JPS5910649B2
(en)
*
|
1977-04-19 |
1984-03-10 |
三菱瓦斯化学株式会社 |
Manufacturing method of terephthalic acid
|
DE2822728C3
(en)
*
|
1978-05-24 |
1981-08-27 |
Asahi Kasei Kogyo K.K., Osaka |
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|
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(en)
*
|
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|
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|
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|
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|
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(en)
*
|
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|
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