Crosslinking control in high impact polystyrene manufacturing process
US-9193839-B2 · Nov 24, 2015 · US
US9593186B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9593186-B2 |
| Application number | US-201514881476-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 13, 2015 |
| Priority date | Mar 14, 2014 |
| Publication date | Mar 14, 2017 |
| Grant date | Mar 14, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The method includes providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor and injecting a retarding agent into the HIPS reaction system prior to the devolitalizer.
Opening claim text (preview).
What is claimed is: 1. A method comprising: providing a high impact polystyrene (HIPS) reaction system, wherein the HIPS reaction system has a devolitalizer downstream of a reactor; adding a retarding agent to a polymer melt in the HIPS reaction system prior to the devolitalizer, wherein the retarding agent is a crosslinking coagent. 2. The method of claim 1 , wherein the crosslinking coagent is a polyfunctional (meth)acrylic monomer. 3. The method of claim 1 , wherein the swell index of the HIPS 15 to 25 over that when no retarding agent is used. 4. The method of claim 1 , wherein the concentration of the retarding agent in the polymer melt prior to the devolitalizer is between 1 ppm and 1% (by weight). 5. The method of claim 4 , wherein the concentration of the retarding agent in the polymer melt prior to the devolitalizer is between 50 and 1000 ppm (by weight). 6. The method of claim 4 , wherein the concentration of the retarding agent in the polymer melt prior to the devolitalizer is between 50 and 150 ppm (by weight). 7. The method of claim 1 , wherein the retarding agent is added to the HIPS reaction system when the polymer melt has reached a conversion of 70 to 75%. 8. The method of claim 1 , wherein the crosslinking coagent is an allylic compound. 9. The method of claim 1 , wherein the crosslinking coagent is a metal salt of an unsaturated monocarboxylic acid.
Styrene · CPC title
Polymerisation using regulators, e.g. chain terminating agents {, e.g. telomerisation} · CPC title
using retarding agents · CPC title
on to polymers of conjugated dienes · CPC title
Crosslinking, e.g. vulcanising, of macromolecules (mechanical aspects B29C35/00; crosslinking agents C08K) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.