Load metallocene catalyst using nano material as carrier and its application
A technology of metallocene catalysts and nanomaterials, which is applied in the field of supported metallocene catalysts, can solve the problems of no significant improvement in polymer properties, high catalyst production costs, and low active and active ingredients, and achieve physical performance improvement and reduction The effect of high elution rate and load rate
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0011] Get 3.50g of the nano material carrier that obtains through cetyltrimethylammonium bromide treatment with montmorillonite, specific surface area is 450m 2 / g, add toluene (the toluene mentioned below is all processed with metal sodium distillation), and stirred for 2 hours at 40°C, then added toluene and MAO solution, and continued to stir for 2 hours at normal temperature; Zirconocene chloride (purchased from Aldrich Company, without purification, Zr content is 30.1%) was added to toluene to make a solution, then the main catalyst solution was transferred to the toluene dispersion of nanomaterials, stirred at 60 ° C for 4 hours, pumped Dry toluene as a solvent and wash with toluene to obtain a supported metallocene catalyst. The ratio of co-catalyst to main catalyst (aluminum-zirconium ratio) is 200. The whole process must be strictly operated under the protection of inert gas. The ratio of metal atom zirconium in the main catalyst to the total weight of the supporte...
Embodiment 2
[0017] 3.50g of hectorite is treated with ω-amino acid to make nanomaterials, and its specific surface area is 390m 2 / g, 0.70g dibutyl zirconium dichloride (made by Beijing Academy of Stone Sciences, Zr content is 17.0%), cocatalyst is MAO, and all the other are with embodiment `1. The zirconium loading on the catalyst was determined to be 2.70wt%. The aluminum-zirconium ratio is 100.
[0018] Use this catalyst to do the slurry copolymerization of ethylene and hexene-1 (hexene content is 15%, polymerization pressure 0.6Kpa, polymerization temperature is 60 ℃, polymerization time 4 hours), its activity is 3.11×10 7 g / (mol h) -1 , the polymerization activity of the catalyst supported by silica is 9.15×10 6 g / (mol h) -1 . The various physical properties of the polymer are tested as follows:
[0019] Polymer properties Mw×10 -4 Mn×10 -4 MDW melting point (°C)
[0020] Catalysts supported by nanomaterials 8.04 3.91 2.06 119
[0021] Catalyst supported on silica 6....
Embodiment 3
[0023] The catalyst of Example 2 is used for the slurry copolymerization of ethylene and octene-1 (octene content is 15%, polymerization pressure is 0.6Kpa, polymerization temperature is 60°C, polymerization time is 4 hours), and its activity is 3.19×10 7 g / (mol h) -1 , the polymerization activity of the catalyst supported by silica is 9.03×10 6 g / (mol h) -1 . The various physical properties of the polymer are tested as follows:
[0024] Polymer properties Mw×10 -4 Mn×10 -4 MDW melting point (°C)
[0025]Catalysts supported by nanomaterials 8.04 3.93 2.05 120
[0026] Catalyst supported on silica 6.93 3.03 2.29 117
PUM
Property | Measurement | Unit |
---|---|---|
Specific surface area | aaaaa | aaaaa |
Specific surface area | aaaaa | aaaaa |
Specific surface area | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com