Methods for improving production in gas phase polymerization
US-12152095-B2 · Nov 26, 2024 · US
US10072109B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10072109-B2 |
| Application number | US-201414898049-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 6, 2014 |
| Priority date | Jun 11, 2013 |
| Publication date | Sep 11, 2018 |
| Grant date | Sep 11, 2018 |
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The present technology relates to container comprising a propylene, ethylene, 1-butene terpolymer wherein in the terpolymer: i) the content of ethylene derived units ranges from 0.5 wt % to 1.8 wt %; ii) the content of 1-butene derived units ranges from 3.5 wt % to 6.5 wt %; iii) the ratio C2 wt %/C4 wt % ranges from 0.12 to 0.22; wherein C2 wt % is the weight percentage of ethylene derived units, and C4 wt % is the weight percentage of 1-butene derived units; iv) the total content of ethylene and 1-butene derived units is comprised between 4.2 wt % and 7.5 wt %; v) the melt flow rate (MFR measured according to ISO 1133, 230° C., 2.16 kg) ranges from 20 to 80 g/10 min; vi) the xylene soluble fraction at 25° C. is lower than 7.0 wt %; and vii) the melting point is higher than 140° C.
Opening claim text (preview).
The invention claimed is: 1. An injection molded container comprising a propylene, ethylene, and 1-butene terpolymer comprising: i) an ethylene derived content of 0.5-1.8 wt %; ii) a 1-butene derived content of 5-6 wt %; iii) a C 2 wt %/C 4 wt % ratio of 0.12-0.22; wherein C 2 wt % is the weight percentage of ethylene derived units and C 4 wt % is the weight percentage of 1-butene derived units; iv) a total content of ethylene and 1-butene derived units of 5.5-7 wt %; v) a melt flow rate (MFR, ISO 1133, 230° C., 2.16 kg) of 20-80 g/10 min; vi) a xylene soluble fraction at 25° C. lower than 7.0 wt %; vii) a melting point higher than 140° C.; and viii) a haze value for a 0.4 mm thick wall of the injection molded container of lower than 3.8%. 2. The injection molded container of claim 1 , wherein the ethylene derived terpolymer content is 0.7-1.5 wt %. 3. The injection molded container of claim 1 , wherein the terpolymer melting point is 140-152° C. 4. The injection molded container of claim 1 , wherein the terpolymer has a gloss as measured on a 1 mm plaque of higher than 120%. 5. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a C 2 wt %/C 4 wt % ratio of 0.14-0.20; wherein C 2 wt % is the weight percentage of ethylene derived units and C 4 wt % is the weight percentage of 1-butene derived units. 6. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a C 2 wt %/C 4 wt % ratio of 0.15-0.20; wherein C 2 wt % is the weight percentage of ethylene derived units and C 4 wt % is the weight percentage of 1-butene derived units. 7. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a melt flow rate (MFR, ISO 1133, 230° C., 2.16 kg) of 25-70 g/10 min. 8. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a melt flow rate (MFR, ISO 1133, 230° C., 2.16 kg) of 31-52 g/10 min. 9. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a xylene soluble fraction at 25° C. lower than 6.0 wt %. 10. The injection molded container of claim 1 , wherein the propylene, ethylene, and 1-butene terpolymer comprises a xylene soluble fraction at 25° C. lower than 5.5 wt %.
Propene · CPC title
Ethene · CPC title
Packaging materials of special type or form · CPC title
Butenes · CPC title
Melt flow index or melt flow ratio · CPC title
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