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Volumn 5, Issue 5, 2003, Pages 497-507

A novel non-phosgene polycarbonate production process using by-product CO2 as starting material

Author keywords

[No Author keywords available]

Indexed keywords

4,4' ISOPROPYLIDENEDIPHENOL; CARBON DIOXIDE; CARBON MONOXIDE; CARCINOGEN; CHLORINE; COKE; DICHLOROMETHANE; ETHYLENE GLYCOL; ETHYLENE OXIDE; HYDROCARBON; OXYGEN; PHOSGENE; POLYCARBONATE;

EID: 0345293143     PISSN: 14639262     EISSN: None     Source Type: Journal    
DOI: 10.1039/b304963a     Document Type: Conference Paper
Times cited : (426)

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    • Komiya, M.K.1    Tojo, M.2    Fukuoka, S.3
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  • 112
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    • Tojo, M.1    Onishi, K.2    Komiya, K.3
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  • 117
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    • Phosgene process (1) about 20 thousand million yen for 60 000 ton/year plant for "T. Co."
    • Singapore Dec. 6
    • The newspapers say that new construction costs of the PC production plants are as follows: (a) Phosgene process (1) About 20 thousand million yen for 60 000 ton/year plant for "T. Co." in Singapore. Sekiyu-Kagaku-Shinbun (Japanese) [The "Petro-Chemical Press" (weekly)], Dec. 6. 1999. (2) About 20 thousand million yen for 40 000 ton/year plant for "S.D. Co." in Japan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Oct. 7. 1993. (b) Non-phosgene Asahi Kasei process About 9 thousand million yen for 50 000 ton/year plant for Chimei-Asahi Corp. in Taiwan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Nov. 8, 1999.
    • (1999) Sekiyu-Kagaku-Shinbun (Japanese) [The "Petro-Chemical Press" (Weekly)]
  • 134
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    • About 20 thousand million yen for 40 000 ton/year plant for "S.D. Co."
    • Japan. Oct. 7
    • The newspapers say that new construction costs of the PC production plants are as follows: (a) Phosgene process (1) About 20 thousand million yen for 60 000 ton/year plant for "T. Co." in Singapore. Sekiyu-Kagaku-Shinbun (Japanese) [The "Petro-Chemical Press" (weekly)], Dec. 6. 1999. (2) About 20 thousand million yen for 40 000 ton/year plant for "S.D. Co." in Japan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Oct. 7. 1993. (b) Non-phosgene Asahi Kasei process About 9 thousand million yen for 50 000 ton/year plant for Chimei-Asahi Corp. in Taiwan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Nov. 8, 1999.
    • (1993) Kagaku Kogyo Nippo (Japanese) [The Chemical Daily]
  • 135
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    • Non-phosgene Asahi Kasei process about 9 thousand million yen for 50 000 ton/year plant for Chimei-Asahi Corp
    • Taiwan. Nov. 8
    • The newspapers say that new construction costs of the PC production plants are as follows: (a) Phosgene process (1) About 20 thousand million yen for 60 000 ton/year plant for "T. Co." in Singapore. Sekiyu-Kagaku-Shinbun (Japanese) [The "Petro-Chemical Press" (weekly)], Dec. 6. 1999. (2) About 20 thousand million yen for 40 000 ton/year plant for "S.D. Co." in Japan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Oct. 7. 1993. (b) Non-phosgene Asahi Kasei process About 9 thousand million yen for 50 000 ton/year plant for Chimei-Asahi Corp. in Taiwan. Kagaku Kogyo Nippo (Japanese) [The Chemical Daily], Nov. 8, 1999.
    • (1999) Kagaku Kogyo Nippo (Japanese) [The Chemical Daily]
  • 136
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    • note
    • 2 and NaOH (raw materials) are wasted as NaCl. At least this point shows that the Asahi Kasei Process is more economical than the phosgene process.
  • 137
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    • Polycarbonate
    • July /Process Review
    • J. Plotkin and E. Glatzer describe our process in the article "Polycarbonate", European Chemical News (ECN), July 2002/Process Review pp. 32-34 as follows (the extract is shown): "Phosgene is a toxic chemical that requires rigorous process design standards to protect the health and safety of workers. Investment requirements are increased by the need for close analytical monitoring and control, equipment designs for lethal service, and treatment of vent streams by caustic scrubbing or incineration. Toughening of environmental restrictions worldwide has added impetus to the search for non-phosgene routes to polycarbonate. In addition to phosgene concerns, the interfacial polymerization process typically uses a chlorinated solvent, methylene chloride, another material with exposure limits. A further incentive to eliminate the use of phosgene is the economic penalty incurred because the chlorine content of the phosgene is wasted and converted to sodium chloride. Caustic soda is consumed in the conversion, and the disposal of waste salt solutions presents ecological problems in itself. In a second stage reactor, the ethylene carbonate is transesterified with methanol to give two products - dimethyl carbonate and ethylene glycol. Since a large portion of ethylene oxide is normally converted to ethylene glycol for use in polyester production, this approach in essence converts methanol to dimethyl carbonate with virtually no addition raw material costs. And, as an extra bonus, selectivity to ethylene glycol is very high, avoiding diethylene glycol and triethylene glycol, which are by-products of conventional ethylene glycol processes via hydrolysis of ethylene oxide".
    • (2002) European Chemical News (ECN) , pp. 32-34
    • Plotkin, J.1    Glatzer, E.2


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.