摘要:
A start-up procedure for use in the disproportionation of co-fed hydrogen and toluene feedstock over a nickel mordenite catalyst containing between 1.0 - 1.5 weight per cent nickel and having a silica to alumina molar ratio of between 16:1 and 22:1. At reaction start-up, the hydrogen to toluene molar ratio is maintained at an unconventionally low level of between 0.5 and 3.3. With an initial temperature of 250°C and under pressure of 550 psig or greater, toluene disproportionation is effected resulting in desirably high selectivity to benzene product and simultaneously low selectivity to undesirable non-aromatic compound by-product.
摘要:
The present invention provides a process for control of desired properties in the polymer product. The catalyst system used in the process includes a supported metallocene catalyst precursor in combination with an oxyorganoaluminum. The process can be applied to the co-polymerization of propylene and ethylene. The randomness of the ethylene incorporation of the co-polymer product is increased as the amount of ethylene in the feed is increased. The amount of ethylene in the feed is up to 6 wt% with a resulting amount of ethylene incorporated into the copolymer product up to 4 mole %.
摘要:
A polyolefin metallocene catalyst which includes two metallocene components, a stereorigid isospecific metallocene catalyst component and a stereorigid syndiospecific metallocene catalyst component, both of which are supported upon the same support. A method of forming a catalyst system includes contacting the above catalyst with a cocatalyst or Lewis acid. A method of polymerization includes contacting an olefin with the catalyst system.
摘要:
The present invention provides a catalyst and a process for increased catalyst activity and polymer yield. The catalyst system used in the process includes at least two supported metallocene catalyst precursor in combination with an oxyorganoaluminum. The process can be applied to the polymerization of olefins, preferably olefin of three carbon atoms and higher, particularly propylene. The catalyst activity and polymer yield for a dual supported metallocene catalyst are increased over that for a single supported metallocene catalyst. The polymer produced by this dual supported metallocene system has a relatively broad molecular weight distribution.
摘要:
The present invention provides a catalyst system that exhibits control of desired properties in the polymer product. The catalyst system includes a conventional supported Ziegler-Natta catalyst containing an organic phosphorus compound in combination with an electron donor having the general formula SiR m (OR') 4-m where R is selected from the group consisting of an alkyl group, a cycloalkyl group, an aryl group and a vinyl group; R' is an alkyl group; and m is 0-3, wherein when R is an alkyl group, R may be identical with R'; when m is 0, 1 or 2, the R' groups may be identical or different; and when m is 1, 2 or 3, the R groups may be identical or different. The system easily achieves efficiencies over 30 kg/g-cat·h. The system also exhibits good control over the xylene solubles of the polymer products and produces a highly crystalline polymer product. The electron donor is preferably described by the formula: wherein R 1 is an alkyl or cycloalkyl group containing a primary, secondary or tertiary carbon atom attached to the silicon atom; R 2 and R 3 are alkyl or aryl groups; and R 4 is an alkyl or cycloalkyl group with a secondary or tertiary carbon atom attached to the silicon atom. More preferably, R 1 and R 4 are both cycloalkyl groups and are both the same. Most preferably, R 1 and R 4 are both cyclopentyl groups and R 2 and R 3 are both methoxy groups. Specifically, the electron donor may be dicyclopentyldimethoxysilane.
摘要:
The present invention provides a catalyst system which includes a Ziegler-Natta titanium catalyst in combination with an electron donor described by the formulae:
wherein R 1 is a terminally-substituted alkyl group containing a primary carbon atom attached to the silicon atom; R 2 , R 3 and R 5 are alkyl or aryl groups; and R 4 is an alkyl group with a primary carbon atom attached to the silicon atom. R 1 is preferably a primary alkyl group of 1-3 carbon atoms (exclusive of the carbon atoms of the alkyl substituent) which has the terminal carbon atom substituted with an alkyl substituent of the following formulae:
N-R'-N'-
N-R'-
where N and N' are an electron-donating group, such as an amino group (NH 2 - and -NH-, respectively), R' is a primary alkyl group of 1-3 carbon atoms and, most preferably is ethyl or propyl; R 2 , R 3 and R 5 are methyl, ethyl, propyl, or butyl groups and not necessarily the same; and R 4 is a primary alkyl group of 1-3 carbon atoms and, most preferably is methyl; R 1 is most preferably 3-aminopropyl or 3-(2-aminoethylamino)propyl; R 4 is most preferably methyl; preferred electron donors are 3-aminoprolylmethyl diethoxysilane(3-APMDS) or 3-(2-aminoethylamino)propyltrimethoxysilane [3-(2-AEA)PTS] or 3-(2-aminoethylamino)propylmethyldimethoxysilane[3(2-AEA)PMDS]. The system has a catalyst efficiency of at least 5 kg/g-cat·h as the Si/Ti mole ratio varies from 2-20 in the system.
摘要:
This invention describes a process for preparing isotactic poly-alpha olefin of melt flow equal to or less than 8 dg/min comprising the steps of: A. providing a suitable catalyst system capable of producing isotactic poly-alpha olefin comprising a metallocene-type catalyst, an alumoxane as cocatalyst or catalyst activator, and optionally a catalyst support; B. ripening the suitable catalyst system of step A by contacting with an alkyl aluminum for a period of time of from 6 hours to 14 days ; C. polymerising a suitable monomer using the ripened catalyst system of step B ; and recovering the desired isotactic polyolefin.