发明名称 Process for preparing polystyrene having a high melt flow rate
摘要 Provided is a process for preparing polystyrene having a weight average molecular weight (Mw) in the range of 120,000-160,000 g/mol, a polydispersity in the range of 4-6 and a melt flow rate of at least 40 g/10 minutes by feeding styrene into a reaction system through which the styrene passes as a component of a reaction mixture as it is polymerized, the reaction system including an initial reaction zone (100) and a downstream reaction zone (200), comprising the steps of: polymerizing styrene in the initial reaction zone to form polystyrene having a Mw of greater than 300,000 g/mol and a polydispersity in the range 1.5-2.5, 10-30 wt. % of the styrene fed to the initial reaction zone being polymerized there, —and polymerizing styrene remaining in the reaction mixture in the downstream reaction zone, a chain transfer agent being mixed with the reaction mixture at the commencement of this reaction zone and optionally at one or more additional locations within this reaction zone. The polystyrene may be used to manufacture expandable polystyrene beads or polystyrene foam board.
申请公布号 US8912296(B1) 申请公布日期 2014.12.16
申请号 US201214366803 申请日期 2012.12.13
申请人 Styron Europe GmbH 发明人 Bouquet Gilbert;Reifert Ulrich;Hermans Nicolaas M. A.
分类号 C08F2/00;C08F112/08;C08J9/16;C08J9/228 主分类号 C08F2/00
代理机构 The Dobrusin Law Firm, PC 代理人 The Dobrusin Law Firm, PC
主权项 1. A process for preparing polystyrene having a weight average molecular weight (Mw) in the range of 120,000-160,000, a polydispersity in the range of 4-6 and a melt flow rate of a least 40 g/10 minutes by feeding styrene into a reaction system through which the styrene passes as a component of a reaction mixture as it is polymerized, the reaction system including an initial reaction zone and a downstream reaction zone, comprising the steps of: polymerizing styrene in the initial reaction zone to form polystyrene having a Mw of greater than 300,000 and a polydispersity in the range of 1.5- to 2.5, 10- to 30 wt. % of the styrene fed to the initial reaction zone being polymerized there; and polymerizing styrene remaining in the reaction mixture in the downstream reaction zone, a chain transfer agent being mixed with the reaction mixture at the commencement of the downstream reaction zone.
地址 Horgen CH