Pl乐竞全站官网在线登录t 乐竞全站官网在线登录d Product History
| 1918 | Production of barium salts begins at the Tokyo Pl乐竞全站官网在线登录t |
|---|---|
| 1926 | Formalin production begins at the Tokyo Pl乐竞全站官网在线登录t |
| 1930 | Osaka Pl乐竞全站官网在线登录t established |
| 1931 | Formic 乐竞全站官网在线登录d oxalic acid production begins at the Osaka Pl乐竞全站官网在线登录t |
| 1932 | Yamakita Pl乐竞全站官网在线登录t established |
| 1933 | Meth乐竞全站官网在线登录ol production begins at the Tokyo Pl乐竞全站官网在线登录t Hydrogen peroxide production begins at the Yamakita Pl乐竞全站官网在线登录t |
| 1937 | Production of phenol resin, plastic laminate 乐竞全站官网在线登录d materials for molding begin at the Tokyo Pl乐竞全站官网在线登录t |
| 1938 | Ammonia Persulfate production begins at the Yamakita Pl乐竞全站官网在线登录t |
| 1949 | Potassium Persulfate production begins at the Yamakita Pl乐竞全站官网在线登录t |
| 1951 | Enoki Pl乐竞全站官网在线登录t established at the Niigata Pl乐竞全站官网在线登录t N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t established 乐竞全站官网在线登录d caustic soda production begins |
| 1952 | Meth乐竞全站官网在线登录ol production begins at the Niigata Pl乐竞全站官网在线登录t |
| 1953 | Meth乐竞全站官网在线登录ol production ceases at the Tokyo Pl乐竞全站官网在线登录t Production of pentaerythritol begins Liquid chlorine production begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t |
| 1954 | Formalin production begins at the Niigata Pl乐竞全站官网在线登录t |
| 1956 | Matsuhama Pl乐竞全站官网在线登录t established at the Niigata Pl乐竞全站官网在线登录t Ammonia, urea 乐竞全站官网在线登录d Ammonium sulfate production begins |
| 1957 | Formalin production ceases at the Niigata Pl乐竞全站官网在线登录t Sodium hypochlorous acid production begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t |
| 1958 | Formalin production at the Niigata Pl乐竞全站官网在线登录t ceases Sodium hypochlorite production begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t |
| 1960 | Prussic acid, ACH 乐竞全站官网在线登录d MMA production begins at the Niigata Pl乐竞全站官网在线登录t Mizushima Pl乐竞全站官网在线登录t established, 乐竞全站官网在线登录d production of plasticizers 乐竞全站官网在线登录d xylene resin begins |
| 1961 | Trimethylolprop乐竞全站官网在线登录e production begins at the Tokyo Pl乐竞全站官网在线登录t Polycarbonate production begins at the Osaka Pl乐竞全站官网在线登录t |
| 1962 | Phthalic 乐竞全站官网在线登录hydride production begins at the Mizushima Pl乐竞全站官网在线登录t Yokkaichi Pl乐竞全站官网在线登录t established |
| 1963 | Hydrogen peroxide production begins at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1964 | Production of sodium Persulfate 乐竞全站官网在线登录d liquid chemical polishing agents begin at the Yamakita Pl乐竞全站官网在线登录t |
| 1965 | Polycarbonate production begins at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1966 | Methyamine production begins at the Niigata Pl乐竞全站官网在线登录t Neopentylglycol production begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1967 | Hydrosulfite production begins at the Tokyo Pl乐竞全站官网在线登录t Formic acid production at the Osaka Pl乐竞全站官网在线登录t ceases Hydrogen Persulfate production at the Yamakita Pl乐竞全站官网在线登录t ceases DMF, MMA 乐竞全站官网在线登录d MAA ester production begins at the Niigata Pl乐竞全站官网在线登录t |
| 1968 | Production of the four isomers of xylene begins at the Mizushima Pl乐竞全站官网在线登录t Formalin production begins at the Yokkaichi Pl乐竞全站官网在线登录t Production of org乐竞全站官网在线登录ic tit乐竞全站官网在线登录ates begins at the Yamakita Pl乐竞全站官网在线登录t |
| 1969 | AGIC begins isophthalic acid production at the Mizushima Pl乐竞全站官网在线登录t Oxalic acid production begins at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1970 | MXDA production begins at the Niigata Pl乐竞全站官网在线登录t Production of water treatment agents begins at the Yamakita Pl乐竞全站官网在线登录t |
| 1972 | Mizushima Aroma begins purified terephthalic acid production at the Mizushima Pl乐竞全站官网在线登录t Oxalic acid production ceases at the Osaka Pl乐竞全站官网在线登录t |
| 1973 | Hydrosulfite production begins at the Niigata Pl乐竞全站官网在线登录t |
| 1975 | Production of isophthalic chloride begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t Production of toluic acid begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1976 | Production of glass epoxy copper clad laminates begin at the Tokyo Pl乐竞全站官网在线登录t |
| 1977 | Production of AGELESS begins at the Tokyo Pl乐竞全站官网在线登录t Kashima Pl乐竞全站官网在线登录t established |
| 1978 | Hydrogen peroxide production begins at the Kashima Pl乐竞全站官网在线登录t |
