Method for preparing ethylene copolymer
US-2017166668-A1 · Jun 15, 2017 · US
US10501561B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10501561-B2 |
| Application number | US-201615738064-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 24, 2016 |
| Priority date | Jun 25, 2015 |
| Publication date | Dec 10, 2019 |
| Grant date | Dec 10, 2019 |
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Ethylene-based polymer, LDPE, is made in a high pressure polymerization process to comprising at least the step of polymerizing a reaction mixture comprising ethylene, using a reactor configuration comprising (A) at least two reaction zones, a first reaction zone (reaction zone 1) and an i reaction zone (reaction zone i where i>2), (B) at least two ethylene feed streams, each feed stream comprising a percentage of the total make-up ethylene fed to the polymerization process, in which a first ethylene feed stream is sent to reaction zone 1 and a second ethylene feed stream is sent to reaction zone i, and (C) a control system to control the percentage of the total make-up ethylene in the ethylene feed stream sent to reaction zone 1 and the percentage of the total make-up ethylene in the ethylene feed stream sent to reaction zone i.
Opening claim text (preview).
The invention claimed is: 1. A high pressure polymerization process to form an ethylene-based polymer, the process comprising at least the following step: polymerizing a reaction mixture comprising ethylene, using a reactor configuration comprising (A) at least two reaction zones, a first reaction zone (reaction zone 1) and an i reaction zone (reaction zone i where i≥2), (B) at least two ethylene feed streams, each feed stream comprising a percentage of the total make-up ethylene fed to the polymerization process, in which a first ethylene feed stream is sent to reaction zone 1 and a second ethylene feed stream is sent to reaction zone i, and (C) a control system to control the percentage of the total make-up ethylene in the ethylene feed stream sent to reaction zone 1 and the percentage of the total make-up ethylene in the ethylene feed stream sent to reaction zone i, wherein the reactor configuration further comprises at least one analyzer for detecting a component of a stream of the reactor configuration or determining a property of the ethylene-based polymer produced by the high pressure polymerization process, wherein the analyzer and a valve of the control system are connected through a feedback loop. 2. The process of claim 1 , wherein the control system comprises a valve on a line through which an ethylene feed stream is delivered to a reaction zone. 3. The process of claim 2 , wherein the valve is a three-port valve. 4. The process of claim 1 , wherein the analyzer is at least one of a gas chromatograph or an infrared spectrometer. 5. The process of claim 1 , wherein the measured property of the ethylene-based polymer is at least one of a rheological property or an optical property. 6. The process of claim 5 , wherein the rheological property is at least one of melt strength and melt elasticity. 7. The process of claim 1 , wherein the percentage of make-up ethylene in each of the first and second ethylene feed streams is from 1 to 99%. 8. The process of claim 1 , wherein each of the first and second ethylene feed streams further comprises a percentage of the total of at least one CTA make-up system fed to the high pressure polymerization process. 9. The process of claim 1 , wherein Z1 is a ratio of moles of CTA to moles of ethylene in reaction zone 1 and Zi is a ratio of moles of CTA to moles of ethylene in reaction zone i, Z1 and Zi reported in units of parts per million (ppm). 10. The process of claim 9 , wherein a ratio Z1/Zi is controlled to be from 0.2 to 2.0.
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