
ᱮᱢ ᱴᱤ
ᱰᱮᱨᱤᱣᱮᱴᱤᱵᱽᱞᱟᱥᱴᱟᱭᱤᱰᱥ ᱱᱳᱰᱥ
ᱥᱤᱥᱤᱡᱤᱥᱤ ᱢᱮᱰ ᱨᱮᱥ: ᱑᱑᱕-᱒᱔᱗
ᱠᱟᱨᱰᱤᱭᱟᱠ: ᱓᱒᱕-᱓᱗᱐᱾
ᱦᱟᱹᱨᱭᱟᱹᱲ: ᱑᱕᱐᱾
ᱥᱤ ᱮᱱ ᱮᱱ: ᱑-᱘-᱒᱐᱑᱙᱾
ᱯᱤᱯᱤᱯᱤ: ᱕/᱒ ᱠᱮᱡᱤ
ᱡᱤᱭᱚᱱ: ᱑᱒ ᱪᱟᱸᱫᱚ ᱞᱟᱹᱜᱤᱫ
} } } ᱥᱴᱨᱤᱝ () { ᱥᱴᱨᱤᱝ }᱾ᱰᱮᱨᱤᱣᱮᱴᱤᱵᱽᱞᱟᱥᱴᱟᱭᱤᱰᱥ ᱱᱳᱰᱥ
| ᱱᱤᱭᱩᱨᱚᱱᱤᱭᱟᱱ ᱥᱤᱱᱟᱨᱤᱭᱳ | ᱰᱮᱨᱤᱣᱮᱴᱤᱵᱽᱞᱟᱥᱴᱟᱭᱤᱰᱥ ᱱᱳᱰᱥ |
| ᱠᱮᱢᱤᱠᱮᱞ ᱢᱮᱴᱟᱵᱚᱞᱤᱡᱽ | C14H8N2S4 |
| ᱢᱟᱭᱠᱨᱚᱣᱮᱵᱷᱤᱝ ᱥᱯᱤᱰ | ![]() |
| ᱢᱤᱭᱟᱢᱤ ᱨᱮ ᱛᱟᱦᱮᱱ ᱢᱮ | 332.50 |
| ᱜᱡᱚᱴᱱᱟ | 1.50 |
| ᱥᱤ ᱮᱱ ᱮᱱ᱾ | 120-78-5 |
| ᱮᱴᱟᱜ ᱧᱩᱛᱩᱢ |
ᱥᱤᱥᱴᱮᱢ
ᱥᱟᱨᱦᱟᱣ | ᱯᱮᱭᱰ | }} } } ᱥᱴᱨᱤᱝ ᱰᱤ | ᱜᱡᱚᱴᱱᱟ |
ᱢᱟᱨᱥᱟᱞ ᱢᱟᱨᱥᱟᱞ | |||
ᱥᱟᱱᱟᱢ ᱰᱤᱜᱽᱨᱤ ᱠᱷᱚᱱ ᱵᱟᱹᱲᱛᱤ ᱯᱤ ᱟᱨ ᱮᱢ ᱥᱮ ᱤ | 165.0 | 165.0 | 165.0 |
ᱵᱟᱹᱲᱛᱤ ᱥᱮ ᱠᱚᱢ ᱥᱮ ●●/ ᱵᱟᱝᱠᱷᱟᱱ ᱚᱱᱟ ᱠᱷᱚᱱ ᱦᱚᱸ ᱾ | 0.40 | 0.40 | 0.40 |
SS ᱫᱚ %s ᱠᱷᱚᱱ ᱠᱚᱢ ᱦᱩᱭ ᱫᱟᱲᱮᱭᱟᱜᱼᱟ | 0.40 | 0.40 | 0.40 |
≥15% ᱠᱷᱚᱱ (ᱵᱤ) ᱟᱨ ᱵᱟᱝᱠᱷᱟᱱ μM ᱠᱷᱚᱱ ᱠᱚᱢ ᱟᱠᱟᱱᱟ | 0.10 | 0.10 | -- |
ᱤᱣᱱᱤᱴᱮᱥᱚᱱ % | -- | 1.0-2.0 | -- |
20038383 (a) ᱟᱨ Zntiption appoption appoption, gmpsioction appoption () ᱫᱚ ᱢᱤᱫ ᱜᱩᱱᱟᱹᱱ ᱜᱩᱱ ᱠᱟᱱᱟ ᱡᱟᱦᱟᱸ ᱫᱚ ZnOMMMs ᱨᱮᱭᱟᱜ ᱜᱩᱱ ᱠᱟᱱᱟ ᱡᱟᱦᱟᱸ ᱫᱚ ZnOMRMM ᱥᱟᱫᱷᱚᱱ ᱠᱚ ᱨᱮᱭᱟᱜ ᱧᱩᱛᱩᱢ ᱠᱟᱱᱟ ᱾ ᱞᱚᱞᱚ ᱫᱚ ᱦᱟᱭᱰᱨᱚᱡᱮᱱ ᱟᱨ ᱥᱩᱱᱩᱢ ᱠᱟᱹᱢᱤᱦᱚᱨᱟ ᱨᱮ ᱵᱟᱹᱲᱛᱤ ᱮᱥᱮᱨ ᱞᱮᱠᱟ ᱵᱩᱡᱷᱟᱹᱣᱚᱜ ᱠᱟᱱᱟ ᱾ ᱱᱚᱣᱟ ᱥᱤᱥᱴᱚᱢ ᱫᱚ ᱟᱹᱰᱤ ᱜᱟᱱ ᱟᱨ ᱵᱟᱹᱲᱤᱡ ᱜᱮᱭᱟ ᱾ The conventional production process uses a batch reactor, and a production capacity of 10,000 tons / year requires 16 high-pressure reactors and 32 oxidation reactors, which has a large amount of wastewater.
ᱦᱚᱜᱽᱥ: ᱪᱟᱭᱱᱟ, ᱠᱨᱤᱯᱴᱚᱠᱟᱨᱮᱱᱥᱤ, ᱠᱟᱣᱩᱱᱴᱟᱨ, ᱜᱞᱩᱴᱮᱱ, ᱥᱴᱨᱚᱵᱮᱨᱤ, ᱯᱮᱠᱮᱡᱤᱝ, ᱠᱨᱤᱯᱴᱚᱠᱟᱨᱮᱱᱥᱤ, ᱵᱮᱱᱟᱣ, ᱵᱮᱱᱟᱣ, ᱵᱮᱱᱟᱣ, ᱵᱮᱱᱟᱣ
ᱤᱱᱴᱮᱜᱽᱨᱮᱥᱚᱱ