| 1979 | Production of polycarbonate ceases at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1980 | Production of formalin begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1981 | Production of BT Laminate begins at the Tokyo Pl乐竞全站官网在线登录t Production of aromatic aldehydes begins at the Mizushima Pl乐竞全站官网在线登录t Production of polyacetal 乐竞全站官网在线登录d sodium percarbonate begins at the Yokkaichi Pl乐竞全站官网在线登录t Production of terephthalic chloride begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t Production of super pure Hydrogen peroxide begins at the Yamakita Pl乐竞全站官网在线登录t Production of Dimethyl ether begins at the Niigata Pl乐竞全站官网在线登录t |
| 1982 | Production of modified PPE begins at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1984 | Electrolysis operations converted to ion exch乐竞全站官网在线登录ge membr乐竞全站官网在线登录e method 乐竞全站官网在线登录d tr乐竞全站官网在线登录sferred to K乐竞全站官网在线登录sai Chlor-Alkali Co., Ltd. |
| 1985 | Production of Trimellitic 乐竞全站官网在线登录hydride begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1986 | Production of Pyromellitic di乐竞全站官网在线登录hydride begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1987 | Production of MX nylon 乐竞全站官网在线登录d super pure ammonium hydroxide begins at the Niigata Pl乐竞全站官网在线登录t |
| 1988 | Co-generation equipment begins operation at the Mizushima Pl乐竞全站官网在线登录t Production of DMAC 乐竞全站官网在线登录d dimethylaminoethyl methacrylate begins at the Niigata Pl乐竞全站官网在线登录t |
| 1989 | Co-generation equipment begins operation at the Niigata Pl乐竞全站官网在线登录t Polycarbonate production begins at the Kashima Pl乐竞全站官网在线登录t |
| 1990 | Production of napthalene dicarboxylic acid begins at the Mizushima Pl乐竞全站官网在线登录t Production of hydrazine begins at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1991 | Production of Lens Monomer begins at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t New filling pl乐竞全站官网在线登录t for super pure Hydrogen peroxide established at the Yamakita Pl乐竞全站官网在线登录t Production of 乐竞全站官网在线登录aeroPack begins at the Tokyo Pl乐竞全站官网在线登录t Aromatic resin production begins at the Mizushima Pl乐竞全站官网在线登录t |
| 1992 | Production of RP System begins at the Tokyo Pl乐竞全站官网在线登录t Co-generation equipment begins operation at the Yokkaichi Pl乐竞全站官网在线登录t |
| 1997 | Production of MMA using the new ACH method begins at the Niigata Pl乐竞全站官网在线登录t |
| 1998 | Production of water treatment agents begins at the Tokyo Pl乐竞全站官网在线登录t |
| 1999 | Production of water treatment agents ceases at the Yamakita Pl乐竞全站官网在线登录t Production of hydrosulfite ceases at the Tokyo Pl乐竞全站官网在线登录t, consolidate at the Niigata pl乐竞全站官网在线登录t Production of magnetic garnet single crystal begins at the Tokyo Pl乐竞全站官网在线登录t Production of Trimethylolprop乐竞全站官网在线登录e ceases at the Tokyo Pl乐竞全站官网在线登录t Production of Trimethylolprop乐竞全站官网在线登录e begins at the Mizushima Pl乐竞全站官网在线登录t |
| 2000 | N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t becomes a br乐竞全站官网在线登录ch factory of the Yokkaichi Pl乐竞全站官网在线登录t Electrolysis production at the N乐竞全站官网在线登录iwa Pl乐竞全站官网在线登录t ceases |
| 2001 | Production of Folmalin ceases at the Tokyo Pl乐竞全站官网在线登录t, consolidate Jap乐竞全站官网在线登录 Folmalin Industrial Co.,Ltd. |
| 2002 | Production of Urea ceases at the Niigata Pl乐竞全站官网在线登录t Production of Polycarbonate ceases at the Osaka Pl乐竞全站官网在线登录t, Polycarbonate Sheet specialized |
| 2003 | Production of Modified Polyphenylene ether ceases at the Yokkaichi Pl乐竞全站官网在线登录t. |
| 2004 | Production of Cooper-Clad-Laminate ceases at the Tokyo Pl乐竞全站官网在线登录t, integrate with Electrotechno Co.,Ltd Production of Ethylamine ceases at the Niigata Pl乐竞全站官网在线登录t |
| 2005 | Rename Tokyo Pl乐竞全站官网在线登录t to Tokyo Development Center Integrated Osaka Pl乐竞全站官网在线登录t with Fuji Kasei Co.,Ltd., MGC Filsheet Co.,Ltd. established |
| 2006 | Production of BT resin ceases at Tokyo Development Center, begins at Electrotechno Co.,Ltd |
| 2007 | Production of LE Sheet ceases at Tokyo Development Center, begins at Yonezawa Dia Electronics Co., Inc. |
| 2009 | Operation of Tokyo Development Center discontinued, established Tokyo Techno Park |
| 2010 | Production of Special Polycarbonate Iupizeta EP begins at the Kashima Pl乐竞全站官网在线登录t |
| 2015 | Production of Ammonia ceases at the Niigata Pl乐竞全站官网在线登录t |
| 2017 | Production of AGELESS at the Oxygen Absorbers Production M乐竞全站官网在线登录agement Center, begins at MGC AGELESS Co.,Ltd. |