摘要:
Process for preparing ethylene copolymers in the presence of free-radical polymerization initiator at pressures in the range of from 160 MPa to 350 MPa and temperatures in the range of from 100° C. to 350° C. in a tubular reactor by copolymerizing ethylene, a bi- or multifunctional comonomer and optionally further comonomers, wherein the bi- or multifunctional comonomer bears at least two different functional groups, of which at least one is a unsaturated group, which can be incorporated into the growing polymer chain, and at least another functional group can act as chain transfer agent in radical ethylene polymerization, ethylene copolymers obtainable by such a process, the use of the ethylene copolymers for extrusion coating and a process for extrusion coating a substrate selected from the group consisting of paper, paperboard, polymeric film, and metal, with such ethylene copolymers.
摘要:
Process for preparing ethylene copolymers in the presence of free-radical polymerization initiator at pressures in the range of from 160 MPa to 350 MPa and temperatures in the range of from 100°C to 350°C in a tubular reactor by copolymerizing ethylene, a bi- or multifunctional comonomer and optionally further comonomers, wherein the bi- or multifunctional comonomer bears at least two different functional groups, of which at least one is a unsaturated group, which can be incorporated into the growing polymer chain, and at least another functional group can act as chain transfer agent in radical ethylene polymerization, ethylene copolymers obtainable by such a process, the use of the ethylene copolymers for extrusion coating and a process for extrusion coating a substrate selected from the group consisting of paper, paperboard, polymeric film, and metal, with such ethylene copolymers.
摘要:
Method of determining the composition of polymer mixtures comprising defined polymer components of differing mean molar masses Mn, which comprises the steps (a) recording of at least one 1H-NMR relaxation curve of the polymer mixture and (b) calculating the proportions of the polymer components by matching the measured relaxation curve with the relaxation curves of the individual polymer components. In this way, the composition of polymer mixtures can be determined quickly and simply. Furthermore, process integration for regulating the polymerization is possible.
摘要:
The invention pertains to a method for the preparation of ultra high molecular mass polyethylene by polymerization in suspension or in gas phase in the presence of a chromium catalyst sitting on an alumosilicate support material. The chromium catalyst has been subjected to a fluorinating treatment and the polymerization is performed under low temperature conditions within a temperature range of from 50 to 100 °C. The invention pertains also to ultra heigh molecular mass polyethylene prepared by that method and having a density in the range of from 0.930 to 0.950 g/cm 3 .
摘要:
Method of determining the composition of polymer mixtures comprising defined polymer components of differing mean molar masses Mn, which comprises the steps (a) recording of at least one 1H-NMR relaxation curve of the polymer mixture and (b) calculating the proportions of the polymer components by matching the measured relaxation curve with the relaxation curves of the individual polymer components. In this way, the composition of polymer mixtures can be determined quickly and simply. Furthermore, process integration for regulating the polymerization is possible.
摘要:
The invention relates to a partly crystalline propylene polymerisate composition which is produced by polymerisation of propylene, ethylene and/or C4-C18 alk-1-enes, whereby at least 50 mol. % of the contained monomer units are derived from propylene and at least 20 wt. % of the propylene polymerisate composition arises from polymerisation by means of metallocene catalysts, with a melting temperature TM in the range from 65 °C to 170 °C. The partly crystalline propylene polymerisate composition may be broken down into from 65 to 85 wt. % of a main component A, from 10 to 35 wt. % of a further component B and from 0 to 25 wt. % of a further component C, whereby the fraction for components A, B and C may be determined by a TREF (Temperature Rising Elution Fractionation).
摘要:
The invention relates to a partly crystalline propylene polymerisate composition which is produced by polymerisation of propylene, ethylene and/or C4-C18 alk-1-enes, whereby at least 50 mol. % of the contained monomer units are derived from propylene and at least 20 wt. % of the propylene polymerisate composition arises from polymerisation by means of metallocene catalysts, with a melting temperature TM in the range from 65 °C to 170 °C. The partly crystalline propylene polymerisate composition may be broken down into from 65 to 85 wt. % of a main component A, from 10 to 35 wt. % of a further component B and from 0 to 25 wt. % of a further component C, whereby the fraction for components A, B and C may be determined by a TREF (Temperature Rising Elution Fractionation).
摘要:
The invention relates to copolymers of ethylene with C3-C12 α olefins which have a molecular weight distribution Mw/Mn of ≤ 10, a density of 0.85 to 0.95 g/cm3, a comonomer share of 1 to 40 % by weight and a molar mass Mn of more than 150000 g/mol. The index of breadth of the composition distribution of the comonomer is more than 70 %. The invention also relates to a method for producing said copolymers and to their use as well as to fibers, molded articles, films or polymer mixtures that contain said copolymers.
摘要:
The invention relates to a method for drying and degassing polyolefins. The polymerisation matter leaving a polymerisation reactor is contacted with a degassing medium and relaxed at the same time. According to the invention, the monomer to be polymerised is used as the degassing medium. Said monomer flows through a relaxation container, especially in a cycle process, and is preferably enriched with ethylene or other low-boiling olefins in an amount ranging from 0 to 100 mol % in relation to the entire amount of the cycle gas. Polymerisation is carried out in the relaxation container in an amount of up to 10 % in relation to the entire polymerisation conversion.