Description

Catalyst Activity of Catalyst (gPE/gcatï&frac*4;ŒOrdinary State) Appearance Application Device Application & Specialty TH*1 ï&frac*4;ˆâ… ï&frac*4;‰ ***0ï&frac*2;ž***0 (resin bulk density: 0.***0.*0 g/cm3) taupe powder Applied mainly for full density polyethylene equipment with UNIPOL and BP process, at ordinary or super-frozen state. For the production of polyethylene products like LLDPE, MDPE, HDPE TH*1 ï&frac*4;ˆâ…¡ï&frac*4;‰ ***0ï&frac*2;ž***0 (resin bulk density: 0.***0.*8 g/cm3) taupe powder Applied mainly for full density polyethylene equipment with UNIPOL and BP process, at ordinary or super-frozen state. For the production of polyethylene products like LLDPE, MDPE, HDPE TH*1 ï&frac*4;ˆâ…¢ï&frac*4;‰ ***0ï&frac*2;ž****0 (resin bulk density: 0.***0.*6 g/cm3) taupe powder Applied mainly for full density polyethylene equipment with UNIPOL and BP process, at ordinary or super-frozen state. For the production of polyethylene products like LLDPE, MDPE, HDPE TH*1L ï&frac*4;ˆAï&frac*4;‰ Over ****0 slurry Applied for full density polyethylene equipment with UNIPOL process, operated at high load frozen state. Real time deoxidization is necessary. Different types of resin can be produced by regulating the deoxidization of catalyst. For the production of polyethylene products like LLDPE, MDPE, HDPE TH*1L ï&frac*4;ˆBï&frac*4;‰ Over ****0 slurry Applied for full density polyethylene equipment with UNIPOL process at non-frozen and frozen state, requiring no real time deoxidization. For the production of LLDPE, MDPE, HDPE. No carrier contained in catalyst, ash content of resin can be reduced. TH*2 ï&frac*4;ˆAï&frac*4;‰ ***0ï&frac*2;ž***0 pea green powder Applied for high density polyethylene equipment with UNIPOL and BP gas phase fluidized bed process. Producing resin with the melt flow index of 1.4ï&frac*2;ž2.5g/*0min, and the density of 0.**8ï&frac*2;ž0.**5g/cm3, mainly used to mould various containers with a volume bigger than **0 liter. TH*2 ï&frac*4;ˆBâ… ï&frac*4;‰ ***0ï&frac*2;ž***0 pea green powder Applied for high density polyethylene equipment with UNIPOL and BP gas phase fluidized bed process. Producing resin with the melt flow index of 8.0ï&frac*2;ž*5g/*0min and the density of 0.**7ï&frac*2;ž0.**3g/cm3, used as special materials for film. TH*2 ï&frac*4;ˆBâ…¡ï&frac*4;‰ ***0ï&frac*2;ž***0 pea green powder Applied for high density polyethylene equipment with UNIPOL and BP gas phase fluidized bed process. Producing resin with the melt flow index of 8.0ï&frac*2;ž*7g/*0min and the density of 0.**9ï&frac*2;ž0.**8g/cm3, used to extrude products. It can be used to produce pipes conforming to PE*0 and PE **0 standard. TH*2 ï&frac*4;ˆBâ…¢ï&frac*4;‰ ***0ï&frac*2;ž***0 pea green powder Applied for high density polyethylene equipment with UNIPOL and BP gas phase fluidized bed process. Producing resin with the melt flow index of *2ï&frac*2;ž*1g/*0min and the density of 0.**9ï&frac*2;ž0.**6g/cm3, used to make containers with a volume less than *0 liter. TH*2 ï&frac*4;ˆBâ…£ï&frac*4;‰ ***0ï&frac*2;ž***0 pea green powder Applied for high density polyethylene equipment with UNIPOL and BP gas phase fluidized bed process. Producing resin with the melt flow index of 7.0ï&frac*2;ž*4g/*0min and the density of 0.**5ï&frac*2;ž0.**2g/cm3, used to make containers with a volume less than **0 liter.