A Novel Non-Phosgene Process for Polycarbonate Production from CO2: Green and Sustainable Chemistry in Practice

被引:61
作者
Fukuoka, Shinsuke [1 ]
Fukawa, Isaburo
Tojo, Masahiro [2 ]
Oonishi, Kazuhiro [2 ]
Hachiya, Hiroshi [3 ]
Aminaka, Muneaki [3 ]
Hasegawa, Kazumi [3 ]
Komiya, Kyosuke
机构
[1] Asahi Kasei Corp, New Business Dev, Chiyoda Ku, Tokyo 1018101, Japan
[2] Asahi Kasei Chem Corp, Chem & Chem Proc Lab, Okayama 7118510, Japan
[3] Asahi Kasei Chem Corp, Technol Licensing Dept, Okayama 7118510, Japan
关键词
Polycarbonate from CO2; Non-Phosgene Process; EO; Cl-free PC; High-purity MEG; Reduction of CO2 emissions; Green Sustainable Chemistry in Practice; AROMATIC POLYESTERS;
D O I
10.1007/s10563-010-9093-5
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This paper focuses on the world's first non-phosgene process using CO2 as starting material succeeded in development and industrialization by Asahi Kasei Corp. The Asahi Kasei Process enables high-yield production of high-quality PC having excellent properties and high-purity monoethylene glycol (MEG), starting from ethylene oxide (EO), by-produced CO2 and bisphenol-A without waste and waste water. The innovative reactive distillation technologies in the monomer production and the innovative gravity-utilized, non-agitation polymerization reactor in the melt polymerization, led the new process to success. The monomer process consists of 3 production steps, ethylene carbonate (EC) from CO2 and EO, dimethyl carbonate (DMC) and MEG from EC and MeOH, and diphenyl carbonate (DPC) and MeOH from DMC and PhOH. All intermediates are recycled. The new type polymerization reactor perfectly overcomes the difficulty based on the extremely high viscosity in the melt polymerization of DPC with Bis-A. The by-produced PhOH is recycled to the monomer process. The reduction of CO2 emissions (0.173t/PC 1t) is also achieved, because CO2 used as raw material is utilized as the main chain components of the products. Four commercial plants (Taiwan: 150,000 t/y, Korea: 2 plants of 65,000 t/y, Russia: 65,000 t/y) using the Asahi Kasei Process are now successfully operating, and the plant of 260,000 t/y in Saudi Arabia will start in 2010.
引用
收藏
页码:146 / 163
页数:18
相关论文
共 239 条
[1]  
Anastas P., 1998, GREEN CHEM THEORY PR
[2]  
[Anonymous], [No title captured]
[3]  
[Anonymous], 1972, Pat., Patent No. 3642858
[4]  
ASAHI, 1991, Patent No. 3109358
[5]  
BOUWENS SM, 2003, Patent No. 6596894
[6]  
BRUNELLE DJ, 2005, ACS SYM SER, V898, P2
[7]  
BRUNELLE DJ, 2006, KIRKOTHMER ENCY CHEM, V19, P815
[8]  
Buysch H.-J., 1992, Process for preparing aromatic carbonates, Patent No. [USP 5,284,965, 5284965]
[9]  
Buysch H.-J, 1980, Patent No. [US 4181676, 4181676]
[10]  
Chalk A. J, 1976, USP, Patent No. [4,096,169, 4096169]