Coating composition, method of preparation thereof and substrate coated therewith
A technology of composition and coating, applied in coating, thin material handling, transportation and packaging, etc., can solve the problem of not giving examples of metallocene catalyst etc.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0070] Polymerizations were carried out in a 5.2 liter bench scale reactor (PMC reactor) containing a premix chamber. Ethylene, hydrogen and comonomer were mixed and heated in the PMC prior to introduction into the reactor and added continuously during the polymerization. Polymerization was carried out in isobutane at 80° C. and about 20 bar. A supported single-site catalyst based on di-n-butylcyclopentadienyl hafnium dichloride activated with MAO was used as catalyst.
[0071] Bimodal polymerizations are carried out in the slurry-slurry phase. Slurry-gas phase conditions can be simulated and polymerizations performed as slurry-gas phase. When the gas phase polymerization takes place for several hours, it is decided to conduct the polymerization in a time-saving manner. Unimodal polymerizations were performed prior to bimodal experiments in order to find suitable polymerization conditions to achieve MFR, density and comonomer content for the first step. Then use the same c...
Embodiment 2
[0079] Polyethylene was produced in a bench scale reactor at 90°C. The polymerization medium was isobutane and the total pressure was 24.2 bar. No comonomer was added to the reactor. Hydrogen is fed together with ethylene. The concentration of hydrogen in ethylene is 3700ppm. The partial pressure of ethylene is 6.5 bar. Production of 1940g MFR 2 134 g / 10 min of polymer. The density is 975kg / m 3 . This polymer is then used as one of the blending components.
[0080] A further component used for blending was prepared in a bench reactor. The reactor temperature was 65°C. The polymerization medium is isobutane. The total pressure is 20 bar. The comonomer content in isobutane was 2.5% by weight. No hydrogen was fed into the reactor. The partial pressure is 10.3 bar. The polymerization time was 60 minutes. Produce 2510g MFR 2 =0.07g / 10min and Mw=285000 and density is 916kg / m 3 of polymers. The MWD is 2.6.
[0081] Two independently produced polyethylenes were comp...
PUM
| Property | Measurement | Unit |
|---|---|---|
| density | aaaaa | aaaaa |
| melt flow index | aaaaa | aaaaa |
| melt flow index | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 