Abstract: The present invention relates to a polyamide ester obtainable by polymerizing a polyamide salt, a polyhydric alcohol containing at least three hydroxyl groups, a dicarboxylic acid, and a chain limiting agent, wherein the polyhydric alcohol and the dicarboxylic acid are used in such amounts that the molar ratio of the excess of carboxylic acid groups from the dicarboxylic acid used to the molar equivalent amount of hydroxyl groups from the polyhydric alcohol used is at least 0.1.

Abstract: The present invention relates to a novel process for the production of a copolyamide comprising a polymerization product of hexamethylene diamine, adipic acid and terephthalic acid. A process for the production of a copolyamide comprising less than 50 mol % of units of hexamethylene terephthalamide may include (a) introducing an aqueous solvent and the monomers adipic acid, terephthalic acid and hexamethylene diamine, or salts thereof, into an evaporator to obtain a mixture; (b) concentrating the mixture obtained in step (a) in the evaporator by evaporation of at least part of the solvent, to obtain a concentrated mixture; (c) transferring the concentrated mixture obtained in step (b) into an autoclave; (d) polymerizing the monomers in the autoclave at a pressure of at least 1.

Abstract: The present invention relates to a process for polymerization of olefins, in particular gas phase polymerization of olefins, with the aid of a supported chromium oxide based catalyst.

Abstract: Polyethylene composition having a density of 950-960 kg/m3, a SHI(1,100) of 4-12, a melt index MI2 between 0.2 and 2 g/10 min, and a relationship between spiral flow ‘SF’ (measured in mm at 250° C./1000 bar/100 mm/s) and ESCR ‘E’ (measured in hours) of E>200?SF. The composition contains 48-62 wt % of an ethylene polymer (A) and 38-52 wt % of an ethylene copolymer (B). Copolymer (B) has a higher weight average molecular weight than polymer (A), and both of fractions (A) and (B) have a reverse comonomer distribution such that comonomer content increases with increasing molecular weight in the individual fraction.

Abstract: The present invention relates to a process for polymerisation of olefins, in particular gas phase polymerisation of olefins, with the aid of a supported chromium oxide based catalyst.

Abstract: Process for polymerizing ethylene in a reactor system containing one or more reactors in series, having a characteristic such that the average polymerization productivity [kgPE/kgcata] per unit ethylene per hour a1 during operation at any first residence time r1 is less than 1.7 (a2r2?a1r1)/(r2?r1), where a2 is the average polymerization productivity [kgPE/kgcata] per unit ethylene per hour during operation at any second residence time r2 where r2>r1, a2 and r2 being measured either in the same reactor in the case of a single reactor polymerization, or in a reactor subsequent to the reactor in which a1 and r1 are measured in the case where the polymerization takes place in more than one reactor. The specific yield of the reactor system is greater than 0.3 tonnes/m3. Operating the system under the above conditions results in improved productivity/unit ethylene.

Abstract: The present invention relates to a chromium catalyzed ethylene copolymer powder exhibiting a superior fragmentation coefficient.

Abstract: Process for the activation of a supported chromium oxide based catalyst in a fluidized bed activation reactor which has a catalyst bed being fluidized by a fluidization gas. The activation includes treatment at temperatures above 500° C., in which in an initial stage, where there is an initial temperature increase, the fluidization velocity (Vf1) of the fluidization gas is maintained below 6.5 centimeters per second (cm/sec) until the temperature inside the activation reactor reaches at least 200° C., and the fluidization gas is then brought to a value (Vf2) which is at least 1 cm/sec higher than Vf1.

Abstract: A slurry process for the polymerisation of ethylene is disclosed, which takes place in a reactor system comprising one or more reactors in series, having a characteristic such that the average polymerisation productivity [kg PE/kgcata] per unit ethylene per hour aI during operation at any first residence time rI is less than 1.7 (a2r2 ?aIrI)/(r2?rI), where a2 is the average polymerisation productivity [kgPE/kgcata] per unit ethylene per hour during operation at any second residence time r2 where r2>rI, a2 and r2 being measured either in the same reactor in the case of a single reactor polymerisation, or in a reactor subsequent to the reactor in which aI and rI are measured in the case where the polymerisation takes place in more than one reactor, and wherein the specific yield of the reactor system is greater than 0.

Abstract: The present invention relates to a chromium catalysed ethylene copolymer powder exhibiting a superior fragmentation coefficient.

Abstract: The present invention relates to a process for the activation of a supported chromium oxide based catalyst.

Abstract: The present invention relates to a process for polymerisation of olefins, in particular gas phase polymerisation of olefins, with the aid of a supported chromium oxide based catalyst.