Methods for operating polyethylene reactor systems
US-2024392119-A1 · Nov 28, 2024 · US
US10364306B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10364306-B2 |
| Application number | US-201515514788-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 9, 2015 |
| Priority date | Oct 1, 2014 |
| Publication date | Jul 30, 2019 |
| Grant date | Jul 30, 2019 |
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The present disclosure provides a low density polyethylene (LDPE) having (A) a density from 0.910 to 0.924 g/cm 3 , determined according to ISO 1183 at 23° C.; (B) an elongational hardening of at least 4.2, at 150° C. at an elongational rate of 1 s −1 ; (C) a ratio Mw/Mn of at least 18, where (i) Mw is the weight average molar mass, measured by a MALLS detector coupled to a GPC, and (ii) Mn is the number average molar mass, measured by GPC (Gel Permeation Chromatography); and (D) a Mw of at least 230,000 g/mol. The present disclosure also provides an article of manufacture made from or containing (A) a substrate and (B) a coating layer made from or containing the disclosed LDPE. The present disclosure further provides a polymerization process occurring (A) in the presence of oxygen as the only radical initiating agent and (B) in the absence of solvents.
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What is claimed is: 1. A low density polyethylene comprising: A) a density from about 0.910 to about 0.924 g/cm 3 , determined according to ISO 1183 at 23° C.; B) an elongational hardening of at least about 4.2, at 150° C. at an elongational rate of 1 s −1 ; C) a ratio Mw/Mn of at least about 18, where (i) Mw is the weight average molar mass, measured by a MALLS detector coupled to a GPC, and (ii) Mn is the number average molar mass, measured by GPC (Gel Permeation Chromatography); and D) Mw from about 230,000 g/mol to about 400,000 g/mol. 2. The low density polyethylene of claim 1 , wherein the low density polyethylene is selected from the group consisting of ethylene homopolymers, ethylene copolymers and mixtures thereof. 3. The low density polyethylene of claim 1 , wherein the low density polyethylene has an elongational hardening of at least about 4.5, at 150° C. at an elongational rate of 5 s −1 . 4. The low density polyethylene of claim 1 , wherein the low density polyethylene has a gpcBR value of at least about 1.5. 5. The low density polyethylene of claim 1 , wherein the low density polyethylene has a melt flow rate (MFR) according to ISO 1133 (190° C., 2.16 kg) from about 1.5 to about 15 g/10 min. 6. An article of manufacture comprising: A) a substrate, and B) a coating layer, wherein the coating layer comprises a low density polyethylene (LDPE) and wherein the LDPE has: (i) a density from about 0.910 to about 0.924 g/cm 3 , determined according to ISO 1183 at 23° C.; (ii) an elongation hardening of at least about 4.2, at 150° C. at an elongational rate of 1 s −1 ; (iii) a ratio Mw/Mn of at least 18, wherein (1) Mw is the weight average molar mass, measured by a MALLS detector coupled to a GPC, and (2) Mn is the number average molar mass, measured by GPC (Gel Permeation Chromatography); and (i) Mw from about 230,000 g/mol to about 400,000 g/mol. 7. A polymerization process for making a low density polyethylene (LDPE) comprising: A) a step of free radical polymerizing reactants, wherein the LDPE comprises (i) a density from about 0.910 to about 0.924 g/cm 3 , determined according to ISO 1183 at 23° C.; (ii) an elongational hardening of at least about 4.2, at 150° C. at an elongational rate of 1 s −1 ; (iii) a ratio Mw/Mn of at least about 18, wherein (1) Mw is the weight average molar mass, measured by a MALLS detector coupled to a GPC, (2) Mn is the number average molar mass, measured by GPC (Gel Permeation Chromatography), and (iv) Mw from about 230,000 g/mol to about 400,000 g/mol wherein the process occurs A) in the presence of oxygen as the only radical initiating agent, and B) in the absence of a solvent. 8. The polymerization process of claim 7 , wherein the step of free-radical polymerizing reactants occurs in a tubular reactor. 9. The polymerization process of claim 7 , further comprises a step of feeding a polymerization gas to the reactor at a pressure from about 1400 to less than about 1900 bar. 10. The polymerization process of claim 7 , where in the step of free-radical polymerizing occurs in a temperature range of from about 150 to about 320° C.
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