Multi-step process for producing polypropylene composition
A polymer and propylene technology, which is applied in the field of producing propylene copolymers with a wide molecular weight distribution, and can solve problems such as catalyst activity reduction
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0164] Operating in liquid-filled mode at a temperature of 26°C and a pressure of 54 bar has a 45dm 3 capacity stirred tank reactor. A large amount of propylene was fed into the reactor so that its average residence time in the reactor was 0.3 hours, and together with 1.1 g / h of hydrogen and 1.4 g / h of polymerization catalyst, the polymerization catalyst was prepared according to the above catalyst examples prepared with triethylaluminum (TEA) as a cocatalyst and dicyclopentyldimethoxysilane (DCPDMS) as an external donor such that the molar ratio of TEA / Ti was about 388 mol / mol, and the TEA / DCPDMS The molar ratio is 6 mol / mol. The slurry from the polymerization reactor is introduced together with 160kg / h of propylene, 2.7kg / h of ethylene and hydrogen into a volume of 150dm 3 In the loop reactor, the molar ratio of hydrogen to propylene is 0.15mol / kmol. The loop reactor was operated at a temperature of 68°C and a pressure of 53 bar. The production rate of propylene copolyme...
Embodiment 2 and Embodiment 3
[0169] Except that the operating conditions in the loop reactor and the gas phase reactor were changed as shown in Table 1, the operating steps of Example 1 were followed.
PUM
| Property | Measurement | Unit |
|---|---|---|
| melt flow index | aaaaa | aaaaa |
| melt flow index | aaaaa | aaaaa |
| melt flow index | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 


