Abstract: The present invention relates to a process for producing a solid Ziegler-Natta catalyst component in the form of solid particles having a median particle size (D50vol) of 5 to 500 µm and the process comprising steps I. providing a solution of a Group 2 metal dihalide (1UPAC, Nomenclature of Inorganic Chemistry, 2005) by dissolving a solid Group 2 metal dihalide in an alcohol mixture comprising at least a monohydric alcohol (A1) of formula ROM, where R is selected from a hydrocarbyl group of 3 to 16 C atoms and an alcohol (A2) comprising in addition to the hydroxyl group another oxygen containing functional group not being a hydroxyl group, contacting the solution of the Group 2 metal dihalide of step I with a compound in a liquid form of a transition metal of Group 4 to 10, or of a lanthanide or actinide, preferably a transition metal of Group 4 to 6 of Periodic Table (1UPAC, Nomenclature of Inorganic Chemistry, 2005), and III.

Abstract: The present invention is directed to a process for producing a modified olefin polymer having increased melt strength in an extruder. The process comprising the steps of: (A) contacting a stream comprising particles of an olefin polymer with a vapour stream of a functionally unsaturated compound in vapour phase thereby producing a first mixed stream; (B) passing the first mixed stream to an extruder; (C) melting the polymer particles of the first mixed stream in the extruder; (D) introducing a stream of a free radical generator either into the first mixed stream or into the extruder; and (E) extruding the first mixed stream and the free radical generator at a temperature which is greater than the decomposition temperature of the free radical generator and the melting temperature of the olefin polymer but less than the decomposition temperature of the olefin polymer thereby producing the modified olefin polymer in the extruder.

Abstract: The present invention is directed to a process for producing a modified olefin polymer having increased melt strength in an extruder. The process comprising the steps of: (A) contacting a stream comprising particles of an olefin polymer with a vapour stream of a functionally unsaturated compound in vapour phase thereby producing a first mixed stream; (B) passing the first mixed stream to an extruder; (C) melting the polymer particles of the first mixed stream in the extruder; (D) introducing a stream of a free radical generator either into the first mixed stream or into the extruder; and (E) extruding the first mixed stream and the free radical generator at a temperature which is greater than the decomposition temperature of the free radical generator and the melting temperature of the olefin polymer but less than the decomposition temperature of the olefin polymer thereby producing the modified olefin polymer in the extruder.

Abstract: The invention relates to a flame-resistant amino resin system, in particular a melamine formaldehyde resin system, a melamine-urea formaldehyde resin system or a urea formaldehyde resin system, having: a) a modified amino resin matrix, the primary aminoplast condensation products being present at least partially in etherified form and the modified amino resin being obtained from an amino resin melt that is essentially devoid of solvent; and b) at least one compound, which acts as the flame-resistant component, contains phosphorus and/or nitrogen and/or boron in chemically bonded form and which is present in the amino resin matrix in encapsulated form. This permits the development of an amino resin system that can be thermoplastically treated, has excellent flame-resistant properties and in addition exhibits optimal curing, processing and surface characteristics.

Abstract: An aminoplast molding compound comprised of mixtures consisting of meltable 20 to 1000-ring polytriazine ethers, in which the triazine rings are primarily linked by binding links of the —NH—CHR2—O—R4—O—CHR2—NH— and —NH—CHR2—NH— type, whereby: R2?H, C1-C7-alkyl; R4?C2-C18-alkylene, —CH(CH3)—CH2—<SB>C2-C12—<SB>-alkylene-O—CH2—CH(CH3)—, —CH(CH3)—CH2—O—<SB>C2-C12—<SB>-arylene-O—CH2—CH(CH3)—, —[CH2—CH2—O—CH2—CH2]n—, —[CH2—CH(CH3)—O—CH2—CH(CH3)]n—, —[—O—CH2—CH2—CH2—CH2—]n—, —[(CH2)2-8—O—CO—<SB>C6-C14—<SB>-arylene-CO—O—(CH2)2-8—]n—, —[(CH2)2-8—O—CO—<SB>C2-C12—<SB>-alkylene-CO—O—(CH2)2-8—]n—, wherein n=1 to 200.