to 5 minutes to less than 5 bar and maintained at a temperature of 10 to 80° C. The pressure in the intermediate container is then increased by 5 to 60 bar by introducing under pressure a gaseous mixture, and the propylene homopolymer is then transferred to a second polymerization step together with the Ziegler-Natta catalyst system. In said second polymerization step, a mixture from propylene and a C 2 -C 8 alk-1-ene is polymerized into the propylene homopolymer at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of 0.5 to 5 hours. The weight ratio between the monomers reacted in the first and those reacted in the second polymerization step are adjusted to be in the range of from 4:1 to 1:1.
-
公开(公告)号:DE50102859D1
公开(公告)日:2004-08-19
申请号:DE50102859
申请日:2001-05-23
Applicant: BASELL POLIOLEFINE SPA
Inventor: DAHN ULRICH , BIDELL WOLFGANG , ZIMMERMANN HANS-JUERGEN , HINGMANN ROLAND , ROESCH JOACHIM , SCHWEIER GUENTHER , OELZE JUERGEN
IPC: C08J5/00 , C08F2/00 , C08F4/642 , C08F10/06 , C08F110/06 , C08F210/06 , C08F297/08 , C08L53/00 , D01F6/30
Abstract: The invention relates to highly flowable propylene block copolymers that comprise 50 to 80 wt.-% of a propylene homopolymer and 10 to 70 wt.-% of a propylene copolymer having 5 to 50 wt.-% of a C 2 -C 8 alk-1-ene polymerized into it that is different from propylene, and that are obtainable from the gaseous phase by a two-step polymerization by means of a Ziegler-Natta catalyst system. In a first polymerization step, the propylene is polymerized at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of the reaction mixture of 0.3 to 5 hours in the presence of at least 2.0% by volume, based on the total volume, of hydrogen. The propylene homopolymer obtained in said first polymerization step is transferred together with the Ziegler-Natta catalyst system into an intermediate container, expanded for 0.01 to 5 minutes to less than 5 bar and maintained at a temperature of 10 to 80° C. The pressure in the intermediate container is then increased by 5 to 60 bar by introducing under pressure a gaseous mixture, and the propylene homopolymer is then transferred to a second polymerization step together with the Ziegler-Natta catalyst system. In said second polymerization step, a mixture from propylene and a C 2 -C 8 alk-1-ene is polymerized into the propylene homopolymer at a pressure of 10 to 50 bar, a temperature of 50 to 100° C. and an average dwelling time of 0.5 to 5 hours. The weight ratio between the monomers reacted in the first and those reacted in the second polymerization step are adjusted to be in the range of from 4:1 to 1:1.
-
公开(公告)号:DE50102281D1
公开(公告)日:2004-06-17
申请号:DE50102281
申请日:2001-08-22
Applicant: BASELL POLIOLEFINE SPA
Inventor: BIDELL WOLFGANG , LUTZ GERALD , LANGHAUSER FRANZ , SCHERER GUENTER , MECKELNBURG DIRK , OELZE JUERGEN , GERBIG HANS-JUERGEN , HUEHNERBEIN JUERGEN
IPC: B01J8/00 , B01J8/24 , C08F2/34 , C08F10/06 , C08F110/06 , C08F210/06 , G01F23/288
Abstract: In a method of measuring the fill level of a reactor in continuously operated polymerization processes using measurement of the respective phase interface in the reactor by means of ionizing radiation, at least one measuring unit comprising a radiation source which emits ionizing radiation and a corresponding detector is brought to the phase interface in the reactor and flexibly installed there, with the fill level of the reactor being measured by determining the phase interface by means of the radioactive backscattering measurement.
-
-
-
-
-
-
-